1754 files changed, 536 insertions, 270677 deletions

diff --git a/.DS_Store b/.DS_Store
deleted file mode 100644
index 1659453..0000000
--- a/.DS_Store
+++ /dev/null
diff --git a/.gitignore b/.gitignore
index 10f3ec9..bb9ac4b 100644
--- a/.gitignore
+++ b/.gitignore
@@ -1,16 +1,38 @@
-OMChem/__pycache__/*
-__pycache__/*
-Simulator/Databases/__pycache__/*
-Simulator/Flowsheet*
-Simulator/Graph*
-Simulator/database.mo
-Simulator/PlotGraph.mos
-Simulator/simulateEQN.mos
-.vscode/settings.json
-__pycache__/*
+src/main/python/OMChem/__pycache__/*
+src/main/python/DockWidgets/__pycache__/*
+src/main/python/utils/__pycache__/*
+src/main/python/Undo.dat
+src/main/python/Redo.dat
+src/main/Simulator/Databases/__pycache__/*
+src/main/Simulator/Flowsheet*
+src/main/Simulator/Graph*
+src/main/Simulator/database.mo
+src/main/Simulator/PlotGraph.mos
+src/main/Simulator/simulateEQN.mos
 .idea/*
-DockWidgets/__pycache__/*
-Undo.dat
-test.py
-Undo.dat
-Undo.dat
+src/main/Simulator/Undo.dat
+src/main/Simulator/Redo.dat
+
+*.pyc
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deleted file mode 100644
index 362d798..0000000
--- a/DockWidgets/__pycache__/DockWidget.cpython-36.pyc
+++ /dev/null
diff --git a/DockWidgets/__pycache__/DockWidget.cpython-37.pyc b/DockWidgets/__pycache__/DockWidget.cpython-37.pyc
deleted file mode 100644
index bb3ffa1..0000000
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deleted file mode 100644
index 35f8cc8..0000000
--- a/DockWidgets/__pycache__/DockWidgetCompoundSeparator.cpython-36.pyc
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deleted file mode 100644
index ac95283..0000000
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index b2d28ee..0000000
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deleted file mode 100644
index 9be19e9..0000000
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deleted file mode 100644
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deleted file mode 100644
index 53e426a..0000000
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deleted file mode 100644
index dcdd91b..0000000
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deleted file mode 100644
index 84d18de..0000000
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deleted file mode 100644
index ddefbdd..0000000
--- a/DockWidgets/__pycache__/DockWidgetSplitter.cpython-36.pyc
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diff --git a/Redo.dat b/Redo.dat
deleted file mode 100644
index e69de29..0000000
--- a/Redo.dat
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diff --git a/Undo.dat b/Undo.dat
deleted file mode 100644
index e69de29..0000000
--- a/Undo.dat
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diff --git a/chemsep1.xml b/chemsep1.xml
deleted file mode 100644
index 547e246..0000000
--- a/chemsep1.xml
+++ /dev/null
@@ -1,94686 +0,0 @@
-<compounds library="ChemSep v7.30 pure component data - Copyright (c) Harry Kooijman and Ross Taylor (2017) - http://www.perlfoundation.org/artistic_license_2_0 modified  on 11/25/2017 01:11:11 AM by harry" file="c:\program files\chemsepl7v30\pcd\chemsep1.xml" create-date="05-07-2018" create-time="12:11:14" create-user="Rahul" >
-
-<compound>
-<LibraryIndex name="Index"  value="915" />
-<CompoundID name="Name"  value="Air" />
-<StructureFormula name="Structure"  value="(N2)0.781 (O2)0.209 (Ar)0.01" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="132.45" />a
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3774000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.09147" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.313" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="78.67" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="59.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="59.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="5642.15" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="28.96" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0329147" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12750" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="199000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.6731" />
-  <B value="0.25637" />
-  <C value="132.51" />
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-  <Tmin units="K"  value="59.15" />
-  <Tmax units="K"  value="132.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="14.794" />
-  <B value="-599.85" />
-  <C value="1.0009" />
-  <D value="-3.9938E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="59.15" />
-  <Tmax units="K"  value="132.5" />
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-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7385651" />
-  <B value="0.276676" />
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-  <D value="-0.836764" />
-  <E value="0.722737" />
-  <Tmin units="K"  value="59.15" />
-  <Tmax units="K"  value="132.45" />
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-  <eqno value="16" />
-  <A value="53628" />
-  <B value="4511.1" />
-  <C value="-143.29" />
-  <D value="1.582" />
-  <E value="-0.0051332" />
-  <Tmin units="K"  value="75" />
-  <Tmax units="K"  value="124" />
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-  <eqno value="100" />
-  <A value="29562.29" />
-  <B value="-7.164949" />
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-  <E value="2.89195E-09" />
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-  <Tmax units="K"  value="1500" />
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-  <eqno value="104" />
-  <A value="0.043047" />
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-  <eqno value="101" />
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-  <eqno value="102" />
-  <A value="0.000001592" />
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-  <eqno value="16" />
-  <A value="-0.21199" />
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-  <eqno value="102" />
-  <A value="0.0003511" />
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-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
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-  <eqno value="10" />
-  <A value="20.72" />
-  <B value="765.88" />
-  <C value="4.6692" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="119" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-6.8411" />
-  <B value="-0.020116" />
-  <C value="-0.000025724" />
-  <Tmin units="K"  value="59.15" />
-  <Tmax units="K"  value="130" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.09147" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.711E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="78.6" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.29056" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="19.7" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00105" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.879574" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="-0.00787976" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0329147" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="-0.00787976" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="12749.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0329147" />
-<CAS name="CAS number"  value="132259-10-0" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="914" />
-<CompoundID name="Name"  value="Argon" />
-<StructureFormula name="Structure"  value="Ar" />
-<Family name="Family"  value="74" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="150.86" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4898000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.07457" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.291" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="87.27" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="83.8039" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="83.8" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="68906.1" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="39.948" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0291" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="-0.002" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="0" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14138.3" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0168" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.67E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="154732" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1184900" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.52483" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="44.333" />
-  <B value="-1.8037E-15" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
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-  <eqno value="105" />
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-  <Tmax units="K"  value="150.86" />
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-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="44.369" />
-  <B value="-1126.1" />
-  <C value="-4.5688" />
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-  <E value="2" />
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-  <eqno value="106" />
-  <A value="7981000" />
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-  <eqno value="16" />
-  <A value="46085" />
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-  <A value="20786" />
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-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.037508" />
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-  <Tmin units="K"  value="75.4" />
-  <Tmax units="K"  value="773.15" />
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-  <eqno value="101" />
-  <A value="-99.903" />
-  <B value="1347.5" />
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-  <Tmax units="K"  value="150" />
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-  <D value="-0.00039294" />
-  <E value="-0.000012209" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="150" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013095" />
-  <B value="0.81923" />
-  <C value="-122.33" />
-  <D value="13993" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="2000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0029464" />
-  <B value="165.33" />
-  <C value="-8.8347" />
-  <D value="0.058394" />
-  <E value="-0.00030536" />
-  <Tmin units="K"  value="83.78" />
-  <Tmax units="K"  value="147.33" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="20786" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.000513" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.673" />
-  <B value="804.37" />
-  <C value="0.74965" />
-  <Tmin units="K"  value="90.84" />
-  <Tmax units="K"  value="135" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-6.9431" />
-  <B value="-0.0071879" />
-  <C value="-0.000089817" />
-  <Tmin units="K"  value="84.1" />
-  <Tmax units="K"  value="150" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.07541" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.454841E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="115.745" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="16.2" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.47531" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00961" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.37018" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="-0.0092" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0285865" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.1074" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.068" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.011721" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.97237" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="-0.002" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14138.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0285865" />
-<GCmethod name="PPR78" >
-  <group id="24"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="201"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7440-37-1" />
-<Smiles name="SMILES"  value="[Ar]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="922" />
-<CompoundID name="Name"  value="Bromine" />
-<StructureFormula name="Structure"  value="BrBr" />
-<Family name="Family"  value="74" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="584.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1.03E+07" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.135" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.286" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="331.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="265.9" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="265.85" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="5853.37" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="159.808" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0514795" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.128997" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="9.69E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23590" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0288" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.18E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="3.091E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3140000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="245350" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.057E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.68333" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="25.7" />
-  <B value="1.8384E-08" />
-  <Tmin units="K"  value="79.15" />
-  <Tmax units="K"  value="88.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.0603" />
-  <B value="0.28982" />
-  <C value="584.15" />
-  <D value="0.28948" />
-  <Tmin units="K"  value="265.85" />
-  <Tmax units="K"  value="584.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="63.657" />
-  <B value="-5321.6" />
-  <C value="-6.3199" />
-  <D value="0.0000054412" />
-  <E value="2" />
-  <Tmin units="K"  value="265.15" />
-  <Tmax units="K"  value="584.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.8419E+07" />
-  <B value="-0.26282" />
-  <C value="2.1808" />
-  <D value="-2.7529" />
-  <E value="1.1823" />
-  <Tmin units="K"  value="265.85" />
-  <Tmax units="K"  value="584.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-8018.8" />
-  <B value="1284.8" />
-  <C value="-11.519" />
-  <D value="0.046329" />
-  <E value="-0.000065817" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="265.9" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="75351" />
-  <B value="-4.87E+07" />
-  <C value="54033" />
-  <D value="102.73" />
-  <E value="0.43775" />
-  <Tmin units="K"  value="265.9" />
-  <Tmax units="K"  value="331.9" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="35000" />
-  <B value="-410" />
-  <C value="8.5" />
-  <D value="-0.00016" />
-  <E value="-0.00000001" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.073884" />
-  <B value="-101.75" />
-  <C value="-12.933" />
-  <D value="11359" />
-  <E value="-33103" />
-  <Tmin units="K"  value="282.08" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-5.9813" />
-  <B value="410.55" />
-  <C value="-0.30036" />
-  <D value="-0.000006936" />
-  <E value="2" />
-  <Tmin units="K"  value="265.85" />
-  <Tmax units="K"  value="350" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.1438E-07" />
-  <B value="0.88111" />
-  <C value="59.595" />
-  <D value="-6723.3" />
-  <Tmin units="K"  value="265.85" />
-  <Tmax units="K"  value="600" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.69183" />
-  <B value="27.775" />
-  <C value="-0.38966" />
-  <D value="0.00057103" />
-  <E value="-8.8462E-07" />
-  <Tmin units="K"  value="260" />
-  <Tmax units="K"  value="584" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000065648" />
-  <B value="1.4785" />
-  <C value="4505.6" />
-  <D value="-870500" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="520" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014274" />
-  <B value="235.98" />
-  <C value="-4.5131" />
-  <D value="0.0059159" />
-  <E value="-0.000010567" />
-  <Tmin units="K"  value="265.85" />
-  <Tmax units="K"  value="584.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="35550.42" />
-  <B value="3.836859" />
-  <C value="-0.0019729" />
-  <D value="3.186391E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.0128" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.108" />
-  <B value="3517.5" />
-  <C value="1.886" />
-  <Tmin units="K"  value="351.95" />
-  <Tmax units="K"  value="517.14" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.1152" />
-  <B value="-0.015793" />
-  <C value="0.000010028" />
-  <Tmin units="K"  value="265.85" />
-  <Tmax units="K"  value="350" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.152689" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.29916E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="421.071" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.279241" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="69" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0233" />
-<SpecificGravity name="Specific gravity"  units="_"  value="3.35803" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.108" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0514795" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.8985" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.672" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.108" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23591.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0514795" />
-<Umr name="UMR" >
-  <group id="208"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7726-95-6" />
-<Smiles name="SMILES"  value="BrBr" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1501" />
-<CompoundID name="Name"  value="Carbon tetrachloride" />
-<StructureFormula name="Structure"  value="CCl4" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="556.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4557000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.276" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.271" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="349.79" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="250.33" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="250.33" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1122.46" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="153.822" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09707" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.187" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.482E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17550" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0523" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.28E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.581E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5.354E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="309910" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2535000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.8319" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.653E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.438" />
-  <B value="-0.0072903" />
-  <C value="0.00003899" />
-  <Tmin units="K"  value="83.15" />
-  <Tmax units="K"  value="250.33" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0721" />
-  <B value="0.28328" />
-  <C value="556.3" />
-  <D value="0.30092" />
-  <Tmin units="K"  value="250.33" />
-  <Tmax units="K"  value="554.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.671" />
-  <B value="-6304.2" />
-  <C value="-9.2247" />
-  <D value="0.0000074352" />
-  <E value="2" />
-  <Tmin units="K"  value="213.45" />
-  <Tmax units="K"  value="556.35" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.1764E+07" />
-  <B value="-1.5729" />
-  <C value="5.2158" />
-  <D value="-5.5259" />
-  <E value="2.1931" />
-  <Tmin units="K"  value="250.33" />
-  <Tmax units="K"  value="553.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="60986" />
-  <B value="-293.46" />
-  <C value="5.2282" />
-  <D value="-0.019314" />
-  <E value="0.00002862" />
-  <Tmin units="K"  value="89.99" />
-  <Tmax units="K"  value="250.33" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="129390" />
-  <B value="1959.2" />
-  <C value="-18.833" />
-  <D value="0.080834" />
-  <E value="-0.000047491" />
-  <Tmin units="K"  value="250.33" />
-  <Tmax units="K"  value="388.71" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="37588.04" />
-  <B value="-242.5309" />
-  <C value="11.66726" />
-  <D value="-0.000446049" />
-  <E value="1.391101E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20113" />
-  <B value="-311.19" />
-  <C value="-16.896" />
-  <D value="-1136.9" />
-  <E value="1442.5" />
-  <Tmin units="K"  value="278.2" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-22.297" />
-  <B value="1645" />
-  <C value="1.7588" />
-  <D value="-0.0000028163" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="455" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000029947" />
-  <B value="0.37756" />
-  <C value="454.35" />
-  <D value="5708.3" />
-  <Tmin units="K"  value="250.33" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.034432" />
-  <B value="-227.95" />
-  <C value="-0.38117" />
-  <D value="-0.0048371" />
-  <E value="-0.0000011782" />
-  <Tmin units="K"  value="250.33" />
-  <Tmax units="K"  value="428.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0001208" />
-  <B value="0.98541" />
-  <C value="1411.1" />
-  <D value="-36584" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010075" />
-  <B value="136.76" />
-  <C value="-4.0687" />
-  <D value="0.0038054" />
-  <E value="-0.0000094387" />
-  <Tmin units="K"  value="250.33" />
-  <Tmax units="K"  value="540.24" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="20936" />
-  <B value="348.23" />
-  <C value="-0.59532" />
-  <D value="0.00047717" />
-  <E value="-0.000000146" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.638772" />
-  <B value="-1100" />
-  <C value="-6.6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.994" />
-  <B value="2974" />
-  <C value="-35.755" />
-  <Tmin units="K"  value="336.67" />
-  <Tmax units="K"  value="498.45" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.26584" />
-  <B value="-0.031175" />
-  <C value="0.000028846" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="455" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2754" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.820829E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="330.3023" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="99.9" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.55223" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0391" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.60128" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1875" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0971395" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.33" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.82" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.82" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2581" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.695" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17546.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0971395" />
-<UnifacVLE name="UNIFAC" >
-  <group id="53"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="39"  value="1" />
-  </UnifacLLE>
-<GCmethod name="PPR78" >
-  <group id="53"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="53"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="52"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="56-23-5" />
-<Smiles name="SMILES"  value="C([Cl])([Cl])([Cl])[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="908" />
-<CompoundID name="Name"  value="Carbon monoxide" />
-<StructureFormula name="Structure"  value="CO" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="132.85" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3494000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0931" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.292" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="81.66" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="68.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="68.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="15400" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="28.01" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.03488" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.045" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.582E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="6402" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.74E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0162" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.78E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.1053E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.3715E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="197556" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="840984" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.5567" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.83E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="38.293" />
-  <B value="-0.062464" />
-  <Tmin units="K"  value="27.26" />
-  <Tmax units="K"  value="68.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.2423" />
-  <B value="0.2437" />
-  <C value="132.93" />
-  <D value="0.24196" />
-  <Tmin units="K"  value="68.13" />
-  <Tmax units="K"  value="132.92" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="42.283" />
-  <B value="-1035.1" />
-  <C value="-4.2012" />
-  <D value="0.000062546" />
-  <E value="2" />
-  <Tmin units="K"  value="64.07" />
-  <Tmax units="K"  value="132.92" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8585000" />
-  <B value="0.4921" />
-  <C value="-0.326" />
-  <D value="0.2231" />
-  <E value="0" />
-  <Tmin units="K"  value="68.13" />
-  <Tmax units="K"  value="132.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-1396" />
-  <B value="-235.75" />
-  <C value="86.77" />
-  <D value="-2.1914" />
-  <E value="0.018145" />
-  <Tmin units="K"  value="11.95" />
-  <Tmax units="K"  value="62" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63364" />
-  <B value="-10524" />
-  <C value="359.6" />
-  <D value="-3.9494" />
-  <E value="0.014624" />
-  <Tmin units="K"  value="68.09" />
-  <Tmax units="K"  value="132" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29100" />
-  <B value="-1979.753" />
-  <C value="10.58274" />
-  <D value="-0.0000790406" />
-  <E value="-1.99685E-07" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.050638" />
-  <B value="-16.861" />
-  <C value="-0.070987" />
-  <D value="-0.00093802" />
-  <E value="0.00049395" />
-  <Tmin units="K"  value="66.46" />
-  <Tmax units="K"  value="664.6" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-82.158" />
-  <B value="1037.8" />
-  <C value="14.229" />
-  <D value="-0.00028204" />
-  <E value="2" />
-  <Tmin units="K"  value="68.15" />
-  <Tmax units="K"  value="131.37" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000012713" />
-  <B value="0.51494" />
-  <C value="105.97" />
-  <D value="-231.11" />
-  <Tmin units="K"  value="68.15" />
-  <Tmax units="K"  value="1273.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.23621" />
-  <B value="-3.5251" />
-  <C value="-0.55788" />
-  <D value="-0.0039362" />
-  <E value="-0.0000082725" />
-  <Tmin units="K"  value="65" />
-  <Tmax units="K"  value="125" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00061581" />
-  <B value="0.6828" />
-  <C value="61.287" />
-  <D value="221.32" />
-  <Tmin units="K"  value="70" />
-  <Tmax units="K"  value="1500" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0087233" />
-  <B value="5.9843" />
-  <C value="-3.6585" />
-  <D value="0.00036163" />
-  <E value="-0.000067401" />
-  <Tmin units="K"  value="68.15" />
-  <Tmax units="K"  value="129.51" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29443.72" />
-  <B value="-5.672939" />
-  <C value="0.0158794" />
-  <D value="-6.436214E-06" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.308" />
-  <B value="678.37" />
-  <C value="-4.4122" />
-  <Tmin units="K"  value="80.95" />
-  <Tmax units="K"  value="119.28" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-5.2198" />
-  <B value="-0.055919" />
-  <C value="0.00017035" />
-  <Tmin units="K"  value="68.15" />
-  <Tmax units="K"  value="131.37" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0921398" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.704834E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="103.1937" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2918" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="18" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0111" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.799388" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0295" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0354426" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.0679" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.112" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.02528" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.093" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="6402.36" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0354426" />
-<GCmethod name="PPR78" >
-  <group id="22"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="214"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="630-08-0" />
-<Smiles name="SMILES"  value="[C+]#[O-]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="909" />
-<CompoundID name="Name"  value="Carbon dioxide" />
-<StructureFormula name="Structure"  value="OCO" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="304.21" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7383000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.094" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.274" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="216.58" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="216.58" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="518672" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="44.0095" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0616782" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.223621" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.04E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14560" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0197" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.23E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.9351E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.9437E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="213677" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9019000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.8255" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="42.04" />
-  <B value="-0.034421" />
-  <C value="-0.0002847" />
-  <Tmin units="K"  value="143.1" />
-  <Tmax units="K"  value="216.58" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.768" />
-  <B value="0.26212" />
-  <C value="304.21" />
-  <D value="0.2908" />
-  <Tmin units="K"  value="216.58" />
-  <Tmax units="K"  value="304.21" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="95.478" />
-  <B value="-4070" />
-  <C value="-12.07" />
-  <D value="0.000029505" />
-  <E value="2" />
-  <Tmin units="K"  value="216.4" />
-  <Tmax units="K"  value="304.21" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.1092E+07" />
-  <B value="0.35366" />
-  <C value="-0.46134" />
-  <D value="0.43554" />
-  <E value="0.037671" />
-  <Tmin units="K"  value="216.58" />
-  <Tmax units="K"  value="304.21" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18283" />
-  <B value="1360.3" />
-  <C value="-12.153" />
-  <D value="0.051584" />
-  <E value="-0.000076997" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="216.58" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="80592" />
-  <B value="108.83" />
-  <C value="-6.9126" />
-  <D value="0.059647" />
-  <E value="0.0000069922" />
-  <Tmin units="K"  value="216.58" />
-  <Tmax units="K"  value="290" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="28933" />
-  <B value="-494.28" />
-  <C value="10.658" />
-  <D value="-0.000027375" />
-  <E value="3.3268E-09" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="2000" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.05255" />
-  <B value="-35.057" />
-  <C value="-1.6557" />
-  <D value="121.54" />
-  <E value="-254.34" />
-  <Tmin units="K"  value="152.1" />
-  <Tmax units="K"  value="1773.15" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.7022" />
-  <B value="-166.34" />
-  <C value="0.38094" />
-  <D value="-0.00004018" />
-  <E value="2" />
-  <Tmin units="K"  value="216.58" />
-  <Tmax units="K"  value="303.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000022464" />
-  <B value="0.45495" />
-  <C value="292.64" />
-  <D value="1669.1" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="1900" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.24975" />
-  <B value="-55.106" />
-  <C value="0.41735" />
-  <D value="-0.0051067" />
-  <E value="0.0000020157" />
-  <Tmin units="K"  value="216.58" />
-  <Tmax units="K"  value="300" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="5.804" />
-  <B value="-0.44522" />
-  <C value="794.13" />
-  <D value="2139600" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="1500" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011629" />
-  <B value="-183.67" />
-  <C value="0.069773" />
-  <D value="-0.012408" />
-  <E value="-0.0000018232" />
-  <Tmin units="K"  value="216.58" />
-  <Tmax units="K"  value="304.21" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="19800" />
-  <B value="73.44" />
-  <C value="-0.05602" />
-  <D value="0.00001715" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.381181" />
-  <B value="-800" />
-  <C value="-4.8" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="424.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.794" />
-  <B value="1725.4" />
-  <C value="-16.793" />
-  <Tmin units="K"  value="216.73" />
-  <Tmax units="K"  value="271.93" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-8.3078" />
-  <B value="0.012091" />
-  <C value="-0.000055826" />
-  <Tmin units="K"  value="216.58" />
-  <Tmax units="K"  value="303.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.104698" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.011624E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="187.9268" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.270937" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="26.9" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.16755" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0132" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.825335" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.231" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0372744" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.2986" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.292" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004474" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.7039" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.231" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14563.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0372744" />
-<GCmethod name="PPR78" >
-  <group id="12"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="215"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="124-38-9" />
-<Smiles name="SMILES"  value="O=C=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1938" />
-<CompoundID name="Name"  value="Carbon disulfide" />
-<StructureFormula name="Structure"  value="SCS" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="552" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7900000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.16" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="319.375" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="161.58" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="161.11" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.4944" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="76.1407" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0606387" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.110697" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.569E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20400" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0312" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.75366E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.169E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.68E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="237900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4393000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.66599" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.0769E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="20.411" />
-  <B value="-1.6913E-08" />
-  <Tmin units="K"  value="157.45" />
-  <Tmax units="K"  value="166.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.7976" />
-  <B value="0.28757" />
-  <C value="552" />
-  <D value="0.32269" />
-  <Tmin units="K"  value="161.11" />
-  <Tmax units="K"  value="552" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="52.62041" />
-  <B value="-4546.02" />
-  <C value="-4.744246" />
-  <D value="4.881551E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="161.11" />
-  <Tmax units="K"  value="552" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.9758E+07" />
-  <B value="0.68679" />
-  <C value="0.18227" />
-  <D value="-1.7985" />
-  <E value="1.3658" />
-  <Tmin units="K"  value="161.11" />
-  <Tmax units="K"  value="552" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11237" />
-  <B value="1443.9" />
-  <C value="-14.995" />
-  <D value="0.077354" />
-  <E value="-0.00014378" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="160" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="69032" />
-  <B value="671.75" />
-  <C value="2.3423" />
-  <D value="0.015972" />
-  <E value="-0.0000043479" />
-  <Tmin units="K"  value="161.11" />
-  <Tmax units="K"  value="552" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="26779" />
-  <B value="-222.87" />
-  <C value="10.557" />
-  <D value="0.00011062" />
-  <E value="-5.3772E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.098838" />
-  <B value="-139" />
-  <C value="-11.954" />
-  <D value="1024.2" />
-  <E value="-2823.7" />
-  <Tmin units="K"  value="276" />
-  <Tmax units="K"  value="1932" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.8702" />
-  <B value="691.26" />
-  <C value="-0.072299" />
-  <D value="1.6489E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="161.58" />
-  <Tmax units="K"  value="441.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.9681E-08" />
-  <B value="0.92304" />
-  <C value="48.01" />
-  <D value="-162.47" />
-  <Tmin units="K"  value="161.11" />
-  <Tmax units="K"  value="800" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.12378" />
-  <B value="-150.01" />
-  <C value="-0.453" />
-  <D value="-0.0078739" />
-  <E value="-0.0000032002" />
-  <Tmin units="K"  value="161.11" />
-  <Tmax units="K"  value="319.37" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00033762" />
-  <B value="0.73827" />
-  <C value="483.3" />
-  <D value="-4769.2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015366" />
-  <B value="31.596" />
-  <C value="-2.7768" />
-  <D value="0.00031369" />
-  <E value="-0.0000054115" />
-  <Tmin units="K"  value="161.11" />
-  <Tmax units="K"  value="552" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="23177" />
-  <B value="96.491" />
-  <C value="-0.087795" />
-  <D value="0.000027305" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.955809" />
-  <B value="-1300" />
-  <C value="-7.8" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.694" />
-  <B value="3154.6" />
-  <C value="-9.3773" />
-  <Tmin units="K"  value="336.03" />
-  <Tmax units="K"  value="495.95" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.3517" />
-  <B value="-0.028388" />
-  <C value="0.000032128" />
-  <Tmin units="K"  value="161.58" />
-  <Tmax units="K"  value="441.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.16899" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.768909E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="345.5016" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="61.7" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.05841" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0256" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.26931" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1035" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0606387" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.057" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.65" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.21329" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.107865" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20410.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0606387" />
-<UnifacVLE name="UNIFAC" >
-  <group id="59"  value="1" />
-  </UnifacVLE>
-<GCmethod name="PPR78" >
-  <group id="59"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="59"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="58"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-15-0" />
-<Smiles name="SMILES"  value="S=C=S" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1894" />
-<CompoundID name="Name"  value="Phosgene" />
-<StructureFormula name="Structure"  value="COCl2" />
-<Family name="Family"  value="71" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="455" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5674200" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.19" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.285" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="280.71" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="145.37" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="145.37" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.920651" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.9161" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0597955" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.201309" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.877E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.9E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0349" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.2E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.189E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.0479E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="283740" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5738400" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.79377" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.746E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.551" />
-  <B value="-3.4911E-17" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.4691" />
-  <B value="0.2768" />
-  <C value="455" />
-  <D value="0.27965" />
-  <Tmin units="K"  value="145.37" />
-  <Tmax units="K"  value="438.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.03568" />
-  <B value="-5112.106" />
-  <C value="-9.267047" />
-  <D value="0.0000119936" />
-  <E value="2" />
-  <Tmin units="K"  value="145.37" />
-  <Tmax units="K"  value="455.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.367252E+07" />
-  <B value="1.081822" />
-  <C value="-0.773774" />
-  <D value="-0.1937" />
-  <E value="0.317951" />
-  <Tmin units="K"  value="145.37" />
-  <Tmax units="K"  value="438.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18843" />
-  <B value="2190.2" />
-  <C value="-28.32" />
-  <D value="0.18" />
-  <E value="-0.00042062" />
-  <Tmin units="K"  value="12.61" />
-  <Tmax units="K"  value="139.51" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="101240" />
-  <B value="-202030" />
-  <C value="196.31" />
-  <D value="2.1704" />
-  <E value="-0.0015512" />
-  <Tmin units="K"  value="139.95" />
-  <Tmax units="K"  value="280" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="32506" />
-  <B value="-282.16" />
-  <C value="11.124" />
-  <D value="-0.00017636" />
-  <E value="4.5651E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.1073" />
-  <B value="-108.96" />
-  <C value="-9.5718" />
-  <D value="1547.3" />
-  <E value="-3904.5" />
-  <Tmin units="K"  value="227.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-789.51" />
-  <B value="22474" />
-  <C value="129.1" />
-  <D value="-0.00032789" />
-  <E value="2" />
-  <Tmin units="K"  value="224.53" />
-  <Tmax units="K"  value="280.71" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.2229E-07" />
-  <B value="0.58405" />
-  <C value="277.35" />
-  <D value="-6111.6" />
-  <Tmin units="K"  value="280.71" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0025061" />
-  <B value="3.5674" />
-  <C value="-1.6592" />
-  <D value="-0.0007952" />
-  <E value="-0.0000018088" />
-  <Tmin units="K"  value="145.37" />
-  <Tmax units="K"  value="312.11" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000024368" />
-  <B value="1.1423" />
-  <C value="246.56" />
-  <D value="4296.5" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="800" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016139" />
-  <B value="28.561" />
-  <C value="-2.9789" />
-  <D value="0.00058557" />
-  <E value="-0.0000072142" />
-  <Tmin units="K"  value="145.37" />
-  <Tmax units="K"  value="438.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="24077" />
-  <B value="146.75" />
-  <C value="-0.13621" />
-  <D value="0.00004266" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.371608" />
-  <B value="-2350" />
-  <C value="-14.1" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="424.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.656" />
-  <B value="2693.4" />
-  <C value="-15.019" />
-  <Tmin units="K"  value="275.74" />
-  <Tmax units="K"  value="406.11" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.2091" />
-  <B value="-0.031794" />
-  <C value="0.000046341" />
-  <Tmin units="K"  value="224.53" />
-  <Tmax units="K"  value="280.71" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.19221" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.838184E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="323.8665" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="64.01" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.01253" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0271" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.381" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.20498" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0705389" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.300593" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.08" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.20305" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1918" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17837.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0705389" />
-<CAS name="CAS number"  value="75-44-5" />
-<Smiles name="SMILES"  value="ClC(=O)Cl" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1855" />
-<CompoundID name="Name"  value="Trichloroacetyl chloride" />
-<StructureFormula name="Structure"  value="CCl3COCl" />
-<Family name="Family"  value="71" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="604" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4320000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3408" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.293" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="391.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="216.2" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="216.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="5.18177" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="181.833" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.112961" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.282386" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.037E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18010" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06337" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.86E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.398E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.8E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="360000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9040000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.062E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.247" />
-  <B value="-0.0070805" />
-  <Tmin units="K"  value="86.48" />
-  <Tmax units="K"  value="216.2" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.76674" />
-  <B value="0.26122" />
-  <C value="604" />
-  <D value="0.28678" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="604" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="174.9617" />
-  <B value="-10592.68" />
-  <C value="-23.45621" />
-  <D value="0.0000238342" />
-  <E value="2" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="604" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.449329E+08" />
-  <B value="7.45895" />
-  <C value="-20.20511" />
-  <D value="23.04844" />
-  <E value="-9.793955" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="604" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="177260" />
-  <B value="-1933.8" />
-  <C value="48.92" />
-  <D value="-0.20004" />
-  <E value="0.00024097" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="600" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="91870" />
-  <B value="-696.64" />
-  <C value="12.555" />
-  <D value="-0.0015691" />
-  <E value="6.1156E-07" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="1200.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25973" />
-  <B value="-344.77" />
-  <C value="-15.647" />
-  <D value="-53770" />
-  <E value="128480" />
-  <Tmin units="K"  value="295" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.095" />
-  <B value="1867" />
-  <C value="-0.00010079" />
-  <D value="1.1286E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="391.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000001265" />
-  <B value="0.7796" />
-  <C value="98.46" />
-  <D value="0.0024692" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.043702" />
-  <B value="-153.3" />
-  <C value="-0.62199" />
-  <D value="-0.0058162" />
-  <E value="0.0000023649" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="391.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0006898" />
-  <B value="0.5929" />
-  <C value="623.5" />
-  <D value="0.0039481" />
-  <Tmin units="K"  value="391.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0090309" />
-  <B value="135.05" />
-  <C value="-3.8737" />
-  <D value="0.003953" />
-  <E value="-0.0000095091" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="604" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="57646" />
-  <B value="236.17" />
-  <C value="-0.225" />
-  <D value="0.000077151" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="1200.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.34" />
-  <B value="2694.7" />
-  <C value="-85.515" />
-  <Tmin units="K"  value="379.48" />
-  <Tmax units="K"  value="542.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="7.2231" />
-  <B value="-0.06534" />
-  <C value="0.000072292" />
-  <Tmin units="K"  value="216.2" />
-  <Tmax units="K"  value="391.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.33807" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.686395E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="474.9781" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="121.91" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0493" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.62992" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.34435" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.112737" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.177323" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.544" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.347734" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18501.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.112737" />
-<CAS name="CAS number"  value="76-02-8" />
-<Smiles name="SMILES"  value="ClC(Cl)(Cl)C(=O)Cl" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1904" />
-<CompoundID name="Name"  value="Hydrogen chloride" />
-<StructureFormula name="Structure"  value="HCl" />
-<Family name="Family"  value="77" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="324.69" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="8310000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.081" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.249" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="188.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="158.97" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="158.97" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="13521.9" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="36.461" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.03028" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.126" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.09E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12190" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.6E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.01602" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.75E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.231E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-9.53E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="186786" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2000000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.66635" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.86E+07" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="41.04" />
-  <B value="-0.0070156" />
-  <Tmin units="K"  value="103.15" />
-  <Tmax units="K"  value="158.97" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.3619" />
-  <B value="0.23301" />
-  <C value="324.69" />
-  <D value="0.25076" />
-  <Tmin units="K"  value="158.97" />
-  <Tmax units="K"  value="324.44" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="138.2562" />
-  <B value="-4825.245" />
-  <C value="-19.73669" />
-  <D value="0.0000650759" />
-  <E value="2" />
-  <Tmin units="K"  value="142.85" />
-  <Tmax units="K"  value="324.65" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.9563E+07" />
-  <B value="-0.79988" />
-  <C value="3.8907" />
-  <D value="-4.9768" />
-  <E value="2.2266" />
-  <Tmin units="K"  value="158.97" />
-  <Tmax units="K"  value="324.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10811" />
-  <B value="1080.6" />
-  <C value="-9.6311" />
-  <D value="0.047728" />
-  <E value="-0.000091003" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="158" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-53340" />
-  <B value="265.92" />
-  <C value="4.243" />
-  <D value="0.058092" />
-  <E value="-0.00013923" />
-  <Tmin units="K"  value="158.97" />
-  <Tmax units="K"  value="188.13" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29096.99" />
-  <B value="-1271.123" />
-  <C value="6.610209" />
-  <D value="0.00378635" />
-  <E value="-0.0000013094" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="1600" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.041738" />
-  <B value="-31.981" />
-  <C value="-2.0074" />
-  <D value="-28.378" />
-  <E value="43.867" />
-  <Tmin units="K"  value="159.05" />
-  <Tmax units="K"  value="1622.33" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-196.43" />
-  <B value="5474.4" />
-  <C value="31.068" />
-  <D value="-0.000094243" />
-  <E value="2" />
-  <Tmin units="K"  value="158.97" />
-  <Tmax units="K"  value="318.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.1969E-07" />
-  <B value="0.66444" />
-  <C value="177.83" />
-  <D value="-3965.9" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.4993" />
-  <B value="-113.3" />
-  <C value="0.99185" />
-  <D value="-0.0023549" />
-  <E value="-0.0000033612" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="323.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0017816" />
-  <B value="0.5013" />
-  <C value="331.03" />
-  <D value="3750.8" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="700" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0056361" />
-  <B value="317.9" />
-  <C value="-7.6858" />
-  <D value="0.026562" />
-  <E value="-0.00006761" />
-  <Tmin units="K"  value="158.97" />
-  <Tmax units="K"  value="324.65" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29475.76" />
-  <B value="-3.761741" />
-  <C value="0.00844854" />
-  <D value="-2.58231E-06" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-3.410371" />
-  <B value="-2300" />
-  <C value="-13.8" />
-  <Tmin units="K"  value="281.9278" />
-  <Tmax units="K"  value="451.9278" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.854" />
-  <B value="1925.3" />
-  <C value="-1.5518" />
-  <Tmin units="K"  value="196.58" />
-  <Tmax units="K"  value="290.95" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.3436" />
-  <B value="-0.038305" />
-  <C value="0.000048386" />
-  <Tmin units="K"  value="158.97" />
-  <Tmax units="K"  value="318.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.11545" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.36E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="328" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="23.31" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.35497" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0125" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.854783" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1254" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.030563" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.056032" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.1" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.3766" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.121" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22003.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.030563" />
-<Umr name="UMR" >
-  <group id="218"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7647-01-0" />
-<Smiles name="SMILES"  value="Cl" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="918" />
-<CompoundID name="Name"  value="Chlorine" />
-<StructureFormula name="Structure"  value="Cl2" />
-<Family name="Family"  value="74" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="417" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7700000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.124" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="239.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="172.12" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="172.12" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1366.04" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.905" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04536" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.073" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.7E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17360" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0241" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.81E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="222972" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6406000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.55192" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="29.476" />
-  <B value="-4.0445E-09" />
-  <Tmin units="K"  value="113.15" />
-  <Tmax units="K"  value="122.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.8293" />
-  <B value="0.25" />
-  <C value="417.16" />
-  <D value="0.26753" />
-  <Tmin units="K"  value="172.12" />
-  <Tmax units="K"  value="417.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="45.776" />
-  <B value="-3292.7" />
-  <C value="-3.7926" />
-  <D value="0.0000049863" />
-  <E value="2" />
-  <Tmin units="K"  value="169.02" />
-  <Tmax units="K"  value="417.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.9601E+07" />
-  <B value="0.77334" />
-  <C value="-1.0279" />
-  <D value="0.93368" />
-  <E value="-0.2926" />
-  <Tmin units="K"  value="172.12" />
-  <Tmax units="K"  value="416.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-22198" />
-  <B value="1876.1" />
-  <C value="-22.303" />
-  <D value="0.12569" />
-  <E value="-0.00025585" />
-  <Tmin units="K"  value="19.81" />
-  <Tmax units="K"  value="164.99" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66547" />
-  <B value="12488" />
-  <C value="-246.3" />
-  <D value="-2.7266" />
-  <E value="-0.021518" />
-  <Tmin units="K"  value="172.12" />
-  <Tmax units="K"  value="239.12" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="28958" />
-  <B value="-398.03" />
-  <C value="10.125" />
-  <D value="-0.0010681" />
-  <E value="3.8414E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.069476" />
-  <B value="-70.479" />
-  <C value="-4.3328" />
-  <D value="1090.9" />
-  <E value="-2256.3" />
-  <Tmin units="K"  value="208.6" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.351" />
-  <B value="502.6" />
-  <C value="0.30506" />
-  <D value="-9.5237E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="172.12" />
-  <Tmax units="K"  value="333.72" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.5899E-07" />
-  <B value="0.74273" />
-  <C value="97.463" />
-  <D value="-22.488" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.48743" />
-  <B value="13.229" />
-  <C value="-0.49371" />
-  <D value="0.00052989" />
-  <E value="-0.0000020491" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="410" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00096588" />
-  <B value="0.54995" />
-  <C value="434.26" />
-  <D value="3605.9" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.082803" />
-  <B value="-1.889" />
-  <C value="-1.8585" />
-  <D value="-0.0013422" />
-  <E value="-4.1394E-07" />
-  <Tmin units="K"  value="172.12" />
-  <Tmax units="K"  value="404.25" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="25409" />
-  <B value="44.655" />
-  <C value="-0.067331" />
-  <D value="0.000047334" />
-  <E value="-1.2685E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.434" />
-  <B value="2268.7" />
-  <C value="-9.9047" />
-  <Tmin units="K"  value="255.79" />
-  <Tmax units="K"  value="374.7" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.8294" />
-  <B value="-0.023375" />
-  <C value="0.000031235" />
-  <Tmin units="K"  value="172.12" />
-  <Tmax units="K"  value="333.72" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.13457" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.380459E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="261.0039" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="38.4" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.01934" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0185" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.41956" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0821999" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0455063" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.5887" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.524" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.59414" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.0547" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20120" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0455063" />
-<Umr name="UMR" >
-  <group id="207"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7782-50-5" />
-<Smiles name="SMILES"  value="ClCl" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1907" />
-<CompoundID name="Name"  value="Hydrogen iodide" />
-<StructureFormula name="Structure"  value="HI" />
-<Family name="Family"  value="77" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="423.85" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="8310000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1219" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.287" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="237.55" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="222.38" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="222.38" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="49326.4" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="127.912" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0507575" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.0380703" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.418E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17120" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02537" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.982E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.65E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1716000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="206481" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2872100" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.55826" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.162E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="27.652" />
-  <B value="1.0295E-08" />
-  <Tmin units="K"  value="78" />
-  <Tmax units="K"  value="87.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.29008" />
-  <B value="0.10272" />
-  <C value="423.85" />
-  <D value="0.12802" />
-  <Tmin units="K"  value="222.38" />
-  <Tmax units="K"  value="422" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="48.208" />
-  <B value="-3309.5" />
-  <C value="-4.2202" />
-  <D value="0.0000058868" />
-  <E value="2" />
-  <Tmin units="K"  value="217.95" />
-  <Tmax units="K"  value="423.85" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.5057E+07" />
-  <B value="2.4036" />
-  <C value="-3.4166" />
-  <D value="1.5877" />
-  <E value="-0.0027034" />
-  <Tmin units="K"  value="222.38" />
-  <Tmax units="K"  value="416.26" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="12463" />
-  <B value="747.87" />
-  <C value="-6.2562" />
-  <D value="0.02194" />
-  <E value="-0.000024523" />
-  <Tmin units="K"  value="100.69" />
-  <Tmax units="K"  value="218" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="47228" />
-  <B value="657.18" />
-  <C value="2.2493" />
-  <D value="0.031778" />
-  <E value="-0.000056365" />
-  <Tmin units="K"  value="222.37" />
-  <Tmax units="K"  value="237.81" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29070.86" />
-  <B value="-1600.955" />
-  <C value="9.445762" />
-  <D value="0.000914155" />
-  <E value="-4.506661E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-20.449" />
-  <B value="-959.41" />
-  <C value="4.2445" />
-  <D value="-0.000095025" />
-  <E value="2" />
-  <Tmin units="K"  value="222.38" />
-  <Tmax units="K"  value="242.89" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.6146E-07" />
-  <B value="0.8587" />
-  <C value="45.387" />
-  <D value="-1595.3" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="650" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.2841" />
-  <B value="21.17" />
-  <C value="-1.299" />
-  <D value="0.00096857" />
-  <E value="-0.0000020056" />
-  <Tmin units="K"  value="225.19" />
-  <Tmax units="K"  value="420.42" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000042343" />
-  <B value="0.89806" />
-  <C value="44.783" />
-  <D value="-39.662" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.05247" />
-  <B value="5.663" />
-  <C value="-2.1706" />
-  <D value="-0.0013606" />
-  <E value="-0.0000012045" />
-  <Tmin units="K"  value="222.38" />
-  <Tmax units="K"  value="413.25" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29521" />
-  <B value="-4.9613" />
-  <C value="0.013867" />
-  <D value="-0.0000053438" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.158041" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="276.3722" />
-  <Tmax units="K"  value="446.3722" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.903" />
-  <B value="1993.1" />
-  <C value="-25.784" />
-  <Tmin units="K"  value="256.02" />
-  <Tmax units="K"  value="381.44" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-16.715" />
-  <B value="0.095325" />
-  <C value="-0.0002226" />
-  <Tmin units="K"  value="222.38" />
-  <Tmax units="K"  value="242.89" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.13492" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.13E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="313" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="32.11" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0185" />
-<SpecificGravity name="Specific gravity"  units="_"  value="2.54382" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0359999" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0457176" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.6724" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.5928" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.0380703" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19866.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0457176" />
-<Umr name="UMR" >
-  <group id="220"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="10034-85-2" />
-<Smiles name="SMILES"  value="I" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="902" />
-<CompoundID name="Name"  value="Hydrogen" />
-<StructureFormula name="Structure"  value="H2" />
-<Family name="Family"  value="74" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="33.19" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1313000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.064147" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.305" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="20.39" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="13.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="13.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7220" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="2.01588" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0285681" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="-0.215993" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.708E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="6648" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.00632" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.43E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="130571" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="117100" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.1252" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4182E+08" />
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.9613" />
-  <B value="0.25981" />
-  <C value="33.19" />
-  <D value="0.19104" />
-  <Tmin units="K"  value="13.84" />
-  <Tmax units="K"  value="33.18" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="13.05" />
-  <B value="-97.534" />
-  <C value="1.0355" />
-  <D value="0.00031816" />
-  <E value="2" />
-  <Tmin units="K"  value="13.08" />
-  <Tmax units="K"  value="33.19" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1534700" />
-  <B value="3.214" />
-  <C value="-8.4567" />
-  <D value="8.4646" />
-  <E value="-2.8057" />
-  <Tmin units="K"  value="13.95" />
-  <Tmax units="K"  value="32.62" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5730" />
-  <B value="-1.3847E-11" />
-  <C value="1.1605E-12" />
-  <D value="-1.2321E-13" />
-  <E value="4.114E-15" />
-  <Tmin units="K"  value="13.95" />
-  <Tmax units="K"  value="23.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="14510" />
-  <B value="-1191.1" />
-  <C value="156.51" />
-  <D value="-6.1773" />
-  <E value="0.087907" />
-  <Tmin units="K"  value="13.84" />
-  <Tmax units="K"  value="32" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="3994.325" />
-  <B value="-48.69006" />
-  <C value="10.36209" />
-  <D value="-0.000340144" />
-  <E value="1.960333E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.02413" />
-  <B value="-2.768" />
-  <C value="-0.00051788" />
-  <D value="2.2059E-07" />
-  <E value="-3.1197E-08" />
-  <Tmin units="K"  value="16.6" />
-  <Tmax units="K"  value="431.6" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-32.531" />
-  <B value="97.304" />
-  <C value="5.9178" />
-  <D value="-0.0031563" />
-  <E value="2" />
-  <Tmin units="K"  value="13.84" />
-  <Tmax units="K"  value="33" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7916E-07" />
-  <B value="0.68557" />
-  <C value="-0.51413" />
-  <D value="132.61" />
-  <Tmin units="K"  value="13.95" />
-  <Tmax units="K"  value="2000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.34238" />
-  <B value="-4.3002" />
-  <C value="-0.53814" />
-  <D value="0.0011639" />
-  <E value="-0.00021792" />
-  <Tmin units="K"  value="13.84" />
-  <Tmax units="K"  value="31" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0026851" />
-  <B value="0.74366" />
-  <C value="13.289" />
-  <D value="-31.305" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1600" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.003232" />
-  <B value="1.9865" />
-  <C value="-5.0915" />
-  <D value="-0.00046122" />
-  <E value="-0.00062971" />
-  <Tmin units="K"  value="13.95" />
-  <Tmax units="K"  value="32.18" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="5" />
-  <A value="23052.64" />
-  <B value="33.74914" />
-  <C value="-0.0639907" />
-  <D value="0.000051023" />
-  <E value="-1.37699E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.000284" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="18.072" />
-  <B value="137.26" />
-  <C value="0.53751" />
-  <Tmin units="K"  value="20.03" />
-  <Tmax units="K"  value="29.14" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-9.6512" />
-  <B value="-0.067852" />
-  <C value="-0.0003859" />
-  <Tmin units="K"  value="13.84" />
-  <Tmax units="K"  value="33" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.06424" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.105589E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="30.15782" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.3139" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="6.12" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0061" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.0698591" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="-0.2324" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0285681" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.4092" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.5516" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.025891" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="6647.875" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.031" />
-<GCmethod name="PPR78" >
-  <group id="16"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="205"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="1333-74-0" />
-<Smiles name="SMILES"  value="[H][H]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1921" />
-<CompoundID name="Name"  value="Water" />
-<StructureFormula name="Structure"  value="HOH" />
-<Family name="Family"  value="84" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="647.14" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2.2064E+07" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.05595" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.229" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="373.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="273.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="273.16" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="611.73" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="18.015" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.01807" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.344" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.15E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="47860" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.17E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.01237" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.26E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.41814E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.2859E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="188724" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6001740" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0783" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="52.967" />
-  <B value="-0.0075822" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="273.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="106" />
-  <A value="32.51621" />
-  <B value="-3.213004" />
-  <C value="7.92411" />
-  <D value="-7.359898" />
-  <E value="2.703522" />
-  <Tmin units="K"  value="253.1" />
-  <Tmax units="K"  value="647.29" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="74.55502" />
-  <B value="-7295.586" />
-  <C value="-7.442448" />
-  <D value="0.0000042881" />
-  <E value="2" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="647.29" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.964E+07" />
-  <B value="0.86515" />
-  <C value="-1.1134" />
-  <D value="0.67764" />
-  <E value="-0.026925" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="647.28" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-262.51" />
-  <B value="140.52" />
-  <C value="-0.0000038869" />
-  <D value="-1.1996E-08" />
-  <E value="7.1879E-11" />
-  <Tmin units="K"  value="3.15" />
-  <Tmax units="K"  value="273.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="75539" />
-  <B value="-22297" />
-  <C value="136.02" />
-  <D value="-0.25622" />
-  <E value="0.00018273" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="533.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33200" />
-  <B value="-878.9001" />
-  <C value="8.436956" />
-  <D value="0.00207627" />
-  <E value="-6.467085E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1600" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.01973" />
-  <B value="-22.635" />
-  <C value="-18.029" />
-  <D value="-2747" />
-  <E value="498.58" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-133.7" />
-  <B value="6785.7" />
-  <C value="18.47" />
-  <D value="-0.000014736" />
-  <E value="2" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="647.13" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.002327E-08" />
-  <B value="0.934576" />
-  <C value="195.6338" />
-  <D value="-13045.99" />
-  <Tmin units="K"  value="273.16" />
-  <Tmax units="K"  value="1073.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-1.5697" />
-  <B value="-55.141" />
-  <C value="0.7832" />
-  <D value="0.0011484" />
-  <E value="-0.0000018151" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="633.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000065986" />
-  <B value="1.3947" />
-  <C value="59.478" />
-  <D value="-15484" />
-  <Tmin units="K"  value="273.16" />
-  <Tmax units="K"  value="1073.15" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.031819" />
-  <B value="167.09" />
-  <C value="-3.6781" />
-  <D value="0.0053717" />
-  <E value="-0.0000084188" />
-  <Tmin units="K"  value="265.1" />
-  <Tmax units="K"  value="647.1" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="33444.62" />
-  <B value="-5.799206" />
-  <C value="0.0251681" />
-  <D value="-0.0000143103" />
-  <E value="2.76249E-09" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="121" />
-  <A value="1.78042" />
-  <B value="28066.24" />
-  <C value="-0.635922" />
-  <D value="-0.0472309" />
-  <E value="1" />
-  <Tmin units="K"  value="238" />
-  <Tmax units="K"  value="635" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.401" />
-  <B value="3987.3" />
-  <C value="-37.161" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="573.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.886" />
-  <B value="-0.026811" />
-  <C value="0.000020554" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="647.13" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.04357" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="2.52E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="775" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2338" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="13.11" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.58321" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00926" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.997986" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="-0.65445" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0180674" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.92" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.4" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="1" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="1.243997" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.201789" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.54619" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.328" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="47812.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0180674" />
-<UnifacVLE name="UNIFAC" >
-  <group id="17"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="17"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="14"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="17"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="17"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="16"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="7732-18-5" />
-<Smiles name="SMILES"  value="O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1922" />
-<CompoundID name="Name"  value="Hydrogen sulfide" />
-<StructureFormula name="Structure"  value="HSH" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="373.53" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="8962910" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0985" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.284" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="212.8" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="187.68" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="187.68" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="23200" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="34.0809" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0438045" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.0941677" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.384E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18000" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.23E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.01872" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.10256E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.063E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.344E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="205600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2376500" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.71153" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.18E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="35.215" />
-  <B value="-8.5522E-16" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.3565" />
-  <B value="0.25354" />
-  <C value="373.53" />
-  <D value="0.26514" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="373.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="48.34868" />
-  <B value="-3078.428" />
-  <C value="-4.229632" />
-  <D value="6.844234E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="177.19" />
-  <Tmax units="K"  value="373.56" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.7198E+07" />
-  <B value="0.69517" />
-  <C value="-0.69951" />
-  <D value="0.51422" />
-  <E value="-0.11694" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="363.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14680" />
-  <B value="1308" />
-  <C value="-20.353" />
-  <D value="0.18038" />
-  <E value="-0.00052695" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="130" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68743" />
-  <B value="-100800" />
-  <C value="1016.4" />
-  <D value="-3.3645" />
-  <E value="0.0037533" />
-  <Tmin units="K"  value="187.67" />
-  <Tmax units="K"  value="370" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33121.9" />
-  <B value="-869.6079" />
-  <C value="9.605736" />
-  <D value="0.00110059" />
-  <E value="-3.859399E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.053996" />
-  <B value="-21.785" />
-  <C value="-7.6379" />
-  <D value="493.56" />
-  <E value="-1758.3" />
-  <Tmin units="K"  value="261.24" />
-  <Tmax units="K"  value="1866" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="7.527" />
-  <B value="261.77" />
-  <C value="-3.1833" />
-  <D value="0.0000078743" />
-  <E value="2" />
-  <Tmin units="K"  value="187.68" />
-  <Tmax units="K"  value="350" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.4328E-08" />
-  <B value="1.0455" />
-  <C value="58.912" />
-  <D value="-13329" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="573.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.078369" />
-  <B value="-33.634" />
-  <C value="-0.24641" />
-  <D value="-0.0025463" />
-  <E value="-0.0000049089" />
-  <Tmin units="K"  value="193.15" />
-  <Tmax units="K"  value="292.42" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1.0611E-07" />
-  <B value="1.8773" />
-  <C value="-355.78" />
-  <D value="45782" />
-  <Tmin units="K"  value="212.8" />
-  <Tmax units="K"  value="600" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.006184" />
-  <B value="258.76" />
-  <C value="-6.4137" />
-  <D value="0.016755" />
-  <E value="-0.000040713" />
-  <Tmin units="K"  value="187.68" />
-  <Tmax units="K"  value="363.75" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="31940" />
-  <B value="1.436" />
-  <C value="0.02432" />
-  <D value="-0.00001176" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1400" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.158329" />
-  <B value="-2900" />
-  <C value="-17.4" />
-  <Tmin units="K"  value="263.0389" />
-  <Tmax units="K"  value="433.0389" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.576" />
-  <B value="2013.6" />
-  <C value="-12.348" />
-  <Tmin units="K"  value="224.47" />
-  <Tmax units="K"  value="334.4" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.3152" />
-  <B value="-0.036018" />
-  <C value="0.00004512" />
-  <Tmin units="K"  value="187.68" />
-  <Tmax units="K"  value="350" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0995289" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.49E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="343" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.285" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="27.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.77777" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0143" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.788408" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0941677" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0358604" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.234" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.241" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="1" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.010699" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.84234" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.0941677" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18000.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0358604" />
-<GCmethod name="PPR78" >
-  <group id="14"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="222"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7783-06-4" />
-<Smiles name="SMILES"  value="S " />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1911" />
-<CompoundID name="Name"  value="Ammonia" />
-<StructureFormula name="Structure"  value="NH3" />
-<Family name="Family"  value="78" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="405.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1.1353E+07" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.07247" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="239.82" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="195.41" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="195.41" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6111.09" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="17.031" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.02496" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.256" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="8.533E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24790" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.9E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0138" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.45E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.5898E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.64E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="192660" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5657000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.8625" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.1683E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="47.973" />
-  <B value="-1.0295E-08" />
-  <Tmin units="K"  value="194.15" />
-  <Tmax units="K"  value="203.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="4.0518" />
-  <B value="0.27129" />
-  <C value="405.4" />
-  <D value="0.31349" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="405.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="62.8849" />
-  <B value="-4136.862" />
-  <C value="-6.320663" />
-  <D value="9.203947E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="191.24" />
-  <Tmax units="K"  value="406.05" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.4542E+07" />
-  <B value="-1.3178" />
-  <C value="4.7194" />
-  <D value="-5.4808" />
-  <E value="2.4196" />
-  <Tmin units="K"  value="195.41" />
-  <Tmax units="K"  value="403.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5983.8" />
-  <B value="380.66" />
-  <C value="-0.59542" />
-  <D value="-0.00029099" />
-  <E value="0.0000049048" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="190" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="77659" />
-  <B value="-45330" />
-  <C value="445.74" />
-  <D value="-1.4197" />
-  <E value="0.0015508" />
-  <Tmin units="K"  value="195.45" />
-  <Tmax units="K"  value="401.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33239" />
-  <B value="-913.64" />
-  <C value="10.802" />
-  <D value="0.00021047" />
-  <E value="-4.1739E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.022146" />
-  <B value="-24.138" />
-  <C value="-4.7806" />
-  <D value="-283.84" />
-  <E value="438.72" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="700" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-39.742" />
-  <B value="1486.5" />
-  <C value="4.7749" />
-  <D value="-0.000015796" />
-  <E value="2" />
-  <Tmin units="K"  value="195.41" />
-  <Tmax units="K"  value="398.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000000459" />
-  <B value="0.96936" />
-  <C value="48.366" />
-  <D value="-2671.4" />
-  <Tmin units="K"  value="194.6" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.95309" />
-  <B value="14.684" />
-  <C value="0.56768" />
-  <D value="-0.00028968" />
-  <E value="-0.0000019238" />
-  <Tmin units="K"  value="195.41" />
-  <Tmax units="K"  value="400.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000016165" />
-  <B value="1.3146" />
-  <C value="75.168" />
-  <D value="-8202.1" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="900" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01195" />
-  <B value="209.99" />
-  <C value="-5.1813" />
-  <D value="0.011762" />
-  <E value="-0.000027715" />
-  <Tmin units="K"  value="195.41" />
-  <Tmax units="K"  value="405.55" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="35237" />
-  <B value="-35.045" />
-  <C value="0.1697" />
-  <D value="-0.00017677" />
-  <E value="6.3273E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="4.496581" />
-  <B value="-2921.581" />
-  <C value="-67.15132" />
-  <Tmin units="K"  value="203" />
-  <Tmax units="K"  value="405" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.41" />
-  <B value="2389.4" />
-  <C value="-20.094" />
-  <Tmin units="K"  value="245.37" />
-  <Tmax units="K"  value="363.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.4864" />
-  <B value="-0.018932" />
-  <C value="0.000013325" />
-  <Tmin units="K"  value="195.41" />
-  <Tmax units="K"  value="398.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.07011" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.15E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="358" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="20.7" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.15459" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0108" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.616067" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.26199" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0249801" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.9097" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.98" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="1" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.975515" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.087598" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.78649" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2517" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="29224.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0249801" />
-<Umr name="UMR" >
-  <group id="223"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7664-41-7" />
-<Smiles name="SMILES"  value="N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="919" />
-<CompoundID name="Name"  value="Neon" />
-<StructureFormula name="Structure"  value="Ne" />
-<Family name="Family"  value="74" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="44.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2653000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0417" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.3" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="27.09" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="24.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="24.56" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="43300" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="20.1797" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0167622" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="-0.0395988" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="0" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="9440" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.01033" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.94E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="146219" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="328100" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.41453" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="74.691" />
-  <B value="-2.7704E-15" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="7.3718" />
-  <B value="0.3067" />
-  <C value="44.4" />
-  <D value="0.2786" />
-  <Tmin units="K"  value="24.56" />
-  <Tmax units="K"  value="44.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="29.459" />
-  <B value="-269.41" />
-  <C value="-2.5349" />
-  <D value="0.00051726" />
-  <E value="2" />
-  <Tmin units="K"  value="23.45" />
-  <Tmax units="K"  value="44.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1420900" />
-  <B value="-0.63029" />
-  <C value="-0.0022325" />
-  <D value="1.6268" />
-  <E value="-0.7611" />
-  <Tmin units="K"  value="24.54" />
-  <Tmax units="K"  value="44" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29948" />
-  <B value="-243.96" />
-  <C value="32.083" />
-  <D value="-0.79445" />
-  <E value="0.01023" />
-  <Tmin units="K"  value="24.56" />
-  <Tmax units="K"  value="40" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="20786" />
-  <B value="-1728.5" />
-  <C value="-21.855" />
-  <D value="0.0020512" />
-  <E value="2.1139E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.015332" />
-  <B value="-1.1833" />
-  <C value="-0.0082949" />
-  <D value="0.0010901" />
-  <E value="-0.00047018" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1332" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-83.002" />
-  <B value="434.94" />
-  <C value="18.35" />
-  <D value="-0.0034996" />
-  <E value="2" />
-  <Tmin units="K"  value="25.09" />
-  <Tmax units="K"  value="44.13" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.6731E-07" />
-  <B value="0.65634" />
-  <C value="5.8941" />
-  <D value="175.84" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="2000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.49811" />
-  <B value="-1.8025" />
-  <C value="-0.49257" />
-  <D value="0.0090166" />
-  <E value="-0.00024023" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="44" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0011717" />
-  <B value="0.66099" />
-  <C value="12.109" />
-  <D value="-70.155" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="2000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013077" />
-  <B value="-9.4638" />
-  <C value="-2.5288" />
-  <D value="-0.052153" />
-  <E value="0.00036172" />
-  <Tmin units="K"  value="24" />
-  <Tmax units="K"  value="43.36" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="20772.31" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.000127" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="18.782" />
-  <B value="165.29" />
-  <C value="-4.297" />
-  <Tmin units="K"  value="26.65" />
-  <Tmax units="K"  value="39.18" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-7.0259" />
-  <B value="-0.062253" />
-  <C value="-0.00034802" />
-  <Tmin units="K"  value="25.09" />
-  <Tmax units="K"  value="44.13" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0551691" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="2.744173E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="38.01305" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="5.98" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00444" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.20168" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="-0.0413762" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0167622" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.680949" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.776" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="-0.0413762" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="9417.34" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0167622" />
-<Umr name="UMR" >
-  <group id="202"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7440-01-9" />
-<Smiles name="SMILES"  value="[Ne]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1903" />
-<CompoundID name="Name"  value="Nitric acid" />
-<StructureFormula name="Structure"  value="HNO3" />
-<Family name="Family"  value="77" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="520" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6890100" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.145" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.231" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="356.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="231.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="231.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="60.7682" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="63.0128" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.041734" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.714406" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.2491E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="29610" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.24E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02486" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.91E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.343E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-7.401E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="266370" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.047E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.1998" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="1.34E+07" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="30.073" />
-  <B value="-1.103E-09" />
-  <Tmin units="K"  value="231.55" />
-  <Tmax units="K"  value="241.05" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="6.9293" />
-  <B value="0.47274" />
-  <C value="520" />
-  <D value="0.49837" />
-  <Tmin units="K"  value="231.55" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="26.654" />
-  <B value="-5017.1" />
-  <C value="-0.036699" />
-  <D value="-0.0000064771" />
-  <E value="2" />
-  <Tmin units="K"  value="231.55" />
-  <Tmax units="K"  value="376.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.01E+07" />
-  <B value="0.68707" />
-  <C value="-0.0019914" />
-  <D value="0.0028792" />
-  <E value="-0.0014403" />
-  <Tmin units="K"  value="231.55" />
-  <Tmax units="K"  value="359.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15807" />
-  <B value="1147" />
-  <C value="-8.2333" />
-  <D value="0.029082" />
-  <E value="-0.000034574" />
-  <Tmin units="K"  value="22.94" />
-  <Tmax units="K"  value="225.42" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="111110" />
-  <B value="-611.57" />
-  <C value="-2.7202" />
-  <D value="0.014286" />
-  <E value="-0.000033905" />
-  <Tmin units="K"  value="238.57" />
-  <Tmax units="K"  value="302.89" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="32639" />
-  <B value="-463.06" />
-  <C value="11.547" />
-  <D value="-0.00011018" />
-  <E value="4.1801E-09" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="264.29" />
-  <B value="-7985" />
-  <C value="-44.099" />
-  <D value="0.000074947" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="367.9" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.2234E-07" />
-  <B value="0.72283" />
-  <C value="140.72" />
-  <D value="-0.0025913" />
-  <Tmin units="K"  value="231.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.15591" />
-  <B value="-186.43" />
-  <C value="-2.2714" />
-  <D value="0.0033214" />
-  <E value="-0.0000018932" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="433.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00063365" />
-  <B value="0.72057" />
-  <C value="645.24" />
-  <D value="0.005306" />
-  <Tmin units="K"  value="356.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="0.0024017" />
-  <B value="-360.8" />
-  <C value="0.85285" />
-  <D value="-0.011656" />
-  <E value="0.00000622" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="313.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="17609.83" />
-  <B value="143.171" />
-  <C value="-0.0711401" />
-  <D value="0" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.093" />
-  <B value="3202.8" />
-  <C value="-52.952" />
-  <Tmin units="K"  value="313.15" />
-  <Tmax units="K"  value="376.1" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.56421" />
-  <B value="-0.038177" />
-  <C value="0.000041918" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="367.9" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.13222" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.688965E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="173.748" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="25.18" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-5.603" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0241" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.52364" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.71438" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.041734" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.638761" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.564" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="8.661" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.714406" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="29605.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.041734" />
-<CAS name="CAS number"  value="7697-37-2" />
-<Smiles name="SMILES"  value="ON(=O)=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="912" />
-<CompoundID name="Name"  value="Nitric oxide" />
-<StructureFormula name="Structure"  value="NO" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="180" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6480000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.058" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="121.38" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="112.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="109.5" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="21890" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="30.006" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.02344" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.582" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.488E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23120" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.1E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0139" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.46487E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="9.025E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="8.657E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="210600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2301000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3447" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-9.02489E+07" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="52.715" />
-  <B value="-0.013637" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="109.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.1354" />
-  <B value="0.19686" />
-  <C value="180.16" />
-  <D value="0.15443" />
-  <Tmin units="K"  value="109.5" />
-  <Tmax units="K"  value="180.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="98.67523" />
-  <B value="-3011.477" />
-  <C value="-13.21121" />
-  <D value="0.000072078" />
-  <E value="2" />
-  <Tmin units="K"  value="106.16" />
-  <Tmax units="K"  value="180.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.4721E+07" />
-  <B value="2.2365" />
-  <C value="-5.8672" />
-  <D value="6.8169" />
-  <E value="-2.7529" />
-  <Tmin units="K"  value="109.5" />
-  <Tmax units="K"  value="176.43" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="38756" />
-  <B value="-323.94" />
-  <C value="15.685" />
-  <D value="-0.060412" />
-  <E value="0.00033434" />
-  <Tmin units="K"  value="109.5" />
-  <Tmax units="K"  value="150" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29831.89" />
-  <B value="-2622.96" />
-  <C value="12.94433" />
-  <D value="-0.00260975" />
-  <E value="6.261468E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.019784" />
-  <B value="-8.5287" />
-  <C value="-0.2596" />
-  <D value="0.022481" />
-  <E value="-0.1424" />
-  <Tmin units="K"  value="90.15" />
-  <Tmax units="K"  value="901.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-50.098" />
-  <B value="734.63" />
-  <C value="8.0267" />
-  <D value="-0.00017996" />
-  <E value="2" />
-  <Tmin units="K"  value="109.15" />
-  <Tmax units="K"  value="180.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010289" />
-  <B value="0.55954" />
-  <C value="89.353" />
-  <D value="515.43" />
-  <Tmin units="K"  value="110" />
-  <Tmax units="K"  value="1773.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.85384" />
-  <B value="4.7868" />
-  <C value="-0.010049" />
-  <D value="0.0010454" />
-  <E value="-0.0000086044" />
-  <Tmin units="K"  value="81" />
-  <Tmax units="K"  value="176.4" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00046657" />
-  <B value="0.73353" />
-  <C value="58.917" />
-  <D value="-625.75" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="750" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0028436" />
-  <B value="551.06" />
-  <C value="-17.017" />
-  <D value="0.13002" />
-  <E value="-0.00047689" />
-  <Tmin units="K"  value="109.5" />
-  <Tmax units="K"  value="176.43" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="37698" />
-  <B value="-63.556" />
-  <C value="0.17178" />
-  <D value="-0.00017926" />
-  <E value="6.7015E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.389" />
-  <B value="1041.3" />
-  <C value="-25.5" />
-  <Tmin units="K"  value="110.7" />
-  <Tmax units="K"  value="161.56" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-6.7207" />
-  <B value="0.0029181" />
-  <C value="-0.00012236" />
-  <Tmin units="K"  value="109.15" />
-  <Tmax units="K"  value="180.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0665" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.794133E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="81.09816" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="10.65" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00897" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.0713227" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.5896" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0234267" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.9163" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.9859" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.582944" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23117.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0234267" />
-<GCmethod name="PPR78" >
-  <group id="27"  value="1" />
-  </GCmethod>
-<CAS name="CAS number"  value="10102-43-9" />
-<Smiles name="SMILES"  value="[N]=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="900" />
-<CompoundID name="Name"  value="Nitrogen dioxide" />
-<StructureFormula name="Structure"  value="ONO" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="431.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1.01325E+07" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.08249" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.233" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="294.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="261.9" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="261.9" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="18728.3" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="46.0055" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.031997" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.851088" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.431E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="33390" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.05E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.01598" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.827E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="3.318E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.1328E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="239920" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.465E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.21704" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.30954E+07" />
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.2179" />
-  <B value="0.22994" />
-  <C value="431.38" />
-  <D value="0.19006" />
-  <Tmin units="K"  value="261.9" />
-  <Tmax units="K"  value="431.37" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="18.404" />
-  <B value="-3508.6" />
-  <C value="0.81255" />
-  <D value="0.0000049983" />
-  <E value="2" />
-  <Tmin units="K"  value="252.77" />
-  <Tmax units="K"  value="431.37" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.37E+07" />
-  <B value="0.3" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="291.15" />
-  <Tmax units="K"  value="431.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="14.968" />
-  <B value="997.55" />
-  <C value="-5.6124" />
-  <D value="0.014033" />
-  <E value="-0.000013158" />
-  <Tmin units="K"  value="261.95" />
-  <Tmax units="K"  value="271.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="77435" />
-  <B value="432.69" />
-  <C value="5.3737" />
-  <D value="0.020804" />
-  <E value="-0.000021695" />
-  <Tmin units="K"  value="261" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="32962.96" />
-  <B value="-578.7755" />
-  <C value="10.44921" />
-  <D value="0.0000793322" />
-  <E value="-5.181036E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-311.49" />
-  <B value="10041" />
-  <C value="49.027" />
-  <D value="-0.00010518" />
-  <E value="2" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2078E-08" />
-  <B value="1.1399" />
-  <C value="-382.56" />
-  <D value="78187" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11611" />
-  <B value="127610" />
-  <C value="-1409.1" />
-  <D value="5.1777" />
-  <E value="-0.0063738" />
-  <Tmin units="K"  value="270" />
-  <Tmax units="K"  value="350" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.070851" />
-  <B value="-0.2143" />
-  <C value="-1258" />
-  <D value="429500" />
-  <Tmin units="K"  value="420" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.093346" />
-  <B value="-80.091" />
-  <C value="-1.095" />
-  <D value="-0.0026037" />
-  <E value="2.0771E-07" />
-  <Tmin units="K"  value="261.9" />
-  <Tmax units="K"  value="422.24" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29053.13" />
-  <B value="34.51315" />
-  <C value="-0.00987307" />
-  <D value="-7.237807E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="27.248" />
-  <B value="5290" />
-  <C value="42.102" />
-  <Tmin units="K"  value="264.04" />
-  <Tmax units="K"  value="386.61" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-8.1207" />
-  <B value="0.013877" />
-  <C value="-0.000042964" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0945914" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.665358E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="148.6014" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="16.76" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.9491" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0129" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.46976" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.86339" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0317854" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.053395" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.1308" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.29742" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.851088" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="33494.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0317854" />
-<CAS name="CAS number"  value="10102-44-0" />
-<Smiles name="SMILES"  value="O=[N]=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="905" />
-<CompoundID name="Name"  value="Nitrogen" />
-<StructureFormula name="Structure"  value="N2" />
-<Family name="Family"  value="74" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="126.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3398000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0901" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.289" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="77.35" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="63.149" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="63.149" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="12520" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="28.014" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.03484" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.037" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.471E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="9082" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0158" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.72E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="191500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="720000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.54268" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="37.87" />
-  <B value="-0.06027" />
-  <Tmin units="K"  value="20.65" />
-  <Tmax units="K"  value="63.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.435" />
-  <B value="0.25137" />
-  <C value="126.27" />
-  <D value="0.249" />
-  <Tmin units="K"  value="63.15" />
-  <Tmax units="K"  value="126.26" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="42.32946" />
-  <B value="-965.9771" />
-  <C value="-4.321774" />
-  <D value="0.0000797271" />
-  <E value="2" />
-  <Tmin units="K"  value="60.81" />
-  <Tmax units="K"  value="126.26" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.7284E+07" />
-  <B value="7.8021" />
-  <C value="-19.125" />
-  <D value="19.518" />
-  <E value="-7.5428" />
-  <Tmin units="K"  value="63.15" />
-  <Tmax units="K"  value="126.26" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="383890" />
-  <B value="-28798" />
-  <C value="875.74" />
-  <D value="-11.589" />
-  <E value="0.057106" />
-  <Tmin units="K"  value="32.8" />
-  <Tmax units="K"  value="63" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="55135" />
-  <B value="217.45" />
-  <C value="-0.9071" />
-  <D value="0.05327" />
-  <E value="0.00024166" />
-  <Tmin units="K"  value="63.15" />
-  <Tmax units="K"  value="115" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29103.63" />
-  <B value="-2305.946" />
-  <C value="11.31935" />
-  <D value="-0.00100557" />
-  <E value="1.706099E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.043512" />
-  <B value="-13.524" />
-  <C value="-0.091223" />
-  <D value="0.10229" />
-  <E value="-0.078721" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="1400" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="3.4358" />
-  <B value="-24.706" />
-  <C value="-2.6748" />
-  <D value="-0.000041603" />
-  <E value="2" />
-  <Tmin units="K"  value="63.15" />
-  <Tmax units="K"  value="125" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.6051E-07" />
-  <B value="0.65049" />
-  <C value="5.8019" />
-  <D value="2822.7" />
-  <Tmin units="K"  value="63.15" />
-  <Tmax units="K"  value="1970" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.21743" />
-  <B value="10.383" />
-  <C value="-1.0631" />
-  <D value="0.00036245" />
-  <E value="-0.000023265" />
-  <Tmin units="K"  value="60" />
-  <Tmax units="K"  value="124" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0003395" />
-  <B value="0.76921" />
-  <C value="19.592" />
-  <D value="293.93" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="2000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0025409" />
-  <B value="96.836" />
-  <C value="-7.6473" />
-  <D value="0.05313" />
-  <E value="-0.00036553" />
-  <Tmin units="K"  value="63.15" />
-  <Tmax units="K"  value="126.2" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="29425" />
-  <B value="-2.1701" />
-  <C value="0.00058201" />
-  <D value="0.000013054" />
-  <E value="-8.2313E-09" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.00058" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.455" />
-  <B value="682.85" />
-  <C value="-0.86615" />
-  <Tmin units="K"  value="76" />
-  <Tmax units="K"  value="112.93" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-5.5907" />
-  <B value="-0.045786" />
-  <C value="0.000062538" />
-  <Tmin units="K"  value="63.15" />
-  <Tmax units="K"  value="125" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0901499" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.710301E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="94.45061" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2906" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="18.5" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0107" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.806374" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0357998" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0346723" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.0415" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.088" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.011016" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.045" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="9081.94" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0346723" />
-<GCmethod name="PPR78" >
-  <group id="13"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="209"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7727-37-9" />
-<Smiles name="SMILES"  value="N#N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="899" />
-<CompoundID name="Name"  value="Nitrous oxide" />
-<StructureFormula name="Structure"  value="NON" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="309.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7255000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.097" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="184.67" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="182.33" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="182.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="87850" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="44.013" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0359" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.162" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="9.537E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="8275" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.57E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0189" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.12637E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="8.205E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.0416E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="219850" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6539000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.72733" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.20482E+07" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="36.489" />
-  <B value="-3.8239E-08" />
-  <Tmin units="K"  value="78.15" />
-  <Tmax units="K"  value="87.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.0978" />
-  <B value="0.2338" />
-  <C value="309.6" />
-  <D value="0.25899" />
-  <Tmin units="K"  value="182.3" />
-  <Tmax units="K"  value="309.55" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="50.69662" />
-  <B value="-2836.473" />
-  <C value="-4.609937" />
-  <D value="7.237315E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="179.17" />
-  <Tmax units="K"  value="309.57" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.585559E+07" />
-  <B value="0.982629" />
-  <C value="-2.292314" />
-  <D value="3.369827" />
-  <E value="-1.65657" />
-  <Tmin units="K"  value="182.3" />
-  <Tmax units="K"  value="309.57" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15429" />
-  <B value="1311.3" />
-  <C value="-11.544" />
-  <D value="0.047904" />
-  <E value="-0.000064108" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="180" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="72525" />
-  <B value="232.93" />
-  <C value="2.2666" />
-  <D value="0.037329" />
-  <E value="-0.000055304" />
-  <Tmin units="K"  value="182.3" />
-  <Tmax units="K"  value="200" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="28650" />
-  <B value="-400.03" />
-  <C value="10.5" />
-  <D value="0.00014292" />
-  <E value="-6.728E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.043828" />
-  <B value="-34.614" />
-  <C value="-1.5496" />
-  <D value="-7.0657" />
-  <E value="0.77444" />
-  <Tmin units="K"  value="154.79" />
-  <Tmax units="K"  value="1773.15" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.876" />
-  <B value="472.99" />
-  <C value="0.14659" />
-  <D value="-0.000013815" />
-  <E value="2" />
-  <Tmin units="K"  value="210" />
-  <Tmax units="K"  value="283.09" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000020512" />
-  <B value="0.47044" />
-  <C value="305.02" />
-  <D value="-521.81" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="1773.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10112" />
-  <B value="-5274.1" />
-  <C value="16.778" />
-  <D value="-0.037729" />
-  <E value="-0.000048678" />
-  <Tmin units="K"  value="277.59" />
-  <Tmax units="K"  value="287.09" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.001121" />
-  <B value="0.66298" />
-  <C value="524.68" />
-  <D value="7332.7" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012364" />
-  <B value="-124.21" />
-  <C value="-1.4299" />
-  <D value="-0.0041148" />
-  <E value="-0.000013653" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="309.57" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="26315" />
-  <B value="28.278" />
-  <C value="0.08223" />
-  <D value="-0.00015631" />
-  <E value="7.3999E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.381181" />
-  <B value="-800" />
-  <C value="-4.8" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="424.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.613" />
-  <B value="1311.9" />
-  <C value="-40.474" />
-  <Tmin units="K"  value="187.55" />
-  <Tmax units="K"  value="276.08" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.4961" />
-  <B value="-0.022349" />
-  <C value="0.000016718" />
-  <Tmin units="K"  value="210" />
-  <Tmax units="K"  value="283.09" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0979999" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.071681E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="188.7555" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="35.9" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.64292" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0142" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.81688" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1691" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.036002" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.238" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.2442" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.9128" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.140894" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20308" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.036002" />
-<CAS name="CAS number"  value="10024-97-2" />
-<Smiles name="SMILES"  value="[O-][N+]#N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="901" />
-<CompoundID name="Name"  value="Oxygen" />
-<StructureFormula name="Structure"  value="O2" />
-<Family name="Family"  value="74" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="154.58" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5043000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.07337" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.288" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="90.17" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="54.361" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="54.361" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="150" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="31.999" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.02785" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.022" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.8E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="8182" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.013" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.35E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="205043" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="444000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.51298" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="44.552" />
-  <B value="-4.4857E-08" />
-  <Tmin units="K"  value="20.65" />
-  <Tmax units="K"  value="30.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.6097" />
-  <B value="0.23614" />
-  <C value="154.78" />
-  <D value="0.23695" />
-  <Tmin units="K"  value="54.35" />
-  <Tmax units="K"  value="154.77" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="40.55487" />
-  <B value="-1120.543" />
-  <C value="-3.776114" />
-  <D value="0.0000485344" />
-  <E value="2" />
-  <Tmin units="K"  value="54.35" />
-  <Tmax units="K"  value="154.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.0672E+07" />
-  <B value="1.5661" />
-  <C value="-3.4356" />
-  <D value="3.5416" />
-  <E value="-1.2718" />
-  <Tmin units="K"  value="54.36" />
-  <Tmax units="K"  value="154.58" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15381" />
-  <B value="1601.9" />
-  <C value="-10.968" />
-  <D value="0.24187" />
-  <E value="-0.0020734" />
-  <Tmin units="K"  value="13.46" />
-  <Tmax units="K"  value="43.78" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="53393" />
-  <B value="-1966.4" />
-  <C value="48.21" />
-  <D value="-0.31631" />
-  <E value="0.0010466" />
-  <Tmin units="K"  value="54.36" />
-  <Tmax units="K"  value="145" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29061.62" />
-  <B value="-1470.897" />
-  <C value="11.10778" />
-  <D value="-0.00128484" />
-  <E value="3.183122E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.039522" />
-  <B value="-15.729" />
-  <C value="-0.082121" />
-  <D value="0.012408" />
-  <E value="-0.0087531" />
-  <Tmin units="K"  value="77.29" />
-  <Tmax units="K"  value="1200" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-5.2319" />
-  <B value="116.13" />
-  <C value="-1.0315" />
-  <D value="0.0000034376" />
-  <E value="2" />
-  <Tmin units="K"  value="54.36" />
-  <Tmax units="K"  value="150" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.0134E-07" />
-  <B value="0.60321" />
-  <C value="56.09" />
-  <D value="1584.9" />
-  <Tmin units="K"  value="54.35" />
-  <Tmax units="K"  value="1950" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.19654" />
-  <B value="-10.535" />
-  <C value="-0.46717" />
-  <D value="-0.0052064" />
-  <E value="-3.3418E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="150" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0004508" />
-  <B value="0.74544" />
-  <C value="58.278" />
-  <D value="-562.62" />
-  <Tmin units="K"  value="60" />
-  <Tmax units="K"  value="2000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0062662" />
-  <B value="17.53" />
-  <C value="-3.9173" />
-  <D value="0.0058473" />
-  <E value="-0.000091613" />
-  <Tmin units="K"  value="54.35" />
-  <Tmax units="K"  value="154.58" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="30182" />
-  <B value="-14.916" />
-  <C value="0.054709" />
-  <D value="-0.00004997" />
-  <E value="1.4883E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.000494" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.836" />
-  <B value="842.12" />
-  <C value="0.35556" />
-  <Tmin units="K"  value="92.87" />
-  <Tmax units="K"  value="138.76" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.5492" />
-  <B value="-0.061584" />
-  <C value="0.00019142" />
-  <Tmin units="K"  value="54.36" />
-  <Tmax units="K"  value="150" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0737899" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.479206E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="114.2561" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2908" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="16.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00953" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.13768" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0297998" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0280225" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.857" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.94" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.019" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="8181.93" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0280225" />
-<GCmethod name="PPR78" >
-  <group id="26"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="210"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7782-44-7" />
-<Smiles name="SMILES"  value="O=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="910" />
-<CompoundID name="Name"  value="Sulfur dioxide" />
-<StructureFormula name="Structure"  value="OSO" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="430.75" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7884100" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.122" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="263.13" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="200" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="197.67" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1674.39" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="64.0638" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04688" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.245381" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.66E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12270" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.44E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02573" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.03E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.9684E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.0012E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="248100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7401000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.86399" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="32.096" />
-  <B value="-0.018032" />
-  <Tmin units="K"  value="79.07" />
-  <Tmax units="K"  value="197.67" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.8477" />
-  <B value="0.24254" />
-  <C value="430.75" />
-  <D value="0.27051" />
-  <Tmin units="K"  value="197.67" />
-  <Tmax units="K"  value="430.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="53.52766" />
-  <B value="-4260.124" />
-  <C value="-4.670429" />
-  <D value="0.0000030272" />
-  <E value="2" />
-  <Tmin units="K"  value="195.12" />
-  <Tmax units="K"  value="430.75" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.8914E+07" />
-  <B value="1.8091" />
-  <C value="-2.9053" />
-  <D value="2.2271" />
-  <E value="-0.64793" />
-  <Tmin units="K"  value="197.67" />
-  <Tmax units="K"  value="430.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-22618" />
-  <B value="1707.9" />
-  <C value="-16.235" />
-  <D value="0.074564" />
-  <E value="-0.00012295" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="197.68" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86911" />
-  <B value="53691" />
-  <C value="-599.94" />
-  <D value="2.2025" />
-  <E value="-0.0025885" />
-  <Tmin units="K"  value="197.67" />
-  <Tmax units="K"  value="350" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33406" />
-  <B value="-516.38" />
-  <C value="10.524" />
-  <D value="0.000013143" />
-  <E value="-6.1535E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.06722" />
-  <B value="-59.185" />
-  <C value="-7.1935" />
-  <D value="-46.116" />
-  <E value="-332.32" />
-  <Tmin units="K"  value="215.4" />
-  <Tmax units="K"  value="1723.2" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="50.887" />
-  <B value="-1574" />
-  <C value="-9.4517" />
-  <D value="1.5898E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000012144" />
-  <B value="0.53923" />
-  <C value="315.41" />
-  <D value="-2659.7" />
-  <Tmin units="K"  value="197.67" />
-  <Tmax units="K"  value="1250" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.21664" />
-  <B value="-2.2484" />
-  <C value="-0.50659" />
-  <D value="-0.0009424" />
-  <E value="-0.0000010218" />
-  <Tmin units="K"  value="197.67" />
-  <Tmax units="K"  value="400" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="23.316" />
-  <B value="-0.95324" />
-  <C value="-1567.4" />
-  <D value="1330100" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="900" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011604" />
-  <B value="175.94" />
-  <C value="-4.6965" />
-  <D value="0.008615" />
-  <E value="-0.000020963" />
-  <Tmin units="K"  value="197.67" />
-  <Tmax units="K"  value="430.75" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29454" />
-  <B value="40.762" />
-  <C value="-0.015859" />
-  <D value="0.0000004275" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-17.87311" />
-  <B value="-7500" />
-  <C value="-45" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="424.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.673" />
-  <B value="2268.2" />
-  <C value="-39.619" />
-  <Tmin units="K"  value="259.01" />
-  <Tmax units="K"  value="381.68" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.4294" />
-  <B value="-0.011984" />
-  <C value="-0.0000026289" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.12522" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.04E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="347" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="41.8" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.27539" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0181" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.39556" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.256" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0438228" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.6961" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.612" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.1906" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2462" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="12272.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0438228" />
-<GCmethod name="PPR78" >
-  <group id="25"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="216"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7446-09-5" />
-<Smiles name="SMILES"  value="O=[S]=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="911" />
-<CompoundID name="Name"  value="Sulfur trioxide" />
-<StructureFormula name="Structure"  value="SO3" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="490.85" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="8210000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.127" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="317.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="289.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="289.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="21130" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="80.0632" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0420954" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.42396" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.189E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="31130" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03254" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.93094E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.9572E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.7095E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="256510" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7532000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1122" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="1.422E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="28.604" />
-  <B value="2.2061E-09" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="182.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.6186" />
-  <B value="0.20129" />
-  <C value="490.85" />
-  <D value="0.42123" />
-  <Tmin units="K"  value="289.95" />
-  <Tmax units="K"  value="490.85" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="351.6001" />
-  <B value="-18247.39" />
-  <C value="-49.77065" />
-  <D value="0.0000409297" />
-  <E value="2" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="490.85" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.1339E+07" />
-  <B value="0.77728" />
-  <C value="-0.42427" />
-  <D value="0.68287" />
-  <E value="-0.4608" />
-  <Tmin units="K"  value="289.94" />
-  <Tmax units="K"  value="490.85" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="136.4" />
-  <B value="10046" />
-  <C value="-51.148" />
-  <D value="0.11574" />
-  <E value="-0.000098203" />
-  <Tmin units="K"  value="289.95" />
-  <Tmax units="K"  value="299.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="258090" />
-  <B value="-3271.8" />
-  <C value="-8.4929" />
-  <D value="0.0035868" />
-  <E value="-0.000028801" />
-  <Tmin units="K"  value="303.15" />
-  <Tmax units="K"  value="312.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="32986" />
-  <B value="-404.97" />
-  <C value="11.171" />
-  <D value="-0.000087925" />
-  <E value="-8.9809E-09" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.085136" />
-  <B value="-80.336" />
-  <C value="-11.216" />
-  <D value="-300.69" />
-  <E value="-904.24" />
-  <Tmin units="K"  value="245.4" />
-  <Tmax units="K"  value="1785.4" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-260.71" />
-  <B value="11505" />
-  <C value="38.839" />
-  <D value="-0.000061621" />
-  <E value="2" />
-  <Tmin units="K"  value="289.95" />
-  <Tmax units="K"  value="329.14" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010033" />
-  <B value="0.54515" />
-  <C value="135.63" />
-  <D value="19402" />
-  <Tmin units="K"  value="198.15" />
-  <Tmax units="K"  value="694.19" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.021077" />
-  <B value="585.52" />
-  <C value="-5.8227" />
-  <D value="0.016099" />
-  <E value="-0.000027318" />
-  <Tmin units="K"  value="282.51" />
-  <Tmax units="K"  value="481.47" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1.1717" />
-  <B value="-0.2465" />
-  <C value="2002.7" />
-  <D value="1327100" />
-  <Tmin units="K"  value="317.9" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010614" />
-  <B value="342.37" />
-  <C value="-5.975" />
-  <D value="0.012246" />
-  <E value="-0.000021992" />
-  <Tmin units="K"  value="289.95" />
-  <Tmax units="K"  value="490.85" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="24221" />
-  <B value="110.09" />
-  <C value="-0.076359" />
-  <D value="0.000018362" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.750077" />
-  <B value="-1800" />
-  <C value="-10.8" />
-  <Tmin units="K"  value="275.2611" />
-  <Tmax units="K"  value="445.2611" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.098" />
-  <B value="1473.6" />
-  <C value="-145.67" />
-  <Tmin units="K"  value="297.45" />
-  <Tmax units="K"  value="437.98" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="13.354" />
-  <B value="-0.096392" />
-  <C value="0.00010215" />
-  <Tmin units="K"  value="289.95" />
-  <Tmax units="K"  value="329.14" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.12556" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.834275E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="234.1028" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="41.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.5483" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0183" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.88018" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.42396" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0420954" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.145023" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.972376" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="14.303" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.42396" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="31130" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0420954" />
-<CAS name="CAS number"  value="7446-11-9" />
-<Smiles name="SMILES"  value="O=S(=O)=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1521" />
-<CompoundID name="Name"  value="Chloroform" />
-<StructureFormula name="Structure"  value="CHCl3" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="536.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5500000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.24" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.296" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="334.33" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="209.63" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="209.63" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="68.1479" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="119.377" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08068" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.226" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.249E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18920" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0435" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.03E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.029E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-7.01E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="295600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9540000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.80821" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.8E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.968" />
-  <B value="-0.0028604" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="209.63" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53556" />
-  <B value="0.18404" />
-  <C value="536.5" />
-  <D value="0.18541" />
-  <Tmin units="K"  value="209" />
-  <Tmax units="K"  value="535.95" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="99.91512" />
-  <B value="-6781.559" />
-  <C value="-11.93873" />
-  <D value="0.0000115883" />
-  <E value="2" />
-  <Tmin units="K"  value="207.15" />
-  <Tmax units="K"  value="536.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.1382E+07" />
-  <B value="0.7027" />
-  <C value="0.36748" />
-  <D value="-1.351" />
-  <E value="0.69236" />
-  <Tmin units="K"  value="209.63" />
-  <Tmax units="K"  value="536.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="92520" />
-  <Tmin units="K"  value="283" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="93132" />
-  <B value="645.44" />
-  <C value="2.3739" />
-  <D value="0.024457" />
-  <E value="-0.000021097" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="366.48" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="36659" />
-  <B value="-308.1" />
-  <C value="11.299" />
-  <D value="0.00003137" />
-  <E value="-3.3538E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.13849" />
-  <B value="-177.09" />
-  <C value="-16.939" />
-  <D value="-624.1" />
-  <E value="-99.389" />
-  <Tmin units="K"  value="252" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-20.923" />
-  <B value="1248.9" />
-  <C value="1.655" />
-  <D value="-0.0000024787" />
-  <E value="2" />
-  <Tmin units="K"  value="209.63" />
-  <Tmax units="K"  value="353.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.8024E-07" />
-  <B value="0.76204" />
-  <C value="109.36" />
-  <D value="-1373.9" />
-  <Tmin units="K"  value="209.63" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.061417" />
-  <B value="-66.692" />
-  <C value="-1.6802" />
-  <D value="-0.001962" />
-  <E value="-0.0000044192" />
-  <Tmin units="K"  value="209.63" />
-  <Tmax units="K"  value="400" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00041167" />
-  <B value="0.84476" />
-  <C value="1870.6" />
-  <D value="-7829.5" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012805" />
-  <B value="80.496" />
-  <C value="-3.4786" />
-  <D value="0.0022559" />
-  <E value="-0.0000078228" />
-  <Tmin units="K"  value="209.63" />
-  <Tmax units="K"  value="536.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="19863" />
-  <B value="217.99" />
-  <C value="-0.26149" />
-  <D value="0.0001544" />
-  <E value="-3.517E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.214982" />
-  <B value="-2750" />
-  <C value="-16.5" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="424.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.534" />
-  <B value="3077.4" />
-  <C value="-26.818" />
-  <Tmin units="K"  value="322.04" />
-  <Tmax units="K"  value="480.55" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.33836" />
-  <B value="-0.03791" />
-  <C value="0.000046198" />
-  <Tmin units="K"  value="209.63" />
-  <Tmax units="K"  value="353.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.22663" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.31E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="355" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="81.21" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.02138" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0326" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.49815" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.21796" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0805048" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.7" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.34" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.34" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.0529" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2059" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18919.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0805048" />
-<UnifacVLE name="UNIFAC" >
-  <group id="51"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="37"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="39"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="51"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="51"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="50"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="67-66-3" />
-<Smiles name="SMILES"  value="C([Cl])([Cl])[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1771" />
-<CompoundID name="Name"  value="Hydrogen cyanide" />
-<StructureFormula name="Structure"  value="HCN" />
-<Family name="Family"  value="38" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="456.65" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5390000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.139" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.197" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="298.85" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="259.91" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="259.833" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="18625" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="27.0253" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0397695" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.409913" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.539E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24810" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.94E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.01813" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.0245E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.35143E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.24725E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="201719" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8405700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.62716" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.2329E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="38.186" />
-  <B value="-2.0999E-15" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3163" />
-  <B value="0.18425" />
-  <C value="456.65" />
-  <D value="0.2794" />
-  <Tmin units="K"  value="259.83" />
-  <Tmax units="K"  value="456.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="42.70101" />
-  <B value="-4001.496" />
-  <C value="-3.208729" />
-  <D value="5.620619E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="254.07" />
-  <Tmax units="K"  value="456.75" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.5225E+07" />
-  <B value="2.0549" />
-  <C value="-4.7432" />
-  <D value="4.7996" />
-  <E value="-1.8366" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="456.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11133" />
-  <B value="756.41" />
-  <C value="-4.0631" />
-  <D value="0.010136" />
-  <E value="-0.0000055005" />
-  <Tmin units="K"  value="21.69" />
-  <Tmax units="K"  value="254.19" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="70227" />
-  <B value="-10279" />
-  <C value="42.028" />
-  <D value="0.069085" />
-  <E value="-0.00024154" />
-  <Tmin units="K"  value="259.83" />
-  <Tmax units="K"  value="298.85" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29289" />
-  <B value="-482.84" />
-  <C value="10.404" />
-  <D value="-0.000041659" />
-  <E value="6.8553E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.056002" />
-  <B value="60.388" />
-  <C value="-41.174" />
-  <D value="14505" />
-  <E value="-43335" />
-  <Tmin units="K"  value="228.4" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.545" />
-  <B value="843.5" />
-  <C value="0.21344" />
-  <D value="-0.0000012673" />
-  <E value="2" />
-  <Tmin units="K"  value="259.83" />
-  <Tmax units="K"  value="298.85" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2749E-08" />
-  <B value="1.0633" />
-  <C value="338.59" />
-  <D value="155.3" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="425" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.06901" />
-  <B value="-183.38" />
-  <C value="0.87895" />
-  <D value="-0.0078031" />
-  <E value="0.000002353" />
-  <Tmin units="K"  value="259.83" />
-  <Tmax units="K"  value="298.85" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000015837" />
-  <B value="1.2055" />
-  <C value="-98.566" />
-  <D value="53091" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="673.15" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.058853" />
-  <B value="3.1548" />
-  <C value="-2.2488" />
-  <D value="-0.00076117" />
-  <E value="-0.000001168" />
-  <Tmin units="K"  value="259.83" />
-  <Tmax units="K"  value="456.65" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="24466" />
-  <B value="45.315" />
-  <C value="-0.025383" />
-  <D value="0.0000059361" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="121" />
-  <A value="1.78" />
-  <B value="30000" />
-  <C value="-1" />
-  <D value="0" />
-  <E value="70" />
-  <Tmin units="K"  value="275.2611" />
-  <Tmax units="K"  value="445.2611" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.862" />
-  <B value="3439.7" />
-  <C value="4.5325" />
-  <Tmin units="K"  value="277.18" />
-  <Tmax units="K"  value="408.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.6579" />
-  <B value="-0.030475" />
-  <C value="0.000035226" />
-  <Tmin units="K"  value="259.83" />
-  <Tmax units="K"  value="298.85" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0964163" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.790323E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="86.01517" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="22.75" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-5.00731" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0145" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.693958" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.409913" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0397695" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.1951" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.2098" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="10.34189" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.409913" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24806" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0397695" />
-<Umr name="UMR" >
-  <group id="221"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="74-90-8" />
-<Smiles name="SMILES"  value="C#N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1001" />
-<CompoundID name="Name"  value="Formaldehyde" />
-<StructureFormula name="Structure"  value="HCHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="408" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6590000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.115" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.223" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="254.05" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="181.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="181.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="887" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="30.026" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04097" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.281846" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.215E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21190" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.77E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0186" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.09E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.086E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.026E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="218660" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7050000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.86009" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.268E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="39.262" />
-  <B value="-0.024084" />
-  <Tmin units="K"  value="72.46" />
-  <Tmax units="K"  value="181.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.9413" />
-  <B value="0.22308" />
-  <C value="408" />
-  <D value="0.28569" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="396.06" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="62.07923" />
-  <B value="-4207.675" />
-  <C value="-6.202287" />
-  <D value="5.521233E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="163.7" />
-  <Tmax units="K"  value="408" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.0902E+07" />
-  <B value="0.29722" />
-  <C value="-0.051281" />
-  <D value="0.13234" />
-  <E value="-0.080686" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="396.06" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="39430" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62716" />
-  <B value="-69.453" />
-  <C value="3.2871" />
-  <D value="0.047782" />
-  <E value="-0.0001008" />
-  <Tmin units="K"  value="204" />
-  <Tmax units="K"  value="304" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33216.06" />
-  <B value="-1212.62" />
-  <C value="11.96032" />
-  <D value="-0.000635943" />
-  <E value="1.549232E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.084764" />
-  <B value="-73.106" />
-  <C value="-5.8267" />
-  <D value="281.42" />
-  <E value="-763.84" />
-  <Tmin units="K"  value="204" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.303" />
-  <B value="753.06" />
-  <C value="-0.013733" />
-  <D value="-4.6837E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="254.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.1997E-07" />
-  <B value="0.57256" />
-  <C value="258.17" />
-  <D value="-5091" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10999" />
-  <B value="-161.62" />
-  <C value="0.83463" />
-  <D value="-0.01142" />
-  <E value="0.0000060772" />
-  <Tmin units="K"  value="204" />
-  <Tmax units="K"  value="234" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="44.841" />
-  <B value="-0.71285" />
-  <C value="-3466.2" />
-  <D value="5262100" />
-  <Tmin units="K"  value="254.05" />
-  <Tmax units="K"  value="994.05" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016101" />
-  <B value="136.53" />
-  <C value="-3.7004" />
-  <D value="0.0067657" />
-  <E value="-0.000021523" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="396.06" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="26385.98" />
-  <B value="18.47571" />
-  <C value="0.0478984" />
-  <D value="-0.000030852" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.331" />
-  <B value="2684.7" />
-  <C value="-5.509" />
-  <Tmin units="K"  value="244.9" />
-  <Tmax units="K"  value="360.24" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.78709" />
-  <B value="-0.049255" />
-  <C value="0.000075747" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="254.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.10819" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.493448E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="120.0801" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="26.63" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0168" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.752445" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.26559" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0369129" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.9183" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.78" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.253" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23824.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0369129" />
-<UnifacVLE name="UNIFAC" >
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="21"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="26"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="50-00-0" />
-<Smiles name="SMILES"  value="C=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1502" />
-<CompoundID name="Name"  value="Methyl chloride" />
-<StructureFormula name="Structure"  value="CH3Cl" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="416.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6680000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.143" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.276" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="248.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="175.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="175.43" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="867.6" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="50.488" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.05059" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.151" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.442E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17320" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.24E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02529" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.92E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-8.196E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5.844E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="234180" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6548000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.72126" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.7538E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="23.768" />
-  <B value="-8.4567E-09" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="182.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.6672" />
-  <B value="0.24865" />
-  <C value="416.26" />
-  <D value="0.26843" />
-  <Tmin units="K"  value="175.43" />
-  <Tmax units="K"  value="416.25" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="73.95113" />
-  <B value="-4332.347" />
-  <C value="-8.308415" />
-  <D value="0.0000132119" />
-  <E value="2" />
-  <Tmin units="K"  value="173.65" />
-  <Tmax units="K"  value="416.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.0406E+07" />
-  <B value="0.41721" />
-  <C value="-0.045158" />
-  <D value="-0.067629" />
-  <E value="0.055437" />
-  <Tmin units="K"  value="175.43" />
-  <Tmax units="K"  value="403.58" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13360" />
-  <B value="1161" />
-  <C value="-7.5627" />
-  <D value="0.02419" />
-  <E value="-0.000020195" />
-  <Tmin units="K"  value="21.27" />
-  <Tmax units="K"  value="174.01" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="72914" />
-  <B value="778.6" />
-  <C value="-9.5627" />
-  <D value="0.081286" />
-  <E value="-0.000092921" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="32790.34" />
-  <B value="-743.4513" />
-  <C value="11.51178" />
-  <D value="-0.0000302967" />
-  <E value="1.138778E-09" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.093165" />
-  <B value="-83.56" />
-  <C value="-5.5445" />
-  <D value="-44.171" />
-  <E value="-96.437" />
-  <Tmin units="K"  value="208.12" />
-  <Tmax units="K"  value="1665" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-60.189" />
-  <B value="2252.1" />
-  <C value="8.022" />
-  <D value="-0.000019477" />
-  <E value="2" />
-  <Tmin units="K"  value="175.43" />
-  <Tmax units="K"  value="413.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.5916E-08" />
-  <B value="0.87071" />
-  <C value="35.619" />
-  <D value="35.603" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="700" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.22503" />
-  <B value="12.649" />
-  <C value="-0.64685" />
-  <D value="-0.0003032" />
-  <E value="-0.0000029812" />
-  <Tmin units="K"  value="175.43" />
-  <Tmax units="K"  value="350" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-22144" />
-  <B value="0.7661" />
-  <C value="-4.8548E+10" />
-  <D value="-3.7839E+10" />
-  <Tmin units="K"  value="213.15" />
-  <Tmax units="K"  value="750" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0076213" />
-  <B value="308.98" />
-  <C value="-6.5963" />
-  <D value="0.015546" />
-  <E value="-0.000032087" />
-  <Tmin units="K"  value="175.43" />
-  <Tmax units="K"  value="403.58" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="29749" />
-  <B value="-14.55" />
-  <C value="0.25534" />
-  <D value="-0.0003088" />
-  <E value="1.1707E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-14.43039" />
-  <B value="-9354.477" />
-  <C value="95.04079" />
-  <Tmin units="K"  value="203" />
-  <Tmax units="K"  value="416" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.62" />
-  <B value="2413.2" />
-  <C value="-9.7185" />
-  <Tmin units="K"  value="250.13" />
-  <Tmax units="K"  value="373.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.7183" />
-  <B value="-0.027855" />
-  <C value="0.000026626" />
-  <Tmin units="K"  value="175.43" />
-  <Tmax units="K"  value="413.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.13628" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.94E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="414" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="43.83" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.00835" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0197" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.915" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1472" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0501264" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.667106" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.568" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.20828" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.153068" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19719.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0501264" />
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="35"  value="1" />
-  </Asog>
-<CAS name="CAS number"  value="74-87-3" />
-<Smiles name="SMILES"  value="C[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1681" />
-<CompoundID name="Name"  value="Methyl iodide" />
-<StructureFormula name="Structure"  value="CH3I" />
-<Family name="Family"  value="31" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="528" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7370000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.185" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.311" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="315.58" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="206.7" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="206.7" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="254.555" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="141.939" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.062667" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.19716" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.035E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20180" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.4E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03285" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.6E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.3E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.47E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="254000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.70016" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-7.096E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="22.404" />
-  <B value="-0.011982" />
-  <Tmin units="K"  value="82.68" />
-  <Tmax units="K"  value="206.7" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3975" />
-  <B value="0.25854" />
-  <C value="528" />
-  <D value="0.2679" />
-  <Tmin units="K"  value="206.7" />
-  <Tmax units="K"  value="528" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="56.57754" />
-  <B value="-4804.529" />
-  <C value="-5.238128" />
-  <D value="3.097144E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="204.8" />
-  <Tmax units="K"  value="528" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.3737E+07" />
-  <B value="-0.25822" />
-  <C value="1.7219" />
-  <D value="-2.0034" />
-  <E value="0.83642" />
-  <Tmin units="K"  value="206.7" />
-  <Tmax units="K"  value="528" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="58860" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81227" />
-  <B value="-510450" />
-  <C value="4831.2" />
-  <D value="-15.234" />
-  <E value="0.016088" />
-  <Tmin units="K"  value="243.45" />
-  <Tmax units="K"  value="315.58" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33243" />
-  <B value="-588.89" />
-  <C value="11.23" />
-  <D value="0.00016737" />
-  <E value="-5.0885E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.091986" />
-  <B value="-122.96" />
-  <C value="-8.7523" />
-  <D value="-736.97" />
-  <E value="-492.42" />
-  <Tmin units="K"  value="264" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.0691" />
-  <B value="650.82" />
-  <C value="-0.30881" />
-  <D value="-1.1201E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="206.7" />
-  <Tmax units="K"  value="315.58" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.1469E-07" />
-  <B value="0.6322" />
-  <C value="292.39" />
-  <D value="-1664.7" />
-  <Tmin units="K"  value="206.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.025022" />
-  <B value="-2.7147" />
-  <C value="-2.1673" />
-  <D value="-0.0005511" />
-  <E value="-0.000004231" />
-  <Tmin units="K"  value="206.7" />
-  <Tmax units="K"  value="315.58" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.15913" />
-  <B value="0.010769" />
-  <C value="1577.4" />
-  <D value="2109400" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0089542" />
-  <B value="133.23" />
-  <C value="-3.9845" />
-  <D value="0.0046929" />
-  <E value="-0.000012515" />
-  <Tmin units="K"  value="206.7" />
-  <Tmax units="K"  value="528" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="14904.66" />
-  <B value="117.0558" />
-  <C value="-0.0691448" />
-  <D value="0.0000175067" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.958672" />
-  <B value="-3550" />
-  <C value="-21.3" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.002" />
-  <B value="3357.9" />
-  <C value="5.1859" />
-  <Tmin units="K"  value="317.11" />
-  <Tmax units="K"  value="460.36" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.7257" />
-  <B value="-0.031602" />
-  <C value="0.000039256" />
-  <Tmin units="K"  value="206.7" />
-  <Tmax units="K"  value="315.58" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.174097" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.318402E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="514.6174" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="52.63" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.026" />
-<SpecificGravity name="Specific gravity"  units="_"  value="2.29293" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.192721" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.062667" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.1651" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.84" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.192721" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20172.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.062667" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="64"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="45"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="64"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="63"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-88-4" />
-<Smiles name="SMILES"  value="CI" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1" />
-<CompoundID name="Name"  value="Methane" />
-<StructureFormula name="Structure"  value="CH4" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="190.56" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4599000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0986" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.286" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="111.66" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="90.694" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="90.694" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="11696" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="16.043" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.03554" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.011" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.118E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="11600" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.01705" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.88E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.452E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5.049E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="186270" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="941400" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.49258" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.0262E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="33.457" />
-  <B value="-0.033547" />
-  <C value="-0.000155" />
-  <Tmin units="K"  value="23.15" />
-  <Tmax units="K"  value="90.69" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.894" />
-  <B value="0.23603" />
-  <C value="191.05" />
-  <D value="0.21974" />
-  <Tmin units="K"  value="90.68" />
-  <Tmax units="K"  value="191.04" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="39.98844" />
-  <B value="-1337.308" />
-  <C value="-3.580049" />
-  <D value="0.0000320698" />
-  <E value="2" />
-  <Tmin units="K"  value="83.65" />
-  <Tmax units="K"  value="191.03" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.4418E+07" />
-  <B value="2.3055" />
-  <C value="-5.4199" />
-  <D value="5.658" />
-  <E value="-2.1286" />
-  <Tmin units="K"  value="90.67" />
-  <Tmax units="K"  value="190.55" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-3039.8" />
-  <B value="1292.4" />
-  <C value="-15.448" />
-  <D value="0.082442" />
-  <E value="-0.000070636" />
-  <Tmin units="K"  value="22.85" />
-  <Tmax units="K"  value="90.67" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="61157" />
-  <B value="5034.1" />
-  <C value="-48.913" />
-  <D value="-0.22998" />
-  <E value="0.0022243" />
-  <Tmin units="K"  value="88.71" />
-  <Tmax units="K"  value="190" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33151.9" />
-  <B value="-1220.001" />
-  <C value="12.0907" />
-  <D value="-0.000384791" />
-  <E value="9.896403E-08" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.051983" />
-  <B value="-25.636" />
-  <C value="-0.24722" />
-  <D value="0.42759" />
-  <E value="-0.39805" />
-  <Tmin units="K"  value="102" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-45.328" />
-  <B value="724.39" />
-  <C value="6.5917" />
-  <D value="-0.00010373" />
-  <E value="2" />
-  <Tmin units="K"  value="88.15" />
-  <Tmax units="K"  value="190" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.3432E-07" />
-  <B value="0.58831" />
-  <C value="114.58" />
-  <D value="-1338.5" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.011567" />
-  <B value="-46.041" />
-  <C value="0.10435" />
-  <D value="-0.012133" />
-  <E value="-0.0000051716" />
-  <Tmin units="K"  value="90.69" />
-  <Tmax units="K"  value="180" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000074705" />
-  <B value="1.4432" />
-  <C value="-57.569" />
-  <D value="587.82" />
-  <Tmin units="K"  value="111.63" />
-  <Tmax units="K"  value="600" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.040703" />
-  <B value="-6.9523" />
-  <C value="-2.3114" />
-  <D value="-0.0055565" />
-  <E value="0.0000057595" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="193.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="37981" />
-  <B value="-74.622" />
-  <C value="0.3019" />
-  <D value="-0.00028327" />
-  <E value="9.0711E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-7.274133" />
-  <B value="-850" />
-  <C value="-5.1" />
-  <Tmin units="K"  value="80.81667" />
-  <Tmax units="K"  value="250.8167" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.701" />
-  <B value="1035" />
-  <C value="1.2704" />
-  <Tmin units="K"  value="114.61" />
-  <Tmax units="K"  value="170.99" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-6.4555" />
-  <B value="-0.023994" />
-  <C value="0.000010045" />
-  <Tmin units="K"  value="88.15" />
-  <Tmax units="K"  value="190" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.09939" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.871667E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="137.3608" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2876" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="25.14" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0129" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.299394" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0074" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0378392" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.1239" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.152" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.012223" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="11618.44" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0378392" />
-<GCmethod name="PPR78" >
-  <group id="5"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="224"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="74-82-8" />
-<Smiles name="SMILES"  value="C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1101" />
-<CompoundID name="Name"  value="Methanol" />
-<StructureFormula name="Structure"  value="CH3OH" />
-<Family name="Family"  value="27" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="512.64" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="8097000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.118" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.224" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="337.69" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="175.47" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="175.47" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.111264" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="32.042" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04073" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.565" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.552E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="29440" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.67E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02171" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.58E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.0094E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.6232E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="239880" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3215000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.4297" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.382E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="30.585" />
-  <B value="-2.2061E-08" />
-  <Tmin units="K"  value="163.15" />
-  <Tmax units="K"  value="172.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.7918" />
-  <B value="0.23929" />
-  <C value="512.64" />
-  <D value="0.21078" />
-  <Tmin units="K"  value="175.47" />
-  <Tmax units="K"  value="503.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="73.40342" />
-  <B value="-6548.076" />
-  <C value="-7.409987" />
-  <D value="5.72492E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="175.47" />
-  <Tmax units="K"  value="512.64" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.8058E+07" />
-  <B value="0.87168" />
-  <C value="-0.81501" />
-  <D value="0.1695" />
-  <E value="0.17846" />
-  <Tmin units="K"  value="175.47" />
-  <Tmax units="K"  value="513.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12206" />
-  <B value="921.15" />
-  <C value="-4.3764" />
-  <D value="0.0056638" />
-  <E value="0.000021471" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="157.35" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62799" />
-  <B value="1254.2" />
-  <C value="-5.9906" />
-  <D value="0.052937" />
-  <E value="-0.00004711" />
-  <Tmin units="K"  value="175.47" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="36313.16" />
-  <B value="-680.4577" />
-  <C value="11.10203" />
-  <D value="0.000756766" />
-  <E value="-2.902645E-07" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.027528" />
-  <B value="39.761" />
-  <C value="-31.725" />
-  <D value="22876" />
-  <E value="-87341" />
-  <Tmin units="K"  value="281.9" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-32.996" />
-  <B value="1981.4" />
-  <C value="3.3666" />
-  <D value="-0.0000039246" />
-  <E value="2" />
-  <Tmin units="K"  value="175.47" />
-  <Tmax units="K"  value="337.85" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.0654E-07" />
-  <B value="0.69658" />
-  <C value="204.87" />
-  <D value="24.304" />
-  <Tmin units="K"  value="240" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.056817" />
-  <B value="13.156" />
-  <C value="-1.2214" />
-  <D value="-0.00028282" />
-  <E value="-0.0000010129" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="430" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="7.8368E-07" />
-  <B value="1.7569" />
-  <C value="108.12" />
-  <D value="-21101" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="684.37" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.094523" />
-  <B value="33.559" />
-  <C value="-2.3648" />
-  <D value="0.001011" />
-  <E value="-0.0000022169" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="503.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="39194" />
-  <B value="-58.085" />
-  <C value="0.35012" />
-  <D value="-0.00036941" />
-  <E value="1.2763E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="121" />
-  <A value="-22.6673" />
-  <B value="18938.42" />
-  <C value="-2.514938" />
-  <D value="0.0203925" />
-  <E value="0.976849" />
-  <Tmin units="K"  value="176" />
-  <Tmax units="K"  value="511" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.354" />
-  <B value="3555.3" />
-  <C value="-37.163" />
-  <Tmin units="K"  value="307.9" />
-  <Tmax units="K"  value="459.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="4.3964" />
-  <B value="-0.066775" />
-  <C value="0.00008964" />
-  <Tmin units="K"  value="175.47" />
-  <Tmax units="K"  value="337.85" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.1198" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.69E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="417" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="31.25" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.66558" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0185" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.794395" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.5536" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0407027" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.43" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.43" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.96" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="1.828343" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.430885" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.12578" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.5589" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="29546.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0407027" />
-<UnifacVLE name="UNIFAC" >
-  <group id="16"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="16"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="16"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="15"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="67-56-1" />
-<Smiles name="SMILES"  value="CO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1701" />
-<CompoundID name="Name"  value="Methylamine" />
-<StructureFormula name="Structure"  value="CH3NH2" />
-<Family name="Family"  value="34" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="430" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7420000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.125" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="266.82" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="179.69" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="179.69" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="176.712" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="31.057" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04734" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.284" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.722E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21270" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02421" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.86E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.297E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.207E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="243300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6134000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.89954" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-9.7508E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="27.369" />
-  <B value="-2.884E-16" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.39" />
-  <B value="0.21405" />
-  <C value="430.05" />
-  <D value="0.2275" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="430.05" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="74.79969" />
-  <B value="-5067.174" />
-  <C value="-8.028002" />
-  <D value="7.988835E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="177.35" />
-  <Tmax units="K"  value="430.05" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.6499E+07" />
-  <B value="1.6058" />
-  <C value="-3.2311" />
-  <D value="3.4082" />
-  <E value="-1.3345" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="416.87" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="1635.5" />
-  <B value="-28.175" />
-  <C value="12.529" />
-  <D value="-0.11137" />
-  <E value="0.0002958" />
-  <Tmin units="K"  value="23.04" />
-  <Tmax units="K"  value="174.75" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="90815" />
-  <B value="374.96" />
-  <C value="2.7431" />
-  <D value="0.031527" />
-  <E value="-0.000044978" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="266.82" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="40540" />
-  <B value="-902.15" />
-  <C value="12.495" />
-  <D value="-0.00072761" />
-  <E value="0.0000002382" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.066821" />
-  <B value="-65.837" />
-  <C value="-8.5011" />
-  <D value="-94.417" />
-  <E value="-459.86" />
-  <Tmin units="K"  value="215" />
-  <Tmax units="K"  value="1720" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="9.645" />
-  <B value="448.12" />
-  <C value="-3.737" />
-  <D value="0.000017508" />
-  <E value="2" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="327.78" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.4475E-07" />
-  <B value="0.58715" />
-  <C value="230.63" />
-  <D value="-2982.2" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.19876" />
-  <B value="9592" />
-  <C value="-137.2" />
-  <D value="0.62482" />
-  <E value="-0.00097954" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-51.979" />
-  <B value="1.0721" />
-  <C value="-4.4966E+08" />
-  <D value="4.2697E+09" />
-  <Tmin units="K"  value="266.82" />
-  <Tmax units="K"  value="650" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.020476" />
-  <B value="2.1889" />
-  <C value="-2.3303" />
-  <D value="-0.001444" />
-  <E value="-0.0000052886" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="416.87" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34863" />
-  <B value="-17.643" />
-  <C value="0.33582" />
-  <D value="-0.00039394" />
-  <E value="1.4559E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-14.41837" />
-  <B value="-9790.434" />
-  <C value="101.0628" />
-  <Tmin units="K"  value="198" />
-  <Tmax units="K"  value="430" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.666" />
-  <B value="2268.7" />
-  <C value="-43.059" />
-  <Tmin units="K"  value="258.75" />
-  <Tmax units="K"  value="379.45" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.21748" />
-  <B value="-0.052484" />
-  <C value="0.000076834" />
-  <Tmin units="K"  value="179.69" />
-  <Tmax units="K"  value="327.78" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.12229" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.719782E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="216.9006" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="31.99" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.02871" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0179" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.667434" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2872" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0447131" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.5959" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.544" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.44308" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.281272" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23116" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0447131" />
-<UnifacVLE name="UNIFAC" >
-  <group id="29"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="29"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="29"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="29"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="28"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-89-5" />
-<Smiles name="SMILES"  value="CN" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1541" />
-<CompoundID name="Name"  value="Trichloroethylene" />
-<StructureFormula name="Structure"  value="CHClCCl2" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="571" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4910000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.256" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="360.1" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="188.4" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="188.4" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.97868" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="131.388" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0901371" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.21662" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.742E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18800" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.57E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04958" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.13E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9620000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.606E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="325090" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.75258" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.6411E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.727" />
-  <B value="-0.0092769" />
-  <Tmin units="K"  value="75.36" />
-  <Tmax units="K"  value="188.4" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0632" />
-  <B value="0.27217" />
-  <C value="571" />
-  <D value="0.2986" />
-  <Tmin units="K"  value="188.4" />
-  <Tmax units="K"  value="571" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="46.56173" />
-  <B value="-5021.974" />
-  <C value="-3.675161" />
-  <D value="4.330407E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="188.4" />
-  <Tmax units="K"  value="571" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.571591E+07" />
-  <B value="0.581727" />
-  <C value="-0.122707" />
-  <D value="-0.842037" />
-  <E value="0.831632" />
-  <Tmin units="K"  value="188.4" />
-  <Tmax units="K"  value="571" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="103410" />
-  <Tmin units="K"  value="293" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="111110" />
-  <B value="1042.6" />
-  <C value="-3.1013" />
-  <D value="0.043029" />
-  <E value="-0.000040867" />
-  <Tmin units="K"  value="188.4" />
-  <Tmax units="K"  value="419.9" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="56305" />
-  <B value="-500.68" />
-  <C value="11.893" />
-  <D value="-0.00053611" />
-  <E value="1.6998E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33837" />
-  <B value="-460.93" />
-  <C value="26.414" />
-  <D value="-44206" />
-  <E value="82630" />
-  <Tmin units="K"  value="285.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-16.947" />
-  <B value="1157.4" />
-  <C value="0.95533" />
-  <D value="0.0000012051" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="360.1" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.5903E-07" />
-  <B value="0.76088" />
-  <C value="56.852" />
-  <D value="7589.2" />
-  <Tmin units="K"  value="188.4" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.079767" />
-  <B value="522.46" />
-  <C value="-9.4979" />
-  <D value="0.032021" />
-  <E value="-0.00005769" />
-  <Tmin units="K"  value="188.4" />
-  <Tmax units="K"  value="419.47" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00050539" />
-  <B value="0.6741" />
-  <C value="584.61" />
-  <D value="3177.4" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.024347" />
-  <B value="-50.763" />
-  <C value="-1.8584" />
-  <D value="-0.0029088" />
-  <E value="-3.9892E-07" />
-  <Tmin units="K"  value="175.84" />
-  <Tmax units="K"  value="571" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29417.29" />
-  <B value="228.8481" />
-  <C value="-0.218112" />
-  <D value="0.0000777596" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1100" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.691856" />
-  <B value="-1700" />
-  <C value="-10.2" />
-  <Tmin units="K"  value="270.2611" />
-  <Tmax units="K"  value="440.2611" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.353" />
-  <B value="3169.3" />
-  <C value="-37.488" />
-  <Tmin units="K"  value="343.15" />
-  <Tmax units="K"  value="510.59" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.81036" />
-  <B value="-0.035482" />
-  <C value="0.000043558" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="360.1" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.263551" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.831272E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="312.7767" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="97.11" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.55295" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0371" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.46" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2456" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0901371" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.31" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.86" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.1391" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2456" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18796.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0901371" />
-<UnifacVLE name="UNIFAC" >
-  <group id="46"  value="1" />
-  <group id="50"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="32"  value="1" />
-  <group id="36"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  <group id="35"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="46"  value="1" />
-  <group id="50"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="46"  value="1" />
-  <group id="50"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="45"  value="1" />
-  <group id="49"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-01-6" />
-<Smiles name="SMILES"  value="C([Cl])=C([Cl])[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1854" />
-<CompoundID name="Name"  value="Dichloroacetyl chloride" />
-<StructureFormula name="Structure"  value="CHCl2COCl" />
-<Family name="Family"  value="71" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="585" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4610000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.283" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="380.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="230" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="230" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="27.15" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="147.388" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0969971" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.308927" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.988E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19510" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.27E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05458" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.61E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.4033E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.915E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="350000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.2647E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.9" />
-  <B value="-5.7788E-17" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.94766" />
-  <B value="0.26857" />
-  <C value="585" />
-  <D value="0.28586" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="585" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="74.72886" />
-  <B value="-6808.875" />
-  <C value="-7.735182" />
-  <D value="4.475716E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="585" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.182114E+08" />
-  <B value="5.662305" />
-  <C value="-14.25375" />
-  <D value="15.19267" />
-  <E value="-6.032208" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="585" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="140380" />
-  <B value="-122.15" />
-  <C value="7.1438" />
-  <D value="0.0089927" />
-  <E value="-3.0698E-07" />
-  <Tmin units="K"  value="292.5" />
-  <Tmax units="K"  value="438.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="54272" />
-  <B value="-346.01" />
-  <C value="11.744" />
-  <D value="-0.00014147" />
-  <E value="6.1056E-08" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.1766" />
-  <B value="-214.27" />
-  <C value="-34.937" />
-  <D value="-11826" />
-  <E value="15252" />
-  <Tmin units="K"  value="292.5" />
-  <Tmax units="K"  value="1849.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.762" />
-  <B value="1691.3" />
-  <C value="-0.020172" />
-  <D value="2.8483E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="380.45" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4668E-07" />
-  <B value="0.7617" />
-  <C value="110.57" />
-  <D value="-0.0060267" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.045516" />
-  <B value="-168.82" />
-  <C value="-0.6335" />
-  <D value="-0.0052944" />
-  <E value="0.0000014358" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="380.45" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00049754" />
-  <B value="0.6638" />
-  <C value="622.43" />
-  <D value="-0.0085753" />
-  <Tmin units="K"  value="380.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011582" />
-  <B value="124.7" />
-  <C value="-3.6985" />
-  <D value="0.0034242" />
-  <E value="-0.0000087498" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="585" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="45446" />
-  <B value="201.42" />
-  <C value="-0.15256" />
-  <D value="0.000042512" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.845" />
-  <B value="3559.7" />
-  <C value="-36.056" />
-  <Tmin units="K"  value="360.79" />
-  <Tmax units="K"  value="515.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="5.3427" />
-  <B value="-0.057555" />
-  <C value="0.000063183" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="380.45" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.290781" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.948562E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="333.6986" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="103.22" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0423" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.5348" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.370509" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.097018" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.597891" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.044" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.370509" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19942.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.097018" />
-<CAS name="CAS number"  value="79-36-7" />
-<Smiles name="SMILES"  value="ClC(Cl)C(=O)Cl" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="4865" />
-<CompoundID name="Name"  value="Trichloroacetaldehyde" />
-<StructureFormula name="Structure"  value="CCl3CHO" />
-<Family name="Family"  value="71" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="565" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4410000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.288" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.27" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="370.85" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="216" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="216" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="10.133" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="147.388" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0983111" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.332334" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.649E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19150" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.54E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05519" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.83E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.97E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.48E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="348000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.72E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.036" />
-  <B value="-0.0072767" />
-  <Tmin units="K"  value="86.4" />
-  <Tmax units="K"  value="216" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.92352" />
-  <B value="0.2658" />
-  <C value="565" />
-  <D value="0.27915" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="565" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="104.1738" />
-  <B value="-7649.009" />
-  <C value="-12.42192" />
-  <D value="0.0000106892" />
-  <E value="2" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="565" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.2611E+07" />
-  <B value="1.7765" />
-  <C value="-3.981" />
-  <D value="4.442" />
-  <E value="-1.8138" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="565" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="141170" />
-  <B value="-5.956" />
-  <C value="6.555" />
-  <D value="0.014383" />
-  <E value="-0.000012896" />
-  <Tmin units="K"  value="282.5" />
-  <Tmax units="K"  value="422.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="75534" />
-  <B value="-497.17" />
-  <C value="11.711" />
-  <D value="-0.00021306" />
-  <E value="5.7567E-08" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17202" />
-  <B value="-198.18" />
-  <C value="-54.361" />
-  <D value="1512" />
-  <E value="-47122" />
-  <Tmin units="K"  value="282.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.452" />
-  <B value="1500.4" />
-  <C value="0.62119" />
-  <D value="1.0267E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="370.85" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9624E-07" />
-  <B value="0.76217" />
-  <C value="181.59" />
-  <D value="-7289.4" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0058147" />
-  <B value="-49.103" />
-  <C value="-1.1431" />
-  <D value="-0.0024848" />
-  <E value="-2.7456E-08" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="370.85" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00037396" />
-  <B value="0.73494" />
-  <C value="540.31" />
-  <D value="2896.6" />
-  <Tmin units="K"  value="370.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010804" />
-  <B value="115.62" />
-  <C value="-3.806" />
-  <D value="0.0033787" />
-  <E value="-0.0000089296" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="565" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="51330" />
-  <B value="196.28" />
-  <C value="-0.15434" />
-  <D value="0.000045652" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.369" />
-  <B value="3131.8" />
-  <C value="-52.731" />
-  <Tmin units="K"  value="344.58" />
-  <Tmax units="K"  value="495.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.5668" />
-  <B value="-0.047882" />
-  <C value="0.00005446" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="370.85" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.294123" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.930245E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="331.033" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261398" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="103.22" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0408" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.515" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.332283" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0983111" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.638102" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.132" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.332283" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19153.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0983111" />
-<CAS name="CAS number"  value="75-87-6" />
-<Smiles name="SMILES"  value="C([Cl])([Cl])([Cl])C=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="401" />
-<CompoundID name="Name"  value="Acetylene" />
-<StructureFormula name="Structure"  value="HCCH" />
-<Family name="Family"  value="15" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="308.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6114000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1122" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="188.4" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="192.4" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="192.4" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="127445" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="26.038" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04347" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.189" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="7.439E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="7921" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0231" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.48E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.282E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.1068E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="200810" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3770000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.76366" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.257E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="28.036" />
-  <B value="-1.6913E-08" />
-  <Tmin units="K"  value="188.15" />
-  <Tmax units="K"  value="197.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.8265" />
-  <B value="0.29316" />
-  <C value="308.3" />
-  <D value="0.31711" />
-  <Tmin units="K"  value="189.54" />
-  <Tmax units="K"  value="307.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.22155" />
-  <B value="-3603.253" />
-  <C value="-10.0271" />
-  <D value="0.0000269397" />
-  <E value="2" />
-  <Tmin units="K"  value="187.75" />
-  <Tmax units="K"  value="308.33" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.8817E+07" />
-  <B value="1.497" />
-  <C value="-1.0261" />
-  <D value="0.037348" />
-  <E value="-0.024401" />
-  <Tmin units="K"  value="192.4" />
-  <Tmax units="K"  value="308.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="36900" />
-  <Tmin units="K"  value="174" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="79227" />
-  <B value="3177.2" />
-  <C value="-44.249" />
-  <D value="0.23814" />
-  <E value="-0.00030171" />
-  <Tmin units="K"  value="192.4" />
-  <Tmax units="K"  value="250" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="28271.69" />
-  <B value="-404.2493" />
-  <C value="11.05572" />
-  <D value="-0.000229636" />
-  <E value="1.424209E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.032935" />
-  <B value="-6.0707" />
-  <C value="-4.922" />
-  <D value="119.69" />
-  <E value="-177.19" />
-  <Tmin units="K"  value="154.16" />
-  <Tmax units="K"  value="1541.65" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.822" />
-  <B value="283.23" />
-  <C value="0.22007" />
-  <D value="-0.0000091126" />
-  <E value="2" />
-  <Tmin units="K"  value="153.15" />
-  <Tmax units="K"  value="273.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010997" />
-  <B value="0.50414" />
-  <C value="259.72" />
-  <D value="2787.3" />
-  <Tmin units="K"  value="192.4" />
-  <Tmax units="K"  value="600" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.060328" />
-  <B value="-110.3" />
-  <C value="0.44567" />
-  <D value="-0.0073832" />
-  <E value="0.0000024581" />
-  <Tmin units="K"  value="192.4" />
-  <Tmax units="K"  value="250" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000078096" />
-  <B value="1.0286" />
-  <C value="-36.515" />
-  <D value="33144" />
-  <Tmin units="K"  value="189.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0058288" />
-  <B value="469.57" />
-  <C value="-10.144" />
-  <D value="0.036848" />
-  <E value="-0.000083224" />
-  <Tmin units="K"  value="183.15" />
-  <Tmax units="K"  value="301.71" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="20038" />
-  <B value="90.844" />
-  <C value="-0.021202" />
-  <D value="-0.000065684" />
-  <E value="4.3568E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.0217" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.46" />
-  <B value="1724.2" />
-  <C value="-14.702" />
-  <Tmin units="K"  value="192.59" />
-  <Tmax units="K"  value="273.16" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-5.8124" />
-  <B value="-0.017889" />
-  <C value="0.000019784" />
-  <Tmin units="K"  value="153.15" />
-  <Tmax units="K"  value="273.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.16741" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.369994E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="175.862" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2712" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="36.42" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.47883" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0157" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.417053" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.20487" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0421382" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.52" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.39" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.001831" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-2.4245" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1841" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18813" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0421382" />
-<UnifacVLE name="UNIFAC" >
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-86-2" />
-<Smiles name="SMILES"  value="C#C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="4868" />
-<CompoundID name="Name"  value="Dichloroacetaldehyde" />
-<StructureFormula name="Structure"  value="CHCl2CHO" />
-<Family name="Family"  value="71" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="555" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4950000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.239" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="362" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="223" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="223" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="30.4712" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.943" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0800261" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.343679" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.419E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21090" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.87E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0464" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.58E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.8E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.387E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="329000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.4E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.11E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.182" />
-  <B value="-0.0082192" />
-  <Tmin units="K"  value="89.2" />
-  <Tmax units="K"  value="223" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0695" />
-  <B value="0.25535" />
-  <C value="555" />
-  <D value="0.28663" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="537.53" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="90.61988" />
-  <B value="-7239.82" />
-  <C value="-10.19237" />
-  <D value="7.278159E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="555" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.4311E+07" />
-  <B value="0.74287" />
-  <C value="-0.97767" />
-  <D value="1.092" />
-  <E value="-0.46681" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="537.53" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="4914.9" />
-  <B value="686.94" />
-  <C value="-1.5072" />
-  <D value="0.0043969" />
-  <E value="-0.0000057306" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="223" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="79819" />
-  <B value="-93.388" />
-  <C value="10.443" />
-  <D value="0.0030492" />
-  <E value="-0.0000015371" />
-  <Tmin units="K"  value="277.5" />
-  <Tmax units="K"  value="407.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68025" />
-  <B value="-873.5" />
-  <C value="12.537" />
-  <D value="-0.00086712" />
-  <E value="2.2298E-07" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.14666" />
-  <B value="-146.64" />
-  <C value="-46.944" />
-  <D value="9273.3" />
-  <E value="-59706" />
-  <Tmin units="K"  value="277.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-19.012" />
-  <B value="2548.4" />
-  <C value="0.73092" />
-  <D value="-0.0000016452" />
-  <E value="2" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="362" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.0229E-07" />
-  <B value="0.67781" />
-  <C value="216.84" />
-  <D value="-7478.9" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.006509" />
-  <B value="-45.732" />
-  <C value="-1.1121" />
-  <D value="-0.0023494" />
-  <E value="-2.6574E-07" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="362" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00042346" />
-  <B value="0.72759" />
-  <C value="609.27" />
-  <D value="10645" />
-  <Tmin units="K"  value="362" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016507" />
-  <B value="102.49" />
-  <C value="-3.2427" />
-  <D value="0.002483" />
-  <E value="-0.0000080057" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="537.53" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="31310" />
-  <B value="196.15" />
-  <C value="-0.12609" />
-  <D value="0.000027886" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.357" />
-  <B value="2972.9" />
-  <C value="-59.701" />
-  <Tmin units="K"  value="339.2" />
-  <Tmax units="K"  value="488.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="11.143" />
-  <B value="-0.089877" />
-  <C value="0.00010345" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="362" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.246373" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.940499E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="268.4541" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.260402" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="84.53" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0358" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.4274" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.343679" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0788193" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.058668" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.632" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.343679" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21250.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0788193" />
-<CAS name="CAS number"  value="79-02-7" />
-<Smiles name="SMILES"  value="[Cl]C([Cl])C(=O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1504" />
-<CompoundID name="Name"  value="Vinyl chloride" />
-<StructureFormula name="Structure"  value="CH2CHCl" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="432" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5670000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.179" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.283" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="259.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="119.36" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="119.36" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0191781" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="62.4982" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0692236" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.100107" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.049E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15960" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03203" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.74E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.845E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.195E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="273540" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4744000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.66941" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.178E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="23.453" />
-  <B value="-0.021899" />
-  <Tmin units="K"  value="47.74" />
-  <Tmax units="K"  value="119.36" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.4882" />
-  <B value="0.26866" />
-  <C value="432" />
-  <D value="0.2693" />
-  <Tmin units="K"  value="119.36" />
-  <Tmax units="K"  value="415.55" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="30.50309" />
-  <B value="-3204.111" />
-  <C value="-1.15716" />
-  <D value="-3.151817E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="119.36" />
-  <Tmax units="K"  value="432" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.6581E+07" />
-  <B value="-2.1189" />
-  <C value="8.303" />
-  <D value="-9.8551" />
-  <E value="4.0685" />
-  <Tmin units="K"  value="119.36" />
-  <Tmax units="K"  value="415.55" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="69150" />
-  <Tmin units="K"  value="293" />
-  <Tmax units="K"  value="4" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29928" />
-  <B value="167.46" />
-  <C value="5.6386" />
-  <D value="0.023319" />
-  <E value="-0.000024747" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39013" />
-  <B value="-667.91" />
-  <C value="11.935" />
-  <D value="-0.00030895" />
-  <E value="9.1245E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.098959" />
-  <B value="-101.3" />
-  <C value="-7.5955" />
-  <D value="2613.5" />
-  <E value="-5619.5" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="1962" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-3.586" />
-  <B value="386.19" />
-  <C value="-1.1014" />
-  <D value="-9.1164E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="130" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.1288E-07" />
-  <B value="0.63726" />
-  <C value="118.97" />
-  <D value="5390.5" />
-  <Tmin units="K"  value="119.36" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.060341" />
-  <B value="155.36" />
-  <C value="-4.6785" />
-  <D value="0.015523" />
-  <E value="-0.000038165" />
-  <Tmin units="K"  value="119.36" />
-  <Tmax units="K"  value="377.59" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-260.51" />
-  <B value="0.58623" />
-  <C value="-1.7838E+08" />
-  <D value="-1.6691E+09" />
-  <Tmin units="K"  value="259.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.022524" />
-  <B value="0.70561" />
-  <C value="-2.4028" />
-  <D value="-0.0019215" />
-  <E value="-0.0000032256" />
-  <Tmin units="K"  value="119.36" />
-  <Tmax units="K"  value="415.55" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13749" />
-  <B value="162.87" />
-  <C value="-0.095843" />
-  <D value="0.000021301" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.716" />
-  <B value="2058.7" />
-  <C value="-35.364" />
-  <Tmin units="K"  value="259.3" />
-  <Tmax units="K"  value="388.71" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.9112" />
-  <B value="-0.029433" />
-  <C value="0.00003364" />
-  <Tmin units="K"  value="130" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.169758" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.783204E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="299.7975" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.281776" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="59.73" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.34884" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.025" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.919257" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.100107" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0646597" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.9124" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.492" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.4731" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.100107" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17766.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0646597" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="46"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="1" />
-  <group id="32"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="35"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="1" />
-  <group id="46"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="45"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-01-4" />
-<Smiles name="SMILES"  value="C=C[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1851" />
-<CompoundID name="Name"  value="Acetyl chloride" />
-<StructureFormula name="Structure"  value="CH3COCl" />
-<Family name="Family"  value="71" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="508" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5740000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.196" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="323.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="160.3" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="160.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0945737" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="78.4976" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0713449" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.334018" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.712E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03699" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.52E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.4351E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.058E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="295000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.75307E+08" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.7599E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="20.469" />
-  <B value="-0.013585" />
-  <Tmin units="K"  value="64.12" />
-  <Tmax units="K"  value="160.3" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.4254" />
-  <B value="0.27938" />
-  <C value="508" />
-  <D value="0.26304" />
-  <Tmin units="K"  value="160.3" />
-  <Tmax units="K"  value="508" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="99.17638" />
-  <B value="-7177.914" />
-  <C value="-11.22425" />
-  <D value="-0.0000057394" />
-  <E value="2" />
-  <Tmin units="K"  value="160.3" />
-  <Tmax units="K"  value="508" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.0E+07" />
-  <B value="0.3" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="160.3" />
-  <Tmax units="K"  value="519.35" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="42690" />
-  <B value="1356.4" />
-  <C value="-2.0032" />
-  <D value="0.038796" />
-  <E value="-0.000032805" />
-  <Tmin units="K"  value="227.44" />
-  <Tmax units="K"  value="381" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="55490" />
-  <B value="-733.46" />
-  <C value="11.97" />
-  <D value="-0.00022853" />
-  <E value="6.1958E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12026" />
-  <B value="-122.6" />
-  <C value="-19.118" />
-  <D value="-10341" />
-  <E value="16844" />
-  <Tmin units="K"  value="254" />
-  <Tmax units="K"  value="1850" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="4.4371" />
-  <B value="130.26" />
-  <C value="-2.2299" />
-  <D value="-8.5166E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="323.9" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.0377E-08" />
-  <B value="0.94052" />
-  <C value="79.768" />
-  <D value="-9041.6" />
-  <Tmin units="K"  value="160.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11965" />
-  <B value="1957.5" />
-  <C value="-32.911" />
-  <D value="0.1548" />
-  <E value="-0.00027429" />
-  <Tmin units="K"  value="160.3" />
-  <Tmax units="K"  value="323.9" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-27944" />
-  <B value="0.34599" />
-  <C value="-4.878E+09" />
-  <D value="-7.8546E+10" />
-  <Tmin units="K"  value="323.9" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.028314" />
-  <B value="13.997" />
-  <C value="-2.5681" />
-  <D value="-0.00040564" />
-  <E value="-0.0000031823" />
-  <Tmin units="K"  value="160.3" />
-  <Tmax units="K"  value="508" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="24995.64" />
-  <B value="170.9624" />
-  <C value="-0.0985039" />
-  <D value="0.0000221861" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-16.34649" />
-  <B value="-7900" />
-  <C value="-47.4" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.285" />
-  <B value="3449.5" />
-  <C value="-3.3316" />
-  <Tmin units="K"  value="306.28" />
-  <Tmax units="K"  value="453.1" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.4531" />
-  <B value="-0.020401" />
-  <C value="0.000018319" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="323.9" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.196053" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.310544E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="282.066" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26125" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="65.84" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0285" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.104" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.334018" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0712327" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.438365" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.208" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.334018" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20189.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0712327" />
-<CAS name="CAS number"  value="75-36-5" />
-<Smiles name="SMILES"  value="CC(=O)Cl" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1524" />
-<CompoundID name="Name"  value="1,1,2-trichloroethane" />
-<StructureFormula name="Structure"  value="CHCl2CH2Cl" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="602" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4480000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.281" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="387" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="236.5" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="236.5" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="44.7475" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="133.404" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0929898" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.259135" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.717E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19890" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.17E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05311" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.36E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.42E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-8.097E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="337100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.13E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.85565" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-9.685E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.57" />
-  <B value="-0.006887" />
-  <Tmin units="K"  value="94.6" />
-  <Tmax units="K"  value="236.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.9055" />
-  <B value="0.25465" />
-  <C value="602" />
-  <D value="0.30987" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="602" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="66.05096" />
-  <B value="-6428.165" />
-  <C value="-6.44717" />
-  <D value="3.27127E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="602" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.0503E+07" />
-  <B value="0.64021" />
-  <C value="-1.1382" />
-  <D value="1.5379" />
-  <E value="-0.66031" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="602" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="654700" />
-  <B value="-14318" />
-  <C value="123.14" />
-  <D value="-0.43554" />
-  <E value="0.00055528" />
-  <Tmin units="K"  value="117.15" />
-  <Tmax units="K"  value="222.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="121000" />
-  <B value="433.16" />
-  <C value="2.2235" />
-  <D value="0.034423" />
-  <E value="-0.000040901" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="300" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="56506" />
-  <B value="-535.36" />
-  <C value="12.166" />
-  <D value="-0.00021958" />
-  <E value="4.8605E-08" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18736" />
-  <B value="-244.22" />
-  <C value="-36.351" />
-  <D value="-1273" />
-  <E value="-10172" />
-  <Tmin units="K"  value="301" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-26.218" />
-  <B value="1571.3" />
-  <C value="2.5992" />
-  <D value="-0.0000081378" />
-  <E value="2" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="387" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.8974E-07" />
-  <B value="0.68713" />
-  <C value="200.47" />
-  <D value="-854.38" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.027258" />
-  <B value="-78.724" />
-  <C value="-0.73941" />
-  <D value="-0.0030401" />
-  <E value="8.8565E-07" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="482" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000095455" />
-  <B value="1.0427" />
-  <C value="1258.3" />
-  <D value="-2960.2" />
-  <Tmin units="K"  value="387" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01087" />
-  <B value="126.61" />
-  <C value="-3.7929" />
-  <D value="0.0032685" />
-  <E value="-0.0000080616" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="602" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="18491.19" />
-  <B value="309.57" />
-  <C value="-0.272542" />
-  <D value="0.0000927467" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-6.355533" />
-  <B value="-3750" />
-  <C value="-22.5" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.075" />
-  <B value="3187" />
-  <C value="-53.379" />
-  <Tmin units="K"  value="366.15" />
-  <Tmax units="K"  value="536.5" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.56855" />
-  <B value="-0.035441" />
-  <C value="0.000035292" />
-  <Tmin units="K"  value="236.5" />
-  <Tmax units="K"  value="387" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.282745" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.389493E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="275.1387" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267821" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="101.73" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0403" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.44" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.259768" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0929898" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.526" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.948" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.259768" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19818.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0929898" />
-<UnifacVLE name="UNIFAC" >
-  <group id="45"  value="1" />
-  <group id="49"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="31"  value="1" />
-  <group id="35"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="1" />
-  <group id="35"  value="1" />
-  <group id="37"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="45"  value="1" />
-  <group id="49"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="45"  value="1" />
-  <group id="49"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="44"  value="1" />
-  <group id="48"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-00-5" />
-<Smiles name="SMILES"  value="C([Cl])([Cl])C[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1772" />
-<CompoundID name="Name"  value="Acetonitrile" />
-<StructureFormula name="Structure"  value="CH3CN" />
-<Family name="Family"  value="38" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="545.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4830000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.173" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.184" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="354.75" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="229.32" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="229.32" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="186.945" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="41.0519" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0528577" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.337886" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.841E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24050" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.31E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02837" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.31E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="7.404E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.1868E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="243290" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8167000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.10072" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.19043E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="26.156" />
-  <B value="-0.012566" />
-  <Tmin units="K"  value="91.73" />
-  <Tmax units="K"  value="229.32" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3064" />
-  <B value="0.22597" />
-  <C value="545.5" />
-  <D value="0.28678" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="545.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="63.90188" />
-  <B value="-5635.018" />
-  <C value="-6.338065" />
-  <D value="5.801644E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="226.15" />
-  <Tmax units="K"  value="545.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.416703E+07" />
-  <B value="0.0989791" />
-  <C value="1.817987" />
-  <D value="-3.443548" />
-  <E value="1.854664" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="545.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-24879" />
-  <B value="1533.9" />
-  <C value="-14.715" />
-  <D value="0.077647" />
-  <E value="-0.00014986" />
-  <Tmin units="K"  value="25.75" />
-  <Tmax units="K"  value="224.56" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78687" />
-  <B value="635.92" />
-  <C value="1.7473" />
-  <D value="0.02389" />
-  <E value="-0.000017421" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="354.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="41003" />
-  <B value="-679.99" />
-  <C value="11.578" />
-  <D value="0.00010104" />
-  <E value="-4.1014E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.0059949" />
-  <B value="-17.326" />
-  <C value="-84.313" />
-  <D value="48578" />
-  <E value="-218790" />
-  <Tmin units="K"  value="301.4" />
-  <Tmax units="K"  value="1918" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-31.531" />
-  <B value="1522.1" />
-  <C value="3.3306" />
-  <D value="-0.0000059061" />
-  <E value="2" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="436.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.1905E-08" />
-  <B value="0.88581" />
-  <C value="38.325" />
-  <D value="87.034" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.18265" />
-  <B value="8401.9" />
-  <C value="-103.1" />
-  <D value="0.40559" />
-  <E value="-0.00056286" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="383.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="4.7622E-08" />
-  <B value="2.1156" />
-  <C value="30.88" />
-  <D value="-14671" />
-  <Tmin units="K"  value="354.75" />
-  <Tmax units="K"  value="994.75" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.020712" />
-  <B value="60.742" />
-  <C value="-3.1145" />
-  <D value="0.0012183" />
-  <E value="-0.0000051841" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="545.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="20459.76" />
-  <B value="119.5411" />
-  <C value="-0.0449278" />
-  <D value="3.213187E-06" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-12.40026" />
-  <B value="-12960.1" />
-  <C value="-29.78921" />
-  <Tmin units="K"  value="295" />
-  <Tmax units="K"  value="545" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.165" />
-  <B value="3643.3" />
-  <C value="-12.319" />
-  <Tmin units="K"  value="329.17" />
-  <Tmax units="K"  value="478.94" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.8595" />
-  <B value="-0.024217" />
-  <C value="0.000023868" />
-  <Tmin units="K"  value="229.32" />
-  <Tmax units="K"  value="436.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.15354" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.927671E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="80.36225" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.260911" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="43.27" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.05284" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0221" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.782" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.30759" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0526772" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.87" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.72" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.33826" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.338174" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24093.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0526772" />
-<UnifacVLE name="UNIFAC" >
-  <group id="41"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="41"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="28"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="41"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="41"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="40"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-05-8" />
-<Smiles name="SMILES"  value="CC#N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="201" />
-<CompoundID name="Name"  value="Ethylene" />
-<StructureFormula name="Structure"  value="CH2CH2" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="282.34" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5041000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1311" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.282" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="169.42" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="104" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="104" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="125.988" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="28.054" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.05107" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.087" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.548E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12440" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02388" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.72E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="5.251E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.844E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="219200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3351000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.61252" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.323E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="29.172" />
-  <B value="-0.027595" />
-  <Tmin units="K"  value="73.15" />
-  <Tmax units="K"  value="104" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.3782" />
-  <B value="0.29542" />
-  <C value="282.36" />
-  <D value="0.32456" />
-  <Tmin units="K"  value="103.18" />
-  <Tmax units="K"  value="282.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="54.53229" />
-  <B value="-2458.42" />
-  <C value="-5.660037" />
-  <D value="0.0000194185" />
-  <E value="2" />
-  <Tmin units="K"  value="104" />
-  <Tmax units="K"  value="282.35" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.1658E+07" />
-  <B value="1.2164" />
-  <C value="-2.1538" />
-  <D value="2.0768" />
-  <E value="-0.73096" />
-  <Tmin units="K"  value="104" />
-  <Tmax units="K"  value="282.35" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="4815.2" />
-  <B value="-937.58" />
-  <C value="68.923" />
-  <D value="-1.0511" />
-  <E value="0.0052386" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="103.97" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68016" />
-  <B value="-22414" />
-  <C value="286.75" />
-  <D value="-1.1802" />
-  <E value="0.0017304" />
-  <Tmin units="K"  value="99.82" />
-  <Tmax units="K"  value="259.95" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33071.93" />
-  <B value="-860.0281" />
-  <C value="12.22807" />
-  <D value="-0.000509703" />
-  <E value="1.628387E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.092447" />
-  <B value="-60.239" />
-  <C value="-0.7957" />
-  <D value="-5.0549" />
-  <E value="5.3309" />
-  <Tmin units="K"  value="120" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.9556" />
-  <B value="288.21" />
-  <C value="-0.21985" />
-  <D value="-0.000010831" />
-  <E value="2" />
-  <Tmin units="K"  value="103.1" />
-  <Tmax units="K"  value="260" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000021134" />
-  <B value="0.41436" />
-  <C value="359.51" />
-  <D value="-2291.7" />
-  <Tmin units="K"  value="169.41" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.19499" />
-  <B value="-11.178" />
-  <C value="-0.31182" />
-  <D value="-0.0034844" />
-  <E value="3.5873E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="280" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000093247" />
-  <B value="1.4607" />
-  <C value="410.48" />
-  <D value="-44405" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="590.92" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.002859" />
-  <B value="236.18" />
-  <C value="-7.9878" />
-  <D value="0.032145" />
-  <E value="-0.000097469" />
-  <Tmin units="K"  value="104" />
-  <Tmax units="K"  value="272.95" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="35095" />
-  <B value="-73.018" />
-  <C value="0.48182" />
-  <D value="-0.00055948" />
-  <E value="2.0878E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.89" />
-  <B value="1502.3" />
-  <C value="-8.9148" />
-  <Tmin units="K"  value="169.41" />
-  <Tmax units="K"  value="253.1" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.3856" />
-  <B value="-0.034465" />
-  <C value="0.000053356" />
-  <Tmin units="K"  value="103.1" />
-  <Tmax units="K"  value="260" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.13097" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.329924E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="193.4561" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.281" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="41.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0177" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.383226" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0882" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0493214" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.57" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.49" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002805" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.0949" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="12436.64" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.061" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="2"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="2"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-85-1" />
-<Smiles name="SMILES"  value="C=C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1522" />
-<CompoundID name="Name"  value="1,1-dichloroethane" />
-<StructureFormula name="Structure"  value="CHCl2CH3" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="523" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5100000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.236" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.277" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="330.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="176.19" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="176.19" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.21455" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.959" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08473" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.244" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.095E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18300" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.87E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04493" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.33E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.2941E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-7.259E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="305010" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7870000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95261" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.1104E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.18" />
-  <B value="-0.010734" />
-  <Tmin units="K"  value="70.48" />
-  <Tmax units="K"  value="176.19" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1057" />
-  <B value="0.26536" />
-  <C value="523" />
-  <D value="0.28703" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="504.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="66.53401" />
-  <B value="-5492.415" />
-  <C value="-6.715993" />
-  <D value="5.298782E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="523" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.458773E+07" />
-  <B value="0.555838" />
-  <C value="0.0209485" />
-  <D value="-0.722234" />
-  <E value="0.56963" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="504.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14894" />
-  <B value="1761.9" />
-  <C value="-17.551" />
-  <D value="0.085912" />
-  <E value="-0.00013498" />
-  <Tmin units="K"  value="14.17" />
-  <Tmax units="K"  value="165.75" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115470" />
-  <B value="479.34" />
-  <C value="1.2009" />
-  <D value="0.029511" />
-  <E value="-0.000025794" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="330.45" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="45661" />
-  <B value="-449.92" />
-  <C value="11.802" />
-  <D value="0.00015496" />
-  <E value="-5.3829E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.065419" />
-  <B value="-59.071" />
-  <C value="-33.932" />
-  <D value="9018.2" />
-  <E value="-20873" />
-  <Tmin units="K"  value="261.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.7803" />
-  <B value="891.16" />
-  <C value="-0.14866" />
-  <D value="-3.5884E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="330.45" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000001814" />
-  <B value="0.74706" />
-  <C value="93.461" />
-  <D value="1513.7" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.011357" />
-  <B value="-64.086" />
-  <C value="-0.98127" />
-  <D value="-0.0039469" />
-  <E value="6.6106E-07" />
-  <Tmin units="K"  value="156.9" />
-  <Tmax units="K"  value="416.9" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013381" />
-  <B value="1.01" />
-  <C value="1042.5" />
-  <D value="-2442" />
-  <Tmin units="K"  value="330.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.043274" />
-  <B value="-3.8245" />
-  <C value="-2.0709" />
-  <D value="-0.0019704" />
-  <E value="-1.9129E-07" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="504.75" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="21701" />
-  <B value="206.64" />
-  <C value="-0.056123" />
-  <D value="-0.000086055" />
-  <E value="5.3462E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-17.65507" />
-  <B value="-8350" />
-  <C value="-50.1" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.36" />
-  <B value="2884.3" />
-  <C value="-37.086" />
-  <Tmin units="K"  value="318.35" />
-  <Tmax units="K"  value="468.24" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.60084" />
-  <B value="-0.045249" />
-  <C value="0.000058588" />
-  <Tmin units="K"  value="176.19" />
-  <Tmax units="K"  value="330.45" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2369" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.38154E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="336.0022" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="83.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.83715" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0336" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.18256" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.23646" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0847207" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.9617" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.532" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.5103" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.244612" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18299.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0847207" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="49"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="35"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="37"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="49"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="48"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-34-3" />
-<Smiles name="SMILES"  value="CC([Cl])[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1523" />
-<CompoundID name="Name"  value="1,2-dichloroethane" />
-<StructureFormula name="Structure"  value="CH2ClCH2Cl" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="561" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.22" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="356.66" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="237.49" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="237.49" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="237.127" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.959" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07945" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.286" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.827E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20260" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.8E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0437" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.3E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.2979E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-7.3945E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="308280" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8830000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.98897" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.105E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.854" />
-  <B value="2.2061E-09" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="232.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1942" />
-  <B value="0.27053" />
-  <C value="561.61" />
-  <D value="0.29157" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="561.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.47902" />
-  <B value="-6503.169" />
-  <C value="-8.960273" />
-  <D value="7.32894E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="561.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.072427E+07" />
-  <B value="0.517321" />
-  <C value="0.205828" />
-  <D value="-0.637156" />
-  <E value="0.265499" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="544.54" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="32947" />
-  <B value="-881.85" />
-  <C value="32.363" />
-  <D value="-0.29817" />
-  <E value="0.00092602" />
-  <Tmin units="K"  value="40.69" />
-  <Tmax units="K"  value="179.69" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="92757" />
-  <B value="224.15" />
-  <C value="8.5223" />
-  <D value="0.0025656" />
-  <E value="0.000005106" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="522.04" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62073" />
-  <B value="-758.84" />
-  <C value="12.345" />
-  <D value="-0.0004196" />
-  <E value="0.0000001146" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15478" />
-  <B value="-169.14" />
-  <C value="-26.602" />
-  <D value="737.05" />
-  <E value="-4862.1" />
-  <Tmin units="K"  value="243" />
-  <Tmax units="K"  value="1964" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="25.747" />
-  <B value="-385.45" />
-  <C value="-5.5912" />
-  <D value="0.0000027937" />
-  <E value="2" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="544.26" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.1983E-07" />
-  <B value="0.79504" />
-  <C value="20.791" />
-  <D value="14003" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.015945" />
-  <B value="-110.67" />
-  <C value="-0.74013" />
-  <D value="-0.0032664" />
-  <E value="-5.0786E-07" />
-  <Tmin units="K"  value="244.26" />
-  <Tmax units="K"  value="499.82" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00023592" />
-  <B value="0.93945" />
-  <C value="1368.6" />
-  <D value="23794" />
-  <Tmin units="K"  value="199.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.022707" />
-  <B value="74.78" />
-  <C value="-2.954" />
-  <D value="0.00056054" />
-  <E value="-0.0000041954" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="544.54" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="24860" />
-  <B value="192.87" />
-  <C value="-0.03359" />
-  <D value="-0.000094203" />
-  <E value="0.0000000513" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-8.970346" />
-  <B value="-5150" />
-  <C value="-30.9" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.473" />
-  <B value="3186" />
-  <C value="-36.407" />
-  <Tmin units="K"  value="337.48" />
-  <Tmax units="K"  value="499.82" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.994" />
-  <B value="-0.021914" />
-  <C value="0.000015517" />
-  <Tmin units="K"  value="237.49" />
-  <Tmax units="K"  value="544.26" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.231863" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.805919E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="267.5597" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="83.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.73831" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0334" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.2604" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2876" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0794424" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.88" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.52" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2388" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2876" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20249.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0794424" />
-<UnifacVLE name="UNIFAC" >
-  <group id="45"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="31"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="2" />
-  <group id="35"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="45"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="45"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="44"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-06-2" />
-<Smiles name="SMILES"  value="[Cl]CC[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1002" />
-<CompoundID name="Name"  value="Acetaldehyde" />
-<StructureFormula name="Structure"  value="CH3CHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="466" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5550000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.154" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.221" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="294" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="150.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="150.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.323203" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="44.0526" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0568878" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.290734" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.083E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20110" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.97E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02881" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.49E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.664E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.333E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="264200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3220000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.19343" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.1045E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="27.289" />
-  <B value="-0.020316" />
-  <Tmin units="K"  value="60.06" />
-  <Tmax units="K"  value="150.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.2346" />
-  <B value="0.22392" />
-  <C value="466" />
-  <D value="0.25025" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="455.37" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="132.6058" />
-  <B value="-7086.883" />
-  <C value="-17.42481" />
-  <D value="0.0000237457" />
-  <E value="2" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="466" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.4565E+07" />
-  <B value="-6.1925" />
-  <C value="18.559" />
-  <D value="-20.707" />
-  <E value="8.5605" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="449.38" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="65440" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="72077" />
-  <B value="1068.4" />
-  <C value="-6.4275" />
-  <D value="0.06878" />
-  <E value="-0.000079154" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="294" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="42578" />
-  <B value="-730.39" />
-  <C value="11.883" />
-  <D value="0.000033485" />
-  <E value="-3.0296E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.078952" />
-  <B value="-74.81" />
-  <C value="-19.77" />
-  <D value="936.76" />
-  <E value="-8295.3" />
-  <Tmin units="K"  value="230.5" />
-  <Tmax units="K"  value="1844" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-4.0316" />
-  <B value="623.05" />
-  <C value="-1.1589" />
-  <D value="8.4583E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="444.26" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.1933E-07" />
-  <B value="0.78879" />
-  <C value="65.293" />
-  <D value="1023.3" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.014392" />
-  <B value="-40.45" />
-  <C value="-0.67323" />
-  <D value="-0.0036191" />
-  <E value="0.0000011083" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="410.93" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="3.2627E-07" />
-  <B value="1.8293" />
-  <C value="-23.073" />
-  <D value="3397.7" />
-  <Tmin units="K"  value="199.82" />
-  <Tmax units="K"  value="994" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.038609" />
-  <B value="8.1469" />
-  <C value="-2.3156" />
-  <D value="-0.0012955" />
-  <E value="-0.0000017377" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="449.38" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="7716" />
-  <B value="182.3" />
-  <C value="-0.1007" />
-  <D value="0.0000238" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-25.20353" />
-  <B value="-10000" />
-  <C value="-65.4" />
-  <Tmin units="K"  value="259.15" />
-  <Tmax units="K"  value="429.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.688" />
-  <B value="3543.8" />
-  <C value="23.246" />
-  <Tmin units="K"  value="282.85" />
-  <Tmax units="K"  value="416.13" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.38" />
-  <B value="-0.03568" />
-  <C value="0.000039369" />
-  <Tmin units="K"  value="150.15" />
-  <Tmax units="K"  value="444.26" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.15309" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.120889E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="132.7735" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="47.15" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.05829" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0217" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.778" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.26469" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0564965" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.9" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.8" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.58913" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.316685" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19818.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0564965" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="21"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="21"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="20"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="21"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="20"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-07-0" />
-<Smiles name="SMILES"  value="CC=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1441" />
-<CompoundID name="Name"  value="Ethylene oxide" />
-<StructureFormula name="Structure"  value="CH2OCH2" />
-<Family name="Family"  value="63" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="469.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7190000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.140296" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25876" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="283.6" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="160.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="160.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.78791" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="44.0526" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0508328" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.197447" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.937E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21050" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02416" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.3E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.263E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.323E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="242990" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5171400" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.78776" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.218E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="29.78" />
-  <B value="-0.02052" />
-  <Tmin units="K"  value="64.26" />
-  <Tmax units="K"  value="160.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.99773" />
-  <B value="0.19368" />
-  <C value="469.15" />
-  <D value="0.19965" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="468.93" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="69.60869" />
-  <B value="-4890.744" />
-  <C value="-7.346771" />
-  <D value="8.198478E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="469.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.9285E+07" />
-  <B value="3.2175" />
-  <C value="-7.404" />
-  <D value="7.8553" />
-  <E value="-3.1858" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="468.93" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-20332" />
-  <B value="1447.4" />
-  <C value="-11.168" />
-  <D value="0.034509" />
-  <E value="0.0000067015" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="160.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81911" />
-  <B value="-50003" />
-  <C value="534.49" />
-  <D value="-1.8654" />
-  <E value="0.00223" />
-  <Tmin units="K"  value="160.6" />
-  <Tmax units="K"  value="285" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="31884.09" />
-  <B value="-715.0886" />
-  <C value="12.13937" />
-  <D value="-0.0000867837" />
-  <E value="-5.187264E-09" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.05805" />
-  <B value="-49.435" />
-  <C value="-18.537" />
-  <D value="7195.3" />
-  <E value="-17758" />
-  <Tmin units="K"  value="234.57" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.5785" />
-  <B value="634.7" />
-  <C value="-0.32031" />
-  <D value="-8.1095E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="469.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010777" />
-  <B value="0.52994" />
-  <C value="452.12" />
-  <D value="-16957" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="1223.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.2748" />
-  <B value="8.1093" />
-  <C value="-0.70065" />
-  <D value="-0.00041054" />
-  <E value="-6.2588E-07" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="433.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.00032904" />
-  <B value="1.1711" />
-  <C value="-7027.1" />
-  <D value="89001" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.041866" />
-  <B value="-3.1134" />
-  <C value="-2.1272" />
-  <D value="-0.0015044" />
-  <E value="-0.0000015749" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="452.91" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-7520.322" />
-  <B value="222.0616" />
-  <C value="-0.125595" />
-  <D value="0.0000259182" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-13.87179" />
-  <B value="-7000" />
-  <C value="-42" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.753" />
-  <B value="2668.9" />
-  <C value="-22.526" />
-  <Tmin units="K"  value="282.36" />
-  <Tmax units="K"  value="420.44" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.1876" />
-  <B value="-0.041268" />
-  <C value="0.000058903" />
-  <Tmin units="K"  value="160.65" />
-  <Tmax units="K"  value="303.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.13515" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.910399E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="235.8602" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="47.15" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.01111" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.02" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.88208" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2114" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0497046" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.5927" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.32" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.12867" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.202" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21584" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0497046" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="1" />
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="1" />
-  <group id="21"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="1" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-21-8" />
-<Smiles name="SMILES"  value="C1OC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1252" />
-<CompoundID name="Name"  value="Acetic acid" />
-<StructureFormula name="Structure"  value="CH3COOH" />
-<Family name="Family"  value="50" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="594.45" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5790000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.171" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.2" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="391.04" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="289.81" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="289.81" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1280" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="60.053" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.05753" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.46" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.61E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19060" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.8E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0333" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.18E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.328E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.745E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="282500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.173E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.29616" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-7.866E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="23.877" />
-  <B value="-0.0096568" />
-  <Tmin units="K"  value="115.92" />
-  <Tmax units="K"  value="289.81" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0627" />
-  <B value="0.22174" />
-  <C value="594.76" />
-  <D value="0.22566" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="594.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="87.50607" />
-  <B value="-7603.906" />
-  <C value="-9.655308" />
-  <D value="7.168835E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="594.75" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.6203E+07" />
-  <B value="6.7121" />
-  <C value="-17.45" />
-  <D value="17.2" />
-  <E value="-6.0038" />
-  <Tmin units="K"  value="289.81" />
-  <Tmax units="K"  value="591.95" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12076" />
-  <B value="1070.4" />
-  <C value="-5.5698" />
-  <D value="0.01112" />
-  <E value="-9.9868E-07" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="289.81" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="49034" />
-  <B value="1051.1" />
-  <C value="0.77564" />
-  <D value="0.031667" />
-  <E value="-0.000028344" />
-  <Tmin units="K"  value="289.69" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="40110" />
-  <B value="-588.24" />
-  <C value="12.017" />
-  <D value="0.00016249" />
-  <E value="-8.6918E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-58.528" />
-  <B value="2990.9" />
-  <C value="7.4911" />
-  <D value="-0.000011028" />
-  <E value="2" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="391.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.3395E-09" />
-  <B value="1.24" />
-  <C value="-175.09" />
-  <D value="25013" />
-  <Tmin units="K"  value="289.81" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11159" />
-  <B value="-531.13" />
-  <C value="1.6359" />
-  <D value="-0.009369" />
-  <E value="-7.1996E-07" />
-  <Tmin units="K"  value="274.09" />
-  <Tmax units="K"  value="391.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.34137" />
-  <B value="-0.80579" />
-  <C value="-824.3" />
-  <D value="175840" />
-  <Tmin units="K"  value="391.05" />
-  <Tmax units="K"  value="468.55" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.025913" />
-  <B value="31.086" />
-  <C value="-2.8254" />
-  <D value="0.000036752" />
-  <E value="-0.0000025639" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="591.95" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="36376" />
-  <B value="-19.93" />
-  <C value="0.56181" />
-  <D value="-0.00072868" />
-  <E value="2.8918E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.091204" />
-  <B value="-3100" />
-  <C value="-18.6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.785" />
-  <B value="4151.5" />
-  <C value="-22.49" />
-  <Tmin units="K"  value="361.02" />
-  <Tmax units="K"  value="533.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.57433" />
-  <B value="-0.034964" />
-  <C value="0.00003435" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="391.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.17407" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.14509E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="118.2324" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="53.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.05202" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0235" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.0515" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.43099" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0575804" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.23" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.04" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.92225" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.4566" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18501.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0575804" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="64-19-7" />
-<Smiles name="SMILES"  value="CC(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1301" />
-<CompoundID name="Name"  value="Methyl formate" />
-<StructureFormula name="Structure"  value="HCOOCH3" />
-<Family name="Family"  value="55" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="487.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.172" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="304.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="174.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="174.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.88085" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="60.053" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.06214" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.253" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.387E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20500" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.9E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03251" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.09E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.524E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.95E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="285200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7531000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.86547" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.924E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="23.868" />
-  <B value="-0.015242" />
-  <Tmin units="K"  value="69.66" />
-  <Tmax units="K"  value="174.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.213" />
-  <B value="0.23619" />
-  <C value="487.2" />
-  <D value="0.24621" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="487.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="70.6458" />
-  <B value="-5401.751" />
-  <C value="-7.334787" />
-  <D value="5.934343E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="487.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.0578E+07" />
-  <B value="3.7855" />
-  <C value="-9.0874" />
-  <D value="9.6043" />
-  <E value="-3.7868" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="487.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="78860" />
-  <Tmin units="K"  value="293" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97064" />
-  <B value="3377.4" />
-  <C value="-42.373" />
-  <D value="0.22648" />
-  <E value="-0.00029763" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="304.9" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="41319" />
-  <B value="-570.15" />
-  <C value="12.038" />
-  <D value="-0.000034216" />
-  <E value="-2.7109E-11" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.095846" />
-  <B value="-103.82" />
-  <C value="-15.924" />
-  <D value="-865.24" />
-  <E value="-816.67" />
-  <Tmin units="K"  value="243.6" />
-  <Tmax units="K"  value="1948.8" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.949" />
-  <B value="1214.4" />
-  <C value="-0.53562" />
-  <D value="0.000010346" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="304.9" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000069776" />
-  <B value="0.31537" />
-  <C value="1034.6" />
-  <D value="13.293" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0090363" />
-  <B value="23.594" />
-  <C value="-1.5627" />
-  <D value="0.00089283" />
-  <E value="-0.0000058101" />
-  <Tmin units="K"  value="146.16" />
-  <Tmax units="K"  value="386.16" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-817050" />
-  <B value="-0.23016" />
-  <C value="2.5314E+08" />
-  <D value="-1.5205E+12" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013259" />
-  <B value="47.144" />
-  <C value="-3.0417" />
-  <D value="0.001159" />
-  <E value="-0.0000083817" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="470.72" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="18932" />
-  <B value="149.77" />
-  <C value="0.096448" />
-  <D value="-0.00024287" />
-  <E value="1.1158E-07" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-7.378946" />
-  <B value="-4250" />
-  <C value="-25.5" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.436" />
-  <B value="2622.4" />
-  <C value="-40.294" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="437.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0549" />
-  <B value="-0.05168" />
-  <C value="0.000071381" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="304.9" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.16931" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.348593E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="232.362" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="53.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.22908" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0245" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.981244" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.25698" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0620841" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.1431" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.036" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.86272" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.257" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20503.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0620841" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="24"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="23"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="24"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="23"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-31-3" />
-<Smiles name="SMILES"  value="COC(=O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1503" />
-<CompoundID name="Name"  value="Ethyl chloride" />
-<StructureFormula name="Structure"  value="CH3CH2Cl" />
-<Family name="Family"  value="65" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="460.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5300000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.199" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.276" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="285.42" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="136.75" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="134.8" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.1249" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="64.514" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07258" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.194" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.267E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03552" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.27E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.1226E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-6.0499E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="275780" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4451800" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.77201" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.2849E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="21.614" />
-  <B value="-0.018098" />
-  <Tmin units="K"  value="53.92" />
-  <Tmax units="K"  value="134.8" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3553" />
-  <B value="0.26895" />
-  <C value="460.36" />
-  <D value="0.24994" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="460.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="51.28342" />
-  <B value="-4206.393" />
-  <C value="-4.478839" />
-  <D value="3.812824E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="460.35" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.61548E+07" />
-  <B value="0.981924" />
-  <C value="-2.026046" />
-  <D value="2.205811" />
-  <E value="-0.774155" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="443.22" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13544" />
-  <B value="1361" />
-  <C value="-5.3607" />
-  <D value="-0.058393" />
-  <E value="0.00049341" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="134.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="95946" />
-  <B value="-7247" />
-  <C value="67.469" />
-  <D value="-0.16696" />
-  <E value="0.00017795" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="340" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="12765.96" />
-  <B value="-117.0948" />
-  <C value="11.04141" />
-  <D value="0.00111696" />
-  <E value="-3.565557E-07" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.11811" />
-  <B value="-121.34" />
-  <C value="-10.857" />
-  <D value="-276.9" />
-  <E value="96.111" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="1841.6" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.065" />
-  <B value="698.32" />
-  <C value="-0.097691" />
-  <D value="8.0018E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.2572E-07" />
-  <B value="0.66869" />
-  <C value="165.43" />
-  <D value="-2726.9" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.062544" />
-  <B value="150.84" />
-  <C value="-4.3182" />
-  <D value="0.012599" />
-  <E value="-0.000031799" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-19.83" />
-  <B value="0.20145" />
-  <C value="-728060" />
-  <D value="-2.7917E+08" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.036834" />
-  <B value="33.167" />
-  <C value="-2.7206" />
-  <D value="0.000040391" />
-  <E value="-0.0000033391" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="443.22" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="25185" />
-  <B value="82.189" />
-  <C value="0.24669" />
-  <D value="-0.00037831" />
-  <E value="1.5556E-07" />
-  <Tmin units="K"  value="134.8" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-8.394" />
-  <B value="-4725" />
-  <C value="-28.35" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.412" />
-  <B value="2616.2" />
-  <C value="-20.799" />
-  <Tmin units="K"  value="276.6" />
-  <Tmax units="K"  value="408.95" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.7339" />
-  <B value="-0.03541" />
-  <C value="0.000044884" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.1858" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.45E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="423" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="64.35" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0268" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.902494" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.18795" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0708426" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.3665" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.112" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.190636" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17772.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0708426" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="45"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="31"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="35"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="45"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="44"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-00-3" />
-<Smiles name="SMILES"  value="CC[Cl]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2" />
-<CompoundID name="Name"  value="Ethane" />
-<StructureFormula name="Structure"  value="CH3CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="305.32" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4872000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1455" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.279" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="184.55" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="90.352" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="90.352" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.13" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="30.07" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04615" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.099" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.826E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12400" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02734" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.24E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-8.382E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.192E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="229120" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2859000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.68638" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.42864E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="25.301" />
-  <B value="-0.012024" />
-  <Tmin units="K"  value="23.15" />
-  <Tmax units="K"  value="90.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3749" />
-  <B value="0.23949" />
-  <C value="305.43" />
-  <D value="0.22875" />
-  <Tmin units="K"  value="88.71" />
-  <Tmax units="K"  value="305.42" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="61.43744" />
-  <B value="-2814.319" />
-  <C value="-6.778053" />
-  <D value="0.0000210827" />
-  <E value="2" />
-  <Tmin units="K"  value="90.35" />
-  <Tmax units="K"  value="305.42" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.3996E+07" />
-  <B value="1.4625" />
-  <C value="-2.8991" />
-  <D value="2.8421" />
-  <E value="-0.99532" />
-  <Tmin units="K"  value="89.88" />
-  <Tmax units="K"  value="305.33" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7021.9" />
-  <B value="-1326.3" />
-  <C value="90.192" />
-  <D value="-1.4782" />
-  <E value="0.0082308" />
-  <Tmin units="K"  value="15.53" />
-  <Tmax units="K"  value="78.55" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68726" />
-  <B value="-1953.6" />
-  <C value="31.772" />
-  <D value="-0.10571" />
-  <E value="0.00019673" />
-  <Tmin units="K"  value="88.71" />
-  <Tmax units="K"  value="290" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="35666.22" />
-  <B value="-616.5198" />
-  <C value="11.69914" />
-  <D value="0.000444525" />
-  <E value="-1.541942E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.080874" />
-  <B value="-61.025" />
-  <C value="-1.5752" />
-  <D value="9.7998" />
-  <E value="-13.178" />
-  <Tmin units="K"  value="115" />
-  <Tmax units="K"  value="1773.15" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-33.92204" />
-  <B value="743.404" />
-  <C value="4.302492" />
-  <D value="-0.0000364469" />
-  <E value="2" />
-  <Tmin units="K"  value="90.35" />
-  <Tmax units="K"  value="300" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.2452E-07" />
-  <B value="0.58906" />
-  <C value="188.8" />
-  <D value="-2953.8" />
-  <Tmin units="K"  value="90.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.073876" />
-  <B value="-9.6787" />
-  <C value="-0.67405" />
-  <D value="-0.003407" />
-  <E value="-0.0000022023" />
-  <Tmin units="K"  value="90.35" />
-  <Tmax units="K"  value="300" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000074549" />
-  <B value="1.168" />
-  <C value="506.4" />
-  <D value="-881.74" />
-  <Tmin units="K"  value="184.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0092564" />
-  <B value="30.13" />
-  <C value="-3.5743" />
-  <D value="0.0026003" />
-  <E value="-0.000021736" />
-  <Tmin units="K"  value="89.88" />
-  <Tmax units="K"  value="305.32" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34738" />
-  <B value="-36.808" />
-  <C value="0.4706" />
-  <D value="-0.000553" />
-  <E value="2.0678E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.962" />
-  <B value="1665.8" />
-  <C value="-7.8809" />
-  <Tmin units="K"  value="183.85" />
-  <Tmax units="K"  value="273.32" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.6951" />
-  <B value="-0.027749" />
-  <C value="0.000033258" />
-  <Tmin units="K"  value="90.35" />
-  <Tmax units="K"  value="300" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.14575" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.540889E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="201.2999" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2793" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="45.66" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.42475" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0197" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.355683" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0983" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0551979" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.8022" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.696" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="1.696" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.012416" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.72531" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.0908" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="12375.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0551979" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="6"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="230"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-84-0" />
-<Smiles name="SMILES"  value="CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1102" />
-<CompoundID name="Name"  value="Ethanol" />
-<StructureFormula name="Structure"  value="CH3CH2OH" />
-<Family name="Family"  value="27" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="513.92" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6148000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.167" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.24" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="351.8" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="159.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="159.05" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000495642" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="46.069" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.05868" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.649" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.259E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="26140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.64E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03194" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.93E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.3495E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.6785E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="280640" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4931000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3327" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.235E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="24.584" />
-  <B value="-0.016742" />
-  <Tmin units="K"  value="63.62" />
-  <Tmax units="K"  value="159.05" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3539" />
-  <B value="0.24957" />
-  <C value="515.66" />
-  <D value="0.22099" />
-  <Tmin units="K"  value="159" />
-  <Tmax units="K"  value="515.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="88.0754" />
-  <B value="-7652.06" />
-  <C value="-9.471507" />
-  <D value="5.928087E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="159.05" />
-  <Tmax units="K"  value="516.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.3899E+07" />
-  <B value="1.2782" />
-  <C value="-2.673" />
-  <D value="2.7973" />
-  <E value="-1.0209" />
-  <Tmin units="K"  value="159.05" />
-  <Tmax units="K"  value="515.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12797" />
-  <B value="1133.1" />
-  <C value="-7.3716" />
-  <D value="0.021296" />
-  <E value="-0.0000012564" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="159" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="76684" />
-  <B value="675.72" />
-  <C value="-0.093875" />
-  <D value="0.037153" />
-  <E value="-0.000031214" />
-  <Tmin units="K"  value="158.5" />
-  <Tmax units="K"  value="399.82" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="44530" />
-  <B value="-660.89" />
-  <C value="12.153" />
-  <D value="0.000019532" />
-  <E value="-1.5636E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.03174" />
-  <B value="-35.721" />
-  <C value="-17.382" />
-  <D value="-6686.6" />
-  <E value="-21212" />
-  <Tmin units="K"  value="263" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="8.061" />
-  <B value="774.76" />
-  <C value="-3.0701" />
-  <D value="-4.3408E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="440" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2467E-07" />
-  <B value="0.7862" />
-  <C value="76.034" />
-  <D value="-2017.3" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10247" />
-  <B value="-120.39" />
-  <C value="-0.48487" />
-  <D value="-0.0071706" />
-  <E value="0.000003461" />
-  <Tmin units="K"  value="159.05" />
-  <Tmax units="K"  value="353.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.01001" />
-  <B value="0.64925" />
-  <C value="-7360.5" />
-  <D value="-255250" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.078773" />
-  <B value="19.874" />
-  <C value="-2.3731" />
-  <D value="0.00067227" />
-  <E value="-0.0000021132" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="503.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="36550" />
-  <B value="5.2215" />
-  <C value="0.46112" />
-  <D value="-0.00058401" />
-  <E value="2.2324E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="121" />
-  <A value="-25.13869" />
-  <B value="17834.39" />
-  <C value="-2.936184" />
-  <D value="0.0226118" />
-  <E value="1.015427" />
-  <Tmin units="K"  value="288" />
-  <Tmax units="K"  value="510" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.994" />
-  <B value="3337.3" />
-  <C value="-60.406" />
-  <Tmin units="K"  value="308.5" />
-  <Tmax units="K"  value="458.7" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.9282" />
-  <B value="-0.045463" />
-  <C value="0.000042849" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="440" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.169282" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.31E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="431" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="51.77" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.96946" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0277" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.79598" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.634" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0586177" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.11" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.97" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.92" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="1.678665" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.216396" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-3.1879" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.634" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="26133.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0586177" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="64-17-5" />
-<Smiles name="SMILES"  value="CCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1401" />
-<CompoundID name="Name"  value="Dimethyl ether" />
-<StructureFormula name="Structure"  value="CH3OCH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="400.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.17" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.276" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="248.31" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="131.66" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="131.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.04959" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="46.069" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.06907" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.191" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.154E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15120" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.34E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03104" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.841E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.128E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="266700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4937000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.77572" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.3284E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="24.059" />
-  <B value="-0.020492" />
-  <Tmin units="K"  value="52.66" />
-  <Tmax units="K"  value="131.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.4889" />
-  <B value="0.26123" />
-  <C value="400.1" />
-  <D value="0.27948" />
-  <Tmin units="K"  value="131.65" />
-  <Tmax units="K"  value="400.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="50.32175" />
-  <B value="-3631.453" />
-  <C value="-4.444735" />
-  <D value="5.290757E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="131.65" />
-  <Tmax units="K"  value="400.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.8521E+07" />
-  <B value="2.2845" />
-  <C value="-5.7518" />
-  <D value="6.5695" />
-  <E value="-2.6976" />
-  <Tmin units="K"  value="131.65" />
-  <Tmax units="K"  value="400.1" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13616" />
-  <B value="1241.9" />
-  <C value="-7.8805" />
-  <D value="0.023826" />
-  <E value="0.0000089126" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="131.64" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97754" />
-  <B value="353.35" />
-  <C value="-1.896" />
-  <D value="0.040999" />
-  <E value="-0.000017816" />
-  <Tmin units="K"  value="131.64" />
-  <Tmax units="K"  value="250" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="37573.94" />
-  <B value="-346.059" />
-  <C value="11.12596" />
-  <D value="0.00118434" />
-  <E value="-4.086847E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.1196" />
-  <B value="-114.27" />
-  <C value="-4.7652" />
-  <D value="-552.86" />
-  <E value="923.94" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.661" />
-  <B value="449.83" />
-  <C value="0.0072727" />
-  <D value="-3.6906E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="131.65" />
-  <Tmax units="K"  value="248.31" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000027281" />
-  <B value="0.3952" />
-  <C value="534.12" />
-  <D value="2319" />
-  <Tmin units="K"  value="131.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.15344" />
-  <B value="-11.847" />
-  <C value="-0.56462" />
-  <D value="-0.0022104" />
-  <E value="5.6048E-07" />
-  <Tmin units="K"  value="120.03" />
-  <Tmax units="K"  value="320.03" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.059968" />
-  <B value="0.26671" />
-  <C value="1018.3" />
-  <D value="1098900" />
-  <Tmin units="K"  value="248.31" />
-  <Tmax units="K"  value="1500" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0093353" />
-  <B value="46.031" />
-  <C value="-3.4828" />
-  <D value="0.0024176" />
-  <E value="-0.000014319" />
-  <Tmin units="K"  value="131.65" />
-  <Tmax units="K"  value="400.1" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="36259" />
-  <B value="50.469" />
-  <C value="0.24104" />
-  <D value="-0.00029774" />
-  <E value="1.0659E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="4" />
-  <A value="14.87198" />
-  <B value="-0.0266292" />
-  <C value="-0.0000434922" />
-  <D value="0.0000000821" />
-  <Tmin units="K"  value="155" />
-  <Tmax units="K"  value="510" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.354" />
-  <B value="2237.8" />
-  <C value="-20.775" />
-  <Tmin units="K"  value="241.96" />
-  <Tmax units="K"  value="357.71" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.0837" />
-  <B value="-0.041241" />
-  <C value="0.000073668" />
-  <Tmin units="K"  value="131.65" />
-  <Tmax units="K"  value="248.31" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.18366" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.21E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="432" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="51.77" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.04503" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0233" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.670302" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1972" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0703107" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.0461" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.936" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.17891" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15212.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0703107" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="25"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="24"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="115-10-6" />
-<Smiles name="SMILES"  value="COC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1201" />
-<CompoundID name="Name"  value="Ethylene glycol" />
-<StructureFormula name="Structure"  value="HOCH2CH2OH" />
-<Family name="Family"  value="49" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="719" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="8200000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.191" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.262" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="470.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="260.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="260.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.21922" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="62.0678" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.055908" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.506776" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.564E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="33840" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.04E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03654" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.62E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.922E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.018E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="304891" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9958000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.25835" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.0527E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="23.236" />
-  <B value="-0.009952" />
-  <Tmin units="K"  value="104.06" />
-  <Tmax units="K"  value="260.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3106" />
-  <B value="0.25084" />
-  <C value="720" />
-  <D value="0.21838" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="695.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="68.11797" />
-  <B value="-9617.267" />
-  <C value="-5.83171" />
-  <D value="-1.13705E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="720" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.414E+07" />
-  <B value="0.16807" />
-  <C value="-0.19694" />
-  <D value="1.0417" />
-  <E value="-0.61488" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="695.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="24975" />
-  <B value="-137.65" />
-  <C value="6.7837" />
-  <D value="-0.041927" />
-  <E value="0.000088083" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="240" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86990" />
-  <B value="-72.326" />
-  <C value="9.7466" />
-  <D value="0.0065456" />
-  <E value="-0.0000047" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="493.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="52948" />
-  <B value="-604.61" />
-  <C value="12.115" />
-  <D value="0.00010607" />
-  <E value="-4.9352E-08" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.078528" />
-  <B value="282.59" />
-  <C value="-200.74" />
-  <D value="1071400" />
-  <E value="-5423600" />
-  <Tmin units="K"  value="360" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-309.38" />
-  <B value="14928" />
-  <C value="45.49" />
-  <D value="-0.000044405" />
-  <E value="2" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="576" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2284E-07" />
-  <B value="0.79557" />
-  <C value="132.87" />
-  <D value="-5540.3" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.1684" />
-  <B value="-313.75" />
-  <C value="-1.072" />
-  <D value="-0.000058054" />
-  <E value="-0.0000032443" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="470.45" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-8962900" />
-  <B value="-0.31257" />
-  <C value="2.5313E+09" />
-  <D value="-1.2955E+13" />
-  <Tmin units="K"  value="279.13" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0064328" />
-  <B value="94.796" />
-  <C value="-3.4232" />
-  <D value="0.001824" />
-  <E value="-0.0000039732" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="470.45" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="12781" />
-  <B value="255.9" />
-  <C value="-0.13868" />
-  <D value="0.000028589" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-9.798016" />
-  <B value="-14083.52" />
-  <C value="-5.743104" />
-  <Tmin units="K"  value="278" />
-  <Tmax units="K"  value="720" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.236" />
-  <B value="3826" />
-  <C value="-113.27" />
-  <Tmin units="K"  value="433.1" />
-  <Tmax units="K"  value="647.39" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="11.094" />
-  <B value="-0.068649" />
-  <C value="0.000060412" />
-  <Tmin units="K"  value="260.15" />
-  <Tmax units="K"  value="576" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.193662" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.361602E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="378.5562" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="57.88" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0334" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.11071" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.48683" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0559089" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.41" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.25" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.48683" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="33703.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0559089" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="15"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="2" />
-  <group id="14"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="2" />
-  <group id="15"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="2" />
-  <group id="15"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="14"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-21-1" />
-<Smiles name="SMILES"  value="OCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1820" />
-<CompoundID name="Name"  value="Dimethyl sulfide" />
-<StructureFormula name="Structure"  value="(CH3)2S" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="503" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5530000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.201" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="310.48" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="174.88" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="174.88" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.86415" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="62.136" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07377" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.19" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.374E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18530" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03814" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.724E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7302000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="285850" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7984700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.87394" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.7443E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="19.669" />
-  <B value="-0.01188" />
-  <Tmin units="K"  value="69.95" />
-  <Tmax units="K"  value="174.88" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1867" />
-  <B value="0.25844" />
-  <C value="503.06" />
-  <D value="0.24773" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="503.05" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="14.07567" />
-  <B value="-3435.088" />
-  <C value="1.598135" />
-  <D value="-0.0000069451" />
-  <E value="2" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="503.04" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.490637E+07" />
-  <B value="1.721854" />
-  <C value="-2.161256" />
-  <D value="0.932609" />
-  <E value="-0.0179494" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="491.99" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12181" />
-  <B value="1107.6" />
-  <C value="-5.0143" />
-  <D value="0.0082042" />
-  <E value="0.000012693" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="170" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="112410" />
-  <B value="-20036" />
-  <C value="201.07" />
-  <D value="-0.63397" />
-  <E value="0.0007177" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="310.48" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="56893" />
-  <B value="-682.39" />
-  <C value="12.01" />
-  <D value="0.00013748" />
-  <E value="-5.7442E-08" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.11611" />
-  <B value="-141.79" />
-  <C value="-13.232" />
-  <D value="-216.03" />
-  <E value="14.289" />
-  <Tmin units="K"  value="251.5" />
-  <Tmax units="K"  value="1760.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.044" />
-  <B value="992.97" />
-  <C value="0.60378" />
-  <D value="0.0000010306" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="310.48" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.8631E-07" />
-  <B value="0.62748" />
-  <C value="355.22" />
-  <D value="-11800" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10006" />
-  <B value="-155.98" />
-  <C value="-0.57159" />
-  <D value="-0.0045066" />
-  <E value="-0.0000087305" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="310.48" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00026184" />
-  <B value="0.91507" />
-  <C value="780.75" />
-  <D value="-32167" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.021126" />
-  <B value="18.794" />
-  <C value="-2.708" />
-  <D value="-0.00021089" />
-  <E value="-0.0000043376" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="485.77" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="29392" />
-  <B value="145.75" />
-  <C value="0.049554" />
-  <D value="-0.00013569" />
-  <E value="5.7869E-08" />
-  <Tmin units="K"  value="174.88" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.185871" />
-  <B value="-3150" />
-  <C value="-18.9" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.142" />
-  <B value="2682.7" />
-  <C value="-31.19" />
-  <Tmin units="K"  value="303.88" />
-  <Tmax units="K"  value="451.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.3718" />
-  <B value="-0.037395" />
-  <C value="0.000048797" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="310.48" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.20227" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.355323E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="279.2898" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.273888" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="68.56" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.85309" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0291" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.848" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.19359" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0730914" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.5141" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.216" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.7269" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.189279" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18513.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0730914" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="102"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="102"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="122"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-18-3" />
-<Smiles name="SMILES"  value="CSC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1802" />
-<CompoundID name="Name"  value="Ethyl mercaptan" />
-<StructureFormula name="Structure"  value="CH3CH2SH" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="499" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5490000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.207" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.274" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="308.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="125.26" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="125.26" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00113837" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="62.136" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07458" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.189" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.363E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.27E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03871" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.75E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.63E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4814000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="296100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4975000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.79757" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.7366E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="20.608" />
-  <B value="-0.018284" />
-  <Tmin units="K"  value="50.1" />
-  <Tmax units="K"  value="125.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.203" />
-  <B value="0.25909" />
-  <C value="499.16" />
-  <D value="0.26567" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="499.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="65.4773" />
-  <B value="-5020.82" />
-  <C value="-6.678317" />
-  <D value="6.449817E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="499.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.1777E+07" />
-  <B value="0.6898" />
-  <C value="-0.36317" />
-  <D value="-0.097723" />
-  <E value="0.16958" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="479.47" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14082" />
-  <B value="1399.4" />
-  <C value="-10.378" />
-  <D value="0.036681" />
-  <E value="-0.0000060677" />
-  <Tmin units="K"  value="14" />
-  <Tmax units="K"  value="125.26" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="112430" />
-  <B value="-35384" />
-  <C value="348.44" />
-  <D value="-1.1065" />
-  <E value="0.0012231" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="315.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39403.72" />
-  <B value="-328.0582" />
-  <C value="11.29594" />
-  <D value="0.000950986" />
-  <E value="-3.249647E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.11733" />
-  <B value="-135.4" />
-  <C value="-13.776" />
-  <D value="-593.18" />
-  <E value="775.57" />
-  <Tmin units="K"  value="249.5" />
-  <Tmax units="K"  value="1996" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.854" />
-  <B value="753.55" />
-  <C value="0.040849" />
-  <D value="-7.5884E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="308.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000001695" />
-  <B value="0.75553" />
-  <C value="151.56" />
-  <D value="-5377.8" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.021257" />
-  <B value="2.7237" />
-  <C value="-1.42" />
-  <D value="-0.0008779" />
-  <E value="-0.0000018277" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="308.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0014607" />
-  <B value="0.7033" />
-  <C value="1243.2" />
-  <D value="53588" />
-  <Tmin units="K"  value="308.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.051518" />
-  <B value="-2.7266" />
-  <C value="-2.1105" />
-  <D value="-0.0014355" />
-  <E value="-5.6772E-07" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="479.47" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="32377" />
-  <B value="107.68" />
-  <C value="0.17061" />
-  <D value="-0.0002733" />
-  <E value="1.0909E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-6.861601" />
-  <B value="-4000" />
-  <C value="-24" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.188" />
-  <B value="2662" />
-  <C value="-32.622" />
-  <Tmin units="K"  value="299.82" />
-  <Tmax units="K"  value="440.11" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.92662" />
-  <B value="-0.056615" />
-  <C value="0.000088024" />
-  <Tmin units="K"  value="125.26" />
-  <Tmax units="K"  value="308.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.20227" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.219166E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="308.2589" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="68.56" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.22578" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0292" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.836507" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.19144" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0746133" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.551747" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.3" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.763226" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.003516" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.43784" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.192074" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18270.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0746133" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="61"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="55"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<CAS name="CAS number"  value="75-08-1" />
-<Smiles name="SMILES"  value="CCS" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1704" />
-<CompoundID name="Name"  value="Ethylamine" />
-<StructureFormula name="Structure"  value="CH3CH2NH2" />
-<Family name="Family"  value="34" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="456.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5630000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1818" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="289.75" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="192.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="192.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="151.827" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="45.084" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.06659" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.276" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.336E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19100" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03444" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.21E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.715E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.616E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="284800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9350000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91282" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.5874E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="22.309" />
-  <B value="-0.012854" />
-  <Tmin units="K"  value="76.86" />
-  <Tmax units="K"  value="192.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3663" />
-  <B value="0.25297" />
-  <C value="456.4" />
-  <D value="0.27948" />
-  <Tmin units="K"  value="183.15" />
-  <Tmax units="K"  value="456.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="115.5255" />
-  <B value="-6764.221" />
-  <C value="-14.43912" />
-  <D value="0.0000155603" />
-  <E value="2" />
-  <Tmin units="K"  value="190.85" />
-  <Tmax units="K"  value="456.35" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.2765E+07" />
-  <B value="0.58718" />
-  <C value="-0.33502" />
-  <D value="0.17251" />
-  <E value="-0.0015134" />
-  <Tmin units="K"  value="192.15" />
-  <Tmax units="K"  value="456.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19740" />
-  <B value="1233.4" />
-  <C value="-7.495" />
-  <D value="0.02025" />
-  <E value="-7.8895E-11" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="160" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="129790" />
-  <B value="-12366" />
-  <C value="-31.003" />
-  <D value="0.53709" />
-  <E value="-0.00091494" />
-  <Tmin units="K"  value="192.15" />
-  <Tmax units="K"  value="348.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="55762" />
-  <B value="-832.71" />
-  <C value="12.632" />
-  <D value="-0.00036845" />
-  <E value="1.1147E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.097539" />
-  <B value="-107.69" />
-  <C value="-12.336" />
-  <D value="-330.4" />
-  <E value="-136.4" />
-  <Tmin units="K"  value="228" />
-  <Tmax units="K"  value="1824" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-41.853" />
-  <B value="1619.5" />
-  <C value="5.3649" />
-  <D value="-0.000030563" />
-  <E value="2" />
-  <Tmin units="K"  value="192.15" />
-  <Tmax units="K"  value="289.73" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.0871E-07" />
-  <B value="0.59417" />
-  <C value="255.23" />
-  <D value="-186.42" />
-  <Tmin units="K"  value="192.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.17744" />
-  <B value="585.82" />
-  <C value="-11.165" />
-  <D value="0.043182" />
-  <E value="-0.000095024" />
-  <Tmin units="K"  value="192.15" />
-  <Tmax units="K"  value="413.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.40679" />
-  <B value="0.005162" />
-  <C value="1280.6" />
-  <D value="1721800" />
-  <Tmin units="K"  value="274.01" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0085203" />
-  <B value="136.14" />
-  <C value="-4.284" />
-  <D value="0.0057402" />
-  <E value="-0.000016476" />
-  <Tmin units="K"  value="192.15" />
-  <Tmax units="K"  value="456.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="38579" />
-  <B value="17.203" />
-  <C value="0.48199" />
-  <D value="-0.00063681" />
-  <E value="2.5301E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.139524" />
-  <B value="-3150" />
-  <C value="-18.9" />
-  <Tmin units="K"  value="275.2611" />
-  <Tmax units="K"  value="445.2611" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.457" />
-  <B value="2460.8" />
-  <C value="-42.073" />
-  <Tmin units="K"  value="275.03" />
-  <Tmax units="K"  value="403.75" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.14104" />
-  <B value="-0.042353" />
-  <C value="0.000044446" />
-  <Tmin units="K"  value="192.15" />
-  <Tmax units="K"  value="289.73" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.1772" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.1558E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="256.8617" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="52.51" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.09415" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0249" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.607317" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.28709" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0656335" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.2703" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.084" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.54441" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.285061" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19493.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0656335" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="30"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="29"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="30"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="29"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-04-7" />
-<Smiles name="SMILES"  value="CCN" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1774" />
-<CompoundID name="Name"  value="Acrylonitrile" />
-<StructureFormula name="Structure"  value="CH2CHCN" />
-<Family name="Family"  value="38" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="535" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4480000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.212" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.214" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="350.5" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="189.63" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="189.63" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.68289" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="53.0626" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0662367" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.349801" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.464E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21560" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.29E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0351" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.13E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.837E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.937E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="275300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6230000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2803" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.69E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="21.906" />
-  <B value="-0.012833" />
-  <Tmin units="K"  value="75.85" />
-  <Tmax units="K"  value="189.63" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0816" />
-  <B value="0.2293" />
-  <C value="535" />
-  <D value="0.28939" />
-  <Tmin units="K"  value="189.63" />
-  <Tmax units="K"  value="535" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="74.54771" />
-  <B value="-6259.727" />
-  <C value="-7.785577" />
-  <D value="4.08032E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="189.63" />
-  <Tmax units="K"  value="535" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.224752E+07" />
-  <B value="0.877802" />
-  <C value="-0.432396" />
-  <D value="-0.672186" />
-  <E value="0.607598" />
-  <Tmin units="K"  value="189.63" />
-  <Tmax units="K"  value="535" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="378880" />
-  <B value="-12940" />
-  <C value="173.11" />
-  <D value="-0.95095" />
-  <E value="0.001872" />
-  <Tmin units="K"  value="109.32" />
-  <Tmax units="K"  value="183.69" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83847" />
-  <B value="240.59" />
-  <C value="6.8887" />
-  <D value="0.0095277" />
-  <E value="-0.0000046046" />
-  <Tmin units="K"  value="189.63" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="42651" />
-  <B value="-533.04" />
-  <C value="11.728" />
-  <D value="0.00013096" />
-  <E value="-6.2176E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16669" />
-  <B value="-180.08" />
-  <C value="-27.078" />
-  <D value="1693.8" />
-  <E value="-10134" />
-  <Tmin units="K"  value="267.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-0.5429" />
-  <B value="318.29" />
-  <C value="-1.481" />
-  <D value="-8.3759E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="350.5" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.616E-08" />
-  <B value="0.90278" />
-  <C value="67.424" />
-  <D value="-1672.6" />
-  <Tmin units="K"  value="189.63" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.15669" />
-  <B value="19.22" />
-  <C value="-1.0721" />
-  <D value="0.00025871" />
-  <E value="-0.0000022582" />
-  <Tmin units="K"  value="189.63" />
-  <Tmax units="K"  value="350.5" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0012317" />
-  <B value="1.2472" />
-  <C value="60863" />
-  <D value="-1968600" />
-  <Tmin units="K"  value="350.5" />
-  <Tmax units="K"  value="990.5" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.031468" />
-  <B value="13.152" />
-  <C value="-2.5363" />
-  <D value="-0.00042782" />
-  <E value="-0.0000025175" />
-  <Tmin units="K"  value="189.63" />
-  <Tmax units="K"  value="535" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="10676.73" />
-  <B value="220.6432" />
-  <C value="-0.156498" />
-  <D value="0.0000460366" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-18.507" />
-  <B value="-10000" />
-  <C value="-99" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.64" />
-  <B value="4865.9" />
-  <C value="50.629" />
-  <Tmin units="K"  value="323.15" />
-  <Tmax units="K"  value="480.47" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.2702" />
-  <B value="-0.022461" />
-  <C value="0.000022239" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="350.5" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.186019" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.077183E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="135.7552" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259865" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="59.17" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.1648" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0272" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.805" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.349801" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0662367" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.31" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.05" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.1533" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.349801" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21555.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0662367" />
-<UnifacVLE name="UNIFAC" >
-  <group id="69"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="49"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="69"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="69"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="68"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-13-1" />
-<Smiles name="SMILES"  value="C=CC#N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="402" />
-<CompoundID name="Name"  value="Methylacetylene" />
-<StructureFormula name="Structure"  value="CH3CCH" />
-<Family name="Family"  value="15" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="402.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5630000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1635" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="250.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="170.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="170.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="414.934" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="40.065" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.06231" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.214" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.908E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15870" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.61E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03327" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.849E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.9384E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="248360" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5350000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.81477" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.8487E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="24.138" />
-  <B value="-0.01566" />
-  <Tmin units="K"  value="68.18" />
-  <Tmax units="K"  value="170.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.5983" />
-  <B value="0.26361" />
-  <C value="402.4" />
-  <D value="0.27835" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="402.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="68.97649" />
-  <B value="-4285.953" />
-  <C value="-7.418705" />
-  <D value="0.000010515" />
-  <E value="2" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="402.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.4954E+07" />
-  <B value="0.52948" />
-  <C value="0.26449" />
-  <D value="-0.89434" />
-  <E value="0.5174" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="402.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="62910" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85291" />
-  <B value="38.538" />
-  <C value="6.7428" />
-  <D value="0.016885" />
-  <E value="-0.000022161" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="249.94" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="34169.26" />
-  <B value="-350.7621" />
-  <C value="11.18743" />
-  <D value="0.000684714" />
-  <E value="-2.185041E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.095128" />
-  <B value="-87.916" />
-  <C value="-5.1804" />
-  <D value="-112.52" />
-  <E value="81.984" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="1821" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-0.91891" />
-  <B value="242.44" />
-  <C value="-1.5439" />
-  <D value="5.0147E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010586" />
-  <B value="0.48791" />
-  <C value="277.58" />
-  <D value="3995.6" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="800" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.065025" />
-  <B value="-121.87" />
-  <C value="-0.025752" />
-  <D value="-0.0097723" />
-  <E value="0.0000047452" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="249.94" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00029245" />
-  <B value="0.88088" />
-  <C value="248.57" />
-  <D value="78809" />
-  <Tmin units="K"  value="249.94" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013277" />
-  <B value="71.214" />
-  <C value="-3.6751" />
-  <D value="0.0034836" />
-  <E value="-0.00001379" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="402.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="26257" />
-  <B value="101.52" />
-  <C value="0.09703" />
-  <D value="-0.00019256" />
-  <E value="8.3311E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.828" />
-  <B value="-1015" />
-  <C value="-6.09" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="420" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.159" />
-  <B value="2098.1" />
-  <C value="-32.215" />
-  <Tmin units="K"  value="242.07" />
-  <Tmax units="K"  value="353.57" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.2379" />
-  <B value="-0.023223" />
-  <C value="0.000025756" />
-  <Tmin units="K"  value="170.45" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.17325" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.803432E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="251.8656" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2703" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="56.93999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.02941" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0227" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.620536" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2161" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0596157" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.1931" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.936" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002337" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.033" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2176" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18393.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0596157" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="66"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="53"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="66"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="65"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-99-7" />
-<Smiles name="SMILES"  value="CC#C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="301" />
-<CompoundID name="Name"  value="Propadiene" />
-<StructureFormula name="Structure"  value="CH2CCH2" />
-<Family name="Family"  value="14" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="394" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5250000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1739" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.279" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="238.77" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="136.87" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="136.87" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="18.2497" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="40.065" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.06095" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.122" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.911E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14010" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03084" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.70603E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.905E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.008E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="243900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4400000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.52532" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.8563E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="24.735" />
-  <B value="-0.020311" />
-  <Tmin units="K"  value="54.75" />
-  <Tmax units="K"  value="136.87" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.86549" />
-  <B value="0.19732" />
-  <C value="394" />
-  <D value="0.21029" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="392.34" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.80183" />
-  <B value="-3745.303" />
-  <C value="-6.036523" />
-  <D value="8.205156E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="394" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.54657E+07" />
-  <B value="-3.722436" />
-  <C value="11.45729" />
-  <D value="-12.9266" />
-  <E value="5.522823" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="380.47" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="62910" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78665" />
-  <B value="-12422" />
-  <C value="151.08" />
-  <D value="-0.53356" />
-  <E value="0.00065986" />
-  <Tmin units="K"  value="137.6" />
-  <Tmax units="K"  value="362.6" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="34671.52" />
-  <B value="-447.4983" />
-  <C value="11.46556" />
-  <D value="0.000444481" />
-  <E value="-1.470826E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.08647" />
-  <B value="-87.335" />
-  <C value="-4.7756" />
-  <D value="123.57" />
-  <E value="-266.38" />
-  <Tmin units="K"  value="196.5" />
-  <Tmax units="K"  value="1965" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.5153" />
-  <B value="310.76" />
-  <C value="-0.034725" />
-  <D value="-0.0000021543" />
-  <E value="2" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="313.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.3119E-07" />
-  <B value="0.52792" />
-  <C value="129.92" />
-  <D value="8459.5" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.06063" />
-  <B value="169.42" />
-  <C value="-4.6941" />
-  <D value="0.014436" />
-  <E value="-0.000036249" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="353.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000059663" />
-  <B value="1.0782" />
-  <C value="9.0271" />
-  <D value="65666" />
-  <Tmin units="K"  value="238.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.047886" />
-  <B value="-2.5247" />
-  <C value="-2.1453" />
-  <D value="-0.0026156" />
-  <E value="8.3096E-07" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="380.47" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="28294" />
-  <B value="52.14" />
-  <C value="0.28169" />
-  <D value="-0.00042512" />
-  <E value="1.7968E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-3.588" />
-  <B value="-1610" />
-  <C value="-9.66" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="400" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.034" />
-  <B value="2061.4" />
-  <C value="-22.057" />
-  <Tmin units="K"  value="236.75" />
-  <Tmax units="K"  value="353.4" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-5.1491" />
-  <B value="-0.021234" />
-  <C value="0.000029507" />
-  <Tmin units="K"  value="136.87" />
-  <Tmax units="K"  value="313.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.1655" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.818957E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="259.7674" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="56.93999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.7583" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0221" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.655593" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.143" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0604292" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.7917" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.528" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.79629" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3125" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17551" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0604292" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="463-49-0" />
-<Smiles name="SMILES"  value="C=C=C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="202" />
-<CompoundID name="Name"  value="Propylene" />
-<StructureFormula name="Structure"  value="CH2CHCH3" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="364.85" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4600000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.185" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.281" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="225.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="87.9" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="87.89" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00117" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="42.0797" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0832412" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.137588" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.2311E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="11890" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.22E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03408" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.06E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.023E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.264E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="267000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2936000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.7091" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.9262E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="20.846" />
-  <B value="-0.020946" />
-  <Tmin units="K"  value="73.15" />
-  <Tmax units="K"  value="88.1" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.98129" />
-  <B value="0.22226" />
-  <C value="365.58" />
-  <D value="0.24039" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="365.57" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="55.10362" />
-  <B value="-3330.452" />
-  <C value="-5.40588" />
-  <D value="0.0000093641" />
-  <E value="2" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="365.57" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.7525E+07" />
-  <B value="0.61217" />
-  <C value="-0.41646" />
-  <D value="0.083772" />
-  <E value="0.12092" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="365" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-1062" />
-  <B value="-87.684" />
-  <C value="46.783" />
-  <D value="-0.8344" />
-  <E value="0.0046648" />
-  <Tmin units="K"  value="14" />
-  <Tmax units="K"  value="87.89" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="79790" />
-  <B value="300.8" />
-  <C value="5.1342" />
-  <D value="0.0095615" />
-  <E value="0.000012777" />
-  <Tmin units="K"  value="87.85" />
-  <Tmax units="K"  value="340" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="38965.36" />
-  <B value="-516.3838" />
-  <C value="11.75322" />
-  <D value="0.000509119" />
-  <E value="-1.771348E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.10916" />
-  <B value="-86.745" />
-  <C value="-4.9899" />
-  <D value="455.7" />
-  <E value="-924.7" />
-  <Tmin units="K"  value="182.43" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-54.05485" />
-  <B value="1437.773" />
-  <C value="7.536247" />
-  <D value="-0.0000342733" />
-  <E value="2" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="333.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.3873E-07" />
-  <B value="0.54213" />
-  <C value="262.33" />
-  <D value="-108.51" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.044587" />
-  <B value="22.061" />
-  <C value="-1.744" />
-  <D value="0.0015214" />
-  <E value="-0.0000078162" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="340.49" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000045373" />
-  <B value="1.2" />
-  <C value="415.83" />
-  <D value="2757.2" />
-  <Tmin units="K"  value="225.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012171" />
-  <B value="10.886" />
-  <C value="-2.9978" />
-  <D value="-0.00044205" />
-  <E value="-0.0000097257" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="364.85" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="5083.56" />
-  <B value="225.639" />
-  <C value="-0.0999265" />
-  <D value="0.0000133106" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-19.10663" />
-  <B value="-5950" />
-  <C value="-35.7" />
-  <Tmin units="K"  value="208.5945" />
-  <Tmax units="K"  value="378.5945" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.886" />
-  <B value="1932.7" />
-  <C value="-18.939" />
-  <Tmin units="K"  value="219.08" />
-  <Tmax units="K"  value="327.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.81493" />
-  <B value="-0.05511" />
-  <C value="0.000087429" />
-  <Tmin units="K"  value="87.89" />
-  <Tmax units="K"  value="333.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.18287" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.877396E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="246.8143" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2785" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="61.56" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.10396" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0249" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.520955" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1455" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.068956" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.25" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.02" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.006163" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.14989" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1477" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13152.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.068956" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="115-07-1" />
-<Smiles name="SMILES"  value="C=CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1051" />
-<CompoundID name="Name"  value="Acetone" />
-<StructureFormula name="Structure"  value="CH3COCH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="508.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4700000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.209" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.233" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="329.22" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="178.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="178.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.78509" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="58.08" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07394" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.307" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.746E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.61E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03904" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.157E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.513E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="295400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5774000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97946" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.659E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.677" />
-  <B value="1.103E-09" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="183.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1051" />
-  <B value="0.24556" />
-  <C value="508.21" />
-  <D value="0.27409" />
-  <Tmin units="K"  value="178" />
-  <Tmax units="K"  value="508.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="72.77713" />
-  <B value="-5752.936" />
-  <C value="-7.680083" />
-  <D value="6.83076E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="178.45" />
-  <Tmax units="K"  value="508.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.6943E+07" />
-  <B value="3.4736" />
-  <C value="-8.9271" />
-  <D value="10.062" />
-  <E value="-4.1656" />
-  <Tmin units="K"  value="178.45" />
-  <Tmax units="K"  value="508.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13993" />
-  <B value="1377" />
-  <C value="-8.1059" />
-  <D value="0.029271" />
-  <E value="-0.00004792" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="178.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="107130" />
-  <B value="725.57" />
-  <C value="0.95296" />
-  <D value="0.025981" />
-  <E value="-0.00001439" />
-  <Tmin units="K"  value="178.45" />
-  <Tmax units="K"  value="329.44" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="52915" />
-  <B value="-669.27" />
-  <C value="12.201" />
-  <D value="0.00012839" />
-  <E value="-5.8844E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.11111" />
-  <B value="-97.677" />
-  <C value="-32.713" />
-  <D value="4172.3" />
-  <E value="-24006" />
-  <Tmin units="K"  value="254.1" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-14.064" />
-  <B value="1000.7" />
-  <C value="0.45349" />
-  <D value="3.9456E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="329.44" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.1012E-08" />
-  <B value="0.97616" />
-  <C value="23.042" />
-  <D value="14.834" />
-  <Tmin units="K"  value="178.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.01013" />
-  <B value="-95.32" />
-  <C value="-0.21151" />
-  <D value="-0.0052616" />
-  <E value="0.0000023043" />
-  <Tmin units="K"  value="178.45" />
-  <Tmax units="K"  value="343.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-26.882" />
-  <B value="0.9036" />
-  <C value="-1.2095E+08" />
-  <D value="-6.0879E+08" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.036769" />
-  <B value="-1.4835" />
-  <C value="-2.315" />
-  <D value="-0.0012473" />
-  <E value="-0.000001404" />
-  <Tmin units="K"  value="178.45" />
-  <Tmax units="K"  value="490.84" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="42620" />
-  <B value="12.563" />
-  <C value="0.4765" />
-  <D value="-0.00059673" />
-  <E value="2.2682E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="121" />
-  <A value="-21.42358" />
-  <B value="9644.46" />
-  <C value="2.243534" />
-  <D value="-0.00962352" />
-  <E value="1" />
-  <Tmin units="K"  value="294" />
-  <Tmax units="K"  value="508" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.434" />
-  <B value="2850.7" />
-  <C value="-41.681" />
-  <Tmin units="K"  value="305" />
-  <Tmax units="K"  value="456.13" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.32411" />
-  <B value="-0.042986" />
-  <C value="0.000056727" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="329.44" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.20983" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.5E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="549" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="67.67" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.27474" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0289" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.79" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3149" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0738386" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.5735" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.336" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.336" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.27841" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3099" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19729.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0738386" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="67-64-1" />
-<Smiles name="SMILES"  value="CC(=O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1302" />
-<CompoundID name="Name"  value="Ethyl formate" />
-<StructureFormula name="Structure"  value="HCOOCH2CH3" />
-<Family name="Family"  value="55" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="508.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4740000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.229" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="327.47" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="193.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="193.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="18.1186" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.079" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08093" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.282" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.963E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19070" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.44E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04274" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.44E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.883E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.031E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="328200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9204800" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91636" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.50696E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.766" />
-  <B value="-0.010171" />
-  <Tmin units="K"  value="77.42" />
-  <Tmax units="K"  value="193.55" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.85568" />
-  <B value="0.22882" />
-  <C value="508.5" />
-  <D value="0.23792" />
-  <Tmin units="K"  value="193.55" />
-  <Tmax units="K"  value="508.45" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="69.04518" />
-  <B value="-5678.642" />
-  <C value="-7.031396" />
-  <D value="0.0000050057" />
-  <E value="2" />
-  <Tmin units="K"  value="193.55" />
-  <Tmax units="K"  value="508.45" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.9813E+07" />
-  <B value="2.1931" />
-  <C value="-4.6587" />
-  <D value="4.7089" />
-  <E value="-1.7696" />
-  <Tmin units="K"  value="193.55" />
-  <Tmax units="K"  value="508.45" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="104870" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115910" />
-  <B value="228.3" />
-  <C value="4.0783" />
-  <D value="0.027366" />
-  <E value="-0.000029781" />
-  <Tmin units="K"  value="254.2" />
-  <Tmax units="K"  value="374.2" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="52378" />
-  <B value="-459.08" />
-  <C value="11.875" />
-  <D value="0.00065506" />
-  <E value="-2.4832E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12511" />
-  <B value="-132.24" />
-  <C value="-21.864" />
-  <D value="-2112.2" />
-  <E value="1102.8" />
-  <Tmin units="K"  value="254.2" />
-  <Tmax units="K"  value="1779.4" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.9483" />
-  <B value="848.56" />
-  <C value="-0.31567" />
-  <D value="2.8582E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="245" />
-  <Tmax units="K"  value="345" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.0691E-07" />
-  <B value="0.60378" />
-  <C value="450.04" />
-  <D value="-20466" />
-  <Tmin units="K"  value="193.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.030927" />
-  <B value="19.999" />
-  <C value="-1.4911" />
-  <D value="-0.000052048" />
-  <E value="-0.0000024111" />
-  <Tmin units="K"  value="193.55" />
-  <Tmax units="K"  value="433.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="381.39" />
-  <B value="0.9159" />
-  <C value="1.8E+09" />
-  <D value="-1.1462E+10" />
-  <Tmin units="K"  value="278.12" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.02094" />
-  <B value="32.394" />
-  <C value="-2.9299" />
-  <D value="0.00035555" />
-  <E value="-0.0000045837" />
-  <Tmin units="K"  value="193.55" />
-  <Tmax units="K"  value="508.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="28653" />
-  <B value="223.54" />
-  <C value="-0.054573" />
-  <D value="-0.0000084089" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.722828" />
-  <B value="-3550" />
-  <C value="-21.3" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.231" />
-  <B value="2723.8" />
-  <C value="-46.87" />
-  <Tmin units="K"  value="309.55" />
-  <Tmax units="K"  value="453.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.5155" />
-  <B value="-0.032057" />
-  <C value="0.000035967" />
-  <Tmin units="K"  value="245" />
-  <Tmax units="K"  value="345" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.22605" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.82913E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="249.4384" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="73.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.06979" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0317" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.928963" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.28499" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0808277" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.8175" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.576" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.17409" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.285" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18938.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0808277" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="24"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="23"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="24"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="23"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-94-4" />
-<Smiles name="SMILES"  value="CCOC(=O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1312" />
-<CompoundID name="Name"  value="Methyl acetate" />
-<StructureFormula name="Structure"  value="CH3COOCH3" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="506.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4690000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.228" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="330.09" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="175.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="175.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.01703" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.079" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07989" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.323" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.996E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19350" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.6E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04254" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.44E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.119E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.242E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="319800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7970000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.96569" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.461E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.35" />
-  <B value="-0.011504" />
-  <Tmin units="K"  value="70.06" />
-  <Tmax units="K"  value="175.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.98331" />
-  <B value="0.2428" />
-  <C value="506.86" />
-  <D value="0.2549" />
-  <Tmin units="K"  value="175.15" />
-  <Tmax units="K"  value="506.85" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="83.01817" />
-  <B value="-6288.581" />
-  <C value="-9.185862" />
-  <D value="7.595367E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="175.15" />
-  <Tmax units="K"  value="506.85" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.9929E+07" />
-  <B value="0.79197" />
-  <C value="-0.73136" />
-  <D value="0.37429" />
-  <E value="-0.019974" />
-  <Tmin units="K"  value="175.15" />
-  <Tmax units="K"  value="506.85" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="104870" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="6314.4" />
-  <B value="680.3" />
-  <C value="4.1767" />
-  <D value="0.026148" />
-  <E value="-0.000027341" />
-  <Tmin units="K"  value="207.38" />
-  <Tmax units="K"  value="373.4" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62235" />
-  <B value="-685.05" />
-  <C value="12.348" />
-  <D value="0.00012363" />
-  <E value="-8.5641E-08" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12428" />
-  <B value="-150.24" />
-  <C value="-26.001" />
-  <D value="-830.67" />
-  <E value="-2742.3" />
-  <Tmin units="K"  value="253.4" />
-  <Tmax units="K"  value="1773.8" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="11.12" />
-  <B value="-100.13" />
-  <C value="-3.2745" />
-  <D value="-5.3051E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="425" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000013226" />
-  <B value="0.48849" />
-  <C value="504.21" />
-  <D value="4.2341" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="800" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.28416" />
-  <B value="27.186" />
-  <C value="-0.94457" />
-  <D value="0.00083974" />
-  <E value="-0.0000024412" />
-  <Tmin units="K"  value="175.15" />
-  <Tmax units="K"  value="386.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-23257" />
-  <B value="-0.1738" />
-  <C value="1.0287E+07" />
-  <D value="-6.9243E+10" />
-  <Tmin units="K"  value="276.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.053249" />
-  <B value="2.5722" />
-  <C value="-2.2027" />
-  <D value="-0.00085349" />
-  <E value="-0.0000011835" />
-  <Tmin units="K"  value="175.15" />
-  <Tmax units="K"  value="506.55" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="35270" />
-  <B value="119.63" />
-  <C value="0.27754" />
-  <D value="-0.0004099" />
-  <E value="1.6055E-07" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.348193" />
-  <B value="-3350" />
-  <C value="-20.1" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.435" />
-  <B value="2829.7" />
-  <C value="-44.587" />
-  <Tmin units="K"  value="305.73" />
-  <Tmax units="K"  value="454.22" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.8922" />
-  <B value="-0.016855" />
-  <C value="0.000011239" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="425" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.22619" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.04E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="418" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="73.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0318" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.939333" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.32049" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0798903" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.8" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.58" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.326" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19435.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0798903" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-20-9" />
-<Smiles name="SMILES"  value="CC(=O)OC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1253" />
-<CompoundID name="Name"  value="Propionic acid" />
-<StructureFormula name="Structure"  value="CH3CH2COOH" />
-<Family name="Family"  value="50" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="604" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4530000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.233" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.207" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="414.31" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="252.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="252.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="13.1" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.079" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07497" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.544" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.107E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19490" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04342" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.53E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.535E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.568E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="294900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.066E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.7827" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.395E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.159" />
-  <B value="-0.0088316" />
-  <Tmin units="K"  value="100.98" />
-  <Tmax units="K"  value="252.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.88103" />
-  <B value="0.22848" />
-  <C value="612.66" />
-  <D value="0.25898" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="612.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="58.42" />
-  <B value="-7261.2" />
-  <C value="-4.9024" />
-  <D value="0.0000010406" />
-  <E value="2" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="600.81" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.8878E+07" />
-  <B value="3.7167" />
-  <C value="-10.822" />
-  <D value="11.498" />
-  <E value="-4.1176" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="600.81" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14676" />
-  <B value="1223.1" />
-  <C value="-7.0075" />
-  <D value="0.021772" />
-  <E value="-0.000020423" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="252.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="120710" />
-  <B value="704.7" />
-  <C value="1.1886" />
-  <D value="0.028883" />
-  <E value="-0.000020278" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="414.32" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="47961" />
-  <B value="-474.81" />
-  <C value="12.167" />
-  <D value="0.00020648" />
-  <E value="-6.6213E-08" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-53.41646" />
-  <B value="2724.985" />
-  <C value="6.7143" />
-  <D value="-9.670276E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="414.32" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.6155E-08" />
-  <B value="1.0459" />
-  <C value="-115.32" />
-  <D value="27680" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.067757" />
-  <B value="-235.87" />
-  <C value="-0.022659" />
-  <D value="-0.0065033" />
-  <E value="0.0000026666" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="543.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.004145" />
-  <B value="0.70902" />
-  <C value="13255" />
-  <D value="-4962900" />
-  <Tmin units="K"  value="414.32" />
-  <Tmax units="K"  value="616.15" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010977" />
-  <B value="146.33" />
-  <C value="-4.0999" />
-  <D value="0.0031834" />
-  <E value="-0.0000071046" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="600.81" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="8861" />
-  <B value="324.07" />
-  <C value="-0.19078" />
-  <D value="0.000043643" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.46964" />
-  <B value="-1550" />
-  <C value="-9.3" />
-  <Tmin units="K"  value="268.5945" />
-  <Tmax units="K"  value="438.5945" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.83" />
-  <B value="4099" />
-  <C value="-51.622" />
-  <Tmin units="K"  value="362.46" />
-  <Tmax units="K"  value="527.47" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.81021" />
-  <B value="-0.03741" />
-  <C value="0.000039093" />
-  <Tmin units="K"  value="252.45" />
-  <Tmax units="K"  value="414.32" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.230362" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.600915E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="135.9701" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="73.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="4.20003" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0303" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.52" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0749523" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.9" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.58" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-9.25219" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.52" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19130.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0749523" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-09-4" />
-<Smiles name="SMILES"  value="CCC(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1876" />
-<CompoundID name="Name"  value="N,n-dimethylformamide" />
-<StructureFormula name="Structure"  value="HCON(CH3)2" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="649.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4420000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.26199" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.214" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="425.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="212.72" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="212.72" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.195325" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="73.0938" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0773903" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.31771" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.027E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23960" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.27E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04681" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.917E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-8.84E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="326000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.615E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.19402" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.78871E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.71" />
-  <B value="-0.0092912" />
-  <Tmin units="K"  value="85.09" />
-  <Tmax units="K"  value="212.72" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.65216" />
-  <B value="0.20032" />
-  <C value="649.6" />
-  <D value="0.24418" />
-  <Tmin units="K"  value="212.72" />
-  <Tmax units="K"  value="649.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="68.99879" />
-  <B value="-7311.388" />
-  <C value="-6.749791" />
-  <D value="3.063845E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="212.72" />
-  <Tmax units="K"  value="649.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.7496E+07" />
-  <B value="0.2466" />
-  <C value="0.21619" />
-  <D value="-0.11587" />
-  <E value="0.026126" />
-  <Tmin units="K"  value="212.72" />
-  <Tmax units="K"  value="649.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="21466" />
-  <B value="82.722" />
-  <C value="-0.65111" />
-  <D value="0.003066" />
-  <E value="-0.0000053042" />
-  <Tmin units="K"  value="83" />
-  <Tmax units="K"  value="208" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="141440" />
-  <B value="162.91" />
-  <C value="4.0696" />
-  <D value="0.019381" />
-  <E value="-0.000013063" />
-  <Tmin units="K"  value="273.82" />
-  <Tmax units="K"  value="466.44" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68728" />
-  <B value="-846.07" />
-  <C value="13.139" />
-  <D value="-0.00064688" />
-  <E value="1.6133E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30845" />
-  <B value="-426.73" />
-  <C value="-16.98" />
-  <D value="-72873" />
-  <E value="162690" />
-  <Tmin units="K"  value="298.28" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.089031" />
-  <B value="826.091" />
-  <C value="-0.0843389" />
-  <D value="-3.479212E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="240" />
-  <Tmax units="K"  value="425.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000034602" />
-  <B value="0.37991" />
-  <C value="1156.9" />
-  <D value="8715.8" />
-  <Tmin units="K"  value="212.72" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.14084" />
-  <B value="-2496" />
-  <C value="20.244" />
-  <D value="-0.064914" />
-  <E value="0.000049356" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="425.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.015205" />
-  <B value="0.35461" />
-  <C value="594.92" />
-  <D value="741220" />
-  <Tmin units="K"  value="425.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.069456" />
-  <B value="-10.189" />
-  <C value="-1.894" />
-  <D value="-0.0010897" />
-  <E value="-1.2078E-07" />
-  <Tmin units="K"  value="212.72" />
-  <Tmax units="K"  value="649.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="6716" />
-  <B value="349.57" />
-  <C value="-0.18657" />
-  <D value="0.000033656" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.780432" />
-  <B value="-10711.33" />
-  <C value="-45.18602" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="649" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.586" />
-  <B value="3764.7" />
-  <C value="-50.993" />
-  <Tmin units="K"  value="396.67" />
-  <Tmax units="K"  value="580.62" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.0021666" />
-  <B value="-0.035024" />
-  <C value="0.000037609" />
-  <Tmin units="K"  value="240" />
-  <Tmax units="K"  value="425.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.24059" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.594689E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="164.8347" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="74.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.74822" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0342" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.953395" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3672" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0773743" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.0856" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.736" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.60584" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.375516" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23964.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0773743" />
-<UnifacVLE name="UNIFAC" >
-  <group id="72"  value="1" />
-  </UnifacVLE>
-<GCmethod name="PPR78" >
-  <group id="72"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="72"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="72"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="68-12-2" />
-<Smiles name="SMILES"  value="CN(C)C=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="3" />
-<CompoundID name="Name"  value="Propane" />
-<StructureFormula name="Structure"  value="CH3CH2CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="369.83" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4248000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.276" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="231.02" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="85.47" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="85.47" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0001685" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="44.097" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07487" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.152" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.431E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13100" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03757" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.59E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.0468E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.439E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="270200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3524000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.75108" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.04311E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.861" />
-  <B value="-0.020332" />
-  <Tmin units="K"  value="23.15" />
-  <Tmax units="K"  value="85.48" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3186" />
-  <B value="0.27005" />
-  <C value="369.86" />
-  <D value="0.27852" />
-  <Tmin units="K"  value="85.47" />
-  <Tmax units="K"  value="369.85" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="55.2725" />
-  <B value="-3396.946" />
-  <C value="-5.423393" />
-  <D value="8.953731E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="85.47" />
-  <Tmax units="K"  value="371.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.0459E+07" />
-  <B value="1.2001" />
-  <C value="-2.1107" />
-  <D value="1.9732" />
-  <E value="-0.65316" />
-  <Tmin units="K"  value="85.44" />
-  <Tmax units="K"  value="369.85" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-9928.1" />
-  <B value="957.89" />
-  <C value="-0.77533" />
-  <D value="-0.03376" />
-  <E value="0.00014632" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="84" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="87486" />
-  <B value="-13371" />
-  <C value="156.92" />
-  <D value="-0.5459" />
-  <E value="0.00068504" />
-  <Tmin units="K"  value="85.47" />
-  <Tmax units="K"  value="360" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="37840.4" />
-  <B value="-445.5789" />
-  <C value="11.83871" />
-  <D value="0.000653764" />
-  <E value="-2.200137E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12162" />
-  <B value="-107.8" />
-  <C value="-3.8081" />
-  <D value="-15.233" />
-  <E value="-13.005" />
-  <Tmin units="K"  value="122" />
-  <Tmax units="K"  value="1849.1" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-35.23159" />
-  <B value="966.1472" />
-  <C value="4.395026" />
-  <D value="-0.0000255079" />
-  <E value="2" />
-  <Tmin units="K"  value="85.47" />
-  <Tmax units="K"  value="363.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.7422E-08" />
-  <B value="0.90416" />
-  <C value="-4.7484" />
-  <D value="478.57" />
-  <Tmin units="K"  value="85.47" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.02937" />
-  <B value="-16.323" />
-  <C value="-1.3313" />
-  <D value="-0.0012596" />
-  <E value="-0.000011206" />
-  <Tmin units="K"  value="85.47" />
-  <Tmax units="K"  value="350" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-1.139" />
-  <B value="0.10904" />
-  <C value="-9898.6" />
-  <D value="-7669600" />
-  <Tmin units="K"  value="231.11" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0093557" />
-  <B value="17.245" />
-  <C value="-3.1909" />
-  <D value="0.00024043" />
-  <E value="-0.000011944" />
-  <Tmin units="K"  value="85.44" />
-  <Tmax units="K"  value="369.98" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="31986" />
-  <B value="42.662" />
-  <C value="0.49978" />
-  <D value="-0.00065626" />
-  <E value="0.000000256" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.381181" />
-  <B value="-800" />
-  <C value="-4.8" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="424.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.04" />
-  <B value="2072.9" />
-  <C value="-13.18" />
-  <Tmin units="K"  value="222" />
-  <Tmax units="K"  value="332.05" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.343" />
-  <B value="-0.040027" />
-  <C value="0.00005517" />
-  <Tmin units="K"  value="85.47" />
-  <Tmax units="K"  value="363.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.20008" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.114825E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="234.5244" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2763" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="66.17999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.31941" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0268" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.506678" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1532" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0757055" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.4766" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.236" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.236" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003791" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.59617" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1538" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13091.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.084" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-98-6" />
-<Smiles name="SMILES"  value="CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1104" />
-<CompoundID name="Name"  value="Isopropanol" />
-<StructureFormula name="Structure"  value="CH3CH(OH)CH3" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="508.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4762000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.22" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="355.39" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="185.28" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="185.28" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0363946" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="60.096" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07692" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.665" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.807E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23420" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.54E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04216" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.27E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.727E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.7347E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="309200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5410000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1433" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.83E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.573" />
-  <B value="-0.011338" />
-  <Tmin units="K"  value="74.11" />
-  <Tmax units="K"  value="185.28" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1898" />
-  <B value="0.26648" />
-  <C value="508.3" />
-  <D value="0.23986" />
-  <Tmin units="K"  value="185.28" />
-  <Tmax units="K"  value="508.3" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="77.70856" />
-  <B value="-7630.115" />
-  <C value="-7.63517" />
-  <D value="9.965114E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="185.28" />
-  <Tmax units="K"  value="508.3" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.100995E+08" />
-  <B value="4.1961" />
-  <C value="-10.70959" />
-  <D value="11.69444" />
-  <E value="-4.625499" />
-  <Tmin units="K"  value="185.28" />
-  <Tmax units="K"  value="508.3" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5999" />
-  <B value="747.79" />
-  <C value="1.6541" />
-  <D value="-0.049958" />
-  <E value="0.0001963" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="185.26" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-188260" />
-  <B value="277.99" />
-  <C value="9.4459" />
-  <D value="0.010702" />
-  <E value="-0.0000091964" />
-  <Tmin units="K"  value="185.26" />
-  <Tmax units="K"  value="480" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="52738" />
-  <B value="-555.28" />
-  <C value="12.347" />
-  <D value="0.000094247" />
-  <E value="-4.5945E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.085006" />
-  <B value="-95.666" />
-  <C value="-21.924" />
-  <D value="-3475.4" />
-  <E value="-29704" />
-  <Tmin units="K"  value="279" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.4407" />
-  <B value="2259.7" />
-  <C value="-1.1149" />
-  <D value="0.0000002963" />
-  <E value="2" />
-  <Tmin units="K"  value="187.35" />
-  <Tmax units="K"  value="355.41" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9931E-07" />
-  <B value="0.72329" />
-  <C value="178.01" />
-  <D value="-15.318" />
-  <Tmin units="K"  value="185.28" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.15761" />
-  <B value="49.41" />
-  <C value="-1.6579" />
-  <D value="0.0019566" />
-  <E value="-0.0000034939" />
-  <Tmin units="K"  value="183.65" />
-  <Tmax units="K"  value="410.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0028843" />
-  <B value="0.91609" />
-  <C value="11082" />
-  <D value="-222500" />
-  <Tmin units="K"  value="278.59" />
-  <Tmax units="K"  value="995.41" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0068771" />
-  <B value="-355.64" />
-  <C value="0.079386" />
-  <D value="-0.0097522" />
-  <E value="0.0000049723" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="355.41" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="27720" />
-  <B value="156.75" />
-  <C value="0.30298" />
-  <D value="-0.00050843" />
-  <E value="2.1144E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-22.81" />
-  <B value="-10000" />
-  <C value="-60.54" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.151" />
-  <B value="2836.6" />
-  <C value="-88.244" />
-  <Tmin units="K"  value="305.37" />
-  <Tmax units="K"  value="457.3" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="14.129" />
-  <B value="-0.10641" />
-  <C value="0.00012806" />
-  <Tmin units="K"  value="187.35" />
-  <Tmax units="K"  value="355.41" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.23883" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.64E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="518" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2493" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="72.28999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="3.2725" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0368" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.786" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.66368" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0768988" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.78" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.51" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.89" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.140334" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="1.269059" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-7.9945" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.7238" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23408.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0768988" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="16"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="67-63-0" />
-<Smiles name="SMILES"  value="CC(O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1103" />
-<CompoundID name="Name"  value="1-propanol" />
-<StructureFormula name="Structure"  value="CH3(CH2)2OH" />
-<Family name="Family"  value="27" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="536.78" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5175000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.219" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="370.93" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="146.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="146.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.69121E-07" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="60.096" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07514" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.629" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.7359E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24450" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.6E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04217" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.28E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.552E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.599E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="322470" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5372000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1406" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.84381E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.17" />
-  <B value="-0.0024097" />
-  <Tmin units="K"  value="146.95" />
-  <Tmax units="K"  value="156.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1537" />
-  <B value="0.26188" />
-  <C value="536.78" />
-  <D value="0.23549" />
-  <Tmin units="K"  value="146.95" />
-  <Tmax units="K"  value="536.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="141.3971" />
-  <B value="-10434.27" />
-  <C value="-17.45829" />
-  <D value="0.0000113246" />
-  <E value="2" />
-  <Tmin units="K"  value="146.95" />
-  <Tmax units="K"  value="536.85" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.36461E+07" />
-  <B value="3.338812" />
-  <C value="-9.831137" />
-  <D value="11.8901" />
-  <E value="-4.905709" />
-  <Tmin units="K"  value="146.95" />
-  <Tmax units="K"  value="536.85" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11319" />
-  <B value="1041" />
-  <C value="-3.5625" />
-  <D value="-0.011478" />
-  <E value="0.00010513" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="148.74" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="100520" />
-  <B value="125.3" />
-  <C value="4.7194" />
-  <D value="0.024513" />
-  <E value="-0.000019669" />
-  <Tmin units="K"  value="146.95" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="56681" />
-  <B value="-627.22" />
-  <C value="12.379" />
-  <D value="0.00012228" />
-  <E value="-5.0293E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.037896" />
-  <B value="-44.849" />
-  <C value="-35.117" />
-  <D value="410.57" />
-  <E value="-27077" />
-  <Tmin units="K"  value="295.19" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-98.08798" />
-  <B value="4904.749" />
-  <C value="13.57131" />
-  <D value="-0.0000219968" />
-  <E value="2" />
-  <Tmin units="K"  value="146.95" />
-  <Tmax units="K"  value="370.35" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.9322E-07" />
-  <B value="0.54936" />
-  <C value="416.77" />
-  <D value="-100.81" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.076645" />
-  <B value="-189.91" />
-  <C value="-0.13475" />
-  <D value="-0.0069283" />
-  <E value="0.0000033645" />
-  <Tmin units="K"  value="164.06" />
-  <Tmax units="K"  value="380.35" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-453.4" />
-  <B value="0.64532" />
-  <C value="-2.843E+08" />
-  <D value="-2.8865E+10" />
-  <Tmin units="K"  value="275.28" />
-  <Tmax units="K"  value="720.25" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0044121" />
-  <B value="-393.81" />
-  <C value="0.44289" />
-  <D value="-0.010936" />
-  <E value="0.0000062593" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="370.35" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="39178" />
-  <B value="54.585" />
-  <C value="0.52464" />
-  <D value="-0.00069351" />
-  <E value="2.6739E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-17.3" />
-  <B value="-10000" />
-  <C value="-30" />
-  <Tmin units="K"  value="243" />
-  <Tmax units="K"  value="536" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.11" />
-  <B value="2968.4" />
-  <C value="-89.944" />
-  <Tmin units="K"  value="323.15" />
-  <Tmax units="K"  value="482.63" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="16.105" />
-  <B value="-0.12454" />
-  <C value="0.00016492" />
-  <Tmin units="K"  value="146.95" />
-  <Tmax units="K"  value="370.35" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.23623" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.71E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="495" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2451" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="72.28999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="2.198" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.038" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.804" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.62489" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0749393" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.78" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.51" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.89" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.169684" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="1.188769" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-4.4989" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.623" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24557.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0749393" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="15"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="71-23-8" />
-<Smiles name="SMILES"  value="CCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1703" />
-<CompoundID name="Name"  value="Trimethylamine" />
-<StructureFormula name="Structure"  value="(CH3)3N" />
-<Family name="Family"  value="35" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="433.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4075000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.254" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="276.02" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="156.08" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="156.08" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="9.92058" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="59.111" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09428" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.206243" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.691E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14360" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.04E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04534" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.59E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.431E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.899E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="287000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6544000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.78024" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.2449E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.673" />
-  <B value="-0.011817" />
-  <Tmin units="K"  value="62.43" />
-  <Tmax units="K"  value="156.08" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.67928" />
-  <B value="0.21649" />
-  <C value="433.3" />
-  <D value="0.20925" />
-  <Tmin units="K"  value="156" />
-  <Tmax units="K"  value="433.25" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="110.254" />
-  <B value="-5770.536" />
-  <C value="-14.1719" />
-  <D value="0.0000238614" />
-  <E value="2" />
-  <Tmin units="K"  value="156.08" />
-  <Tmax units="K"  value="433.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.743116E+07" />
-  <B value="0.966273" />
-  <C value="0.752593" />
-  <D value="-2.762744" />
-  <E value="1.513109" />
-  <Tmin units="K"  value="156.07" />
-  <Tmax units="K"  value="433.25" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12954" />
-  <B value="1371.3" />
-  <C value="-11.233" />
-  <D value="0.058409" />
-  <E value="-0.00010157" />
-  <Tmin units="K"  value="11.87" />
-  <Tmax units="K"  value="150" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="112140" />
-  <B value="1253.3" />
-  <C value="-12.905" />
-  <D value="0.10424" />
-  <E value="-0.00013798" />
-  <Tmin units="K"  value="156.08" />
-  <Tmax units="K"  value="276.02" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65203" />
-  <B value="-794.87" />
-  <C value="12.953" />
-  <D value="-0.00031634" />
-  <E value="6.4426E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15207" />
-  <B value="-148.22" />
-  <C value="-10.138" />
-  <D value="-64.001" />
-  <E value="-71.395" />
-  <Tmin units="K"  value="216.6" />
-  <Tmax units="K"  value="1732.8" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="9.9961" />
-  <B value="-126.46" />
-  <C value="-3.1956" />
-  <D value="-6.7828E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="308.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000001161" />
-  <B value="0.48519" />
-  <C value="364.43" />
-  <D value="10928" />
-  <Tmin units="K"  value="156.08" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0043132" />
-  <B value="-14.875" />
-  <C value="-1.2529" />
-  <D value="-0.0019969" />
-  <E value="-0.0000017575" />
-  <Tmin units="K"  value="156.07" />
-  <Tmax units="K"  value="276.02" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00027205" />
-  <B value="0.90104" />
-  <C value="140.75" />
-  <D value="139110" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0074159" />
-  <B value="80.747" />
-  <C value="-4.002" />
-  <D value="0.0040961" />
-  <E value="-0.000015382" />
-  <Tmin units="K"  value="156.08" />
-  <Tmax units="K"  value="433.25" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="13802" />
-  <B value="231.97" />
-  <C value="0.20928" />
-  <D value="-0.00042379" />
-  <E value="1.8209E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.800705" />
-  <B value="-1250" />
-  <C value="-7.5" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.042" />
-  <B value="2412.6" />
-  <C value="-22.718" />
-  <Tmin units="K"  value="260.65" />
-  <Tmax units="K"  value="389.49" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.3856" />
-  <B value="-0.019318" />
-  <C value="0.000016915" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="308.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.24421" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.789818E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="240.589" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="73.03" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.15515" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0322" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.640181" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.20498" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0902163" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.99" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.64" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.42677" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.205" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15311.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0902163" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="35"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="31"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="35"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="34"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-50-3" />
-<Smiles name="SMILES"  value="CN(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="418" />
-<CompoundID name="Name"  value="Vinylacetylene" />
-<StructureFormula name="Structure"  value="CH2CHCCH" />
-<Family name="Family"  value="15" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="454" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4860000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.205" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="278.25" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="52.0746" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0769826" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.106852" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.552E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16360" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04001" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.66E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="3.046E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.06E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="279400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.62332" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.362E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.306" />
-  <B value="-0.0011393" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="179.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.2594" />
-  <B value="0.25931" />
-  <C value="454" />
-  <D value="0.29553" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="439.22" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="79.0442" />
-  <B value="-5001.865" />
-  <C value="-8.984128" />
-  <D value="0.0000129415" />
-  <E value="2" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="454" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.313507E+07" />
-  <B value="-0.0105563" />
-  <C value="0.71867" />
-  <D value="-0.291074" />
-  <E value="0.0215152" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="439.22" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="103140" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68382" />
-  <B value="-63.514" />
-  <C value="9.912" />
-  <D value="0.0031404" />
-  <E value="-1.0307E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="278.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="49981" />
-  <B value="-581.7" />
-  <C value="12.052" />
-  <D value="-0.00010825" />
-  <E value="3.173E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12452" />
-  <B value="-135.51" />
-  <C value="-8.7131" />
-  <D value="845.68" />
-  <E value="-2148" />
-  <Tmin units="K"  value="227" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-2.2453" />
-  <B value="320.68" />
-  <C value="-1.2895" />
-  <D value="-5.6512E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="364" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.7484E-07" />
-  <B value="0.5304" />
-  <C value="230.17" />
-  <D value="-0.0024795" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.05887" />
-  <B value="-27.718" />
-  <C value="-0.92317" />
-  <D value="-0.0023581" />
-  <E value="1.5773E-07" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="278.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000054197" />
-  <B value="1.0632" />
-  <C value="-70.589" />
-  <D value="90617" />
-  <Tmin units="K"  value="278.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.12991" />
-  <B value="-13.795" />
-  <C value="-1.4402" />
-  <D value="-0.0017832" />
-  <E value="0.0000011318" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="439.22" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="6742.516" />
-  <B value="283.8803" />
-  <C value="-0.226384" />
-  <D value="0.0000745714" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.717" />
-  <B value="2173" />
-  <C value="-42.271" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="454" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.5937" />
-  <B value="-0.024995" />
-  <C value="0.000028281" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="364" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.19966" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.439658E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="245.3258" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.281184" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="72.84" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.15143" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.028" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.688432" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.13346" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0740148" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.526" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.94" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.68289" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.11815" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17035" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0740148" />
-<UnifacVLE name="UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="66"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="5"  value="1" />
-  <group id="8"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="5"  value="1" />
-  <group id="66"  value="1" />
-  <group id="8"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="65"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="689-97-4" />
-<Smiles name="SMILES"  value="C=CC#C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1821" />
-<CompoundID name="Name"  value="Thiophene" />
-<StructureFormula name="Structure"  value="-S(CH)4-" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="580" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5660000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.219" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="357.31" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="234.94" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="234.94" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="185.638" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.142" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07947" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.186" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.781E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20120" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.8E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04354" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.05E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.1544E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.267E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="278400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5085600" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.84548" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4352E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.705" />
-  <B value="-0.010977" />
-  <Tmin units="K"  value="88.15" />
-  <Tmax units="K"  value="234.94" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.73395" />
-  <B value="0.21494" />
-  <C value="580" />
-  <D value="0.2288" />
-  <Tmin units="K"  value="234.94" />
-  <Tmax units="K"  value="579.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="88.26733" />
-  <B value="-6809.188" />
-  <C value="-9.975872" />
-  <D value="0.0000074967" />
-  <E value="2" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="579.35" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.87E+07" />
-  <B value="0.35468" />
-  <C value="0.57965" />
-  <D value="-0.92941" />
-  <E value="0.39593" />
-  <Tmin units="K"  value="234.94" />
-  <Tmax units="K"  value="579.35" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-9558700" />
-  <B value="185260" />
-  <C value="-1322.1" />
-  <D value="4.147" />
-  <E value="-0.0048149" />
-  <Tmin units="K"  value="169.71" />
-  <Tmax units="K"  value="266.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84631" />
-  <B value="-77.085" />
-  <C value="9.4174" />
-  <D value="0.0060386" />
-  <E value="-0.0000042543" />
-  <Tmin units="K"  value="234.94" />
-  <Tmax units="K"  value="357.31" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="31580" />
-  <B value="-546.03" />
-  <C value="12.548" />
-  <D value="-0.00032144" />
-  <E value="9.6227E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.14506" />
-  <B value="-254.09" />
-  <C value="-14.715" />
-  <D value="-955.11" />
-  <E value="2193.7" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.561" />
-  <B value="1306.6" />
-  <C value="0.66009" />
-  <D value="3.2071E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010722" />
-  <B value="0.54275" />
-  <C value="557.27" />
-  <D value="2874.5" />
-  <Tmin units="K"  value="234.94" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.024119" />
-  <B value="-20.319" />
-  <C value="-1.5338" />
-  <D value="-0.0014869" />
-  <E value="-6.6677E-07" />
-  <Tmin units="K"  value="234.94" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013168" />
-  <B value="0.98328" />
-  <C value="649.4" />
-  <D value="-5290.1" />
-  <Tmin units="K"  value="357.31" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0069688" />
-  <B value="140.5" />
-  <C value="-4.0531" />
-  <D value="0.0044052" />
-  <E value="-0.000011144" />
-  <Tmin units="K"  value="234.94" />
-  <Tmax units="K"  value="579.35" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="25467" />
-  <B value="12.638" />
-  <C value="0.79104" />
-  <D value="-0.0011748" />
-  <E value="5.0619E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.19455" />
-  <B value="-1400" />
-  <C value="-8.4" />
-  <Tmin units="K"  value="269.7056" />
-  <Tmax units="K"  value="439.7056" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.049" />
-  <B value="2962.4" />
-  <C value="-46.375" />
-  <Tmin units="K"  value="351.52" />
-  <Tmax units="K"  value="513.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.34111" />
-  <B value="-0.034802" />
-  <C value="0.000037492" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.22777" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.880023E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="265.0838" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.274238" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="95.74" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.64559" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0333" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.071" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.19336" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0794773" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.8569" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.14" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.5664" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.192846" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20219.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0794773" />
-<UnifacVLE name="UNIFAC" >
-  <group id="106"  value="1" />
-  </UnifacVLE>
-<GCmethod name="PPR78" >
-  <group id="106"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="106"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="110-02-1" />
-<Smiles name="SMILES"  value="S1C=CC=C1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1775" />
-<CompoundID name="Name"  value="Methacrylonitrile" />
-<StructureFormula name="Structure"  value="CH2C(CH3)CN" />
-<Family name="Family"  value="38" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="554" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3880000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.265" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.223" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="363.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="237.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="237.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="268.868" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="67.0892" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0844058" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.301271" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.172E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19090" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.23E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04532" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.78E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="9.803E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.64E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="223800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.92207" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.243E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.205" />
-  <B value="-0.0076417" />
-  <Tmin units="K"  value="94.94" />
-  <Tmax units="K"  value="237.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.89537" />
-  <B value="0.23729" />
-  <C value="554" />
-  <D value="0.29629" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="537.33" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="56.07917" />
-  <B value="-5342.951" />
-  <C value="-5.152858" />
-  <D value="4.011012E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="228.65" />
-  <Tmax units="K"  value="554" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.4103E+07" />
-  <B value="0.56334" />
-  <C value="-0.51577" />
-  <D value="0.31852" />
-  <E value="-0.072403" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="537.33" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5234" />
-  <B value="706.96" />
-  <C value="-1.4898" />
-  <D value="0.0041536" />
-  <E value="-0.000005155" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="237.35" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="125060" />
-  <B value="169.88" />
-  <C value="6.1441" />
-  <D value="0.015707" />
-  <E value="-0.000014502" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="363.45" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68640" />
-  <B value="-664.02" />
-  <C value="12.252" />
-  <D value="0.000039427" />
-  <E value="-4.9098E-08" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="1600.1" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19092" />
-  <B value="-216.75" />
-  <C value="-39.481" />
-  <D value="-32963" />
-  <E value="57710" />
-  <Tmin units="K"  value="277" />
-  <Tmax units="K"  value="1771" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-14.973" />
-  <B value="1174.5" />
-  <C value="0.57272" />
-  <D value="-0.0000017357" />
-  <E value="2" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="363.45" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.3003E-07" />
-  <B value="0.64938" />
-  <C value="329.57" />
-  <D value="-240" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.095479" />
-  <B value="1984.5" />
-  <C value="-23.334" />
-  <D value="0.076497" />
-  <E value="-0.000098215" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="513.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0010085" />
-  <B value="1.2282" />
-  <C value="49915" />
-  <D value="0.89214" />
-  <Tmin units="K"  value="363.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0074463" />
-  <B value="179.83" />
-  <C value="-4.4863" />
-  <D value="0.0047455" />
-  <E value="-0.000011145" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="537.33" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="23959" />
-  <B value="264.31" />
-  <C value="-0.1392" />
-  <D value="0.000026399" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="1600.1" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.733" />
-  <B value="3597.2" />
-  <C value="-11.461" />
-  <Tmin units="K"  value="337.34" />
-  <Tmax units="K"  value="487.34" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.5428" />
-  <B value="-0.036813" />
-  <C value="0.000040428" />
-  <Tmin units="K"  value="237.35" />
-  <Tmax units="K"  value="363.45" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.240561" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.255952E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="163.0499" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="79.69" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0333" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.804731" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.301271" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0844058" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.987475" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.712" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.301271" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19094" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0844058" />
-<CAS name="CAS number"  value="126-98-7" />
-<Smiles name="SMILES"  value="C=C(C)C#N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="404" />
-<CompoundID name="Name"  value="Dimethylacetylene" />
-<StructureFormula name="Structure"  value="CH3CCCH3" />
-<Family name="Family"  value="15" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="473.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4870000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.221" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.274" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="300.13" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="240.91" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="240.91" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6121.21" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="54.0904" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0788997" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.238542" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.519E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17480" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.32E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04344" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.2E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.457E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.849E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="283300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9234000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.843411" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4189E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="20.891" />
-  <B value="1.4333E-16" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1717" />
-  <B value="0.25895" />
-  <C value="473.2" />
-  <D value="0.27289" />
-  <Tmin units="K"  value="240.91" />
-  <Tmax units="K"  value="460.97" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="66.56107" />
-  <B value="-4998.053" />
-  <C value="-6.834282" />
-  <D value="6.682052E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="235.35" />
-  <Tmax units="K"  value="473.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4761730" />
-  <B value="-11.5565" />
-  <C value="30.6629" />
-  <D value="-31.89366" />
-  <E value="12.67797" />
-  <Tmin units="K"  value="240.91" />
-  <Tmax units="K"  value="483.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-22058" />
-  <B value="1434.2" />
-  <C value="-6.035" />
-  <D value="-0.0026008" />
-  <E value="0.00007651" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="140" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116500" />
-  <B value="35.116" />
-  <C value="5.8634" />
-  <D value="0.0049877" />
-  <E value="0.000013087" />
-  <Tmin units="K"  value="240.91" />
-  <Tmax units="K"  value="416.29" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62226" />
-  <B value="-826.04" />
-  <C value="12.513" />
-  <D value="-0.0002013" />
-  <E value="4.9424E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.1305" />
-  <B value="-139.22" />
-  <C value="-10.692" />
-  <D value="-76.88" />
-  <E value="-253.62" />
-  <Tmin units="K"  value="244" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-0.045622" />
-  <B value="305.04" />
-  <C value="-1.6582" />
-  <D value="-4.749E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="240.91" />
-  <Tmax units="K"  value="371" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000021802" />
-  <B value="0.39407" />
-  <C value="508.41" />
-  <D value="3758" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0074431" />
-  <B value="-154.13" />
-  <C value="-0.25098" />
-  <D value="-0.0046292" />
-  <E value="-7.3662E-08" />
-  <Tmin units="K"  value="240.91" />
-  <Tmax units="K"  value="428.44" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00021497" />
-  <B value="0.91998" />
-  <C value="214.54" />
-  <D value="130500" />
-  <Tmin units="K"  value="276.59" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0028208" />
-  <B value="1162.8" />
-  <C value="-14.995" />
-  <D value="0.042251" />
-  <E value="-0.000058944" />
-  <Tmin units="K"  value="240.91" />
-  <Tmax units="K"  value="488.68" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="24704" />
-  <B value="201.33" />
-  <C value="-0.063295" />
-  <D value="0.0000018433" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.304" />
-  <B value="2609.4" />
-  <C value="-33.287" />
-  <Tmin units="K"  value="286.57" />
-  <Tmax units="K"  value="424.3" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.9474" />
-  <B value="-0.021183" />
-  <C value="0.000020132" />
-  <Tmin units="K"  value="240.91" />
-  <Tmax units="K"  value="371" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.230469" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.334271E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="292.3209" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="77.46" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0302" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.695843" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.238542" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0789036" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.8635" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.48" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.109294" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1301" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17463.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0789036" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="67"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="54"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="67"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="66"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="503-17-3" />
-<Smiles name="SMILES"  value="CC#CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="403" />
-<CompoundID name="Name"  value="Ethylacetylene" />
-<StructureFormula name="Structure"  value="CH3CH2CCH" />
-<Family name="Family"  value="15" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="440" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4600000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.208" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.262" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="281.21" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="147.429" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="147.43" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.17966" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="54.092" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08322" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.245" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.616E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15950" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.7E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0435" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.19E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.652E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.0225E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="290390" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6029270" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.86034" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4647E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="19.004" />
-  <B value="-0.015369" />
-  <Tmin units="K"  value="58.97" />
-  <Tmax units="K"  value="147.43" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3447" />
-  <B value="0.27928" />
-  <C value="440" />
-  <D value="0.29778" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="440" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="76.044" />
-  <B value="-5031.59" />
-  <C value="-8.40406" />
-  <D value="9.681824E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="440" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.604722E+07" />
-  <B value="0.546439" />
-  <C value="-0.26185" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="463.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16604" />
-  <B value="1465.2" />
-  <C value="-11.028" />
-  <D value="0.042838" />
-  <E value="-0.000042808" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="140" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="109820" />
-  <B value="1148.7" />
-  <C value="-9.607" />
-  <D value="0.084548" />
-  <E value="-0.00010384" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="298.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="44709" />
-  <B value="-441.89" />
-  <C value="11.889" />
-  <D value="0.00039371" />
-  <E value="-1.2645E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.11439" />
-  <B value="-115.33" />
-  <C value="-13.916" />
-  <D value="565.16" />
-  <E value="-1644.3" />
-  <Tmin units="K"  value="231.85" />
-  <Tmax units="K"  value="1896" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-4.3451" />
-  <B value="354.46" />
-  <C value="-0.92921" />
-  <D value="-0.0000006027" />
-  <E value="2" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000027867" />
-  <B value="0.37696" />
-  <C value="663.32" />
-  <D value="30.832" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="800" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.032845" />
-  <B value="13.956" />
-  <C value="-1.5811" />
-  <D value="-0.00025138" />
-  <E value="-0.0000029965" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000036868" />
-  <B value="1.1429" />
-  <C value="-57.854" />
-  <D value="83816" />
-  <Tmin units="K"  value="281.22" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018233" />
-  <B value="58.318" />
-  <C value="-3.4452" />
-  <D value="0.0022742" />
-  <E value="-0.0000088254" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="440" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="24902" />
-  <B value="172.94" />
-  <C value="0.12971" />
-  <D value="-0.00028785" />
-  <E value="1.2671E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.172" />
-  <B value="2381.3" />
-  <C value="-34.36" />
-  <Tmin units="K"  value="264.46" />
-  <Tmax units="K"  value="393.8" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.5057" />
-  <B value="-0.026061" />
-  <C value="0.000030844" />
-  <Tmin units="K"  value="147.43" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.230791" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.516173E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="231.3399" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="77.46" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0299" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.659288" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.246864" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0809511" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.8675" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.476" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.246864" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16554" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0809511" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="66"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="53"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="66"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-00-6" />
-<Smiles name="SMILES"  value="CCC#C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="302" />
-<CompoundID name="Name"  value="1,2-butadiene" />
-<StructureFormula name="Structure"  value="CH2CCHCH3" />
-<Family name="Family"  value="14" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="452" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4360000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.22" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="284" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="136.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="136.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.4472" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="54.0904" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0838169" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.165877" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.724E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15650" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.34E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04104" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.06E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.623E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.986E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="293000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6962000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.86993" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4617E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="19.23" />
-  <B value="-0.016101" />
-  <Tmin units="K"  value="54.78" />
-  <Tmax units="K"  value="136.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.86492" />
-  <B value="0.22148" />
-  <C value="452" />
-  <D value="0.28373" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="452" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="53.27585" />
-  <B value="-4559.624" />
-  <C value="-4.46417" />
-  <D value="-6.771964E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="452" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.715905E+07" />
-  <B value="0.824251" />
-  <C value="0.000387028" />
-  <D value="-2.253417" />
-  <E value="2.024613" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="452" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12633" />
-  <B value="1064.1" />
-  <C value="-2.6638" />
-  <D value="-0.022763" />
-  <E value="0.00013729" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="135" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="109750" />
-  <B value="-2425.1" />
-  <C value="12.655" />
-  <D value="0.059068" />
-  <E value="-0.00014415" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="290" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39504.04" />
-  <B value="-354.1475" />
-  <C value="11.62099" />
-  <D value="0.00074321" />
-  <E value="-2.513775E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12404" />
-  <B value="-118.51" />
-  <C value="-9.2537" />
-  <D value="405.61" />
-  <E value="-950.52" />
-  <Tmin units="K"  value="212.5" />
-  <Tmax units="K"  value="1912.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.9134" />
-  <B value="468.65" />
-  <C value="-0.069814" />
-  <D value="2.8031E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="389.66" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.4328E-07" />
-  <B value="0.52378" />
-  <C value="170.73" />
-  <D value="9690.7" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.29344" />
-  <B value="3.1314" />
-  <C value="-0.70701" />
-  <D value="-0.00052702" />
-  <E value="-3.6665E-07" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="424.31" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000085434" />
-  <B value="1.0359" />
-  <C value="127.53" />
-  <D value="78342" />
-  <Tmin units="K"  value="272.31" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0071904" />
-  <B value="58.358" />
-  <C value="-3.6032" />
-  <D value="0.002556" />
-  <E value="-0.000013035" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="452" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="9801.858" />
-  <B value="280.0477" />
-  <C value="-0.159682" />
-  <D value="0.0000372564" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.862" />
-  <B value="2320" />
-  <C value="-35.494" />
-  <Tmin units="K"  value="273.29" />
-  <Tmax units="K"  value="402.26" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.9521" />
-  <B value="-0.026624" />
-  <C value="0.000034949" />
-  <Tmin units="K"  value="136.95" />
-  <Tmax units="K"  value="389.66" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.21829" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.805919E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="215.5739" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="77.46" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.09464" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0295" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.6507" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2492" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0816506" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.466" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.024" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.90162" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3394" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16360.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0816506" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="4"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="4"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="4"  value="1" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="4"  value="1" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="4"  value="1" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="590-19-2" />
-<Smiles name="SMILES"  value="C=C=CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="303" />
-<CompoundID name="Name"  value="1,3-butadiene" />
-<StructureFormula name="Structure"  value="CH2CHCHCH2" />
-<Family name="Family"  value="14" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="425" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4320000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.221" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.27" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="268.62" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="164.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="164.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="69.1989" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="54.092" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08804" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.195" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.602E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14460" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04082" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.88E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.0924E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.4972E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="278890" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7984000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.78024" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.409E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.877" />
-  <B value="-5.0524E-16" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3314" />
-  <B value="0.28213" />
-  <C value="425" />
-  <D value="0.30137" />
-  <Tmin units="K"  value="164.2" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="64.81816" />
-  <B value="-4314.788" />
-  <C value="-6.766483" />
-  <D value="8.589719E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="164" />
-  <Tmax units="K"  value="425.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.4211E+07" />
-  <B value="0.45981" />
-  <C value="0.016247" />
-  <D value="-0.15407" />
-  <E value="0.054476" />
-  <Tmin units="K"  value="164.25" />
-  <Tmax units="K"  value="413.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-6476.2" />
-  <B value="813.54" />
-  <C value="1.359" />
-  <D value="-0.057544" />
-  <E value="0.00024886" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="164.24" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="88166" />
-  <B value="583.44" />
-  <C value="1.8231" />
-  <D value="0.030118" />
-  <E value="-0.000025695" />
-  <Tmin units="K"  value="164.24" />
-  <Tmax units="K"  value="350" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="38238.49" />
-  <B value="-511.235" />
-  <C value="12.39338" />
-  <D value="-0.000121482" />
-  <E value="4.39211E-08" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12533" />
-  <B value="-119.09" />
-  <C value="-9.668" />
-  <D value="379.91" />
-  <E value="-922.02" />
-  <Tmin units="K"  value="169" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="12.653" />
-  <B value="-139.12" />
-  <C value="-3.6735" />
-  <D value="-0.0000014093" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.4426E-07" />
-  <B value="0.6407" />
-  <C value="174.17" />
-  <D value="-2393.4" />
-  <Tmin units="K"  value="164.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.096853" />
-  <B value="19.016" />
-  <C value="-1.4201" />
-  <D value="0.00020099" />
-  <E value="-0.0000029536" />
-  <Tmin units="K"  value="164.25" />
-  <Tmax units="K"  value="386.43" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-18588" />
-  <B value="0.94195" />
-  <C value="-7.31E+10" />
-  <D value="-9.6975E+11" />
-  <Tmin units="K"  value="268.74" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.017149" />
-  <B value="-4.9201" />
-  <C value="-2.6201" />
-  <D value="-0.0017212" />
-  <E value="-0.0000040904" />
-  <Tmin units="K"  value="164.25" />
-  <Tmax units="K"  value="411.28" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="29990" />
-  <B value="42.279" />
-  <C value="0.68619" />
-  <D value="-0.0010286" />
-  <E value="4.4241E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.853" />
-  <B value="2221.4" />
-  <C value="-30.643" />
-  <Tmin units="K"  value="255.37" />
-  <Tmax units="K"  value="381" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.2847" />
-  <B value="-0.019089" />
-  <C value="0.000012468" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2202" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.429242E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="249.0071" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2713" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="77.46" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.03369" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0297" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.619744" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.19336" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0830243" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.6908" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.352" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.009137" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.29204" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2028" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14195.77" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.088" />
-<UnifacVLE name="UNIFAC" >
-  <group id="5"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="5"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="5"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="5"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="5"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-99-0" />
-<Smiles name="SMILES"  value="C=CC=C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="204" />
-<CompoundID name="Name"  value="1-butene" />
-<StructureFormula name="Structure"  value="CH2CHCH2CH3" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="419.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4020000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2408" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.278" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="266.92" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="87.8" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="87.8" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000000694" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="56.108" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09534" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.194" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.762E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13630" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.13E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04431" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.41E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-500000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.041E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="307400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3848000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.76818" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.5408E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="18.071" />
-  <B value="-0.022407" />
-  <Tmin units="K"  value="35.12" />
-  <Tmax units="K"  value="87.8" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.98" />
-  <B value="0.25169" />
-  <C value="419.54" />
-  <D value="0.26645" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="419.53" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="41.66588" />
-  <B value="-3605.004" />
-  <C value="-2.983562" />
-  <D value="6.665773E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="419.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.5338E+07" />
-  <B value="0.68186" />
-  <C value="-0.28099" />
-  <D value="-0.25369" />
-  <E value="0.26017" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="419.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="1585.7" />
-  <B value="-577.54" />
-  <C value="64.19" />
-  <D value="-1.0389" />
-  <E value="0.0053848" />
-  <Tmin units="K"  value="6" />
-  <Tmax units="K"  value="87.82" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="100270" />
-  <B value="86.345" />
-  <C value="7.7333" />
-  <D value="0.00096546" />
-  <E value="0.000020281" />
-  <Tmin units="K"  value="81.29" />
-  <Tmax units="K"  value="380" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="53529" />
-  <B value="-619.26" />
-  <C value="12.431" />
-  <D value="0.000096632" />
-  <E value="-3.9013E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15917" />
-  <B value="-163.92" />
-  <C value="-3.9976" />
-  <D value="-1573.8" />
-  <E value="2763.7" />
-  <Tmin units="K"  value="209.75" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.764" />
-  <B value="591.51" />
-  <C value="-0.0017307" />
-  <D value="2.5723E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="335.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.0347E-07" />
-  <B value="0.54535" />
-  <C value="308.83" />
-  <D value="-232.73" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.071267" />
-  <B value="99.471" />
-  <C value="-4.2011" />
-  <D value="0.014325" />
-  <E value="-0.000041157" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="363.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000092115" />
-  <B value="1.1181" />
-  <C value="717.19" />
-  <D value="13037" />
-  <Tmin units="K"  value="266.91" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011829" />
-  <B value="10.929" />
-  <C value="-2.9412" />
-  <D value="-0.00056522" />
-  <E value="-0.0000074409" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="419.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="36492" />
-  <B value="66.383" />
-  <C value="0.51076" />
-  <D value="-0.00068154" />
-  <E value="2.6315E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.09" />
-  <B value="2368.5" />
-  <C value="-19.25" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="373.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.33753" />
-  <B value="-0.055494" />
-  <C value="0.000090567" />
-  <Tmin units="K"  value="87.8" />
-  <Tmax units="K"  value="335.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2377" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.394403E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="273.0275" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2736" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="82.08" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.24598" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0321" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.593789" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1921" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0896329" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.92" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.56" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.001178" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.98463" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2085" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13827.58" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0953" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-98-9" />
-<Smiles name="SMILES"  value="C=CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="205" />
-<CompoundID name="Name"  value="Cis-2-butene" />
-<StructureFormula name="Structure"  value="CH3CHCHCH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="435.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4210000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2338" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="276.87" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="134.26" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="134.26" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.272" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="56.108" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09101" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.203" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.833E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14720" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04428" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.4E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7400000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.536E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="301200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7309400" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.79077" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.5339E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.618" />
-  <B value="-0.014457" />
-  <Tmin units="K"  value="53.7" />
-  <Tmax units="K"  value="134.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1591" />
-  <B value="0.27085" />
-  <C value="435.5" />
-  <D value="0.28116" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="435.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.92441" />
-  <B value="-5022.628" />
-  <C value="-9.652369" />
-  <D value="0.0000133961" />
-  <E value="2" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="435.58" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.4358E+07" />
-  <B value="0.38004" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="435.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11156" />
-  <B value="837.19" />
-  <C value="4.9352" />
-  <D value="-0.095117" />
-  <E value="0.00037586" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="134.26" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="79532" />
-  <B value="110.96" />
-  <C value="9.7654" />
-  <D value="-0.0036798" />
-  <E value="0.000019578" />
-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="366.48" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="53149" />
-  <B value="-719.47" />
-  <C value="12.619" />
-  <D value="-0.000047815" />
-  <E value="4.5198E-10" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.13022" />
-  <B value="-102.71" />
-  <C value="-12.899" />
-  <D value="-102.28" />
-  <E value="-123.99" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="1959.98" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-17.96838" />
-  <B value="892.0637" />
-  <C value="1.159883" />
-  <D value="-2.883463E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="333.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.0697E-08" />
-  <B value="0.91942" />
-  <C value="-12.143" />
-  <D value="1343.2" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.032373" />
-  <B value="19.125" />
-  <C value="-1.716" />
-  <D value="0.00030408" />
-  <E value="-0.0000042934" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000075196" />
-  <B value="1.0578" />
-  <C value="-53.701" />
-  <D value="131760" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1273.15" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010924" />
-  <B value="29.613" />
-  <C value="-3.1507" />
-  <D value="0.00043968" />
-  <E value="-0.0000087176" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="435.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="30672" />
-  <B value="159.5" />
-  <C value="0.18541" />
-  <D value="-0.00028485" />
-  <E value="1.0443E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.051" />
-  <B value="2387.1" />
-  <C value="-26.243" />
-  <Tmin units="K"  value="263.27" />
-  <Tmax units="K"  value="387.94" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.8527" />
-  <B value="-0.034875" />
-  <C value="0.000051621" />
-  <Tmin units="K"  value="134.26" />
-  <Tmax units="K"  value="333.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.23104" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.556787E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="251.7732" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2705" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="82.08" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.05879" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0315" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.625953" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.20385" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0874127" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.9189" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.563" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005287" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.28413" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2575" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13827.58" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0912" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="590-18-1" />
-<Smiles name="SMILES"  value="C/C=C\C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="206" />
-<CompoundID name="Name"  value="Trans-2-butene" />
-<StructureFormula name="Structure"  value="CH3CHCHCH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="428.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4100000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2377" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.276" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="274.03" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="167.62" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="167.62" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="74.5" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="56.108" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09365" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.218" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.734E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14210" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04428" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.4E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.1E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.32E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="296500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9757500" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.80878" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.53E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.597" />
-  <B value="-0.011008" />
-  <Tmin units="K"  value="67.05" />
-  <Tmax units="K"  value="167.62" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1523" />
-  <B value="0.27235" />
-  <C value="428.6" />
-  <D value="0.28543" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="428.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="56.602" />
-  <B value="-4026.7" />
-  <C value="-5.5178" />
-  <D value="0.0000079176" />
-  <E value="2" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="428.63" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.3476E+07" />
-  <B value="0.31355" />
-  <C value="0.41478" />
-  <D value="-0.75555" />
-  <E value="0.40695" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="428.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11577" />
-  <B value="924.59" />
-  <C value="-0.075824" />
-  <D value="-0.037583" />
-  <E value="0.00018647" />
-  <Tmin units="K"  value="14.56" />
-  <Tmax units="K"  value="167.62" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="98730" />
-  <B value="549.96" />
-  <C value="0.83133" />
-  <D value="0.038607" />
-  <E value="-0.000044392" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="280" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="60006" />
-  <B value="-649.72" />
-  <C value="12.368" />
-  <D value="0.00014661" />
-  <E value="-5.1566E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.13647" />
-  <B value="-137.68" />
-  <C value="-9.943" />
-  <D value="-263.89" />
-  <E value="304.81" />
-  <Tmin units="K"  value="214.3" />
-  <Tmax units="K"  value="1928.75" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-16.05639" />
-  <B value="833.2986" />
-  <C value="0.849646" />
-  <D value="-2.292227E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="333.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010493" />
-  <B value="0.48674" />
-  <C value="358.01" />
-  <D value="137.53" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.060004" />
-  <B value="368.81" />
-  <C value="-7.3737" />
-  <D value="0.025078" />
-  <E value="-0.000049526" />
-  <Tmin units="K"  value="167.6" />
-  <Tmax units="K"  value="392.74" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000078563" />
-  <B value="1.0565" />
-  <C value="14.753" />
-  <D value="105810" />
-  <Tmin units="K"  value="274.03" />
-  <Tmax units="K"  value="1257" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0071116" />
-  <B value="84.381" />
-  <C value="-4.1149" />
-  <D value="0.0047521" />
-  <E value="-0.000016755" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="428.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="46428" />
-  <B value="-40.658" />
-  <C value="0.75936" />
-  <D value="-0.00091251" />
-  <E value="3.3965E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.171" />
-  <B value="2448.5" />
-  <C value="-20.174" />
-  <Tmin units="K"  value="258.29" />
-  <Tmax units="K"  value="383.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.7304" />
-  <B value="-0.027775" />
-  <C value="0.000037636" />
-  <Tmin units="K"  value="167.62" />
-  <Tmax units="K"  value="333.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.23668" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.417894E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="271.7928" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2721" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="82.08" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.18256" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0318" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.608684" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.21525" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0893483" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.9189" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.563" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.016832" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.8876" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2138" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14207.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0893483" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="624-64-6" />
-<Smiles name="SMILES"  value="C/C=C/C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="207" />
-<CompoundID name="Name"  value="Isobutene" />
-<StructureFormula name="Structure"  value="CH2C(CH3)2" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="417.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2388" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="266.24" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="132.81" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="132.81" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.644929" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="56.108" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09524" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.875E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13660" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.67E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04429" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.71E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.71E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.808E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="293090" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5931200" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.60897" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.5242E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.138" />
-  <B value="-0.014341" />
-  <Tmin units="K"  value="53.12" />
-  <Tmax units="K"  value="132.81" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.01" />
-  <B value="0.25611" />
-  <C value="417.9" />
-  <D value="0.2642" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="417.9" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="47.13879" />
-  <B value="-3682.162" />
-  <C value="-3.952514" />
-  <D value="4.044185E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="417.9" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.916E+07" />
-  <B value="1.1638" />
-  <C value="-1.4033" />
-  <D value="0.81203" />
-  <E value="-0.13521" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="417.9" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34336" />
-  <B value="57.654" />
-  <C value="2.3469" />
-  <D value="-0.0024921" />
-  <E value="0.0000076414" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="130" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="95317" />
-  <B value="-68.58" />
-  <C value="9.3268" />
-  <D value="0.0023434" />
-  <E value="0.0000076824" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="343.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="49784" />
-  <B value="-472.84" />
-  <C value="12.012" />
-  <D value="0.00052863" />
-  <E value="-1.7772E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.14292" />
-  <B value="-112.61" />
-  <C value="-10.11" />
-  <D value="-321.37" />
-  <E value="359.29" />
-  <Tmin units="K"  value="194" />
-  <Tmax units="K"  value="1880.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.717" />
-  <B value="644.93" />
-  <C value="0.3696" />
-  <D value="-0.0000023983" />
-  <E value="2" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="343.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000028839" />
-  <B value="0.33897" />
-  <C value="365.04" />
-  <D value="17752" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.061493" />
-  <B value="33.335" />
-  <C value="-2.4686" />
-  <D value="0.0041425" />
-  <E value="-0.000023609" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="395.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-418.21" />
-  <B value="0.91306" />
-  <C value="-1.5105E+09" />
-  <D value="3.1789E+10" />
-  <Tmin units="K"  value="266.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0085717" />
-  <B value="38.109" />
-  <C value="-3.4301" />
-  <D value="0.0015866" />
-  <E value="-0.000012058" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="417.9" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="26864" />
-  <B value="174.18" />
-  <C value="0.19231" />
-  <D value="-0.00032834" />
-  <E value="0.0000001302" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.012" />
-  <B value="2312" />
-  <C value="-22.509" />
-  <Tmin units="K"  value="250.95" />
-  <Tmax units="K"  value="373.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.049" />
-  <B value="-0.038545" />
-  <C value="0.000054221" />
-  <Tmin units="K"  value="132.81" />
-  <Tmax units="K"  value="343.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2369" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.449925E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="261.5672" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2727" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="82.08" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="1.044" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0318" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.592793" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.19584" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0953727" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.9195" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.684" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.684" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.000612" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-2.20386" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1951" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13659.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0953727" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="7"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="8"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="7"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="7"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="7"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="115-11-7" />
-<Smiles name="SMILES"  value="C=C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1006" />
-<CompoundID name="Name"  value="2-methylpropanal" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="507" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4100000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.263" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="337.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="208.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="208.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="34.8247" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.1057" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0920264" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.36218" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.176E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18450" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04927" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.19E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.158E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.214E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="331200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.2E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0845" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.2913E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.457" />
-  <B value="-0.0083248" />
-  <Tmin units="K"  value="83.26" />
-  <Tmax units="K"  value="208.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.97266" />
-  <B value="0.25698" />
-  <C value="507" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="507" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="102.1731" />
-  <B value="-7116.016" />
-  <C value="-12.16592" />
-  <D value="0.0000111612" />
-  <E value="2" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="507" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.95108E+07" />
-  <B value="0.263532" />
-  <C value="1.209662" />
-  <D value="-2.271572" />
-  <E value="1.223299" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="507" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="117460" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="143330" />
-  <B value="110.87" />
-  <C value="5.2999" />
-  <D value="0.018869" />
-  <E value="-0.000016131" />
-  <Tmin units="K"  value="214.6" />
-  <Tmax units="K"  value="380.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68500" />
-  <B value="-741.45" />
-  <C value="12.977" />
-  <D value="-0.00061649" />
-  <E value="3.0243E-07" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="1200.1" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17413" />
-  <B value="-177.39" />
-  <C value="-23.578" />
-  <D value="-1169.2" />
-  <E value="-870.73" />
-  <Tmin units="K"  value="253.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.535" />
-  <B value="970.52" />
-  <C value="-0.049339" />
-  <D value="1.1673E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="337.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9586E-07" />
-  <B value="0.71384" />
-  <C value="159.71" />
-  <D value="-212.67" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10024" />
-  <B value="-223.61" />
-  <C value="-0.25771" />
-  <D value="-0.00474" />
-  <E value="-0.000011884" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="337.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-2151.4" />
-  <B value="-0.21039" />
-  <C value="974960" />
-  <D value="-5.0943E+09" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0080335" />
-  <B value="138.78" />
-  <C value="-4.3351" />
-  <D value="0.0046959" />
-  <E value="-0.000012308" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="507" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-1651.2" />
-  <B value="409.22" />
-  <C value="-0.26544" />
-  <D value="0.000076956" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="1200.1" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.001" />
-  <B value="3260.1" />
-  <C value="-26.391" />
-  <Tmin units="K"  value="309.26" />
-  <Tmax units="K"  value="444.08" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.27451" />
-  <B value="-0.041473" />
-  <C value="0.000050862" />
-  <Tmin units="K"  value="208.15" />
-  <Tmax units="K"  value="337.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.261872" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.133037E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="245.2365" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="88.19" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.0423" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0348" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.79414" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.37009" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0920137" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.2471" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.872" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.9594" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.37009" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18234.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0920137" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="21"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="21"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="20"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="21"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="20"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="78-84-2" />
-<Smiles name="SMILES"  value="CC(C)C=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1052" />
-<CompoundID name="Name"  value="Methyl ethyl ketone" />
-<StructureFormula name="Structure"  value="CH3COCH2CH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="536.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4210000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.267" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="352.71" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="186.48" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="186.48" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.3904" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.107" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09013" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.322" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.135E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18880" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.21E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04927" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.19E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.39E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.47E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="339400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8385000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0746" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.268E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.07" />
-  <B value="-0.0096025" />
-  <Tmin units="K"  value="74.59" />
-  <Tmax units="K"  value="186.48" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.16518" />
-  <B value="0.10716" />
-  <C value="536.8" />
-  <D value="0.15066" />
-  <Tmin units="K"  value="186.48" />
-  <Tmax units="K"  value="535.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="84.00012" />
-  <B value="-6498.964" />
-  <C value="-9.389584" />
-  <D value="8.32043E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="186.48" />
-  <Tmax units="K"  value="535.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.7221E+07" />
-  <B value="0.30759" />
-  <C value="0.48591" />
-  <D value="-0.8645" />
-  <E value="0.45018" />
-  <Tmin units="K"  value="186.48" />
-  <Tmax units="K"  value="535.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-17129" />
-  <B value="1720.2" />
-  <C value="-12.568" />
-  <D value="0.048242" />
-  <E value="-0.000060858" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="186.51" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="137210" />
-  <B value="245.98" />
-  <C value="6.3249" />
-  <D value="0.009404" />
-  <E value="3.3143E-07" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="69404" />
-  <B value="-545.04" />
-  <C value="12.139" />
-  <D value="0.00045578" />
-  <E value="-1.6351E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.072002" />
-  <B value="-61.582" />
-  <C value="-63.847" />
-  <D value="32101" />
-  <E value="-95322" />
-  <Tmin units="K"  value="277.75" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-0.60519" />
-  <B value="503.02" />
-  <C value="-1.5659" />
-  <D value="5.5782E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="186.48" />
-  <Tmax units="K"  value="535.5" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.8817E-08" />
-  <B value="0.96765" />
-  <C value="-28.58" />
-  <D value="7703" />
-  <Tmin units="K"  value="186.48" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.17871" />
-  <B value="4.3086" />
-  <C value="-1.0343" />
-  <D value="0.00010801" />
-  <E value="-0.0000015411" />
-  <Tmin units="K"  value="184.45" />
-  <Tmax units="K"  value="422.04" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-4970700" />
-  <B value="-0.23106" />
-  <C value="2.2577E+09" />
-  <D value="-1.0834E+13" />
-  <Tmin units="K"  value="199.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.022005" />
-  <B value="17.777" />
-  <C value="-2.7497" />
-  <D value="-0.00035582" />
-  <E value="-0.0000031774" />
-  <Tmin units="K"  value="186.48" />
-  <Tmax units="K"  value="535.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="52789" />
-  <B value="91.975" />
-  <C value="0.40334" />
-  <D value="-0.00053911" />
-  <E value="2.0528E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-9.711039" />
-  <B value="-13984.86" />
-  <C value="-7.272391" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="536" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.449" />
-  <B value="3070.5" />
-  <C value="-43.309" />
-  <Tmin units="K"  value="325.82" />
-  <Tmax units="K"  value="480.39" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.4713" />
-  <B value="-0.024147" />
-  <C value="0.000020964" />
-  <Tmin units="K"  value="186.48" />
-  <Tmax units="K"  value="535.5" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.261872" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.281568E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="245.3396" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="88.19" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.77001" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.036" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.80904" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3241" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0901936" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.25" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.88" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.095" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3241" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18878.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0901936" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="78-93-3" />
-<Smiles name="SMILES"  value="CC(=O)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1479" />
-<CompoundID name="Name"  value="Tetrahydrofuran" />
-<StructureFormula name="Structure"  value="-CH2CH2CH2CH2O-" />
-<Family name="Family"  value="63" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="540.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5190000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.224" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="339.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="164.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="164.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.195542" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.107" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08171" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.225" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.694E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18970" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.44E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04348" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.43E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.8418E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-7.969E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="297290" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8540000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.89818" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.325E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.756" />
-  <B value="-0.011931" />
-  <Tmin units="K"  value="65.86" />
-  <Tmax units="K"  value="164.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.054" />
-  <B value="0.25754" />
-  <C value="540.2" />
-  <D value="0.26776" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="540.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.74347" />
-  <B value="-6236.553" />
-  <C value="-9.221137" />
-  <D value="0.0000078089" />
-  <E value="2" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="540.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.770629E+07" />
-  <B value="0.8303" />
-  <C value="-0.617577" />
-  <D value="-0.253996" />
-  <E value="0.501899" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="540.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-21080" />
-  <B value="1625.4" />
-  <C value="-13.019" />
-  <D value="0.054426" />
-  <E value="-0.00007435" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="164.76" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83351" />
-  <B value="774.14" />
-  <C value="0.38273" />
-  <D value="0.036255" />
-  <E value="-0.00003559" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="339.12" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="41616" />
-  <B value="-744.85" />
-  <C value="13.048" />
-  <D value="-0.00029616" />
-  <E value="7.4486E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.13601" />
-  <B value="-158.27" />
-  <C value="-17.134" />
-  <D value="-685.86" />
-  <E value="573.36" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="1890.7" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.047" />
-  <B value="896.61" />
-  <C value="-0.11864" />
-  <D value="2.5625E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.3286E-07" />
-  <B value="0.67758" />
-  <C value="342.35" />
-  <D value="-15667" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.22085" />
-  <B value="9.5971" />
-  <C value="-0.99496" />
-  <D value="-0.00017415" />
-  <E value="-6.4958E-07" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="433.56" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000010439" />
-  <B value="1.4482" />
-  <C value="729.36" />
-  <D value="-9829.3" />
-  <Tmin units="K"  value="273.57" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.036886" />
-  <B value="4.45" />
-  <C value="-2.3412" />
-  <D value="-0.00098178" />
-  <E value="-0.0000015349" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="540.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="42994" />
-  <B value="-161.83" />
-  <C value="1.3686" />
-  <D value="-0.0016978" />
-  <E value="6.6516E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-6.376" />
-  <B value="-3760" />
-  <C value="-22.56" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.254" />
-  <B value="2946.8" />
-  <C value="-36.192" />
-  <Tmin units="K"  value="328.14" />
-  <Tmax units="K"  value="483.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.1285" />
-  <B value="-0.041831" />
-  <C value="0.000052" />
-  <Tmin units="K"  value="164.65" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.23149" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.732815E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="272.4877" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="88.19" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.66911" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0332" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.889" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.22269" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0819417" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.94" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.4" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.4245" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.225" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19042.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0819417" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="3" />
-  <group id="28"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="3" />
-  <group id="30"  value="1" />
-  </UnifacLLE>
-<Umr name="UMR" >
-  <group id="2"  value="3" />
-  <group id="28"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="27"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-99-9" />
-<Smiles name="SMILES"  value="C1COCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1421" />
-<CompoundID name="Name"  value="1,4-dioxane" />
-<StructureFormula name="Structure"  value="-OCH2CH2OCH2CH2-" />
-<Family name="Family"  value="63" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="587" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5170000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.238" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="374.5" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="284.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="284.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2532.46" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.106" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08529" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.279262" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.017E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20540" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04662" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.9E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.158E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.816E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="300120" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.284E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.85142" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.1863E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.349" />
-  <B value="1.6331E-16" />
-  <Tmin units="K"  value="284.15" />
-  <Tmax units="K"  value="293.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0039" />
-  <B value="0.25926" />
-  <C value="587" />
-  <D value="0.28278" />
-  <Tmin units="K"  value="273.83" />
-  <Tmax units="K"  value="587" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="50.11504" />
-  <B value="-5577.21" />
-  <C value="-4.046854" />
-  <D value="2.080567E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="284.95" />
-  <Tmax units="K"  value="587" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.1367E+08" />
-  <B value="9.1812" />
-  <C value="-22.992" />
-  <D value="23.854" />
-  <E value="-9.34" />
-  <Tmin units="K"  value="274.17" />
-  <Tmax units="K"  value="587.56" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="59198" />
-  <B value="-738.71" />
-  <C value="10.567" />
-  <D value="-0.045677" />
-  <E value="0.000073474" />
-  <Tmin units="K"  value="70" />
-  <Tmax units="K"  value="272.9" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="151550" />
-  <B value="-65314" />
-  <C value="519.35" />
-  <D value="-1.3402" />
-  <E value="0.0011989" />
-  <Tmin units="K"  value="284.93" />
-  <Tmax units="K"  value="374.47" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="46250" />
-  <B value="-613.41" />
-  <C value="12.822" />
-  <D value="0.000004782" />
-  <E value="-2.2238E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15508" />
-  <B value="-121.34" />
-  <C value="-57.373" />
-  <D value="-20817" />
-  <E value="36332" />
-  <Tmin units="K"  value="293.5" />
-  <Tmax units="K"  value="1877.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-79.28" />
-  <B value="4198.4" />
-  <C value="10.393" />
-  <D value="-0.0000085568" />
-  <E value="2" />
-  <Tmin units="K"  value="284.95" />
-  <Tmax units="K"  value="374.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.7334E-07" />
-  <B value="0.7393" />
-  <C value="129.93" />
-  <D value="-0.0004206" />
-  <Tmin units="K"  value="284.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.089834" />
-  <B value="46.421" />
-  <C value="-1.1898" />
-  <D value="-0.0037338" />
-  <E value="-0.0000061358" />
-  <Tmin units="K"  value="284.95" />
-  <Tmax units="K"  value="374.47" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="2.3873E-07" />
-  <B value="1.8505" />
-  <C value="-94.575" />
-  <D value="7804.2" />
-  <Tmin units="K"  value="276.15" />
-  <Tmax units="K"  value="768.01" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01539" />
-  <B value="-237.84" />
-  <C value="-0.68129" />
-  <D value="-0.0050984" />
-  <E value="-3.5247E-07" />
-  <Tmin units="K"  value="274.86" />
-  <Tmax units="K"  value="587" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="31013" />
-  <B value="15.39" />
-  <C value="0.97953" />
-  <D value="-0.0012972" />
-  <E value="5.1358E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.572938" />
-  <B value="-1100" />
-  <C value="-6.6" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.067" />
-  <B value="2959.2" />
-  <C value="-64.038" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="527.59" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="3.8781" />
-  <B value="-0.054192" />
-  <C value="0.000062327" />
-  <Tmin units="K"  value="284.95" />
-  <Tmax units="K"  value="374.65" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.25238" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.96013E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="279.96" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="94.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.48017" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0363" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.03891" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2779" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0856635" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.07" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.28" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.216" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.280373" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20163.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0856635" />
-<Umr name="UMR" >
-  <group id="2"  value="2" />
-  <group id="26"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="25"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="123-91-1" />
-<Smiles name="SMILES"  value="C1OCCOC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1256" />
-<CompoundID name="Name"  value="N-butyric acid" />
-<StructureFormula name="Structure"  value="CH3CH2CH2COOH" />
-<Family name="Family"  value="50" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="624" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4030000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.292" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.227" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="436.87" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="267.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="267.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="10.3" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.106" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09246" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.72" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.61E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20180" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05365" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.88E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.758E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.6E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="360100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.159E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.34915" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.008E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.238" />
-  <B value="-0.0069956" />
-  <Tmin units="K"  value="90.15" />
-  <Tmax units="K"  value="267.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.702" />
-  <B value="0.22902" />
-  <C value="628.16" />
-  <D value="0.24275" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="628.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="54.31047" />
-  <B value="-7692.649" />
-  <C value="-4.148708" />
-  <D value="2.624319E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="625.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.1387E+07" />
-  <B value="1.1517" />
-  <C value="-2.7656" />
-  <D value="2.6617" />
-  <E value="-0.66983" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="615.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-1354100" />
-  <B value="26070" />
-  <C value="-174.59" />
-  <D value="0.51718" />
-  <E value="-0.00056018" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="298.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="135560" />
-  <B value="664.7" />
-  <C value="1.9592" />
-  <D value="0.027685" />
-  <E value="-0.000020111" />
-  <Tmin units="K"  value="267.89" />
-  <Tmax units="K"  value="436.42" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="75565" />
-  <B value="-613.25" />
-  <C value="12.671" />
-  <D value="-0.000058773" />
-  <E value="-2.4845E-08" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="14.241" />
-  <B value="534.99" />
-  <C value="-4.0411" />
-  <D value="0.0000053437" />
-  <E value="2" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="436.42" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.2745E-08" />
-  <B value="1.0055" />
-  <C value="13.097" />
-  <D value="182.58" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.043955" />
-  <B value="57.698" />
-  <C value="-1.8847" />
-  <D value="0.00050649" />
-  <E value="-0.0000013441" />
-  <Tmin units="K"  value="259.29" />
-  <Tmax units="K"  value="573.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00010747" />
-  <B value="1.3444" />
-  <C value="19634" />
-  <D value="-7296600" />
-  <Tmin units="K"  value="436.42" />
-  <Tmax units="K"  value="706.95" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0076127" />
-  <B value="373.93" />
-  <C value="-6.0915" />
-  <D value="0.0084349" />
-  <E value="-0.000011979" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="615.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="9096.2" />
-  <B value="429.44" />
-  <C value="-0.26202" />
-  <D value="0.000057916" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.149" />
-  <B value="3703.9" />
-  <C value="-87.868" />
-  <Tmin units="K"  value="374.82" />
-  <Tmax units="K"  value="560.79" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.4201" />
-  <B value="-0.037098" />
-  <C value="0.000035218" />
-  <Tmin units="K"  value="267.95" />
-  <Tmax units="K"  value="436.42" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.285694" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.336263E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="195.7901" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="94.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0372" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.95962" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.683" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0924567" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5512" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.152" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.683" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20262.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0924567" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-92-6" />
-<Smiles name="SMILES"  value="CCCC(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1313" />
-<CompoundID name="Name"  value="Ethyl acetate" />
-<StructureFormula name="Structure"  value="CH3COOC2H5" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="523.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3830000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.286" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="350.21" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="189.6" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="189.6" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.43179" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.106" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09855" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.361" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.468E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18350" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.94E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05277" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.79E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.445E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.28E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="359700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.048E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0408" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.061E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.57" />
-  <B value="-0.0085904" />
-  <Tmin units="K"  value="75.84" />
-  <Tmax units="K"  value="189.6" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.78926" />
-  <B value="0.24295" />
-  <C value="523.26" />
-  <D value="0.25762" />
-  <Tmin units="K"  value="189.6" />
-  <Tmax units="K"  value="523.25" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="93.16862" />
-  <B value="-7073.291" />
-  <C value="-10.65983" />
-  <D value="8.16528E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="189.6" />
-  <Tmax units="K"  value="523.3" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.9527E+07" />
-  <B value="0.37029" />
-  <C value="0.072685" />
-  <D value="-0.077493" />
-  <E value="0.017381" />
-  <Tmin units="K"  value="189.6" />
-  <Tmax units="K"  value="505.74" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-45470" />
-  <B value="2386.6" />
-  <C value="-15.442" />
-  <D value="0.037388" />
-  <E value="0.000010613" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="189.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="129430" />
-  <B value="961.92" />
-  <C value="-0.12694" />
-  <D value="0.034745" />
-  <E value="-0.000031346" />
-  <Tmin units="K"  value="189.3" />
-  <Tmax units="K"  value="391.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97183" />
-  <B value="-1121.4" />
-  <C value="13.827" />
-  <D value="-0.0012343" />
-  <E value="3.6158E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16068" />
-  <B value="-181.45" />
-  <C value="-31.475" />
-  <D value="-5830.1" />
-  <E value="6599.7" />
-  <Tmin units="K"  value="261.6" />
-  <Tmax units="K"  value="1831.2" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="16.428" />
-  <B value="-219.29" />
-  <C value="-4.124" />
-  <D value="6.0568E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000034514" />
-  <B value="0.35236" />
-  <C value="732.29" />
-  <D value="-3982.4" />
-  <Tmin units="K"  value="189.6" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.040771" />
-  <B value="-127.25" />
-  <C value="-0.26995" />
-  <D value="-0.0055753" />
-  <E value="9.9363E-07" />
-  <Tmin units="K"  value="189.6" />
-  <Tmax units="K"  value="350.21" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="2.3264E-07" />
-  <B value="1.902" />
-  <C value="102.58" />
-  <D value="-17015" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="990.21" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.025331" />
-  <B value="12.715" />
-  <C value="-2.6443" />
-  <D value="-0.0005937" />
-  <E value="-0.0000027669" />
-  <Tmin units="K"  value="189.6" />
-  <Tmax units="K"  value="505.74" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="85040" />
-  <B value="-124.28" />
-  <C value="1.0836" />
-  <D value="-0.0013084" />
-  <E value="4.9879E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.708549" />
-  <B value="-3000" />
-  <C value="-18" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.18" />
-  <B value="2832.5" />
-  <C value="-56.935" />
-  <Tmin units="K"  value="314.55" />
-  <Tmax units="K"  value="470.61" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.3439" />
-  <B value="-0.018487" />
-  <C value="0.000012476" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.28529" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.24E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="499" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="94.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.17686" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0387" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.904856" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.35949" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0985939" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.48" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.12" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.49506" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.362" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18345.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0985939" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="23"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="26"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="23"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="22"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="141-78-6" />
-<Smiles name="SMILES"  value="CC(=O)OCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1322" />
-<CompoundID name="Name"  value="Methyl propionate" />
-<StructureFormula name="Structure"  value="CH3CH2COOCH3" />
-<Family name="Family"  value="57" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="530.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.282" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="352.6" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="185.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="185.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.634091" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.106" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09693" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.349" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.49E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18630" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.681E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05277" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.79E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.275E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.11E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="359600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.01E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.019" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.078E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.807" />
-  <B value="-0.008787" />
-  <Tmin units="K"  value="74.26" />
-  <Tmax units="K"  value="185.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.72945" />
-  <B value="0.23284" />
-  <C value="530.6" />
-  <D value="0.24422" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="530.55" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="91.97365" />
-  <B value="-7071.987" />
-  <C value="-10.4626" />
-  <D value="7.767427E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="530.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.6303E+07" />
-  <B value="2.9196" />
-  <C value="-6.5593" />
-  <D value="6.8235" />
-  <E value="-2.6926" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="530.55" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="130880" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="140380" />
-  <B value="1173.7" />
-  <C value="0.81056" />
-  <D value="0.020863" />
-  <E value="-0.000005642" />
-  <Tmin units="K"  value="253.71" />
-  <Tmax units="K"  value="423.71" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="11365" />
-  <B value="-258.45" />
-  <C value="12.315" />
-  <D value="0.00033508" />
-  <E value="-7.4281E-08" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15762" />
-  <B value="-192.95" />
-  <C value="-33.685" />
-  <D value="-4171.3" />
-  <E value="3538.6" />
-  <Tmin units="K"  value="265.3" />
-  <Tmax units="K"  value="1591.8" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.2868" />
-  <B value="807.93" />
-  <C value="-0.36444" />
-  <D value="-0.0000010038" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="352.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.2912E-07" />
-  <B value="0.63237" />
-  <C value="126.55" />
-  <D value="15669" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.034599" />
-  <B value="27.577" />
-  <C value="-2.1207" />
-  <D value="0.00098891" />
-  <E value="-0.0000051703" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="475" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-197.62" />
-  <B value="-0.13413" />
-  <C value="101740" />
-  <D value="-8.2156E+08" />
-  <Tmin units="K"  value="350" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01525" />
-  <B value="32.131" />
-  <C value="-2.9556" />
-  <D value="0.00026339" />
-  <E value="-0.0000051671" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="512.44" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-416.05" />
-  <B value="484.46" />
-  <C value="-0.3614" />
-  <D value="0.00011182" />
-  <Tmin units="K"  value="185.65" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.091" />
-  <B value="-3100" />
-  <C value="-18.6" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.223" />
-  <B value="2894.8" />
-  <C value="-54.265" />
-  <Tmin units="K"  value="321.91" />
-  <Tmax units="K"  value="476.13" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.6879" />
-  <B value="-0.02954" />
-  <C value="0.000030971" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="352.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.28047" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.277307E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="256.6518" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="94.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.14006" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0383" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.919835" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.34999" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0969396" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.4786" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.116" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.3999" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.391" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18626.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0969396" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="22"  value="1" />
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-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
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-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="554-12-1" />
-<Smiles name="SMILES"  value="CCC(=O)OC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1303" />
-<CompoundID name="Name"  value="N-propyl formate" />
-<StructureFormula name="Structure"  value="HCOOCH2CH2CH3" />
-<Family name="Family"  value="55" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="538" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4060000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.285" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="354.69" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="180.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="180.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.211011" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.106" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09794" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.32" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.364E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18470" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05297" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.79E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.076E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.936E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="367800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.32E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91319" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.041E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.696" />
-  <B value="-0.0089769" />
-  <Tmin units="K"  value="72.1" />
-  <Tmax units="K"  value="180.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.915" />
-  <B value="0.26134" />
-  <C value="538" />
-  <D value="0.28" />
-  <Tmin units="K"  value="180.25" />
-  <Tmax units="K"  value="538" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="71.35267" />
-  <B value="-6244.56" />
-  <C value="-7.280094" />
-  <D value="4.220422E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="180.25" />
-  <Tmax units="K"  value="538" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.414398E+07" />
-  <B value="0.597341" />
-  <C value="-0.589234" />
-  <D value="1.004533" />
-  <E value="-0.602007" />
-  <Tmin units="K"  value="180.25" />
-  <Tmax units="K"  value="538" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="130880" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="76453" />
-  <B value="-41.853" />
-  <C value="10.797" />
-  <D value="0.0021776" />
-  <E value="0.0000016375" />
-  <Tmin units="K"  value="188.3" />
-  <Tmax units="K"  value="433.3" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="48655" />
-  <B value="-455.54" />
-  <C value="12.53" />
-  <D value="0.000075917" />
-  <E value="-4.246E-09" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15811" />
-  <B value="-174.27" />
-  <C value="-31.648" />
-  <D value="-4516.6" />
-  <E value="3566.6" />
-  <Tmin units="K"  value="269" />
-  <Tmax units="K"  value="1883" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-51.649" />
-  <B value="2317.7" />
-  <C value="6.5556" />
-  <D value="-0.000012396" />
-  <E value="2" />
-  <Tmin units="K"  value="180.25" />
-  <Tmax units="K"  value="353.97" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.0899E-07" />
-  <B value="0.58607" />
-  <C value="368.57" />
-  <D value="-171.06" />
-  <Tmin units="K"  value="180.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.017242" />
-  <B value="-22.474" />
-  <C value="-1.4478" />
-  <D value="-0.0011278" />
-  <E value="-0.0000020716" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="483.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="661.08" />
-  <B value="0.99232" />
-  <C value="5.8449E+09" />
-  <D value="-9.0597E+10" />
-  <Tmin units="K"  value="350" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.017831" />
-  <B value="28.209" />
-  <C value="-2.943" />
-  <D value="0.00018306" />
-  <E value="-0.0000042883" />
-  <Tmin units="K"  value="180.25" />
-  <Tmax units="K"  value="538" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-1865.2" />
-  <B value="457.73" />
-  <C value="-0.29209" />
-  <D value="0.000073654" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-6.820192" />
-  <B value="-3950" />
-  <C value="-23.7" />
-  <Tmin units="K"  value="273.0389" />
-  <Tmax units="K"  value="443.0389" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.052" />
-  <B value="2837.7" />
-  <C value="-56.289" />
-  <Tmin units="K"  value="322.95" />
-  <Tmax units="K"  value="483.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.9885" />
-  <B value="-0.052442" />
-  <C value="0.000067436" />
-  <Tmin units="K"  value="180.25" />
-  <Tmax units="K"  value="353.97" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.28231" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.21203E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="271.378" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="94.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.32658" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0387" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.910145" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.314" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0979424" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.4919" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.116" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.58645" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.314" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18339.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0979424" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="24"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="23"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="24"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="23"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-74-7" />
-<Smiles name="SMILES"  value="CCCOC(=O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1845" />
-<CompoundID name="Name"  value="Sulfolane" />
-<StructureFormula name="Structure"  value="-(CH2)2SO2(CH2)2-" />
-<Family name="Family"  value="70" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="855" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7290000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3365" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.345074" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="560.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="300.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="300.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.704459" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.17" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0952677" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.5234" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.309E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="26110" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.56E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06122" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.0E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.727E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.431E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="347500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1373000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.397E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.313" />
-  <B value="-0.0048955" />
-  <Tmin units="K"  value="120.22" />
-  <Tmax units="K"  value="300.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.89997" />
-  <B value="0.26972" />
-  <C value="853" />
-  <D value="0.30746" />
-  <Tmin units="K"  value="300.55" />
-  <Tmax units="K"  value="853" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="112.0995" />
-  <B value="-12237.47" />
-  <C value="-12.64533" />
-  <D value="4.157394E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="853" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.605659E+08" />
-  <B value="3.828131" />
-  <C value="-7.67047" />
-  <D value="6.739132" />
-  <E value="-2.353929" />
-  <Tmin units="K"  value="300.55" />
-  <Tmax units="K"  value="853" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-785.07" />
-  <B value="-58445" />
-  <C value="597.38" />
-  <D value="-2.0114" />
-  <E value="0.0022509" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="302.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122690" />
-  <B value="-336.31" />
-  <C value="11.614" />
-  <D value="0.0017011" />
-  <E value="-5.0866E-07" />
-  <Tmin units="K"  value="300.55" />
-  <Tmax units="K"  value="711.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="92921" />
-  <B value="-999.97" />
-  <C value="13.757" />
-  <D value="-0.00093192" />
-  <E value="0.0000002258" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21162" />
-  <B value="-345.47" />
-  <C value="-201.18" />
-  <D value="-901260" />
-  <E value="2067300" />
-  <Tmin units="K"  value="426.5" />
-  <Tmax units="K"  value="1575.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-56.251" />
-  <B value="4046.1" />
-  <C value="6.7894" />
-  <D value="-0.0000052803" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="682.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.9074E-08" />
-  <B value="0.97453" />
-  <C value="81.209" />
-  <D value="-9361.1" />
-  <Tmin units="K"  value="300.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.079581" />
-  <B value="-84.501" />
-  <C value="-1.1134" />
-  <D value="-0.0025206" />
-  <E value="2.9748E-07" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="450" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000077821" />
-  <B value="1.0313" />
-  <C value="528.38" />
-  <D value="54551" />
-  <Tmin units="K"  value="558.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014132" />
-  <B value="101.47" />
-  <C value="-3.0694" />
-  <D value="0.00080277" />
-  <E value="-0.0000027696" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="853" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-16512" />
-  <B value="535.08" />
-  <C value="-0.32273" />
-  <D value="0.000068445" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="4.6" />
-  <B value="-10000" />
-  <C value="-45" />
-  <Tmin units="K"  value="303" />
-  <Tmax units="K"  value="853" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.827" />
-  <B value="5019" />
-  <C value="-73.207" />
-  <Tmin units="K"  value="521.53" />
-  <Tmax units="K"  value="765.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="3.0048" />
-  <B value="-0.032316" />
-  <C value="0.000023123" />
-  <Tmin units="K"  value="300.55" />
-  <Tmax units="K"  value="682.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.327425" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.990302E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="212.828" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.257009" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="117.2" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0454" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.26697" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.377998" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0952677" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.0357" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.2" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.2" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.377998" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="26335.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0952677" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="118"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="56"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="59"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="2" />
-  <group id="118"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="78"  value="2" />
-  <group id="110"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="126-33-0" />
-<Smiles name="SMILES"  value="S1(=O)(=O)CCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2856" />
-<CompoundID name="Name"  value="N,n-dimethylacetamide" />
-<StructureFormula name="Structure"  value="(CH3)2NCOCH3" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="658" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4030000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.321" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.236" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="439.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="253.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="253.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.64072" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="87.1204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0930285" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.363509" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.368E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22350" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.27088E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05704" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.19E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.25E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-8.85E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="351000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.04182E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.38E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.194" />
-  <B value="-0.0062154" />
-  <Tmin units="K"  value="101.26" />
-  <Tmax units="K"  value="253.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.72553" />
-  <B value="0.2328" />
-  <C value="658" />
-  <D value="0.27034" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="636.69" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="67.333" />
-  <B value="-7592.9" />
-  <C value="-6.3978" />
-  <D value="0.0000021543" />
-  <E value="2" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="658" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.8939E+07" />
-  <B value="0.34564" />
-  <C value="-0.28415" />
-  <D value="0.52832" />
-  <E value="-0.2171" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="636.69" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5764.2" />
-  <B value="751.46" />
-  <C value="-1.5181" />
-  <D value="0.004037" />
-  <E value="-0.0000047604" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="253.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="175450" />
-  <B value="252.77" />
-  <C value="11.249" />
-  <D value="-0.052983" />
-  <E value="0.00011812" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="409" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="41899" />
-  <B value="-423.52" />
-  <C value="12.444" />
-  <D value="0.00039958" />
-  <E value="-1.2339E-07" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22953" />
-  <B value="-303.05" />
-  <C value="-68.186" />
-  <D value="-13212" />
-  <E value="-9988.7" />
-  <Tmin units="K"  value="329" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="16.727" />
-  <B value="-219.71" />
-  <C value="-4.0135" />
-  <D value="-0.0000013942" />
-  <E value="2" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="439.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.4592E-07" />
-  <B value="0.64442" />
-  <C value="412.29" />
-  <D value="-8784" />
-  <Tmin units="K"  value="439.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.06447" />
-  <B value="-206.75" />
-  <C value="-0.7204" />
-  <D value="0.00031649" />
-  <E value="-0.000010441" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="439.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0011762" />
-  <B value="0.72055" />
-  <C value="943.06" />
-  <D value="275760" />
-  <Tmin units="K"  value="439.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0049495" />
-  <B value="166.75" />
-  <C value="-4.146" />
-  <D value="0.0038773" />
-  <E value="-0.000009444" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="636.69" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-9221.9" />
-  <B value="475.24" />
-  <C value="-0.26167" />
-  <D value="0.000056823" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.469" />
-  <B value="3699.8" />
-  <C value="-66.946" />
-  <Tmin units="K"  value="402.31" />
-  <Tmax units="K"  value="572.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.5469" />
-  <B value="-0.018051" />
-  <C value="0.000010457" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="439.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.304288" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.226349E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="237.4774" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.258662" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="95.04" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0386" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.94469" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.363509" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0930285" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.760053" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.276" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.363509" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22352.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0930285" />
-<CAS name="CAS number"  value="127-19-5" />
-<Smiles name="SMILES"  value="CC(=O)N(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="5" />
-<CompoundID name="Name"  value="N-butane" />
-<StructureFormula name="Structure"  value="CH3(CH2)2CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="425.12" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3796000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.255" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.274" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="272.66" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="134.86" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="134.86" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.67358" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="58.123" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10048" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.199" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.886E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13510" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0478" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.94E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.2579E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.67E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="309910" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4661000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.84209" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.65732E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.194" />
-  <B value="-0.0068444" />
-  <Tmin units="K"  value="23.15" />
-  <Tmax units="K"  value="134.86" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0023" />
-  <B value="0.26457" />
-  <C value="425.17" />
-  <D value="0.27138" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="425.16" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="68.5773" />
-  <B value="-4444.916" />
-  <C value="-7.395837" />
-  <D value="9.857432E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="425.16" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.6258E+07" />
-  <B value="0.83741" />
-  <C value="-0.83676" />
-  <D value="0.41526" />
-  <E value="-0.007606" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="425.16" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-24310" />
-  <B value="1912.6" />
-  <C value="-19.664" />
-  <D value="0.12331" />
-  <E value="-0.00026167" />
-  <Tmin units="K"  value="22.35" />
-  <Tmax units="K"  value="130.16" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115150" />
-  <B value="-3564.7" />
-  <C value="41.067" />
-  <D value="-0.098803" />
-  <E value="0.0001183" />
-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="44749.95" />
-  <B value="-338.1412" />
-  <C value="11.81452" />
-  <D value="0.00097744" />
-  <E value="-3.359129E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.14916" />
-  <B value="-144.06" />
-  <C value="-9.8812" />
-  <D value="-360.23" />
-  <E value="516.2" />
-  <Tmin units="K"  value="212.58" />
-  <Tmax units="K"  value="1913.22" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-46.56549" />
-  <B value="1439.945" />
-  <C value="6.168131" />
-  <D value="-0.000023917" />
-  <E value="2" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="420" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.7078E-08" />
-  <B value="0.97147" />
-  <C value="-51.16" />
-  <D value="6431" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.00024966" />
-  <B value="-43.155" />
-  <C value="-0.78129" />
-  <D value="-0.0043776" />
-  <E value="-4.136E-08" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="400" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.042635" />
-  <B value="0.45147" />
-  <C value="4234" />
-  <D value="1756600" />
-  <Tmin units="K"  value="272.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035324" />
-  <B value="4.5815" />
-  <C value="-2.4942" />
-  <D value="-0.0015096" />
-  <E value="-0.0000013297" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="409.84" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="46120" />
-  <B value="46.029" />
-  <C value="0.6699" />
-  <D value="-0.00087892" />
-  <E value="3.4372E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.213511" />
-  <B value="-700" />
-  <C value="-4.2" />
-  <Tmin units="K"  value="253.0389" />
-  <Tmax units="K"  value="423.0389" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.958" />
-  <B value="2350.4" />
-  <C value="-23.412" />
-  <Tmin units="K"  value="255.37" />
-  <Tmax units="K"  value="380.37" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.2039" />
-  <B value="-0.019582" />
-  <C value="0.000014014" />
-  <Tmin units="K"  value="134.86" />
-  <Tmax units="K"  value="420" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.25439" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.594883E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="262.6193" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2728" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="86.7" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.46406" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0339" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.583223" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2008" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0965533" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.151" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.776" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.776" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.00301" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.84619" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1953" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13766.21" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1014" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-97-8" />
-<Smiles name="SMILES"  value="CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="4" />
-<CompoundID name="Name"  value="Isobutane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="407.85" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3640000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2627" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.278" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="261.34" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="113.54" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="113.54" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0120622" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="58.123" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10436" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.186" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.948E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12560" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.4E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04779" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.93E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.3499E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.144E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="295500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4540000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.75157" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.64812E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.956" />
-  <B value="-0.015646" />
-  <Tmin units="K"  value="45.42" />
-  <Tmax units="K"  value="113.54" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.89934" />
-  <B value="0.25371" />
-  <C value="407.85" />
-  <D value="0.25125" />
-  <Tmin units="K"  value="113.54" />
-  <Tmax units="K"  value="407.84" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="70.58866" />
-  <B value="-4298.161" />
-  <C value="-7.798635" />
-  <D value="0.0000116" />
-  <E value="2" />
-  <Tmin units="K"  value="113.54" />
-  <Tmax units="K"  value="408" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.4869E+07" />
-  <B value="0.64449" />
-  <C value="-0.15424" />
-  <D value="-0.28822" />
-  <E value="0.20982" />
-  <Tmin units="K"  value="113.54" />
-  <Tmax units="K"  value="407.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-58597" />
-  <B value="5767.7" />
-  <C value="-111.79" />
-  <D value="0.90616" />
-  <E value="-0.0024065" />
-  <Tmin units="K"  value="77" />
-  <Tmax units="K"  value="107" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="89466" />
-  <B value="-323.61" />
-  <C value="12.827" />
-  <D value="-0.010476" />
-  <E value="0.000025037" />
-  <Tmin units="K"  value="113.54" />
-  <Tmax units="K"  value="380" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39746.03" />
-  <B value="-371.573" />
-  <C value="12.02593" />
-  <D value="0.000755039" />
-  <E value="-2.59608E-07" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15963" />
-  <B value="-143.05" />
-  <C value="-7.3449" />
-  <D value="-502.57" />
-  <E value="799.28" />
-  <Tmin units="K"  value="204.07" />
-  <Tmax units="K"  value="1836.59" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-39.10125" />
-  <B value="1315.145" />
-  <C value="4.876982" />
-  <D value="-0.0000203993" />
-  <E value="2" />
-  <Tmin units="K"  value="110" />
-  <Tmax units="K"  value="310.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.951E-08" />
-  <B value="0.90975" />
-  <C value="-52.076" />
-  <D value="8625.4" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.029586" />
-  <B value="56.323" />
-  <C value="-2.8746" />
-  <D value="0.0051627" />
-  <E value="-0.000017826" />
-  <Tmin units="K"  value="113.54" />
-  <Tmax units="K"  value="400" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.091178" />
-  <B value="0.18264" />
-  <C value="626.56" />
-  <D value="1124600" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.007942" />
-  <B value="27.727" />
-  <C value="-3.375" />
-  <D value="0.0010263" />
-  <E value="-0.000011845" />
-  <Tmin units="K"  value="113.54" />
-  <Tmax units="K"  value="407.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="27862" />
-  <B value="148.69" />
-  <C value="0.45538" />
-  <D value="-0.00067339" />
-  <E value="2.6964E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.913" />
-  <B value="2269.9" />
-  <C value="-19.458" />
-  <Tmin units="K"  value="249.82" />
-  <Tmax units="K"  value="366.48" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.42505" />
-  <B value="-0.057646" />
-  <C value="0.000091229" />
-  <Tmin units="K"  value="110" />
-  <Tmax units="K"  value="310.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.25683" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.553216E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="265.4452" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.275" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="86.7" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.03973" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0339" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.561966" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1825" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.105238" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.1502" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.772" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.772" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.006209" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.18616" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1825" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13766.21" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1055" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-28-5" />
-<Smiles name="SMILES"  value="CC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1105" />
-<CompoundID name="Name"  value="1-butanol" />
-<StructureFormula name="Structure"  value="CH3(CH2)3OH" />
-<Family name="Family"  value="27" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="563.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4423000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.275" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="390.88" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="183.85" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="184.51" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000320123" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.123" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09196" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.591" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.225E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23510" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.83737E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0524" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.62E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.746E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.503E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="361480" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9372000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0818" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.45601E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.1" />
-  <B value="9.192E-09" />
-  <Tmin units="K"  value="184.51" />
-  <Tmax units="K"  value="194.01" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.7931" />
-  <B value="0.24201" />
-  <C value="563.05" />
-  <D value="0.22263" />
-  <Tmin units="K"  value="184.51" />
-  <Tmax units="K"  value="543.08" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="94.3424" />
-  <B value="-9140.942" />
-  <C value="-10.0038" />
-  <D value="1.706963E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="184.51" />
-  <Tmax units="K"  value="563" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.03317E+08" />
-  <B value="2.061287" />
-  <C value="-3.612692" />
-  <D value="3.240107" />
-  <E value="-1.125287" />
-  <Tmin units="K"  value="184.51" />
-  <Tmax units="K"  value="563" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13649" />
-  <B value="1130.7" />
-  <C value="-3.374" />
-  <D value="-0.0057232" />
-  <E value="0.000046587" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="184.54" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="118540" />
-  <B value="928.1" />
-  <C value="-3.4067" />
-  <D value="0.053827" />
-  <E value="-0.000053611" />
-  <Tmin units="K"  value="184.51" />
-  <Tmax units="K"  value="390.81" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63521" />
-  <B value="-568.25" />
-  <C value="12.587" />
-  <D value="0.0001566" />
-  <E value="-5.9966E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.11374" />
-  <B value="-82.42" />
-  <C value="-54.273" />
-  <D value="35653" />
-  <E value="-154650" />
-  <Tmin units="K"  value="281.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-44.688" />
-  <B value="3409.1" />
-  <C value="4.8758" />
-  <D value="-0.0000057302" />
-  <E value="2" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="390.81" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000014735" />
-  <B value="0.46162" />
-  <C value="554.37" />
-  <D value="6760.2" />
-  <Tmin units="K"  value="184.51" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.019408" />
-  <B value="-19.063" />
-  <C value="-1.4625" />
-  <D value="-0.0014843" />
-  <E value="-4.7683E-07" />
-  <Tmin units="K"  value="184.51" />
-  <Tmax units="K"  value="390.81" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00022746" />
-  <B value="1.1142" />
-  <C value="3597.3" />
-  <D value="-411420" />
-  <Tmin units="K"  value="370.7" />
-  <Tmax units="K"  value="712.94" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.033153" />
-  <B value="70.924" />
-  <C value="-3.2742" />
-  <D value="0.0018256" />
-  <E value="-0.0000040925" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="413.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="37141" />
-  <B value="136.32" />
-  <C value="0.55607" />
-  <D value="-0.00080567" />
-  <E value="3.2127E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-30.12876" />
-  <B value="-11453.99" />
-  <C value="-54.40369" />
-  <Tmin units="K"  value="283" />
-  <Tmax units="K"  value="563" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.469" />
-  <B value="2804" />
-  <C value="-108.82" />
-  <Tmin units="K"  value="338.95" />
-  <Tmax units="K"  value="503.24" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="12.049" />
-  <B value="-0.092422" />
-  <C value="0.00010714" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="390.81" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.28409" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.110187E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="287.9812" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2538" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="92.81" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="2.3141" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0486" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.813869" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.5928" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.09197" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.4543" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.052" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.88" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.29395" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="1.005612" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-4.1355" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.593" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23289.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0919432" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="71-36-3" />
-<Smiles name="SMILES"  value="CCCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1106" />
-<CompoundID name="Name"  value="2-methyl-1-propanol" />
-<StructureFormula name="Structure"  value="(CH3)2CHCH2OH" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="547.78" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4300000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.273" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.258" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="381.04" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="165.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="165.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.46096E-06" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.123" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09291" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.59" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.332E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22900" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.47E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05239" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.62E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.832E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.549E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="348000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6322000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2052" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.449E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.341" />
-  <B value="-0.010401" />
-  <Tmin units="K"  value="66.06" />
-  <Tmax units="K"  value="165.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.80194" />
-  <B value="0.24515" />
-  <C value="547.81" />
-  <D value="0.21175" />
-  <Tmin units="K"  value="165.15" />
-  <Tmax units="K"  value="547.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="174.0368" />
-  <B value="-12288.81" />
-  <C value="-22.23928" />
-  <D value="0.0000131856" />
-  <E value="2" />
-  <Tmin units="K"  value="165.15" />
-  <Tmax units="K"  value="547.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.1411E+07" />
-  <B value="-0.67703" />
-  <C value="2.6884" />
-  <D value="-2.3416" />
-  <E value="0.75942" />
-  <Tmin units="K"  value="165.15" />
-  <Tmax units="K"  value="527.66" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10092" />
-  <B value="1083.5" />
-  <C value="-3.0549" />
-  <D value="-0.01591" />
-  <E value="0.00010676" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="171.2" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="114500" />
-  <B value="844.65" />
-  <C value="-3.6753" />
-  <D value="0.058766" />
-  <E value="-0.000062464" />
-  <Tmin units="K"  value="165.15" />
-  <Tmax units="K"  value="403.87" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="20857" />
-  <B value="-275.26" />
-  <C value="12.137" />
-  <D value="0.00070478" />
-  <E value="-0.0000002462" />
-  <Tmin units="K"  value="255.37" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.1509" />
-  <B value="-136.83" />
-  <C value="-28.494" />
-  <D value="728.11" />
-  <E value="-79012" />
-  <Tmin units="K"  value="301.25" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-107.9662" />
-  <B value="6199.736" />
-  <C value="14.5721" />
-  <D value="-0.000017552" />
-  <E value="2" />
-  <Tmin units="K"  value="210.93" />
-  <Tmax units="K"  value="544.26" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.9881E-07" />
-  <B value="0.52424" />
-  <C value="295.54" />
-  <D value="17281" />
-  <Tmin units="K"  value="165.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.27685" />
-  <B value="36.722" />
-  <C value="-1.0689" />
-  <D value="0.00066056" />
-  <E value="-0.0000014048" />
-  <Tmin units="K"  value="165.15" />
-  <Tmax units="K"  value="488.71" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="2189.9" />
-  <B value="0.91222" />
-  <C value="1.1244E+10" />
-  <D value="-5.1003E+11" />
-  <Tmin units="K"  value="199.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010474" />
-  <B value="-225.69" />
-  <C value="-0.88163" />
-  <D value="-0.0069349" />
-  <E value="0.0000033337" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="380.81" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-7708" />
-  <B value="468.9" />
-  <C value="-0.2884" />
-  <D value="0.00007231" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-18.41508" />
-  <B value="-8850" />
-  <C value="-53.1" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.336" />
-  <B value="2645.8" />
-  <C value="-111.22" />
-  <Tmin units="K"  value="330.35" />
-  <Tmax units="K"  value="488.71" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="10.484" />
-  <B value="-0.074098" />
-  <C value="0.000068531" />
-  <Tmin units="K"  value="210.93" />
-  <Tmax units="K"  value="544.26" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.273" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.152084E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="272.4898" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="92.81" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.75293" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.048" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.804234" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.58828" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.09235" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.4535" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.048" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.88" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.58613" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.592" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23750.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0930277" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="78-83-1" />
-<Smiles name="SMILES"  value="OCC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1107" />
-<CompoundID name="Name"  value="2-butanol" />
-<StructureFormula name="Structure"  value="CH3CH2CH(OH)CH3" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="536.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4179000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.269" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="372.66" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="158.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="158.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.16526E-06" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.123" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09235" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.574" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.203E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22620" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.54E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05239" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.62E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.929E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.696E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="364690" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5971000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2365" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4408E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.976" />
-  <B value="-0.011447" />
-  <Tmin units="K"  value="63.38" />
-  <Tmax units="K"  value="158.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.65041" />
-  <B value="0.21558" />
-  <C value="536.05" />
-  <D value="0.22084" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="516.32" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="145.55" />
-  <B value="-10811" />
-  <C value="-17.957" />
-  <D value="0.0000094132" />
-  <E value="2" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="536.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.123771E+07" />
-  <B value="1.779726" />
-  <C value="-3.389854" />
-  <D value="3.546493" />
-  <E value="-1.385264" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="516.32" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10538" />
-  <B value="1245.7" />
-  <C value="-7.8474" />
-  <D value="0.033221" />
-  <E value="-0.000052097" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="184.73" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68513" />
-  <B value="631.42" />
-  <C value="2.7425" />
-  <D value="0.03164" />
-  <E value="-0.000028572" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="372.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="70319" />
-  <B value="-564.51" />
-  <C value="12.517" />
-  <D value="0.00018661" />
-  <E value="-6.3166E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18777" />
-  <B value="-172.62" />
-  <C value="-36.943" />
-  <D value="-5764.3" />
-  <E value="4704.5" />
-  <Tmin units="K"  value="268.1" />
-  <Tmax units="K"  value="1955" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="19.329" />
-  <B value="3026.9" />
-  <C value="-6.6532" />
-  <D value="0.000029986" />
-  <E value="2" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.3231E-07" />
-  <B value="0.76798" />
-  <C value="139.73" />
-  <D value="-4888.6" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.031711" />
-  <B value="-158.34" />
-  <C value="-0.24491" />
-  <D value="-0.0057475" />
-  <E value="0.000002591" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="398.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000011661" />
-  <B value="1.7056" />
-  <C value="340.33" />
-  <D value="-60553" />
-  <Tmin units="K"  value="281.21" />
-  <Tmax units="K"  value="992.7" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013468" />
-  <B value="-124.81" />
-  <C value="-1.739" />
-  <D value="-0.0040653" />
-  <E value="6.6383E-07" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="372.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="32094" />
-  <B value="237.47" />
-  <C value="0.22682" />
-  <D value="-0.00042736" />
-  <E value="1.7602E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-30.07289" />
-  <B value="-11424.69" />
-  <C value="-54.73557" />
-  <Tmin units="K"  value="283" />
-  <Tmax units="K"  value="536" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.402" />
-  <B value="2657.7" />
-  <C value="-103.45" />
-  <Tmin units="K"  value="323.15" />
-  <Tmax units="K"  value="476.56" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="18.793" />
-  <B value="-0.12678" />
-  <C value="0.00014902" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.28029" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.297213E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="244.9968" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="92.81" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.21667" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0476" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.813869" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.5792" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.09235" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.4535" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.048" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.88" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.601957" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.600508" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.94166" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.571133" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22629.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0921178" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="78-92-2" />
-<Smiles name="SMILES"  value="CCC(O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1108" />
-<CompoundID name="Name"  value="2-methyl-2-propanol" />
-<StructureFormula name="Structure"  value="C(CH3)3OH" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="506.21" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3973000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.275" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="355.49" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="298.97" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="298.97" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="5884.28" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.123" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09488" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.613" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.067E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21620" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.57E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05238" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.62E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.124E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.776E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="326300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6703000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.199" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4239E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.269" />
-  <B value="-0.0042735" />
-  <Tmin units="K"  value="119.59" />
-  <Tmax units="K"  value="298.97" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.40838" />
-  <B value="0.17034" />
-  <C value="508.88" />
-  <D value="0.1974" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="508.87" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="196.8976" />
-  <B value="-12439.78" />
-  <C value="-26.03107" />
-  <D value="0.0000198743" />
-  <E value="2" />
-  <Tmin units="K"  value="252.75" />
-  <Tmax units="K"  value="506.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.49928E+07" />
-  <B value="1.077392" />
-  <C value="-0.185452" />
-  <D value="-0.822732" />
-  <E value="0.535399" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="506.2" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6950.4" />
-  <B value="346.65" />
-  <C value="4.7374" />
-  <D value="-0.035946" />
-  <E value="0.000081348" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="286.13" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-158220" />
-  <B value="-166.8" />
-  <C value="13.168" />
-  <D value="0.0013959" />
-  <E value="-0.0000019876" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65560" />
-  <B value="-540.88" />
-  <C value="12.558" />
-  <D value="0.00014695" />
-  <E value="-5.2324E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18659" />
-  <B value="-157.11" />
-  <C value="-31.789" />
-  <D value="-4775.1" />
-  <E value="5156.6" />
-  <Tmin units="K"  value="253.1" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-933.24" />
-  <B value="39184" />
-  <C value="142.25" />
-  <D value="-0.0001583" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="451.21" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.5934E-07" />
-  <B value="0.64853" />
-  <C value="136.6" />
-  <D value="9124.5" />
-  <Tmin units="K"  value="298.97" />
-  <Tmax units="K"  value="600" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0056947" />
-  <B value="358.71" />
-  <C value="-5.5774" />
-  <D value="0.012913" />
-  <E value="-0.000018273" />
-  <Tmin units="K"  value="298.97" />
-  <Tmax units="K"  value="404.96" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="4.2365E-07" />
-  <B value="1.7929" />
-  <C value="-130.93" />
-  <D value="17989" />
-  <Tmin units="K"  value="278.59" />
-  <Tmax units="K"  value="766.87" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="0.0025589" />
-  <B value="-1098.2" />
-  <C value="4.0953" />
-  <D value="-0.014096" />
-  <E value="-0.0000031561" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="355.57" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="21709" />
-  <B value="299.75" />
-  <C value="0.12613" />
-  <D value="-0.00036251" />
-  <E value="1.6188E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.291" />
-  <B value="2437.7" />
-  <C value="-105.93" />
-  <Tmin units="K"  value="303.83" />
-  <Tmax units="K"  value="451.67" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="17.837" />
-  <B value="-0.11457" />
-  <C value="0.00012188" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="451.21" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2876" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.110187E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="258.9095" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="92.81" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="1.1555" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0466" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.781255" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.61339" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.09488" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.4528" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.128" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="0.88" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.745244" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.484002" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.2932" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.612" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21491.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0948614" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-65-0" />
-<Smiles name="SMILES"  value="CC(C)(O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1402" />
-<CompoundID name="Name"  value="Diethyl ether" />
-<StructureFormula name="Structure"  value="CH3CH2OCH2CH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="466.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3640000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.28" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="307.59" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="156.85" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="156.85" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.395447" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.123" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10475" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.281" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.177E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15420" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0515" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.521E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.221E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="342300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7190000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.9084" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.5035E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.584" />
-  <B value="-0.010419" />
-  <Tmin units="K"  value="62.74" />
-  <Tmax units="K"  value="156.85" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.97479" />
-  <B value="0.27114" />
-  <C value="466.7" />
-  <D value="0.28433" />
-  <Tmin units="K"  value="156.85" />
-  <Tmax units="K"  value="466.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="75.39748" />
-  <B value="-5436.852" />
-  <C value="-8.193869" />
-  <D value="7.812562E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="156.85" />
-  <Tmax units="K"  value="466.74" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.331574E+07" />
-  <B value="0.876213" />
-  <C value="0.475413" />
-  <D value="-1.944676" />
-  <E value="1.061631" />
-  <Tmin units="K"  value="156.85" />
-  <Tmax units="K"  value="466.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15828" />
-  <B value="1425.3" />
-  <C value="-4.6851" />
-  <D value="-0.021451" />
-  <E value="0.00015406" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="156.92" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="145290" />
-  <B value="-2.8208" />
-  <C value="5.9722" />
-  <D value="0.017041" />
-  <E value="-0.0000078238" />
-  <Tmin units="K"  value="156.92" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81727" />
-  <B value="-660.7" />
-  <C value="12.61" />
-  <D value="0.00016979" />
-  <E value="-7.4028E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15776" />
-  <B value="-130.42" />
-  <C value="-20.822" />
-  <D value="-1690" />
-  <E value="2592.4" />
-  <Tmin units="K"  value="233.35" />
-  <Tmax units="K"  value="1866.8" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="10.139" />
-  <B value="-61.707" />
-  <C value="-3.2168" />
-  <D value="-9.5022E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000019481" />
-  <B value="0.40997" />
-  <C value="495.46" />
-  <D value="85.073" />
-  <Tmin units="K"  value="156.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.14221" />
-  <B value="30.008" />
-  <C value="-1.3139" />
-  <D value="0.00048013" />
-  <E value="-0.0000026572" />
-  <Tmin units="K"  value="156.85" />
-  <Tmax units="K"  value="433.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.0044909" />
-  <B value="0.61494" />
-  <C value="-3258.3" />
-  <D value="85.806" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="600" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0086293" />
-  <B value="70.513" />
-  <C value="-3.7435" />
-  <D value="0.002828" />
-  <E value="-0.0000115" />
-  <Tmin units="K"  value="156.85" />
-  <Tmax units="K"  value="466.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="38346" />
-  <B value="311.73" />
-  <C value="-0.15548" />
-  <D value="0.00010942" />
-  <E value="-5.8035E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-3.371722" />
-  <B value="-2150" />
-  <C value="-12.9" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.982" />
-  <B value="2524.9" />
-  <C value="-40.677" />
-  <Tmin units="K"  value="283.9" />
-  <Tmax units="K"  value="417.78" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.7993" />
-  <B value="-0.020592" />
-  <C value="0.000017313" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2838" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.49E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="362" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="92.81" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.00625" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0376" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.713" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.28099" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.104692" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.39" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.02" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.024" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.284607" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15530.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.104692" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="21"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="60-29-7" />
-<Smiles name="SMILES"  value="CCOCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1202" />
-<CompoundID name="Name"  value="Diethylene glycol" />
-<StructureFormula name="Structure"  value="HOCH2CH2OCH2CH2OH" />
-<Family name="Family"  value="49" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="744.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4600000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.312" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.232" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="517.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="262.7" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="262.7" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00319709" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="106.12" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0952681" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.622105" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.739E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="28920" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.41E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0607" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.92E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.464E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.84E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="440000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.3481E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="3.1418" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.155E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.607" />
-  <B value="-0.0056939" />
-  <Tmin units="K"  value="105.08" />
-  <Tmax units="K"  value="262.7" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.81894" />
-  <B value="0.25823" />
-  <C value="744.6" />
-  <D value="0.23979" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="719.24" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="46.26595" />
-  <B value="-10205.15" />
-  <C value="-2.102723" />
-  <D value="-7.036466E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="744.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.0853E+08" />
-  <B value="-0.00876655" />
-  <C value="1.770951" />
-  <D value="-1.359893" />
-  <E value="-0.0210292" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="744.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5791.1" />
-  <B value="739.7" />
-  <C value="-1.4583" />
-  <D value="0.003773" />
-  <E value="-0.0000043193" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="262.7" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="188290" />
-  <B value="227.63" />
-  <C value="5.7157" />
-  <D value="0.020545" />
-  <E value="-0.000018798" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="513.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="82107" />
-  <B value="-687.16" />
-  <C value="13.353" />
-  <D value="-0.00070647" />
-  <E value="2.4155E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.0058126" />
-  <B value="205.06" />
-  <C value="-277.68" />
-  <D value="1325800" />
-  <E value="-7165900" />
-  <Tmin units="K"  value="372.3" />
-  <Tmax units="K"  value="1564" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-374.29" />
-  <B value="18192" />
-  <C value="55.132" />
-  <D value="-0.000049166" />
-  <E value="2" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="595.68" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.4523E-08" />
-  <B value="0.8468" />
-  <C value="24.322" />
-  <D value="7352.9" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.11579" />
-  <B value="8.2246" />
-  <C value="-1.6466" />
-  <D value="0.002673" />
-  <E value="-0.0000035412" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="517.95" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="500.16" />
-  <B value="1.0276" />
-  <C value="7.9617E+09" />
-  <D value="-7.5258E+11" />
-  <Tmin units="K"  value="456.48" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.030468" />
-  <B value="-174.37" />
-  <C value="-1.1319" />
-  <D value="-0.0029512" />
-  <E value="4.9272E-07" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="518.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-8099.9" />
-  <B value="599.05" />
-  <C value="-0.41929" />
-  <D value="0.00011046" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-10.44195" />
-  <B value="-9962.105" />
-  <C value="-59.06982" />
-  <Tmin units="K"  value="278" />
-  <Tmax units="K"  value="744" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.901" />
-  <B value="3422.4" />
-  <C value="-153.31" />
-  <Tmin units="K"  value="447.33" />
-  <Tmax units="K"  value="668.51" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="9.862" />
-  <B value="-0.057143" />
-  <C value="0.000042368" />
-  <Tmin units="K"  value="262.7" />
-  <Tmax units="K"  value="595.68" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3889" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.306526E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="252.6928" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="105.03" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-8.3213" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0583" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.12142" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.2005" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0952681" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.9415" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.8" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="13.224" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.621104" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="27775.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0952681" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="3" />
-  <group id="15"  value="2" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="3" />
-  <group id="14"  value="2" />
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="3" />
-  <group id="15"  value="2" />
-  <group id="21"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="3" />
-  <group id="15"  value="2" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="3" />
-  <group id="14"  value="2" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-46-6" />
-<Smiles name="SMILES"  value="OCCOCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1710" />
-<CompoundID name="Name"  value="Diethylamine" />
-<StructureFormula name="Structure"  value="C2H5NHC2H5" />
-<Family name="Family"  value="35" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="496.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3710000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.301" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.27" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="328.6" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="223.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="223.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="374.108" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="73.138" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10424" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.303856" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.172E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16610" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05588" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.93E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.142E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.308E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="352200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.14E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.94091" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.8003E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.411" />
-  <B value="-0.0066259" />
-  <Tmin units="K"  value="89.34" />
-  <Tmax units="K"  value="223.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.73036" />
-  <B value="0.23814" />
-  <C value="496.66" />
-  <D value="0.24991" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="496.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="64.68388" />
-  <B value="-5484.939" />
-  <C value="-6.37255" />
-  <D value="4.185124E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="496.65" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.911798E+07" />
-  <B value="0.292165" />
-  <C value="-0.28266" />
-  <D value="0.355094" />
-  <E value="0.0257197" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="482.22" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="4978.9" />
-  <B value="695.29" />
-  <C value="-1.524" />
-  <D value="0.0044408" />
-  <E value="-0.0000057807" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="223.35" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="107090" />
-  <B value="694.46" />
-  <C value="2.8508" />
-  <D value="0.027204" />
-  <E value="-0.000024864" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="368.3" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85298" />
-  <B value="-793.64" />
-  <C value="13.085" />
-  <D value="-0.00026826" />
-  <E value="6.6572E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16812" />
-  <B value="-207.88" />
-  <C value="-22.248" />
-  <D value="-1109.7" />
-  <E value="896.13" />
-  <Tmin units="K"  value="248.3" />
-  <Tmax units="K"  value="1986.4" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-21.138" />
-  <B value="1492" />
-  <C value="1.4401" />
-  <D value="-0.0000012994" />
-  <E value="2" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="329.1" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.3797E-07" />
-  <B value="0.60244" />
-  <C value="253.34" />
-  <D value="-614.36" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.066644" />
-  <B value="-97.786" />
-  <C value="-0.73312" />
-  <D value="-0.0054502" />
-  <E value="-7.5663E-08" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="453.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000016939" />
-  <B value="1.2488" />
-  <C value="-114.17" />
-  <D value="77881" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.045239" />
-  <B value="-2.3813" />
-  <C value="-2.2833" />
-  <D value="-0.0012617" />
-  <E value="-7.5666E-07" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="482.22" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="25176" />
-  <B value="269.16" />
-  <C value="0.23513" />
-  <D value="-0.00045738" />
-  <E value="1.9123E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-0.95" />
-  <B value="-1000" />
-  <C value="-75" />
-  <Tmin units="K"  value="243" />
-  <Tmax units="K"  value="496" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.038" />
-  <B value="2654.5" />
-  <C value="-49.762" />
-  <Tmin units="K"  value="297.97" />
-  <Tmax units="K"  value="443.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0998" />
-  <B value="-0.048496" />
-  <C value="0.000059737" />
-  <Tmin units="K"  value="223.35" />
-  <Tmax units="K"  value="329.1" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.29183" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.018163E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="290.9575" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.27" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="93.55" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0392" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.707" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3045" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.104234" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.68" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.17" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.303733" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16543.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.104234" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="33"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="30"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="33"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="32"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-89-7" />
-<Smiles name="SMILES"  value="CCNCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1889" />
-<CompoundID name="Name"  value="Furfural" />
-<StructureFormula name="Structure"  value="(OC4H3)CHO" />
-<Family name="Family"  value="45" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="670.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5660000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.252" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="434.85" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="236.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="236.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.54565" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="96.0841" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0832248" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.367784" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.35E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23610" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.2E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04812" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.25E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.51E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.028E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="333300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.44E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.4331" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.2564E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.038" />
-  <B value="-0.0073899" />
-  <Tmin units="K"  value="94.66" />
-  <Tmax units="K"  value="236.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0614" />
-  <B value="0.26706" />
-  <C value="670.15" />
-  <D value="0.30028" />
-  <Tmin units="K"  value="236.65" />
-  <Tmax units="K"  value="647.33" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="25.656" />
-  <B value="-5514" />
-  <C value="-0.19573" />
-  <D value="-0.0000013402" />
-  <E value="2" />
-  <Tmin units="K"  value="236.65" />
-  <Tmax units="K"  value="670.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.3009E+07" />
-  <B value="0.4784" />
-  <C value="0.066802" />
-  <D value="-0.59102" />
-  <E value="0.42453" />
-  <Tmin units="K"  value="236.65" />
-  <Tmax units="K"  value="647.33" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6836.7" />
-  <B value="503.49" />
-  <C value="-0.0034192" />
-  <D value="-0.0033694" />
-  <E value="0.0000088513" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="236.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122630" />
-  <B value="404.51" />
-  <C value="3.0587" />
-  <D value="0.029945" />
-  <E value="-0.000031496" />
-  <Tmin units="K"  value="246.56" />
-  <Tmax units="K"  value="471.95" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="45855" />
-  <B value="-497.61" />
-  <C value="12.549" />
-  <D value="-0.000033724" />
-  <E value="-2.8785E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15692" />
-  <B value="-204.6" />
-  <C value="-63.981" />
-  <D value="-111350" />
-  <E value="220560" />
-  <Tmin units="K"  value="335.07" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="2.6487" />
-  <B value="910.16" />
-  <C value="-2.1754" />
-  <D value="0.0000028413" />
-  <E value="2" />
-  <Tmin units="K"  value="236.65" />
-  <Tmax units="K"  value="536.12" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.1928E-08" />
-  <B value="0.91224" />
-  <C value="70.285" />
-  <D value="-5476.4" />
-  <Tmin units="K"  value="236.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.13228" />
-  <B value="19058" />
-  <C value="-182.25" />
-  <D value="0.56426" />
-  <E value="-0.00059782" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="466.63" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00022183" />
-  <B value="0.91119" />
-  <C value="617.18" />
-  <D value="55137" />
-  <Tmin units="K"  value="434.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.023307" />
-  <B value="51.068" />
-  <C value="-2.7476" />
-  <D value="0.00047578" />
-  <E value="-0.000003172" />
-  <Tmin units="K"  value="236.65" />
-  <Tmax units="K"  value="647.33" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="4779.126" />
-  <B value="385.556" />
-  <C value="-0.233346" />
-  <D value="0.0000499707" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="4" />
-  <B value="-10000" />
-  <C value="-50" />
-  <Tmin units="K"  value="293" />
-  <Tmax units="K"  value="670" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.467" />
-  <B value="4392.1" />
-  <C value="-32.683" />
-  <Tmin units="K"  value="405.3" />
-  <Tmax units="K"  value="601.7" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.70056" />
-  <B value="-0.032345" />
-  <C value="0.000028487" />
-  <Tmin units="K"  value="236.65" />
-  <Tmax units="K"  value="536.12" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.255652" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.046311E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="324.1523" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.258287" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="100.96" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.25422" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0384" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.15394" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.383" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.08323" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.168" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.484" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.484" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.5842" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.383" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23643.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0831649" />
-<UnifacVLE name="UNIFAC" >
-  <group id="62"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="22"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="48"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="62"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="62"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="61"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="98-01-1" />
-<Smiles name="SMILES"  value="O1C=CC=C1(C=O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1791" />
-<CompoundID name="Name"  value="Pyridine" />
-<StructureFormula name="Structure"  value="-CHCHCHCHCHN-" />
-<Family name="Family"  value="36" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="620" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5670000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.254" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="388.37" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="231.53" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="231.51" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="20.5354" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="79.101" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08088" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.242" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.938E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21570" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.31E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0455" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.65E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.4037E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.9049E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="282780" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8280000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.87684" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.6721E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.748" />
-  <B value="-0.0080994" />
-  <Tmin units="K"  value="92.6" />
-  <Tmax units="K"  value="231.51" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.67102" />
-  <B value="0.2057" />
-  <C value="620" />
-  <D value="0.26001" />
-  <Tmin units="K"  value="231.51" />
-  <Tmax units="K"  value="619.95" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.05373" />
-  <B value="-7269.578" />
-  <C value="-8.810082" />
-  <D value="4.816564E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="231.51" />
-  <Tmax units="K"  value="619.95" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.4421E+07" />
-  <B value="2.7457" />
-  <C value="-5.3078" />
-  <D value="4.8654" />
-  <E value="-1.7952" />
-  <Tmin units="K"  value="231.48" />
-  <Tmax units="K"  value="619.95" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11015" />
-  <B value="1416.6" />
-  <C value="-12.963" />
-  <D value="0.059131" />
-  <E value="-0.000091912" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="231.51" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="101830" />
-  <B value="209.77" />
-  <C value="5.3544" />
-  <D value="0.019802" />
-  <E value="-0.000018129" />
-  <Tmin units="K"  value="231.49" />
-  <Tmax units="K"  value="388.41" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="36223" />
-  <B value="-620.9" />
-  <C value="12.812" />
-  <D value="-0.00029215" />
-  <E value="7.7524E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12072" />
-  <B value="-161.9" />
-  <C value="-37.161" />
-  <D value="-139.47" />
-  <E value="-4487.4" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1860" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-82.798" />
-  <B value="4102.8" />
-  <C value="11.028" />
-  <D value="-0.0000093419" />
-  <E value="2" />
-  <Tmin units="K"  value="231.53" />
-  <Tmax units="K"  value="495.96" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.339E-08" />
-  <B value="0.90066" />
-  <C value="85.55" />
-  <D value="-5060.2" />
-  <Tmin units="K"  value="231.51" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.018788" />
-  <B value="-54.761" />
-  <C value="-1.2916" />
-  <D value="-0.00062226" />
-  <E value="-0.0000029942" />
-  <Tmin units="K"  value="231.51" />
-  <Tmax units="K"  value="563.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-7052.4" />
-  <B value="0.17223" />
-  <C value="-5.768E+07" />
-  <D value="-1.624E+11" />
-  <Tmin units="K"  value="366.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011563" />
-  <B value="125.96" />
-  <C value="-3.6937" />
-  <D value="0.0030162" />
-  <E value="-0.0000074304" />
-  <Tmin units="K"  value="231.51" />
-  <Tmax units="K"  value="619.95" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-29142" />
-  <B value="410.64" />
-  <C value="-0.14517" />
-  <D value="-0.00013262" />
-  <E value="9.121E-08" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-12.907" />
-  <B value="-6630" />
-  <C value="-39.78" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.746" />
-  <B value="2867.3" />
-  <C value="-77.074" />
-  <Tmin units="K"  value="372.6" />
-  <Tmax units="K"  value="555.37" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.2319" />
-  <B value="-0.040488" />
-  <C value="0.000043237" />
-  <Tmin units="K"  value="231.53" />
-  <Tmax units="K"  value="495.96" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.241529" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.763807E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="348.9357" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269325" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="77.29" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.32187" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0357" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.98877" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.238898" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0808341" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.16" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.84706" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.238898" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21804.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0808341" />
-<UnifacVLE name="UNIFAC" >
-  <group id="38"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="50"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="47"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="38"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="38"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="196"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-86-1" />
-<Smiles name="SMILES"  value="n1ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="309" />
-<CompoundID name="Name"  value="Isoprene" />
-<StructureFormula name="Structure"  value="CH2C(CH3)CHCH2" />
-<Family name="Family"  value="14" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="484" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3850030" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.276" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="307.205" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="127.27" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="127.27" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00247682" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="68.117" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.100775" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.158323" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.213E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15330" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.3391E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05103" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.53E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="7.57304E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.45896E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="315641" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4924570" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.58571" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.98424E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.48" />
-  <B value="-0.013452" />
-  <Tmin units="K"  value="50.91" />
-  <Tmax units="K"  value="127.27" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.95762" />
-  <B value="0.265" />
-  <C value="484" />
-  <D value="0.28587" />
-  <Tmin units="K"  value="127.27" />
-  <Tmax units="K"  value="465.22" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.64382" />
-  <B value="-4808.579" />
-  <C value="-5.723014" />
-  <D value="3.325462E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="127.27" />
-  <Tmax units="K"  value="484" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.7482E+07" />
-  <B value="1.7472" />
-  <C value="-3.7153" />
-  <D value="4.0508" />
-  <E value="-1.6134" />
-  <Tmin units="K"  value="127.27" />
-  <Tmax units="K"  value="465.22" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16398" />
-  <B value="1662.9" />
-  <C value="-14.306" />
-  <D value="0.058927" />
-  <E value="-0.000016497" />
-  <Tmin units="K"  value="20.39" />
-  <Tmax units="K"  value="115.35" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="111430" />
-  <B value="579.88" />
-  <C value="0.11179" />
-  <D value="0.042713" />
-  <E value="-0.000046991" />
-  <Tmin units="K"  value="130.32" />
-  <Tmax units="K"  value="307.2" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="46067" />
-  <B value="-400.72" />
-  <C value="12.189" />
-  <D value="0.00043981" />
-  <E value="-1.4681E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16606" />
-  <B value="-184.38" />
-  <C value="-17.394" />
-  <D value="5931.3" />
-  <E value="-15000" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.3004" />
-  <B value="457.06" />
-  <C value="-0.22583" />
-  <D value="-0.0000048674" />
-  <E value="2" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="307.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.2484E-07" />
-  <B value="0.58768" />
-  <C value="291.05" />
-  <D value="-6176.5" />
-  <Tmin units="K"  value="307.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0093138" />
-  <B value="-47.475" />
-  <C value="-0.82654" />
-  <D value="-0.0037828" />
-  <E value="8.2245E-07" />
-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="307.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0010775" />
-  <B value="0.73105" />
-  <C value="657.17" />
-  <D value="112780" />
-  <Tmin units="K"  value="307.21" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011474" />
-  <B value="19.002" />
-  <C value="-3.0114" />
-  <D value="-0.00040883" />
-  <E value="-0.000005756" />
-  <Tmin units="K"  value="127.27" />
-  <Tmax units="K"  value="465.22" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="5017.2" />
-  <B value="394.61" />
-  <C value="-0.22753" />
-  <D value="0.000050803" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.515" />
-  <B value="2346.3" />
-  <C value="-46.175" />
-  <Tmin units="K"  value="293.36" />
-  <Tmax units="K"  value="427.67" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.485" />
-  <B value="-0.018048" />
-  <C value="0.000015516" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="307.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2691" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.006525E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="261.5367" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="97.98" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.99129" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0361" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.684846" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.17" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.100775" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.36" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.01" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.023298" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.31457" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.1642" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15333.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.100775" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  <group id="7"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  <group id="8"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  <group id="7"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  <group id="7"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  <group id="7"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="78-79-5" />
-<Smiles name="SMILES"  value="C=C(C)C=C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="104" />
-<CompoundID name="Name"  value="Cyclopentane" />
-<StructureFormula name="Structure"  value="-(CH2)5-" />
-<Family name="Family"  value="5" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="511.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4508000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.26" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.276" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="322.38" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="179.311" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="179.28" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="9.07217" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09473" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.194" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.85E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16550" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04969" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.75E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.703E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.885E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="292900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="608800" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.77594" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.0709E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.24" />
-  <B value="-0.010626" />
-  <Tmin units="K"  value="71.71" />
-  <Tmax units="K"  value="179.28" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.92461" />
-  <B value="0.26305" />
-  <C value="511.77" />
-  <D value="0.22002" />
-  <Tmin units="K"  value="179.28" />
-  <Tmax units="K"  value="511.76" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-74.77148" />
-  <B value="-401.0576" />
-  <C value="15.6271" />
-  <D value="-0.0000260872" />
-  <E value="2" />
-  <Tmin units="K"  value="179.28" />
-  <Tmax units="K"  value="511.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.513618E+07" />
-  <B value="1.248318" />
-  <C value="-2.311302" />
-  <D value="2.401073" />
-  <E value="-0.943348" />
-  <Tmin units="K"  value="179.28" />
-  <Tmax units="K"  value="494.2" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-39074" />
-  <B value="2770.3" />
-  <C value="-35.305" />
-  <D value="0.22637" />
-  <E value="-0.000515" />
-  <Tmin units="K"  value="26.16" />
-  <Tmax units="K"  value="163.83" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84725" />
-  <B value="368.5" />
-  <C value="3.0559" />
-  <D value="0.030633" />
-  <E value="-0.000031124" />
-  <Tmin units="K"  value="179.28" />
-  <Tmax units="K"  value="322.4" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39785" />
-  <B value="-704.2" />
-  <C value="13.082" />
-  <D value="-0.00014913" />
-  <E value="2.4491E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.14457" />
-  <B value="-136.77" />
-  <C value="-19.525" />
-  <D value="1064.5" />
-  <E value="-3861.2" />
-  <Tmin units="K"  value="255.8" />
-  <Tmax units="K"  value="1790.6" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-5.1843" />
-  <B value="670.87" />
-  <C value="-0.84082" />
-  <D value="-7.0656E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="325" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.1433E-07" />
-  <B value="0.68815" />
-  <C value="135.42" />
-  <D value="-1597.6" />
-  <Tmin units="K"  value="179.28" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10961" />
-  <B value="-598.59" />
-  <C value="3.5098" />
-  <D value="-0.016258" />
-  <E value="-0.0000091635" />
-  <Tmin units="K"  value="179.28" />
-  <Tmax units="K"  value="322.4" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000098408" />
-  <B value="1.4611" />
-  <C value="639.53" />
-  <D value="7396.1" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0069318" />
-  <B value="73.276" />
-  <C value="-3.5449" />
-  <D value="0.0024935" />
-  <E value="-0.000011185" />
-  <Tmin units="K"  value="179.28" />
-  <Tmax units="K"  value="494.2" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="41730" />
-  <B value="-164.08" />
-  <C value="1.4897" />
-  <D value="-0.0018039" />
-  <E value="6.8303E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.4825" />
-  <B value="-1000" />
-  <C value="-6" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.116" />
-  <B value="2809.4" />
-  <C value="-29.479" />
-  <Tmin units="K"  value="310.22" />
-  <Tmax units="K"  value="459.21" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.2213" />
-  <B value="-0.033291" />
-  <C value="0.000037759" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="325" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.26001" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.582283E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="324.4265" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2687" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="102.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.036" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.748874" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.19686" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0935089" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.3" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.47" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003383" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2051" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16589.01" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0947" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="5" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="5" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="13"  value="5" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="2"  value="5" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="2"  value="5" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="78"  value="5" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="287-92-3" />
-<Smiles name="SMILES"  value="C1CCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="212" />
-<CompoundID name="Name"  value="2-methyl-1-butene" />
-<StructureFormula name="Structure"  value="CH2C(CH3)CH2CH3" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="465" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3447000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.292" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="304.305" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="135.578" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="135.578" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0205382" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.1329" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10872" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.234056" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.287E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14700" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.7E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05452" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.06E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.53E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.668E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="339500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7910700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.83569" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.1159E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.346" />
-  <B value="-0.01138" />
-  <Tmin units="K"  value="54.23" />
-  <Tmax units="K"  value="135.58" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.91622" />
-  <B value="0.26752" />
-  <C value="465" />
-  <D value="0.28165" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="465" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="77.29304" />
-  <B value="-5304.146" />
-  <C value="-8.607604" />
-  <D value="9.513458E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="465" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.6374E+07" />
-  <B value="1.4214" />
-  <C value="-2.5789" />
-  <D value="2.5516" />
-  <E value="-0.95454" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="465" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-17830" />
-  <B value="1684.7" />
-  <C value="-14.234" />
-  <D value="0.073506" />
-  <E value="-0.00014133" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="135.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="121560" />
-  <B value="527.31" />
-  <C value="1.2291" />
-  <D value="0.036295" />
-  <E value="-0.000037525" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="304.31" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81218" />
-  <B value="-803.24" />
-  <C value="13.077" />
-  <D value="-0.00034159" />
-  <E value="9.7536E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16678" />
-  <B value="-164.7" />
-  <C value="-17.388" />
-  <D value="-73.693" />
-  <E value="-374.88" />
-  <Tmin units="K"  value="232.5" />
-  <Tmax units="K"  value="1860" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.065" />
-  <B value="690.04" />
-  <C value="-0.13044" />
-  <D value="0.0000004745" />
-  <E value="2" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="304.3" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.0873E-07" />
-  <B value="0.55006" />
-  <C value="197.77" />
-  <D value="-68.455" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.024046" />
-  <B value="2.4654" />
-  <C value="-1.5931" />
-  <D value="-0.00074325" />
-  <E value="-0.0000024745" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="304.3" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00018088" />
-  <B value="0.94101" />
-  <C value="77.857" />
-  <D value="153680" />
-  <Tmin units="K"  value="304.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0087828" />
-  <B value="42.635" />
-  <C value="-3.4174" />
-  <D value="0.001427" />
-  <E value="-0.0000096911" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="465" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-289.0224" />
-  <B value="434.7176" />
-  <C value="-0.232806" />
-  <D value="0.0000469361" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.951" />
-  <B value="2552.6" />
-  <C value="-33.481" />
-  <Tmin units="K"  value="280.07" />
-  <Tmax units="K"  value="412.99" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.24348" />
-  <B value="-0.050824" />
-  <C value="0.000078622" />
-  <Tmin units="K"  value="135.58" />
-  <Tmax units="K"  value="304.3" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2887" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.233585E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="237.8319" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.270022" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="102.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.06763" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0387" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.65438" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.23544" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10868" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5939" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.224" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.00351" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.08406" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.228663" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14695.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.10868" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="563-46-2" />
-<Smiles name="SMILES"  value="C=C(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="213" />
-<CompoundID name="Name"  value="3-methyl-1-butene" />
-<StructureFormula name="Structure"  value="CH2CHCH(CH3)CH3" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="452.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3550000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3049" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.288" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="293.21" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="104.66" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="104.66" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000144678" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.11277" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.211" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.272E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13780" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05453" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.75E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.76E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.605E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="333900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5359700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.82876" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.1253E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.464" />
-  <B value="-0.015739" />
-  <Tmin units="K"  value="41.86" />
-  <Tmax units="K"  value="104.66" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.85968" />
-  <B value="0.26229" />
-  <C value="452.7" />
-  <D value="0.27579" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="434.38" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="74.66163" />
-  <B value="-4956.256" />
-  <C value="-8.290047" />
-  <D value="0.0000100425" />
-  <E value="2" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="452.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.9174E+07" />
-  <B value="0.58094" />
-  <C value="0.12579" />
-  <D value="-0.78785" />
-  <E value="0.49354" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="434.38" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-31134" />
-  <B value="2580.1" />
-  <C value="-35.586" />
-  <D value="0.27843" />
-  <E value="-0.00080931" />
-  <Tmin units="K"  value="29.5" />
-  <Tmax units="K"  value="104.71" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94996" />
-  <B value="92.422" />
-  <C value="8.4061" />
-  <D value="0.009093" />
-  <E value="-0.0000045826" />
-  <Tmin units="K"  value="103.08" />
-  <Tmax units="K"  value="300" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="82557" />
-  <B value="-671.08" />
-  <C value="12.784" />
-  <D value="-0.00012458" />
-  <E value="4.234E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17117" />
-  <B value="-168.7" />
-  <C value="-14.362" />
-  <D value="-474.16" />
-  <E value="518.37" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="1841" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.214" />
-  <B value="821.55" />
-  <C value="-0.010133" />
-  <D value="9.4673E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="362.16" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000016555" />
-  <B value="0.42535" />
-  <C value="455.3" />
-  <D value="876.91" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.017622" />
-  <B value="5.9209" />
-  <C value="-1.694" />
-  <D value="-0.00045405" />
-  <E value="-0.0000033564" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="293.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00014816" />
-  <B value="0.97375" />
-  <C value="75.281" />
-  <D value="116540" />
-  <Tmin units="K"  value="293.21" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01585" />
-  <B value="5.8469" />
-  <C value="-2.8491" />
-  <D value="-0.0010934" />
-  <E value="-0.0000040903" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="434.38" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="17527" />
-  <B value="348.48" />
-  <C value="-0.034588" />
-  <D value="-0.00016105" />
-  <E value="7.932E-08" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.734" />
-  <B value="2400.8" />
-  <C value="-32.491" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="397.75" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.3377" />
-  <B value="-0.058937" />
-  <C value="0.000086079" />
-  <Tmin units="K"  value="104.66" />
-  <Tmax units="K"  value="362.16" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.29398" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.593622E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="334.6082" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272045" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="102.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0389" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.63127" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2266" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.111819" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5945" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.1" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.011281" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2285" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14010.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.111819" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="563-45-1" />
-<Smiles name="SMILES"  value="C=CC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="214" />
-<CompoundID name="Name"  value="2-methyl-2-butene" />
-<StructureFormula name="Structure"  value="CH3CHC(CH3)CH3" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="470" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3860000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.292" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.288" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="311.7" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="139.39" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="139.39" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.01937" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10757" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.339" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.281E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15210" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.13E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05449" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.05E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.18E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.045E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="338600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7597700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91429" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.1088E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.146" />
-  <B value="-0.010308" />
-  <Tmin units="K"  value="55.76" />
-  <Tmax units="K"  value="139.39" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.93623" />
-  <B value="0.2731" />
-  <C value="470" />
-  <D value="0.25849" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="470" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.2327" />
-  <B value="-5590.502" />
-  <C value="-9.366663" />
-  <D value="0.0000104545" />
-  <E value="2" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="470" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.3456E+07" />
-  <B value="0.64226" />
-  <C value="-0.070051" />
-  <D value="-0.5395" />
-  <E value="0.35656" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="470" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16158" />
-  <B value="1388.9" />
-  <C value="-5.5663" />
-  <D value="0.0010355" />
-  <E value="0.000064486" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="139.4" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="127040" />
-  <B value="1071.7" />
-  <C value="-7.883" />
-  <D value="0.075072" />
-  <E value="-0.000089164" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="311.71" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="75343" />
-  <B value="-774.17" />
-  <C value="12.975" />
-  <D value="-0.00022009" />
-  <E value="6.0763E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15944" />
-  <B value="-148.27" />
-  <C value="-25.542" />
-  <D value="2329.9" />
-  <E value="-6400.9" />
-  <Tmin units="K"  value="235" />
-  <Tmax units="K"  value="1880" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.234" />
-  <B value="703.42" />
-  <C value="0.094871" />
-  <D value="-0.0000017625" />
-  <E value="2" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="311.7" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.6256E-07" />
-  <B value="0.47637" />
-  <C value="263.56" />
-  <D value="-2475.7" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.050847" />
-  <B value="3.0532" />
-  <C value="-1.4724" />
-  <D value="-0.00063704" />
-  <E value="-0.0000020121" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="311.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00020806" />
-  <B value="0.92265" />
-  <C value="107.34" />
-  <D value="175680" />
-  <Tmin units="K"  value="311.71" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01137" />
-  <B value="35.757" />
-  <C value="-3.2605" />
-  <D value="0.00094463" />
-  <E value="-0.0000079469" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="470" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="10310" />
-  <B value="326.78" />
-  <C value="0.022449" />
-  <D value="-0.00020786" />
-  <E value="9.3122E-08" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.057" />
-  <B value="2659.5" />
-  <C value="-32.673" />
-  <Tmin units="K"  value="282.62" />
-  <Tmax units="K"  value="417.8" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.6872" />
-  <B value="-0.046426" />
-  <C value="0.000068039" />
-  <Tmin units="K"  value="139.39" />
-  <Tmax units="K"  value="311.7" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2883" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.513596E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="347.3953" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.260813" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="102.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.00916" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0386" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.666109" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.28518" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.106707" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5919" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.22" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004255" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.46734" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.27667" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15247.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.106707" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="8"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="7"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="8"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="8"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="8"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="513-35-9" />
-<Smiles name="SMILES"  value="CC(C)=CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="209" />
-<CompoundID name="Name"  value="1-pentene" />
-<StructureFormula name="Structure"  value="CH2CH(CH2)2CH3" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="464.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3560000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2984" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="303.11" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="108.016" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="108.016" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000037" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1104" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.237" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.231E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14410" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.7E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05454" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.76E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.162E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.837E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="346200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5937400" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.85507" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.13037E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.614" />
-  <B value="-0.014969" />
-  <Tmin units="K"  value="43.21" />
-  <Tmax units="K"  value="108.02" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.44335" />
-  <B value="0.18566" />
-  <C value="473.43" />
-  <D value="0.23587" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="473.42" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="39.52954" />
-  <B value="-3893.399" />
-  <C value="-2.686504" />
-  <D value="1.952359E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="465.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.077277E+07" />
-  <B value="-0.570706" />
-  <C value="2.243398" />
-  <D value="-2.258065" />
-  <E value="0.928488" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="464.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-9888.9" />
-  <B value="900.04" />
-  <C value="11.178" />
-  <D value="-0.22603" />
-  <E value="0.0010726" />
-  <Tmin units="K"  value="11" />
-  <Tmax units="K"  value="108.02" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="92753" />
-  <B value="117.21" />
-  <C value="8.6537" />
-  <D value="0.007447" />
-  <E value="-0.0000026759" />
-  <Tmin units="K"  value="107.9" />
-  <Tmax units="K"  value="372" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66520" />
-  <B value="-609.44" />
-  <C value="12.683" />
-  <D value="0.000062395" />
-  <E value="-2.5354E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20469" />
-  <B value="-223.9" />
-  <C value="-8.6984" />
-  <D value="-4100.9" />
-  <E value="7778.7" />
-  <Tmin units="K"  value="228" />
-  <Tmax units="K"  value="1858.96" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.79591" />
-  <B value="682.8004" />
-  <C value="0.00564316" />
-  <D value="-9.176806E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="303.22" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000017549" />
-  <B value="0.42295" />
-  <C value="561.21" />
-  <D value="-17046" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.010825" />
-  <B value="-30.065" />
-  <C value="-1.1172" />
-  <D value="-0.0023327" />
-  <E value="-0.0000015541" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="423.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000026412" />
-  <B value="1.549" />
-  <C value="-2.5891" />
-  <D value="24389" />
-  <Tmin units="K"  value="303.22" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011552" />
-  <B value="7.0878" />
-  <C value="-2.8382" />
-  <D value="-0.0011232" />
-  <E value="-0.0000052785" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="464.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="42229" />
-  <B value="99.1" />
-  <C value="0.65169" />
-  <D value="-0.00091143" />
-  <E value="3.6426E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.56045" />
-  <B value="-1050" />
-  <C value="-6.3" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.064" />
-  <B value="2629.6" />
-  <C value="-27.471" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="413.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.34306" />
-  <B value="-0.057696" />
-  <C value="0.000095563" />
-  <Tmin units="K"  value="108.02" />
-  <Tmax units="K"  value="303.22" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2951" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.870098E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="290.9223" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2944" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="102.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.01383" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0391" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.638723" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2824" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.110474" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5953" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.104" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.00367" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.37379" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2198" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14420.78" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1104" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-67-1" />
-<Smiles name="SMILES"  value="C=CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="210" />
-<CompoundID name="Name"  value="Cis-2-pentene" />
-<StructureFormula name="Structure"  value="CH3CHCHCH2CH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="475" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3690000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3021" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="310.07" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="121.75" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="121.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000554" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10785" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.253" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.33E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15060" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.008E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05451" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.75E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.63E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.37E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="346300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7112000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.84852" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.123E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.871" />
-  <B value="-0.013598" />
-  <Tmin units="K"  value="48.7" />
-  <Tmax units="K"  value="121.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.90921" />
-  <B value="0.26313" />
-  <C value="475" />
-  <D value="0.30422" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="475" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="87.54937" />
-  <B value="-5782.462" />
-  <C value="-10.18969" />
-  <D value="0.00001126" />
-  <E value="2" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="475" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.808893E+07" />
-  <B value="0.541071" />
-  <C value="-0.876512" />
-  <D value="1.300916" />
-  <E value="-0.612383" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="475" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13230" />
-  <B value="1127" />
-  <C value="1.3684" />
-  <D value="-0.072985" />
-  <E value="0.00034019" />
-  <Tmin units="K"  value="13.51" />
-  <Tmax units="K"  value="121.78" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="132080" />
-  <B value="-10569" />
-  <C value="112.64" />
-  <D value="-0.34846" />
-  <E value="0.00041161" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="310.08" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68358" />
-  <B value="-741.07" />
-  <C value="12.923" />
-  <D value="-0.00013529" />
-  <E value="3.1324E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17521" />
-  <B value="-182.66" />
-  <C value="-16.753" />
-  <D value="-994" />
-  <E value="1468.3" />
-  <Tmin units="K"  value="238" />
-  <Tmax units="K"  value="1904" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.01" />
-  <B value="644.41" />
-  <C value="-0.11124" />
-  <D value="1.3682E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="310.08" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.0321E-08" />
-  <B value="0.83123" />
-  <C value="33.115" />
-  <D value="-394.35" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.06994" />
-  <B value="-6.3331" />
-  <C value="-1.1883" />
-  <D value="-0.0013351" />
-  <E value="-7.8623E-07" />
-  <Tmin units="K"  value="120" />
-  <Tmax units="K"  value="310.08" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00017973" />
-  <B value="0.95148" />
-  <C value="124.65" />
-  <D value="170420" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010506" />
-  <B value="20.208" />
-  <C value="-3.0727" />
-  <D value="0.0001059" />
-  <E value="-0.0000070674" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="475" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="24120" />
-  <B value="264.28" />
-  <C value="0.15315" />
-  <D value="-0.00032867" />
-  <E value="1.3378E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.878" />
-  <B value="2544.1" />
-  <C value="-38.058" />
-  <Tmin units="K"  value="285.51" />
-  <Tmax units="K"  value="419.22" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.36839" />
-  <B value="-0.050845" />
-  <C value="0.000079655" />
-  <Tmin units="K"  value="121.75" />
-  <Tmax units="K"  value="310.08" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.28749" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.946116E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="289.5959" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="102.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.02929" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.039" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.659575" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.24255" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10792" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5933" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.103" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.00233" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.13212" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.206" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14420.78" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1078" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="627-20-3" />
-<Smiles name="SMILES"  value="C/C=C\CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="211" />
-<CompoundID name="Name"  value="Trans-2-pentene" />
-<StructureFormula name="Structure"  value="CH3CHCHCH2CH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="474.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3660000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.293" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="309.49" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="132.89" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="132.89" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00574" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="70.1329" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1091" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.248372" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.28E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14970" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05451" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.75E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.11E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.98E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="343100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8351700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.84315" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.119E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.26" />
-  <B value="-0.011808" />
-  <Tmin units="K"  value="53.16" />
-  <Tmax units="K"  value="132.89" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.9122" />
-  <B value="0.26869" />
-  <C value="474.2" />
-  <D value="0.28253" />
-  <Tmin units="K"  value="132.89" />
-  <Tmax units="K"  value="474.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="77.717" />
-  <B value="-5422.6" />
-  <C value="-8.6403" />
-  <D value="0.0000092035" />
-  <E value="2" />
-  <Tmin units="K"  value="132.89" />
-  <Tmax units="K"  value="474.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.3712E+07" />
-  <B value="0.84137" />
-  <C value="-0.81266" />
-  <D value="0.47134" />
-  <E value="-0.094225" />
-  <Tmin units="K"  value="132.89" />
-  <Tmax units="K"  value="474.2" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12202" />
-  <B value="1040.4" />
-  <C value="1.6545" />
-  <D value="-0.062663" />
-  <E value="0.00025784" />
-  <Tmin units="K"  value="12.77" />
-  <Tmax units="K"  value="132.93" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="117170" />
-  <B value="204.39" />
-  <C value="5.1039" />
-  <D value="0.022516" />
-  <E value="-0.00002152" />
-  <Tmin units="K"  value="132.93" />
-  <Tmax units="K"  value="310" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="79715" />
-  <B value="-780.23" />
-  <C value="12.979" />
-  <D value="-0.00024552" />
-  <E value="0.0000000696" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17394" />
-  <B value="-181.62" />
-  <C value="-16.872" />
-  <D value="-647.46" />
-  <E value="513.41" />
-  <Tmin units="K"  value="203" />
-  <Tmax units="K"  value="1900" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.52" />
-  <B value="657.15" />
-  <C value="-0.02693" />
-  <D value="1.6882E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="132.89" />
-  <Tmax units="K"  value="309.49" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2614E-07" />
-  <B value="0.75299" />
-  <C value="74.21" />
-  <D value="1685.7" />
-  <Tmin units="K"  value="132.89" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.074338" />
-  <B value="-10.004" />
-  <C value="-1.1218" />
-  <D value="-0.0016085" />
-  <E value="-2.2796E-07" />
-  <Tmin units="K"  value="130" />
-  <Tmax units="K"  value="309.49" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000026669" />
-  <B value="1.1894" />
-  <C value="-123.11" />
-  <D value="111540" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0093368" />
-  <B value="32.021" />
-  <C value="-3.2884" />
-  <D value="0.0008863" />
-  <E value="-0.0000084191" />
-  <Tmin units="K"  value="132.89" />
-  <Tmax units="K"  value="474.2" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="2246.808" />
-  <B value="415.4754" />
-  <C value="-0.211798" />
-  <D value="0.0000400409" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.965" />
-  <B value="2590.5" />
-  <C value="-35.057" />
-  <Tmin units="K"  value="284.95" />
-  <Tmax units="K"  value="420.31" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.78372" />
-  <B value="-0.047294" />
-  <C value="0.000072515" />
-  <Tmin units="K"  value="132.89" />
-  <Tmax units="K"  value="309.49" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.29289" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.911778E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="285.3139" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.268765" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="102.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.02405" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0392" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.652263" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.23984" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.109083" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5933" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.103" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001574" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.09675" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.209" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14420.78" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.109" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="646-04-8" />
-<Smiles name="SMILES"  value="C/C=C/CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1053" />
-<CompoundID name="Name"  value="3-pentanone" />
-<StructureFormula name="Structure"  value="CH3CH2COCH2CH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="561.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3730000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.336" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="375.14" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="234.18" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="234.18" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="73.4224" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10641" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.342" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.583E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18410" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.41E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0595" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.579E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.344E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="370000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.159E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.069" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.8804E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.822" />
-  <B value="-0.0061115" />
-  <Tmin units="K"  value="93.67" />
-  <Tmax units="K"  value="234.18" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.68664" />
-  <B value="0.23603" />
-  <C value="561.5" />
-  <D value="0.27471" />
-  <Tmin units="K"  value="234.18" />
-  <Tmax units="K"  value="543.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="58.885" />
-  <B value="-6044.5" />
-  <C value="-5.3259" />
-  <D value="0.0000023057" />
-  <E value="2" />
-  <Tmin units="K"  value="234.18" />
-  <Tmax units="K"  value="560.95" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.083729E+07" />
-  <B value="0.764461" />
-  <C value="-0.828447" />
-  <D value="-0.00277131" />
-  <E value="0.530942" />
-  <Tmin units="K"  value="234.18" />
-  <Tmax units="K"  value="560.95" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-6392" />
-  <B value="777.74" />
-  <C value="17.353" />
-  <D value="-0.29853" />
-  <E value="0.001372" />
-  <Tmin units="K"  value="11.16" />
-  <Tmax units="K"  value="119.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="169130" />
-  <B value="405.25" />
-  <C value="3.0239" />
-  <D value="0.024087" />
-  <E value="-0.000018434" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="93124" />
-  <B value="-637.87" />
-  <C value="12.577" />
-  <D value="0.00022827" />
-  <E value="-1.0612E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.13293" />
-  <B value="-126.32" />
-  <C value="-67.641" />
-  <D value="17238" />
-  <E value="-66712" />
-  <Tmin units="K"  value="280.45" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-1.367" />
-  <B value="550.49" />
-  <C value="-1.4469" />
-  <D value="4.9148E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="234.18" />
-  <Tmax units="K"  value="375.14" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000002611" />
-  <B value="0.65778" />
-  <C value="216.39" />
-  <D value="-3537.8" />
-  <Tmin units="K"  value="234.18" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0080662" />
-  <B value="16.294" />
-  <C value="-1.6509" />
-  <D value="-0.0010676" />
-  <E value="-9.5001E-07" />
-  <Tmin units="K"  value="187.86" />
-  <Tmax units="K"  value="375.14" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="22.162" />
-  <B value="1.0028" />
-  <C value="1.8597E+08" />
-  <D value="9.2842E+08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0083353" />
-  <B value="223.31" />
-  <C value="-5.0336" />
-  <D value="0.0065645" />
-  <E value="-0.000012203" />
-  <Tmin units="K"  value="234.18" />
-  <Tmax units="K"  value="560.95" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="67106" />
-  <B value="113.53" />
-  <C value="0.50885" />
-  <D value="-0.00069318" />
-  <E value="2.7047E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-15.7804" />
-  <B value="-7700" />
-  <C value="-46.2" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.615" />
-  <B value="3357.7" />
-  <C value="-42.268" />
-  <Tmin units="K"  value="337.37" />
-  <Tmax units="K"  value="492.16" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.9137" />
-  <B value="-0.027945" />
-  <C value="0.000028415" />
-  <Tmin units="K"  value="234.18" />
-  <Tmax units="K"  value="375.14" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3188" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.298875E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="320.2936" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="108.71" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.45383" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0426" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.806" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.34599" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.106401" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9223" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.416" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.59305" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.344" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18259.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.106401" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="20"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="20"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="20"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="19"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="96-22-0" />
-<Smiles name="SMILES"  value="CCC(=O)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1061" />
-<CompoundID name="Name"  value="Methyl isopropyl ketone" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)COCH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="567.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3620000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.31" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.238" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="367.55" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="180.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="180.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.295357" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10791" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.216" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.465E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17710" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.21E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05949" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.53E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.626E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.393E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="369900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9343000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97206" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.877E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.23" />
-  <B value="-0.0077997" />
-  <Tmin units="K"  value="72.06" />
-  <Tmax units="K"  value="181.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.22922" />
-  <B value="0.13849" />
-  <C value="567.7" />
-  <D value="0.18207" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="533.76" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="57.033" />
-  <B value="-5794.3" />
-  <C value="-5.09" />
-  <D value="0.0000023975" />
-  <E value="2" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="553.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.3282E+07" />
-  <B value="-7.596951" />
-  <C value="21.963" />
-  <D value="-24.77369" />
-  <E value="10.66731" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="553.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10888" />
-  <B value="1207.3" />
-  <C value="-2.162" />
-  <D value="-0.01776" />
-  <E value="0.00010358" />
-  <Tmin units="K"  value="11.38" />
-  <Tmax units="K"  value="168.93" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="142840" />
-  <B value="463.87" />
-  <C value="4.1439" />
-  <D value="0.020347" />
-  <E value="-0.000013989" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="440" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65899" />
-  <B value="-628.39" />
-  <C value="12.858" />
-  <D value="0.000023331" />
-  <E value="-5.0246E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15924" />
-  <B value="-129.27" />
-  <C value="-49.269" />
-  <D value="147.14" />
-  <E value="-29532" />
-  <Tmin units="K"  value="276.7" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.042" />
-  <B value="1043.1" />
-  <C value="-0.038423" />
-  <D value="1.1535E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="367.55" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.5484E-07" />
-  <B value="0.72865" />
-  <C value="149.15" />
-  <D value="-3826.1" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.11038" />
-  <B value="18.412" />
-  <C value="-1.2824" />
-  <D value="-0.000057222" />
-  <E value="-0.000001541" />
-  <Tmin units="K"  value="165.9" />
-  <Tmax units="K"  value="435.9" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-6058400" />
-  <B value="-0.090573" />
-  <C value="3.176E+09" />
-  <D value="-2.84E+13" />
-  <Tmin units="K"  value="367.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.034236" />
-  <B value="-71.227" />
-  <C value="-1.6594" />
-  <D value="-0.0035924" />
-  <E value="0.00000136" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="553.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-2912.064" />
-  <B value="498.7328" />
-  <C value="-0.293257" />
-  <D value="0.0000666093" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.404" />
-  <B value="3959.7" />
-  <C value="-3.419" />
-  <Tmin units="K"  value="346.95" />
-  <Tmax units="K"  value="494.47" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0599" />
-  <B value="-0.046952" />
-  <C value="0.00005801" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="367.55" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3156" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.070876E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="211.2074" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="108.71" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0421" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.814223" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3323" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.106975" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9215" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.412" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.350039" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18253.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.106975" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="563-80-4" />
-<Smiles name="SMILES"  value="CC(=O)C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1314" />
-<CompoundID name="Name"  value="N-propyl acetate" />
-<StructureFormula name="Structure"  value="CH3COO(CH2)2CH3" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="549.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3330000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.345" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="374.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="178.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="178.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0171129" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.133" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.11572" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.389" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.969E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17890" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.97E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.063" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.14E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.648E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.204E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="402300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.12E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1143" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.672E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.418" />
-  <B value="-0.0076611" />
-  <Tmin units="K"  value="71.26" />
-  <Tmax units="K"  value="178.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.57751" />
-  <B value="0.2255" />
-  <C value="549.4" />
-  <D value="0.25884" />
-  <Tmin units="K"  value="178.15" />
-  <Tmax units="K"  value="549.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="106.6613" />
-  <B value="-8095.022" />
-  <C value="-12.62161" />
-  <D value="8.999471E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="178.15" />
-  <Tmax units="K"  value="549.73" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.047503E+07" />
-  <B value="1.798019" />
-  <C value="-2.259874" />
-  <D value="1.293466" />
-  <E value="-0.333711" />
-  <Tmin units="K"  value="178.15" />
-  <Tmax units="K"  value="549.35" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="156890" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="124410" />
-  <B value="36.932" />
-  <C value="8.3883" />
-  <D value="0.012662" />
-  <E value="-0.000012028" />
-  <Tmin units="K"  value="192.29" />
-  <Tmax units="K"  value="404.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="108820" />
-  <B value="-937.38" />
-  <C value="13.511" />
-  <D value="-0.00062962" />
-  <E value="1.4249E-07" />
-  <Tmin units="K"  value="246.45" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18145" />
-  <B value="-204.54" />
-  <C value="-46.716" />
-  <D value="-11288" />
-  <E value="16065" />
-  <Tmin units="K"  value="274.7" />
-  <Tmax units="K"  value="1922.9" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="15.453" />
-  <B value="-157.9" />
-  <C value="-3.9304" />
-  <D value="-3.2102E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9633E-07" />
-  <B value="0.69295" />
-  <C value="104.27" />
-  <D value="10438" />
-  <Tmin units="K"  value="178.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.045513" />
-  <B value="-31.328" />
-  <C value="-1.5572" />
-  <D value="-0.00066538" />
-  <E value="-0.0000053334" />
-  <Tmin units="K"  value="164.82" />
-  <Tmax units="K"  value="434.82" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1128.5" />
-  <B value="1.014" />
-  <C value="1.1605E+10" />
-  <D value="-1.2869E+11" />
-  <Tmin units="K"  value="374.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012713" />
-  <B value="36.014" />
-  <C value="-3.0794" />
-  <D value="0.00042548" />
-  <E value="-0.0000053616" />
-  <Tmin units="K"  value="178.15" />
-  <Tmax units="K"  value="530.17" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="10223" />
-  <B value="486.13" />
-  <C value="-0.25647" />
-  <D value="0.000046499" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.185871" />
-  <B value="-3150" />
-  <C value="-18.9" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.084" />
-  <B value="2976" />
-  <C value="-63.384" />
-  <Tmin units="K"  value="331.31" />
-  <Tmax units="K"  value="493.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.1165" />
-  <B value="-0.017929" />
-  <C value="0.000010882" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.34279" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.841805E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="251.0983" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="114.82" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.46308" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0454" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.892752" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.391" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.115712" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.153" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.656" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.147" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.391" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18004.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.115712" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-60-4" />
-<Smiles name="SMILES"  value="CC(=O)OCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="8" />
-<CompoundID name="Name"  value="Isopentane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CH2CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="460.39" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3381000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3083" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="300.99" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="113.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="113.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00012144" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.15" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.11646" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.229" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.324E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13870" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.34E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05802" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.28E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.537E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.405E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="343740" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5150000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.88771" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.23954E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.656" />
-  <B value="-0.013374" />
-  <Tmin units="K"  value="45.3" />
-  <Tmax units="K"  value="113.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.73194" />
-  <B value="0.24835" />
-  <C value="460.99" />
-  <D value="0.25733" />
-  <Tmin units="K"  value="113.15" />
-  <Tmax units="K"  value="460.98" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="71.04288" />
-  <B value="-4967.235" />
-  <C value="-7.674379" />
-  <D value="8.659929E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="113.25" />
-  <Tmax units="K"  value="460.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.14248E+07" />
-  <B value="0.799342" />
-  <C value="-0.581969" />
-  <D value="0.0834724" />
-  <E value="0.117826" />
-  <Tmin units="K"  value="113.25" />
-  <Tmax units="K"  value="460.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-9226.8" />
-  <B value="944.22" />
-  <C value="12.156" />
-  <D value="-0.25376" />
-  <E value="0.0012526" />
-  <Tmin units="K"  value="13" />
-  <Tmax units="K"  value="113.36" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="112460" />
-  <B value="-54.259" />
-  <C value="8.8747" />
-  <D value="0.0083911" />
-  <E value="-0.0000034773" />
-  <Tmin units="K"  value="113.25" />
-  <Tmax units="K"  value="310" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="59843" />
-  <B value="-493.27" />
-  <C value="12.516" />
-  <D value="0.00046099" />
-  <E value="-1.5305E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16392" />
-  <B value="-173.55" />
-  <C value="-19.026" />
-  <D value="1021.5" />
-  <E value="-2755.1" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="1841.56" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.596" />
-  <B value="889.14" />
-  <C value="0.20472" />
-  <D value="4.0592E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="310" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.6346E-08" />
-  <B value="0.82828" />
-  <C value="-68.082" />
-  <D value="25303" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.061061" />
-  <B value="89.857" />
-  <C value="-3.522" />
-  <D value="0.0075154" />
-  <E value="-0.000023032" />
-  <Tmin units="K"  value="113.25" />
-  <Tmax units="K"  value="368.13" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00090019" />
-  <B value="0.7738" />
-  <C value="456.82" />
-  <D value="231390" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014311" />
-  <B value="8.316" />
-  <C value="-2.8974" />
-  <D value="-0.00090151" />
-  <E value="-0.0000046238" />
-  <Tmin units="K"  value="113.25" />
-  <Tmax units="K"  value="442.13" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="16288" />
-  <B value="317.54" />
-  <C value="0.20237" />
-  <D value="-0.00043027" />
-  <E value="1.8001E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.366" />
-  <B value="-925" />
-  <C value="-5.55" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.89" />
-  <B value="2541.9" />
-  <C value="-29.563" />
-  <Tmin units="K"  value="276.92" />
-  <Tmax units="K"  value="410" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.49033" />
-  <B value="-0.05312" />
-  <C value="0.00007775" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="310" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.30959" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.012938E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="277.0048" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2716" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="107.22" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.50468" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0408" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.623442" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.23995" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.117098" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.82" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.31" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005345" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.94255" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2104" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14359.41" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1174" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="78-78-4" />
-<Smiles name="SMILES"  value="CC(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="7" />
-<CompoundID name="Name"  value="N-pentane" />
-<StructureFormula name="Structure"  value="CH3(CH2)3CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="469.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3370000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.311" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="309.22" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="143.42" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="143.42" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0686418" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.15" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.11522" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.251" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.337E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14380" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05803" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.29E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.4676E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-8813000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="349450" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8401500" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.92983" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.24494E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.533" />
-  <B value="-0.006061" />
-  <Tmin units="K"  value="23.15" />
-  <Tmax units="K"  value="143.46" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77386" />
-  <B value="0.25574" />
-  <C value="469.7" />
-  <D value="0.26319" />
-  <Tmin units="K"  value="143.42" />
-  <Tmax units="K"  value="469.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="72.14242" />
-  <B value="-5265.589" />
-  <C value="-7.720709" />
-  <D value="7.151866E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="143.42" />
-  <Tmax units="K"  value="469.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.0854E+07" />
-  <B value="0.25483" />
-  <C value="0.96045" />
-  <D value="-1.5349" />
-  <E value="0.72504" />
-  <Tmin units="K"  value="143.42" />
-  <Tmax units="K"  value="469.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10054" />
-  <B value="1010.4" />
-  <C value="4.2663" />
-  <D value="-0.10165" />
-  <E value="0.00042186" />
-  <Tmin units="K"  value="12.29" />
-  <Tmax units="K"  value="134.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122980" />
-  <B value="401.5" />
-  <C value="3.9651" />
-  <D value="0.024056" />
-  <E value="-0.000020161" />
-  <Tmin units="K"  value="143.42" />
-  <Tmax units="K"  value="390" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81062" />
-  <B value="-706.86" />
-  <C value="12.962" />
-  <D value="-0.000049298" />
-  <E value="2.8357E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17575" />
-  <B value="-176.68" />
-  <C value="-20.64" />
-  <D value="923.52" />
-  <E value="-3199.2" />
-  <Tmin units="K"  value="217" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-28.93847" />
-  <B value="1176.355" />
-  <C value="3.050544" />
-  <D value="-9.721368E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="137.15" />
-  <Tmax units="K"  value="465.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.9173E-08" />
-  <B value="0.85109" />
-  <C value="8.4138" />
-  <D value="3723.2" />
-  <Tmin units="K"  value="143.42" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.023649" />
-  <B value="-75.089" />
-  <C value="-0.64229" />
-  <D value="-0.005078" />
-  <E value="-2.7196E-07" />
-  <Tmin units="K"  value="143.42" />
-  <Tmax units="K"  value="445" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-603.2" />
-  <B value="0.74698" />
-  <C value="-8.1823E+08" />
-  <D value="-8.7865E+09" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013012" />
-  <B value="17.72" />
-  <C value="-3.0334" />
-  <D value="-0.00028732" />
-  <E value="-0.0000056151" />
-  <Tmin units="K"  value="143.42" />
-  <Tmax units="K"  value="452.53" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="62808" />
-  <B value="-3.0597" />
-  <C value="0.98493" />
-  <D value="-0.0012421" />
-  <E value="4.7833E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.327715" />
-  <B value="-900" />
-  <C value="-5.4" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.95" />
-  <B value="2607.3" />
-  <C value="-32.561" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="421.87" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.2534" />
-  <B value="-0.029652" />
-  <C value="0.000029293" />
-  <Tmin units="K"  value="137.15" />
-  <Tmax units="K"  value="465.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.31132" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.13861E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="267.9286" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2685" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="107.22" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.57909" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.041" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.629729" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2522" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.116126" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.8254" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.316" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.316" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000636" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.1375" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2387" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14359.41" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1161" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-66-0" />
-<Smiles name="SMILES"  value="CCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="9" />
-<CompoundID name="Name"  value="Neopentane" />
-<StructureFormula name="Structure"  value="C(CH3)4" />
-<Family name="Family"  value="3" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="433.75" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3199000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3032" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="282.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="256.6" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="256.6" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="35745.2" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.15" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12216" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.197" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.161E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12510" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05801" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.48E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.6807E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.714E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="305890" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3146000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.78325" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.25039E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.325" />
-  <B value="-0.0069832" />
-  <Tmin units="K"  value="218.8" />
-  <Tmax units="K"  value="248.9" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.90246" />
-  <B value="0.2775" />
-  <C value="433.8" />
-  <D value="0.29085" />
-  <Tmin units="K"  value="256.6" />
-  <Tmax units="K"  value="433.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="85.887" />
-  <B value="-5169" />
-  <C value="-10.119" />
-  <D value="0.000013061" />
-  <E value="2" />
-  <Tmin units="K"  value="246.05" />
-  <Tmax units="K"  value="433.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.3957E+07" />
-  <B value="0.38208" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="256.6" />
-  <Tmax units="K"  value="433.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-30040" />
-  <B value="2752.6" />
-  <C value="-37.153" />
-  <D value="0.25213" />
-  <E value="-0.00053456" />
-  <Tmin units="K"  value="20.16" />
-  <Tmax units="K"  value="139.34" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116590" />
-  <B value="146.32" />
-  <C value="1.9197" />
-  <D value="0.044936" />
-  <E value="-0.000054657" />
-  <Tmin units="K"  value="256.6" />
-  <Tmax units="K"  value="288.71" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="31525" />
-  <B value="-309.56" />
-  <C value="12.21" />
-  <D value="0.00085791" />
-  <E value="-2.6395E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17011" />
-  <B value="-163.18" />
-  <C value="-15.199" />
-  <D value="1090.5" />
-  <E value="-2506.9" />
-  <Tmin units="K"  value="216.87" />
-  <Tmax units="K"  value="1951.87" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-36.861" />
-  <B value="2459.5" />
-  <C value="3.4416" />
-  <D value="0.0000070474" />
-  <E value="2" />
-  <Tmin units="K"  value="256.6" />
-  <Tmax units="K"  value="304" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.1019E-07" />
-  <B value="0.5294" />
-  <C value="468.47" />
-  <D value="-22580" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.027667" />
-  <B value="-243.53" />
-  <C value="0.83395" />
-  <D value="-0.010754" />
-  <E value="0.0000058849" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="282.65" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000044729" />
-  <B value="1.4644" />
-  <C value="-142.95" />
-  <D value="66180" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0033983" />
-  <B value="725.98" />
-  <C value="-11.296" />
-  <D value="0.029733" />
-  <E value="-0.000047837" />
-  <Tmin units="K"  value="256.58" />
-  <Tmax units="K"  value="424.47" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13269.77" />
-  <B value="532.8823" />
-  <C value="-0.298739" />
-  <D value="0.0000708818" />
-  <E value="-1.227225E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.305" />
-  <B value="-885" />
-  <C value="-5.31" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.717" />
-  <B value="2353.3" />
-  <C value="-26.585" />
-  <Tmin units="K"  value="262.75" />
-  <Tmax units="K"  value="390" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="3.7101" />
-  <B value="-0.069319" />
-  <C value="0.000096523" />
-  <Tmin units="K"  value="256.6" />
-  <Tmax units="K"  value="304" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.31257" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.059712E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="250.7615" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2762" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="107.22" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.09145" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0402" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.595593" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.1975" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.119551" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.8239" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.392" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.000695" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.58084" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.195" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14359.41" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1233" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="463-82-1" />
-<Smiles name="SMILES"  value="CC(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1592" />
-<CompoundID name="Name"  value="1,2,4-trichlorobenzene" />
-<StructureFormula name="Structure"  value="(C6H3)Cl3" />
-<Family name="Family"  value="29" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="725" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3720000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.395" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="486.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="290.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="290.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="33.0937" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="181.447" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12525" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.358106" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.832E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20620" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.20291E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10098" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.233E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.1757E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.30523E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380911" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.55647E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.65632E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.194" />
-  <B value="-0.0039041" />
-  <Tmin units="K"  value="116.06" />
-  <Tmax units="K"  value="290.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61713" />
-  <B value="0.2524" />
-  <C value="725" />
-  <D value="0.2857" />
-  <Tmin units="K"  value="290.15" />
-  <Tmax units="K"  value="725" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="47.20405" />
-  <B value="-7460.647" />
-  <C value="-3.164866" />
-  <D value="-3.316432E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="290.15" />
-  <Tmax units="K"  value="725" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.897E+07" />
-  <B value="0.4026" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="290.15" />
-  <Tmax units="K"  value="725" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6586.2" />
-  <B value="796.22" />
-  <C value="-1.4691" />
-  <D value="0.0035279" />
-  <E value="-0.0000037266" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="290.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="145370" />
-  <B value="234.69" />
-  <C value="6.2789" />
-  <D value="0.017012" />
-  <E value="-0.000015675" />
-  <Tmin units="K"  value="290.15" />
-  <Tmax units="K"  value="486.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63130" />
-  <B value="-426.63" />
-  <C value="12.569" />
-  <D value="-0.000095696" />
-  <E value="1.4713E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27285" />
-  <B value="-397.07" />
-  <C value="-111.19" />
-  <D value="28956" />
-  <E value="-249060" />
-  <Tmin units="K"  value="362.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-241" />
-  <B value="9893.2" />
-  <C value="36.115" />
-  <D value="-0.000047458" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="580" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.2097E-08" />
-  <B value="0.80621" />
-  <C value="99.511" />
-  <D value="1477.5" />
-  <Tmin units="K"  value="486.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.070105" />
-  <B value="-290.72" />
-  <C value="-0.20366" />
-  <D value="-0.0074415" />
-  <E value="0.0000024779" />
-  <Tmin units="K"  value="285.15" />
-  <Tmax units="K"  value="486.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-743.07" />
-  <B value="0.74159" />
-  <C value="-2.1746E+09" />
-  <D value="-6.4502E+10" />
-  <Tmin units="K"  value="486.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0099086" />
-  <B value="212.19" />
-  <C value="-4.1394" />
-  <D value="0.0037352" />
-  <E value="-0.0000066653" />
-  <Tmin units="K"  value="290.15" />
-  <Tmax units="K"  value="725" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13485" />
-  <B value="490.78" />
-  <C value="-0.36646" />
-  <D value="0.000098813" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.92" />
-  <B value="4632.7" />
-  <C value="-40.49" />
-  <Tmin units="K"  value="435.15" />
-  <Tmax units="K"  value="633.45" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.8536" />
-  <B value="-0.0055643" />
-  <C value="-0.0000085016" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="580" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.563146" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.440056E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="295.0221" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259136" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="147.03" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0577" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.4595" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.358106" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.12525" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.0625" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.732" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.358106" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20618.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.12525" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="54"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="40"  value="3" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  <group id="42"  value="3" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="3" />
-  <group id="54"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="53"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="120-82-1" />
-<Smiles name="SMILES"  value="c1(Cl)c(Cl)cc(Cl)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1573" />
-<CompoundID name="Name"  value="M-dichlorobenzene" />
-<StructureFormula name="Structure"  value="(C6H4)Cl2" />
-<Family name="Family"  value="29" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="683.95" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4070000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.351" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="446.23" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="248.39" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="248.39" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.40787" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="147.002" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.114533" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.27898" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.389E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19570" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.74E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06732" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.22E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.57E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.79E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="343530" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.259E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.89625" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.825E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.566" />
-  <B value="-0.0051312" />
-  <Tmin units="K"  value="99.36" />
-  <Tmax units="K"  value="248.39" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.74132" />
-  <B value="0.26094" />
-  <C value="683.95" />
-  <D value="0.31392" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="683.95" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="100.37" />
-  <B value="-9087" />
-  <C value="-11.404" />
-  <D value="0.0000055122" />
-  <E value="2" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="683.95" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.2076E+07" />
-  <B value="0.15554" />
-  <C value="-0.20298" />
-  <D value="0.94291" />
-  <E value="-0.55524" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="683.95" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="35.885" />
-  <B value="2025.5" />
-  <C value="-13.455" />
-  <D value="0.039723" />
-  <E value="-0.000043973" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="230.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="89111" />
-  <B value="785.31" />
-  <C value="3.6098" />
-  <D value="0.022491" />
-  <E value="-0.00001896" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="446.23" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="56066" />
-  <B value="-490.93" />
-  <C value="12.649" />
-  <D value="-0.00012726" />
-  <E value="2.3703E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24322" />
-  <B value="-355.19" />
-  <C value="-67.685" />
-  <D value="-40405" />
-  <E value="47635" />
-  <Tmin units="K"  value="341.97" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-114.79" />
-  <B value="4907.5" />
-  <C value="16.374" />
-  <D value="-0.000020623" />
-  <E value="2" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="547.16" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.3524E-07" />
-  <B value="0.71383" />
-  <C value="257.29" />
-  <D value="1880.2" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.042347" />
-  <B value="-224.09" />
-  <C value="-0.2096" />
-  <D value="-0.006185" />
-  <E value="0.0000024486" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="446.23" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-1552.3" />
-  <B value="0.68852" />
-  <C value="-2.6293E+09" />
-  <D value="-1.7751E+11" />
-  <Tmin units="K"  value="446.23" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018573" />
-  <B value="119.26" />
-  <C value="-3.5049" />
-  <D value="0.0018889" />
-  <E value="-0.0000041728" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="683.95" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-13602.18" />
-  <B value="548.9826" />
-  <C value="-0.450282" />
-  <D value="0.00014267" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-3.829242" />
-  <B value="-2500" />
-  <C value="-15" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.137" />
-  <B value="3719.2" />
-  <C value="-59.169" />
-  <Tmin units="K"  value="413.64" />
-  <Tmax units="K"  value="615.18" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.2726" />
-  <B value="-0.019593" />
-  <C value="0.00001463" />
-  <Tmin units="K"  value="248.39" />
-  <Tmax units="K"  value="547.16" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.36165" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.914152E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="308.1505" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="128.34" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0514" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.2946" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.215834" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.114641" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.4376" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.288" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.215834" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19575.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.114641" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="54"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="40"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="42"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="54"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="53"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="541-73-1" />
-<Smiles name="SMILES"  value="c1c([Cl])cccc1([Cl])" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1572" />
-<CompoundID name="Name"  value="O-dichlorobenzene" />
-<StructureFormula name="Structure"  value="(C6H4)Cl2" />
-<Family name="Family"  value="29" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="705" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4070000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.351" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="453.57" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="256.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="256.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.48939" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="147.002" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.112969" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.219189" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.186E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20310" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.34E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0673" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.22E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="3.02E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="8.29E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="341850" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.266E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.66193" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.826E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="4.3487" />
-  <B value="0.023944" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="256.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.74261" />
-  <B value="0.26108" />
-  <C value="705" />
-  <D value="0.30655" />
-  <Tmin units="K"  value="256.15" />
-  <Tmax units="K"  value="705" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="75.75983" />
-  <B value="-8226.762" />
-  <C value="-7.552754" />
-  <D value="6.191298E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="256.15" />
-  <Tmax units="K"  value="705" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.774E+07" />
-  <B value="2.8227" />
-  <C value="-6.8433" />
-  <D value="7.6547" />
-  <E value="-3.1275" />
-  <Tmin units="K"  value="256.15" />
-  <Tmax units="K"  value="705" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34.618" />
-  <B value="1984.3" />
-  <C value="-12.98" />
-  <D value="0.037736" />
-  <E value="-0.000041136" />
-  <Tmin units="K"  value="224.65" />
-  <Tmax units="K"  value="234.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="127840" />
-  <B value="-59.156" />
-  <C value="8.3728" />
-  <D value="0.0093569" />
-  <E value="-0.0000051714" />
-  <Tmin units="K"  value="266.02" />
-  <Tmax units="K"  value="528.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="55560" />
-  <B value="-490.51" />
-  <C value="12.648" />
-  <D value="-0.00012186" />
-  <E value="2.1792E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23253" />
-  <B value="-364.15" />
-  <C value="-75.666" />
-  <D value="-71505" />
-  <E value="114590" />
-  <Tmin units="K"  value="352.5" />
-  <Tmax units="K"  value="1937.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-37.699" />
-  <B value="2377" />
-  <C value="4.0848" />
-  <D value="-0.0000020768" />
-  <E value="2" />
-  <Tmin units="K"  value="256.15" />
-  <Tmax units="K"  value="453.57" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.6041E-07" />
-  <B value="0.76289" />
-  <C value="205.1" />
-  <D value="-39.728" />
-  <Tmin units="K"  value="256.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.06919" />
-  <B value="-379.09" />
-  <C value="0.89948" />
-  <D value="-0.0099037" />
-  <E value="0.0000041677" />
-  <Tmin units="K"  value="262.87" />
-  <Tmax units="K"  value="351.71" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-1200.2" />
-  <B value="0.7235" />
-  <C value="-2.8422E+09" />
-  <D value="-8.8684E+10" />
-  <Tmin units="K"  value="453.57" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.003373" />
-  <B value="482.91" />
-  <C value="-6.8665" />
-  <D value="0.011374" />
-  <E value="-0.00001512" />
-  <Tmin units="K"  value="256.15" />
-  <Tmax units="K"  value="705" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14297.98" />
-  <B value="550.447" />
-  <C value="-0.451286" />
-  <D value="0.000142863" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-6.104208" />
-  <B value="-3750" />
-  <C value="-22.5" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.671" />
-  <B value="3414.3" />
-  <C value="-79.992" />
-  <Tmin units="K"  value="428.95" />
-  <Tmax units="K"  value="634.13" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0621" />
-  <B value="-0.037459" />
-  <C value="0.000039274" />
-  <Tmin units="K"  value="256.15" />
-  <Tmax units="K"  value="453.57" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.361537" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.152857E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="286.8836" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.271326" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="128.34" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="1.1558" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0495" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.3118" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.214215" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.11318" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.4376" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.288" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.5483" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.214215" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20271.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.11318" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="54"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="40"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="42"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="54"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="53"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="95-50-1" />
-<Smiles name="SMILES"  value="c1([Cl])ccccc1([Cl])" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1574" />
-<CompoundID name="Name"  value="P-dichlorobenzene" />
-<StructureFormula name="Structure"  value="(C6H4)Cl2" />
-<Family name="Family"  value="29" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="684.75" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4070000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.351" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="447.21" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="326.14" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="326.14" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1225.03" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="147.002" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.117406" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.284638" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.149E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19330" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06732" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.22E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.25E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.67E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="336740" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.82E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.61751" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.802E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.872" />
-  <B value="-0.0022226" />
-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="326.14" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.74861" />
-  <B value="0.26271" />
-  <C value="684.75" />
-  <D value="0.30815" />
-  <Tmin units="K"  value="326.14" />
-  <Tmax units="K"  value="684.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="40.63688" />
-  <B value="-6607.72" />
-  <C value="-2.221184" />
-  <D value="-3.90747E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="684.75" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.112633E+07" />
-  <B value="0.426201" />
-  <C value="-0.0366365" />
-  <D value="0.00811781" />
-  <E value="-0.00754654" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="684.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5903.9" />
-  <B value="798.4" />
-  <C value="-2.8553" />
-  <D value="0.0083402" />
-  <E value="-0.0000080094" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="320" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="155200" />
-  <B value="855.07" />
-  <C value="0.88585" />
-  <D value="0.024843" />
-  <E value="-0.000014582" />
-  <Tmin units="K"  value="326.14" />
-  <Tmax units="K"  value="513.56" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="55695" />
-  <B value="-489.46" />
-  <C value="12.649" />
-  <D value="-0.00012524" />
-  <E value="2.3115E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23632" />
-  <B value="-343.91" />
-  <C value="-71.253" />
-  <D value="-46.219" />
-  <E value="-58041" />
-  <Tmin units="K"  value="342.37" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-131.86" />
-  <B value="5312.8" />
-  <C value="19.284" />
-  <D value="-0.000029085" />
-  <E value="2" />
-  <Tmin units="K"  value="326.14" />
-  <Tmax units="K"  value="447.21" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.5946E-07" />
-  <B value="0.76369" />
-  <C value="193.94" />
-  <D value="-148.97" />
-  <Tmin units="K"  value="326.14" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.02927" />
-  <B value="-28.287" />
-  <C value="-2.0319" />
-  <D value="0.000077764" />
-  <E value="-0.0000037797" />
-  <Tmin units="K"  value="208.5" />
-  <Tmax units="K"  value="548.5" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-2269.7" />
-  <B value="0.68598" />
-  <C value="-3.774E+09" />
-  <D value="-2.6655E+11" />
-  <Tmin units="K"  value="447.21" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0075966" />
-  <B value="340.08" />
-  <C value="-5.3586" />
-  <D value="0.0064741" />
-  <E value="-0.0000095368" />
-  <Tmin units="K"  value="326.14" />
-  <Tmax units="K"  value="684.75" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14350.7" />
-  <B value="553.2085" />
-  <C value="-0.455679" />
-  <D value="0.000144745" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.165126" />
-  <B value="-1430" />
-  <C value="-8.58" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.115" />
-  <B value="3752.8" />
-  <C value="-56.114" />
-  <Tmin units="K"  value="420.51" />
-  <Tmax units="K"  value="609.25" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-4.2213" />
-  <B value="-0.0089482" />
-  <C value="6.2913E-07" />
-  <Tmin units="K"  value="326.14" />
-  <Tmax units="K"  value="447.21" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.36165" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.914152E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="308.5109" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.265583" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="128.34" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="2.1786" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0501" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.2962" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.234279" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.117341" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.4376" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.288" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-3.8932" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.234279" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19187.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.117341" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="54"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="40"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="42"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="54"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="53"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-46-7" />
-<Smiles name="SMILES"  value="c1cc([Cl])ccc1([Cl])" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1680" />
-<CompoundID name="Name"  value="Bromobenzene" />
-<StructureFormula name="Structure"  value="(C6H5)Br" />
-<Family name="Family"  value="30" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="670.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4519100" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.324" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="429.236" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="242.43" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="242.43" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.8364" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="157.008" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.105567" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.250575" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.466E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19940" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.67059E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06016" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.34E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.05018E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.38532E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="324386" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.06274E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95208" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.01917E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.8219" />
-  <B value="0.0072956" />
-  <Tmin units="K"  value="93.15" />
-  <Tmax units="K"  value="242.43" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.8226" />
-  <B value="0.26632" />
-  <C value="670.15" />
-  <D value="0.2821" />
-  <Tmin units="K"  value="242.43" />
-  <Tmax units="K"  value="670.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="146.6319" />
-  <B value="-10375.07" />
-  <C value="-18.74897" />
-  <D value="0.0000147083" />
-  <E value="2" />
-  <Tmin units="K"  value="242.43" />
-  <Tmax units="K"  value="670.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.656362E+07" />
-  <B value="0.347537" />
-  <C value="0.135082" />
-  <D value="0.0123621" />
-  <E value="-0.140849" />
-  <Tmin units="K"  value="242.43" />
-  <Tmax units="K"  value="647.64" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="23455" />
-  <B value="406.81" />
-  <C value="-1.101" />
-  <D value="0.0059523" />
-  <E value="-0.0000047316" />
-  <Tmin units="K"  value="89.99" />
-  <Tmax units="K"  value="239.99" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97487" />
-  <B value="953.8" />
-  <C value="2.1839" />
-  <D value="0.023716" />
-  <E value="-0.000017458" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="495.08" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65656" />
-  <B value="-767.67" />
-  <C value="13.165" />
-  <D value="-0.00063667" />
-  <E value="1.8215E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20016" />
-  <B value="-288.53" />
-  <C value="-61.836" />
-  <D value="76562" />
-  <E value="-287190" />
-  <Tmin units="K"  value="335.08" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-54.93" />
-  <B value="2754.4" />
-  <C value="6.973" />
-  <D value="-0.000009784" />
-  <E value="2" />
-  <Tmin units="K"  value="242.43" />
-  <Tmax units="K"  value="429.24" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.2327E-07" />
-  <B value="0.71456" />
-  <C value="185.02" />
-  <D value="-22.393" />
-  <Tmin units="K"  value="429.24" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.032562" />
-  <B value="-180.04" />
-  <C value="-0.56464" />
-  <D value="-0.0046562" />
-  <E value="1.7973E-07" />
-  <Tmin units="K"  value="242.43" />
-  <Tmax units="K"  value="429.24" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00025787" />
-  <B value="0.79923" />
-  <C value="269.79" />
-  <D value="163730" />
-  <Tmin units="K"  value="429.24" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014274" />
-  <B value="52.267" />
-  <C value="-2.9864" />
-  <D value="0.00054996" />
-  <E value="-0.0000038815" />
-  <Tmin units="K"  value="242.43" />
-  <Tmax units="K"  value="647.64" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-28313.55" />
-  <B value="532.5813" />
-  <C value="-0.404723" />
-  <D value="0.000119696" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.349052" />
-  <B value="-2700" />
-  <C value="-16.2" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.853" />
-  <B value="3407.3" />
-  <C value="-63.769" />
-  <Tmin units="K"  value="403.15" />
-  <Tmax units="K"  value="602.62" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.83085" />
-  <B value="-0.037331" />
-  <C value="0.000039165" />
-  <Tmin units="K"  value="242.43" />
-  <Tmax units="K"  value="429.24" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.321534" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.365214E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="357.2119" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="110.55" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.77161" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0459" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.50093" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.250575" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.105567" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9709" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.952" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.5658" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.250575" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19944.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.105567" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="65"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="44"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="65"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  <group id="64"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-86-1" />
-<Smiles name="SMILES"  value="c1(Br)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1571" />
-<CompoundID name="Name"  value="Monochlorobenzene" />
-<StructureFormula name="Structure"  value="C6H5Cl" />
-<Family name="Family"  value="29" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="632.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4520000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.308" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="404.91" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="227.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="227.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="8.4456" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.558" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10222" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.251" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.603E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19350" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.64E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05784" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.14E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="5.109E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.829E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="314030" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9556000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.81651" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.976E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.164" />
-  <B value="-0.0063358" />
-  <Tmin units="K"  value="91.18" />
-  <Tmax units="K"  value="227.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.78287" />
-  <B value="0.25464" />
-  <C value="632.4" />
-  <D value="0.26342" />
-  <Tmin units="K"  value="227.95" />
-  <Tmax units="K"  value="632.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="51.41334" />
-  <B value="-6020.539" />
-  <C value="-4.204143" />
-  <D value="1.293848E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="227.95" />
-  <Tmax units="K"  value="632.35" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.9039E+07" />
-  <B value="0.24473" />
-  <C value="-0.048652" />
-  <D value="0.40537" />
-  <E value="-0.25012" />
-  <Tmin units="K"  value="227.95" />
-  <Tmax units="K"  value="632.35" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15722" />
-  <B value="756.66" />
-  <C value="1.4275" />
-  <D value="-0.025177" />
-  <E value="0.000067134" />
-  <Tmin units="K"  value="89.99" />
-  <Tmax units="K"  value="227.95" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="139150" />
-  <B value="-333.42" />
-  <C value="10.906" />
-  <D value="-0.018036" />
-  <E value="0.000054846" />
-  <Tmin units="K"  value="227.95" />
-  <Tmax units="K"  value="360" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="74680" />
-  <B value="-1001.5" />
-  <C value="13.827" />
-  <D value="-0.0014014" />
-  <E value="4.6413E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19009" />
-  <B value="-259.98" />
-  <C value="-46.648" />
-  <D value="20404" />
-  <E value="-83538" />
-  <Tmin units="K"  value="316.18" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="0.029483" />
-  <B value="556.49" />
-  <C value="-1.5963" />
-  <D value="1.2171E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.1217E-07" />
-  <B value="0.79382" />
-  <C value="109.37" />
-  <D value="1134.4" />
-  <Tmin units="K"  value="227.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.083427" />
-  <B value="-157.94" />
-  <C value="-0.89724" />
-  <D value="-0.0049259" />
-  <E value="-0.0000027589" />
-  <Tmin units="K"  value="227.95" />
-  <Tmax units="K"  value="404.87" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0004167" />
-  <B value="0.92033" />
-  <C value="1902.9" />
-  <D value="123750" />
-  <Tmin units="K"  value="400" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0095824" />
-  <B value="101.65" />
-  <C value="-3.6063" />
-  <D value="0.0024021" />
-  <E value="-0.0000068537" />
-  <Tmin units="K"  value="227.95" />
-  <Tmax units="K"  value="632.35" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="864.71" />
-  <B value="318.34" />
-  <C value="0.15033" />
-  <D value="-0.00047659" />
-  <E value="2.2599E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.352017" />
-  <B value="-2800" />
-  <C value="-16.8" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.211" />
-  <B value="3480.2" />
-  <C value="-45.686" />
-  <Tmin units="K"  value="383.15" />
-  <Tmax units="K"  value="568.5" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.6012" />
-  <B value="-0.01988" />
-  <C value="0.000015158" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.30667" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.202025E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="346.4098" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="109.65" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.33097" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0434" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.106" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.24605" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10229" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.79" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.84" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.65335" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2459" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19345.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.10229" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="54"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="5" />
-  <group id="40"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="42"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="54"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="53"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-90-7" />
-<Smiles name="SMILES"  value="c1ccccc1([Cl])" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1691" />
-<CompoundID name="Name"  value="Iodobenzene" />
-<StructureFormula name="Structure"  value="C6H5I" />
-<Family name="Family"  value="31" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="721.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4519100" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.351" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="461.6" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="241.83" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="241.83" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.17521" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="204.008" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.111976" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.246574" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.359E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20450" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.67E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06548" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.82E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.649E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.902E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="334100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9749000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.88464" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.05E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.3334" />
-  <B value="2.2E-16" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="251.33" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.7521" />
-  <B value="0.26381" />
-  <C value="721.15" />
-  <D value="0.2895" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="721.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="79.186" />
-  <B value="-8185.3" />
-  <C value="-8.2636" />
-  <D value="0.0000035963" />
-  <E value="2" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="721.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.148821E+07" />
-  <B value="0.433906" />
-  <C value="-0.0102943" />
-  <D value="-0.0130647" />
-  <E value="-0.0329532" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="721.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6576" />
-  <B value="738.1" />
-  <C value="-3.3528" />
-  <D value="0.013129" />
-  <E value="-0.000016135" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="241.83" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="139830" />
-  <B value="578.69" />
-  <C value="1.6453" />
-  <D value="0.031278" />
-  <E value="-0.000034279" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="350" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63442" />
-  <B value="-692.72" />
-  <C value="13.003" />
-  <D value="-0.00048297" />
-  <E value="1.3499E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22331" />
-  <B value="-352.07" />
-  <C value="-71.715" />
-  <D value="-10058" />
-  <E value="-45757" />
-  <Tmin units="K"  value="360.57" />
-  <Tmax units="K"  value="1980.6" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-57.177" />
-  <B value="3157.8" />
-  <C value="7.1529" />
-  <D value="-0.0000070913" />
-  <E value="2" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="461.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.1908E-07" />
-  <B value="0.74366" />
-  <C value="231.22" />
-  <D value="-43.688" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.077923" />
-  <B value="1284.8" />
-  <C value="-17.082" />
-  <D value="0.050362" />
-  <E value="-0.00006779" />
-  <Tmin units="K"  value="216.35" />
-  <Tmax units="K"  value="461.6" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00026878" />
-  <B value="0.78911" />
-  <C value="373.97" />
-  <D value="187720" />
-  <Tmin units="K"  value="461.6" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010772" />
-  <B value="65.841" />
-  <C value="-3.1409" />
-  <D value="0.0010009" />
-  <E value="-0.0000042785" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="721.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-24781" />
-  <B value="533.2927" />
-  <C value="-0.414111" />
-  <D value="0.000125704" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-3.488623" />
-  <B value="-2300" />
-  <C value="-13.8" />
-  <Tmin units="K"  value="154" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.202" />
-  <B value="3942.3" />
-  <C value="-54.218" />
-  <Tmin units="K"  value="433.15" />
-  <Tmax units="K"  value="645.47" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.2239" />
-  <B value="-0.04181" />
-  <C value="0.000043079" />
-  <Tmin units="K"  value="241.83" />
-  <Tmax units="K"  value="461.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.351265" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.47817E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="395.0244" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="118.45" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.26194" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0498" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.83757" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.246574" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.111976" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2857" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.112" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.61965" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.246574" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20367.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.111976" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
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-  </UnifacVLE>
-<Asog name="ASOG" >
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-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="64"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  <group id="63"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="591-50-4" />
-<Smiles name="SMILES"  value="c1(I)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1886" />
-<CompoundID name="Name"  value="Nitrobenzene" />
-<StructureFormula name="Structure"  value="C6H5NO2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="719" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.349" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="483.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="278.91" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="278.87" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.69814" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="123.109" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.102717" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.449158" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.944E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22610" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.41E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06264" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.85E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="6.75E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.63E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="342100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.16E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.4767" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.9782E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="5.1859" />
-  <B value="0.020494" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="282.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.69124" />
-  <B value="0.24124" />
-  <C value="719" />
-  <D value="0.28137" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="719" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="112.2302" />
-  <B value="-10538.91" />
-  <C value="-12.95686" />
-  <D value="5.116363E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="719" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.9884E+07" />
-  <B value="-2.0813" />
-  <C value="7.5215" />
-  <D value="-8.8126" />
-  <E value="3.6947" />
-  <Tmin units="K"  value="278.91" />
-  <Tmax units="K"  value="695.84" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="39285" />
-  <B value="201.2" />
-  <C value="0.90502" />
-  <D value="-0.0016563" />
-  <E value="0.0000028762" />
-  <Tmin units="K"  value="70" />
-  <Tmax units="K"  value="270" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="146460" />
-  <B value="1160.6" />
-  <C value="0.44135" />
-  <D value="0.024575" />
-  <E value="-0.000013049" />
-  <Tmin units="K"  value="278.87" />
-  <Tmax units="K"  value="483.95" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="112710" />
-  <B value="-1114.3" />
-  <C value="13.93" />
-  <D value="-0.0013044" />
-  <E value="3.7699E-07" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23371" />
-  <B value="-316.86" />
-  <C value="-98.829" />
-  <D value="-51500" />
-  <E value="36178" />
-  <Tmin units="K"  value="359.5" />
-  <Tmax units="K"  value="1974.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-78.652" />
-  <B value="4202" />
-  <C value="10.37" />
-  <D value="-0.0000091095" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="480.75" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.1361E-07" />
-  <B value="0.80626" />
-  <C value="193.03" />
-  <D value="-46.762" />
-  <Tmin units="K"  value="278.87" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11293" />
-  <B value="-401.92" />
-  <C value="1.2826" />
-  <D value="-0.013207" />
-  <E value="0.0000075932" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="400" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00014373" />
-  <B value="0.9615" />
-  <C value="718" />
-  <D value="-0.0027852" />
-  <Tmin units="K"  value="483.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018708" />
-  <B value="98.592" />
-  <C value="-3.1839" />
-  <D value="0.0013401" />
-  <E value="-0.0000036822" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="719" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="16636" />
-  <B value="456.07" />
-  <C value="-0.27615" />
-  <D value="0.00006178" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-6.224487" />
-  <B value="-8439.716" />
-  <C value="-90.14595" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="719" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.399" />
-  <B value="4170.3" />
-  <C value="-61.504" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="626.34" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.9368" />
-  <B value="-0.038924" />
-  <C value="0.000038297" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="480.75" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.335341" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.708113E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="352.6966" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.251146" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="105.41" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.7519" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0479" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.20656" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.447966" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.102717" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.13" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.14" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="4.5743" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.447966" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22612.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.102717" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="58"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="34"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="58"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="57"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="98-95-3" />
-<Smiles name="SMILES"  value="c1(N(=O)=O)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="501" />
-<CompoundID name="Name"  value="Benzene" />
-<StructureFormula name="Structure"  value="-CHCHCHCHCHCH-" />
-<Family name="Family"  value="16" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="562.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4895000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.256" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="353.24" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="278.68" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="278.68" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="4764.22" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="78.114" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08941" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.209" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.004E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18700" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0484" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.0E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="8.288E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.296E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="269300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9866000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.8356" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.136E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.059" />
-  <B value="-0.00034838" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="282.6" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.99938" />
-  <B value="0.26348" />
-  <C value="562.05" />
-  <D value="0.27856" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="562.05" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="88.368" />
-  <B value="-6712.9" />
-  <C value="-10.022" />
-  <D value="0.000007694" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="562.16" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.881E+07" />
-  <B value="0.61066" />
-  <C value="-0.25882" />
-  <D value="0.032238" />
-  <E value="0.022475" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="562.05" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-124.61" />
-  <B value="909.02" />
-  <C value="-6.049" />
-  <D value="0.022885" />
-  <E value="-0.000024638" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="278.7" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="111460" />
-  <B value="-1854.3" />
-  <C value="22.399" />
-  <D value="-0.028936" />
-  <E value="0.000028991" />
-  <Tmin units="K"  value="278.68" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="34010.24" />
-  <B value="-588.0978" />
-  <C value="12.81777" />
-  <D value="-0.000197306" />
-  <E value="5.142899E-08" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17507" />
-  <B value="-220.13" />
-  <C value="-18.085" />
-  <D value="-7404.6" />
-  <E value="16690" />
-  <Tmin units="K"  value="281.02" />
-  <Tmax units="K"  value="1967" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-24.61" />
-  <B value="1576.5" />
-  <C value="2.1698" />
-  <D value="-0.0000051366" />
-  <E value="2" />
-  <Tmin units="K"  value="278.68" />
-  <Tmax units="K"  value="545" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.1366E-08" />
-  <B value="0.9675" />
-  <C value="8.0285" />
-  <D value="-35.629" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.049539" />
-  <B value="-177.97" />
-  <C value="0.19475" />
-  <D value="-0.0073805" />
-  <E value="0.0000027938" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000049549" />
-  <B value="1.4519" />
-  <C value="154.14" />
-  <D value="26202" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.02575" />
-  <B value="-212.19" />
-  <C value="-0.62089" />
-  <D value="-0.0059738" />
-  <E value="0.0000021771" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="562.05" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="29525" />
-  <B value="-51.417" />
-  <C value="1.1944" />
-  <D value="-0.0016468" />
-  <E value="6.8461E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.717467" />
-  <B value="-1150" />
-  <C value="-6.9" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.075" />
-  <B value="2977.3" />
-  <C value="-41.505" />
-  <Tmin units="K"  value="338" />
-  <Tmax units="K"  value="505.4" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.719" />
-  <B value="-0.019734" />
-  <C value="0.000013263" />
-  <Tmin units="K"  value="278.68" />
-  <Tmax units="K"  value="545" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.25639" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.753029E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="320.6073" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2696" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="90.95999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.375" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0367" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.882619" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.21367" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.08941" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.1878" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.4" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.4" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000318" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.9715" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.213" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18736.78" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0894" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="6" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="6" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="6" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="6" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="6" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="6" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="71-43-2" />
-<Smiles name="SMILES"  value="c1ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1181" />
-<CompoundID name="Name"  value="Phenol" />
-<StructureFormula name="Structure"  value="(C6H5)OH" />
-<Family name="Family"  value="48" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="694.25" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6130000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.229" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.243" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="455.04" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="314.06" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="314.06" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="187.979" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="94.113" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08787" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.442" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.415E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24630" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0538" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.79E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.6399E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.2637E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="314810" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.151E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.524" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.921E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.394" />
-  <B value="0.0020984" />
-  <Tmin units="K"  value="261.15" />
-  <Tmax units="K"  value="314.06" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.4937" />
-  <B value="0.32883" />
-  <C value="694.25" />
-  <D value="0.34018" />
-  <Tmin units="K"  value="314.06" />
-  <Tmax units="K"  value="688.71" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="300.97" />
-  <B value="-20269" />
-  <C value="-40.743" />
-  <D value="0.000021631" />
-  <E value="2" />
-  <Tmin units="K"  value="310.45" />
-  <Tmax units="K"  value="694.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.270282E+07" />
-  <B value="-0.265673" />
-  <C value="2.248545" />
-  <D value="-2.018709" />
-  <E value="0.353169" />
-  <Tmin units="K"  value="314.06" />
-  <Tmax units="K"  value="674.24" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="2513.5" />
-  <B value="793.73" />
-  <C value="-4.1506" />
-  <D value="0.014189" />
-  <E value="-0.000014807" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="314.05" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86710" />
-  <B value="-628.11" />
-  <C value="15.735" />
-  <D value="-0.0091743" />
-  <E value="0.0000081827" />
-  <Tmin units="K"  value="314.05" />
-  <Tmax units="K"  value="655.37" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39758" />
-  <B value="-470.56" />
-  <C value="12.627" />
-  <D value="0.000068347" />
-  <E value="-4.9708E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22714" />
-  <B value="-180.33" />
-  <C value="-95.063" />
-  <D value="-17328" />
-  <E value="21635" />
-  <Tmin units="K"  value="323.15" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-203.001" />
-  <B value="10884.21" />
-  <C value="28.73615" />
-  <D value="-0.0000224564" />
-  <E value="2" />
-  <Tmin units="K"  value="291.45" />
-  <Tmax units="K"  value="555.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.0771E-07" />
-  <B value="0.79384" />
-  <C value="145.89" />
-  <D value="-11364" />
-  <Tmin units="K"  value="199.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.14109" />
-  <B value="-966.5" />
-  <C value="10.659" />
-  <D value="-0.049095" />
-  <E value="0.000038703" />
-  <Tmin units="K"  value="314.06" />
-  <Tmax units="K"  value="454.99" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.03495" />
-  <B value="0.27845" />
-  <C value="1585.2" />
-  <D value="862070" />
-  <Tmin units="K"  value="199.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.047876" />
-  <B value="-16.307" />
-  <C value="-2.0376" />
-  <D value="-0.0009046" />
-  <E value="-0.0000007358" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="674.24" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="21468" />
-  <B value="145.51" />
-  <C value="0.73949" />
-  <D value="-0.0012002" />
-  <E value="5.2523E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="11.2" />
-  <B value="-1000" />
-  <C value="-50" />
-  <Tmin units="K"  value="313" />
-  <Tmax units="K"  value="694" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.465" />
-  <B value="3610.5" />
-  <C value="-91.898" />
-  <Tmin units="K"  value="417" />
-  <Tmax units="K"  value="620" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.57041" />
-  <B value="-0.0078308" />
-  <C value="-0.000023564" />
-  <Tmin units="K"  value="291.45" />
-  <Tmax units="K"  value="555.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2809" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.234419E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="278.3631" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="97.06999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-3.46962" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.04" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.05593" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.42969" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.08314" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.5517" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.68" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="1.78" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="7.50049" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.442" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24632.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0889403" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="18"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="5" />
-  <group id="18"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="16"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="18"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="17"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-95-2" />
-<Smiles name="SMILES"  value="c1ccccc1(O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1792" />
-<CompoundID name="Name"  value="Aniline" />
-<StructureFormula name="Structure"  value="C6H5NH2" />
-<Family name="Family"  value="36" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="699" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5310000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.2739" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="457.17" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="267.13" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="267.13" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.13219" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="93.128" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09152" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.38" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.436E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24120" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.1E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05638" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.04E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="8.71E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.668E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="319800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.054E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.23512" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.239E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.175" />
-  <B value="-0.0058627" />
-  <Tmin units="K"  value="106.85" />
-  <Tmax units="K"  value="267.13" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0034" />
-  <B value="0.27828" />
-  <C value="699.16" />
-  <D value="0.26553" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="699.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="51.415" />
-  <B value="-7256.776" />
-  <C value="-3.968851" />
-  <D value="1.89237E-06" />
-  <E value="1.941839" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="699.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.518054E+07" />
-  <B value="-0.829815" />
-  <C value="5.221579" />
-  <D value="-7.587726" />
-  <E value="3.672676" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="699.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="3106" />
-  <B value="718.22" />
-  <C value="-3.6674" />
-  <D value="0.016118" />
-  <E value="-0.000021313" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="267.13" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="113560" />
-  <B value="-229.45" />
-  <C value="12.348" />
-  <D value="-0.001777" />
-  <E value="0.0000025731" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="457.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="53776" />
-  <B value="-561.43" />
-  <C value="12.878" />
-  <D value="-0.00018357" />
-  <E value="4.6595E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.043471" />
-  <B value="-226.46" />
-  <C value="-55.939" />
-  <D value="-9629.2" />
-  <E value="9349.5" />
-  <Tmin units="K"  value="260" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-411.9909" />
-  <B value="17880.72" />
-  <C value="61.83069" />
-  <D value="-0.0000659764" />
-  <E value="2" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="559.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.8398E-07" />
-  <B value="0.71832" />
-  <C value="209.33" />
-  <D value="-5579.1" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.065783" />
-  <B value="-186.09" />
-  <C value="-0.85045" />
-  <D value="-0.0016475" />
-  <E value="-0.0000028261" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="633.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00025341" />
-  <B value="0.90822" />
-  <C value="897.01" />
-  <D value="-19862" />
-  <Tmin units="K"  value="457.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.05644" />
-  <B value="-22.461" />
-  <C value="-1.8774" />
-  <D value="-0.0010936" />
-  <E value="-4.1576E-07" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="699" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="21601" />
-  <B value="165.76" />
-  <C value="0.70158" />
-  <D value="-0.0011115" />
-  <E value="0.0000004681" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.694498" />
-  <B value="-3535" />
-  <C value="-21.21" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.729" />
-  <B value="3936.8" />
-  <C value="-71.33" />
-  <Tmin units="K"  value="420.7" />
-  <Tmax units="K"  value="623.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="7.3538" />
-  <B value="-0.06058" />
-  <C value="0.000058645" />
-  <Tmin units="K"  value="267.13" />
-  <Tmax units="K"  value="559.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2901" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.21662E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="338.1071" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="97.80999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.62382" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0422" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.02441" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.38089" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0916034" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.72" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.82" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.45596" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.404143" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24125.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0916034" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="37"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="5" />
-  <group id="43"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="29"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="37"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="36"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="62-53-3" />
-<Smiles name="SMILES"  value="c1(N)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1080" />
-<CompoundID name="Name"  value="Cyclohexanone" />
-<StructureFormula name="Structure"  value="-CH2CO(CH2)3CH2-" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="653" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.311" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.229" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="428.58" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="242" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="242" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.80118" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.143" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.104111" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.299006" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.511E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.03E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06171" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.78E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.261E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-9.028E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="334260" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1190000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.931362" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.299E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.803" />
-  <B value="-0.0058836" />
-  <Tmin units="K"  value="96.8" />
-  <Tmax units="K"  value="242" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.8601" />
-  <B value="0.26829" />
-  <C value="653" />
-  <D value="0.29808" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="631.37" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="69.93885" />
-  <B value="-7280.529" />
-  <C value="-6.943105" />
-  <D value="3.624646E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="241.45" />
-  <Tmax units="K"  value="653" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.763E+07" />
-  <B value="1.0666" />
-  <C value="-1.0647" />
-  <D value="0.39633" />
-  <E value="0.019258" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="631.37" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5371.7" />
-  <B value="717.87" />
-  <C value="-1.4937" />
-  <D value="0.0041059" />
-  <E value="-0.0000050183" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="242" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="17987" />
-  <B value="-72.539" />
-  <C value="10.794" />
-  <D value="0.0063056" />
-  <E value="-0.0000049607" />
-  <Tmin units="K"  value="250.9" />
-  <Tmax units="K"  value="489.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63931" />
-  <B value="-772.15" />
-  <C value="13.468" />
-  <D value="-0.00038098" />
-  <E value="7.7306E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.191" />
-  <B value="-261.99" />
-  <C value="-70.335" />
-  <D value="-58777" />
-  <E value="93808" />
-  <Tmin units="K"  value="326.5" />
-  <Tmax units="K"  value="1791.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-37.877" />
-  <B value="3012.8" />
-  <C value="3.7501" />
-  <D value="0.0000021994" />
-  <E value="2" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="428.58" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.3484E-08" />
-  <B value="0.89115" />
-  <C value="65.345" />
-  <D value="-657.26" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11507" />
-  <B value="-853.65" />
-  <C value="4.7946" />
-  <D value="-0.021722" />
-  <E value="0.0000091954" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="428.58" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-1104.9" />
-  <B value="-0.018396" />
-  <C value="479160" />
-  <D value="-8.1392E+09" />
-  <Tmin units="K"  value="428.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011699" />
-  <B value="67.123" />
-  <C value="-3.1713" />
-  <D value="0.0010174" />
-  <E value="-0.0000048961" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="631.37" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-37786.54" />
-  <B value="553.5432" />
-  <C value="-0.19528" />
-  <D value="-0.000015263" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-19.94714" />
-  <B value="-9100" />
-  <C value="-54.6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.878" />
-  <B value="4095.6" />
-  <C value="-32.667" />
-  <Tmin units="K"  value="392" />
-  <Tmax units="K"  value="566.47" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="6.2624" />
-  <B value="-0.062923" />
-  <C value="0.000071015" />
-  <Tmin units="K"  value="242" />
-  <Tmax units="K"  value="428.58" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3271" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.4136E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="211.4629" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.23" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="124.61" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0447" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.950333" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.44089" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.104167" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.07" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.11" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.445" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20139.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.104167" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="20"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="4" />
-  <group id="20"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="5" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="4" />
-  <group id="20"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="19"  value="1" />
-  <group id="78"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-94-1" />
-<Smiles name="SMILES"  value="C1(=O)CCCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="137" />
-<CompoundID name="Name"  value="Cyclohexane" />
-<StructureFormula name="Structure"  value="-(CH2)6-" />
-<Family name="Family"  value="5" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="553.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4073000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.308" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="353.93" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="279.69" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="279.69" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="5362.51" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.161" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10875" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.211" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.242E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16740" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0614" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.1E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.233E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.191E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="297276" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2740000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.84082" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.656E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.172" />
-  <B value="-1.6546E-09" />
-  <Tmin units="K"  value="93.15" />
-  <Tmax units="K"  value="102.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.93459" />
-  <B value="0.28022" />
-  <C value="553.5" />
-  <D value="0.29409" />
-  <Tmin units="K"  value="279.69" />
-  <Tmax units="K"  value="539.37" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="79.82965" />
-  <B value="-6246.688" />
-  <C value="-8.778766" />
-  <D value="6.933726E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="263.06" />
-  <Tmax units="K"  value="553.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.4856E+07" />
-  <B value="0.35691" />
-  <C value="0.26181" />
-  <D value="-0.47647" />
-  <E value="0.25741" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="543.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15676" />
-  <B value="1496.2" />
-  <C value="-12.474" />
-  <D value="0.05833" />
-  <E value="-0.000090756" />
-  <Tmin units="K"  value="12.72" />
-  <Tmax units="K"  value="214.1" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116110" />
-  <B value="127.67" />
-  <C value="6.7654" />
-  <D value="0.01311" />
-  <E value="-0.0000060013" />
-  <Tmin units="K"  value="279.69" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="42569" />
-  <B value="-588.9" />
-  <C value="12.962" />
-  <D value="0.00028376" />
-  <E value="-1.4009E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18016" />
-  <B value="-184.14" />
-  <C value="-29.307" />
-  <D value="-1704.4" />
-  <E value="611.89" />
-  <Tmin units="K"  value="276.7" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-132.2852" />
-  <B value="5905.41" />
-  <C value="18.88092" />
-  <D value="-0.000023942" />
-  <E value="2" />
-  <Tmin units="K"  value="279.69" />
-  <Tmax units="K"  value="443.04" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.7726E-08" />
-  <B value="0.83665" />
-  <C value="36.786" />
-  <D value="-20.301" />
-  <Tmin units="K"  value="279.69" />
-  <Tmax units="K"  value="900" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.073881" />
-  <B value="-301.5" />
-  <C value="0.30119" />
-  <D value="-0.0068406" />
-  <E value="-0.0000028646" />
-  <Tmin units="K"  value="279.69" />
-  <Tmax units="K"  value="353.87" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="8.5865E-07" />
-  <B value="1.771" />
-  <C value="243.16" />
-  <D value="-9.1779" />
-  <Tmin units="K"  value="325" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0087482" />
-  <B value="76.318" />
-  <C value="-3.6017" />
-  <D value="0.0023868" />
-  <E value="-0.0000086088" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="539.37" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="33549" />
-  <B value="-36.858" />
-  <C value="1.3997" />
-  <D value="-0.0017273" />
-  <E value="6.4404E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.079" />
-  <B value="3073.1" />
-  <C value="-32.254" />
-  <Tmin units="K"  value="333.15" />
-  <Tmax units="K"  value="498.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.4141" />
-  <B value="-0.040658" />
-  <C value="0.000041452" />
-  <Tmin units="K"  value="279.69" />
-  <Tmax units="K"  value="443.04" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.30899" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.984576E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="337.4554" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2729" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.39847" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.043" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.781822" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.21277" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10886" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.0464" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.24" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.24" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004637" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.94148" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2032" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16773.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1087" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="6" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="6" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="13"  value="6" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="2"  value="6" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="2"  value="6" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="78"  value="6" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-82-7" />
-<Smiles name="SMILES"  value="C1CCCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="216" />
-<CompoundID name="Name"  value="1-hexene" />
-<StructureFormula name="Structure"  value="CH2CH(CH2)3CH3" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="504" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3143000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3551" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="336.63" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="133.39" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="133.39" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000516" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.161" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1259" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.281" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.66E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15130" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06477" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.11E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.167E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="8.7E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="386300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9347000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91267" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.7397E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.136" />
-  <B value="-0.0098653" />
-  <Tmin units="K"  value="53.36" />
-  <Tmax units="K"  value="133.39" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.42588" />
-  <B value="0.20073" />
-  <C value="504" />
-  <D value="0.21659" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="503.53" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="61.18966" />
-  <B value="-5302.032" />
-  <C value="-5.914346" />
-  <D value="4.387106E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="504" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.3654E+07" />
-  <B value="0.036065" />
-  <C value="1.7176" />
-  <D value="-2.6805" />
-  <E value="1.3349" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="484.49" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-4541.5" />
-  <B value="446.61" />
-  <C value="22.183" />
-  <D value="-0.29201" />
-  <E value="0.0010887" />
-  <Tmin units="K"  value="11" />
-  <Tmax units="K"  value="132" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="120740" />
-  <B value="197.35" />
-  <C value="7.4671" />
-  <D value="0.012038" />
-  <E value="-0.0000076352" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="404" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="79063" />
-  <B value="-588.63" />
-  <C value="12.822" />
-  <D value="0.00010837" />
-  <E value="-3.9549E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20992" />
-  <B value="-237.14" />
-  <C value="-25.743" />
-  <D value="-1791.1" />
-  <E value="2218.7" />
-  <Tmin units="K"  value="251.99" />
-  <Tmax units="K"  value="1763.93" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.027" />
-  <B value="774.41" />
-  <C value="-0.14562" />
-  <D value="-2.993E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="336.63" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.708E-08" />
-  <B value="0.81478" />
-  <C value="53.202" />
-  <D value="774.03" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.049094" />
-  <B value="18.334" />
-  <C value="-2.2175" />
-  <D value="0.0015607" />
-  <E value="-0.000010695" />
-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="383.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000064257" />
-  <B value="1.1355" />
-  <C value="445.14" />
-  <D value="64830" />
-  <Tmin units="K"  value="336.63" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012297" />
-  <B value="11.887" />
-  <C value="-2.8945" />
-  <D value="-0.00077443" />
-  <E value="-0.0000046447" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="484.49" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="52406" />
-  <B value="102.7" />
-  <C value="0.8529" />
-  <D value="-0.0011866" />
-  <E value="4.7459E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.306" />
-  <B value="2992.5" />
-  <C value="-30.644" />
-  <Tmin units="K"  value="302.74" />
-  <Tmax units="K"  value="445.48" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.31346" />
-  <B value="-0.05007" />
-  <C value="0.000071081" />
-  <Tmin units="K"  value="133.39" />
-  <Tmax units="K"  value="336.63" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.35089" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.473968E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="279.8451" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0462" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.671653" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.28499" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.125765" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.27" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.64" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003219" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2463" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15136.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1258" />
-<UnifacVLE name="UNIFAC" >
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-<UnifacLLE name="UNIFAC-LLE" >
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-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
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-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="592-41-6" />
-<Smiles name="SMILES"  value="C=CCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="105" />
-<CompoundID name="Name"  value="Methylcyclopentane" />
-<StructureFormula name="Structure"  value="(C5H9)CH3" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="532.79" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3784000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.319" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="344.98" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="130.73" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="130.73" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000224525" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.161" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.11313" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.227" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.299E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16100" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06017" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.52E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.062E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.63E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="339900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6929000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.89391" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.6741E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.305" />
-  <B value="-0.011236" />
-  <Tmin units="K"  value="52.29" />
-  <Tmax units="K"  value="130.73" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.63455" />
-  <B value="0.23477" />
-  <C value="532.79" />
-  <D value="0.24394" />
-  <Tmin units="K"  value="130.73" />
-  <Tmax units="K"  value="532.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="63.18203" />
-  <B value="-5470.368" />
-  <C value="-6.215132" />
-  <D value="4.384737E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="130.73" />
-  <Tmax units="K"  value="532.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.986429E+07" />
-  <B value="0.75425" />
-  <C value="-0.186227" />
-  <D value="-0.50621" />
-  <E value="0.35999" />
-  <Tmin units="K"  value="130.72" />
-  <Tmax units="K"  value="532.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-21181" />
-  <B value="1799.3" />
-  <C value="-12.463" />
-  <D value="0.018536" />
-  <E value="0.00015326" />
-  <Tmin units="K"  value="20.92" />
-  <Tmax units="K"  value="130.72" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="102830" />
-  <B value="317.53" />
-  <C value="4.999" />
-  <D value="0.022368" />
-  <E value="-0.000020298" />
-  <Tmin units="K"  value="126.58" />
-  <Tmax units="K"  value="366.48" />
-  </LiquidHeatCapacityCp>
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-  <eqno value="16" />
-  <A value="55624" />
-  <B value="-676.34" />
-  <C value="13.207" />
-  <D value="-0.0001363" />
-  <E value="2.6321E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12419" />
-  <B value="-105.76" />
-  <C value="-38.365" />
-  <D value="4383.1" />
-  <E value="-10749" />
-  <Tmin units="K"  value="250.72" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.2288" />
-  <B value="846.65" />
-  <C value="-0.18612" />
-  <D value="-0.0000022383" />
-  <E value="2" />
-  <Tmin units="K"  value="248.15" />
-  <Tmax units="K"  value="353.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000009078" />
-  <B value="0.495" />
-  <C value="355.78" />
-  <D value="10.622" />
-  <Tmin units="K"  value="130.73" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.040815" />
-  <B value="4.4808" />
-  <C value="-1.5434" />
-  <D value="-0.00050494" />
-  <E value="-0.0000017671" />
-  <Tmin units="K"  value="130.73" />
-  <Tmax units="K"  value="344.95" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0076653" />
-  <B value="0.48521" />
-  <C value="479.72" />
-  <D value="658190" />
-  <Tmin units="K"  value="344.96" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0093168" />
-  <B value="26.403" />
-  <C value="-3.0884" />
-  <D value="0.00036246" />
-  <E value="-0.0000065372" />
-  <Tmin units="K"  value="130.73" />
-  <Tmax units="K"  value="532.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="44724" />
-  <B value="-68.661" />
-  <C value="1.4378" />
-  <D value="-0.0017998" />
-  <E value="6.8702E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.957" />
-  <B value="2887.5" />
-  <C value="-38.834" />
-  <Tmin units="K"  value="319.7" />
-  <Tmax units="K"  value="477.59" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.3777" />
-  <B value="-0.03038" />
-  <C value="0.00003135" />
-  <Tmin units="K"  value="248.15" />
-  <Tmax units="K"  value="353.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.31812" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.081712E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="320.5659" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.53959" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0432" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.752065" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.23217" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.113042" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.97" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.01" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001461" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.1464" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2346" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16057.17" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1131" />
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-  <group id="3"  value="1" />
-  </GCmethod>
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-  <group id="3"  value="1" />
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-  <group id="78"  value="4" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="96-37-7" />
-<Smiles name="SMILES"  value="C1(C)CCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1151" />
-<CompoundID name="Name"  value="Cyclohexanol" />
-<StructureFormula name="Structure"  value="-CH(OH)(CH2)4CH2-" />
-<Family name="Family"  value="47" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="650.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4260000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.322" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="434" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="296.6" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="296.6" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="76.4997" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.159" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.105751" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.369047" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.601E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06484" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.78E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.862E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.095E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="327700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1783000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.70742" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.4639E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.987" />
-  <B value="-0.004344" />
-  <Tmin units="K"  value="118.64" />
-  <Tmax units="K"  value="296.6" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.90826" />
-  <B value="0.27716" />
-  <C value="650.1" />
-  <D value="0.30685" />
-  <Tmin units="K"  value="296.6" />
-  <Tmax units="K"  value="631.49" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-31.63718" />
-  <B value="-3989.985" />
-  <C value="9.013268" />
-  <D value="-0.0000126698" />
-  <E value="2" />
-  <Tmin units="K"  value="296.6" />
-  <Tmax units="K"  value="650.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.128838E+07" />
-  <B value="0.392061" />
-  <C value="-2.168338" />
-  <D value="5.552036" />
-  <E value="-3.376933" />
-  <Tmin units="K"  value="296.6" />
-  <Tmax units="K"  value="631.49" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-7568.9" />
-  <B value="1079.5" />
-  <C value="-5.8888" />
-  <D value="0.020493" />
-  <E value="-0.000021735" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="260" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-69485" />
-  <B value="774.7" />
-  <C value="4.4167" />
-  <D value="0.025384" />
-  <E value="-0.000022994" />
-  <Tmin units="K"  value="296.6" />
-  <Tmax units="K"  value="434" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="82477" />
-  <B value="-807.95" />
-  <C value="13.526" />
-  <D value="-0.00028702" />
-  <E value="2.5016E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21842" />
-  <B value="-283.51" />
-  <C value="-60.937" />
-  <D value="-15490" />
-  <E value="3379.6" />
-  <Tmin units="K"  value="325.05" />
-  <Tmax units="K"  value="1992" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-437.51" />
-  <B value="22529" />
-  <C value="63.787" />
-  <D value="-0.000049001" />
-  <E value="2" />
-  <Tmin units="K"  value="296.6" />
-  <Tmax units="K"  value="520.08" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.1528E-08" />
-  <B value="0.83387" />
-  <C value="90.96" />
-  <D value="4936.6" />
-  <Tmin units="K"  value="296.6" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.075187" />
-  <B value="-249.81" />
-  <C value="-0.16784" />
-  <D value="-0.0068233" />
-  <E value="0.0000026882" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="563.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0030349" />
-  <B value="0.6097" />
-  <C value="669.35" />
-  <D value="478820" />
-  <Tmin units="K"  value="434" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.026687" />
-  <B value="-3.1724" />
-  <C value="-2.4129" />
-  <D value="-0.00081796" />
-  <E value="-0.0000016257" />
-  <Tmin units="K"  value="289.35" />
-  <Tmax units="K"  value="631.49" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-55496.57" />
-  <B value="720.9032" />
-  <C value="-0.408358" />
-  <D value="0.0000822993" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.352" />
-  <B value="2624.4" />
-  <C value="-136.7" />
-  <Tmin units="K"  value="393.5" />
-  <Tmax units="K"  value="575.68" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="19.441" />
-  <B value="-0.10551" />
-  <C value="0.000099651" />
-  <Tmin units="K"  value="296.6" />
-  <Tmax units="K"  value="520.08" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3377" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.623128E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="305.6995" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.24" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="129.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="2.33694" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0456" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.961934" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.5296" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.104294" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.27" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.51" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-2.208" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.514148" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23672.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.104294" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="78"  value="5" />
-  <group id="79"  value="1" />
-  <group id="81"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-93-0" />
-<Smiles name="SMILES"  value="OC1CCCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="14" />
-<CompoundID name="Name"  value="2,2-dimethylbutane" />
-<StructureFormula name="Structure"  value="CH3CH2C(CH3)3" />
-<Family name="Family"  value="3" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="488.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3080000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3591" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="322.87" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="174.28" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="174.28" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="4.0748" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.177" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13373" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.233" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.476E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13770" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06824" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.83E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.8468E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-8745000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="358340" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="579100" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.8342" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.8411E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.998" />
-  <B value="-0.0069098" />
-  <Tmin units="K"  value="69.71" />
-  <Tmax units="K"  value="174.28" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.68727" />
-  <B value="0.26184" />
-  <C value="489.01" />
-  <D value="0.26217" />
-  <Tmin units="K"  value="174.28" />
-  <Tmax units="K"  value="489" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="94.2252" />
-  <B value="-6117.857" />
-  <C value="-11.25759" />
-  <D value="0.0000123761" />
-  <E value="2" />
-  <Tmin units="K"  value="174.28" />
-  <Tmax units="K"  value="489" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.850808E+07" />
-  <B value="1.595989" />
-  <C value="-1.437803" />
-  <D value="0.0287957" />
-  <E value="0.293443" />
-  <Tmin units="K"  value="174.28" />
-  <Tmax units="K"  value="472.44" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19150" />
-  <B value="1973.9" />
-  <C value="-19.068" />
-  <D value="0.10881" />
-  <E value="-0.0001861" />
-  <Tmin units="K"  value="12.86" />
-  <Tmax units="K"  value="167.68" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="117360" />
-  <B value="-28.344" />
-  <C value="9.2143" />
-  <D value="0.0086854" />
-  <E value="-0.00000596" />
-  <Tmin units="K"  value="174.28" />
-  <Tmax units="K"  value="322.88" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="73375" />
-  <B value="-521.55" />
-  <C value="12.775" />
-  <D value="0.00038975" />
-  <E value="-1.1854E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19877" />
-  <B value="-197.24" />
-  <C value="-29.493" />
-  <D value="-899.68" />
-  <E value="-190.18" />
-  <Tmin units="K"  value="244.37" />
-  <Tmax units="K"  value="1954.92" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="22.562" />
-  <B value="-455.85" />
-  <C value="-5.0804" />
-  <D value="-5.7101E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="322.88" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9362E-07" />
-  <B value="0.68259" />
-  <C value="102.35" />
-  <D value="-10.082" />
-  <Tmin units="K"  value="174.28" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.038291" />
-  <B value="4.8824" />
-  <C value="-1.6311" />
-  <D value="-0.00047294" />
-  <E value="-0.0000023877" />
-  <Tmin units="K"  value="174.28" />
-  <Tmax units="K"  value="322.89" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00018521" />
-  <B value="0.9549" />
-  <C value="83.825" />
-  <D value="174320" />
-  <Tmin units="K"  value="322.88" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012433" />
-  <B value="29.735" />
-  <C value="-3.2504" />
-  <D value="0.00031415" />
-  <E value="-0.0000057433" />
-  <Tmin units="K"  value="174.28" />
-  <Tmax units="K"  value="472.44" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="25002" />
-  <B value="324.75" />
-  <C value="0.40334" />
-  <D value="-0.00068536" />
-  <E value="2.7995E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.782" />
-  <B value="2690.4" />
-  <C value="-32.326" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="439.31" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-3.3309" />
-  <B value="-0.018831" />
-  <C value="0.00001104" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="322.88" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.366863" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.326557E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="294.0381" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="127.74" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.0743" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0475" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.65323" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.23385" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.133712" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.4983" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.932" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.006195" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.31834" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.23385" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13771.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.133712" />
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-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
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-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
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-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
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-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-83-2" />
-<Smiles name="SMILES"  value="CC(C)(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="15" />
-<CompoundID name="Name"  value="2,3-dimethylbutane" />
-<StructureFormula name="Structure"  value="(CH3)2CHCH(CH3)2" />
-<Family name="Family"  value="3" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="499.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3130000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3576" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="331.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="145.19" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="145.19" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0152127" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.177" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13117" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.248" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.636E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14300" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06824" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.62E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.768E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3125000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="365920" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="799100" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.85804" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.84761E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.428" />
-  <B value="-0.008415" />
-  <Tmin units="K"  value="58.08" />
-  <Tmax units="K"  value="145.19" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.67999" />
-  <B value="0.25932" />
-  <C value="500.01" />
-  <D value="0.25836" />
-  <Tmin units="K"  value="145.19" />
-  <Tmax units="K"  value="500" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="76.80058" />
-  <B value="-5679.218" />
-  <C value="-8.443302" />
-  <D value="7.93783E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="145.19" />
-  <Tmax units="K"  value="500" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.7443E+07" />
-  <B value="0.91932" />
-  <C value="-0.91329" />
-  <D value="0.50392" />
-  <E value="-0.089442" />
-  <Tmin units="K"  value="145.19" />
-  <Tmax units="K"  value="481.33" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-21392" />
-  <B value="2002.6" />
-  <C value="-18.844" />
-  <D value="0.11065" />
-  <E value="-0.00021726" />
-  <Tmin units="K"  value="17.2" />
-  <Tmax units="K"  value="136.07" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="126350" />
-  <B value="-53.429" />
-  <C value="8.8794" />
-  <D value="0.010279" />
-  <E value="-0.0000080841" />
-  <Tmin units="K"  value="145.19" />
-  <Tmax units="K"  value="331.13" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="46722" />
-  <B value="-391.59" />
-  <C value="12.599" />
-  <D value="0.00056088" />
-  <E value="-1.7583E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20289" />
-  <B value="-208.43" />
-  <C value="-28.236" />
-  <D value="-12822" />
-  <E value="38509" />
-  <Tmin units="K"  value="295.95" />
-  <Tmax units="K"  value="1999.72" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="6.9204" />
-  <B value="231.1" />
-  <C value="-2.7393" />
-  <D value="-1.3079E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="331.13" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.8449E-07" />
-  <B value="0.52371" />
-  <C value="291.92" />
-  <D value="-3199.1" />
-  <Tmin units="K"  value="145.19" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.05308" />
-  <B value="-5.5491" />
-  <C value="-1.4118" />
-  <D value="-0.0011735" />
-  <E value="-7.4229E-07" />
-  <Tmin units="K"  value="140" />
-  <Tmax units="K"  value="331.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000032078" />
-  <B value="1.1749" />
-  <C value="-107.52" />
-  <D value="129270" />
-  <Tmin units="K"  value="331.13" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013057" />
-  <B value="15.542" />
-  <C value="-3.0183" />
-  <D value="-0.0004395" />
-  <E value="-0.0000046347" />
-  <Tmin units="K"  value="145.19" />
-  <Tmax units="K"  value="481.33" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18408" />
-  <B value="618.2" />
-  <C value="-0.30739" />
-  <D value="0.000022699" />
-  <E value="2.5609E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.905" />
-  <B value="2797" />
-  <C value="-32.946" />
-  <Tmin units="K"  value="300.4" />
-  <Tmax units="K"  value="443.98" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.7621" />
-  <B value="-0.029455" />
-  <C value="0.000029461" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="331.13" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.361" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.40238E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="289.0044" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2694" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="127.74" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.02497" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0473" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.665168" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2477" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.13105" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.4982" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.848" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004579" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.01856" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.24754" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14352.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.13105" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-29-8" />
-<Smiles name="SMILES"  value="CC(C)C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="11" />
-<CompoundID name="Name"  value="N-hexane" />
-<StructureFormula name="Structure"  value="CH3(CH2)4CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="507.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3025000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.368" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="341.88" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="177.83" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="177.83" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.901695" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.177" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13159" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.297" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.769E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14870" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06826" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.64E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.6694E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-66340" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="388740" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.308E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93264" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.8551E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.657" />
-  <B value="-0.004653" />
-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="177.86" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.55661" />
-  <B value="0.23506" />
-  <C value="507.6" />
-  <D value="0.24183" />
-  <Tmin units="K"  value="177.83" />
-  <Tmax units="K"  value="507.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="71.56625" />
-  <B value="-5848.968" />
-  <C value="-7.46028" />
-  <D value="0.0000050823" />
-  <E value="2" />
-  <Tmin units="K"  value="174.15" />
-  <Tmax units="K"  value="507.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.086241E+07" />
-  <B value="-1.014854" />
-  <C value="4.97802" />
-  <D value="-6.266175" />
-  <E value="2.685532" />
-  <Tmin units="K"  value="177.83" />
-  <Tmax units="K"  value="493.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-24158" />
-  <B value="1979.3" />
-  <C value="-14.888" />
-  <D value="0.068541" />
-  <E value="-0.0001167" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="177.86" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="155690" />
-  <B value="5.9137" />
-  <C value="7.3123" />
-  <D value="0.013809" />
-  <E value="-0.0000093814" />
-  <Tmin units="K"  value="177.83" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94649" />
-  <B value="-698.41" />
-  <C value="13.164" />
-  <D value="-0.00011992" />
-  <E value="2.9719E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25955" />
-  <B value="-274.01" />
-  <C value="-26.704" />
-  <D value="-1514.2" />
-  <E value="-624.88" />
-  <Tmin units="K"  value="184" />
-  <Tmax units="K"  value="1775.9" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-62.582" />
-  <B value="2308.7" />
-  <C value="8.5085" />
-  <D value="-0.000019741" />
-  <E value="2" />
-  <Tmin units="K"  value="174.65" />
-  <Tmax units="K"  value="406.08" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.3843E-07" />
-  <B value="0.62082" />
-  <C value="239.17" />
-  <D value="-260.6" />
-  <Tmin units="K"  value="177.83" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.12682" />
-  <B value="-1.5015" />
-  <C value="-1.0467" />
-  <D value="-0.00088709" />
-  <E value="-9.3679E-07" />
-  <Tmin units="K"  value="177.83" />
-  <Tmax units="K"  value="370" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-569.52" />
-  <B value="0.7943" />
-  <C value="-1.1379E+09" />
-  <D value="-8.2055E+09" />
-  <Tmin units="K"  value="339.09" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.10385" />
-  <B value="-14.131" />
-  <C value="-1.6676" />
-  <D value="-0.0015618" />
-  <E value="8.4369E-07" />
-  <Tmin units="K"  value="177.83" />
-  <Tmax units="K"  value="493.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="73425" />
-  <B value="-1.3802" />
-  <C value="1.1891" />
-  <D value="-0.0015227" />
-  <E value="5.9232E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.746" />
-  <B value="2711.8" />
-  <C value="-47.914" />
-  <Tmin units="K"  value="304.74" />
-  <Tmax units="K"  value="455.53" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.4168" />
-  <B value="-0.034217" />
-  <C value="0.000039014" />
-  <Tmin units="K"  value="174.65" />
-  <Tmax units="K"  value="406.08" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3682" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.611036E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="274.2893" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2635" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="127.74" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0479" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.662664" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3007" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.131306" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.4998" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.856" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.856" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.007459" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2927" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14870.79" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1316" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-54-3" />
-<Smiles name="SMILES"  value="CCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="12" />
-<CompoundID name="Name"  value="2-methylpentane" />
-<StructureFormula name="Structure"  value="CH3CH2CH2CH(CH3)2" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="497.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3010000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3667" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="333.4" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="119.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="119.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000206558" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.177" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13289" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.278" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.784E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14400" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06825" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.63E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.7455E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5338000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380890" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6268000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95879" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.84915E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.67" />
-  <B value="-0.010749" />
-  <Tmin units="K"  value="47.82" />
-  <Tmax units="K"  value="119.55" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.657" />
-  <B value="0.25467" />
-  <C value="497.71" />
-  <D value="0.26808" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="497.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="77.6873" />
-  <B value="-5802.911" />
-  <C value="-8.543267" />
-  <D value="7.871718E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="497.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.724E+07" />
-  <B value="0.784961" />
-  <C value="-0.571271" />
-  <D value="0.114935" />
-  <E value="0.0796185" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="477.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16692" />
-  <B value="1658.2" />
-  <C value="-10.279" />
-  <D value="0.040384" />
-  <E value="-0.000049521" />
-  <Tmin units="K"  value="18" />
-  <Tmax units="K"  value="119.53" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="137510" />
-  <B value="-55.266" />
-  <C value="8.2006" />
-  <D value="0.013273" />
-  <E value="-0.00001165" />
-  <Tmin units="K"  value="103.56" />
-  <Tmax units="K"  value="333.41" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="70761" />
-  <B value="-504.8" />
-  <C value="12.795" />
-  <D value="0.00029839" />
-  <E value="-9.4564E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20379" />
-  <B value="-202.65" />
-  <C value="-31.838" />
-  <D value="492.86" />
-  <E value="-3834.6" />
-  <Tmin units="K"  value="248.73" />
-  <Tmax units="K"  value="1989.8" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.416" />
-  <B value="938.41" />
-  <C value="0.18259" />
-  <D value="4.2586E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="333.41" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000020458" />
-  <B value="0.38326" />
-  <C value="542.64" />
-  <D value="-1147.6" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.099248" />
-  <B value="3.6931" />
-  <C value="-1.2881" />
-  <D value="-0.00063949" />
-  <E value="-0.0000011122" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="389.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000056887" />
-  <B value="1.0953" />
-  <C value="-66.761" />
-  <D value="139530" />
-  <Tmin units="K"  value="333.41" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015522" />
-  <B value="7.9529" />
-  <C value="-2.8734" />
-  <D value="-0.0008781" />
-  <E value="-0.0000036183" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="477.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="17427" />
-  <B value="385.95" />
-  <C value="0.25974" />
-  <D value="-0.0005678" />
-  <E value="2.4129E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.737" />
-  <B value="2653.5" />
-  <C value="-45.343" />
-  <Tmin units="K"  value="298.67" />
-  <Tmax units="K"  value="437.99" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.1171" />
-  <B value="-0.062164" />
-  <C value="0.00009219" />
-  <Tmin units="K"  value="119.55" />
-  <Tmax units="K"  value="333.41" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3677" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.51431E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="279.9927" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2581" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="127.74" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.45339" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.048" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.656507" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2791" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.132931" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.499" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.852" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003898" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.85782" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2791" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14417.6" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.132931" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-83-5" />
-<Smiles name="SMILES"  value="CC(C)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="13" />
-<CompoundID name="Name"  value="3-methylpentane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)CH2CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="504.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3120000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3667" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="336.4" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="110.251" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="110.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="4.13745E-07" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.177" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13062" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.273" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.695E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14680" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06825" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.63E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.72E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3420000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="383000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5303200" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0567" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.85137E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.818" />
-  <B value="-0.011634" />
-  <Tmin units="K"  value="44.1" />
-  <Tmax units="K"  value="110.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.64191" />
-  <B value="0.2518" />
-  <C value="504.61" />
-  <D value="0.25114" />
-  <Tmin units="K"  value="110.25" />
-  <Tmax units="K"  value="504.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="103.3869" />
-  <B value="-6792.289" />
-  <C value="-12.56583" />
-  <D value="0.0000127267" />
-  <E value="2" />
-  <Tmin units="K"  value="110.25" />
-  <Tmax units="K"  value="504.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.261039E+07" />
-  <B value="1.021512" />
-  <C value="-0.656827" />
-  <D value="-0.222599" />
-  <E value="0.294618" />
-  <Tmin units="K"  value="110.25" />
-  <Tmax units="K"  value="483.84" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16129" />
-  <B value="1666.4" />
-  <C value="-9.7944" />
-  <D value="0.031943" />
-  <E value="-0.0000041663" />
-  <Tmin units="K"  value="15.63" />
-  <Tmax units="K"  value="110.25" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="124870" />
-  <B value="37.47" />
-  <C value="8.4986" />
-  <D value="0.010489" />
-  <E value="-0.0000074005" />
-  <Tmin units="K"  value="79.81" />
-  <Tmax units="K"  value="336.43" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66323" />
-  <B value="-479.35" />
-  <C value="12.713" />
-  <D value="0.00041058" />
-  <E value="-1.3725E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2197" />
-  <B value="-311.6" />
-  <C value="-21.56" />
-  <D value="108.65" />
-  <E value="-1264.8" />
-  <Tmin units="K"  value="252.2" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-4.4466" />
-  <B value="561.39" />
-  <C value="-0.97496" />
-  <D value="-4.1525E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="336.42" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000014857" />
-  <B value="0.42502" />
-  <C value="455.77" />
-  <D value="119.73" />
-  <Tmin units="K"  value="110.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.013685" />
-  <B value="32.912" />
-  <C value="-2.24" />
-  <D value="0.00097964" />
-  <E value="-0.0000056292" />
-  <Tmin units="K"  value="110.25" />
-  <Tmax units="K"  value="402" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000050178" />
-  <B value="1.1143" />
-  <C value="-67.556" />
-  <D value="138050" />
-  <Tmin units="K"  value="336.42" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013421" />
-  <B value="7.9798" />
-  <C value="-2.865" />
-  <D value="-0.00092552" />
-  <E value="-0.0000040501" />
-  <Tmin units="K"  value="110.25" />
-  <Tmax units="K"  value="483.84" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="3600.2" />
-  <B value="92.648" />
-  <C value="0.060696" />
-  <D value="-0.00013403" />
-  <E value="5.737E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.831" />
-  <B value="2755" />
-  <C value="-40.41" />
-  <Tmin units="K"  value="304.91" />
-  <Tmax units="K"  value="442.33" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.2793" />
-  <B value="-0.02952" />
-  <C value="0.00003287" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="336.42" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.36333" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.342884E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="307.5203" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2575" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="127.74" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.3701" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0473" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.667684" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2741" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.130633" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.499" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.852" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.009786" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.7417" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.275" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14871.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.130633" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="96-14-0" />
-<Smiles name="SMILES"  value="CCC(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1203" />
-<CompoundID name="Name"  value="Triethylene glycol" />
-<StructureFormula name="Structure"  value="HOCH2CH2OCH2CH2OCH2CH2OH" />
-<Family name="Family"  value="49" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="769.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3320000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.443" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.23" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="561.5" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="265.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="265.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000327262" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="150.173" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.134127" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.755952" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.71E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="25710" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.97E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08486" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.22E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.251E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4.86E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="556500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.82E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.6" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.2498E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.6467" />
-  <B value="-0.0040367" />
-  <Tmin units="K"  value="106.38" />
-  <Tmax units="K"  value="265.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.60697" />
-  <B value="0.26444" />
-  <C value="769.5" />
-  <D value="0.24805" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="769.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-148.0973" />
-  <B value="-1446.895" />
-  <C value="26.95817" />
-  <D value="-0.0000266538" />
-  <E value="2" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="769.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.392895E+08" />
-  <B value="1.422819" />
-  <C value="-1.625802" />
-  <D value="1.207667" />
-  <E value="-0.563316" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="769.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7555" />
-  <B value="958.48" />
-  <C value="-1.8743" />
-  <D value="0.0048051" />
-  <E value="-0.0000054467" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="265.95" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="234210" />
-  <B value="-89.741" />
-  <C value="10.328" />
-  <D value="0.0058089" />
-  <E value="-0.0000030565" />
-  <Tmin units="K"  value="265.79" />
-  <Tmax units="K"  value="666.48" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="88442" />
-  <B value="-417.2" />
-  <C value="12.845" />
-  <D value="0.00037163" />
-  <E value="-1.3999E-07" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26304" />
-  <B value="-239.99" />
-  <C value="-308.91" />
-  <D value="-754640" />
-  <E value="1516300" />
-  <Tmin units="K"  value="384.75" />
-  <Tmax units="K"  value="1950" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-354.9911" />
-  <B value="16471.68" />
-  <C value="54.55389" />
-  <D value="-0.0481353" />
-  <E value="1" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="615.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.2508E-08" />
-  <B value="0.8077" />
-  <C value="134.01" />
-  <D value="-6653.4" />
-  <Tmin units="K"  value="265.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.089806" />
-  <B value="0.43077" />
-  <C value="-1.6802" />
-  <D value="0.0024003" />
-  <E value="-0.0000033612" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="666.48" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000048035" />
-  <B value="1.4025" />
-  <C value="164.43" />
-  <D value="15114" />
-  <Tmin units="K"  value="199.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.053881" />
-  <B value="-24.705" />
-  <C value="-1.9439" />
-  <D value="-0.00084717" />
-  <E value="-3.9189E-07" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="548.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="14259" />
-  <B value="713.43" />
-  <C value="-0.4134" />
-  <D value="0.000089194" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-12.58412" />
-  <B value="-10424.37" />
-  <C value="-5.193019" />
-  <Tmin units="K"  value="268" />
-  <Tmax units="K"  value="769" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.583" />
-  <B value="3555.2" />
-  <C value="-168.11" />
-  <Tmin units="K"  value="463.15" />
-  <Tmax units="K"  value="689.99" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="12.563" />
-  <B value="-0.071122" />
-  <C value="0.000060989" />
-  <Tmin units="K"  value="265.95" />
-  <Tmax units="K"  value="615.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.463689" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.297988E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="253.1291" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.224225" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.18" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0853" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.12845" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.758714" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.134187" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5342" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.12" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.758714" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23437.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.134187" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  <group id="26"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="4" />
-  <group id="14"  value="2" />
-  <group id="28"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  <group id="21"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  <group id="26"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="14"  value="2" />
-  <group id="25"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="112-27-6" />
-<Smiles name="SMILES"  value="OCCOCCOCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1706" />
-<CompoundID name="Name"  value="Triethylamine" />
-<StructureFormula name="Structure"  value="(C2H5)3N" />
-<Family name="Family"  value="35" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="535" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.39" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="362.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="158.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="158.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0106462" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="101.192" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13996" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.316193" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.73E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15170" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07603" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.064E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.58E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.141E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="405400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8520000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0865" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.0405E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.511" />
-  <B value="-0.0073745" />
-  <Tmin units="K"  value="63.38" />
-  <Tmax units="K"  value="158.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.74443" />
-  <B value="0.28147" />
-  <C value="535" />
-  <D value="0.29639" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="515.32" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="109.5632" />
-  <B value="-7670.939" />
-  <C value="-13.23524" />
-  <D value="8.526035E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="535.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.6361E+07" />
-  <B value="1.8179" />
-  <C value="-4.3508" />
-  <D value="5.0206" />
-  <E value="-2.0828" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="515.32" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="197480" />
-  <Tmin units="K"  value="293" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-68176" />
-  <B value="-83.963" />
-  <C value="12.887" />
-  <D value="-0.00053012" />
-  <E value="0.0000014554" />
-  <Tmin units="K"  value="172.06" />
-  <Tmax units="K"  value="362.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="118700" />
-  <B value="-798.83" />
-  <C value="13.439" />
-  <D value="-0.00026576" />
-  <E value="5.0253E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23952" />
-  <B value="-295.39" />
-  <C value="-29.513" />
-  <D value="-868.33" />
-  <E value="-1051.4" />
-  <Tmin units="K"  value="267.5" />
-  <Tmax units="K"  value="1872.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.1405" />
-  <B value="722.62" />
-  <C value="-0.37234" />
-  <D value="-0.0000014417" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="359.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.6298E-07" />
-  <B value="0.63337" />
-  <C value="296.37" />
-  <D value="-2057.9" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.073124" />
-  <B value="-11.318" />
-  <C value="-1.1721" />
-  <D value="-0.001404" />
-  <E value="-1.7908E-07" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="483.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013191" />
-  <B value="0.98598" />
-  <C value="87.622" />
-  <D value="150050" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013624" />
-  <B value="18.483" />
-  <C value="-2.9718" />
-  <D value="-0.00033783" />
-  <E value="-0.0000042148" />
-  <Tmin units="K"  value="158.45" />
-  <Tmax units="K"  value="515.32" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="38089" />
-  <B value="333.32" />
-  <C value="0.48166" />
-  <D value="-0.00083411" />
-  <E value="3.4863E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.736" />
-  <B value="2807.5" />
-  <C value="-56.935" />
-  <Tmin units="K"  value="321.01" />
-  <Tmax units="K"  value="475.67" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-2.4562" />
-  <B value="-0.026558" />
-  <C value="0.000027095" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="359.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.40259" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.771002E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="285.1725" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.262814" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="134.59" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.90597" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0526" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.73294" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.31959" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.139672" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.01" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.26" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.5972" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.316157" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15176.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.139672" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="36"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="31"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="36"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="35"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="121-44-8" />
-<Smiles name="SMILES"  value="CCN(CC)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="502" />
-<CompoundID name="Name"  value="Toluene" />
-<StructureFormula name="Structure"  value="(C6H5)CH3" />
-<Family name="Family"  value="16" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="591.75" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4108000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.316" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="383.79" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="178.18" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="178.18" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0475285" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="92.141" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10687" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.264" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.472E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05951" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.42E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="5.017E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.222E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="320990" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6636000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.94689" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.734E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.8605" />
-  <B value="0.013514" />
-  <Tmin units="K"  value="93.15" />
-  <Tmax units="K"  value="178.18" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.89799" />
-  <B value="0.27359" />
-  <C value="591.75" />
-  <D value="0.30006" />
-  <Tmin units="K"  value="163.1" />
-  <Tmax units="K"  value="589.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="32.89891" />
-  <B value="-5013.81" />
-  <C value="-1.348918" />
-  <D value="-1.869928E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="178.18" />
-  <Tmax units="K"  value="592.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.3752E+07" />
-  <B value="0.50341" />
-  <C value="0.24755" />
-  <D value="-0.72898" />
-  <E value="0.37794" />
-  <Tmin units="K"  value="178.18" />
-  <Tmax units="K"  value="569.98" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13924" />
-  <B value="1776.9" />
-  <C value="-16.369" />
-  <D value="0.074493" />
-  <E value="-0.00011377" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="178.18" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="28291" />
-  <B value="48.171" />
-  <C value="10.912" />
-  <D value="0.0020542" />
-  <E value="8.7875E-07" />
-  <Tmin units="K"  value="178.1" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="47225" />
-  <B value="-565.85" />
-  <C value="12.856" />
-  <D value="0.000005535" />
-  <E value="-1.998E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18928" />
-  <B value="-219.15" />
-  <C value="-45.645" />
-  <D value="1631.9" />
-  <E value="-13947" />
-  <Tmin units="K"  value="254" />
-  <Tmax units="K"  value="1775" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-152.84" />
-  <B value="5644.6" />
-  <C value="22.826" />
-  <D value="-0.000040987" />
-  <E value="2" />
-  <Tmin units="K"  value="178.18" />
-  <Tmax units="K"  value="383.78" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.5581E-07" />
-  <B value="0.49514" />
-  <C value="307.82" />
-  <D value="1891.6" />
-  <Tmin units="K"  value="178.18" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.072922" />
-  <B value="-23.153" />
-  <C value="-1.0277" />
-  <D value="-0.0017074" />
-  <E value="3.6787E-07" />
-  <Tmin units="K"  value="178.18" />
-  <Tmax units="K"  value="474.85" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000006541" />
-  <B value="1.4227" />
-  <C value="190.97" />
-  <D value="21890" />
-  <Tmin units="K"  value="383.78" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014261" />
-  <B value="19.666" />
-  <C value="-2.7922" />
-  <D value="-0.00035188" />
-  <E value="-0.0000037637" />
-  <Tmin units="K"  value="178.18" />
-  <Tmax units="K"  value="569.98" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-43647.49" />
-  <B value="603.542" />
-  <C value="-0.399451" />
-  <D value="0.000104382" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.864" />
-  <B value="3019.2" />
-  <C value="-60.13" />
-  <Tmin units="K"  value="355.37" />
-  <Tmax units="K"  value="526.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="4.3267" />
-  <B value="-0.064947" />
-  <C value="0.000084431" />
-  <Tmin units="K"  value="178.18" />
-  <Tmax units="K"  value="383.78" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.31369" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.283707E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="319.761" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2646" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="111.48" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.58961" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0435" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.870044" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2651" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10685" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9228" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.968" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="2.968" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005125" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2132" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2591" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18245.86" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1068" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="12"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="5" />
-  <group id="11"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="12"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="11"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-88-3" />
-<Smiles name="SMILES"  value="c1ccccc1(C)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1183" />
-<CompoundID name="Name"  value="M-cresol" />
-<StructureFormula name="Structure"  value="CH3(C6H4)OH" />
-<Family name="Family"  value="48" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="705.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4560000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.312" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.241" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="475.38" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="285.39" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="285.39" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="5.86242" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="108.14" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10499" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.452" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.87E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23900" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06503" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.18E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.323E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4.019E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="356040" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.0707E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.16481" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.52783E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="1.0425" />
-  <B value="0.033348" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="285.39" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.76595" />
-  <B value="0.25907" />
-  <C value="705.86" />
-  <D value="0.2605" />
-  <Tmin units="K"  value="285.39" />
-  <Tmax units="K"  value="705.85" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="143.16" />
-  <B value="-12586" />
-  <C value="-17.327" />
-  <D value="0.0000073113" />
-  <E value="2" />
-  <Tmin units="K"  value="285.39" />
-  <Tmax units="K"  value="705.85" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.4557E+07" />
-  <B value="0.36419" />
-  <C value="1.602" />
-  <D value="-2.5634" />
-  <E value="1.0947" />
-  <Tmin units="K"  value="285.39" />
-  <Tmax units="K"  value="705.85" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-8624" />
-  <B value="1322.8" />
-  <C value="-8.6572" />
-  <D value="0.031074" />
-  <E value="-0.000035842" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="285.39" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62676" />
-  <B value="-205.39" />
-  <C value="12.221" />
-  <D value="0.0027125" />
-  <E value="-0.0000038975" />
-  <Tmin units="K"  value="283" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="58129" />
-  <B value="-537.86" />
-  <C value="12.936" />
-  <D value="-0.000090368" />
-  <E value="1.797E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18861" />
-  <B value="-374.13" />
-  <C value="-74.545" />
-  <D value="-19672" />
-  <E value="24912" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-1098.989" />
-  <B value="45628.63" />
-  <C value="168.1502" />
-  <D value="-0.000185183" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="564.68" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4432E-07" />
-  <B value="0.74376" />
-  <C value="166.32" />
-  <D value="-45.138" />
-  <Tmin units="K"  value="285.39" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10478" />
-  <B value="-476.78" />
-  <C value="0.8844" />
-  <D value="-0.0090128" />
-  <E value="0.0000031516" />
-  <Tmin units="K"  value="285.39" />
-  <Tmax units="K"  value="475.43" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016795" />
-  <B value="0.9362" />
-  <C value="585.89" />
-  <D value="24552" />
-  <Tmin units="K"  value="475.43" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.037429" />
-  <B value="67.939" />
-  <C value="-2.7738" />
-  <D value="0.00028133" />
-  <E value="-0.0000016386" />
-  <Tmin units="K"  value="285.39" />
-  <Tmax units="K"  value="683.72" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="23954" />
-  <B value="227.87" />
-  <C value="0.66042" />
-  <D value="-0.0011161" />
-  <E value="4.8581E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-3.829242" />
-  <B value="-2500" />
-  <C value="-15" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.349" />
-  <B value="3668.1" />
-  <C value="-101.91" />
-  <Tmin units="K"  value="425" />
-  <Tmax units="K"  value="635" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="10.702" />
-  <B value="-0.065218" />
-  <C value="0.000050873" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="564.68" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.342" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.980332E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="274.6595" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.241" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="117.59" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.28602" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0461" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.03693" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.45399" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.104996" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7567" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.888" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.33197" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.45" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24080.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.104996" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-39-4" />
-<Smiles name="SMILES"  value="c1(O)cc(C)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1182" />
-<CompoundID name="Name"  value="O-cresol" />
-<StructureFormula name="Structure"  value="CH3(C6H4)OH" />
-<Family name="Family"  value="48" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="697.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.282" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.243" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="464.17" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="304.19" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="304.19" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="65.3261" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="108.14" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10364" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.435" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.787E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22870" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06503" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.18E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.2857E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.543E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="352590" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.582E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2881" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.528E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="4.5708" />
-  <B value="0.019375" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="307.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1115" />
-  <B value="0.30952" />
-  <C value="697.6" />
-  <D value="0.31161" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="676.85" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="140.51" />
-  <B value="-11819" />
-  <C value="-17.163" />
-  <D value="0.0000087043" />
-  <E value="2" />
-  <Tmin units="K"  value="303.15" />
-  <Tmax units="K"  value="697.65" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.9721E+07" />
-  <B value="1.0333" />
-  <C value="0.08043" />
-  <D value="-1.2193" />
-  <E value="0.58124" />
-  <Tmin units="K"  value="304.19" />
-  <Tmax units="K"  value="697.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-8031.4" />
-  <B value="1109.1" />
-  <C value="-6.0897" />
-  <D value="0.022423" />
-  <E value="-0.000027975" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="304.19" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="146600" />
-  <B value="-116.23" />
-  <C value="11.009" />
-  <D value="0.0034596" />
-  <E value="-0.0000033446" />
-  <Tmin units="K"  value="304.19" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="64367" />
-  <B value="-535.92" />
-  <C value="12.871" />
-  <D value="-0.000033383" />
-  <E value="-2.2759E-09" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19264" />
-  <B value="-372.93" />
-  <C value="-69.055" />
-  <D value="-19860" />
-  <E value="28563" />
-  <Tmin units="K"  value="313.15" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-455.0775" />
-  <B value="20670.83" />
-  <C value="67.87773" />
-  <D value="-0.0000660983" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="558.04" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.7371E-08" />
-  <B value="0.80775" />
-  <C value="98.538" />
-  <D value="-0.0034513" />
-  <Tmin units="K"  value="304.19" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.065471" />
-  <B value="92.351" />
-  <C value="-2.8415" />
-  <D value="0.0012245" />
-  <E value="-0.0000029956" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="464.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00018648" />
-  <B value="0.9302" />
-  <C value="709.37" />
-  <D value="-0.0036596" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0094371" />
-  <B value="291.18" />
-  <C value="-4.9944" />
-  <D value="0.0057186" />
-  <E value="-0.0000083653" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="697.55" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="23912" />
-  <B value="217.36" />
-  <C value="0.71039" />
-  <D value="-0.0011838" />
-  <E value="5.1458E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-10.30921" />
-  <B value="-5750" />
-  <C value="-34.5" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.629" />
-  <B value="3891.6" />
-  <C value="-79.086" />
-  <Tmin units="K"  value="419.41" />
-  <Tmax units="K"  value="625" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="8.2341" />
-  <B value="-0.06124" />
-  <C value="0.000056109" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="558.04" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.33928" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.682421E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="279.7063" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="117.59" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.4627" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0458" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.03606" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.43299" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.104368" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7567" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.888" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.2512" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.433455" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23397.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.104368" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="95-48-7" />
-<Smiles name="SMILES"  value="c1(O)c(C)cccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1184" />
-<CompoundID name="Name"  value="P-cresol" />
-<StructureFormula name="Structure"  value="CH3(C6H4)OH" />
-<Family name="Family"  value="48" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="704.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5150000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.277" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="475.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="307.93" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="307.93" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="34.4658" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="108.14" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.105" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.51" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.762E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24030" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06503" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.18E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.2535E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.166E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="350750" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.2707E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.5401" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.52256E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.671" />
-  <B value="2.0813E-16" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="307.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.94818" />
-  <B value="0.2877" />
-  <C value="704.66" />
-  <D value="0.2873" />
-  <Tmin units="K"  value="307.89" />
-  <Tmax units="K"  value="704.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="236.9207" />
-  <B value="-17215.31" />
-  <C value="-31.28645" />
-  <D value="0.0000163766" />
-  <E value="2" />
-  <Tmin units="K"  value="307.93" />
-  <Tmax units="K"  value="704.65" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.3617E+08" />
-  <B value="1.404" />
-  <C value="0.8091" />
-  <D value="-3.6055" />
-  <E value="2.0268" />
-  <Tmin units="K"  value="307.93" />
-  <Tmax units="K"  value="704.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-8780.1" />
-  <B value="1223.4" />
-  <C value="-7.2115" />
-  <D value="0.025844" />
-  <E value="-0.000031593" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="307.93" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="142400" />
-  <B value="625.27" />
-  <C value="3.2944" />
-  <D value="0.02818" />
-  <E value="-0.000027958" />
-  <Tmin units="K"  value="307.93" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="58748" />
-  <B value="-529.02" />
-  <C value="12.887" />
-  <D value="-0.0000351" />
-  <E value="-1.6131E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19347" />
-  <B value="-378.82" />
-  <C value="-72.032" />
-  <D value="-21261" />
-  <E value="30195" />
-  <Tmin units="K"  value="313.15" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-820.7853" />
-  <B value="35522.87" />
-  <C value="124.3969" />
-  <D value="-0.000127538" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="563.72" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4308E-07" />
-  <B value="0.74508" />
-  <C value="159.9" />
-  <D value="-24.834" />
-  <Tmin units="K"  value="307.93" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.061771" />
-  <B value="-123.88" />
-  <C value="-1.1823" />
-  <D value="-0.0033339" />
-  <E value="0.0000010151" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="475.13" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016735" />
-  <B value="0.93839" />
-  <C value="592.49" />
-  <D value="25704" />
-  <Tmin units="K"  value="475.13" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.051662" />
-  <B value="10.481" />
-  <C value="-2.2269" />
-  <D value="-0.00060182" />
-  <E value="-6.5093E-07" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="683.77" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-37249.74" />
-  <B value="691.7826" />
-  <C value="-0.559108" />
-  <D value="0.000190677" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.853943" />
-  <B value="-2500" />
-  <C value="-15" />
-  <Tmin units="K"  value="249.7056" />
-  <Tmax units="K"  value="419.7056" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.566" />
-  <B value="3833.1" />
-  <C value="-93.483" />
-  <Tmin units="K"  value="425" />
-  <Tmax units="K"  value="633.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="11.503" />
-  <B value="-0.069766" />
-  <C value="0.000057848" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="563.72" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.34907" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.610035E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="286.6801" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="117.59" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-3.0397" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0463" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.03031" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.50498" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.104957" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7567" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.888" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="7.2058" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.508" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23827.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.104957" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-44-5" />
-<Smiles name="SMILES"  value="c1(O)ccc(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="138" />
-<CompoundID name="Name"  value="Methylcyclohexane" />
-<StructureFormula name="Structure"  value="(C6H11)CH3" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="572.19" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3471000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.368" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="374.09" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="146.58" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="146.58" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000152251" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.188" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12835" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.235" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.643E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16060" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07046" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.87E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.548E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.733E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="343300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6751000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.25714E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.429" />
-  <B value="-0.0085395" />
-  <Tmin units="K"  value="58.63" />
-  <Tmax units="K"  value="146.58" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54994" />
-  <B value="0.23476" />
-  <C value="572.19" />
-  <D value="0.25237" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="572.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="84.02524" />
-  <B value="-6720.084" />
-  <C value="-9.367446" />
-  <D value="6.892527E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="572.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.3741E+07" />
-  <B value="0.65698" />
-  <C value="0.0050875" />
-  <D value="-0.53082" />
-  <E value="0.29149" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="572.1" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13069" />
-  <B value="1384.8" />
-  <C value="-9.1718" />
-  <D value="0.036062" />
-  <E value="-0.000031442" />
-  <Tmin units="K"  value="12" />
-  <Tmax units="K"  value="146.58" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="121540" />
-  <B value="-7.0302" />
-  <C value="8.197" />
-  <D value="0.012761" />
-  <E value="-0.000010388" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="320" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="82902" />
-  <B value="-804.58" />
-  <C value="13.697" />
-  <D value="-0.00042977" />
-  <E value="1.1051E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20875" />
-  <B value="-247.9" />
-  <C value="-33.881" />
-  <D value="-2750.8" />
-  <E value="4328.8" />
-  <Tmin units="K"  value="286" />
-  <Tmax units="K"  value="1828" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.411" />
-  <B value="1214.3" />
-  <C value="0.0090457" />
-  <D value="-0.0000000327" />
-  <E value="2" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="457.68" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.5256E-07" />
-  <B value="0.52942" />
-  <C value="310.39" />
-  <D value="23.825" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.035771" />
-  <B value="-249.64" />
-  <C value="0.10904" />
-  <D value="-0.0066567" />
-  <E value="0.0000013937" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="374.08" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000074754" />
-  <B value="1.119" />
-  <C value="613.15" />
-  <D value="22882" />
-  <Tmin units="K"  value="374.08" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0071052" />
-  <B value="37.192" />
-  <C value="-3.2268" />
-  <D value="0.0007377" />
-  <E value="-0.0000068537" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="572.1" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="26174" />
-  <B value="153.3" />
-  <C value="1.1328" />
-  <D value="-0.0015625" />
-  <E value="6.1228E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.844" />
-  <B value="3088.6" />
-  <C value="-42.601" />
-  <Tmin units="K"  value="344.14" />
-  <Tmax units="K"  value="510.93" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.6248" />
-  <B value="-0.050338" />
-  <C value="0.000057219" />
-  <Tmin units="K"  value="146.58" />
-  <Tmax units="K"  value="457.68" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3709" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.492807E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="326.3914" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2699" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.82199" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0497" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.772427" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2371" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.12834" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.72" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.776" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.776" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000172" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.8218" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2421" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16016.26" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1283" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="78"  value="5" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-87-2" />
-<Smiles name="SMILES"  value="C1CCCCC1(C)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="107" />
-<CompoundID name="Name"  value="Ethylcyclopentane" />
-<StructureFormula name="Structure"  value="(C5H9)CH2CH3" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="569.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3397000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.375" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="376.59" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="134.71" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="134.71" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.71437E-06" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.188" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12883" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.27" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.734E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0704" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.87E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.269E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.48E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="378300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6869700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.92806" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.2839E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.431" />
-  <B value="-0.0092953" />
-  <Tmin units="K"  value="53.88" />
-  <Tmax units="K"  value="134.71" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.72259" />
-  <B value="0.26996" />
-  <C value="569.5" />
-  <D value="0.2784" />
-  <Tmin units="K"  value="134.71" />
-  <Tmax units="K"  value="546.62" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="95.769" />
-  <B value="-7366.4" />
-  <C value="-11.099" />
-  <D value="0.0000081014" />
-  <E value="2" />
-  <Tmin units="K"  value="134.71" />
-  <Tmax units="K"  value="569.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.78221E+07" />
-  <B value="0.856257" />
-  <C value="-0.338119" />
-  <D value="-0.391894" />
-  <E value="0.299953" />
-  <Tmin units="K"  value="134.71" />
-  <Tmax units="K"  value="546.62" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12482" />
-  <B value="1503.5" />
-  <C value="-7.4405" />
-  <D value="0.0091338" />
-  <E value="0.000058554" />
-  <Tmin units="K"  value="12.14" />
-  <Tmax units="K"  value="126.86" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="128880" />
-  <B value="403.43" />
-  <C value="3.1567" />
-  <D value="0.031507" />
-  <E value="-0.000033176" />
-  <Tmin units="K"  value="134.71" />
-  <Tmax units="K"  value="301.82" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="61352" />
-  <B value="-623.48" />
-  <C value="13.275" />
-  <D value="-0.000068613" />
-  <E value="9.3089E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21463" />
-  <B value="-224.87" />
-  <C value="-41.025" />
-  <D value="-7128.8" />
-  <E value="10923" />
-  <Tmin units="K"  value="284.75" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-3.6105" />
-  <B value="709.69" />
-  <C value="-1.12" />
-  <D value="8.8328E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="378.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000021783" />
-  <B value="0.38064" />
-  <C value="577.64" />
-  <D value="269.9" />
-  <Tmin units="K"  value="134.71" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.019932" />
-  <B value="6.51" />
-  <C value="-1.7114" />
-  <D value="-0.0004148" />
-  <E value="-0.0000019629" />
-  <Tmin units="K"  value="134.71" />
-  <Tmax units="K"  value="376.62" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0047981" />
-  <B value="0.52948" />
-  <C value="335.74" />
-  <D value="590020" />
-  <Tmin units="K"  value="376.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016425" />
-  <B value="10.598" />
-  <C value="-2.7862" />
-  <D value="-0.00069695" />
-  <E value="-0.0000029932" />
-  <Tmin units="K"  value="134.71" />
-  <Tmax units="K"  value="546.62" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="48615" />
-  <B value="-0.39909" />
-  <C value="1.4556" />
-  <D value="-0.0018703" />
-  <E value="0.0000007197" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.962" />
-  <B value="3131.9" />
-  <C value="-44.732" />
-  <Tmin units="K"  value="343.06" />
-  <Tmax units="K"  value="510.93" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.4246" />
-  <B value="-0.029561" />
-  <C value="0.000030457" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="378.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.374" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.504581E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="329.2419" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.33548" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0503" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.769565" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2689" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.128749" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.72" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.776" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002891" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.69675" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.271548" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16339.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.128749" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="10"  value="5" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="78"  value="4" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1640-89-7" />
-<Smiles name="SMILES"  value="C1(CC)CCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="234" />
-<CompoundID name="Name"  value="1-heptene" />
-<StructureFormula name="Structure"  value="CH2CH(CH2)4CH3" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="537.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2920000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.409" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="366.79" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="154.12" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="154.12" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00186" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.188" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14177" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.343" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.083E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15310" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.1E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.075" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.046E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.289E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.482E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="425200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.264E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0461" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.3499E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.448" />
-  <B value="-0.0076501" />
-  <Tmin units="K"  value="61.65" />
-  <Tmax units="K"  value="154.27" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.26107" />
-  <B value="0.16952" />
-  <C value="537.3" />
-  <D value="0.1874" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="536.53" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="109.9184" />
-  <B value="-7605.67" />
-  <C value="-13.43227" />
-  <D value="0.0000123163" />
-  <E value="2" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="537.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.631368E+07" />
-  <B value="1.145386" />
-  <C value="-1.731438" />
-  <D value="1.615943" />
-  <E value="-0.650835" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="517.23" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5969.6" />
-  <B value="597.62" />
-  <C value="18.112" />
-  <D value="-0.2191" />
-  <E value="0.0007294" />
-  <Tmin units="K"  value="11.4" />
-  <Tmax units="K"  value="142.69" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="58419" />
-  <B value="89.259" />
-  <C value="10.549" />
-  <D value="0.0039271" />
-  <E value="-8.6181E-07" />
-  <Tmin units="K"  value="151.79" />
-  <Tmax units="K"  value="430" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94067" />
-  <B value="-609.56" />
-  <C value="13.043" />
-  <D value="0.000046316" />
-  <E value="-2.1105E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20796" />
-  <B value="-241.14" />
-  <C value="-48.774" />
-  <D value="3433.8" />
-  <E value="-14358" />
-  <Tmin units="K"  value="255" />
-  <Tmax units="K"  value="1880.3" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.29" />
-  <B value="827.04" />
-  <C value="-0.087144" />
-  <D value="0.0000001052" />
-  <E value="2" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="429.92" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.4687E-08" />
-  <B value="0.81173" />
-  <C value="52.725" />
-  <D value="1460.7" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.038053" />
-  <B value="-34.158" />
-  <C value="-1.0057" />
-  <D value="-0.0023353" />
-  <E value="-3.7702E-08" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="433.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000013676" />
-  <B value="1.341" />
-  <C value="365.19" />
-  <D value="6251.8" />
-  <Tmin units="K"  value="366.79" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010568" />
-  <B value="24.026" />
-  <C value="-3.0595" />
-  <D value="-0.0001793" />
-  <E value="-0.0000051634" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="517.23" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="62525" />
-  <B value="106.62" />
-  <C value="1.0534" />
-  <D value="-0.0014615" />
-  <E value="5.8492E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.78" />
-  <B value="2900.8" />
-  <C value="-53.334" />
-  <Tmin units="K"  value="324.12" />
-  <Tmax units="K"  value="476.88" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.0377" />
-  <B value="-0.035732" />
-  <C value="0.000041467" />
-  <Tmin units="K"  value="154.12" />
-  <Tmax units="K"  value="429.92" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.405616" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.755735E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="302.3922" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.260462" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.60949" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0531" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.70084" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.358" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.141709" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.9441" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.184" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.006221" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2762" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.358" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15313.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.141709" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="592-76-7" />
-<Smiles name="SMILES"  value="C=CCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="17" />
-<CompoundID name="Name"  value="N-heptane" />
-<StructureFormula name="Structure"  value="CH3(CH2)5CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="540.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2740000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.428" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="371.57" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="182.57" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="182.57" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.182694" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14747" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.35" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.173E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15240" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07849" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.099E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.8765E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="8165000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="427980" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.405E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.00313" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.46473E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.1435" />
-  <B value="-0.0028756" />
-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="182.58" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.57043" />
-  <B value="0.25304" />
-  <C value="540.2" />
-  <D value="0.27335" />
-  <Tmin units="K"  value="182.57" />
-  <Tmax units="K"  value="540.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="89.80457" />
-  <B value="-7084.845" />
-  <C value="-10.17918" />
-  <D value="7.441708E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="182.57" />
-  <Tmax units="K"  value="540.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.275764E+07" />
-  <B value="-1.051245" />
-  <C value="4.601706" />
-  <D value="-5.558946" />
-  <E value="2.369496" />
-  <Tmin units="K"  value="182.57" />
-  <Tmax units="K"  value="540.2" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-20510" />
-  <B value="1728.5" />
-  <C value="-6.4728" />
-  <D value="-0.0018307" />
-  <E value="0.000070938" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="182.58" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="134750" />
-  <B value="14.937" />
-  <C value="10.603" />
-  <D value="0.001438" />
-  <E value="0.0000036711" />
-  <Tmin units="K"  value="182.55" />
-  <Tmax units="K"  value="520" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="109310" />
-  <B value="-704.2" />
-  <C value="13.352" />
-  <D value="-0.00017922" />
-  <E value="4.6992E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23983" />
-  <B value="-244.66" />
-  <C value="-54.176" />
-  <D value="2830.8" />
-  <E value="-15702" />
-  <Tmin units="K"  value="264" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-61.08861" />
-  <B value="2532.297" />
-  <C value="8.091665" />
-  <D value="-0.0000152585" />
-  <E value="2" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="432.16" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.6134E-08" />
-  <B value="0.948" />
-  <C value="-37.497" />
-  <D value="9005.3" />
-  <Tmin units="K"  value="182.57" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.083657" />
-  <B value="49.111" />
-  <C value="-3.4536" />
-  <D value="0.0077989" />
-  <E value="-0.000025112" />
-  <Tmin units="K"  value="182.57" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.076333" />
-  <B value="0.38025" />
-  <C value="-7539.9" />
-  <D value="-2646800" />
-  <Tmin units="K"  value="339.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.007741" />
-  <B value="65.405" />
-  <C value="-3.6478" />
-  <D value="0.001894" />
-  <E value="-0.0000081692" />
-  <Tmin units="K"  value="182.57" />
-  <Tmax units="K"  value="540.2" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="80102" />
-  <B value="34.555" />
-  <C value="1.2882" />
-  <D value="-0.0016684" />
-  <E value="6.4603E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.995" />
-  <B value="3044.2" />
-  <C value="-50.149" />
-  <Tmin units="K"  value="324.35" />
-  <Tmax units="K"  value="483.73" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.018303" />
-  <B value="-0.039206" />
-  <C value="0.000043234" />
-  <Tmin units="K"  value="180.15" />
-  <Tmax units="K"  value="432.16" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.43044" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.048406E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="280.139" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2611" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0549" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.686815" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.35069" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.147014" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1742" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.396" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="4.396" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003031" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3403" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15230" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1475" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="142-82-5" />
-<Smiles name="SMILES"  value="CCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="601" />
-<CompoundID name="Name"  value="Styrene" />
-<StructureFormula name="Structure"  value="(C6H5)CHCH2" />
-<Family name="Family"  value="18" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="636" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3840000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.352" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="418.31" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="242.54" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="242.54" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="10.6132" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="104.149" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.115667" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.297097" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.81E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19020" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.33E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06625" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.27E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.474E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.139E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="345100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.095E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93739" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.219E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.7167" />
-  <B value="-9.6333E-09" />
-  <Tmin units="K"  value="93.15" />
-  <Tmax units="K"  value="102.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.57789" />
-  <B value="0.23139" />
-  <C value="640.77" />
-  <D value="0.26351" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="640.76" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="399.8489" />
-  <B value="-19017.34" />
-  <C value="-58.96286" />
-  <D value="0.0000747957" />
-  <E value="2" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="636" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.110621E+08" />
-  <B value="3.429275" />
-  <C value="-6.061051" />
-  <D value="4.605581" />
-  <E value="-1.408226" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="615.29" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19432" />
-  <B value="1905.5" />
-  <C value="-18.713" />
-  <D value="0.095712" />
-  <E value="-0.00015273" />
-  <Tmin units="K"  value="15.28" />
-  <Tmax units="K"  value="240.03" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="134310" />
-  <B value="-99.916" />
-  <C value="9.4935" />
-  <D value="0.0058294" />
-  <E value="-0.0000013972" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="418.31" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="57806.72" />
-  <B value="-550.4249" />
-  <C value="12.95376" />
-  <D value="-0.0000950882" />
-  <E value="2.294759E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21818" />
-  <B value="-307.77" />
-  <C value="-59.025" />
-  <D value="55700" />
-  <E value="-203800" />
-  <Tmin units="K"  value="324" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-24.717" />
-  <B value="1824" />
-  <C value="1.9977" />
-  <D value="-4.7933E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="418.31" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.6968E-08" />
-  <B value="0.90482" />
-  <C value="-32.023" />
-  <D value="10027" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="1273.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.071817" />
-  <B value="-30.013" />
-  <C value="-1.0262" />
-  <D value="-0.0015623" />
-  <E value="2.7674E-07" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="598.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.010229" />
-  <B value="0.40085" />
-  <C value="535.56" />
-  <D value="704200" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="0.014356" />
-  <B value="-415.6" />
-  <C value="0.14176" />
-  <D value="-0.011441" />
-  <E value="0.0000063214" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="418.31" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-36913.76" />
-  <B value="665.256" />
-  <C value="-0.485051" />
-  <D value="0.000140879" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.888" />
-  <B value="3339.6" />
-  <C value="-61.724" />
-  <Tmin units="K"  value="383" />
-  <Tmax units="K"  value="553.17" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.77036" />
-  <B value="-0.039418" />
-  <C value="0.000042054" />
-  <Tmin units="K"  value="242.54" />
-  <Tmax units="K"  value="418.31" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.34819" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.758825E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="307.6339" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="127.38" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0621" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.909306" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.24199" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.115667" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.37" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.3" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.3" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.01967" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2302" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19015.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.115667" />
-<UnifacVLE name="UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="1" />
-  <group id="9"  value="5" />
-  <group id="13"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="5"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="5"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="100-42-5" />
-<Smiles name="SMILES"  value="C=Cc1ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="504" />
-<CompoundID name="Name"  value="Ethylbenzene" />
-<StructureFormula name="Structure"  value="(C6H5)CH2CH3" />
-<Family name="Family"  value="16" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="617.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3609000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.374" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="409.36" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="178.2" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="178.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00390778" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="106.167" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12308" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.304" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.897E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17980" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06974" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.8E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.992E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.3073E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="360630" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9180300" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0026" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.3448E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.465" />
-  <B value="-0.007103" />
-  <Tmin units="K"  value="71.28" />
-  <Tmax units="K"  value="178.2" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.66155" />
-  <B value="0.25394" />
-  <C value="617.21" />
-  <D value="0.27883" />
-  <Tmin units="K"  value="163.1" />
-  <Tmax units="K"  value="617.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="137.5088" />
-  <B value="-9745.069" />
-  <C value="-17.34457" />
-  <D value="0.0000127987" />
-  <E value="2" />
-  <Tmin units="K"  value="178.2" />
-  <Tmax units="K"  value="617.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.990732E+07" />
-  <B value="0.380483" />
-  <C value="1.094304" />
-  <D value="-2.185536" />
-  <E value="1.1369" />
-  <Tmin units="K"  value="178.15" />
-  <Tmax units="K"  value="594.05" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-8883.6" />
-  <B value="1417.5" />
-  <C value="-10.145" />
-  <D value="0.048416" />
-  <E value="-0.000088579" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="178.2" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="131820" />
-  <B value="-90.983" />
-  <C value="10.031" />
-  <D value="0.0026504" />
-  <E value="0.0000033965" />
-  <Tmin units="K"  value="178.17" />
-  <Tmax units="K"  value="409.35" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65434" />
-  <B value="-619.34" />
-  <C value="13.166" />
-  <D value="-0.00016412" />
-  <E value="4.1529E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23456" />
-  <B value="-304.77" />
-  <C value="-54.496" />
-  <D value="-5921.9" />
-  <E value="-7767.5" />
-  <Tmin units="K"  value="307" />
-  <Tmax units="K"  value="1967" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-14.506" />
-  <B value="1237.2" />
-  <C value="0.52859" />
-  <D value="-9.1363E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="178.2" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000016833" />
-  <B value="0.39831" />
-  <C value="366.45" />
-  <D value="23750" />
-  <Tmin units="K"  value="178.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.026087" />
-  <B value="13.301" />
-  <C value="-1.6623" />
-  <D value="-0.00027844" />
-  <E value="-0.0000018214" />
-  <Tmin units="K"  value="178.2" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000015932" />
-  <B value="1.3226" />
-  <C value="486.47" />
-  <D value="14367" />
-  <Tmin units="K"  value="409.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012337" />
-  <B value="28.706" />
-  <C value="-2.9284" />
-  <D value="-0.0000060499" />
-  <E value="-0.0000040717" />
-  <Tmin units="K"  value="178.2" />
-  <Tmax units="K"  value="594.05" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="37781" />
-  <B value="87.95" />
-  <C value="1.1344" />
-  <D value="-0.0016027" />
-  <E value="0.0000006556" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197605" />
-  <B value="-1500" />
-  <C value="-9" />
-  <Tmin units="K"  value="278.5945" />
-  <Tmax units="K"  value="448.5945" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.113" />
-  <B value="3424.2" />
-  <C value="-52.199" />
-  <Tmin units="K"  value="370.3" />
-  <Tmax units="K"  value="554.84" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0993" />
-  <B value="-0.043006" />
-  <C value="0.000049165" />
-  <Tmin units="K"  value="178.2" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3702" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.677111E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="328.9612" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="132" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.58093" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0504" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.870033" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3048" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.122763" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.6" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.51" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.51" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004227" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2097" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2936" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17979.95" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1231" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="5" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="5" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="5" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="5" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="100-41-4" />
-<Smiles name="SMILES"  value="c1ccccc1(CC)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="506" />
-<CompoundID name="Name"  value="M-xylene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="617" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3541000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.375" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="412.34" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="225.3" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="225.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.18019" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="106.167" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12347" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.327" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.937E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18050" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07066" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.732E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.1876E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="358540" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.157E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0367" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.3318E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.9327" />
-  <B value="0.00073817" />
-  <Tmin units="K"  value="78.15" />
-  <Tmax units="K"  value="225.3" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.68902" />
-  <B value="0.26086" />
-  <C value="617" />
-  <D value="0.27479" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="617" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="97.968" />
-  <B value="-8164.7" />
-  <C value="-11.269" />
-  <D value="0.0000072101" />
-  <E value="2" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="617.05" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.9562E+07" />
-  <B value="0.67841" />
-  <C value="-0.38938" />
-  <D value="0.0061115" />
-  <E value="0.10219" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="617" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-25435" />
-  <B value="2467.9" />
-  <C value="-25.474" />
-  <D value="0.12997" />
-  <E value="-0.0002333" />
-  <Tmin units="K"  value="14.62" />
-  <Tmax units="K"  value="225.3" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="127090" />
-  <B value="-62.999" />
-  <C value="9.3762" />
-  <D value="0.0068549" />
-  <E value="-0.0000032778" />
-  <Tmin units="K"  value="217" />
-  <Tmax units="K"  value="540.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62092" />
-  <B value="-572.21" />
-  <C value="12.975" />
-  <D value="0.000062577" />
-  <E value="-3.7811E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.04628" />
-  <B value="237.59" />
-  <C value="-144.13" />
-  <D value="5318.3" />
-  <E value="-22675" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-13.362" />
-  <B value="1141.4" />
-  <C value="0.37182" />
-  <D value="-3.9423E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.2954E-08" />
-  <B value="0.8097" />
-  <C value="14.386" />
-  <D value="8844.3" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="1273.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.021158" />
-  <B value="-27.324" />
-  <C value="-1.2663" />
-  <D value="-0.0016664" />
-  <E value="-3.6744E-07" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="2.8001E-09" />
-  <B value="2.4298" />
-  <C value="-575.12" />
-  <D value="122260" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0081275" />
-  <B value="86.069" />
-  <C value="-3.5983" />
-  <D value="0.0020602" />
-  <E value="-0.0000069588" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="617" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="33275" />
-  <B value="145.81" />
-  <C value="0.8805" />
-  <D value="-0.0012502" />
-  <E value="4.9953E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.301" />
-  <B value="3581.9" />
-  <C value="-45.994" />
-  <Tmin units="K"  value="371" />
-  <Tmax units="K"  value="555.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.65909" />
-  <B value="-0.033111" />
-  <C value="0.000034785" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.37312" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.807103E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="311.2272" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2593" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="132" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.55541" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0502" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.866882" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.32699" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.123391" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.66" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.54" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.54" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005645" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.002" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3045" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18041.31" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1235" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="12"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="11"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="12"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="11"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-38-3" />
-<Smiles name="SMILES"  value="c1(C)cc(C)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="505" />
-<CompoundID name="Name"  value="O-xylene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="630.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3732000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.37" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="417.59" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="247.98" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="247.98" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="21.842" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="106.167" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12125" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.312" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.836E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18390" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.1E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07066" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.908E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.22E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="353830" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.36E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.03316" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.333E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.582" />
-  <B value="-0.0039991" />
-  <Tmin units="K"  value="203.1" />
-  <Tmax units="K"  value="248" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.69962" />
-  <B value="0.26143" />
-  <C value="630.3" />
-  <D value="0.27365" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="630.3" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="88.08217" />
-  <B value="-7844.793" />
-  <C value="-9.738423" />
-  <D value="5.713756E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="630.33" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.6979E+07" />
-  <B value="1.259" />
-  <C value="-1.849" />
-  <D value="1.5198" />
-  <E value="-0.50455" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="612" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12409" />
-  <B value="1322.1" />
-  <C value="-6.4842" />
-  <D value="0.018683" />
-  <E value="-0.000013938" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="247.98" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="134490" />
-  <B value="-170.61" />
-  <C value="10.247" />
-  <D value="0.0049096" />
-  <E value="-0.0000031727" />
-  <Tmin units="K"  value="247.8" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="73986" />
-  <B value="-589.13" />
-  <C value="12.936" />
-  <D value="0.000080122" />
-  <E value="-4.5074E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18068" />
-  <B value="-139.72" />
-  <C value="-79.094" />
-  <D value="-34596" />
-  <E value="63013" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.059" />
-  <B value="1251.7" />
-  <C value="-0.076438" />
-  <D value="0.000001254" />
-  <E value="2" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="418.1" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.783E-08" />
-  <B value="0.82039" />
-  <C value="-1.2715" />
-  <D value="13072" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="1273.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.018751" />
-  <B value="-22.77" />
-  <C value="-1.3391" />
-  <D value="-0.0014281" />
-  <E value="-6.1692E-07" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="417.58" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000059387" />
-  <B value="1.356" />
-  <C value="-206" />
-  <D value="65058" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011942" />
-  <B value="49.212" />
-  <C value="-3.1236" />
-  <D value="0.00059647" />
-  <E value="-0.0000045152" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="610.18" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="27346" />
-  <B value="283.89" />
-  <C value="0.41481" />
-  <D value="-0.00069301" />
-  <E value="2.7754E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.955809" />
-  <B value="-1300" />
-  <C value="-7.8" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.286" />
-  <B value="3609.8" />
-  <C value="-47.763" />
-  <Tmin units="K"  value="381.4" />
-  <Tmax units="K"  value="563.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.10974" />
-  <B value="-0.03518" />
-  <C value="0.000036077" />
-  <Tmin units="K"  value="247.98" />
-  <Tmax units="K"  value="418.1" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.36733" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.653221E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="335.9706" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2633" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="132" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.66585" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.05" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.883145" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3118" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.121145" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.66" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.54" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.54" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.006569" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.1646" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2904" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18389.04" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1212" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="12"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="11"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="12"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="11"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="95-47-6" />
-<Smiles name="SMILES"  value="c1(C)ccccc1(C)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="507" />
-<CompoundID name="Name"  value="P-xylene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="616.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3511000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.378" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="411.53" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="286.41" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="286.41" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="575.533" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="106.167" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12393" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.322" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.831E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17910" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07066" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.803E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.214E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="352165" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.711E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0563" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.333E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.9" />
-  <B value="-0.021882" />
-  <Tmin units="K"  value="273.25" />
-  <Tmax units="K"  value="286.41" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.67752" />
-  <B value="0.25887" />
-  <C value="616.2" />
-  <D value="0.27596" />
-  <Tmin units="K"  value="286.41" />
-  <Tmax units="K"  value="616.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="97.352" />
-  <B value="-8082.1" />
-  <C value="-11.197" />
-  <D value="0.0000072605" />
-  <E value="2" />
-  <Tmin units="K"  value="282.99" />
-  <Tmax units="K"  value="616.23" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.6332E+07" />
-  <B value="0.37965" />
-  <C value="0.42395" />
-  <D value="-0.85683" />
-  <E value="0.43704" />
-  <Tmin units="K"  value="286.41" />
-  <Tmax units="K"  value="616.2" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19759" />
-  <B value="1635.7" />
-  <C value="-9.6261" />
-  <D value="0.031794" />
-  <E value="-0.000036966" />
-  <Tmin units="K"  value="19.11" />
-  <Tmax units="K"  value="286.41" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63084" />
-  <B value="-343.38" />
-  <C value="13.438" />
-  <D value="-0.0033851" />
-  <E value="0.0000045592" />
-  <Tmin units="K"  value="286.4" />
-  <Tmax units="K"  value="600" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62397" />
-  <B value="-585.6" />
-  <C value="13.025" />
-  <D value="0.0000037921" />
-  <E value="-1.7044E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.06505" />
-  <B value="248.78" />
-  <C value="-160.39" />
-  <D value="115610" />
-  <E value="-382400" />
-  <Tmin units="K"  value="338.9" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-23.916" />
-  <B value="1499.8" />
-  <C value="2.0719" />
-  <D value="-0.0000037065" />
-  <E value="2" />
-  <Tmin units="K"  value="286.41" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.4281E-08" />
-  <B value="0.95421" />
-  <C value="-91.329" />
-  <D value="17547" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1273.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.00066881" />
-  <B value="-122.94" />
-  <C value="-0.60875" />
-  <D value="-0.0037322" />
-  <E value="9.7446E-07" />
-  <Tmin units="K"  value="286.41" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000001261" />
-  <B value="1.8916" />
-  <C value="-453.43" />
-  <D value="111720" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0080188" />
-  <B value="66.097" />
-  <C value="-3.4878" />
-  <D value="0.0018353" />
-  <E value="-0.0000068516" />
-  <Tmin units="K"  value="273.1" />
-  <Tmax units="K"  value="616.2" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34197" />
-  <B value="123.96" />
-  <C value="0.98194" />
-  <D value="-0.0013905" />
-  <E value="5.6006E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.717467" />
-  <B value="-1150" />
-  <C value="-6.9" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.116" />
-  <B value="3447.8" />
-  <C value="-51.968" />
-  <Tmin units="K"  value="370.2" />
-  <Tmax units="K"  value="553" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.8388" />
-  <B value="-0.025762" />
-  <C value="0.000023732" />
-  <Tmin units="K"  value="286.41" />
-  <Tmax units="K"  value="413.1" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.374" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.825207E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="310.8236" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2589" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="132" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.89953" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0503" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.864229" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.32159" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.123921" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.66" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.54" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="3.54" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.010556" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.7717" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2969" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17939.04" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.124" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="12"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="11"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="12"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="11"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-42-3" />
-<Smiles name="SMILES"  value="c1(C)ccc(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="140" />
-<CompoundID name="Name"  value="Ethylcyclohexane" />
-<StructureFormula name="Structure"  value="(C6H11)CH2CH3" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="609.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3040000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.43" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.258" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="404.945" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="161.839" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="161.839" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000357389" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.143036" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.245525" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.932E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16340" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08069" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.022E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.715E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.955E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="382600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8334100" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.82185" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.87051E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.986" />
-  <B value="-0.0068877" />
-  <Tmin units="K"  value="64.74" />
-  <Tmax units="K"  value="161.84" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61774" />
-  <B value="0.26525" />
-  <C value="609.15" />
-  <D value="0.28064" />
-  <Tmin units="K"  value="161.84" />
-  <Tmax units="K"  value="609.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="80.60435" />
-  <B value="-7221.846" />
-  <C value="-8.661516" />
-  <D value="4.619539E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="161.84" />
-  <Tmax units="K"  value="609.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.1066E+07" />
-  <B value="1.1095" />
-  <C value="-1.6401" />
-  <D value="1.5232" />
-  <E value="-0.54256" />
-  <Tmin units="K"  value="161.84" />
-  <Tmax units="K"  value="609.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13926" />
-  <B value="1604.5" />
-  <C value="-10.433" />
-  <D value="0.036407" />
-  <E value="-0.000012874" />
-  <Tmin units="K"  value="12" />
-  <Tmax units="K"  value="156" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="106540" />
-  <B value="50.724" />
-  <C value="9.3758" />
-  <D value="0.0085193" />
-  <E value="-0.0000058679" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="404.95" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="99579" />
-  <B value="-799.66" />
-  <C value="13.811" />
-  <D value="-0.00043634" />
-  <E value="1.1487E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24249" />
-  <B value="-292.83" />
-  <C value="-55.328" />
-  <D value="-12007" />
-  <E value="19757" />
-  <Tmin units="K"  value="304.57" />
-  <Tmax units="K"  value="1948.58" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-22.531" />
-  <B value="1686" />
-  <C value="1.7093" />
-  <D value="-0.0000001282" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="404.94" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.2871E-07" />
-  <B value="0.57053" />
-  <C value="258.88" />
-  <D value="-2237.2" />
-  <Tmin units="K"  value="161.84" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.040212" />
-  <B value="3.9673" />
-  <C value="-1.6044" />
-  <D value="-0.00049691" />
-  <E value="-0.0000012623" />
-  <Tmin units="K"  value="161.84" />
-  <Tmax units="K"  value="404.94" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000062751" />
-  <B value="1.1219" />
-  <C value="488.85" />
-  <D value="45648" />
-  <Tmin units="K"  value="404.95" />
-  <Tmax units="K"  value="1000" />
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-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.007744" />
-  <B value="40.259" />
-  <C value="-3.2447" />
-  <D value="0.0006801" />
-  <E value="-0.0000057319" />
-  <Tmin units="K"  value="161.84" />
-  <Tmax units="K"  value="609.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-60082.24" />
-  <B value="864.6654" />
-  <C value="-0.464047" />
-  <D value="0.0000830984" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.544" />
-  <B value="3077.4" />
-  <C value="-63.681" />
-  <Tmin units="K"  value="367.48" />
-  <Tmax units="K"  value="538.52" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.2715" />
-  <B value="-0.048749" />
-  <C value="0.000057505" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="404.94" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.42269" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.157986E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="303.0179" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.20684" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0564" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.790679" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.24966" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.143117" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3944" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.316" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.03518" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2426" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16360" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.143117" />
-<UnifacVLE name="UNIFAC" >
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-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
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-  <group id="3"  value="1" />
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-  <group id="2"  value="1" />
-  <group id="12"  value="1" />
-  <group id="13"  value="5" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="78"  value="5" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1678-91-7" />
-<Smiles name="SMILES"  value="C1CCCCC1(CC)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="114" />
-<CompoundID name="Name"  value="N-propylcyclopentane" />
-<StructureFormula name="Structure"  value="(C5H9)CH2CH2CH3" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="596" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3020000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.428" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="404.11" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="155.81" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="155.81" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000458874" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.145193" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.326642" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.135E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16360" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08062" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.022E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.481E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.344E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.003E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.89356E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.906" />
-  <B value="-0.0070521" />
-  <Tmin units="K"  value="62.32" />
-  <Tmax units="K"  value="155.81" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.63061" />
-  <B value="0.26934" />
-  <C value="596" />
-  <D value="0.28169" />
-  <Tmin units="K"  value="155.81" />
-  <Tmax units="K"  value="572.83" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="95.39512" />
-  <B value="-7846.538" />
-  <C value="-10.93845" />
-  <D value="7.332031E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="155.81" />
-  <Tmax units="K"  value="596" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.088104E+07" />
-  <B value="1.477689" />
-  <C value="-1.919309" />
-  <D value="1.219865" />
-  <E value="-0.332624" />
-  <Tmin units="K"  value="155.81" />
-  <Tmax units="K"  value="572.83" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-21119" />
-  <B value="1855.5" />
-  <C value="-9.5485" />
-  <D value="0.012148" />
-  <E value="0.000065366" />
-  <Tmin units="K"  value="20.68" />
-  <Tmax units="K"  value="155.81" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="121270" />
-  <B value="281.76" />
-  <C value="6.7151" />
-  <D value="0.017545" />
-  <E value="-0.000016082" />
-  <Tmin units="K"  value="155.81" />
-  <Tmax units="K"  value="404.11" />
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-  <eqno value="16" />
-  <A value="82387" />
-  <B value="-676.01" />
-  <C value="13.514" />
-  <D value="-0.00019546" />
-  <E value="4.9854E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2479" />
-  <B value="-262.92" />
-  <C value="-60.711" />
-  <D value="-16273" />
-  <E value="25758" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1500" />
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-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-22.725" />
-  <B value="1601.8" />
-  <C value="1.7512" />
-  <D value="2.3108E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="404.11" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000028167" />
-  <B value="0.32978" />
-  <C value="562.31" />
-  <D value="4948.1" />
-  <Tmin units="K"  value="155.81" />
-  <Tmax units="K"  value="1000" />
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-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.033741" />
-  <B value="2.5308" />
-  <C value="-1.6237" />
-  <D value="-0.00058186" />
-  <E value="-0.0000013118" />
-  <Tmin units="K"  value="155.81" />
-  <Tmax units="K"  value="404.11" />
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-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000098309" />
-  <B value="1.0636" />
-  <C value="611.41" />
-  <D value="33175" />
-  <Tmin units="K"  value="404.11" />
-  <Tmax units="K"  value="1000" />
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-  <eqno value="16" />
-  <A value="-0.014846" />
-  <B value="15.619" />
-  <C value="-2.8681" />
-  <D value="-0.00048241" />
-  <E value="-0.0000031204" />
-  <Tmin units="K"  value="155.81" />
-  <Tmax units="K"  value="572.83" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-64605.14" />
-  <B value="897.217" />
-  <C value="-0.586513" />
-  <D value="0.000162009" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.961" />
-  <B value="3302.2" />
-  <C value="-54.096" />
-  <Tmin units="K"  value="358.15" />
-  <Tmax units="K"  value="526.5" />
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-  <eqno value="13" />
-  <A value="1.393" />
-  <B value="-0.045558" />
-  <C value="0.000054398" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="404.11" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.43959" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.048406E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="309.076" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0573" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.779333" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.34698" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.145193" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3944" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.316" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.012036" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.27189" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16393.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.145193" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
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-<UnifacLLE name="UNIFAC-LLE" >
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-<GCmethod name="PPR78" >
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-<Umr name="UMR" >
-  <group id="1"  value="1" />
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-  <group id="79"  value="1" />
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-<Smiles name="SMILES"  value="C1CCCC1(CCC)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="27" />
-<CompoundID name="Name"  value="N-octane" />
-<StructureFormula name="Structure"  value="CH3(CH2)6CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="568.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2490000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.492" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="398.82" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="216.38" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="216.38" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.1083" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16353" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.397" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.546E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15490" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08872" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.234E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.0875E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.6E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="467230" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.074E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.99752" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.07415E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
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-  <Tmin units="K"  value="133.15" />
-  <Tmax units="K"  value="216.38" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
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-  <D value="0.25171" />
-  <Tmin units="K"  value="216.38" />
-  <Tmax units="K"  value="568.76" />
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-  <eqno value="101" />
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-  <E value="2" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="568.74" />
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-  <eqno value="106" />
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-  <E value="0.114898" />
-  <Tmin units="K"  value="216.38" />
-  <Tmax units="K"  value="568.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-23993" />
-  <B value="1947.3" />
-  <C value="-8.5369" />
-  <D value="0.013403" />
-  <E value="0.000020934" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="216.37" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="184080" />
-  <B value="362.58" />
-  <C value="6.1268" />
-  <D value="0.015908" />
-  <E value="-0.000010697" />
-  <Tmin units="K"  value="216.37" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="123360" />
-  <B value="-700.1" />
-  <C value="13.486" />
-  <D value="-0.00019118" />
-  <E value="4.5401E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22234" />
-  <B value="-247.06" />
-  <C value="-83.099" />
-  <D value="9339.9" />
-  <E value="-40370" />
-  <Tmin units="K"  value="256" />
-  <Tmax units="K"  value="1990.66" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-67.06275" />
-  <B value="2937.699" />
-  <C value="8.939458" />
-  <D value="-0.0000146474" />
-  <E value="2" />
-  <Tmin units="K"  value="211.15" />
-  <Tmax units="K"  value="454.96" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.2215E-09" />
-  <B value="1.1166" />
-  <C value="-127.08" />
-  <D value="17623" />
-  <Tmin units="K"  value="216.38" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.03316" />
-  <B value="17.841" />
-  <C value="-1.6367" />
-  <D value="-0.000047737" />
-  <E value="-0.0000026501" />
-  <Tmin units="K"  value="216.38" />
-  <Tmax units="K"  value="398.83" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-8968.5" />
-  <B value="0.84408" />
-  <C value="-2.7564E+10" />
-  <D value="-6.5097E+10" />
-  <Tmin units="K"  value="339" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010282" />
-  <B value="15.557" />
-  <C value="-3.0383" />
-  <D value="-0.00026764" />
-  <E value="-0.0000044265" />
-  <Tmin units="K"  value="216.38" />
-  <Tmax units="K"  value="568.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="89996" />
-  <B value="41.431" />
-  <C value="1.4759" />
-  <D value="-0.0019237" />
-  <E value="7.4664E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.4825" />
-  <B value="-1000" />
-  <C value="-6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.909" />
-  <B value="3157.8" />
-  <C value="-62.156" />
-  <Tmin units="K"  value="344.31" />
-  <Tmax units="K"  value="510.48" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.23434" />
-  <B value="-0.034984" />
-  <C value="0.000035201" />
-  <Tmin units="K"  value="211.15" />
-  <Tmax units="K"  value="454.96" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.49042" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.452013E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="286.8637" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2567" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.58036" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.062" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.705377" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3998" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.163455" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8486" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.936" />
-<UniquacQP name="UNIQUAC q'"  units="_"  value="4.936" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000821" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.2075" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3992" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15445.57" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.163455" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="6" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="6" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="6" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="6" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="6" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="6" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-65-9" />
-<Smiles name="SMILES"  value="CCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="40" />
-<CompoundID name="Name"  value="2,2,3-trimethylpentane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2CH(CH3)CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="563.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2730000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.436" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="382.99" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="160.89" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="160.89" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0021759" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16043" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.298" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.913E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14690" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08869" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.252E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.1995E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.7726E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="423880" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8619000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.99028" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06754E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9338" />
-  <B value="-0.0061647" />
-  <Tmin units="K"  value="64.36" />
-  <Tmax units="K"  value="160.89" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53892" />
-  <B value="0.263" />
-  <C value="563.51" />
-  <D value="0.24185" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="563.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="87.50671" />
-  <B value="-7031.238" />
-  <C value="-9.863302" />
-  <D value="7.128886E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="563.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.030131E+07" />
-  <B value="1.053957" />
-  <C value="-0.826185" />
-  <D value="0.00124096" />
-  <E value="0.214352" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="542.31" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="170570" />
-  <B value="-194.18" />
-  <C value="8.4382" />
-  <D value="0.017272" />
-  <E value="-0.000019404" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="383" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="45546" />
-  <B value="-344.09" />
-  <C value="12.853" />
-  <D value="0.00059243" />
-  <E value="-1.8071E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26813" />
-  <B value="-335.1" />
-  <C value="-52.252" />
-  <D value="-7705.4" />
-  <E value="11664" />
-  <Tmin units="K"  value="281.75" />
-  <Tmax units="K"  value="1800" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.9806" />
-  <B value="1118.5" />
-  <C value="-0.42179" />
-  <D value="0.000001606" />
-  <E value="2" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="383" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.6777E-07" />
-  <B value="0.5509" />
-  <C value="223.7" />
-  <D value="10.797" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.050146" />
-  <B value="3.605" />
-  <C value="-1.5994" />
-  <D value="-0.00051269" />
-  <E value="-0.0000013443" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="383" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000016836" />
-  <B value="1.25" />
-  <C value="-167.06" />
-  <D value="132290" />
-  <Tmin units="K"  value="383" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015221" />
-  <B value="12.964" />
-  <C value="-2.9325" />
-  <D value="-0.00061856" />
-  <E value="-0.000002993" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="542.31" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-37332" />
-  <B value="898.15" />
-  <C value="-0.53928" />
-  <D value="0.00011981" />
-  <E value="1.1807E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.851" />
-  <B value="3143.8" />
-  <C value="-45.907" />
-  <Tmin units="K"  value="340.92" />
-  <Tmax units="K"  value="504.02" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.8115" />
-  <B value="-0.055178" />
-  <C value="0.000068762" />
-  <Tmin units="K"  value="160.89" />
-  <Tmax units="K"  value="383" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.4679" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.327233E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="264.9302" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.5705" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.06" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.718651" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.29649" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.160344" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.85" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.94" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001434" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2584" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2975" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14768.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.160344" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="564-02-3" />
-<Smiles name="SMILES"  value="CC(C)(C)C(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="41" />
-<CompoundID name="Name"  value="2,2,4-trimethylpentane" />
-<StructureFormula name="Structure"  value="(CH3)3CCH2CH(CH3)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="543.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2570000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4697" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="372.39" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="165.777" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="165.777" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0170695" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16607" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.304" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.091E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14080" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08869" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.252E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.2401E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.394E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="422960" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9196000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97675" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06528E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.773" />
-  <B value="-0.0058781" />
-  <Tmin units="K"  value="66.31" />
-  <Tmax units="K"  value="165.78" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.48523" />
-  <B value="0.24924" />
-  <C value="543.9" />
-  <D value="0.25602" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="543.89" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="83.71044" />
-  <B value="-6701.601" />
-  <C value="-9.312194" />
-  <D value="6.808451E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="543.89" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.633E+07" />
-  <B value="0.37451" />
-  <C value="-0.066775" />
-  <D value="-0.010135" />
-  <E value="0.080832" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="543.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="3861.3" />
-  <B value="1005.9" />
-  <C value="-1.0592" />
-  <D value="0.0042173" />
-  <E value="-0.0000083422" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="165.79" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="159470" />
-  <B value="-380.54" />
-  <C value="12.372" />
-  <D value="-0.00044236" />
-  <E value="0.0000034887" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="520" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84635" />
-  <B value="-470.35" />
-  <C value="13.011" />
-  <D value="0.00041124" />
-  <E value="-1.2926E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26688" />
-  <B value="-321.67" />
-  <C value="-47.437" />
-  <D value="-5317.2" />
-  <E value="7275.9" />
-  <Tmin units="K"  value="271.9" />
-  <Tmax units="K"  value="1771" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-22.241" />
-  <B value="1365.6" />
-  <C value="1.8379" />
-  <D value="-0.0000051189" />
-  <E value="2" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="541.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9933E-07" />
-  <B value="0.67222" />
-  <C value="163.02" />
-  <D value="-5306.3" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.044744" />
-  <B value="-42.414" />
-  <C value="-1.7361" />
-  <D value="-0.0023225" />
-  <E value="-0.0000040597" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="372.39" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000011401" />
-  <B value="1.3632" />
-  <C value="286.23" />
-  <D value="6065.2" />
-  <Tmin units="K"  value="355.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0097592" />
-  <B value="31.944" />
-  <C value="-3.3103" />
-  <D value="0.0003744" />
-  <E value="-0.0000053994" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="543.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="3192.8" />
-  <B value="640.7" />
-  <C value="0.055291" />
-  <D value="-0.0004627" />
-  <E value="2.1776E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.714" />
-  <B value="2972" />
-  <C value="-48.851" />
-  <Tmin units="K"  value="327.85" />
-  <Tmax units="K"  value="488.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.727" />
-  <B value="-0.025461" />
-  <C value="0.000019917" />
-  <Tmin units="K"  value="165.78" />
-  <Tmax units="K"  value="541.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.47894" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.106578E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="301.9995" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.38564" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0608" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.694955" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3045" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.165452" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.85" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.94" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004045" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.82187" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3033" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14050.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.165452" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="540-84-1" />
-<Smiles name="SMILES"  value="CC(C)(C)CC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="42" />
-<CompoundID name="Name"  value="2,3,3-trimethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)C(CH3)2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="573.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2820000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4551" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="387.92" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="172.22" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="172.22" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0168197" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15815" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.291" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.96E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14920" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08869" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.252E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.1845E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.828E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="427020" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="857720" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91681" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06876E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9997" />
-  <B value="-0.0058029" />
-  <Tmin units="K"  value="68.89" />
-  <Tmax units="K"  value="172.22" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.56592" />
-  <B value="0.26622" />
-  <C value="573.5" />
-  <D value="0.26429" />
-  <Tmin units="K"  value="172.22" />
-  <Tmax units="K"  value="573.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.87517" />
-  <B value="-6894.749" />
-  <C value="-9.15013" />
-  <D value="6.430758E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="172.22" />
-  <Tmax units="K"  value="573.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.838161E+07" />
-  <B value="1.059379" />
-  <C value="-1.234692" />
-  <D value="0.816701" />
-  <E value="-0.225175" />
-  <Tmin units="K"  value="172.22" />
-  <Tmax units="K"  value="573.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="0" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="217000" />
-  <B value="82.075" />
-  <C value="1.8853" />
-  <D value="0.036678" />
-  <E value="-0.000031911" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="320" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="48585" />
-  <B value="-365.95" />
-  <C value="12.926" />
-  <D value="0.00051631" />
-  <E value="-1.5846E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26872" />
-  <B value="-341.85" />
-  <C value="-55.056" />
-  <D value="-7881.5" />
-  <E value="10783" />
-  <Tmin units="K"  value="286.75" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.941" />
-  <B value="1191.2" />
-  <C value="-0.045562" />
-  <D value="-0.0000023087" />
-  <E value="2" />
-  <Tmin units="K"  value="172.22" />
-  <Tmax units="K"  value="452.22" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.2493E-07" />
-  <B value="0.49302" />
-  <C value="371.93" />
-  <D value="-89.774" />
-  <Tmin units="K"  value="387.91" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.040193" />
-  <B value="3.6823" />
-  <C value="-1.645" />
-  <D value="-0.00052834" />
-  <E value="-0.0000014091" />
-  <Tmin units="K"  value="172.22" />
-  <Tmax units="K"  value="387.91" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000018829" />
-  <B value="1.2378" />
-  <C value="-181.1" />
-  <D value="146480" />
-  <Tmin units="K"  value="387.91" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01117" />
-  <B value="27.611" />
-  <C value="-3.1709" />
-  <D value="0.00013513" />
-  <E value="-0.0000044446" />
-  <Tmin units="K"  value="172.22" />
-  <Tmax units="K"  value="573.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-47609" />
-  <B value="980.6" />
-  <C value="-0.74331" />
-  <D value="0.00033358" />
-  <E value="-6.7846E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.868" />
-  <B value="3199.9" />
-  <C value="-45.369" />
-  <Tmin units="K"  value="345.13" />
-  <Tmax units="K"  value="513.19" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.0041" />
-  <B value="-0.04624" />
-  <C value="0.000049116" />
-  <Tmin units="K"  value="172.22" />
-  <Tmax units="K"  value="452.22" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.46322" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.938163E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="331.5544" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0601" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.729041" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.28889" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.158155" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.85" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.94" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003849" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2903" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14919.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.158155" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
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-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="560-21-4" />
-<Smiles name="SMILES"  value="CC(C)C(C)(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="43" />
-<CompoundID name="Name"  value="2,3,4-trimethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CH(CH3)CH(CH3)CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="566.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2730000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4562" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="386.62" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="163.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="163.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00303425" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15974" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.316" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.061E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14940" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08869" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.231E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.1732E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.9E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="428400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9267560" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0137" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06943E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9934" />
-  <B value="-0.006099" />
-  <Tmin units="K"  value="65.58" />
-  <Tmax units="K"  value="163.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.44061" />
-  <B value="0.23657" />
-  <C value="566.41" />
-  <D value="0.23009" />
-  <Tmin units="K"  value="163.95" />
-  <Tmax units="K"  value="566.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="83.41936" />
-  <B value="-6957.084" />
-  <C value="-9.207327" />
-  <D value="0.0000063783" />
-  <E value="2" />
-  <Tmin units="K"  value="163.95" />
-  <Tmax units="K"  value="566.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.6943E+07" />
-  <B value="0.86512" />
-  <C value="-0.77048" />
-  <D value="0.30586" />
-  <E value="0.021601" />
-  <Tmin units="K"  value="163.95" />
-  <Tmax units="K"  value="545.22" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="39.715" />
-  <B value="1634.5" />
-  <C value="-9.2594" />
-  <D value="0.036339" />
-  <E value="-0.000053437" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="169.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="108880" />
-  <B value="-13.14" />
-  <C value="10.55" />
-  <D value="0.00536" />
-  <E value="-0.0000028819" />
-  <Tmin units="K"  value="163.63" />
-  <Tmax units="K"  value="320" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="26624" />
-  <B value="-291.65" />
-  <C value="12.829" />
-  <D value="0.00059553" />
-  <E value="-0.0000001821" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27457" />
-  <B value="-374.14" />
-  <C value="-48.597" />
-  <D value="-10331" />
-  <E value="20216" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="1807.15" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-6.3467" />
-  <B value="935.74" />
-  <C value="-0.76144" />
-  <D value="7.5545E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="163.95" />
-  <Tmax units="K"  value="443.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.7868E-07" />
-  <B value="0.51422" />
-  <C value="325.4" />
-  <D value="22.347" />
-  <Tmin units="K"  value="386.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.048086" />
-  <B value="3.7835" />
-  <C value="-1.6094" />
-  <D value="-0.00050636" />
-  <E value="-0.0000013704" />
-  <Tmin units="K"  value="163.95" />
-  <Tmax units="K"  value="386.62" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000017892" />
-  <B value="1.241" />
-  <C value="-169.67" />
-  <D value="132780" />
-  <Tmin units="K"  value="386.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013874" />
-  <B value="14.819" />
-  <C value="-2.967" />
-  <D value="-0.00050079" />
-  <E value="-0.0000033582" />
-  <Tmin units="K"  value="163.95" />
-  <Tmax units="K"  value="545.22" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-9210.924" />
-  <B value="785.5524" />
-  <C value="-0.439805" />
-  <D value="0.0000969271" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.9" />
-  <B value="3174.1" />
-  <C value="-48.02" />
-  <Tmin units="K"  value="340.98" />
-  <Tmax units="K"  value="505.05" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.1859" />
-  <B value="-0.043813" />
-  <C value="0.0000493" />
-  <Tmin units="K"  value="163.95" />
-  <Tmax units="K"  value="443.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.46889" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.006212E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="318.7133" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.48909" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0602" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.721958" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.31439" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.159513" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.85" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.94" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004313" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.96638" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.316137" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14934.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.159513" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="3"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="3"  value="3" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="3"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="5" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="3"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="3"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="565-75-3" />
-<Smiles name="SMILES"  value="CC(C)C(C)C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1204" />
-<CompoundID name="Name"  value="Tetraethylene glycol" />
-<StructureFormula name="Structure"  value="HOCH2(CH2OCH2)3CH2OH" />
-<Family name="Family"  value="49" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="795" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2590000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.564" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.221" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="602.7" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="268.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="268.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000138348" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="194.226" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.172862" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.917442" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.602E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23690" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.08E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10902" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.552E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-8.83E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5.599E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="650100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3.66E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.8" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.3431E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.4822" />
-  <B value="-0.0031101" />
-  <Tmin units="K"  value="107.26" />
-  <Tmax units="K"  value="268.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.46229" />
-  <B value="0.26105" />
-  <C value="795" />
-  <D value="0.27055" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="795" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="106.7938" />
-  <B value="-15323.17" />
-  <C value="-10.86107" />
-  <D value="-5.284752E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="795" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.282157E+08" />
-  <B value="0.159236" />
-  <C value="1.504015" />
-  <D value="-1.941373" />
-  <E value="0.658104" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="795" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="9682.3" />
-  <B value="1222.8" />
-  <C value="-2.3781" />
-  <D value="0.0060594" />
-  <E value="-0.000006823" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="268.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="180650" />
-  <B value="-180.95" />
-  <C value="12.547" />
-  <D value="0.0020505" />
-  <E value="-0.0000018444" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="600.45" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122630" />
-  <B value="-416.14" />
-  <C value="13.02" />
-  <D value="0.00050957" />
-  <E value="-2.1012E-07" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="1200.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.56254" />
-  <B value="-662.06" />
-  <C value="-258.7" />
-  <D value="201090" />
-  <E value="-5319300" />
-  <Tmin units="K"  value="397.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-702.8128" />
-  <B value="30403.47" />
-  <C value="106.7279" />
-  <D value="-0.000116388" />
-  <E value="2" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="636" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.6872E-08" />
-  <B value="0.801" />
-  <C value="119.91" />
-  <D value="0.29361" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.11138" />
-  <B value="-134.47" />
-  <C value="-0.46393" />
-  <D value="-0.00084854" />
-  <E value="-4.1141E-07" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="602.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016749" />
-  <B value="0.91863" />
-  <C value="699.93" />
-  <D value="16777" />
-  <Tmin units="K"  value="602.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015451" />
-  <B value="194.65" />
-  <C value="-3.9184" />
-  <D value="0.0029026" />
-  <E value="-0.0000044511" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="795" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="17162" />
-  <B value="938.31" />
-  <C value="-0.55677" />
-  <D value="0.00012535" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="1200.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.098" />
-  <B value="4853.6" />
-  <C value="-143.25" />
-  <Tmin units="K"  value="477.43" />
-  <Tmax units="K"  value="711.81" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="10.586" />
-  <B value="-0.059489" />
-  <C value="0.00004594" />
-  <Tmin units="K"  value="268.15" />
-  <Tmax units="K"  value="636" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.83332" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="9.434827E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="226.5127" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="199.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0807" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.13028" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.7224" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.173363" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="8.1269" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="7.440001" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.930639" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23571.8" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.173363" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="5" />
-  <group id="15"  value="2" />
-  <group id="26"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="5" />
-  <group id="14"  value="2" />
-  <group id="28"  value="3" />
-  </UnifacLLE>
-<Asog name="ASOG" >
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-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="5" />
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-  <group id="26"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="5" />
-  <group id="14"  value="2" />
-  <group id="25"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="112-60-7" />
-<Smiles name="SMILES"  value="OCCOCCOCCOCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="803" />
-<CompoundID name="Name"  value="Indene" />
-<StructureFormula name="Structure"  value="C6H4(CH2CHCH)" />
-<Family name="Family"  value="23" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="687" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3820000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.368" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.246" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="455.77" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="271.7" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="271.7" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="17.0209" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="116.16" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.116856" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.333766" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.839E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20310" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.23E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06723" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.23E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.6328E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.3396E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="336870" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.02E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2681" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.61948E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.129" />
-  <B value="-0.0046181" />
-  <Tmin units="K"  value="108.68" />
-  <Tmax units="K"  value="271.7" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.68574" />
-  <B value="0.25341" />
-  <C value="687" />
-  <D value="0.30914" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="665.14" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="198.3126" />
-  <B value="-13212.05" />
-  <C value="-26.47637" />
-  <D value="0.0000206314" />
-  <E value="2" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="687" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.127174E+08" />
-  <B value="2.195635" />
-  <C value="-2.278889" />
-  <D value="0.782692" />
-  <E value="-0.231351" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="665.14" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-52909" />
-  <B value="1891.2" />
-  <C value="-10.945" />
-  <D value="0.035915" />
-  <E value="-0.000041132" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="271.7" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="87661" />
-  <B value="-18.633" />
-  <C value="10.258" />
-  <D value="0.0056195" />
-  <E value="-0.0000040934" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="54598" />
-  <B value="-572.63" />
-  <C value="13.077" />
-  <D value="-0.000062304" />
-  <E value="-1.4084E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.40021" />
-  <B value="-548.58" />
-  <C value="-63.413" />
-  <D value="-36103" />
-  <E value="53578" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-136.89" />
-  <B value="6165.4" />
-  <C value="19.669" />
-  <D value="-0.000025488" />
-  <E value="2" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="455.77" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.1278E-07" />
-  <B value="0.4938" />
-  <C value="370.54" />
-  <D value="-3708.9" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0034145" />
-  <B value="-80.459" />
-  <C value="-0.91571" />
-  <D value="-0.0024408" />
-  <E value="2.3991E-07" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="455.77" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000075165" />
-  <B value="1.055" />
-  <C value="558.89" />
-  <D value="35355" />
-  <Tmin units="K"  value="455.77" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0084894" />
-  <B value="135.54" />
-  <C value="-3.7264" />
-  <D value="0.0026269" />
-  <E value="-0.0000065847" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="665.14" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-34733" />
-  <B value="643.24" />
-  <C value="-0.38654" />
-  <D value="0.00008602" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.786" />
-  <B value="3534.8" />
-  <C value="-73.926" />
-  <Tmin units="K"  value="413.15" />
-  <Tmax units="K"  value="599.57" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.2731" />
-  <B value="-0.040741" />
-  <C value="0.000039218" />
-  <Tmin units="K"  value="271.7" />
-  <Tmax units="K"  value="455.77" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.36114" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.195685E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="287.8965" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261272" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="124.98" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.481" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0516" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.00263" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.262" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.116856" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.431773" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.892" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.02812" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="4.8814" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.262" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20467.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.116856" />
-<UnifacVLE name="UNIFAC" >
-  <group id="6"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="6"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="1" />
-  <group id="6"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="6"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="6"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="95-13-6" />
-<Smiles name="SMILES"  value="c1(CC=C2)c2cccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="820" />
-<CompoundID name="Name"  value="Indane" />
-<StructureFormula name="Structure"  value="C6H4(CH2)3" />
-<Family name="Family"  value="23" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="684.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3950000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.393" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="451" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="221.74" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="221.74" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.152927" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="118.178" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12315" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.309213" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.85E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19420" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.8E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07075" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.77E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="6.07E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.668E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="348910" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8598000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.87712" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.7626E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.978" />
-  <B value="-0.0055307" />
-  <Tmin units="K"  value="88.7" />
-  <Tmax units="K"  value="221.74" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.63627" />
-  <B value="0.25179" />
-  <C value="684.9" />
-  <D value="0.29165" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="684.9" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="97.02207" />
-  <B value="-8795.05" />
-  <C value="-11.00248" />
-  <D value="6.105132E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="684.9" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.2067E+07" />
-  <B value="-0.0045874" />
-  <C value="2.0817" />
-  <D value="-3.2476" />
-  <E value="1.6013" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="684.9" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-355.12" />
-  <B value="1287.7" />
-  <C value="-10.018" />
-  <D value="0.047026" />
-  <E value="-0.000077286" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="221.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="136380" />
-  <B value="-29.478" />
-  <C value="8.0608" />
-  <D value="0.01305" />
-  <E value="-0.000010993" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="451.12" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="60321" />
-  <B value="-643.06" />
-  <C value="13.337" />
-  <D value="-0.00018807" />
-  <E value="3.6677E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.087726" />
-  <B value="-163.08" />
-  <C value="-117.03" />
-  <D value="24981" />
-  <E value="-82865" />
-  <Tmin units="K"  value="342.45" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-151.95" />
-  <B value="6810.2" />
-  <C value="21.863" />
-  <D value="-0.00002342" />
-  <E value="2" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="547.92" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000002842" />
-  <B value="0.64259" />
-  <C value="225.95" />
-  <D value="-643.44" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.041318" />
-  <B value="5.7098" />
-  <C value="-1.5369" />
-  <D value="-0.00043639" />
-  <E value="-0.0000010195" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="451.12" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0089527" />
-  <B value="0.43447" />
-  <C value="617.91" />
-  <D value="764370" />
-  <Tmin units="K"  value="451.12" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0094403" />
-  <B value="81.588" />
-  <C value="-3.3664" />
-  <D value="0.0013789" />
-  <E value="-0.000005115" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="684.9" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-47835" />
-  <B value="715.44" />
-  <C value="-0.41555" />
-  <D value="0.0000889" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.208" />
-  <B value="3817.3" />
-  <C value="-56.866" />
-  <Tmin units="K"  value="412" />
-  <Tmax units="K"  value="611.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="3.0311" />
-  <B value="-0.045083" />
-  <C value="0.000044726" />
-  <Tmin units="K"  value="221.74" />
-  <Tmax units="K"  value="547.92" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.381158" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.491035E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="417.5667" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.263427" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="147.9" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.40707" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0528" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.862893" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.305" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.123128" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.66381" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.108" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.85719" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.305" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19405.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.123128" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="1" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="3" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  <group id="10"  value="3" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="496-11-7" />
-<Smiles name="SMILES"  value="C1=CC2=C(C=C1)CCC2" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="510" />
-<CompoundID name="Name"  value="Cumene" />
-<StructureFormula name="Structure"  value="(C6H5)CH(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="631" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3209000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4347" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="425.52" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="177.14" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="177.14" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000471313" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.194" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14017" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.326" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.322E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17420" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07996" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.014E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="4000000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.379E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="386000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7326000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97464" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.951E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.07" />
-  <B value="-0.0062914" />
-  <Tmin units="K"  value="70.86" />
-  <Tmax units="K"  value="177.14" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50221" />
-  <B value="0.23722" />
-  <C value="631.11" />
-  <D value="0.26133" />
-  <Tmin units="K"  value="153.1" />
-  <Tmax units="K"  value="631.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="118.1491" />
-  <B value="-9251.635" />
-  <C value="-14.30054" />
-  <D value="9.196883E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="177.14" />
-  <Tmax units="K"  value="631.05" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.766E+07" />
-  <B value="0.38939" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="177.14" />
-  <Tmax units="K"  value="631" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10800" />
-  <B value="1565.7" />
-  <C value="-10.507" />
-  <D value="0.040966" />
-  <E value="-0.000034539" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="177.16" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="41467" />
-  <B value="-297.98" />
-  <C value="13.905" />
-  <D value="-0.0047724" />
-  <E value="0.0000064694" />
-  <Tmin units="K"  value="177.14" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86134" />
-  <B value="-649.19" />
-  <C value="13.375" />
-  <D value="-0.00027067" />
-  <E value="7.9617E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25813" />
-  <B value="-351.41" />
-  <C value="-75.368" />
-  <D value="-30164" />
-  <E value="51230" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1893" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-16.711" />
-  <B value="1557.8" />
-  <C value="0.70915" />
-  <D value="0.000002636" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.9385E-07" />
-  <B value="0.59572" />
-  <C value="281.33" />
-  <D value="-806.82" />
-  <Tmin units="K"  value="177.14" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.085857" />
-  <B value="481.58" />
-  <C value="-8.587" />
-  <D value="0.025021" />
-  <E value="-0.000042138" />
-  <Tmin units="K"  value="177.14" />
-  <Tmax units="K"  value="500" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1.6743E-07" />
-  <B value="1.8369" />
-  <C value="-449.46" />
-  <D value="112760" />
-  <Tmin units="K"  value="380" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0080328" />
-  <B value="47.667" />
-  <C value="-3.2474" />
-  <D value="0.00083757" />
-  <E value="-0.0000055542" />
-  <Tmin units="K"  value="177.14" />
-  <Tmax units="K"  value="631" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="24819" />
-  <B value="284.32" />
-  <C value="0.99258" />
-  <D value="-0.0016755" />
-  <E value="0.0000007419" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.498" />
-  <B value="3116.8" />
-  <C value="-78.092" />
-  <Tmin units="K"  value="380.45" />
-  <Tmax units="K"  value="562.1" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.7243" />
-  <B value="-0.05195" />
-  <C value="0.000062446" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.42713" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.084995E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="327.2265" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2617" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0567" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.864757" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.32769" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.139854" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2708" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.044" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.008698" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3353" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17436.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.139854" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="98-82-8" />
-<Smiles name="SMILES"  value="c1(C(C)C)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="509" />
-<CompoundID name="Name"  value="N-propylbenzene" />
-<StructureFormula name="Structure"  value="(C6H5)CH2CH2CH3" />
-<Family name="Family"  value="16" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="638.35" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3200000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.44" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="432.35" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="173.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="173.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000181372" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.194" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1402" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.345" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.344E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17670" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.23E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07997" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.012E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="7900000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.376E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="400140" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9268000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0802" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.95415E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.129" />
-  <B value="-0.0065012" />
-  <Tmin units="K"  value="69.42" />
-  <Tmax units="K"  value="173.55" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.56872" />
-  <B value="0.25108" />
-  <C value="638.35" />
-  <D value="0.29337" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="638.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="90.904" />
-  <B value="-8254.5" />
-  <C value="-10.105" />
-  <D value="0.0000055769" />
-  <E value="2" />
-  <Tmin units="K"  value="173.55" />
-  <Tmax units="K"  value="638.35" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.1312E+07" />
-  <B value="1.0445" />
-  <C value="-0.61076" />
-  <D value="-0.59569" />
-  <E value="0.63332" />
-  <Tmin units="K"  value="173.55" />
-  <Tmax units="K"  value="639.84" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18982" />
-  <B value="1868.5" />
-  <C value="-13.446" />
-  <D value="0.053298" />
-  <E value="-0.000064273" />
-  <Tmin units="K"  value="15.78" />
-  <Tmax units="K"  value="173.59" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="44429" />
-  <B value="65.841" />
-  <C value="10.897" />
-  <D value="0.0032658" />
-  <E value="-5.4402E-07" />
-  <Tmin units="K"  value="173.55" />
-  <Tmax units="K"  value="432.39" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="82370" />
-  <B value="-622.6" />
-  <C value="13.289" />
-  <D value="-0.00014307" />
-  <E value="2.6658E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27002" />
-  <B value="-373.98" />
-  <C value="-70.824" />
-  <D value="-57233" />
-  <E value="135160" />
-  <Tmin units="K"  value="319" />
-  <Tmax units="K"  value="1914.9" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.601" />
-  <B value="1467.9" />
-  <C value="0.61045" />
-  <D value="8.0442E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="432.39" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.6834E-07" />
-  <B value="0.55936" />
-  <C value="217.09" />
-  <D value="10253" />
-  <Tmin units="K"  value="173.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.081391" />
-  <B value="2.87" />
-  <C value="-1.3455" />
-  <D value="-0.00061835" />
-  <E value="-5.1664E-07" />
-  <Tmin units="K"  value="173.55" />
-  <Tmax units="K"  value="583.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.025018" />
-  <B value="0.26728" />
-  <C value="100.66" />
-  <D value="971170" />
-  <Tmin units="K"  value="432.39" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010179" />
-  <B value="31.565" />
-  <C value="-3.0234" />
-  <D value="0.00013909" />
-  <E value="-0.0000042396" />
-  <Tmin units="K"  value="173.55" />
-  <Tmax units="K"  value="638.35" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="39569" />
-  <B value="199.18" />
-  <C value="0.98601" />
-  <D value="-0.0014461" />
-  <E value="5.8733E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.146" />
-  <B value="3610.6" />
-  <C value="-57.056" />
-  <Tmin units="K"  value="383.15" />
-  <Tmax units="K"  value="564.96" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.6832" />
-  <B value="-0.043893" />
-  <C value="0.00004826" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="432.39" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.42982" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.985018E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="349.669" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2599" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.70588" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0577" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.864757" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.34319" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.139831" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2716" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.048" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.007551" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.4065" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3444" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17805.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.139831" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="103-65-1" />
-<Smiles name="SMILES"  value="c1(CCC)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="149" />
-<CompoundID name="Name"  value="N-propylcyclohexane" />
-<StructureFormula name="Structure"  value="(C6H11)CH2CH2CH3" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="639.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2807000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.477" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="429.897" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="178.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="178.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000859078" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="126.239" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.159758" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.259535" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.367E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16350" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09092" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.157E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.933E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.738E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="419530" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.037E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.87516" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.47966E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8087" />
-  <B value="-0.005494" />
-  <Tmin units="K"  value="71.3" />
-  <Tmax units="K"  value="178.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.55532" />
-  <B value="0.26594" />
-  <C value="639.15" />
-  <D value="0.29886" />
-  <Tmin units="K"  value="178.25" />
-  <Tmax units="K"  value="639.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.958" />
-  <B value="-7871.7" />
-  <C value="-8.8759" />
-  <D value="0.0000037842" />
-  <E value="2" />
-  <Tmin units="K"  value="178.25" />
-  <Tmax units="K"  value="639.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.8086E+07" />
-  <B value="1.2548" />
-  <C value="-2.1193" />
-  <D value="2.1809" />
-  <E value="-0.84474" />
-  <Tmin units="K"  value="178.25" />
-  <Tmax units="K"  value="639.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-17515" />
-  <B value="1789.5" />
-  <C value="-10.949" />
-  <D value="0.037847" />
-  <E value="-0.000022183" />
-  <Tmin units="K"  value="20.44" />
-  <Tmax units="K"  value="166.83" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="47569" />
-  <B value="39.903" />
-  <C value="11.009" />
-  <D value="0.0038436" />
-  <E value="-0.0000012583" />
-  <Tmin units="K"  value="178.25" />
-  <Tmax units="K"  value="429.9" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="123230" />
-  <B value="-835.51" />
-  <C value="14.003" />
-  <D value="-0.00055451" />
-  <E value="1.5912E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27598" />
-  <B value="-333.23" />
-  <C value="-82.257" />
-  <D value="-29470" />
-  <E value="49574" />
-  <Tmin units="K"  value="319" />
-  <Tmax units="K"  value="1754" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-18.964" />
-  <B value="1768.3" />
-  <C value="1.0133" />
-  <D value="0.0000031666" />
-  <E value="2" />
-  <Tmin units="K"  value="248.15" />
-  <Tmax units="K"  value="429.9" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010206" />
-  <B value="0.44533" />
-  <C value="352.16" />
-  <D value="7219.8" />
-  <Tmin units="K"  value="178.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.049742" />
-  <B value="3.3035" />
-  <C value="-1.5814" />
-  <D value="-0.00048571" />
-  <E value="-0.000001015" />
-  <Tmin units="K"  value="178.25" />
-  <Tmax units="K"  value="429.9" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000001205" />
-  <B value="1.6222" />
-  <C value="-42.945" />
-  <D value="15739" />
-  <Tmin units="K"  value="429.9" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011029" />
-  <B value="31.201" />
-  <C value="-3.1062" />
-  <D value="0.00016942" />
-  <E value="-0.000003854" />
-  <Tmin units="K"  value="178.25" />
-  <Tmax units="K"  value="639.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-62027.8" />
-  <B value="982.0266" />
-  <C value="-0.560028" />
-  <D value="0.000114244" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.417" />
-  <B value="3136.4" />
-  <C value="-77.095" />
-  <Tmin units="K"  value="383.78" />
-  <Tmax units="K"  value="566.38" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.8674" />
-  <B value="-0.044293" />
-  <C value="0.000049254" />
-  <Tmin units="K"  value="248.15" />
-  <Tmax units="K"  value="429.9" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.4812" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.622026E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="292.1178" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="184.68" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0646" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.796026" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.26539" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.159758" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.068799" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.856" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2577" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16377.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.159758" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="7" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="7" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="12"  value="1" />
-  <group id="13"  value="5" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="7" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="78"  value="5" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1678-92-8" />
-<Smiles name="SMILES"  value="C1CCCCC1CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="46" />
-<CompoundID name="Name"  value="N-nonane" />
-<StructureFormula name="Structure"  value="CH3(CH2)7CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="594.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2290000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.555" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="423.97" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="219.66" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="219.66" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.430583" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.258" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1797" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.443" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.814E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15630" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09895" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.369E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.2874E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.498E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="506400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.547E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.99218" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.68455E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.4283" />
-  <B value="-0.0023699" />
-  <Tmin units="K"  value="193.15" />
-  <Tmax units="K"  value="219.66" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.46379" />
-  <B value="0.25569" />
-  <C value="594.6" />
-  <D value="0.27961" />
-  <Tmin units="K"  value="219.66" />
-  <Tmax units="K"  value="594.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="34.38252" />
-  <B value="-6235.412" />
-  <C value="-1.153933" />
-  <D value="-6.408486E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="219.66" />
-  <Tmax units="K"  value="594.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.427482E+07" />
-  <B value="1.573752" />
-  <C value="-1.785921" />
-  <D value="0.692082" />
-  <E value="0.00268541" />
-  <Tmin units="K"  value="219.63" />
-  <Tmax units="K"  value="594.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-28596" />
-  <B value="2152.5" />
-  <C value="-8.5201" />
-  <D value="0.0044645" />
-  <E value="0.000055805" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="217.21" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="263370" />
-  <B value="-14466" />
-  <C value="134.04" />
-  <D value="-0.36823" />
-  <E value="0.00038456" />
-  <Tmin units="K"  value="219.66" />
-  <Tmax units="K"  value="325" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="137710" />
-  <B value="-699.52" />
-  <C value="13.613" />
-  <D value="-0.00021735" />
-  <E value="5.3695E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.46778" />
-  <B value="-570.55" />
-  <C value="-46.368" />
-  <D value="-127140" />
-  <E value="315920" />
-  <Tmin units="K"  value="297.83" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-75.488" />
-  <B value="3420.7" />
-  <C value="10.183" />
-  <D value="-0.000014836" />
-  <E value="2" />
-  <Tmin units="K"  value="218.15" />
-  <Tmax units="K"  value="593.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.0363E-07" />
-  <B value="0.77284" />
-  <C value="221.39" />
-  <D value="-190.1" />
-  <Tmin units="K"  value="219.66" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.022998" />
-  <B value="-23.224" />
-  <C value="-1.6475" />
-  <D value="-0.000633" />
-  <E value="-0.0000035211" />
-  <Tmin units="K"  value="219.66" />
-  <Tmax units="K"  value="423.97" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.065472" />
-  <B value="0.27739" />
-  <C value="-3569.2" />
-  <D value="-1629700" />
-  <Tmin units="K"  value="423.97" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0056952" />
-  <B value="124.02" />
-  <C value="-4.2139" />
-  <D value="0.0035336" />
-  <E value="-0.0000093096" />
-  <Tmin units="K"  value="219.66" />
-  <Tmax units="K"  value="594.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="101040" />
-  <B value="38.039" />
-  <C value="1.6975" />
-  <D value="-0.0022264" />
-  <E value="8.7011E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.4825" />
-  <B value="-1000" />
-  <C value="-6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.112" />
-  <B value="3452.4" />
-  <C value="-63.768" />
-  <Tmin units="K"  value="357.73" />
-  <Tmax units="K"  value="515.67" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.5536" />
-  <B value="-0.024184" />
-  <C value="0.000017792" />
-  <Tmin units="K"  value="218.15" />
-  <Tmax units="K"  value="593.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550289" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.8299E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="291.6737" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.251687" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="1.1157" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0686" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.720247" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.4437" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.179507" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.523" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.476" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.005435" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-2.3143" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.4439" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15648.08" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1796" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="7" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="7" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="7" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="7" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="7" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="7" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-84-2" />
-<Smiles name="SMILES"  value="CCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="701" />
-<CompoundID name="Name"  value="Naphthalene" />
-<StructureFormula name="Structure"  value="(C6H4)(C4H4)" />
-<Family name="Family"  value="19" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="748.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4050000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.407" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="491.16" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="353.434" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="353.43" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="991.297" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.174" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12913" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.304" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.045E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19490" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07464" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.42E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.5058E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.2408E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="333150" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.898E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.96523" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.9809E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.819" />
-  <B value="-0.0022406" />
-  <Tmin units="K"  value="281.46" />
-  <Tmax units="K"  value="353.43" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.45282" />
-  <B value="0.21953" />
-  <C value="748.4" />
-  <D value="0.23236" />
-  <Tmin units="K"  value="333.15" />
-  <Tmax units="K"  value="748.35" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="93.15947" />
-  <B value="-9448.063" />
-  <C value="-10.23844" />
-  <D value="4.335455E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="748.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.732822E+07" />
-  <B value="1.116621" />
-  <C value="-1.313575" />
-  <D value="0.672121" />
-  <E value="-0.00584514" />
-  <Tmin units="K"  value="353.43" />
-  <Tmax units="K"  value="749.42" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7014.1" />
-  <B value="684.23" />
-  <C value="-2.2709" />
-  <D value="0.008208" />
-  <E value="-0.0000076772" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="353.43" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="149170" />
-  <B value="579.65" />
-  <C value="3.8152" />
-  <D value="0.021624" />
-  <E value="-0.000015657" />
-  <Tmin units="K"  value="353.43" />
-  <Tmax units="K"  value="491.14" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="49831" />
-  <B value="-547.92" />
-  <C value="13.201" />
-  <D value="-0.00013999" />
-  <E value="2.8208E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.13484" />
-  <B value="-251.35" />
-  <C value="-132.06" />
-  <D value="-59271" />
-  <E value="77447" />
-  <Tmin units="K"  value="350" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.2151" />
-  <B value="1338.2" />
-  <C value="-0.46592" />
-  <D value="0.00000135" />
-  <E value="2" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="633.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2323E-08" />
-  <B value="1.0475" />
-  <C value="-162.06" />
-  <D value="35144" />
-  <Tmin units="K"  value="325.8" />
-  <Tmax units="K"  value="1266.41" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.033214" />
-  <B value="-361.89" />
-  <C value="-0.012818" />
-  <D value="-0.0040236" />
-  <E value="0.0000012782" />
-  <Tmin units="K"  value="353.43" />
-  <Tmax units="K"  value="694.96" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000017754" />
-  <B value="1.2123" />
-  <C value="69.759" />
-  <D value="78517" />
-  <Tmin units="K"  value="371.64" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0074501" />
-  <B value="94.11" />
-  <C value="-3.4217" />
-  <D value="0.0018602" />
-  <E value="-0.0000054745" />
-  <Tmin units="K"  value="353.43" />
-  <Tmax units="K"  value="727.61" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="24021" />
-  <B value="118.95" />
-  <C value="1.3285" />
-  <D value="-0.0019897" />
-  <E value="8.4583E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.318" />
-  <B value="4256.5" />
-  <C value="-56.542" />
-  <Tmin units="K"  value="452.66" />
-  <Tmax units="K"  value="673.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.8047" />
-  <B value="-0.019941" />
-  <C value="0.000014687" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="633.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.38343" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.805835E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="409.9511" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="140.88" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.35375" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0554" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.969046" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.130825" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.920237" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.368" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005006" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.78227" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.302" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19187.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.130825" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="8" />
-  <group id="11"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="8" />
-  <group id="10"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="8" />
-  <group id="11"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="8" />
-  <group id="11"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="8" />
-  <group id="10"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="91-20-3" />
-<Smiles name="SMILES"  value="c1cccc2ccccc21" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="723" />
-<CompoundID name="Name"  value="1-methylindene" />
-<StructureFormula name="Structure"  value="CH3(C9H7)" />
-<Family name="Family"  value="23" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="703" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3460000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.436" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.258" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="471.65" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="130.186" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.134643" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.334861" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.195E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19120" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07745" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.56E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.912E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.97E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="354000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.28E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.82" />
-  <B value="-1.1395E-16" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61191" />
-  <B value="0.25938" />
-  <C value="703" />
-  <D value="0.29267" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="680.74" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="86.18824" />
-  <B value="-8859.756" />
-  <C value="-9.212247" />
-  <D value="3.741568E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="703" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.0901E+07" />
-  <B value="1.9933" />
-  <C value="-4.5733" />
-  <D value="5.098" />
-  <E value="-2.0923" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="680.74" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-3419.9" />
-  <B value="1162.6" />
-  <C value="-5.6175" />
-  <D value="0.02291" />
-  <E value="-0.000035065" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="293.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="152820" />
-  <B value="-189.88" />
-  <C value="10.81" />
-  <D value="0.00256" />
-  <E value="-0.0000011085" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="471.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-133130" />
-  <B value="-213.74" />
-  <C value="13.196" />
-  <D value="0.00017372" />
-  <E value="-4.8074E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28669" />
-  <B value="-413.47" />
-  <C value="-98.347" />
-  <D value="-24136" />
-  <E value="-27455" />
-  <Tmin units="K"  value="351.5" />
-  <Tmax units="K"  value="1931.5" />
-  </SecondVirialCoefficient>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000033072" />
-  <B value="0.32792" />
-  <C value="786.18" />
-  <D value="680.97" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.018671" />
-  <B value="-66.592" />
-  <C value="-0.99313" />
-  <D value="-0.0021306" />
-  <E value="2.0941E-07" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="471.65" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000091267" />
-  <B value="1.0385" />
-  <C value="720.72" />
-  <D value="-19410" />
-  <Tmin units="K"  value="471.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011077" />
-  <B value="98.828" />
-  <C value="-3.4597" />
-  <D value="0.0014463" />
-  <E value="-0.0000045421" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="680.74" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-96611" />
-  <B value="1045.1" />
-  <C value="-0.86408" />
-  <D value="0.00027375" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.371" />
-  <B value="4079.4" />
-  <C value="-58.289" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="703" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.419867" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.191125E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="349.703" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261176" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="145.5" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0578" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.97441" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.33569" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.134207" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.105471" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.424" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.33569" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18312.4" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.134207" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="767-59-9" />
-<Smiles name="SMILES"  value="C1=CC=C2C(=C1)C=CC2C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="724" />
-<CompoundID name="Name"  value="2-methylindene" />
-<StructureFormula name="Structure"  value="CH3(C9H7)" />
-<Family name="Family"  value="23" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="711" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3460000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.436" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="479.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="353.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="353.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3020.69" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="130.186" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13407" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.350814" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.21E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19650" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07744" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.88E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.15E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.19E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="361000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.21E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8568" />
-  <B value="-0.0013205" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="353.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.58652" />
-  <B value="0.25339" />
-  <C value="711" />
-  <D value="0.28941" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="711" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="92.273" />
-  <B value="-9299.2" />
-  <C value="-10.097" />
-  <D value="0.0000042786" />
-  <E value="2" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="711" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.303067E+07" />
-  <B value="0.433923" />
-  <C value="0.764504" />
-  <D value="-1.615634" />
-  <E value="0.843055" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="711" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-3419.9" />
-  <B value="1162.6" />
-  <C value="-5.6175" />
-  <D value="0.02291" />
-  <E value="-0.000035065" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="293.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="156160" />
-  <B value="-200.07" />
-  <C value="10.512" />
-  <D value="0.0025015" />
-  <E value="-0.0000010635" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="479.45" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-154380" />
-  <B value="-193.88" />
-  <C value="13.203" />
-  <D value="0.00019348" />
-  <E value="-5.2535E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.29598" />
-  <B value="-426.37" />
-  <C value="-103.51" />
-  <D value="-35570" />
-  <E value="-7294.6" />
-  <Tmin units="K"  value="355.5" />
-  <Tmax units="K"  value="1877" />
-  </SecondVirialCoefficient>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.6835E-07" />
-  <B value="0.47111" />
-  <C value="397.83" />
-  <D value="9327.5" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.057046" />
-  <B value="-181.52" />
-  <C value="-0.63312" />
-  <D value="-0.0038758" />
-  <E value="-8.2839E-07" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="479.45" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00009568" />
-  <B value="1.0268" />
-  <C value="701.49" />
-  <D value="-31051" />
-  <Tmin units="K"  value="458" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.046165" />
-  <B value="-77.721" />
-  <C value="-1.5311" />
-  <D value="-0.0027248" />
-  <E value="9.8161E-07" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="711" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-89608" />
-  <B value="1020.3" />
-  <C value="-0.836" />
-  <D value="0.00026368" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.171" />
-  <B value="3944.4" />
-  <C value="-70.171" />
-  <Tmin units="K"  value="438.79" />
-  <Tmax units="K"  value="620.26" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.419809" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.292766E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="339.0997" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259776" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="145.5" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0578" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.97849" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.32769" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.133656" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.104812" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.552" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.32769" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17790.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.133656" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="7"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="8"  value="1" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2177-47-1" />
-<Smiles name="SMILES"  value="C1=CC=C2C(=C1)C=C(C2)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="316" />
-<CompoundID name="Name"  value="Dicyclopentadiene" />
-<StructureFormula name="Structure"  value="C10H12" />
-<Family name="Family"  value="14" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="660" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3060000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.445" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="443" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="305.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="305.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="566.19" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="132.202" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.134736" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.288011" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.981E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17800" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08146" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.3E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.961E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.75E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="240000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2090000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.00701" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.535E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.4692" />
-  <B value="-0.0037207" />
-  <Tmin units="K"  value="122.06" />
-  <Tmax units="K"  value="307" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.41899" />
-  <B value="0.20539" />
-  <C value="660" />
-  <D value="0.34053" />
-  <Tmin units="K"  value="299.82" />
-  <Tmax units="K"  value="641.32" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="72.31496" />
-  <B value="-7292.827" />
-  <C value="-7.388294" />
-  <D value="3.746895E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="243.37" />
-  <Tmax units="K"  value="660" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.0543E+07" />
-  <B value="1.9867" />
-  <C value="-4.6545" />
-  <D value="5.1772" />
-  <E value="-2.0831" />
-  <Tmin units="K"  value="215.37" />
-  <Tmax units="K"  value="641.32" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5863.1" />
-  <B value="689.22" />
-  <C value="-1.2292" />
-  <D value="0.0028409" />
-  <E value="-0.0000028796" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="305.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83937" />
-  <B value="-392.22" />
-  <C value="13.886" />
-  <D value="-0.0031138" />
-  <E value="0.000003368" />
-  <Tmin units="K"  value="226.76" />
-  <Tmax units="K"  value="443.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="38735" />
-  <B value="-535.99" />
-  <C value="13.553" />
-  <D value="-0.00031277" />
-  <E value="0.0000001075" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30263" />
-  <B value="-423.69" />
-  <C value="-80.39" />
-  <D value="-8399.9" />
-  <E value="-29911" />
-  <Tmin units="K"  value="330" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.633" />
-  <B value="1272.8" />
-  <C value="0.067676" />
-  <D value="-1.2999E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="210" />
-  <Tmax units="K"  value="443" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000004337" />
-  <B value="0.561" />
-  <C value="232.6" />
-  <D value="-0.00081701" />
-  <Tmin units="K"  value="305.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.029848" />
-  <B value="47.178" />
-  <C value="-2.5363" />
-  <D value="0.0023572" />
-  <E value="-0.0000058893" />
-  <Tmin units="K"  value="215.37" />
-  <Tmax units="K"  value="443" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00025878" />
-  <B value="0.8604" />
-  <C value="51.14" />
-  <D value="244020" />
-  <Tmin units="K"  value="443" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0036707" />
-  <B value="-111.23" />
-  <C value="-2.5419" />
-  <D value="0.0011565" />
-  <E value="-0.0000087684" />
-  <Tmin units="K"  value="289.37" />
-  <Tmax units="K"  value="641.32" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-93645" />
-  <B value="1047.4" />
-  <C value="-0.74596" />
-  <D value="0.00019876" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.716" />
-  <B value="3463.4" />
-  <C value="-65.612" />
-  <Tmin units="K"  value="397.37" />
-  <Tmax units="K"  value="593.37" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0484" />
-  <B value="-0.038478" />
-  <C value="0.000039089" />
-  <Tmin units="K"  value="210" />
-  <Tmax units="K"  value="443" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.47426" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.592001E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="284.7627" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.42" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0577" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.99181" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2851" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.138585" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8156" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.548" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.285111" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17445.1" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.138585" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="3"  value="4" />
-  <group id="6"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="2" />
-  <group id="3"  value="4" />
-  <group id="6"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="2" />
-  <group id="3"  value="4" />
-  <group id="6"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="2" />
-  <group id="3"  value="4" />
-  <group id="6"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="6"  value="2" />
-  <group id="78"  value="2" />
-  <group id="79"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="77-73-6" />
-<Smiles name="SMILES"  value="C1=CC2C(C3)C=CC3C2C1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="518" />
-<CompoundID name="Name"  value="N-butylbenzene" />
-<StructureFormula name="Structure"  value="(C6H5)(CH2)3CH3" />
-<Family name="Family"  value="16" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="660.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2890000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.497" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.262" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="456.42" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="185.3" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="185.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000154386" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.221" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15678" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.393" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.849E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17510" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.23E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0902" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.147E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.314E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.454E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="439490" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.122E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.218" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5644E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.915" />
-  <B value="-0.0053456" />
-  <Tmin units="K"  value="74.12" />
-  <Tmax units="K"  value="185.3" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50648" />
-  <B value="0.25203" />
-  <C value="660.5" />
-  <D value="0.29203" />
-  <Tmin units="K"  value="183.15" />
-  <Tmax units="K"  value="660.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="100.11" />
-  <B value="-9186.6" />
-  <C value="-11.379" />
-  <D value="0.0000058585" />
-  <E value="2" />
-  <Tmin units="K"  value="185.3" />
-  <Tmax units="K"  value="660.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.5698E+07" />
-  <B value="0.30842" />
-  <C value="0.67062" />
-  <D value="-1.1135" />
-  <E value="0.53276" />
-  <Tmin units="K"  value="185.3" />
-  <Tmax units="K"  value="660.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18859" />
-  <B value="1942.8" />
-  <C value="-11.998" />
-  <D value="0.0352" />
-  <E value="-0.0000012248" />
-  <Tmin units="K"  value="15.46" />
-  <Tmax units="K"  value="176.91" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="173590" />
-  <B value="115.14" />
-  <C value="7.4501" />
-  <D value="0.014631" />
-  <E value="-0.000011875" />
-  <Tmin units="K"  value="185.3" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97423" />
-  <B value="-619.62" />
-  <C value="13.35" />
-  <D value="-0.000032816" />
-  <E value="-9.3502E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28148" />
-  <B value="-399.22" />
-  <C value="-98.306" />
-  <D value="-38470" />
-  <E value="66230" />
-  <Tmin units="K"  value="330" />
-  <Tmax units="K"  value="1815" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-18.829" />
-  <B value="1737.7" />
-  <C value="1.0385" />
-  <D value="0.0000015468" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="456.46" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.4687E-07" />
-  <B value="0.59512" />
-  <C value="233.67" />
-  <D value="177.63" />
-  <Tmin units="K"  value="185.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.081204" />
-  <B value="245.71" />
-  <C value="-5.5946" />
-  <D value="0.01322" />
-  <E value="-0.00002506" />
-  <Tmin units="K"  value="185.3" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.19225" />
-  <B value="-0.0011093" />
-  <C value="-156.74" />
-  <D value="1712400" />
-  <Tmin units="K"  value="456.46" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0077709" />
-  <B value="39.218" />
-  <C value="-3.1402" />
-  <D value="0.00039689" />
-  <E value="-0.0000047539" />
-  <Tmin units="K"  value="185.3" />
-  <Tmax units="K"  value="660.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="53961" />
-  <B value="158.64" />
-  <C value="1.3025" />
-  <D value="-0.0018341" />
-  <E value="7.3891E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.151" />
-  <B value="3770" />
-  <C value="-64.789" />
-  <Tmin units="K"  value="400.04" />
-  <Tmax units="K"  value="585.47" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.5752" />
-  <B value="-0.047333" />
-  <C value="0.000051973" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="456.46" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.49211" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.374551E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="347.2727" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.3181" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.064" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.863174" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3921" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.156494" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.946" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.588" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005215" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.7426" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3923" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17450.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.156494" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="10"  value="5" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="9"  value="5" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="104-51-8" />
-<Smiles name="SMILES"  value="c1(CCCC)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="152" />
-<CompoundID name="Name"  value="N-butylcyclohexane" />
-<StructureFormula name="Structure"  value="(C6H11)CH2CH2CH2CH3" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="667" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2570000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.534" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.247" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="454.131" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="198.42" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="198.42" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00365804" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="140.266" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.176266" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.274326" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.831E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16400" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10115" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.292E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.1317E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.654E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="458480" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.416E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0128" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.0902E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.8228" />
-  <B value="-0.0043849" />
-  <Tmin units="K"  value="79.37" />
-  <Tmax units="K"  value="198.42" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.49786" />
-  <B value="0.26572" />
-  <C value="667" />
-  <D value="0.30254" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="642.34" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.702" />
-  <B value="-8417.7" />
-  <C value="-8.6968" />
-  <D value="0.0000027713" />
-  <E value="2" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="667" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.7656E+07" />
-  <B value="1.637" />
-  <C value="-3.3269" />
-  <D value="3.6698" />
-  <E value="-1.48" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="642.34" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18810" />
-  <B value="1861.7" />
-  <C value="-9.714" />
-  <D value="0.029711" />
-  <E value="-0.000021893" />
-  <Tmin units="K"  value="19.69" />
-  <Tmax units="K"  value="182.77" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="117850" />
-  <B value="44.861" />
-  <C value="10.356" />
-  <D value="0.0053947" />
-  <E value="-0.0000020204" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="667" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="145450" />
-  <B value="-890.37" />
-  <C value="14.241" />
-  <D value="-0.0007098" />
-  <E value="2.1101E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30987" />
-  <B value="-371.48" />
-  <C value="-115.93" />
-  <D value="-59916" />
-  <E value="103120" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="1834" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-66.15115" />
-  <B value="3536.438" />
-  <C value="8.46644" />
-  <D value="-7.612217E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="533.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.6992E-07" />
-  <B value="0.52089" />
-  <C value="326.29" />
-  <D value="-3328.7" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.040753" />
-  <B value="3.9448" />
-  <C value="-1.6588" />
-  <D value="-0.00045987" />
-  <E value="-0.0000010215" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="454.43" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000063509" />
-  <B value="1.1032" />
-  <C value="470.22" />
-  <D value="42922" />
-  <Tmin units="K"  value="454.13" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0078825" />
-  <B value="39.221" />
-  <C value="-3.1848" />
-  <D value="0.00024234" />
-  <E value="-0.0000043706" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="642.34" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-60324.92" />
-  <B value="1061.481" />
-  <C value="-0.587852" />
-  <D value="0.000112386" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.259" />
-  <B value="3153.7" />
-  <C value="-92.942" />
-  <Tmin units="K"  value="406.1" />
-  <Tmax units="K"  value="593.01" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="3.0207" />
-  <B value="-0.046654" />
-  <C value="0.000047972" />
-  <Tmin units="K"  value="198.42" />
-  <Tmax units="K"  value="533.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.56133" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.106917E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="283.6273" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="205.2" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0704" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.801447" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.42513" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.176266" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.7432" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.396" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.028388" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3618" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16411.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.176266" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="12"  value="1" />
-  <group id="13"  value="5" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="78"  value="5" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1678-93-9" />
-<Smiles name="SMILES"  value="C1CCCCC1CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="56" />
-<CompoundID name="Name"  value="N-decane" />
-<StructureFormula name="Structure"  value="CH3(CH2)8CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="617.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2110000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.624" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="447.3" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="243.51" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="243.51" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.39297" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.285" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.19595" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.491" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.148E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15720" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1092" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.504E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.4946E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.318E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="545700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.871E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2407" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.29422E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.8978" />
-  <B value="-0.0024599" />
-  <Tmin units="K"  value="193.15" />
-  <Tmax units="K"  value="243.51" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.37424" />
-  <B value="0.2405" />
-  <C value="617.7" />
-  <D value="0.27182" />
-  <Tmin units="K"  value="243.51" />
-  <Tmax units="K"  value="617.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="6.023802" />
-  <B value="-5713.196" />
-  <C value="3.410225" />
-  <D value="-0.000012633" />
-  <E value="2" />
-  <Tmin units="K"  value="243.51" />
-  <Tmax units="K"  value="617.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.7689E+07" />
-  <B value="-1.1412" />
-  <C value="5.1463" />
-  <D value="-6.2946" />
-  <E value="2.6623" />
-  <Tmin units="K"  value="243.51" />
-  <Tmax units="K"  value="617.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-31951" />
-  <B value="2362.8" />
-  <C value="-10.206" />
-  <D value="0.015203" />
-  <E value="0.000023859" />
-  <Tmin units="K"  value="19.93" />
-  <Tmax units="K"  value="243.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="160660" />
-  <B value="291.43" />
-  <C value="8.5687" />
-  <D value="0.0098408" />
-  <E value="-0.0000060811" />
-  <Tmin units="K"  value="242.3" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="152020" />
-  <B value="-697.29" />
-  <C value="13.714" />
-  <D value="-0.00021747" />
-  <E value="4.9426E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.42912" />
-  <B value="-507.47" />
-  <C value="-102.75" />
-  <D value="-147160" />
-  <E value="373570" />
-  <Tmin units="K"  value="309.23" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-102.98" />
-  <B value="4517.9" />
-  <C value="14.495" />
-  <D value="-0.00002056" />
-  <E value="2" />
-  <Tmin units="K"  value="240.05" />
-  <Tmax units="K"  value="494.16" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.3638E-08" />
-  <B value="0.95886" />
-  <C value="24.698" />
-  <D value="7541.9" />
-  <Tmin units="K"  value="243.51" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.071684" />
-  <B value="-217.03" />
-  <C value="-0.47424" />
-  <D value="-0.0039028" />
-  <E value="-0.0000049442" />
-  <Tmin units="K"  value="243.15" />
-  <Tmax units="K"  value="447.3" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-668.49" />
-  <B value="0.93224" />
-  <C value="-4.0687E+09" />
-  <D value="-1.0176E+09" />
-  <Tmin units="K"  value="447.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0051431" />
-  <B value="154.8" />
-  <C value="-4.4562" />
-  <D value="0.0041164" />
-  <E value="-0.0000095358" />
-  <Tmin units="K"  value="243.51" />
-  <Tmax units="K"  value="617.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="111970" />
-  <B value="34.414" />
-  <C value="1.9229" />
-  <D value="-0.002534" />
-  <E value="9.9524E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.4825" />
-  <B value="-1000" />
-  <C value="-6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.985" />
-  <B value="3507.8" />
-  <C value="-76.505" />
-  <Tmin units="K"  value="375.01" />
-  <Tmax units="K"  value="538.92" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.056572" />
-  <B value="-0.032506" />
-  <C value="0.000029737" />
-  <Tmin units="K"  value="240.05" />
-  <Tmax units="K"  value="494.16" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.61922" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.179973E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="298.7822" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2503" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.82" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.34943" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0756" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.732721" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.4916" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.195806" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.2" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.02" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.003324" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.7327" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.4869" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15791.26" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.196" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="8" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="8" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="8" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="8" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="8" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="8" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="124-18-5" />
-<Smiles name="SMILES"  value="CCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="702" />
-<CompoundID name="Name"  value="1-methylnaphthalene" />
-<StructureFormula name="Structure"  value="(C6H4)(C4H3)CH3" />
-<Family name="Family"  value="19" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="772" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3600000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.462" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="517.84" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="242.67" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="242.67" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.043382" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.2" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13937" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.348" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.435E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19890" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.7E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08511" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.169E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.179E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="377400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6945000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.96548" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5958E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.4144" />
-  <B value="-0.0042867" />
-  <Tmin units="K"  value="97.07" />
-  <Tmax units="K"  value="242.67" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.59739" />
-  <B value="0.26468" />
-  <C value="772" />
-  <D value="0.2918" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="753.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="73.89852" />
-  <B value="-9115.529" />
-  <C value="-7.252019" />
-  <D value="2.094885E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="772.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.0001E+07" />
-  <B value="0.3382" />
-  <C value="0.060354" />
-  <D value="-0.021035" />
-  <E value="-0.0086978" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="772.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10175" />
-  <B value="1369.3" />
-  <C value="-8.8231" />
-  <D value="0.038851" />
-  <E value="-0.000058806" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="240.81" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="134210" />
-  <B value="116.27" />
-  <C value="8.3119" />
-  <D value="0.012175" />
-  <E value="-0.000010378" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="67134" />
-  <B value="-530.75" />
-  <C value="13.222" />
-  <D value="-0.000033319" />
-  <E value="-3.2916E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15567" />
-  <B value="-253.83" />
-  <C value="-196.1" />
-  <D value="-31135" />
-  <E value="-111130" />
-  <Tmin units="K"  value="340" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="8.170859" />
-  <B value="1169.912" />
-  <C value="-3.261889" />
-  <D value="6.874562E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="517.83" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.4606E-07" />
-  <B value="0.6456" />
-  <C value="239.2" />
-  <D value="-8656.8" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.049867" />
-  <B value="2.2749" />
-  <C value="-1.45" />
-  <D value="-0.00045282" />
-  <E value="-7.0729E-07" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="517.83" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1.5229" />
-  <B value="-0.35024" />
-  <C value="-1389.7" />
-  <D value="2465100" />
-  <Tmin units="K"  value="517.83" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013368" />
-  <B value="52.546" />
-  <C value="-2.9174" />
-  <D value="0.00019752" />
-  <E value="-0.0000028051" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="744.14" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-46869" />
-  <B value="820.01" />
-  <C value="-0.41207" />
-  <D value="-0.000085888" />
-  <E value="1.0651E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.512" />
-  <B value="4531" />
-  <C value="-63.887" />
-  <Tmin units="K"  value="464" />
-  <Tmax units="K"  value="693.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="6.0924" />
-  <B value="-0.056774" />
-  <C value="0.000057342" />
-  <Tmin units="K"  value="242.67" />
-  <Tmax units="K"  value="517.83" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.465187" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.297362E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="389.4123" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="161.4" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.37108" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0623" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.0232" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3337" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1398" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.610415" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.936" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.056699" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.77801" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3337" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20129.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1398" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="7" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="7" />
-  <group id="10"  value="2" />
-  <group id="11"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="7" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="7"  value="7" />
-  <group id="8"  value="3" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="7" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="7" />
-  <group id="10"  value="2" />
-  <group id="11"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="90-12-0" />
-<Smiles name="SMILES"  value="c1(C)cccc2ccccc21" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="703" />
-<CompoundID name="Name"  value="2-methylnaphthalene" />
-<StructureFormula name="Structure"  value="(C6H4)(C4H3)CH3" />
-<Family name="Family"  value="19" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="761" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3540000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.462" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.258" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="514.2" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="307.73" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="307.73" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="18.6897" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.2" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14577" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.374" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.426E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19680" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.4E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08511" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.161E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.163E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.212E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.00411" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.58286E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9663" />
-  <B value="-0.0049976" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="307.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53405" />
-  <B value="0.25024" />
-  <C value="761.16" />
-  <D value="0.28587" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="761.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="98.05854" />
-  <B value="-10275.56" />
-  <C value="-10.82814" />
-  <D value="3.919145E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="307.73" />
-  <Tmax units="K"  value="761.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.0724E+07" />
-  <B value="1.2004" />
-  <C value="-1.1581" />
-  <D value="0.47852" />
-  <E value="-0.081108" />
-  <Tmin units="K"  value="307.73" />
-  <Tmax units="K"  value="761.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-4930.5" />
-  <B value="1192.6" />
-  <C value="-5.4492" />
-  <D value="0.016185" />
-  <E value="-0.000012597" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="307.73" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="74335" />
-  <B value="-307.25" />
-  <C value="13.46" />
-  <D value="-0.0028051" />
-  <E value="0.000003645" />
-  <Tmin units="K"  value="307.73" />
-  <Tmax units="K"  value="514.26" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="69292" />
-  <B value="-534.4" />
-  <C value="13.21" />
-  <D value="-0.00001663" />
-  <E value="-8.8386E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22212" />
-  <B value="-342.38" />
-  <C value="-170.61" />
-  <D value="-97471" />
-  <E value="108730" />
-  <Tmin units="K"  value="340" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-88.346" />
-  <B value="4977.8" />
-  <C value="11.629" />
-  <D value="-0.0000078261" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="608.8" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000029847" />
-  <B value="0.34183" />
-  <C value="891.22" />
-  <D value="-28677" />
-  <Tmin units="K"  value="307.73" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0084839" />
-  <B value="-307.37" />
-  <C value="0.18174" />
-  <D value="-0.0046509" />
-  <E value="0.0000016652" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="514.26" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000098384" />
-  <B value="1.0234" />
-  <C value="722.6" />
-  <D value="42453" />
-  <Tmin units="K"  value="514.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.042844" />
-  <B value="-52.703" />
-  <C value="-1.7419" />
-  <D value="-0.0021776" />
-  <E value="5.2767E-07" />
-  <Tmin units="K"  value="307.73" />
-  <Tmax units="K"  value="737.14" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-38837" />
-  <B value="780.58" />
-  <C value="-0.36035" />
-  <D value="-0.00011067" />
-  <E value="0.0000001095" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.535" />
-  <B value="3740.1" />
-  <C value="-99.198" />
-  <Tmin units="K"  value="460.76" />
-  <Tmax units="K"  value="673.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.90585" />
-  <B value="-0.032061" />
-  <C value="0.00002781" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="608.8" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.465187" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.331317E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="378.5547" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="161.4" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0624" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.0073" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3815" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.143396" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.610415" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.936" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000472" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3815" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19870.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.143396" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="7" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="7" />
-  <group id="10"  value="2" />
-  <group id="11"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="7" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="7"  value="7" />
-  <group id="8"  value="3" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="7" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="7" />
-  <group id="10"  value="2" />
-  <group id="11"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="91-57-6" />
-<Smiles name="SMILES"  value="c1c(C)ccc2ccccc21" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="63" />
-<CompoundID name="Name"  value="N-undecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)9CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="639" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1980000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.689" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="469.08" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="247.571" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="247.571" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.408414" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="156.312" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.21224" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.538" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.496E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15880" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1194" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.639E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.7043E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.116E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="584930" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.218E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3766" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.9036E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.2757" />
-  <B value="-0.0028242" />
-  <Tmin units="K"  value="99.03" />
-  <Tmax units="K"  value="247.57" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.36785" />
-  <B value="0.24938" />
-  <C value="639" />
-  <D value="0.28395" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="639" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="128.8551" />
-  <B value="-11029.21" />
-  <C value="-15.54009" />
-  <D value="8.030888E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="639" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.9735E+07" />
-  <B value="0.81788" />
-  <C value="0.31647" />
-  <D value="-1.4781" />
-  <E value="0.80673" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="639" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-39053" />
-  <B value="2684.8" />
-  <C value="-12.418" />
-  <D value="0.023835" />
-  <E value="0.000012675" />
-  <Tmin units="K"  value="28.87" />
-  <Tmax units="K"  value="214.07" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="208030" />
-  <B value="521.1" />
-  <C value="6.1551" />
-  <D value="0.017086" />
-  <E value="-0.000013175" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="433.42" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="177700" />
-  <B value="-730.83" />
-  <C value="13.81" />
-  <D value="-0.00021088" />
-  <E value="5.7776E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.60629" />
-  <B value="-760.54" />
-  <C value="-75.703" />
-  <D value="-307370" />
-  <E value="805010" />
-  <Tmin units="K"  value="319" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-92.575" />
-  <B value="4408.9" />
-  <C value="12.698" />
-  <D value="-0.000015556" />
-  <E value="2" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="511.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.9213E-08" />
-  <B value="0.9335" />
-  <C value="118.62" />
-  <D value="-4363.8" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.015185" />
-  <B value="-212.29" />
-  <C value="-0.044539" />
-  <D value="-0.0049614" />
-  <E value="0.0000013629" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="469.08" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.037608" />
-  <B value="0.6852" />
-  <C value="33443" />
-  <D value="9124600" />
-  <Tmin units="K"  value="469.08" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.099094" />
-  <B value="-34.281" />
-  <C value="-1.5565" />
-  <D value="-0.0016817" />
-  <E value="9.0654E-07" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="639" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-11238.22" />
-  <B value="1067.841" />
-  <C value="-0.600948" />
-  <D value="0.000132394" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.4825" />
-  <B value="-1000" />
-  <C value="-6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.005" />
-  <B value="3654.7" />
-  <C value="-83.504" />
-  <Tmin units="K"  value="384.11" />
-  <Tmax units="K"  value="556.59" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.80609" />
-  <B value="-0.035059" />
-  <C value="0.00003251" />
-  <Tmin units="K"  value="247.57" />
-  <Tmax units="K"  value="511.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.684519" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.41521E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="313.4536" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.243351" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="230.34" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.98384" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0825" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.742846" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.5349" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.212215" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.871799" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.556" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.012698" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.1446" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.521" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15934.45" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2122" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="9" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="9" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="9" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="9" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="9" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="9" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1120-21-4" />
-<Smiles name="SMILES"  value="CCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="808" />
-<CompoundID name="Name"  value="Acenaphthene" />
-<StructureFormula name="Structure"  value="C12H10" />
-<Family name="Family"  value="20" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="803.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3100000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.553" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="550.54" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="366.56" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="366.56" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="199.997" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="154.208" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.149792" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.381147" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.468E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19480" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.5E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0909799" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.9E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.55E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.602E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="368900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.1462E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.0014E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.7696" />
-  <B value="-0.0028899" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="366.56" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.39942" />
-  <B value="0.22066" />
-  <C value="803.15" />
-  <D value="0.24043" />
-  <Tmin units="K"  value="366.56" />
-  <Tmax units="K"  value="803.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="73.737" />
-  <B value="-9735.5" />
-  <C value="-7.1321" />
-  <D value="0.0000016079" />
-  <E value="2" />
-  <Tmin units="K"  value="363.15" />
-  <Tmax units="K"  value="803.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.785978E+08" />
-  <B value="10.14483" />
-  <C value="-25.41937" />
-  <D value="26.03775" />
-  <E value="-9.982155" />
-  <Tmin units="K"  value="366.56" />
-  <Tmax units="K"  value="803.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="2546" />
-  <B value="828.81" />
-  <C value="-2.4427" />
-  <D value="0.0073064" />
-  <E value="-0.0000044872" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="366.56" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="173930" />
-  <B value="379.65" />
-  <C value="5.6292" />
-  <D value="0.017939" />
-  <E value="-0.000013551" />
-  <Tmin units="K"  value="366.56" />
-  <Tmax units="K"  value="550.54" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="60762" />
-  <B value="-515.4" />
-  <C value="13.307" />
-  <D value="-0.000026823" />
-  <E value="-1.013E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.53731" />
-  <B value="401.04" />
-  <C value="-321.41" />
-  <D value="-48048" />
-  <E value="-100110" />
-  <Tmin units="K"  value="260" />
-  <Tmax units="K"  value="800" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.2073" />
-  <B value="1373.2" />
-  <C value="-0.25871" />
-  <D value="-0.0000036859" />
-  <E value="2" />
-  <Tmin units="K"  value="366.56" />
-  <Tmax units="K"  value="550.54" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000015547" />
-  <B value="0.4064" />
-  <C value="630.11" />
-  <D value="26.274" />
-  <Tmin units="K"  value="550.54" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.059552" />
-  <B value="-91.592" />
-  <C value="-1.7169" />
-  <D value="-0.0019056" />
-  <E value="1.2951E-07" />
-  <Tmin units="K"  value="366.56" />
-  <Tmax units="K"  value="550.54" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000078027" />
-  <B value="1.0286" />
-  <C value="593.39" />
-  <D value="37622" />
-  <Tmin units="K"  value="550.54" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0090914" />
-  <B value="266.35" />
-  <C value="-4.4764" />
-  <D value="0.0037262" />
-  <E value="-0.00000553" />
-  <Tmin units="K"  value="366.56" />
-  <Tmax units="K"  value="803.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-54576" />
-  <B value="908.74" />
-  <C value="-0.58719" />
-  <D value="0.00014077" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.25834" />
-  <B value="-1500" />
-  <C value="-9" />
-  <Tmin units="K"  value="275.2611" />
-  <Tmax units="K"  value="445.2611" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.212" />
-  <B value="4475.2" />
-  <C value="-88.378" />
-  <Tmin units="K"  value="483.15" />
-  <Tmax units="K"  value="711.24" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.07954" />
-  <B value="-0.022051" />
-  <C value="0.000012441" />
-  <Tmin units="K"  value="366.56" />
-  <Tmax units="K"  value="550.54" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.500752" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.820483E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="393.9754" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.257114" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="177.3" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0645" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.08499" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.382" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.149792" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.997356" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.96" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.382" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19480.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.149792" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="6" />
-  <group id="11"  value="2" />
-  <group id="13"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="6" />
-  <group id="10"  value="2" />
-  <group id="12"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="2" />
-  <group id="10"  value="6" />
-  <group id="11"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="2"  value="2" />
-  <group id="7"  value="6" />
-  <group id="8"  value="4" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="6" />
-  <group id="11"  value="2" />
-  <group id="13"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="6" />
-  <group id="10"  value="2" />
-  <group id="12"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="83-32-9" />
-<Smiles name="SMILES"  value="C12=CC=CC3=C1C(=CC=C3)CC2" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="558" />
-<CompoundID name="Name"  value="Biphenyl" />
-<StructureFormula name="Structure"  value="(C6H5)2" />
-<Family name="Family"  value="21" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="789.26" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3847270" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.491118" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.294" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="528.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="342.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="342.372" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="84.2725" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="154.211" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.155536" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.3643" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.834E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19383" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0916799" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.066E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.82088E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.80077E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="392668" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.85769E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.08574" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.0317E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.53" />
-  <B value="8.742E-09" />
-  <Tmin units="K"  value="342.2" />
-  <Tmax units="K"  value="351.7" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50803" />
-  <B value="0.25417" />
-  <C value="789.26" />
-  <D value="0.2795" />
-  <Tmin units="K"  value="342.37" />
-  <Tmax units="K"  value="789.26" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="154.3401" />
-  <B value="-13555.42" />
-  <C value="-19.05582" />
-  <D value="8.30386E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="342.37" />
-  <Tmax units="K"  value="789.26" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.680865E+07" />
-  <B value="0.473092" />
-  <C value="1.061004" />
-  <D value="-2.226343" />
-  <E value="1.156876" />
-  <Tmin units="K"  value="342.37" />
-  <Tmax units="K"  value="789.26" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="221670" />
-  <B value="-2517.1" />
-  <C value="16.838" />
-  <D value="-0.039851" />
-  <E value="0.000036033" />
-  <Tmin units="K"  value="185" />
-  <Tmax units="K"  value="342.2" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="24132" />
-  <B value="-12.395" />
-  <C value="11.585" />
-  <D value="0.0029407" />
-  <E value="-0.0000014331" />
-  <Tmin units="K"  value="342.2" />
-  <Tmax units="K"  value="623.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="79583" />
-  <B value="-635.84" />
-  <C value="13.574" />
-  <D value="-0.00034935" />
-  <E value="9.291E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26138" />
-  <B value="-245.47" />
-  <C value="-216.33" />
-  <D value="-240010" />
-  <E value="501010" />
-  <Tmin units="K"  value="395" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.998" />
-  <B value="1574.4" />
-  <C value="-0.022671" />
-  <D value="-3.4058E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="373.15" />
-  <Tmax units="K"  value="723.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7776E-07" />
-  <B value="0.70632" />
-  <C value="118.6" />
-  <D value="61798" />
-  <Tmin units="K"  value="373.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.086277" />
-  <B value="-343.48" />
-  <C value="0.36261" />
-  <D value="-0.00791" />
-  <E value="0.0000032504" />
-  <Tmin units="K"  value="357.65" />
-  <Tmax units="K"  value="528" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000031971" />
-  <B value="1.1528" />
-  <C value="215.14" />
-  <D value="115000" />
-  <Tmin units="K"  value="373.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0069524" />
-  <B value="142.55" />
-  <C value="-3.829" />
-  <D value="0.0025886" />
-  <E value="-0.0000054473" />
-  <Tmin units="K"  value="342.37" />
-  <Tmax units="K"  value="789.26" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-7009.1" />
-  <B value="510.44" />
-  <C value="0.52814" />
-  <D value="-0.0011436" />
-  <E value="5.1292E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.881" />
-  <B value="4024.6" />
-  <C value="-97.95" />
-  <Tmin units="K"  value="474.02" />
-  <Tmax units="K"  value="707.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.8372" />
-  <B value="-0.017826" />
-  <C value="0.000010734" />
-  <Tmin units="K"  value="373.15" />
-  <Tmax units="K"  value="723.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.48899" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.396712E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="628.324" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="177.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.068" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.619296" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.36329" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.155536" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0434" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.24" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.000398" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3643" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19383" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.155536" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="10" />
-  <group id="11"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="10" />
-  <group id="10"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="10" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="10" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="10" />
-  <group id="11"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="10" />
-  <group id="10"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="92-52-4" />
-<Smiles name="SMILES"  value="c1ccccc1(c2ccccc2)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="64" />
-<CompoundID name="Name"  value="N-dodecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)10CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="658" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1820000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.754" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="489.48" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="263.568" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="263.568" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.615203" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="170.338" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.22859" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.571" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.914E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15930" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1296" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.774E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.9072E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.981E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="624150" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3.684E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3026" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-7.51368E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="5.7375" />
-  <B value="-0.0024301" />
-  <Tmin units="K"  value="105.43" />
-  <Tmax units="K"  value="263.57" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.30334" />
-  <B value="0.23617" />
-  <C value="658" />
-  <D value="0.2706" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="658" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="127.8877" />
-  <B value="-11582.12" />
-  <C value="-15.22541" />
-  <D value="6.680034E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="263.57" />
-  <Tmax units="K"  value="658.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.812979E+07" />
-  <B value="0.939672" />
-  <C value="-0.0412509" />
-  <D value="-0.949322" />
-  <E value="0.501567" />
-  <Tmin units="K"  value="263.57" />
-  <Tmax units="K"  value="658" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-40692" />
-  <B value="2827.2" />
-  <C value="-13.076" />
-  <D value="0.027179" />
-  <E value="0.0000013665" />
-  <Tmin units="K"  value="29.97" />
-  <Tmax units="K"  value="258.41" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="203950" />
-  <B value="627.31" />
-  <C value="6.2796" />
-  <D value="0.014676" />
-  <E value="-0.0000079758" />
-  <Tmin units="K"  value="263.57" />
-  <Tmax units="K"  value="433.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="193680" />
-  <B value="-732.61" />
-  <C value="13.902" />
-  <D value="-0.00022284" />
-  <E value="6.2257E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.89899" />
-  <B value="-1118.5" />
-  <C value="-43.998" />
-  <D value="-559660" />
-  <E value="1526700" />
-  <Tmin units="K"  value="329" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-83.21108" />
-  <B value="4238.311" />
-  <C value="11.14639" />
-  <D value="-0.0000124656" />
-  <E value="2" />
-  <Tmin units="K"  value="262.15" />
-  <Tmax units="K"  value="526.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.4481E-08" />
-  <B value="0.85223" />
-  <C value="245.71" />
-  <D value="-11928" />
-  <Tmin units="K"  value="263.57" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.029364" />
-  <B value="-108.04" />
-  <C value="-0.7007" />
-  <D value="-0.0040791" />
-  <E value="6.1377E-07" />
-  <Tmin units="K"  value="263.44" />
-  <Tmax units="K"  value="489.47" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000055504" />
-  <B value="1.4726" />
-  <C value="558.15" />
-  <D value="3563.6" />
-  <Tmin units="K"  value="489.47" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0049404" />
-  <B value="162.06" />
-  <C value="-4.4354" />
-  <D value="0.0037865" />
-  <E value="-0.0000084256" />
-  <Tmin units="K"  value="263.57" />
-  <Tmax units="K"  value="658" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="143250" />
-  <B value="-60.213" />
-  <C value="2.6541" />
-  <D value="-0.0035189" />
-  <E value="0.0000014153" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.4825" />
-  <B value="-1000" />
-  <C value="-6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.859" />
-  <B value="3663.7" />
-  <C value="-96.745" />
-  <Tmin units="K"  value="399.53" />
-  <Tmax units="K"  value="574.96" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.30944" />
-  <B value="-0.030368" />
-  <C value="0.000024892" />
-  <Tmin units="K"  value="262.15" />
-  <Tmax units="K"  value="526.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.75581" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.921276E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="296.4588" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2466" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="250.86" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.00586" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0894" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.751145" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.58069" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.228633" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="8.5462" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="7.096" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001931" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.18518" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.561" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16036.72" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2286" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="10" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="10" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="10" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="10" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="10" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="10" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="112-40-3" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="738" />
-<CompoundID name="Name"  value="Fluorene" />
-<StructureFormula name="Structure"  value="(C6H4)CH2(C6H4)" />
-<Family name="Family"  value="20" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="826" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.524" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.229" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="570.44" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="387.94" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="387.94" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="281.665" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="166.219" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15327" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.404163" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.806E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19820" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.3E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09367" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.019E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.869E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.901E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="381500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.9578E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95089" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.4251E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.2313" />
-  <B value="-2.9598E-09" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="302.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.43683" />
-  <B value="0.229" />
-  <C value="826" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="826" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="141.8746" />
-  <B value="-13833.84" />
-  <C value="-17.04805" />
-  <D value="0.0000063782" />
-  <E value="2" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="870" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.581E+07" />
-  <B value="1.317" />
-  <C value="-1.4739" />
-  <D value="-0.0034969" />
-  <E value="0.61586" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="826" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="181.01" />
-  <B value="986.6" />
-  <C value="-3.6964" />
-  <D value="0.012043" />
-  <E value="-0.000010424" />
-  <Tmin units="K"  value="98.37" />
-  <Tmax units="K"  value="387.94" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="172320" />
-  <B value="813.11" />
-  <C value="3.2969" />
-  <D value="0.023275" />
-  <E value="-0.000018014" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="57825" />
-  <B value="-560.42" />
-  <C value="13.575" />
-  <D value="-0.00027161" />
-  <E value="7.5804E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-1.7303" />
-  <B value="1592" />
-  <C value="-617.99" />
-  <D value="-13420" />
-  <E value="-481950" />
-  <Tmin units="K"  value="260" />
-  <Tmax units="K"  value="800" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-33.053" />
-  <B value="2454.9" />
-  <C value="3.4575" />
-  <D value="-0.0000042581" />
-  <E value="2" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="570.44" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.7084E-07" />
-  <B value="0.56204" />
-  <C value="373.69" />
-  <D value="-49.196" />
-  <Tmin units="K"  value="570.44" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.013258" />
-  <B value="-130.68" />
-  <C value="-0.68476" />
-  <D value="-0.0022566" />
-  <E value="3.0043E-07" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="570.44" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00017437" />
-  <B value="0.9152" />
-  <C value="500.25" />
-  <D value="62613" />
-  <Tmin units="K"  value="570.44" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0067753" />
-  <B value="569.69" />
-  <C value="-6.1981" />
-  <D value="0.007814" />
-  <E value="-0.000008755" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="826" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-79598" />
-  <B value="1036.6" />
-  <C value="-0.70705" />
-  <D value="0.00017819" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.876" />
-  <B value="4244" />
-  <C value="-116.23" />
-  <Tmin units="K"  value="503.15" />
-  <Tmax units="K"  value="733.78" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.1567" />
-  <B value="-0.019014" />
-  <C value="0.000011754" />
-  <Tmin units="K"  value="387.94" />
-  <Tmax units="K"  value="570.44" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.517307" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.821711E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="267.486" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="193.2" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="1.5595" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0696" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.29618" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.349259" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.128237" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.174687" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.076" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-3.571" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.349259" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21645.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.128237" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="8" />
-  <group id="11"  value="3" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="8" />
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="1" />
-  <group id="10"  value="8" />
-  <group id="11"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="8" />
-  <group id="8"  value="4" />
-  <group id="10"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="8" />
-  <group id="11"  value="3" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="8" />
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="86-73-7" />
-<Smiles name="SMILES"  value="C1=CC=CC2=C1C(C=CC=C3)=C3C2" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="65" />
-<CompoundID name="Name"  value="N-tridecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)11CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="675" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1680000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.823" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.246" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="508.63" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="267.76" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="267.76" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.250959" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="184.365" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.24494" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.61" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.198E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16060" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1398" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.909E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.1177E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.771E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="663370" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.85E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3955" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.1229E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="5.0333" />
-  <B value="-0.00042229" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="267.76" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.29787" />
-  <B value="0.24164" />
-  <C value="675" />
-  <D value="0.29254" />
-  <Tmin units="K"  value="267.76" />
-  <Tmax units="K"  value="675" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="143.3256" />
-  <B value="-12766.72" />
-  <C value="-17.45421" />
-  <D value="7.99709E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="267.76" />
-  <Tmax units="K"  value="675" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.732822E+07" />
-  <B value="0.667983" />
-  <C value="0.462399" />
-  <D value="-1.329972" />
-  <E value="0.649193" />
-  <Tmin units="K"  value="267.76" />
-  <Tmax units="K"  value="675" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-30593" />
-  <B value="2351.8" />
-  <C value="-3.2425" />
-  <D value="-0.035182" />
-  <E value="0.00013219" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="255" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="37167" />
-  <B value="123.48" />
-  <C value="11.52" />
-  <D value="0.0033147" />
-  <E value="-0.0000011194" />
-  <Tmin units="K"  value="267.76" />
-  <Tmax units="K"  value="508.62" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="191240" />
-  <B value="-657.52" />
-  <C value="13.861" />
-  <D value="-0.00011498" />
-  <E value="3.3409E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34822" />
-  <B value="-309.7" />
-  <C value="-296.34" />
-  <D value="-20030" />
-  <E value="-158270" />
-  <Tmin units="K"  value="337.5" />
-  <Tmax units="K"  value="1858" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-81.45907" />
-  <B value="4309.552" />
-  <C value="10.81921" />
-  <D value="-0.000011395" />
-  <E value="2" />
-  <Tmin units="K"  value="267.67" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.0146E-08" />
-  <B value="0.91936" />
-  <C value="136.12" />
-  <D value="2279.8" />
-  <Tmin units="K"  value="267.76" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.037294" />
-  <B value="-193.16" />
-  <C value="-0.1108" />
-  <D value="-0.0058295" />
-  <E value="0.0000022551" />
-  <Tmin units="K"  value="267.76" />
-  <Tmax units="K"  value="508.62" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000050471" />
-  <B value="1.4806" />
-  <C value="553.99" />
-  <D value="7554.4" />
-  <Tmin units="K"  value="508.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.090941" />
-  <B value="-41.14" />
-  <C value="-1.5711" />
-  <D value="-0.0017455" />
-  <E value="8.9906E-07" />
-  <Tmin units="K"  value="267.76" />
-  <Tmax units="K"  value="675" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="154200" />
-  <B value="-63.489" />
-  <C value="2.8771" />
-  <D value="-0.0038228" />
-  <E value="0.0000015389" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.322" />
-  <B value="4115.8" />
-  <C value="-88" />
-  <Tmin units="K"  value="410.76" />
-  <Tmax units="K"  value="605.76" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0999" />
-  <B value="-0.033761" />
-  <C value="0.000029279" />
-  <Tmin units="K"  value="267.67" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.83173" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="9.409996E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="282.8677" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2465" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="271.38" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.20131" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0972" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.758814" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.634" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.244445" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="9.2206" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="7.636" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.42096" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.6002" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16139" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2449" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="11" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="11" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="11" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="11" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="11" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="11" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-50-5" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="805" />
-<CompoundID name="Name"  value="Phenanthrene" />
-<StructureFormula name="Structure"  value="C14H10" />
-<Family name="Family"  value="20" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="869" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2900000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.554" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.222" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="610.03" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="372.38" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="372.38" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="29.2781" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="178.229" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.167077" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.470716" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.961E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19910" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09956" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.084E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.012E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.0219E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="394500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.6463E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.4497" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.8282E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.1455" />
-  <B value="-0.0018632" />
-  <Tmin units="K"  value="292.61" />
-  <Tmax units="K"  value="372.38" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.4558" />
-  <B value="0.25237" />
-  <C value="869" />
-  <D value="0.24848" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="869" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="275.0593" />
-  <B value="-20918.1" />
-  <C value="-36.87097" />
-  <D value="0.0000193212" />
-  <E value="2" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="869" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.2455E+07" />
-  <B value="0.28979" />
-  <C value="1.1393" />
-  <D value="-1.9946" />
-  <E value="0.92537" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="869" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-2147.6" />
-  <B value="1126" />
-  <C value="-5.164" />
-  <D value="0.018832" />
-  <E value="-0.000019443" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="300.18" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115950" />
-  <B value="-43.82" />
-  <C value="10.979" />
-  <D value="0.0042773" />
-  <E value="-0.0000023928" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66200" />
-  <B value="-509.49" />
-  <C value="13.435" />
-  <D value="-0.000075274" />
-  <E value="6.0366E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.5297" />
-  <B value="-840.06" />
-  <C value="-298.35" />
-  <D value="228040" />
-  <E value="-2652600" />
-  <Tmin units="K"  value="434.62" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-22.439" />
-  <B value="2565.4" />
-  <C value="1.5699" />
-  <D value="3.8655E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="610.03" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000004717" />
-  <B value="0.52643" />
-  <C value="268.46" />
-  <D value="10947" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11683" />
-  <B value="-580.68" />
-  <C value="-0.62222" />
-  <D value="-0.006256" />
-  <E value="4.1638E-07" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="610.03" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000092871" />
-  <B value="0.99317" />
-  <C value="671.87" />
-  <D value="29972" />
-  <Tmin units="K"  value="610.03" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035674" />
-  <B value="5.5102" />
-  <C value="-2.2869" />
-  <D value="-0.00066502" />
-  <E value="-6.3839E-07" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="869" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-62288" />
-  <B value="1031.8" />
-  <C value="-0.68956" />
-  <D value="0.00017028" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.518" />
-  <B value="6374.5" />
-  <C value="-31.508" />
-  <Tmin units="K"  value="521.65" />
-  <Tmax units="K"  value="764.45" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.0724" />
-  <B value="-0.027036" />
-  <C value="0.000019559" />
-  <Tmin units="K"  value="372.38" />
-  <Tmax units="K"  value="610.03" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.554142" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="9.328059E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="251.6539" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.249255" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.1" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.0273" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0735" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.11841" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.54" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.167078" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.562953" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.336" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.3356" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.54" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20142.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.167078" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="10" />
-  <group id="11"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="10" />
-  <group id="10"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="10" />
-  <group id="11"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="10" />
-  <group id="8"  value="4" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="10" />
-  <group id="11"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="10" />
-  <group id="10"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="85-01-8" />
-<Smiles name="SMILES"  value="C1=CC2=C(C=C1)C1=C(C=CC=C1)C=C2" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="66" />
-<CompoundID name="Name"  value="N-tetradecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)12CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="693" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1570000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.894" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="526.76" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="279.01" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="279.01" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.252685" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="198.392" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.26132" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.644" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.427E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1501" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.044E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.3244E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.599E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="702590" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4.507E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.4596" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.73282E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="4.6071" />
-  <B value="-1.9678E-17" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.26297" />
-  <B value="0.23695" />
-  <C value="693" />
-  <D value="0.26861" />
-  <Tmin units="K"  value="279.01" />
-  <Tmax units="K"  value="693" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="141.7696" />
-  <B value="-13265.67" />
-  <C value="-17.07041" />
-  <D value="6.905252E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="279.01" />
-  <Tmax units="K"  value="693" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.216371E+08" />
-  <B value="1.28014" />
-  <C value="-0.352636" />
-  <D value="-1.241735" />
-  <E value="0.826459" />
-  <Tmin units="K"  value="279.01" />
-  <Tmax units="K"  value="693" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-49970" />
-  <B value="3309.6" />
-  <C value="-15.927" />
-  <D value="0.037566" />
-  <E value="-0.000014829" />
-  <Tmin units="K"  value="29.98" />
-  <Tmax units="K"  value="279.02" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84257" />
-  <B value="110.32" />
-  <C value="11.507" />
-  <D value="0.0033723" />
-  <E value="-0.0000011739" />
-  <Tmin units="K"  value="279.01" />
-  <Tmax units="K"  value="526.73" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="204940" />
-  <B value="-657.01" />
-  <C value="13.943" />
-  <D value="-0.00013248" />
-  <E value="4.0902E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.3799" />
-  <B value="-326.59" />
-  <C value="-350.35" />
-  <D value="-74172" />
-  <E value="-110230" />
-  <Tmin units="K"  value="346.5" />
-  <Tmax units="K"  value="1913" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-84.61448" />
-  <B value="4567.43" />
-  <C value="11.25434" />
-  <D value="-0.0000111579" />
-  <E value="2" />
-  <Tmin units="K"  value="277.65" />
-  <Tmax units="K"  value="554.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.4874E-09" />
-  <B value="1.2039" />
-  <C value="-69.467" />
-  <D value="11809" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.039135" />
-  <B value="-208.63" />
-  <C value="-0.066493" />
-  <D value="-0.005844" />
-  <E value="0.0000021711" />
-  <Tmin units="K"  value="279.01" />
-  <Tmax units="K"  value="526.73" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-122.4" />
-  <B value="0.86814" />
-  <C value="-5.5021E+08" />
-  <D value="-2.1347E+10" />
-  <Tmin units="K"  value="526.73" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0044248" />
-  <B value="172.78" />
-  <C value="-4.4693" />
-  <D value="0.0037172" />
-  <E value="-0.0000079542" />
-  <Tmin units="K"  value="279.01" />
-  <Tmax units="K"  value="693" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="152780" />
-  <B value="54.751" />
-  <C value="2.6862" />
-  <D value="-0.0035472" />
-  <E value="0.0000013794" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.35" />
-  <B value="4247.1" />
-  <C value="-94.486" />
-  <Tmin units="K"  value="419.9" />
-  <Tmax units="K"  value="605.84" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.95817" />
-  <B value="-0.030978" />
-  <C value="0.000024066" />
-  <Tmin units="K"  value="277.65" />
-  <Tmax units="K"  value="554.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.90219" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="9.768391E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="282.0005" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.234049" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="291.9" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.50737" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.103" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.762913" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.68207" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.261791" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="9.895" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="8.176001" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.010085" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.4459" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.6399" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16200.36" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2613" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="12" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="12" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="12" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="12" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="12" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="12" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-59-4" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="67" />
-<CompoundID name="Name"  value="N-pentadecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)13CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="708" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1480000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.966" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.243" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="543.83" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="283.072" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="283.072" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.128872" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="212.419" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.27771" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.685" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="6.729E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16210" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1603" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.179E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.5311E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.426E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="741810" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3.459E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.48184" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-9.34237E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="4.3" />
-  <B value="8.5322E-17" />
-  <Tmin units="K"  value="283.07" />
-  <Tmax units="K"  value="292.57" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.26611" />
-  <B value="0.24483" />
-  <C value="708" />
-  <D value="0.29579" />
-  <Tmin units="K"  value="283.07" />
-  <Tmax units="K"  value="685.64" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="105.7905" />
-  <B value="-12176.19" />
-  <C value="-11.51031" />
-  <D value="2.157424E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="283.07" />
-  <Tmax units="K"  value="708" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.334182E+08" />
-  <B value="1.382258" />
-  <C value="-0.345375" />
-  <D value="-1.508041" />
-  <E value="0.995233" />
-  <Tmin units="K"  value="283.07" />
-  <Tmax units="K"  value="685.64" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-31815" />
-  <B value="2469.2" />
-  <C value="-1.2562" />
-  <D value="-0.049055" />
-  <E value="0.0001557" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="270.9" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="44888" />
-  <B value="73.977" />
-  <C value="11.979" />
-  <D value="0.0027483" />
-  <E value="-9.4622E-07" />
-  <Tmin units="K"  value="283.07" />
-  <Tmax units="K"  value="543.84" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="218790" />
-  <B value="-655.87" />
-  <C value="14.013" />
-  <D value="-0.00013811" />
-  <E value="4.3573E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.37154" />
-  <B value="-266.84" />
-  <C value="-432.43" />
-  <D value="-95870" />
-  <E value="-140270" />
-  <Tmin units="K"  value="353" />
-  <Tmax units="K"  value="1938" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-91.37005" />
-  <B value="4965.801" />
-  <C value="12.24551" />
-  <D value="-0.0000115231" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="543.84" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.2252E-08" />
-  <B value="0.90575" />
-  <C value="168.22" />
-  <D value="3233.4" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.010742" />
-  <B value="-152.75" />
-  <C value="-0.43594" />
-  <D value="-0.0040245" />
-  <E value="0.0000012373" />
-  <Tmin units="K"  value="283.07" />
-  <Tmax units="K"  value="543.84" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000047787" />
-  <B value="1.4851" />
-  <C value="642.9" />
-  <D value="182.7" />
-  <Tmin units="K"  value="543.84" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.070366" />
-  <B value="-47.05" />
-  <C value="-1.6737" />
-  <D value="-0.0019561" />
-  <E value="9.2369E-07" />
-  <Tmin units="K"  value="283.07" />
-  <Tmax units="K"  value="685.64" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="176100" />
-  <B value="-70.041" />
-  <C value="3.3232" />
-  <D value="-0.0044308" />
-  <E value="0.0000017861" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.805" />
-  <B value="4671.3" />
-  <C value="-88.708" />
-  <Tmin units="K"  value="434.49" />
-  <Tmax units="K"  value="633.1" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.8636" />
-  <B value="-0.035377" />
-  <C value="0.000030301" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="543.84" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.97724" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.007341E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="283.8762" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.245" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="312.42" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.11" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.770405" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.72539" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.277673" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="10.5694" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="8.716001" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.033625" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.6743" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16282.18" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2778" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="13" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="13" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="13" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="13" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="13" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="13" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-62-9" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="717" />
-<CompoundID name="Name"  value="Fluoranthene" />
-<StructureFormula name="Structure"  value="C16H10" />
-<Family name="Family"  value="20" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="905" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2610000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.655" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.227" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="655.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="383.33" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="383.33" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="15.7016" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="202.251" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.184362" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.587526" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.357E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19290" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.6E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10904" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.126E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.889E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.862E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="418500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.873E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.4356" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-7.695E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.1853" />
-  <B value="-3.0518E-09" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="307.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.34656" />
-  <B value="0.22699" />
-  <C value="905" />
-  <D value="0.28508" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="905" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="96.11781" />
-  <B value="-12362.08" />
-  <C value="-10.3511" />
-  <D value="0.0000032319" />
-  <E value="2" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="905" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.442678E+08" />
-  <B value="2.403711" />
-  <C value="-3.376173" />
-  <D value="1.404001" />
-  <E value="0.0327511" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="905" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="10497" />
-  <B value="781.34" />
-  <C value="-1.5505" />
-  <D value="0.0075603" />
-  <E value="-0.0000095863" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="383.33" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="241580" />
-  <B value="1296.9" />
-  <C value="0.78013" />
-  <D value="0.023496" />
-  <E value="-0.000011773" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="59938" />
-  <B value="-461.32" />
-  <C value="13.513" />
-  <D value="-0.00005781" />
-  <E value="-5.6701E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-2.6301" />
-  <B value="2731" />
-  <C value="-1234.5" />
-  <D value="-125480" />
-  <E value="-2369300" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="800" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-68.502" />
-  <B value="5208.9" />
-  <C value="8.4007" />
-  <D value="-0.0000042979" />
-  <E value="2" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="655.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010875" />
-  <B value="0.41309" />
-  <C value="444.51" />
-  <D value="-25.424" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.045864" />
-  <B value="-83.397" />
-  <C value="-0.96049" />
-  <D value="-0.0013219" />
-  <E value="-5.1355E-10" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="655.95" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00011776" />
-  <B value="0.94788" />
-  <C value="660.84" />
-  <D value="38292" />
-  <Tmin units="K"  value="655.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0081035" />
-  <B value="309.57" />
-  <C value="-4.4853" />
-  <D value="0.0031868" />
-  <E value="-0.0000043723" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="905" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-68523" />
-  <B value="1184.2" />
-  <C value="-0.82804" />
-  <D value="0.00021044" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.781" />
-  <B value="7232" />
-  <C value="-13.315" />
-  <Tmin units="K"  value="543.15" />
-  <Tmax units="K"  value="795.17" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.8909" />
-  <B value="-0.030333" />
-  <C value="0.000021268" />
-  <Tmin units="K"  value="383.33" />
-  <Tmax units="K"  value="655.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.615194" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="9.603459E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="283.9585" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.239005" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="222.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.4092" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0815" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.16484" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.5" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.184693" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.187871" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.504" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.5027" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.5" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19277.2" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.184693" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="10" />
-  <group id="11"  value="6" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="10" />
-  <group id="10"  value="6" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="10" />
-  <group id="11"  value="6" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="10" />
-  <group id="11"  value="6" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="10" />
-  <group id="10"  value="6" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="206-44-0" />
-<Smiles name="SMILES"  value="C1=CC2=C(C=C1)C1=CC=CC3=C1C2=CC=C3" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="807" />
-<CompoundID name="Name"  value="Pyrene" />
-<StructureFormula name="Structure"  value="C16H10" />
-<Family name="Family"  value="20" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="936" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2610000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.66" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.221" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="667.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="423.81" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="423.81" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="70.0313" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="202.251" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.184923" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.507416" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.152E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19670" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10904" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.126E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.25E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.272E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="402000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.736E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.4078" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-7.63094E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.2841" />
-  <B value="7.4227E-17" />
-  <Tmin units="K"  value="295.85" />
-  <Tmax units="K"  value="305.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54272" />
-  <B value="0.27165" />
-  <C value="936" />
-  <D value="0.41522" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="909.04" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="68.91405" />
-  <B value="-11628.85" />
-  <C value="-6.184331" />
-  <D value="6.420723E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="423.81" />
-  <Tmax units="K"  value="936" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.198843E+07" />
-  <B value="-0.224752" />
-  <C value="1.989996" />
-  <D value="-2.139885" />
-  <E value="0.666532" />
-  <Tmin units="K"  value="423.81" />
-  <Tmax units="K"  value="909.04" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34428" />
-  <B value="193.16" />
-  <C value="2.988" />
-  <D value="-0.0075382" />
-  <E value="0.0000090005" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="423.81" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="149400" />
-  <B value="-94.468" />
-  <C value="11.128" />
-  <D value="0.0038746" />
-  <E value="-0.0000019128" />
-  <Tmin units="K"  value="423.81" />
-  <Tmax units="K"  value="600" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="117680" />
-  <B value="-754.3" />
-  <C value="14.068" />
-  <D value="-0.00069165" />
-  <E value="2.0484E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.50411" />
-  <B value="-846.36" />
-  <C value="-528.72" />
-  <D value="-815460" />
-  <E value="-79126" />
-  <Tmin units="K"  value="468" />
-  <Tmax units="K"  value="1731" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-131.9" />
-  <B value="8597.1" />
-  <C value="17.746" />
-  <D value="-0.000010523" />
-  <E value="2" />
-  <Tmin units="K"  value="423.35" />
-  <Tmax units="K"  value="667.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.4284E-07" />
-  <B value="0.52754" />
-  <C value="289.9" />
-  <D value="15025" />
-  <Tmin units="K"  value="423.81" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10165" />
-  <B value="-731.42" />
-  <C value="0.75712" />
-  <D value="-0.0079846" />
-  <E value="0.0000028317" />
-  <Tmin units="K"  value="288.65" />
-  <Tmax units="K"  value="550" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000092503" />
-  <B value="0.97453" />
-  <C value="647.35" />
-  <D value="45503" />
-  <Tmin units="K"  value="667.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.007329" />
-  <B value="346.59" />
-  <C value="-4.6696" />
-  <D value="0.0036569" />
-  <E value="-0.0000046813" />
-  <Tmin units="K"  value="423.81" />
-  <Tmax units="K"  value="909.04" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-33015" />
-  <B value="969.84" />
-  <C value="-0.55466" />
-  <D value="0.00011137" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.723" />
-  <B value="6010.1" />
-  <C value="-76.729" />
-  <Tmin units="K"  value="573.15" />
-  <Tmax units="K"  value="833.56" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="2.0317" />
-  <B value="-0.026367" />
-  <C value="0.000016432" />
-  <Tmin units="K"  value="423.35" />
-  <Tmax units="K"  value="667.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.615194" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="9.942347E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="266.6866" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.246034" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="222.6" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.4079" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0807" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.27404" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.507416" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.17368" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.187871" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.504" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.1204" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.344" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20762.5" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.17368" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="10" />
-  <group id="11"  value="6" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="10" />
-  <group id="10"  value="6" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="10" />
-  <group id="11"  value="6" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="10" />
-  <group id="11"  value="6" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="10" />
-  <group id="10"  value="6" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="129-00-0" />
-<Smiles name="SMILES"  value="C1=CC2=C3C(=C1)C=CC1=CC=CC(=C31)C=C2" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="710" />
-<CompoundID name="Name"  value="1-phenylnaphthalene" />
-<StructureFormula name="Structure"  value="(C6H4)(C4H3)(C6H5)" />
-<Family name="Family"  value="19" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="849" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2630000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.656" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="607.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="318.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="318.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.282425" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="204.266" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.189925" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.530878" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.641E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19910" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1165" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.296E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.47E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.71108E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="459000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-7.92E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="5.3654" />
-  <B value="-3.9158E-09" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="302.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.36822" />
-  <B value="0.24155" />
-  <C value="849" />
-  <D value="0.29048" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="849" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="136.2471" />
-  <B value="-14614.66" />
-  <C value="-16.02104" />
-  <D value="5.425361E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="849" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.0967E+08" />
-  <B value="1.3201" />
-  <C value="-2.3901" />
-  <D value="2.4598" />
-  <E value="-0.96728" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="849" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5568.7" />
-  <B value="1416" />
-  <C value="-6.3534" />
-  <D value="0.022718" />
-  <E value="-0.000029424" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="318.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="180260" />
-  <B value="-2.5213" />
-  <C value="10.037" />
-  <D value="0.0072742" />
-  <E value="-0.0000049656" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="607.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="77509" />
-  <B value="-521.03" />
-  <C value="13.602" />
-  <D value="-0.000094316" />
-  <E value="9.2363E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.47323" />
-  <B value="-716.5" />
-  <C value="-343.69" />
-  <D value="-698990" />
-  <E value="1354800" />
-  <Tmin units="K"  value="424.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-6.144" />
-  <B value="1205.6" />
-  <C value="-0.56682" />
-  <D value="-0.0000005706" />
-  <E value="2" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="678.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000030793" />
-  <B value="0.30949" />
-  <C value="742.15" />
-  <D value="16342" />
-  <Tmin units="K"  value="607.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.052282" />
-  <B value="-21.251" />
-  <C value="-1.3126" />
-  <D value="-0.00073663" />
-  <E value="-3.6032E-07" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="607.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000092251" />
-  <B value="0.99676" />
-  <C value="619.05" />
-  <D value="42835" />
-  <Tmin units="K"  value="607.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0092731" />
-  <B value="179.4" />
-  <C value="-3.7906" />
-  <D value="0.0020974" />
-  <E value="-0.0000040352" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="849" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-76343" />
-  <B value="1203.5" />
-  <C value="-0.80842" />
-  <D value="0.00020016" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.23" />
-  <B value="4746.4" />
-  <C value="-118.29" />
-  <Tmin units="K"  value="513.73" />
-  <Tmax units="K"  value="742.83" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-0.84135" />
-  <B value="-0.019285" />
-  <C value="0.000012308" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="678.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.664833" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.810728E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="345.4811" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="227.22" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0865" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.097" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.530878" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.189925" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.679631" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.184" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.530878" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19911.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.189925" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="12" />
-  <group id="11"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="12" />
-  <group id="10"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="12" />
-  <group id="11"  value="4" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="12" />
-  <group id="11"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="12" />
-  <group id="10"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="605-02-7" />
-<Smiles name="SMILES"  value="c1(c2ccccc2)cccc2ccccc21" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="68" />
-<CompoundID name="Name"  value="N-hexadecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)14CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="723" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.034" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.241" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="559.98" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="291.308" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="291.308" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0922432" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="226.446" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.29411" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.726" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="7.063E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16190" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1706" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.314E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.7417E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="8.216E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="781020" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5.3358E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.5924" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-9.95145E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="5.1175" />
-  <B value="-0.0038943" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="291.32" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.23237" />
-  <B value="0.23642" />
-  <C value="723" />
-  <D value="0.28403" />
-  <Tmin units="K"  value="291.31" />
-  <Tmax units="K"  value="723" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="138.0173" />
-  <B value="-14151.1" />
-  <C value="-16.24379" />
-  <D value="5.027608E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="288.95" />
-  <Tmax units="K"  value="723" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.2775E+08" />
-  <B value="0.92612" />
-  <C value="0.52583" />
-  <D value="-2.1415" />
-  <E value="1.2039" />
-  <Tmin units="K"  value="291.31" />
-  <Tmax units="K"  value="723" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-53303" />
-  <B value="3589.2" />
-  <C value="-16.544" />
-  <D value="0.037386" />
-  <E value="-0.000012242" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="291.33" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="387360" />
-  <B value="-123.61" />
-  <C value="10.738" />
-  <D value="0.005" />
-  <E value="-0.0000019617" />
-  <Tmin units="K"  value="291.31" />
-  <Tmax units="K"  value="560.01" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="232700" />
-  <B value="-655.34" />
-  <C value="14.079" />
-  <D value="-0.0001451" />
-  <E value="4.6597E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.50464" />
-  <B value="-439.04" />
-  <C value="-445.03" />
-  <D value="-345290" />
-  <E value="480120" />
-  <Tmin units="K"  value="361" />
-  <Tmax units="K"  value="1981" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-84.70059" />
-  <B value="4841.907" />
-  <C value="11.15158" />
-  <D value="-9.617336E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="278.15" />
-  <Tmax units="K"  value="564.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.3203E-07" />
-  <B value="0.72722" />
-  <C value="424.3" />
-  <D value="4562.7" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.006807" />
-  <B value="-152.97" />
-  <C value="-0.44096" />
-  <D value="-0.0038892" />
-  <E value="0.0000012245" />
-  <Tmin units="K"  value="291.31" />
-  <Tmax units="K"  value="560.01" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000035961" />
-  <B value="1.5118" />
-  <C value="510.88" />
-  <D value="23814" />
-  <Tmin units="K"  value="560.01" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0036644" />
-  <B value="220.16" />
-  <C value="-4.8209" />
-  <D value="0.0045419" />
-  <E value="-0.0000084745" />
-  <Tmin units="K"  value="291.31" />
-  <Tmax units="K"  value="723" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="417.3407" />
-  <B value="1457.374" />
-  <C value="-0.708733" />
-  <D value="0.0000535634" />
-  <E value="4.151662E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.891" />
-  <B value="4049.7" />
-  <C value="-127.22" />
-  <Tmin units="K"  value="438.29" />
-  <Tmax units="K"  value="632.12" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.725" />
-  <B value="-0.033627" />
-  <C value="0.000027668" />
-  <Tmin units="K"  value="278.15" />
-  <Tmax units="K"  value="564.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.067071" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.040714E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="281.3927" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.226854" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="332.94" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.64299" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.116" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.775481" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.74714" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.294064" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="11.24" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="9.26" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002741" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.5125" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.7078" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16343.54" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2941" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="14" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="14" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="14" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="14" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="14" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="14" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="544-76-3" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="806" />
-<CompoundID name="Name"  value="Chrysene" />
-<StructureFormula name="Structure"  value="C18H12" />
-<Family name="Family"  value="20" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="979" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2390000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.749" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.22" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="714.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="531.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="531.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1028.09" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="228.288" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.223221" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.603008" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.74E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18920" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.33E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.12516" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.326E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.698E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.03E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="440000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.62E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.6796E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="5.6375" />
-  <B value="-4.596E-09" />
-  <Tmin units="K"  value="389.35" />
-  <Tmax units="K"  value="398.85" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.30846" />
-  <B value="0.21991" />
-  <C value="979" />
-  <D value="0.32162" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="979" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="171.0845" />
-  <B value="-19845.5" />
-  <C value="-20.41887" />
-  <D value="4.689312E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="531.15" />
-  <Tmax units="K"  value="979" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.2779E+08" />
-  <B value="0.96651" />
-  <C value="-1.3609" />
-  <D value="1.2985" />
-  <E value="-0.49651" />
-  <Tmin units="K"  value="531.15" />
-  <Tmax units="K"  value="979" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="13800" />
-  <B value="1090" />
-  <C value="-0.4" />
-  <D value="6.6062E-09" />
-  <E value="-6.1574E-12" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="531.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="314190" />
-  <B value="239.97" />
-  <C value="9.0147" />
-  <D value="0.0068894" />
-  <E value="-0.0000035685" />
-  <Tmin units="K"  value="531.15" />
-  <Tmax units="K"  value="714.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="124010" />
-  <B value="-668.94" />
-  <C value="14.001" />
-  <D value="-0.0004632" />
-  <E value="1.3177E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.58487" />
-  <B value="-948.55" />
-  <C value="-766.23" />
-  <D value="-2021000" />
-  <E value="1913400" />
-  <Tmin units="K"  value="489.5" />
-  <Tmax units="K"  value="1809.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.612" />
-  <B value="2823.3" />
-  <C value="-0.058693" />
-  <D value="2.8981E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="588.75" />
-  <Tmax units="K"  value="714.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.4146E-07" />
-  <B value="0.54263" />
-  <C value="230.08" />
-  <D value="-3.8758" />
-  <Tmin units="K"  value="531.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.032525" />
-  <B value="-322.45" />
-  <C value="-0.056163" />
-  <D value="-0.0034819" />
-  <E value="4.4935E-07" />
-  <Tmin units="K"  value="531.15" />
-  <Tmax units="K"  value="714.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0001111" />
-  <B value="0.947" />
-  <C value="689.64" />
-  <D value="45041" />
-  <Tmin units="K"  value="714.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0048828" />
-  <B value="1479.4" />
-  <C value="-10.166" />
-  <D value="0.012571" />
-  <E value="-0.0000093954" />
-  <Tmin units="K"  value="531.15" />
-  <Tmax units="K"  value="979" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-68216" />
-  <B value="1261.7" />
-  <C value="-0.82371" />
-  <D value="0.00019855" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.413" />
-  <B value="5704.7" />
-  <C value="-137.81" />
-  <Tmin units="K"  value="598.33" />
-  <Tmax units="K"  value="867.04" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="0.19518" />
-  <B value="-0.020395" />
-  <C value="0.000010474" />
-  <Tmin units="K"  value="588.75" />
-  <Tmax units="K"  value="714.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.724274" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.042713E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="274.4211" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.237646" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="259.02" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0932" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.27729" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.603954" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.210334" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="8.250494" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.304" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.603954" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19486.9" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.210334" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="12" />
-  <group id="11"  value="6" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="12" />
-  <group id="10"  value="6" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="12" />
-  <group id="11"  value="6" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="12" />
-  <group id="8"  value="6" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="12" />
-  <group id="11"  value="6" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="12" />
-  <group id="10"  value="6" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="218-01-9" />
-<Smiles name="SMILES"  value="C1=CC2=C(C=C1)C=CC1=C2C=CC2=C1C=CC=C2" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="153" />
-<CompoundID name="Name"  value="Cis-decahydronaphthalene" />
-<StructureFormula name="Structure"  value="(CH2)4CHCH(CH2)4" />
-<Family name="Family"  value="8" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="702.25" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3242400" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.48" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="468.965" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="230.17" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="230.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.157166" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="138.253" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.154615" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.294204" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.206E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17625.3" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09426" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.137E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.6924E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="8.552E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="377730" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9489000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93532" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.89213E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.97" />
-  <B value="-8.742E-09" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="239.7" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.5563" />
-  <B value="0.26613" />
-  <C value="702.25" />
-  <D value="0.2872" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="702.25" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="133.51" />
-  <B value="-10671" />
-  <C value="-16.446" />
-  <D value="0.0000090618" />
-  <E value="2" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="702.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.893812E+07" />
-  <B value="1.120046" />
-  <C value="-0.590284" />
-  <D value="-0.648808" />
-  <E value="0.601197" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="702.25" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5463.3" />
-  <B value="610.38" />
-  <C value="3.7884" />
-  <D value="-0.041328" />
-  <E value="0.00011576" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="220" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="22875" />
-  <B value="183.22" />
-  <C value="9.7191" />
-  <D value="0.0080113" />
-  <E value="-0.0000053261" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="600" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="90923" />
-  <B value="-788.66" />
-  <C value="14.021" />
-  <D value="-0.00046171" />
-  <E value="0.0000001235" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.037954" />
-  <B value="-145.9" />
-  <C value="-175.13" />
-  <D value="-52628" />
-  <E value="40101" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="693.15" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-102.87" />
-  <B value="5387.9" />
-  <C value="14.086" />
-  <D value="-0.000014127" />
-  <E value="2" />
-  <Tmin units="K"  value="243.15" />
-  <Tmax units="K"  value="468.96" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.2745E-07" />
-  <B value="0.51364" />
-  <C value="404.18" />
-  <D value="49.274" />
-  <Tmin units="K"  value="468.96" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.087597" />
-  <B value="-101" />
-  <C value="-1.0253" />
-  <D value="-0.0090174" />
-  <E value="0.0000045064" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="468.96" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000017593" />
-  <B value="1.7742" />
-  <C value="317.62" />
-  <D value="37605" />
-  <Tmin units="K"  value="468.96" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0073102" />
-  <B value="159.63" />
-  <C value="-4.1152" />
-  <D value="0.0030369" />
-  <E value="-0.0000064896" />
-  <Tmin units="K"  value="230.2" />
-  <Tmax units="K"  value="702.25" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-45272" />
-  <B value="665.72" />
-  <C value="0.42113" />
-  <D value="-0.00097745" />
-  <E value="4.2304E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.082" />
-  <B value="3127.3" />
-  <C value="-102.92" />
-  <Tmin units="K"  value="424.98" />
-  <Tmax units="K"  value="627.72" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="6.7247" />
-  <B value="-0.061114" />
-  <C value="0.000064934" />
-  <Tmin units="K"  value="243.15" />
-  <Tmax units="K"  value="468.96" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.52096" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.12599E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="395.2259" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.264744" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="200.58" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.23541" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0321597" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.90094" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.294204" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.154615" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.289" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.776" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.00602" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.63311" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.294204" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17625.3" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.154615" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="78"  value="8" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="493-01-6" />
-<Smiles name="SMILES"  value="C1C[C@]2(CCCC[C@]2(CC1)([H]))([H])" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="154" />
-<CompoundID name="Name"  value="Trans-decahydronaphthalene" />
-<StructureFormula name="Structure"  value="(CH2)4CHCH(CH2)4" />
-<Family name="Family"  value="8" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="687.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2837100" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.48" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.238" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="460.46" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="242.77" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="242.79" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.14983" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="138.253" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.159325" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.253611" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.314E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17042.7" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09426" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.137E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.8217E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.355E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="374550" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.441E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.92251" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.88088E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.68" />
-  <B value="-7.1526E-09" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="252.29" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.5599" />
-  <B value="0.26991" />
-  <C value="687.05" />
-  <D value="0.2952" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="687.05" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="112.0059" />
-  <B value="-9619.314" />
-  <C value="-13.21808" />
-  <D value="6.974439E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="687.05" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.646155E+07" />
-  <B value="0.918445" />
-  <C value="0.395142" />
-  <D value="-2.202434" />
-  <E value="1.398354" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="687.05" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="248890" />
-  <B value="-17.544" />
-  <C value="0.10636" />
-  <D value="-0.00028659" />
-  <E value="2.8955E-07" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="252.29" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="110470" />
-  <B value="-81.629" />
-  <C value="10.313" />
-  <D value="0.0068781" />
-  <E value="-0.0000045952" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="460.46" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81351" />
-  <B value="-707.34" />
-  <C value="13.793" />
-  <D value="-0.00018944" />
-  <E value="2.0365E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.02487" />
-  <B value="-133.31" />
-  <C value="-173.25" />
-  <D value="-48380" />
-  <E value="36572" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="673.15" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-47.21" />
-  <B value="3037.9" />
-  <C value="5.4682" />
-  <D value="-0.0000042842" />
-  <E value="2" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="460.46" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.7061E-07" />
-  <B value="0.60485" />
-  <C value="153.09" />
-  <D value="81.09" />
-  <Tmin units="K"  value="460.46" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.087771" />
-  <B value="45.415" />
-  <C value="-2.1613" />
-  <D value="-0.0061939" />
-  <E value="0.0000022159" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="460.46" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-13.928" />
-  <B value="0.65448" />
-  <C value="-2837300" />
-  <D value="-2.043E+09" />
-  <Tmin units="K"  value="460.46" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0072992" />
-  <B value="137.99" />
-  <C value="-3.9696" />
-  <D value="0.0025043" />
-  <E value="-0.0000061602" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="687.05" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-17918" />
-  <B value="447.75" />
-  <C value="1.0485" />
-  <D value="-0.0017445" />
-  <E value="7.5379E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.316" />
-  <B value="3335.5" />
-  <C value="-80.854" />
-  <Tmin units="K"  value="413.15" />
-  <Tmax units="K"  value="616.9" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="3.8573" />
-  <B value="-0.048752" />
-  <C value="0.000050406" />
-  <Tmin units="K"  value="242.79" />
-  <Tmax units="K"  value="460.46" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.52096" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.180246E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="255.6104" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.268306" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="200.58" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.23673" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0652" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.87461" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.253611" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.159325" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.289" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.776" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.011339" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.61125" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.253611" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17042.7" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.159325" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="2"  value="8" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="78"  value="8" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="493-02-7" />
-<Smiles name="SMILES"  value="C1C[C@@]2(CCCC[C@]2(CC1)([H]))([H])" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1405" />
-<CompoundID name="Name"  value="Methyl tert-butyl ether" />
-<StructureFormula name="Structure"  value="CH3OC(CH3)3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="497.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3430000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.329" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="328.35" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="164.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="164.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.535656" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.1482" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.119887" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.266059" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.179E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15070" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.54E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06171" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.08E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.835E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.175E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="357800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7600000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.88771" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.1049E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.4" />
-  <B value="-0.0084317" />
-  <Tmin units="K"  value="65.82" />
-  <Tmax units="K"  value="164.55" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.013" />
-  <B value="0.29119" />
-  <C value="513.95" />
-  <D value="0.39929" />
-  <Tmin units="K"  value="164.55" />
-  <Tmax units="K"  value="513.94" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="63.31041" />
-  <B value="-5322.676" />
-  <C value="-6.212745" />
-  <D value="3.951136E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="164.55" />
-  <Tmax units="K"  value="497.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.685222E+07" />
-  <B value="4.561833" />
-  <C value="-12.06881" />
-  <D value="13.61234" />
-  <E value="-5.569118" />
-  <Tmin units="K"  value="164.55" />
-  <Tmax units="K"  value="497.1" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11840" />
-  <B value="1396" />
-  <C value="-5.8523" />
-  <D value="-0.0092711" />
-  <E value="0.00016154" />
-  <Tmin units="K"  value="11.5" />
-  <Tmax units="K"  value="164.56" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="135550" />
-  <B value="-54.229" />
-  <C value="8.6558" />
-  <D value="0.010329" />
-  <E value="-0.0000078206" />
-  <Tmin units="K"  value="164.55" />
-  <Tmax units="K"  value="328.35" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="89729" />
-  <B value="-682.14" />
-  <C value="12.912" />
-  <D value="0.000021441" />
-  <E value="-2.0192E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18862" />
-  <B value="-199.25" />
-  <C value="-24.367" />
-  <D value="-1558.5" />
-  <E value="1368.5" />
-  <Tmin units="K"  value="248.6" />
-  <Tmax units="K"  value="1809.6" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.136" />
-  <B value="821.59" />
-  <C value="-0.64419" />
-  <D value="4.8322E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="449.93" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.6185E-07" />
-  <B value="0.73614" />
-  <C value="130.03" />
-  <D value="-727.78" />
-  <Tmin units="K"  value="164.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.073008" />
-  <B value="306.73" />
-  <C value="-6.3111" />
-  <D value="0.019235" />
-  <E value="-0.000037933" />
-  <Tmin units="K"  value="164.55" />
-  <Tmax units="K"  value="460.87" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00023034" />
-  <B value="0.92128" />
-  <C value="391.6" />
-  <D value="80274" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.032821" />
-  <B value="-29.327" />
-  <C value="-1.9813" />
-  <D value="-0.0032789" />
-  <E value="0.0000010144" />
-  <Tmin units="K"  value="164.55" />
-  <Tmax units="K"  value="497.1" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="17448" />
-  <B value="439.33" />
-  <C value="-0.18821" />
-  <D value="0.000026432" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.427" />
-  <B value="2381.9" />
-  <C value="-60.58" />
-  <Tmin units="K"  value="299.35" />
-  <Tmax units="K"  value="444.59" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="-1.2431" />
-  <B value="-0.0329" />
-  <C value="0.000034374" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="449.93" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.330153" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.11761E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="303.0697" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267213" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="113.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.07186" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0447" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.745835" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.266059" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.119887" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.0678" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.632" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.956082" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.053074" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.32865" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.266059" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15070" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.119887" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="25"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="24"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1634-04-4" />
-<Smiles name="SMILES"  value="COC(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1427" />
-<CompoundID name="Name"  value="Methyl tert-pentyl ether" />
-<StructureFormula name="Structure"  value="CH3OC(CH3)2CH2CH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="534" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3040000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.386" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="359.51" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.175" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.133437" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.298071" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.465E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15480" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.90339E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07194" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.043E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.054E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.137E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="408000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0449" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.71229E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.1" />
-  <B value="-6.0195E-16" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.68843" />
-  <B value="0.26574" />
-  <C value="534" />
-  <D value="0.27067" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="534" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="127.09" />
-  <B value="-8433.7" />
-  <C value="-15.94" />
-  <D value="0.000013112" />
-  <E value="2" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="534" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.112039E+07" />
-  <B value="2.144847" />
-  <C value="-4.987322" />
-  <D value="5.569725" />
-  <E value="-2.294462" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="534" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="184600" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="96936" />
-  <B value="-844.6" />
-  <C value="17.426" />
-  <D value="-0.01423" />
-  <E value="0.000014683" />
-  <Tmin units="K"  value="267" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86134" />
-  <B value="-503.3" />
-  <C value="12.828" />
-  <D value="0.00026316" />
-  <E value="-9.3404E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24596" />
-  <B value="-275.48" />
-  <C value="-36.668" />
-  <D value="-851.22" />
-  <E value="-5476.3" />
-  <Tmin units="K"  value="267" />
-  <Tmax units="K"  value="1947" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.271" />
-  <B value="991.37" />
-  <C value="-0.019082" />
-  <D value="-2.1664E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="359.51" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.9893E-08" />
-  <B value="0.83491" />
-  <C value="61.227" />
-  <D value="-3034.8" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.10613" />
-  <B value="12.391" />
-  <C value="-1.3082" />
-  <D value="-0.00026248" />
-  <E value="-0.0000013654" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="425" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.12493" />
-  <B value="0.14978" />
-  <C value="1706.4" />
-  <D value="1349200" />
-  <Tmin units="K"  value="359.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0083071" />
-  <B value="83.854" />
-  <C value="-3.8901" />
-  <D value="0.003534" />
-  <E value="-0.000010373" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="534" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="3885.8" />
-  <B value="620.93" />
-  <C value="-0.34528" />
-  <D value="0.000073697" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.355" />
-  <B value="3194.9" />
-  <C value="-35.861" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="534" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="1.2135" />
-  <B value="-0.051268" />
-  <C value="0.000067114" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="359.51" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.387974" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.717114E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="288.555" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.264404" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="133.85" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.84722" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0516" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.77448" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.298071" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.133437" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7422" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.172" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.905443" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.010549" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.7281" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.298071" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15480" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.133437" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="25"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="24"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="994-05-8" />
-<Smiles name="SMILES"  value="COC(C)(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1111" />
-<CompoundID name="Name"  value="2-methyl-2-butanol" />
-<StructureFormula name="Structure"  value="CH3CH2C(CH3)(OH)CH3" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="545" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3790000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.323" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.27" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="375.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="264.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="264.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="161.196" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.15" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1095" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.478" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.359E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20840" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.67E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06261" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.17E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.297E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.652E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="362800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4456000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.78274" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.0391E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.041" />
-  <B value="-0.0051748" />
-  <Tmin units="K"  value="105.74" />
-  <Tmax units="K"  value="264.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.71131" />
-  <B value="0.24603" />
-  <C value="545" />
-  <D value="0.25077" />
-  <Tmin units="K"  value="264.35" />
-  <Tmax units="K"  value="529" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="111.96" />
-  <B value="-9620.4" />
-  <C value="-12.673" />
-  <D value="0.0000022964" />
-  <E value="2" />
-  <Tmin units="K"  value="264.35" />
-  <Tmax units="K"  value="543.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.022286E+08" />
-  <B value="1.245977" />
-  <C value="-0.515176" />
-  <D value="-0.350588" />
-  <E value="0.262112" />
-  <Tmin units="K"  value="264.35" />
-  <Tmax units="K"  value="543.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-3330500" />
-  <B value="79184" />
-  <C value="-676.61" />
-  <D value="2.5428" />
-  <E value="-0.0035268" />
-  <Tmin units="K"  value="152.5" />
-  <Tmax units="K"  value="214.3" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="145240" />
-  <B value="-80.948" />
-  <C value="10.283" />
-  <D value="0.0042992" />
-  <E value="0.0000021924" />
-  <Tmin units="K"  value="264.35" />
-  <Tmax units="K"  value="375.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="74328" />
-  <B value="-529.61" />
-  <C value="12.79" />
-  <D value="0.000073612" />
-  <E value="-9.0525E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2317" />
-  <B value="-245.23" />
-  <C value="-25.84" />
-  <D value="30078" />
-  <E value="-127780" />
-  <Tmin units="K"  value="271.85" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-783.84" />
-  <B value="31606" />
-  <C value="120.39" />
-  <D value="-0.00015466" />
-  <E value="2" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="434.96" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.8945E-07" />
-  <B value="0.71394" />
-  <C value="173.97" />
-  <D value="-1855.4" />
-  <Tmin units="K"  value="264.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.052544" />
-  <B value="-120.78" />
-  <C value="-0.20746" />
-  <D value="-0.0081579" />
-  <E value="0.0000039201" />
-  <Tmin units="K"  value="163.55" />
-  <Tmax units="K"  value="433.55" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1156.2" />
-  <B value="0.93842" />
-  <C value="5.9829E+09" />
-  <D value="-1.5337E+11" />
-  <Tmin units="K"  value="375.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.004975" />
-  <B value="709.64" />
-  <C value="-10.143" />
-  <D value="0.02288" />
-  <E value="-0.000029901" />
-  <Tmin units="K"  value="264.35" />
-  <Tmax units="K"  value="543.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="35603" />
-  <B value="226.55" />
-  <C value="0.55283" />
-  <D value="-0.00088824" />
-  <E value="3.7199E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.923" />
-  <B value="2458.2" />
-  <C value="-113.51" />
-  <Tmin units="K"  value="328.15" />
-  <Tmax units="K"  value="484.89" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="13" />
-  <A value="19.92" />
-  <B value="-0.12833" />
-  <C value="0.0001442" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="434.96" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.335173" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.161351E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="319.315" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248616" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="113.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="3.08387" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0428" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.813536" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.478" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1095" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5972" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.284" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-4.0988" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.478" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20840" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1095" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-85-4" />
-<Smiles name="SMILES"  value="CCC(C)(C)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="904" />
-<CompoundID name="Name"  value="Nitrogen trioxide" />
-<StructureFormula name="Structure"  value="O2NNO" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="451" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6990000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.195" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.386" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="276.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="171.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="172.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="15.1767" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="76.0116" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0531885" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.431227" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.346E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="32600" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.078E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.026378" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.407E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="8.2843E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.39727E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="308450" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-8.2843E+07" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="23.709" />
-  <B value="-0.0033974" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="20.15" />
-  <Tmax units="K"  value="170" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.7664" />
-  <B value="0.37489" />
-  <C value="451" />
-  <D value="0.040027" />
-  <E value="0" />
-  <Tmin units="K"  value="243.15" />
-  <Tmax units="K"  value="275.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="137.96" />
-  <B value="-7584.5" />
-  <C value="-17.9" />
-  <D value="0.000022014" />
-  <E value="2" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="425" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.1243E+07" />
-  <B value="0.17457" />
-  <C value="-0.20195" />
-  <D value="-0.16172" />
-  <E value="0.24757" />
-  <Tmin units="K"  value="246" />
-  <Tmax units="K"  value="255.5" />
-  </HeatOfVaporization>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="37365" />
-  <B value="-232.94" />
-  <C value="10.977" />
-  <D value="0.00031169" />
-  <E value="-1.1931E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="2" />
-  <A value="-3.7052E-07" />
-  <B value="2.2773E-08" />
-  <Tmin units="K"  value="276.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29751" />
-  <B value="158.25" />
-  <C value="-0.13576" />
-  <D value="0.000041065" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.203" />
-  <B value="2466.4" />
-  <C value="-44.307" />
-  <Tmin units="K"  value="272" />
-  <Tmax units="K"  value="399.5" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.139908" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.391187E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="956.7623" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.386" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0111154" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.431227" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0531885" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.738827" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.7628" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.431227" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="32600" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0531885" />
-<CAS name="CAS number"  value="10544-73-7" />
-<Smiles name="SMILES"  value="O=N(=O)N=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="906" />
-<CompoundID name="Name"  value="Nitrogen tetroxide" />
-<StructureFormula name="Structure"  value="O2NNO2" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="431.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1.00312E+07" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.08249" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.233" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="294.3" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="263.01" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="261.9" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="18558.7" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="92.011" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.06407" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.853274" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.918E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24123.32" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03008" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.96E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="9162960" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.785E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="304320" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.465E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.29223" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="1983170" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="21.508" />
-  <B value="-2.416E-08" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="78.15" />
-  <Tmax units="K"  value="87.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.117" />
-  <B value="0.32671" />
-  <C value="431.15" />
-  <D value="0.20832" />
-  <Tmin units="K"  value="261.9" />
-  <Tmax units="K"  value="343.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="72.419" />
-  <B value="-5432" />
-  <C value="-7.7259" />
-  <D value="0.00001711" />
-  <E value="2" />
-  <Tmin units="K"  value="252.77" />
-  <Tmax units="K"  value="431.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.0678E+07" />
-  <B value="0.17744" />
-  <C value="-0.16521" />
-  <D value="-0.11792" />
-  <E value="0.13193" />
-  <Tmin units="K"  value="294.25" />
-  <Tmax units="K"  value="303.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10482" />
-  <B value="1238.4" />
-  <C value="-7.4993" />
-  <D value="0.025528" />
-  <E value="-0.000031204" />
-  <Tmin units="K"  value="30.18" />
-  <Tmax units="K"  value="300" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="112080" />
-  <B value="15.081" />
-  <C value="5.5387" />
-  <D value="0.025083" />
-  <E value="-0.000030338" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39950.82" />
-  <B value="-260.1236" />
-  <C value="11.41281" />
-  <D value="0.000224817" />
-  <E value="-1.049284E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-340.1" />
-  <B value="10957" />
-  <C value="53.641" />
-  <D value="-0.00011365" />
-  <E value="2" />
-  <Tmin units="K"  value="261" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000080298" />
-  <B value="0.2905" />
-  <C value="212.56" />
-  <D value="117290" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11499" />
-  <B value="26916" />
-  <C value="-297.75" />
-  <D value="1.089" />
-  <E value="-0.0013592" />
-  <Tmin units="K"  value="270" />
-  <Tmax units="K"  value="400" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000019664" />
-  <B value="1.1277" />
-  <C value="265.48" />
-  <D value="-210280" />
-  <Tmin units="K"  value="380" />
-  <Tmax units="K"  value="400" />
-  </VaporThermalConductivity>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="28036" />
-  <B value="221.65" />
-  <C value="-0.18724" />
-  <D value="0.000054692" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.96278" />
-  <B value="-1250" />
-  <C value="-7.5" />
-  <Tmin units="K"  value="268.5945" />
-  <Tmax units="K"  value="438.5945" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="26.91" />
-  <B value="5073.2" />
-  <C value="35.325" />
-  <Tmin units="K"  value="263.15" />
-  <Tmax units="K"  value="386.61" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4749" />
-  <B value="-0.014594" />
-  <Tmin units="K"  value="261" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.159449" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.665358E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="148.6014" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.233" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-4.24638" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00859559" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.46343" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.853274" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.06407" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.982861" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.984" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.80727" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.853274" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24123.32" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.06407" />
-<CAS name="CAS number"  value="10544-72-6" />
-<Smiles name="SMILES"  value="O=N(=O)N(=O)=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="913" />
-<CompoundID name="Name"  value="Helium-4" />
-<StructureFormula name="Structure"  value="He" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="5.19" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="227000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0573" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.301" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="4.3" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="1.763" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="1.763" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1478.21" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="4.003" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.03254" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="-0.39" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="0" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="1222" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.00692" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.48E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="126044" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="50000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="-0.1555" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="47.969" />
-  <B value="7.3751E-08" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="1.73" />
-  <Tmax units="K"  value="11.23" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.31844" />
-  <B value="0.089499" />
-  <C value="5.21" />
-  <D value="0.063807" />
-  <Tmin units="K"  value="1.2" />
-  <Tmax units="K"  value="5.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="8.8804" />
-  <B value="-4.8932" />
-  <C value="2.5648" />
-  <D value="0.0062779" />
-  <E value="2" />
-  <Tmin units="K"  value="1.4" />
-  <Tmax units="K"  value="11.26" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="191120" />
-  <B value="4.6881" />
-  <C value="-12.652" />
-  <D value="12.947" />
-  <E value="-4.5859" />
-  <Tmin units="K"  value="2.2" />
-  <Tmax units="K"  value="5.18" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-72432" />
-  <B value="14.864" />
-  <C value="0.90909" />
-  <D value="1.9106" />
-  <E value="-0.057997" />
-  <Tmin units="K"  value="3.7" />
-  <Tmax units="K"  value="11.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="20786" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="1" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.016091" />
-  <B value="-0.3836" />
-  <C value="-3.2519E-07" />
-  <D value="3.3839E-14" />
-  <E value="-6.7038E-16" />
-  <Tmin units="K"  value="2" />
-  <Tmax units="K"  value="150" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-21.436" />
-  <B value="10.949" />
-  <C value="5.7389" />
-  <D value="-0.11646" />
-  <E value="2" />
-  <Tmin units="K"  value="2.2" />
-  <Tmax units="K"  value="11.7" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.3098E-07" />
-  <B value="0.71183" />
-  <C value="-10.485" />
-  <D value="126.3" />
-  <Tmin units="K"  value="14.4" />
-  <Tmax units="K"  value="2000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.19278" />
-  <B value="-0.8853" />
-  <C value="-0.83633" />
-  <D value="-0.19115" />
-  <E value="0.016867" />
-  <Tmin units="K"  value="2.2" />
-  <Tmax units="K"  value="11.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00226" />
-  <B value="0.7305" />
-  <C value="-18.63" />
-  <D value="440" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="2000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="0.00015359" />
-  <B value="-20.248" />
-  <C value="20.138" />
-  <D value="-11.865" />
-  <E value="1.2499" />
-  <Tmin units="K"  value="1.25" />
-  <Tmax units="K"  value="4.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="20786" />
-  <B value="7.6827E-14" />
-  <C value="-1.6203E-16" />
-  <D value="2.6645E-20" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="1" />
-  <A value="1.055" />
-  <Tmin units="K"  value="1" />
-  <Tmax units="K"  value="1500" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="15.213" />
-  <B value="15.497" />
-  <C value="-0.0068635" />
-  <Tmin units="K"  value="3.15" />
-  <Tmax units="K"  value="4.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="2" />
-  <A value="0" />
-  <B value="0" />
-  <Tmin units="K"  value="2.2" />
-  <Tmax units="K"  value="11.7" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.037046" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.038669E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="4.496969" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.301" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="2.67" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00399858" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.124064" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="-0.39" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.03254" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.456163" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.592" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="-0.39" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="1222" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.03254" />
-<GCmethod name="PPR78" >
-  <group id="23"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="200"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7440-59-7" />
-<Smiles name="SMILES"  value="[He]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="917" />
-<CompoundID name="Name"  value="Fluorine" />
-<StructureFormula name="Structure"  value="F2" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="144.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5215000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0662" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.288" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="84.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="53.53" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="53.48" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="252" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="37.997" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.02516" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.051" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="9.081E-11" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15210" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0142" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.5E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="202690" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="510360" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.57194" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="54.682" />
-  <B value="-0.11345" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="23" />
-  <Tmax units="K"  value="53.48" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.7003" />
-  <B value="0.23171" />
-  <C value="144.42" />
-  <D value="0.21541" />
-  <Tmin units="K"  value="53.48" />
-  <Tmax units="K"  value="144.41" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="19.18299" />
-  <B value="-840.6862" />
-  <C value="0.560464" />
-  <D value="-0.0000352006" />
-  <E value="2" />
-  <Tmin units="K"  value="53.45" />
-  <Tmax units="K"  value="144.41" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.7497E+07" />
-  <B value="7.2112" />
-  <C value="-17.699" />
-  <D value="17.895" />
-  <E value="-6.7781" />
-  <Tmin units="K"  value="53.48" />
-  <Tmax units="K"  value="144.41" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-25122" />
-  <B value="3384" />
-  <C value="-116.81" />
-  <D value="2.5952" />
-  <E value="-0.020438" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="53.54" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="56031" />
-  <B value="-8382.1" />
-  <C value="267.49" />
-  <D value="-2.7228" />
-  <E value="0.0096889" />
-  <Tmin units="K"  value="53.48" />
-  <Tmax units="K"  value="110" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29021.05" />
-  <B value="-721.5995" />
-  <C value="10.44015" />
-  <D value="-0.00105401" />
-  <E value="3.331903E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.03545" />
-  <B value="-12.768" />
-  <C value="-0.0732" />
-  <D value="0.032456" />
-  <E value="-0.023131" />
-  <Tmin units="K"  value="79.37" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="9.2895" />
-  <B value="-86.903" />
-  <C value="-3.7445" />
-  <D value="0.0000058477" />
-  <E value="2" />
-  <Tmin units="K"  value="53.48" />
-  <Tmax units="K"  value="140" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.0875E-07" />
-  <B value="0.64956" />
-  <C value="73.747" />
-  <D value="-637.02" />
-  <Tmin units="K"  value="53.48" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.15422" />
-  <B value="9.0003" />
-  <C value="-1.0608" />
-  <D value="-0.0018487" />
-  <E value="-0.00001682" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="130" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00012664" />
-  <B value="0.93229" />
-  <C value="1.6645" />
-  <D value="205.53" />
-  <Tmin units="K"  value="70" />
-  <Tmax units="K"  value="700" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0023955" />
-  <B value="117.16" />
-  <C value="-8.211" />
-  <D value="0.06394" />
-  <E value="-0.00037668" />
-  <Tmin units="K"  value="53.48" />
-  <Tmax units="K"  value="144.12" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="27829" />
-  <B value="3.8829" />
-  <C value="0.043734" />
-  <D value="-0.000066017" />
-  <E value="2.7438E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.897" />
-  <B value="777.75" />
-  <C value="-1.967" />
-  <Tmin units="K"  value="86.6" />
-  <Tmax units="K"  value="129.81" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-5.905" />
-  <B value="-0.027953" />
-  <Tmin units="K"  value="53.48" />
-  <Tmax units="K"  value="140" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0756619" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.361966E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="106.6577" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.288" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="29.4" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.00883306" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.5" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.051" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.02516" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="0.75" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="0.88" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.051" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15210" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.02516" />
-<Umr name="UMR" >
-  <group id="206"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7782-41-4" />
-<Smiles name="SMILES"  value="FF" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="920" />
-<CompoundID name="Name"  value="Krypton" />
-<StructureFormula name="Structure"  value="Kr" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="209.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5500000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0912" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.288" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="119.74" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="115.77" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="115.78" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="73149.9" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="83.8" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.03463" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.005" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="0" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15280" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="163975" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1640130" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.47685" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="33.723" />
-  <B value="-1.7802E-08" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="115.76" />
-  <Tmax units="K"  value="125.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.5742" />
-  <B value="0.26395" />
-  <C value="209.4" />
-  <D value="0.25018" />
-  <Tmin units="K"  value="115.76" />
-  <Tmax units="K"  value="209.39" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="48.208" />
-  <B value="-1609" />
-  <C value="-4.9593" />
-  <D value="0.0000342" />
-  <E value="2" />
-  <Tmin units="K"  value="109.95" />
-  <Tmax units="K"  value="209.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.7515E+07" />
-  <B value="2.6595" />
-  <C value="-6.0031" />
-  <D value="6.068" />
-  <E value="-2.2776" />
-  <Tmin units="K"  value="115.76" />
-  <Tmax units="K"  value="209.39" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="36193" />
-  <B value="105.13" />
-  <C value="3.9876" />
-  <D value="0.048456" />
-  <E value="-0.0001134" />
-  <Tmin units="K"  value="115.78" />
-  <Tmax units="K"  value="125.28" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="20754" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.047877" />
-  <B value="-27.168" />
-  <C value="-0.22682" />
-  <D value="-0.035005" />
-  <E value="0.047036" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1073.15" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.7422" />
-  <B value="-0.3975" />
-  <C value="-0.00054036" />
-  <D value="-9.2221E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="119.75" />
-  <Tmax units="K"  value="129.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000018282" />
-  <B value="0.5384" />
-  <C value="165.83" />
-  <D value="-1432.5" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1773.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.22624" />
-  <B value="-10.133" />
-  <C value="-0.77044" />
-  <D value="-0.0023081" />
-  <E value="-0.0000013009" />
-  <Tmin units="K"  value="115" />
-  <Tmax units="K"  value="209.35" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00075369" />
-  <B value="0.52925" />
-  <C value="198.58" />
-  <D value="-4150.2" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="2000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0038578" />
-  <B value="222.03" />
-  <C value="-8.5239" />
-  <D value="0.041178" />
-  <E value="-0.00015364" />
-  <Tmin units="K"  value="115.78" />
-  <Tmax units="K"  value="209.35" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="20786" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.332" />
-  <B value="977.58" />
-  <C value="-8.874" />
-  <Tmin units="K"  value="125.94" />
-  <Tmax units="K"  value="184.73" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-7.7494" />
-  <B value="-1.046E-09" />
-  <Tmin units="K"  value="119.75" />
-  <Tmax units="K"  value="129.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0912" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="3.740867E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="154.7757" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.288" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="24.5" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0123743" />
-<SpecificGravity name="Specific gravity"  units="_"  value="2.42087" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.005" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.03463" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.12" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.12" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.005" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15280" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.03463" />
-<Umr name="UMR" >
-  <group id="203"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7439-90-9" />
-<Smiles name="SMILES"  value="[Kr]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="959" />
-<CompoundID name="Name"  value="Xenon" />
-<StructureFormula name="Structure"  value="Xe" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="289.74" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5840000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.118" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.286" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="165.01" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="161.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="161.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="81667.9" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="131.29" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.04291" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.006" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="0" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15910" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="0" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="0" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="169578" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2294950" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.48315" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="0" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="26.963" />
-  <B value="-2.7339E-08" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="161.36" />
-  <Tmax units="K"  value="170.86" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.4063" />
-  <B value="0.28552" />
-  <C value="289.74" />
-  <D value="0.28967" />
-  <Tmin units="K"  value="161.36" />
-  <Tmax units="K"  value="289.74" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="31.497" />
-  <B value="-1758.9" />
-  <C value="-1.8727" />
-  <D value="0.0000091652" />
-  <E value="2" />
-  <Tmin units="K"  value="155.55" />
-  <Tmax units="K"  value="290" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.740633E+07" />
-  <B value="-0.233725" />
-  <C value="3.148357" />
-  <D value="-4.995262" />
-  <E value="2.477111" />
-  <Tmin units="K"  value="161.36" />
-  <Tmax units="K"  value="289.74" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="44610" />
-  <B value="-221" />
-  <C value="1.0811" />
-  <D value="0.026515" />
-  <E value="-0.000013257" />
-  <Tmin units="K"  value="163.15" />
-  <Tmax units="K"  value="172.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="20786" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.065789" />
-  <B value="-49.796" />
-  <C value="-0.7443" />
-  <D value="-0.092289" />
-  <E value="0.83555" />
-  <Tmin units="K"  value="144.87" />
-  <Tmax units="K"  value="1448.7" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.7421" />
-  <B value="-0.53776" />
-  <C value="-0.00050184" />
-  <D value="-5.2934E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="165.02" />
-  <Tmax units="K"  value="174.52" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000014055" />
-  <B value="0.57778" />
-  <C value="188.46" />
-  <D value="-312.26" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1773.15" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.012175" />
-  <B value="143.58" />
-  <C value="-4.2655" />
-  <D value="0.011041" />
-  <E value="-0.000032937" />
-  <Tmin units="K"  value="145.9" />
-  <Tmax units="K"  value="270" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00026719" />
-  <B value="0.62046" />
-  <C value="215.6" />
-  <D value="-8144.4" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0032828" />
-  <B value="498.28" />
-  <C value="-11.457" />
-  <D value="0.046655" />
-  <E value="-0.00011349" />
-  <Tmin units="K"  value="161.36" />
-  <Tmax units="K"  value="289.74" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="20786" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.626" />
-  <B value="1889.6" />
-  <C value="22.713" />
-  <Tmin units="K"  value="174.87" />
-  <Tmax units="K"  value="260" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-7.7494" />
-  <B value="-6.6574E-10" />
-  <Tmin units="K"  value="165.02" />
-  <Tmax units="K"  value="174.52" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.118" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.110548E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="208.8524" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.286" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="32.7" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0164353" />
-<SpecificGravity name="Specific gravity"  units="_"  value="2.95262" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.006" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.04291" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.13" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.13" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.006" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15910" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.04291" />
-<Umr name="UMR" >
-  <group id="204"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="7440-63-3" />
-<Smiles name="SMILES"  value="[Xe]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="924" />
-<CompoundID name="Name"  value="Ozone" />
-<StructureFormula name="Structure"  value="O3" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="261.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5570000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.0894" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.229" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="161.8" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="22.1499" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="80.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.734621" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="47.998" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0354" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.224" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.544E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18740" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.8E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.016687" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.175E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.431E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.63164E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="238823" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2000000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.755282" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.42671E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="36.026" />
-  <B value="-0.000044231" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="77.15" />
-  <Tmax units="K"  value="86.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.6432" />
-  <B value="0.26544" />
-  <C value="261.05" />
-  <D value="0.25239" />
-  <Tmin units="K"  value="77.55" />
-  <Tmax units="K"  value="261" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="33.80011" />
-  <B value="-2066.264" />
-  <C value="-1.865143" />
-  <D value="3.696996E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="80.15" />
-  <Tmax units="K"  value="261" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.6254E+07" />
-  <B value="-0.073447" />
-  <C value="0.14823" />
-  <D value="0.62225" />
-  <E value="-0.43277" />
-  <Tmin units="K"  value="80.15" />
-  <Tmax units="K"  value="261" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="40260" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="261.05" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="64500" />
-  <B value="-60.205" />
-  <C value="9.9787" />
-  <D value="0.0080434" />
-  <E value="-0.000010929" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="150" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="32859.57" />
-  <B value="-604.7407" />
-  <C value="10.91207" />
-  <D value="-0.000287995" />
-  <E value="2.632407E-08" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.062399" />
-  <B value="-35.678" />
-  <C value="-1.1646" />
-  <D value="22.22" />
-  <E value="-31.557" />
-  <Tmin units="K"  value="130.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-37.036" />
-  <B value="815.78" />
-  <C value="4.8971" />
-  <D value="-0.000047646" />
-  <E value="2" />
-  <Tmin units="K"  value="77.55" />
-  <Tmax units="K"  value="208.8" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000001896" />
-  <B value="0.78539" />
-  <C value="36.908" />
-  <D value="-2041.9" />
-  <Tmin units="K"  value="80.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.23255" />
-  <B value="-678.09" />
-  <C value="-6.5705" />
-  <D value="-0.074977" />
-  <E value="0.00025391" />
-  <Tmin units="K"  value="77.35" />
-  <Tmax units="K"  value="161.85" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0043907" />
-  <B value="0.47832" />
-  <C value="709.48" />
-  <D value="233.72" />
-  <Tmin units="K"  value="161.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0083875" />
-  <B value="70.417" />
-  <C value="-4.4511" />
-  <D value="0.011555" />
-  <E value="-0.000053029" />
-  <Tmin units="K"  value="77.2" />
-  <Tmax units="K"  value="261" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34139" />
-  <B value="-31.67" />
-  <C value="0.26033" />
-  <D value="-0.00035752" />
-  <E value="1.5074E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.205" />
-  <B value="1378.5" />
-  <C value="-19.313" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="232.44" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.661" />
-  <B value="-0.027987" />
-  <Tmin units="K"  value="77.55" />
-  <Tmax units="K"  value="208.8" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.0888007" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.892771E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="84.53657" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.229" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="18.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0135255" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.25782" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.224" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0354" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.1" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.27" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.224" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18740" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0354" />
-<Umr name="UMR" >
-  <group id="211"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="10028-15-6" />
-<Smiles name="SMILES"  value="O=[O+][O-]" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1893" />
-<CompoundID name="Name"  value="Carbonyl sulfide" />
-<StructureFormula name="Structure"  value="OCS" />
-<Family name="Family"  value="24" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="375.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6349000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.14" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="223.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="134.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="134.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="101.325" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="60.0751" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0510474" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.137779" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.176E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14270" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0259" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.05247E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.3841E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.692E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="231470" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4725000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.7" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.4827E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="28.192" />
-  <B value="-0.022652" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="53.72" />
-  <Tmax units="K"  value="134.3" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.8896" />
-  <B value="0.27226" />
-  <C value="378.81" />
-  <D value="0.25315" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="378.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="74.34266" />
-  <B value="-3813.497" />
-  <C value="-8.620386" />
-  <D value="0.0000180431" />
-  <E value="2" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="378.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.0555E+07" />
-  <B value="0.84937" />
-  <C value="-0.32129" />
-  <D value="-0.52716" />
-  <E value="0.40226" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="365.93" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16418" />
-  <B value="1744.6" />
-  <C value="-20.143" />
-  <D value="0.10176" />
-  <E value="-0.00014754" />
-  <Tmin units="K"  value="15.53" />
-  <Tmax units="K"  value="131.07" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="71808" />
-  <B value="-8528.4" />
-  <C value="73.159" />
-  <D value="-0.16854" />
-  <E value="0.00016953" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="378" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="28351" />
-  <B value="-363.89" />
-  <C value="10.752" />
-  <D value="-0.00019902" />
-  <E value="7.0945E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.07781" />
-  <B value="-70.275" />
-  <C value="-3.5992" />
-  <D value="374.85" />
-  <E value="-723.14" />
-  <Tmin units="K"  value="189.4" />
-  <Tmax units="K"  value="1889.4" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.091" />
-  <B value="494.42" />
-  <C value="-0.20653" />
-  <D value="-6.4588E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="223" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000010184" />
-  <B value="0.2938" />
-  <C value="1012.7" />
-  <D value="-12250" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.032218" />
-  <B value="-41.011" />
-  <C value="-0.83624" />
-  <D value="-0.0051268" />
-  <E value="0.0000012154" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="223" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0012701" />
-  <B value="0.60437" />
-  <C value="545.23" />
-  <D value="3627.6" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0021071" />
-  <B value="518.04" />
-  <C value="-11.034" />
-  <D value="0.04165" />
-  <E value="-0.000087273" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="365.93" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="21713" />
-  <B value="84.752" />
-  <C value="-0.070005" />
-  <D value="0.000020554" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.073" />
-  <B value="1954.8" />
-  <C value="-19.521" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="333.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.2041" />
-  <B value="-0.017582" />
-  <Tmin units="K"  value="134.3" />
-  <Tmax units="K"  value="223" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.137387" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.621734E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="225.718" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="44.91" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0194842" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.24" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.096" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0510474" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.707317" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.620988" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.59245" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.02642" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.096" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14270" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0510474" />
-<GCmethod name="PPR78" >
-  <group id="227"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="227"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="463-58-1" />
-<Smiles name="SMILES"  value="O=C=S" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1940" />
-<CompoundID name="Name"  value="Sulfur hexafluoride" />
-<StructureFormula name="Structure"  value="SF6" />
-<Family name="Family"  value="55" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="318.72" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3760000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.1984" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.282" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="209.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="222.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="223.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="232670" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="146.056" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.07981" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.208" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="7681" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0468" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.2E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.209E+09" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.1053E+09" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="291710" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5024200" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93506" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="9.24E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.46" />
-  <B value="-3.8147E-08" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="191.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0016" />
-  <B value="0.23435" />
-  <C value="318.74" />
-  <D value="0.24027" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="318.73" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-17.60907" />
-  <B value="-1028.369" />
-  <C value="6.556299" />
-  <D value="-0.0000178874" />
-  <E value="2" />
-  <Tmin units="K"  value="215.15" />
-  <Tmax units="K"  value="318.69" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.0769E+07" />
-  <B value="8.5605" />
-  <C value="-25.709" />
-  <D value="29.437" />
-  <E value="-11.774" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="318.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15357" />
-  <B value="2400" />
-  <C value="-27.232" />
-  <D value="0.044332" />
-  <E value="0.00082624" />
-  <Tmin units="K"  value="7.97" />
-  <Tmax units="K"  value="96.24" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119500" />
-  <B value="-2040" />
-  <C value="-9.5251" />
-  <D value="0.005216" />
-  <E value="-0.000044691" />
-  <Tmin units="K"  value="230.15" />
-  <Tmax units="K"  value="239.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="32322" />
-  <B value="-368.1" />
-  <C value="12.478" />
-  <D value="-0.00063326" />
-  <E value="1.9169E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.14952" />
-  <B value="-95.249" />
-  <C value="-2.9927" />
-  <D value="87.512" />
-  <E value="-180.54" />
-  <Tmin units="K"  value="286.82" />
-  <Tmax units="K"  value="1593.45" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="20.959" />
-  <B value="-457.46" />
-  <C value="-4.9486" />
-  <D value="0.0000065105" />
-  <E value="2" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="318.69" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.9343E-07" />
-  <B value="0.62415" />
-  <C value="62.573" />
-  <D value="13289" />
-  <Tmin units="K"  value="205.15" />
-  <Tmax units="K"  value="2000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.064331" />
-  <B value="-179.32" />
-  <C value="0.36969" />
-  <D value="-0.0050683" />
-  <E value="-0.0000040693" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="318.69" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0013269" />
-  <B value="0.52727" />
-  <C value="30.264" />
-  <D value="73930" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018755" />
-  <B value="-184.08" />
-  <C value="-0.62328" />
-  <D value="-0.010678" />
-  <E value="0.0000067659" />
-  <Tmin units="K"  value="205" />
-  <Tmax units="K"  value="253.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="1143.5" />
-  <B value="420.89" />
-  <C value="-0.39558" />
-  <D value="0.00012305" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.964" />
-  <B value="2204.2" />
-  <C value="6.0906" />
-  <Tmin units="K"  value="225.15" />
-  <Tmax units="K"  value="283.49" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-5.6415" />
-  <B value="-0.0085625" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="318.69" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.248529" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.971185E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="218.3832" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.282" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="111.1" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.97874" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0259655" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.243" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.208" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.07981" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.085036" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.28" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="7.8864" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.208" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="7681" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.07981" />
-<Umr name="UMR" >
-  <group id="226"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="2551-62-4" />
-<Smiles name="SMILES"  value="FS(F)(F)(F)(F)F" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1844" />
-<CompoundID name="Name"  value="Dimethyl sulfoxide" />
-<StructureFormula name="Structure"  value="CH3SOCH3" />
-<Family name="Family"  value="70" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="729" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5650000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.227" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.212" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="462.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="291.67" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="291.67" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="50.2288" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="78.1334" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.071277" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.280551" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.84E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="26750" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.32E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04288" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.18E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.092E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.157E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="306300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.393E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.934577" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.6054E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.743" />
-  <B value="1.2716E-09" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="278.15" />
-  <Tmax units="K"  value="287.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1064" />
-  <B value="0.25156" />
-  <C value="729" />
-  <D value="0.33043" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="705.98" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="87.24911" />
-  <B value="-9095.583" />
-  <C value="-9.246359" />
-  <D value="3.215062E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="729" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.1934E+08" />
-  <B value="12.701" />
-  <C value="-33.974" />
-  <D value="36.922" />
-  <E value="-14.839" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="705.98" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-3951.7" />
-  <B value="764.12" />
-  <C value="-1.607" />
-  <D value="-0.0031255" />
-  <E value="0.000017557" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="280" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="148920" />
-  <B value="274.35" />
-  <C value="2.2127" />
-  <D value="0.017296" />
-  <E value="-0.000001184" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="422.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="61635" />
-  <B value="-582.63" />
-  <C value="12.205" />
-  <D value="-0.000053872" />
-  <E value="2.2232E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17475" />
-  <B value="-282.77" />
-  <C value="-60.169" />
-  <D value="75677" />
-  <E value="-324810" />
-  <Tmin units="K"  value="363" />
-  <Tmax units="K"  value="1993" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="33.492" />
-  <B value="223.29" />
-  <C value="-7.3227" />
-  <D value="0.000014294" />
-  <E value="2" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="464" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.6219E-08" />
-  <B value="0.83436" />
-  <C value="168.37" />
-  <D value="-97.445" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.081843" />
-  <B value="-215.42" />
-  <C value="0.15922" />
-  <D value="-0.0051305" />
-  <E value="0.0000011114" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="464" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0006441" />
-  <B value="0.77214" />
-  <C value="1010.2" />
-  <D value="82198" />
-  <Tmin units="K"  value="462.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035188" />
-  <B value="-130.57" />
-  <C value="-1.0743" />
-  <D value="-0.0038643" />
-  <E value="0.0000013151" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="705.98" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="22599" />
-  <B value="269.86" />
-  <C value="-0.15903" />
-  <D value="0.000036573" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="6.679602" />
-  <B value="-11091.2" />
-  <C value="-21.74851" />
-  <Tmin units="K"  value="288" />
-  <Tmax units="K"  value="729" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.505" />
-  <B value="3949.9" />
-  <C value="-67.269" />
-  <Tmin units="K"  value="438.5" />
-  <Tmax units="K"  value="642.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8682" />
-  <B value="-0.011565" />
-  <Tmin units="K"  value="291.67" />
-  <Tmax units="K"  value="464" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.227469" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.322352E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="178.8339" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.212" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="74.67" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0325977" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.10543" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.280551" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.071277" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.8266" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.472" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.280551" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="26750" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.071277" />
-<UnifacVLE name="UNIFAC" >
-  <group id="68"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="68"  value="1" />
-  </UnifacLLE>
-<Umr name="UMR" >
-  <group id="68"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="67"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="67-68-5" />
-<Smiles name="SMILES"  value="CS(=O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="69" />
-<CompoundID name="Name"  value="N-heptadecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)15CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="736" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1340000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.103" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.242" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="574.56" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="295.127" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="295.134" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0465559" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="240.473" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.31045" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.762" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="7.355E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16100" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1808" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.449E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.939E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.083E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="820230" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4.0459E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.7889" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.05618E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="4.0831" />
-  <B value="-0.001532" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="118.05" />
-  <Tmax units="K"  value="295.13" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.1972" />
-  <B value="0.22446" />
-  <C value="736" />
-  <D value="0.27261" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="736" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="230.4768" />
-  <B value="-19512.15" />
-  <C value="-29.73776" />
-  <D value="0.0000119109" />
-  <E value="2" />
-  <Tmin units="K"  value="295.13" />
-  <Tmax units="K"  value="736" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.1837E+08" />
-  <B value="0.45937" />
-  <C value="1.0501" />
-  <D value="-1.8353" />
-  <E value="0.77357" />
-  <Tmin units="K"  value="295.13" />
-  <Tmax units="K"  value="736" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-59944" />
-  <B value="3834.8" />
-  <C value="-16.853" />
-  <D value="0.031845" />
-  <E value="0.0000086344" />
-  <Tmin units="K"  value="30.46" />
-  <Tmax units="K"  value="270.7" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="341660" />
-  <B value="-48.077" />
-  <C value="11.234" />
-  <D value="0.0041437" />
-  <E value="-0.0000017269" />
-  <Tmin units="K"  value="295" />
-  <Tmax units="K"  value="575.3" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="247870" />
-  <B value="-663.74" />
-  <C value="14.166" />
-  <D value="-0.00017722" />
-  <E value="5.7891E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.44015" />
-  <B value="-297.46" />
-  <C value="-550.48" />
-  <D value="-414510" />
-  <E value="499680" />
-  <Tmin units="K"  value="366.69" />
-  <Tmax units="K"  value="1686.69" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-77.193" />
-  <B value="4597" />
-  <C value="9.9892" />
-  <D value="-0.0000084702" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="588.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.2694E-07" />
-  <B value="0.5961" />
-  <C value="448.22" />
-  <D value="45523" />
-  <Tmin units="K"  value="295.13" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.015537" />
-  <B value="-239.33" />
-  <C value="0.042685" />
-  <D value="-0.0038367" />
-  <E value="8.6547E-07" />
-  <Tmin units="K"  value="295.13" />
-  <Tmax units="K"  value="575.3" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-115.33" />
-  <B value="1.0524" />
-  <C value="-2.1515E+09" />
-  <D value="-1.3137E+10" />
-  <Tmin units="K"  value="575.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.038127" />
-  <B value="-105.48" />
-  <C value="-1.5195" />
-  <D value="-0.0033062" />
-  <E value="0.000001514" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="736" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="197990" />
-  <B value="-76.576" />
-  <C value="3.7692" />
-  <D value="-0.0050387" />
-  <E value="0.0000020333" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.204" />
-  <B value="4403.1" />
-  <C value="-120.35" />
-  <Tmin units="K"  value="448.16" />
-  <Tmax units="K"  value="650" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0515" />
-  <B value="-0.0099131" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="588.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.149922" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.058091E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="290.7544" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.242" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="353.46" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.9601" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.122765" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.779388" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.762" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.31045" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="11.9182" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="9.796" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="4.6926" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.762" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16100" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.31045" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="15" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="15" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="15" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="15" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="15" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="15" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-78-7" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="70" />
-<CompoundID name="Name"  value="N-octadecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)16CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="747" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1290000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.189" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.247" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="588.3" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="301.33" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="301.33" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0339091" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="254.5" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.32666" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.808" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="7.655E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16100" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.191" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.584E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.1457E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.921E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="859450" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6.1986E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.6378" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.11726E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="5.0277" />
-  <B value="-0.0050559" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="301.32" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.21099" />
-  <B value="0.23901" />
-  <C value="748.16" />
-  <D value="0.28153" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="748.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="156.4726" />
-  <B value="-16120.27" />
-  <C value="-18.72498" />
-  <D value="5.38655E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="301.31" />
-  <Tmax units="K"  value="750.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.214E+08" />
-  <B value="0.36333" />
-  <C value="1.283" />
-  <D value="-2.0514" />
-  <E value="0.85175" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="723.54" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-62135" />
-  <B value="4107.1" />
-  <C value="-20.184" />
-  <D value="0.052076" />
-  <E value="-0.000032879" />
-  <Tmin units="K"  value="20.8" />
-  <Tmax units="K"  value="298.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="332820" />
-  <B value="-15.176" />
-  <C value="11.369" />
-  <D value="0.0039066" />
-  <E value="-0.0000015738" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="589.86" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="258960" />
-  <B value="-641.43" />
-  <C value="14.136" />
-  <D value="-0.000068602" />
-  <E value="1.814E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.37194" />
-  <B value="-125.23" />
-  <C value="-684.43" />
-  <D value="-279030" />
-  <E value="-217610" />
-  <Tmin units="K"  value="372.63" />
-  <Tmax units="K"  value="1712.63" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-83.956" />
-  <B value="4978.7" />
-  <C value="10.99" />
-  <D value="-0.0000089834" />
-  <E value="2" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="613.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.2955E-07" />
-  <B value="0.58255" />
-  <C value="343.75" />
-  <D value="67974" />
-  <Tmin units="K"  value="301.31" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.046627" />
-  <B value="-130.56" />
-  <C value="-0.64842" />
-  <D value="-0.0017182" />
-  <E value="-4.6995E-07" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="589.86" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-198.99" />
-  <B value="1.1011" />
-  <C value="-5.9685E+09" />
-  <D value="5.2419E+11" />
-  <Tmin units="K"  value="589.86" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0056568" />
-  <B value="50.95" />
-  <C value="-3.3461" />
-  <D value="0.00054721" />
-  <E value="-0.0000042845" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="723.54" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="208940" />
-  <B value="-79.844" />
-  <C value="3.9922" />
-  <D value="-0.0053425" />
-  <E value="0.0000021569" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.043" />
-  <B value="4346" />
-  <C value="-132.5" />
-  <Tmin units="K"  value="450" />
-  <Tmax units="K"  value="653.17" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0265" />
-  <B value="-0.0096674" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="613.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.234017" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.058609E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="317.6455" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.247" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="373.98" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.127864" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.78311" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.808" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.32666" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="12.5926" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="10.336" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003612" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.808" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16100" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.32666" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="16" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="16" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="16" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="16" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="16" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="16" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="593-45-3" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="71" />
-<CompoundID name="Name"  value="N-nonadecane" />
-<StructureFormula name="Structure"  value="CH3(CH2)17CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="760" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1230000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.1" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.215" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="603.75" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="305.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="305.04" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0159089" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="268.521" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.343701" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.8271" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="7.983E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16200" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2012" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.719E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.3514E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.075E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="898930" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5.02E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.68901" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.17812E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="3.6651" />
-  <B value="-0.0013337" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="122.02" />
-  <Tmax units="K"  value="305.33" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.20149" />
-  <B value="0.23831" />
-  <C value="760" />
-  <D value="0.29903" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="734.16" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="182.4003" />
-  <B value="-17843.62" />
-  <C value="-22.48728" />
-  <D value="7.349606E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="305.04" />
-  <Tmax units="K"  value="760.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.5404E+08" />
-  <B value="1.2215" />
-  <C value="-0.32899" />
-  <D value="-1.0541" />
-  <E value="0.6821" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="758" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="171240" />
-  <B value="-1715.3" />
-  <C value="33.643" />
-  <D value="-0.15717" />
-  <E value="0.00026291" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="300" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="244790" />
-  <B value="42.54" />
-  <C value="11.446" />
-  <D value="0.0046334" />
-  <E value="-0.0000026668" />
-  <Tmin units="K"  value="305" />
-  <Tmax units="K"  value="603.05" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="274480" />
-  <B value="-648.39" />
-  <C value="14.221" />
-  <D value="-0.00011095" />
-  <E value="3.3607E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.32673" />
-  <B value="14.285" />
-  <C value="-813.39" />
-  <D value="-219560" />
-  <E value="-742530" />
-  <Tmin units="K"  value="377.97" />
-  <Tmax units="K"  value="1737.97" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-84.761" />
-  <B value="5101" />
-  <C value="11.082" />
-  <D value="-0.0000087239" />
-  <E value="2" />
-  <Tmin units="K"  value="303.15" />
-  <Tmax units="K"  value="623.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.0651E-07" />
-  <B value="0.58942" />
-  <C value="341.93" />
-  <D value="67425" />
-  <Tmin units="K"  value="305.04" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.057019" />
-  <B value="73.111" />
-  <C value="-2.1518" />
-  <D value="0.0021618" />
-  <E value="-0.0000035171" />
-  <Tmin units="K"  value="305.04" />
-  <Tmax units="K"  value="603.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000043333" />
-  <B value="1.271" />
-  <C value="2799.6" />
-  <D value="138170" />
-  <Tmin units="K"  value="603.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0038905" />
-  <B value="102.44" />
-  <C value="-3.8793" />
-  <D value="0.0021193" />
-  <E value="-0.0000060226" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="758" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="6522.3" />
-  <B value="1719.5" />
-  <C value="-0.89542" />
-  <D value="0.00017419" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.282" />
-  <B value="4624.1" />
-  <C value="-129.45" />
-  <Tmin units="K"  value="456.75" />
-  <Tmax units="K"  value="662.64" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0344" />
-  <B value="-0.0094781" />
-  <Tmin units="K"  value="303.15" />
-  <Tmax units="K"  value="623.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.318669" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.21838E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="196.1125" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.215" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="394.5" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.135494" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.787872" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.8271" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.343701" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="13.267" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="10.876" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.8271" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16200" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.343701" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="17" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="17" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="17" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="17" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="17" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="17" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-92-5" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="74" />
-<CompoundID name="Name"  value="N-heneicosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)19CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="798.64" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1391000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.197" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.211" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="629.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="313.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="313.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00621532" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="296.574" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.376581" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.942004" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="8.535E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15900" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2217" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="2.989E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.778E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.229E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="985000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4.7698E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.678346" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.296E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="3.3536" />
-  <B value="-0.0013378" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="125.34" />
-  <Tmax units="K"  value="313.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.0010945" />
-  <B value="0.018629" />
-  <C value="798.64" />
-  <D value="0.095543" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="778" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="107.2451" />
-  <B value="-14833.82" />
-  <C value="-11.21418" />
-  <D value="3.606473E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="313.35" />
-  <Tmax units="K"  value="778" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.0592E+08" />
-  <B value="3.1557" />
-  <C value="-6.6833" />
-  <D value="7.1267" />
-  <E value="-3.099" />
-  <Tmin units="K"  value="313.35" />
-  <Tmax units="K"  value="778" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5.0726" />
-  <B value="-375.05" />
-  <C value="13.437" />
-  <D value="-0.02297" />
-  <E value="0.000013281" />
-  <Tmin units="K"  value="291.15" />
-  <Tmax units="K"  value="300.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="268470" />
-  <B value="50.971" />
-  <C value="11.858" />
-  <D value="0.0031331" />
-  <E value="-0.0000010628" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="740" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="253120" />
-  <B value="-507.31" />
-  <C value="13.984" />
-  <D value="0.00027572" />
-  <E value="-9.6316E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.73028" />
-  <B value="-515.12" />
-  <C value="-797.83" />
-  <D value="-1492800" />
-  <E value="2875300" />
-  <Tmin units="K"  value="389" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-25.108" />
-  <B value="2540.9" />
-  <C value="2.0324" />
-  <D value="-0.0000013549" />
-  <E value="2" />
-  <Tmin units="K"  value="313.35" />
-  <Tmax units="K"  value="630.79" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.9575E-07" />
-  <B value="0.62136" />
-  <C value="718.74" />
-  <D value="3255.3" />
-  <Tmin units="K"  value="313.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.22263" />
-  <B value="31.196" />
-  <C value="-1.0701" />
-  <D value="0.0001617" />
-  <E value="-7.0064E-07" />
-  <Tmin units="K"  value="313.15" />
-  <Tmax units="K"  value="629.65" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-237.86" />
-  <B value="1.0527" />
-  <C value="-4.9708E+09" />
-  <D value="-8.9521E+10" />
-  <Tmin units="K"  value="629.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035118" />
-  <B value="-77.945" />
-  <C value="-1.8055" />
-  <D value="-0.0025383" />
-  <E value="0.0000008909" />
-  <Tmin units="K"  value="313.35" />
-  <Tmax units="K"  value="778" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-8894.6" />
-  <B value="1961.7" />
-  <C value="-1.0696" />
-  <D value="0.00022407" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.466" />
-  <B value="4900.1" />
-  <C value="-136.52" />
-  <Tmin units="K"  value="484.54" />
-  <Tmax units="K"  value="704.63" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9063" />
-  <B value="-0.0093353" />
-  <Tmin units="K"  value="313.35" />
-  <Tmax units="K"  value="630.79" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.486861" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.281752E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="192.611" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.211" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="435.54" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.158831" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.792195" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.942004" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.376581" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="14.6158" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="11.956" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.942004" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15900" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.376581" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="19" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="19" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="19" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="19" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="19" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="19" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-94-7" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="75" />
-<CompoundID name="Name"  value="N-docosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)20CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="808.83" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1339000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.252" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.209" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="641.75" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="318.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="317.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00359575" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="310.601" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.393226" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.973" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="8.799E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2319" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.124E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.985E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.307E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1019000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4.8953E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.744627" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.357E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="3.2062" />
-  <B value="-0.0012637" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="126.86" />
-  <Tmax units="K"  value="317.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.00088994" />
-  <B value="0.017172" />
-  <C value="808.83" />
-  <D value="0.094179" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="787" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="270.663" />
-  <B value="-22731.61" />
-  <C value="-35.81794" />
-  <D value="0.0000193308" />
-  <E value="2" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="787" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.5383E+08" />
-  <B value="1.0955" />
-  <C value="-1.2067" />
-  <D value="1.3977" />
-  <E value="-0.85529" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="787" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="22469" />
-  <B value="2585.1" />
-  <C value="-4.4911" />
-  <D value="0.010078" />
-  <E value="-0.000009896" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="317.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94846" />
-  <B value="-114.81" />
-  <C value="13.466" />
-  <D value="0.000531" />
-  <E value="3.3532E-07" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="740" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="291820" />
-  <B value="-567.43" />
-  <C value="14.157" />
-  <D value="0.00012912" />
-  <E value="-4.9166E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.76617" />
-  <B value="-496.25" />
-  <C value="-894.79" />
-  <D value="-1799300" />
-  <E value="3495100" />
-  <Tmin units="K"  value="393.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-27.314" />
-  <B value="2728.1" />
-  <C value="2.3358" />
-  <D value="-0.0000013135" />
-  <E value="2" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="643.03" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.8858E-07" />
-  <B value="0.62154" />
-  <C value="714.54" />
-  <D value="4582.3" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.148" />
-  <B value="-22.716" />
-  <C value="-0.91136" />
-  <D value="-0.00059496" />
-  <E value="-3.4759E-07" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="641.75" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-270.77" />
-  <B value="1.0546" />
-  <C value="-5.8977E+09" />
-  <D value="-1.0935E+11" />
-  <Tmin units="K"  value="641.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.03075" />
-  <B value="-73.068" />
-  <C value="-1.9074" />
-  <D value="-0.002422" />
-  <E value="7.0531E-07" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="787" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-16805" />
-  <B value="2089.4" />
-  <C value="-1.1669" />
-  <D value="0.00025179" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.153082" />
-  <B value="-1000" />
-  <C value="-6" />
-  <Tmin units="K"  value="304.15" />
-  <Tmax units="K"  value="474.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.952" />
-  <B value="5415.6" />
-  <C value="-122.39" />
-  <Tmin units="K"  value="490.15" />
-  <Tmax units="K"  value="712.81" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.7996" />
-  <B value="-0.0093671" />
-  <Tmin units="K"  value="317.15" />
-  <Tmax units="K"  value="643.03" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.567299" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.316045E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="188.4938" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.209" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="456.06" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.167898" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.795185" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.973" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.393226" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="15.2902" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="12.496" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.973" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.393226" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="20" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="20" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="20" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="20" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="20" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="20" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-97-0" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="76" />
-<CompoundID name="Name"  value="N-tricosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)21CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="818.25" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1290000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.307" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.208" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="653.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="320.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="320.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00186855" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="324.627" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.4074" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.02617" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="9.065E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2422" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.259E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.192E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.39E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1064000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5.3974E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.8" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.417E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="3.0671" />
-  <B value="-0.0011957" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="128.26" />
-  <Tmax units="K"  value="320.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.048866" />
-  <B value="0.12922" />
-  <C value="818.25" />
-  <D value="0.20531" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="770.98" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-22.08031" />
-  <B value="-9534.111" />
-  <C value="8.274049" />
-  <D value="-0.0000125255" />
-  <E value="2" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="796" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.6434E+08" />
-  <B value="1.0068" />
-  <C value="-0.55169" />
-  <D value="0.31454" />
-  <E value="-0.3244" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="796" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="6630" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="320.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-58655" />
-  <B value="-99.845" />
-  <C value="13.754" />
-  <D value="0.00030768" />
-  <E value="3.7705E-07" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="750" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="304710" />
-  <B value="-567.01" />
-  <C value="14.201" />
-  <D value="0.00012862" />
-  <E value="-4.8999E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.80211" />
-  <B value="-472.21" />
-  <C value="-1000" />
-  <D value="-2157000" />
-  <E value="4225100" />
-  <Tmin units="K"  value="398" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.8394" />
-  <B value="1949.8" />
-  <C value="-0.47088" />
-  <D value="0.0000010446" />
-  <E value="2" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="654.75" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.8518E-07" />
-  <B value="0.61933" />
-  <C value="704.01" />
-  <D value="6598.3" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.18218" />
-  <B value="0.19147" />
-  <C value="-0.94906" />
-  <D value="-0.00035642" />
-  <E value="-3.5025E-07" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="653.35" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-232.83" />
-  <B value="1.0566" />
-  <C value="-5.2747E+09" />
-  <D value="-9.8604E+10" />
-  <Tmin units="K"  value="653.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.03252" />
-  <B value="-86.948" />
-  <C value="-1.7797" />
-  <D value="-0.0026525" />
-  <E value="9.2007E-07" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="796" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-17575" />
-  <B value="2183.7" />
-  <C value="-1.2207" />
-  <D value="0.00026363" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.773" />
-  <B value="5247.8" />
-  <C value="-140.8" />
-  <Tmin units="K"  value="493.15" />
-  <Tmax units="K"  value="720.94" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8318" />
-  <B value="-0.0091216" />
-  <Tmin units="K"  value="320.65" />
-  <Tmax units="K"  value="654.75" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.644437" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.342746E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="187.4249" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.208" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="476.58" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.17165" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.798403" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.02617" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.4074" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="15.9646" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="13.036" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.02617" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.4074" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="21" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="21" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="21" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="21" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="21" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="21" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="638-67-5" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="77" />
-<CompoundID name="Name"  value="N-tetracosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)22CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="810" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1020000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.36" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.207" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="664.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="324.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="323.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00138507" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="338.654" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.426088" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.07102" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="9.321E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2524" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.394E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.4E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.472E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1097000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5.4894E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.912905" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.479E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="2.705" />
-  <B value="-0.000046396" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="323.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.013821" />
-  <B value="0.07087" />
-  <C value="810" />
-  <D value="0.13885" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="804" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="118.4643" />
-  <B value="-17014.83" />
-  <C value="-12.51446" />
-  <D value="1.109888E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="323.75" />
-  <Tmax units="K"  value="804" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.5462E+08" />
-  <B value="0.24892" />
-  <C value="1.8808" />
-  <D value="-2.829" />
-  <E value="1.1319" />
-  <Tmin units="K"  value="323.75" />
-  <Tmax units="K"  value="804" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-127900" />
-  <B value="6840.6" />
-  <C value="-42.334" />
-  <D value="0.13573" />
-  <E value="-0.00013432" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="290" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="397960" />
-  <B value="-97.814" />
-  <C value="12.108" />
-  <D value="0.0038156" />
-  <E value="-0.0000022229" />
-  <Tmin units="K"  value="323.75" />
-  <Tmax units="K"  value="664.45" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="318880" />
-  <B value="-569.39" />
-  <C value="14.249" />
-  <D value="0.00012213" />
-  <E value="-4.6983E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.66108" />
-  <B value="-157.86" />
-  <C value="-1201.7" />
-  <D value="-2514500" />
-  <E value="5035800" />
-  <Tmin units="K"  value="402" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-64.748" />
-  <B value="4433" />
-  <C value="8.0272" />
-  <D value="-0.0000059771" />
-  <E value="2" />
-  <Tmin units="K"  value="323.75" />
-  <Tmax units="K"  value="793.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.9788E-07" />
-  <B value="0.59708" />
-  <C value="514.64" />
-  <D value="49388" />
-  <Tmin units="K"  value="323.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.046069" />
-  <B value="-245.01" />
-  <C value="-0.62562" />
-  <D value="-0.0019192" />
-  <E value="-0.0000023135" />
-  <Tmin units="K"  value="323.15" />
-  <Tmax units="K"  value="683.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-232.02" />
-  <B value="1.063" />
-  <C value="-5.6529E+09" />
-  <D value="-8.4042E+10" />
-  <Tmin units="K"  value="664.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.087025" />
-  <B value="-29.702" />
-  <C value="-1.7009" />
-  <D value="-0.0013432" />
-  <E value="5.7868E-07" />
-  <Tmin units="K"  value="323.75" />
-  <Tmax units="K"  value="804" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-18646" />
-  <B value="2279.4" />
-  <C value="-1.2759" />
-  <D value="0.0002759" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.919" />
-  <B value="5413.7" />
-  <C value="-142.61" />
-  <Tmin units="K"  value="487.25" />
-  <Tmax units="K"  value="728.17" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.2184" />
-  <B value="-0.0080348" />
-  <Tmin units="K"  value="323.75" />
-  <Tmax units="K"  value="793.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.715072" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.368548E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="182.344" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.207" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="497.1" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.173787" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.797216" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.07102" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.426088" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="16.639" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="13.576" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.07102" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.426088" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="22" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="22" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="22" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="22" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="22" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="22" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="646-31-1" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="78" />
-<CompoundID name="Name"  value="N-pentacosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)23CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="836.31" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1202000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.418" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.205" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="675.05" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="327.9" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="326.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00079876" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="352.68" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.442767" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.10526" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="9.58E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2626" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.529E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.607E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.553E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1143000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5.7739E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.856007" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.539E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="2.8278" />
-  <B value="-0.0010821" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="130.66" />
-  <Tmax units="K"  value="326.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.00063401" />
-  <B value="0.015388" />
-  <C value="836.31" />
-  <D value="0.093752" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="812" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-203.2504" />
-  <B value="-1095.063" />
-  <C value="35.1974" />
-  <D value="-0.0000282197" />
-  <E value="2" />
-  <Tmin units="K"  value="326.65" />
-  <Tmax units="K"  value="812" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.9288E+08" />
-  <B value="1.8937" />
-  <C value="-3.4712" />
-  <D value="3.9636" />
-  <E value="-1.9344" />
-  <Tmin units="K"  value="326.65" />
-  <Tmax units="K"  value="812" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="162660" />
-  <B value="-988.28" />
-  <C value="34.605" />
-  <D value="-0.17879" />
-  <E value="0.00032498" />
-  <Tmin units="K"  value="91.3" />
-  <Tmax units="K"  value="294.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="528340" />
-  <B value="-126.87" />
-  <C value="12.075" />
-  <D value="0.002955" />
-  <E value="-9.8642E-07" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="750" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="330530" />
-  <B value="-566.25" />
-  <C value="14.283" />
-  <D value="0.00012874" />
-  <E value="-4.9096E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.87493" />
-  <B value="-408.43" />
-  <C value="-1227.2" />
-  <D value="-3003700" />
-  <E value="5985700" />
-  <Tmin units="K"  value="406" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.804" />
-  <B value="1971.8" />
-  <C value="-0.26998" />
-  <D value="3.9914E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="326.65" />
-  <Tmax units="K"  value="677.92" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.8769E-07" />
-  <B value="0.61575" />
-  <C value="746.72" />
-  <D value="4040.4" />
-  <Tmin units="K"  value="326.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0058343" />
-  <B value="-203.86" />
-  <C value="-0.37432" />
-  <D value="-0.0029792" />
-  <E value="2.4773E-07" />
-  <Tmin units="K"  value="326.65" />
-  <Tmax units="K"  value="675.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-266.99" />
-  <B value="1.0606" />
-  <C value="-6.4961E+09" />
-  <D value="-1.2167E+11" />
-  <Tmin units="K"  value="675.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.028179" />
-  <B value="-85.291" />
-  <C value="-1.8555" />
-  <D value="-0.0026056" />
-  <E value="7.8884E-07" />
-  <Tmin units="K"  value="326.65" />
-  <Tmax units="K"  value="812" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-19038" />
-  <B value="2371.9" />
-  <C value="-1.3272" />
-  <D value="0.00028688" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.542" />
-  <B value="5136.2" />
-  <C value="-161.6" />
-  <Tmin units="K"  value="503.15" />
-  <Tmax units="K"  value="735.37" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8494" />
-  <B value="-0.0087525" />
-  <Tmin units="K"  value="326.65" />
-  <Tmax units="K"  value="677.92" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.778027" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.403995E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="181.8002" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.205" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="517.62" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.189742" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.803521" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.442767" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="17.3134" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="14.116" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.10526" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.442767" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="23" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="23" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="23" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="23" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="23" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="23" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-99-2" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="79" />
-<CompoundID name="Name"  value="N-hexacosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)24CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="844.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="1162000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.473" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.203" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="685.35" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="329.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="329.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000515816" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="366.707" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.4561" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.15444" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="9.83E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2729" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.664E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.814E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.636E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1176000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5.9496E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.875734" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.6E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="3.1664" />
-  <B value="-0.0021136" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="292.25" />
-  <Tmax units="K"  value="329.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.0012458" />
-  <B value="0.021983" />
-  <C value="844.7" />
-  <D value="0.10464" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="819" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-181.3952" />
-  <B value="-2296.288" />
-  <C value="31.90668" />
-  <D value="-0.0000256231" />
-  <E value="2" />
-  <Tmin units="K"  value="329.25" />
-  <Tmax units="K"  value="819" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.0502E+08" />
-  <B value="2.0708" />
-  <C value="-3.8957" />
-  <D value="4.3419" />
-  <E value="-2.0579" />
-  <Tmin units="K"  value="329.25" />
-  <Tmax units="K"  value="819" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-38418" />
-  <B value="3706.2" />
-  <C value="-2.4141" />
-  <D value="-0.050428" />
-  <E value="0.00014632" />
-  <Tmin units="K"  value="13.83" />
-  <Tmax units="K"  value="320.36" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="657670" />
-  <B value="-651.68" />
-  <C value="14.164" />
-  <D value="-0.00036454" />
-  <E value="7.7672E-07" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="750" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="342560" />
-  <B value="-564.25" />
-  <C value="14.318" />
-  <D value="0.00013185" />
-  <E value="-5.001E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.91137" />
-  <B value="-367.77" />
-  <C value="-1348.9" />
-  <D value="-3484600" />
-  <E value="6989300" />
-  <Tmin units="K"  value="409.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-92.13292" />
-  <B value="5845.982" />
-  <C value="12.08985" />
-  <D value="-8.198834E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="329.25" />
-  <Tmax units="K"  value="813.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.7977E-07" />
-  <B value="0.616" />
-  <C value="732.48" />
-  <D value="6359.2" />
-  <Tmin units="K"  value="329.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.020148" />
-  <B value="-211.96" />
-  <C value="-0.39294" />
-  <D value="-0.0031327" />
-  <E value="1.9698E-07" />
-  <Tmin units="K"  value="329.25" />
-  <Tmax units="K"  value="685.35" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-164.53" />
-  <B value="1.0626" />
-  <C value="-4.163E+09" />
-  <D value="-7.6944E+10" />
-  <Tmin units="K"  value="685.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.066949" />
-  <B value="-1.3964" />
-  <C value="-2.0199" />
-  <D value="-0.0011254" />
-  <E value="0.0000003598" />
-  <Tmin units="K"  value="329.25" />
-  <Tmax units="K"  value="819" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-19227" />
-  <B value="2464" />
-  <C value="-1.3788" />
-  <D value="0.00029808" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.698" />
-  <B value="5292.3" />
-  <C value="-164.22" />
-  <Tmin units="K"  value="509.68" />
-  <Tmax units="K"  value="741.67" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.5609" />
-  <B value="-0.0092454" />
-  <Tmin units="K"  value="329.25" />
-  <Tmax units="K"  value="813.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.831535" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.438745E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="177.2562" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.203" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="538.14" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.197603" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.803608" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.03" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.4561" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="17.9878" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="14.656" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.15444" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15800" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.4561" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="24" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="24" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="24" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="24" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="24" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="24" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="630-01-3" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="80" />
-<CompoundID name="Name"  value="N-heptacosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)25CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="826" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="883000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.58" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.203" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="695.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="332.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="332.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000283125" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="380.734" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.48815" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.21357" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.017E-09" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15810" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.28309" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.799E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.021E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.716E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1216000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6.0417E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.15" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.66E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="2.6193" />
-  <B value="-0.00098572" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="132.86" />
-  <Tmax units="K"  value="332.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.13373" />
-  <B value="0.23061" />
-  <C value="826" />
-  <D value="0.29272" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="800.01" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="254.28" />
-  <B value="-25266" />
-  <C value="-32.268" />
-  <D value="0.0000098574" />
-  <E value="2" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="826" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.738E+08" />
-  <B value="0.55455" />
-  <C value="0.6619" />
-  <D value="-1.1864" />
-  <E value="0.39235" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="800.01" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="131.35" />
-  <B value="10430" />
-  <C value="-49.252" />
-  <D value="0.10336" />
-  <E value="-0.000081339" />
-  <Tmin units="K"  value="313" />
-  <Tmax units="K"  value="322.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="287690" />
-  <B value="-499.88" />
-  <C value="15.238" />
-  <D value="-0.0020847" />
-  <E value="0.000001614" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="695.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="324210" />
-  <B value="-507.11" />
-  <C value="14.235" />
-  <D value="0.00027032" />
-  <E value="-9.4813E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.94678" />
-  <B value="-319.68" />
-  <C value="-1479.8" />
-  <D value="-4020400" />
-  <E value="8104800" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.337" />
-  <B value="2071.7" />
-  <C value="-0.014083" />
-  <D value="1.056E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="695.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.7943E-07" />
-  <B value="0.60493" />
-  <C value="599.04" />
-  <D value="42458" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.12846" />
-  <B value="8.4662" />
-  <C value="-1.1232" />
-  <D value="-0.00036291" />
-  <E value="-3.8993E-07" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="695.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-177.26" />
-  <B value="1.0676" />
-  <C value="-4.7446E+09" />
-  <D value="-7.2852E+10" />
-  <Tmin units="K"  value="695.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.065365" />
-  <B value="-27.602" />
-  <C value="-1.8659" />
-  <D value="-0.0014826" />
-  <E value="5.6633E-07" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="800.01" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-11687" />
-  <B value="2518.7" />
-  <C value="-1.3794" />
-  <D value="0.00029016" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.746" />
-  <B value="5352.8" />
-  <C value="-170.98" />
-  <Tmin units="K"  value="514.09" />
-  <Tmax units="K"  value="727.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.756" />
-  <B value="-0.0086105" />
-  <Tmin units="K"  value="332.15" />
-  <Tmax units="K"  value="695.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.871975" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.472771E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="173.3321" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.203" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="558.66" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.191283" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.805702" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.21357" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.48815" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="18.6622" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="15.196" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.21357" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15810" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.48815" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="25" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="25" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="25" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="25" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="25" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="25" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="593-49-7" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="81" />
-<CompoundID name="Name"  value="N-octacosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)26CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="843" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="888000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.58" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.2" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="704.75" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="334.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="334.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000104457" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="394.76" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.492645" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.23752" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.033E-09" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15700" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.2933" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="3.934E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.228E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.799E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1255000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6.4643E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.06" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.722E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="2.5213" />
-  <B value="-0.00094263" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="133.74" />
-  <Tmax units="K"  value="334.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.0073167" />
-  <B value="0.055448" />
-  <C value="843" />
-  <D value="0.13236" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="832" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="196.5874" />
-  <B value="-22285.21" />
-  <C value="-23.91336" />
-  <D value="7.155924E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="832" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.0593E+08" />
-  <B value="0.90796" />
-  <C value="0.4061" />
-  <D value="-1.298" />
-  <E value="0.44283" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="832" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-84888" />
-  <B value="5947.6" />
-  <C value="-27.952" />
-  <D value="0.062726" />
-  <E value="-0.0000046784" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="250" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="494250" />
-  <B value="-131.76" />
-  <C value="12.406" />
-  <D value="0.0033619" />
-  <E value="-0.0000018387" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="704.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="335140" />
-  <B value="-505.51" />
-  <C value="14.268" />
-  <D value="0.00027376" />
-  <E value="-9.6008E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="1.7412" />
-  <B value="-1526.5" />
-  <C value="-1143.7" />
-  <D value="-7580800" />
-  <E value="1.9977E+07" />
-  <Tmin units="K"  value="416" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-110.67" />
-  <B value="6750.2" />
-  <C value="14.886" />
-  <D value="-0.000010312" />
-  <E value="2" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="723.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000003028" />
-  <B value="0.58316" />
-  <C value="487.28" />
-  <D value="64252" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0095167" />
-  <B value="-82.828" />
-  <C value="-0.8204" />
-  <D value="-0.0023614" />
-  <E value="5.0131E-07" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="704.75" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-190.77" />
-  <B value="1.0711" />
-  <C value="-5.355E+09" />
-  <D value="-7.036E+10" />
-  <Tmin units="K"  value="704.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.063455" />
-  <B value="-39.315" />
-  <C value="-1.8285" />
-  <D value="-0.0015529" />
-  <E value="5.9113E-07" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="832" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-11108" />
-  <B value="2607.2" />
-  <C value="-1.4263" />
-  <D value="0.00029964" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.188" />
-  <B value="5872" />
-  <C value="-153.33" />
-  <Tmin units="K"  value="508.11" />
-  <Tmax units="K"  value="753.42" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.5887" />
-  <B value="-0.0088828" />
-  <Tmin units="K"  value="334.35" />
-  <Tmax units="K"  value="723.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.897158" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.499321E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="167.6674" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="579.18" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.207041" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.804469" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.152" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.492645" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="19.3366" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="15.736" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.23752" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15700" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.492645" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="26" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="26" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="26" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="26" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="26" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="26" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="630-02-4" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="82" />
-<CompoundID name="Name"  value="N-nonacosane" />
-<StructureFormula name="Structure"  value="CH3(CH2)27CH3" />
-<Family name="Family"  value="1" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="838" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="826000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.69" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.2" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="713.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="339.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="336.85" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000684619" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="408.787" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.523824" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.26531" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.066E-09" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15500" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.30355" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.069E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.435E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.879E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1295000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6.6107E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.22" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.782E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="2.4398" />
-  <B value="-0.00090537" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="134.74" />
-  <Tmax units="K"  value="336.85" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.12857" />
-  <B value="0.23366" />
-  <C value="838" />
-  <D value="0.30121" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="811.62" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-4.241455" />
-  <B value="-11668.64" />
-  <C value="5.534214" />
-  <D value="-8.103778E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="838" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.9213E+08" />
-  <B value="0.53282" />
-  <C value="0.78359" />
-  <D value="-0.96953" />
-  <E value="0.062608" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="811.62" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="7750" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="336.85" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-89782" />
-  <B value="-199.31" />
-  <C value="14.448" />
-  <D value="-0.00027681" />
-  <E value="5.1812E-07" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="713.95" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="383900" />
-  <B value="-568.27" />
-  <C value="14.435" />
-  <D value="0.00012081" />
-  <E value="-4.6695E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="1.0196" />
-  <B value="-209.07" />
-  <C value="-1754" />
-  <D value="-5213400" />
-  <E value="1.0619E+07" />
-  <Tmin units="K"  value="419" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.543" />
-  <B value="2141.6" />
-  <C value="0.0076776" />
-  <D value="-5.4408E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="713.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.7904E-07" />
-  <B value="0.59854" />
-  <C value="575.23" />
-  <D value="50800" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1272" />
-  <B value="8.851" />
-  <C value="-1.1267" />
-  <D value="-0.00035068" />
-  <E value="-3.6961E-07" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="713.95" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-257.69" />
-  <B value="1.0697" />
-  <C value="-7.2501E+09" />
-  <D value="-1.1593E+11" />
-  <Tmin units="K"  value="713.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.067484" />
-  <B value="-24.584" />
-  <C value="-1.877" />
-  <D value="-0.0013532" />
-  <E value="4.7688E-07" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="811.62" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-22489" />
-  <B value="2750.8" />
-  <C value="-1.5436" />
-  <D value="0.00033453" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.591" />
-  <B value="5404.9" />
-  <C value="-176.93" />
-  <Tmin units="K"  value="516.55" />
-  <Tmax units="K"  value="732.49" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.7316" />
-  <B value="-0.0085077" />
-  <Tmin units="K"  value="336.85" />
-  <Tmax units="K"  value="713.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.69" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.533337E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="166.673" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.2" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="599.7" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.207949" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.809984" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.31" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.523824" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="20.011" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="16.276" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.26531" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15500" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.523824" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="27" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="27" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="27" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="27" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="27" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="27" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="630-03-5" />
-<Smiles name="SMILES"  value="CCCCCCCCCCCCCCCCCCCCCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="55" />
-<CompoundID name="Name"  value="Squalane" />
-<StructureFormula name="Structure"  value="((CH3)2CH(C3H6CH(CH3))2C2H4)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="863" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="868000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="1.64" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.198" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="623.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="235.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="235.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.70072E-12" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="422.813" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.526135" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.915303" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.147E-09" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14490" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.31372" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.198E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.896E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.868E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1272000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4.7E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.8" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.85E+10" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="2.5508" />
-  <B value="-0.001356" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="94.06" />
-  <Tmax units="K"  value="235.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.15996" />
-  <B value="0.26223" />
-  <C value="863" />
-  <D value="0.38604" />
-  <Tmin units="K"  value="235.15" />
-  <Tmax units="K"  value="863" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="518.45" />
-  <B value="-40342" />
-  <C value="-70.491" />
-  <D value="0.00002486" />
-  <E value="2" />
-  <Tmin units="K"  value="235.15" />
-  <Tmax units="K"  value="863" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.3274E+08" />
-  <B value="0.38" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="235.15" />
-  <Tmax units="K"  value="863" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="21100" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="235.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-38276" />
-  <B value="-113.46" />
-  <C value="13.728" />
-  <D value="0.001186" />
-  <E value="-3.7363E-07" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="720" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="369830" />
-  <B value="-553.39" />
-  <C value="14.489" />
-  <D value="0.00010319" />
-  <E value="-3.8186E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="1.4043" />
-  <B value="-1190.2" />
-  <C value="-1952.6" />
-  <D value="-3198600" />
-  <E value="3136900" />
-  <Tmin units="K"  value="431.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="118" />
-  <A value="-347.8968" />
-  <B value="71874.9" />
-  <C value="53.72611" />
-  <D value="-0.0000616157" />
-  <E value="1.3" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="720" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.2128E-07" />
-  <B value="0.5436" />
-  <C value="144.2" />
-  <D value="25.787" />
-  <Tmin units="K"  value="235.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.045427" />
-  <B value="7.6198" />
-  <C value="-1.8982" />
-  <D value="-0.00026051" />
-  <E value="-5.9557E-07" />
-  <Tmin units="K"  value="235.15" />
-  <Tmax units="K"  value="720" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000056714" />
-  <B value="1.0625" />
-  <C value="551.79" />
-  <D value="75579" />
-  <Tmin units="K"  value="720" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.068044" />
-  <B value="-20.425" />
-  <C value="-1.8668" />
-  <D value="-0.0015438" />
-  <E value="7.0904E-07" />
-  <Tmin units="K"  value="235.15" />
-  <Tmax units="K"  value="863" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-51533" />
-  <B value="2946.8" />
-  <C value="-1.7001" />
-  <D value="0.00038015" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.512" />
-  <B value="5091.9" />
-  <C value="-151.93" />
-  <Tmin units="K"  value="532.15" />
-  <Tmax units="K"  value="763.87" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="15.101" />
-  <B value="-0.059092" />
-  <Tmin units="K"  value="233.15" />
-  <Tmax units="K"  value="720" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="1.64" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="1.536483E-09" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="165.546" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.198" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="620.22" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.21451" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.810331" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="-0.2" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.526135" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="20.6854" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="16.816" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.915303" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14490" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.526135" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="28" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="28" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="28" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="28" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="28" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="28" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-01-3" />
-<Smiles name="SMILES"  value="CC(C)CCCC(C)CCCC(C)CCCCC(C)CCCC(C)CCCC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="18" />
-<CompoundID name="Name"  value="2-methylhexane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)(CH2)3CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="530.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2730000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.421" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="363.18" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="154.9" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="154.9" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00429886" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1486" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.331" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.167E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07848" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.098E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.9472E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3470000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="420410" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9184000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.021" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.45935E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.913" />
-  <B value="-0.0071489" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="61.96" />
-  <Tmax units="K"  value="154.9" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.4821" />
-  <B value="0.23526" />
-  <C value="530.41" />
-  <D value="0.23824" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="530.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="90.20617" />
-  <B value="-6876.202" />
-  <C value="-10.31895" />
-  <D value="8.219062E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="530.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.861947E+07" />
-  <B value="0.640142" />
-  <C value="-0.832218" />
-  <D value="0.945728" />
-  <E value="-0.370956" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="510.64" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-93650" />
-  <B value="5393.4" />
-  <C value="-66.789" />
-  <D value="0.4004" />
-  <E value="-0.00085798" />
-  <Tmin units="K"  value="60" />
-  <Tmax units="K"  value="154.91" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="142210" />
-  <B value="82.605" />
-  <C value="8.5784" />
-  <D value="0.010085" />
-  <E value="-0.000006336" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="363.2" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="88324" />
-  <B value="-552.27" />
-  <C value="13.044" />
-  <D value="0.00017909" />
-  <E value="-6.2753E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24129" />
-  <B value="-294.06" />
-  <C value="-38.004" />
-  <D value="-4376.2" />
-  <E value="6364" />
-  <Tmin units="K"  value="265" />
-  <Tmax units="K"  value="1931" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.237" />
-  <B value="971.42" />
-  <C value="-0.18335" />
-  <D value="0.0000010057" />
-  <E value="2" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="363.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000041509" />
-  <B value="0.28637" />
-  <C value="700.76" />
-  <D value="14523" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.060786" />
-  <B value="305.44" />
-  <C value="-6.3461" />
-  <D value="0.018265" />
-  <E value="-0.000033419" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="426.33" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000062491" />
-  <B value="1.0749" />
-  <C value="-62.587" />
-  <D value="153720" />
-  <Tmin units="K"  value="363.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013533" />
-  <B value="18.468" />
-  <C value="-3.0315" />
-  <D value="-0.00031495" />
-  <E value="-0.0000041446" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="510.64" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="28702" />
-  <B value="385.57" />
-  <C value="0.45281" />
-  <D value="-0.00082105" />
-  <E value="3.3998E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.843" />
-  <B value="2915.6" />
-  <C value="-50.214" />
-  <Tmin units="K"  value="318.13" />
-  <Tmax units="K"  value="473.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.256" />
-  <B value="-0.015273" />
-  <Tmin units="K"  value="154.9" />
-  <Tmax units="K"  value="363.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425893" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.009769E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="274.9013" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.44187" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0548484" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.682411" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.331" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1486" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1734" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.392" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002745" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.96509" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.331" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14730" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1486" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="591-76-4" />
-<Smiles name="SMILES"  value="CC(C)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="19" />
-<CompoundID name="Name"  value="3-methylhexane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)CH2CH2CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="535.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2810000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.404" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="365" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="153.75" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="153.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00321303" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14674" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.323" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.078E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14950" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07848" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.098E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.9133E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5080000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="425930" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9460000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0009" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.46177E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.934" />
-  <B value="-0.007197" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="61.5" />
-  <Tmax units="K"  value="153.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53784" />
-  <B value="0.24926" />
-  <C value="535.2" />
-  <D value="0.22945" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="535.19" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="86.76736" />
-  <B value="-6773.074" />
-  <C value="-9.77749" />
-  <D value="7.535909E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="535.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.817768E+07" />
-  <B value="1.085699" />
-  <C value="-1.05321" />
-  <D value="0.37877" />
-  <E value="0.0254378" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="515.12" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-60717" />
-  <B value="5410" />
-  <C value="-46.69" />
-  <D value="0.17474" />
-  <E value="-0.00023062" />
-  <Tmin units="K"  value="89.2" />
-  <Tmax units="K"  value="289.2" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="151720" />
-  <B value="437.07" />
-  <C value="3.0907" />
-  <D value="0.032504" />
-  <E value="-0.000034822" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="365" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="80171" />
-  <B value="-511.41" />
-  <C value="12.979" />
-  <D value="0.00025345" />
-  <E value="-8.5984E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24147" />
-  <B value="-297.07" />
-  <C value="-38.97" />
-  <D value="-4831.4" />
-  <E value="7213.9" />
-  <Tmin units="K"  value="267" />
-  <Tmax units="K"  value="1947" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.794" />
-  <B value="999.53" />
-  <C value="0.086997" />
-  <D value="-2.3727E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="365" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.5226E-07" />
-  <B value="0.55481" />
-  <C value="210.53" />
-  <D value="14.061" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.14432" />
-  <B value="11.474" />
-  <C value="-1.2132" />
-  <D value="-0.00022172" />
-  <E value="-0.0000010949" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="425" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000041038" />
-  <B value="1.1288" />
-  <C value="-121.44" />
-  <D value="150080" />
-  <Tmin units="K"  value="365" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014185" />
-  <B value="14.535" />
-  <C value="-2.9491" />
-  <D value="-0.00055881" />
-  <E value="-0.0000037071" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="515.12" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-9515.9" />
-  <B value="684.74" />
-  <C value="-0.35808" />
-  <D value="0.000070956" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.869" />
-  <B value="2945.4" />
-  <C value="-49.691" />
-  <Tmin units="K"  value="325.5" />
-  <Tmax units="K"  value="474.97" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8534" />
-  <B value="-0.016863" />
-  <Tmin units="K"  value="153.75" />
-  <Tmax units="K"  value="365" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425893" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.109797E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="255.2548" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.255" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.35301" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0540085" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.692371" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.323" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14674" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1734" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.392" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002806" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.7712" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.323" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14950" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14674" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="589-34-4" />
-<Smiles name="SMILES"  value="CCC(C)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="20" />
-<CompoundID name="Name"  value="3-ethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH2CH3)CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="540.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2890000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4158" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="366.63" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="154.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="154.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00170947" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1444" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.311" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.943E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15040" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0784799" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.098E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.89661E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.09202E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="411540" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9547890" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.99001" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.4642E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.258" />
-  <B value="-0.0073712" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="61.82" />
-  <Tmax units="K"  value="154.55" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.56112" />
-  <B value="0.24813" />
-  <C value="540.61" />
-  <D value="0.27074" />
-  <Tmin units="K"  value="154.55" />
-  <Tmax units="K"  value="540.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="89.99315" />
-  <B value="-6915.896" />
-  <C value="-10.27777" />
-  <D value="8.039283E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="154.55" />
-  <Tmax units="K"  value="540.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.3257E+07" />
-  <B value="1.2647" />
-  <C value="-2.6729" />
-  <D value="3.1124" />
-  <E value="-1.3109" />
-  <Tmin units="K"  value="154.55" />
-  <Tmax units="K"  value="520.28" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="197190" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="540.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="152590" />
-  <B value="204.56" />
-  <C value="5.9318" />
-  <D value="0.021701" />
-  <E value="-0.000022224" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="300" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="102980" />
-  <B value="-630.04" />
-  <C value="13.15" />
-  <D value="0.000058616" />
-  <E value="-2.6799E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24168" />
-  <B value="-300.63" />
-  <C value="-39.661" />
-  <D value="-8353.5" />
-  <E value="16171" />
-  <Tmin units="K"  value="270.3" />
-  <Tmax units="K"  value="1971.32" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.885" />
-  <B value="1001.1" />
-  <C value="0.10351" />
-  <D value="-0.0000003544" />
-  <E value="2" />
-  <Tmin units="K"  value="154.55" />
-  <Tmax units="K"  value="366.62" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.1521E-07" />
-  <B value="0.52741" />
-  <C value="287.77" />
-  <D value="1840.5" />
-  <Tmin units="K"  value="366.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.055574" />
-  <B value="4.7874" />
-  <C value="-1.5746" />
-  <D value="-0.0003945" />
-  <E value="-0.0000016303" />
-  <Tmin units="K"  value="154.55" />
-  <Tmax units="K"  value="366.62" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000065519" />
-  <B value="1.0691" />
-  <C value="-74.423" />
-  <D value="161360" />
-  <Tmin units="K"  value="366.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012077" />
-  <B value="20.986" />
-  <C value="-3.0408" />
-  <D value="-0.00022974" />
-  <E value="-0.0000045333" />
-  <Tmin units="K"  value="154.55" />
-  <Tmax units="K"  value="520.28" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="63173" />
-  <B value="162.52" />
-  <C value="0.96789" />
-  <D value="-0.0013392" />
-  <E value="0.0000005303" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.873" />
-  <B value="2975.2" />
-  <C value="-48.333" />
-  <Tmin units="K"  value="326.9" />
-  <Tmax units="K"  value="479.64" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9085" />
-  <B value="-0.016578" />
-  <Tmin units="K"  value="154.55" />
-  <Tmax units="K"  value="366.62" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425892" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.792969E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="304.1931" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.36464" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0540613" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.704619" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.311" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1444" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1734" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.392" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.000168" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.76463" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.311" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15040" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1444" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="617-78-7" />
-<Smiles name="SMILES"  value="CCC(CC)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="21" />
-<CompoundID name="Name"  value="2,2-dimethylpentane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2CH2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="520.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2770000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4158" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="352.32" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="149.34" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="149.34" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00317517" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14967" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.287" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.922E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14260" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07847" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.118E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.06146E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="550000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="392580" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5824000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.96525" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.45048E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.9776" />
-  <B value="-0.0074425" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="59.74" />
-  <Tmax units="K"  value="149.34" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.5639" />
-  <B value="0.25328" />
-  <C value="520.51" />
-  <D value="0.25578" />
-  <Tmin units="K"  value="149.34" />
-  <Tmax units="K"  value="520.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="85.15112" />
-  <B value="-6377.959" />
-  <C value="-9.646055" />
-  <D value="8.426861E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="149.34" />
-  <Tmax units="K"  value="520.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.34663E+07" />
-  <B value="0.794603" />
-  <C value="-0.00994342" />
-  <D value="-0.969824" />
-  <E value="0.623819" />
-  <Tmin units="K"  value="149.34" />
-  <Tmax units="K"  value="503" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-151610" />
-  <B value="8029.6" />
-  <C value="-109.32" />
-  <D value="0.68084" />
-  <E value="-0.0014889" />
-  <Tmin units="K"  value="69.95" />
-  <Tmax units="K"  value="149.43" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="129920" />
-  <B value="-35.818" />
-  <C value="9.4637" />
-  <D value="0.0091865" />
-  <E value="-0.0000074351" />
-  <Tmin units="K"  value="149.43" />
-  <Tmax units="K"  value="310" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="80553" />
-  <B value="-507.91" />
-  <C value="12.99" />
-  <D value="0.00027095" />
-  <E value="-7.6982E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25329" />
-  <B value="-290.61" />
-  <C value="-31.592" />
-  <D value="-7598.3" />
-  <E value="14076" />
-  <Tmin units="K"  value="260.25" />
-  <Tmax units="K"  value="1898.25" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-24.348" />
-  <B value="1370.4" />
-  <C value="2.2619" />
-  <D value="-0.0000092505" />
-  <E value="2" />
-  <Tmin units="K"  value="149.34" />
-  <Tmax units="K"  value="352.34" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.1425E-07" />
-  <B value="0.61072" />
-  <C value="160.83" />
-  <D value="5436.3" />
-  <Tmin units="K"  value="352.34" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.052706" />
-  <B value="3.783" />
-  <C value="-1.5822" />
-  <D value="-0.00046167" />
-  <E value="-0.0000017248" />
-  <Tmin units="K"  value="149.34" />
-  <Tmax units="K"  value="352.34" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000010009" />
-  <B value="1.3247" />
-  <C value="-199.43" />
-  <D value="115550" />
-  <Tmin units="K"  value="352.34" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010753" />
-  <B value="30.074" />
-  <C value="-3.2695" />
-  <D value="0.00035683" />
-  <E value="-0.0000056635" />
-  <Tmin units="K"  value="149.34" />
-  <Tmax units="K"  value="500.97" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="10934" />
-  <B value="502.71" />
-  <C value="0.23389" />
-  <D value="-0.00063356" />
-  <E value="2.8552E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.759" />
-  <B value="2846.1" />
-  <C value="-44.131" />
-  <Tmin units="K"  value="313.48" />
-  <Tmax units="K"  value="463.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.8111" />
-  <B value="-0.019605" />
-  <Tmin units="K"  value="149.34" />
-  <Tmax units="K"  value="352.34" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425834" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.823625E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="288.9511" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.266" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.424" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0539877" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.682101" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.287" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14967" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1727" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.472" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.003786" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.86847" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.287" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14260" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14967" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="590-35-2" />
-<Smiles name="SMILES"  value="CC(C)(C)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="22" />
-<CompoundID name="Name"  value="2,3-dimethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)CH(CH3)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="537.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2910000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.393" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="362.91" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14505" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.297" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.917E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14820" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07847" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.097E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.941E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5610000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414550" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.88928" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.45567E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.21" />
-  <B value="-5.0318E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.60743" />
-  <B value="0.26317" />
-  <C value="537.3" />
-  <D value="0.2444" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="537.25" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.051" />
-  <B value="-6444.3" />
-  <C value="-8.9383" />
-  <D value="0.0000069583" />
-  <E value="2" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="537.3" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.686611E+07" />
-  <B value="1.319959" />
-  <C value="-1.914129" />
-  <D value="1.410201" />
-  <E value="-0.377243" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="517.44" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5151" />
-  <B value="688.15" />
-  <C value="37.701" />
-  <D value="-0.85477" />
-  <E value="0.0056064" />
-  <Tmin units="K"  value="11.98" />
-  <Tmax units="K"  value="81.37" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="144370" />
-  <B value="-45.964" />
-  <C value="9.0642" />
-  <D value="0.010184" />
-  <E value="-0.0000082901" />
-  <Tmin units="K"  value="83.99" />
-  <Tmax units="K"  value="385.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33579" />
-  <B value="-324.43" />
-  <C value="12.683" />
-  <D value="0.00063287" />
-  <E value="-2.0243E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24143" />
-  <B value="-309.97" />
-  <C value="-36.759" />
-  <D value="-3835.1" />
-  <E value="5611.3" />
-  <Tmin units="K"  value="268" />
-  <Tmax units="K"  value="1955" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-16.952" />
-  <B value="1255.2" />
-  <C value="0.89405" />
-  <D value="-0.0000015964" />
-  <E value="2" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="362.93" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000005037" />
-  <B value="0.54462" />
-  <C value="227.41" />
-  <D value="8.0354" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.054333" />
-  <B value="2.0859" />
-  <C value="-1.4922" />
-  <D value="-0.00079317" />
-  <E value="-0.0000012037" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="362.93" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000019733" />
-  <B value="1.2301" />
-  <C value="-158.93" />
-  <D value="129950" />
-  <Tmin units="K"  value="362.93" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013919" />
-  <B value="16.742" />
-  <C value="-2.9807" />
-  <D value="-0.00044342" />
-  <E value="-0.0000038565" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="517.44" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-35869" />
-  <B value="804.08" />
-  <C value="-0.53662" />
-  <D value="0.00018516" />
-  <E value="-2.6024E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.174" />
-  <B value="3137.4" />
-  <C value="-38.214" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="537.3" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0645" />
-  <B value="-0.018776" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="362.93" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425834" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.011665E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="259.8926" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.256" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.18338" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0536701" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.699521" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.297" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14505" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1726" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.388" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001338" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.27172" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.297" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14820" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14505" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="565-59-3" />
-<Smiles name="SMILES"  value="CC(C)C(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="23" />
-<CompoundID name="Name"  value="2,4-dimethylpentane" />
-<StructureFormula name="Structure"  value="(CH3)2CHCH2CH(CH3)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="519.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2740000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4175" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="353.62" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="153.908" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="153.912" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0066994" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14995" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.304" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.931E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14290" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07847" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.097E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.0167E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3310000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="397000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6845000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.98683" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.454E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.8066" />
-  <B value="-0.0070643" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="61.56" />
-  <Tmax units="K"  value="153.91" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.49944" />
-  <B value="0.24101" />
-  <C value="519.81" />
-  <D value="0.23086" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="519.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="86.23433" />
-  <B value="-6498.287" />
-  <C value="-9.772628" />
-  <D value="8.133363E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="519.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.636917E+07" />
-  <B value="1.083678" />
-  <C value="-0.919235" />
-  <D value="0.1428" />
-  <E value="0.13605" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="500.54" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12608" />
-  <B value="1762.6" />
-  <C value="-13.048" />
-  <D value="0.063651" />
-  <E value="-0.00007828" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="153.97" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="90283" />
-  <B value="22.117" />
-  <C value="10.293" />
-  <D value="0.0058192" />
-  <E value="-0.0000033296" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="353.64" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66100" />
-  <B value="-427.67" />
-  <C value="12.876" />
-  <D value="0.00036594" />
-  <E value="-1.1245E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24162" />
-  <B value="-300.13" />
-  <C value="-33.208" />
-  <D value="-3009.2" />
-  <E value="4339.2" />
-  <Tmin units="K"  value="259.89" />
-  <Tmax units="K"  value="1898" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.849" />
-  <B value="1204.5" />
-  <C value="0.70216" />
-  <D value="-0.0000021284" />
-  <E value="2" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="353.64" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.8633E-07" />
-  <B value="0.67603" />
-  <C value="100.62" />
-  <D value="-68.047" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.10048" />
-  <B value="3.798" />
-  <C value="-1.3824" />
-  <D value="-0.00040413" />
-  <E value="-0.0000011783" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="353.64" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0002569" />
-  <B value="0.9033" />
-  <C value="147.33" />
-  <D value="182490" />
-  <Tmin units="K"  value="353.64" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012625" />
-  <B value="19.642" />
-  <C value="-3.0872" />
-  <D value="-0.00025299" />
-  <E value="-0.0000045089" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="500.54" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-26049" />
-  <B value="814.18" />
-  <C value="-0.5747" />
-  <D value="0.00020154" />
-  <E value="-2.0786E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.806" />
-  <B value="2858.9" />
-  <C value="-45.57" />
-  <Tmin units="K"  value="314.93" />
-  <Tmax units="K"  value="463.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.3132" />
-  <B value="-0.018947" />
-  <Tmin units="K"  value="153.91" />
-  <Tmax units="K"  value="353.64" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425834" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.863866E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="284.6761" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.265" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.47506" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0543304" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.676494" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.304" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14995" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1726" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.388" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.000811" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.0567" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.304" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14290" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14995" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-08-7" />
-<Smiles name="SMILES"  value="CC(C)CC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="24" />
-<CompoundID name="Name"  value="3,3-dimethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH2C(CH3)2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="536.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2950000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4141" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.274" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="359.19" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="138.7" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="138.7" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000229687" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1454" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.269" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.768E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14530" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07847" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.118E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.0146E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2719600" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="398150" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7066780" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93732" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.45458E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.356" />
-  <B value="-0.0082936" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="55.48" />
-  <Tmax units="K"  value="138.7" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.57981" />
-  <B value="0.25238" />
-  <C value="536.41" />
-  <D value="0.28345" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="536.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="74.58125" />
-  <B value="-6059.883" />
-  <C value="-7.986446" />
-  <D value="6.250113E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="536.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.254E+07" />
-  <B value="1.1834" />
-  <C value="-1.8011" />
-  <D value="1.5275" />
-  <E value="-0.48856" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="515.47" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10707" />
-  <B value="1309.2" />
-  <C value="-1.4394" />
-  <D value="-0.047767" />
-  <E value="0.00027764" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="138.75" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122500" />
-  <B value="86.779" />
-  <C value="8.7861" />
-  <D value="0.0099608" />
-  <E value="-0.0000069264" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="370" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="67595" />
-  <B value="-428.94" />
-  <C value="12.79" />
-  <D value="0.00052141" />
-  <E value="-1.6453E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23671" />
-  <B value="-275.05" />
-  <C value="-39.954" />
-  <D value="-5103.8" />
-  <E value="7728.1" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.1051" />
-  <B value="998.94" />
-  <C value="-0.73694" />
-  <D value="0.0000026961" />
-  <E value="2" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="359.21" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.3561E-07" />
-  <B value="0.48169" />
-  <C value="385.32" />
-  <D value="9.0702" />
-  <Tmin units="K"  value="359.21" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.050708" />
-  <B value="3.465" />
-  <C value="-1.5874" />
-  <D value="-0.00046821" />
-  <E value="-0.000001622" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="359.21" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000069501" />
-  <B value="1.0643" />
-  <C value="-68.32" />
-  <D value="160740" />
-  <Tmin units="K"  value="359.21" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012361" />
-  <B value="17.687" />
-  <C value="-3.0268" />
-  <D value="-0.00037187" />
-  <E value="-0.0000042897" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="515.47" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-3990.9" />
-  <B value="610.41" />
-  <C value="-0.061527" />
-  <D value="-0.00029616" />
-  <E value="1.5149E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.798" />
-  <B value="2942.1" />
-  <C value="-41.889" />
-  <Tmin units="K"  value="325.25" />
-  <Tmax units="K"  value="477.89" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.473" />
-  <B value="-0.020618" />
-  <Tmin units="K"  value="138.7" />
-  <Tmax units="K"  value="359.21" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425834" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.576266E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="331.3011" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.274" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.41501" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0543081" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.696441" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.269" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1454" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1727" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.472" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004779" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.77243" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.269" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14530" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1454" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="562-49-2" />
-<Smiles name="SMILES"  value="CCC(C)(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="25" />
-<CompoundID name="Name"  value="2,2,3-trimethylbutane" />
-<StructureFormula name="Structure"  value="(CH3)3CCH(CH3)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="531.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2950000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3976" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="354.01" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="248.253" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="248.57" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="914.054" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.204" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14615" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.25" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.96E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07846" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.117E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.04765E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4600000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="383340" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2261030" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.90201" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.45223E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.2018" />
-  <B value="-0.0041183" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="99.43" />
-  <Tmax units="K"  value="248.57" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.36152" />
-  <B value="0.20413" />
-  <C value="531.16" />
-  <D value="0.1958" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="531.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="68.92285" />
-  <B value="-5729.492" />
-  <C value="-7.139255" />
-  <D value="5.482993E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="532.22" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.4282E+07" />
-  <B value="0.37696" />
-  <C value="0.13995" />
-  <D value="-0.28638" />
-  <E value="0.1473" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="531.1" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-88737" />
-  <B value="3960" />
-  <C value="-26.907" />
-  <D value="0.088352" />
-  <E value="-0.00010431" />
-  <Tmin units="K"  value="109.37" />
-  <Tmax units="K"  value="248.58" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="95157" />
-  <B value="-51.889" />
-  <C value="10.538" />
-  <D value="0.0057229" />
-  <E value="-0.0000043706" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="354.03" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="64561" />
-  <B value="-425.21" />
-  <C value="12.779" />
-  <D value="0.00055174" />
-  <E value="-1.7221E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.14216" />
-  <B value="-209.59" />
-  <C value="-43.536" />
-  <D value="-1884.6" />
-  <E value="974.47" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="15.143" />
-  <B value="240.01" />
-  <C value="-4.2433" />
-  <D value="0.0000080652" />
-  <E value="2" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="354.03" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.5825E-08" />
-  <B value="0.78963" />
-  <C value="152.98" />
-  <D value="-29510" />
-  <Tmin units="K"  value="343.45" />
-  <Tmax units="K"  value="535.25" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.044619" />
-  <B value="-214.12" />
-  <C value="0.30167" />
-  <D value="-0.0096656" />
-  <E value="0.0000053979" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="354.03" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000030164" />
-  <B value="1.1874" />
-  <C value="-102.65" />
-  <D value="141040" />
-  <Tmin units="K"  value="354.03" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.029346" />
-  <B value="-148.89" />
-  <C value="-1.2217" />
-  <D value="-0.0050964" />
-  <E value="0.0000023937" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="531.1" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5911.6" />
-  <B value="611.63" />
-  <C value="-0.083727" />
-  <D value="-0.00025093" />
-  <E value="1.3162E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.742" />
-  <B value="2891.8" />
-  <C value="-40.291" />
-  <Tmin units="K"  value="320.3" />
-  <Tmax units="K"  value="472.71" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.9222" />
-  <B value="-0.01192" />
-  <Tmin units="K"  value="248.57" />
-  <Tmax units="K"  value="354.03" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.425775" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.722577E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="294.8922" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.266" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.26" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.33657" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0538741" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.694069" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.25" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14615" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.1719" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.468" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.64331" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.25" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14250" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14615" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="464-06-2" />
-<Smiles name="SMILES"  value="CC(C)(C)C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="28" />
-<CompoundID name="Name"  value="2-methylheptane" />
-<StructureFormula name="Structure"  value="(CH3)2CH(CH2)4CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="559.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2480000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4882" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="390.8" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="164.16" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="164.16" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0010587" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16463" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.378" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.57E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15050" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08871" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.233E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.154E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.18E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="459570" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.1878E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0962" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06933E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.7811" />
-  <B value="-0.005901" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="65.66" />
-  <Tmax units="K"  value="164.16" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.40246" />
-  <B value="0.22797" />
-  <C value="559.66" />
-  <D value="0.23428" />
-  <Tmin units="K"  value="164.15" />
-  <Tmax units="K"  value="559.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="97.9971" />
-  <B value="-7746.664" />
-  <C value="-11.37588" />
-  <D value="8.143433E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="164.16" />
-  <Tmax units="K"  value="559.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.657838E+07" />
-  <B value="1.352117" />
-  <C value="-1.871983" />
-  <D value="1.354613" />
-  <E value="-0.391149" />
-  <Tmin units="K"  value="164.16" />
-  <Tmax units="K"  value="544" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18952" />
-  <B value="1822.8" />
-  <C value="-7.7108" />
-  <D value="0.011722" />
-  <E value="0.000030044" />
-  <Tmin units="K"  value="18" />
-  <Tmax units="K"  value="164.19" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66821" />
-  <B value="33.207" />
-  <C value="11.285" />
-  <D value="0.0021902" />
-  <E value="8.6142E-07" />
-  <Tmin units="K"  value="164" />
-  <Tmax units="K"  value="530" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="108850" />
-  <B value="-612.4" />
-  <C value="13.327" />
-  <D value="-0.0000091854" />
-  <E value="-2.9587E-09" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27395" />
-  <B value="-342.75" />
-  <C value="-53.371" />
-  <D value="-19390" />
-  <E value="42045" />
-  <Tmin units="K"  value="279.82" />
-  <Tmax units="K"  value="1785.82" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.3762" />
-  <B value="968.16" />
-  <C value="-0.65227" />
-  <D value="0.0000018143" />
-  <E value="2" />
-  <Tmin units="K"  value="164.16" />
-  <Tmax units="K"  value="423.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.5347E-07" />
-  <B value="0.55194" />
-  <C value="231.19" />
-  <D value="-1256.6" />
-  <Tmin units="K"  value="164.16" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.00038221" />
-  <B value="38.981" />
-  <C value="-2.075" />
-  <D value="0.00062625" />
-  <E value="-0.0000038423" />
-  <Tmin units="K"  value="164.15" />
-  <Tmax units="K"  value="503.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000048089" />
-  <B value="1.0964" />
-  <C value="-142.76" />
-  <D value="170130" />
-  <Tmin units="K"  value="390.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014212" />
-  <B value="12.912" />
-  <C value="-2.9385" />
-  <D value="-0.00062163" />
-  <E value="-0.0000032482" />
-  <Tmin units="K"  value="164.16" />
-  <Tmax units="K"  value="538.88" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="43709" />
-  <B value="342.46" />
-  <C value="0.80975" />
-  <D value="-0.0013047" />
-  <E value="5.4626E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.942" />
-  <B value="3153.9" />
-  <C value="-55.828" />
-  <Tmin units="K"  value="336.84" />
-  <Tmax units="K"  value="503.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8962" />
-  <B value="-0.015367" />
-  <Tmin units="K"  value="164.16" />
-  <Tmax units="K"  value="423.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486909" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.398487E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="286.2166" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.42249" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0616339" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.702794" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.378" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16463" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8478" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.932" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002094" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.83669" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.378" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15050" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16463" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="592-27-8" />
-<Smiles name="SMILES"  value="CC(C)CCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="29" />
-<CompoundID name="Name"  value="3-methylheptane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)(CH2)3CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="563.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2550000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4711" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="392.08" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="152.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="152.6" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000523002" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16278" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.371" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.49E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15180" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08871" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.233E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.1251E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.275E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="465510" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.163E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0872" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.0721E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8888" />
-  <B value="-0.0064444" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="61.04" />
-  <Tmax units="K"  value="152.6" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.48768" />
-  <B value="0.25064" />
-  <C value="563.66" />
-  <D value="0.24544" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="563.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="94.76732" />
-  <B value="-7652.539" />
-  <C value="-10.86325" />
-  <D value="7.450521E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="563.67" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.899021E+07" />
-  <B value="1.39863" />
-  <C value="-1.771662" />
-  <D value="1.093723" />
-  <E value="-0.270846" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="548" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-22283" />
-  <B value="1860.6" />
-  <C value="-6.4838" />
-  <D value="-0.0071294" />
-  <E value="0.00010229" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="152.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="137930" />
-  <B value="50.329" />
-  <C value="9.9028" />
-  <D value="0.0059467" />
-  <E value="-0.0000024618" />
-  <Tmin units="K"  value="107.25" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="103080" />
-  <B value="-583.42" />
-  <C value="13.271" />
-  <D value="0.000052348" />
-  <E value="-2.126E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.32697" />
-  <B value="-423.7" />
-  <C value="-35.42" />
-  <D value="-43617" />
-  <E value="102800" />
-  <Tmin units="K"  value="281.8" />
-  <Tmax units="K"  value="1799.84" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.3817" />
-  <B value="976.23" />
-  <C value="-0.66335" />
-  <D value="0.0000021183" />
-  <E value="2" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="392.08" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000069865" />
-  <B value="0.21161" />
-  <C value="854.03" />
-  <D value="-2592.5" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.043161" />
-  <B value="22.706" />
-  <C value="-1.6829" />
-  <D value="-0.000063735" />
-  <E value="-0.0000020484" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="503.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000042535" />
-  <B value="1.1138" />
-  <C value="-151.71" />
-  <D value="168420" />
-  <Tmin units="K"  value="392.08" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010132" />
-  <B value="18.511" />
-  <C value="-3.0971" />
-  <D value="-0.000087581" />
-  <E value="-0.0000046928" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="541.97" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="950.75" />
-  <B value="729.2" />
-  <C value="-0.35201" />
-  <D value="0.000060241" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.965" />
-  <B value="3188.8" />
-  <C value="-54.285" />
-  <Tmin units="K"  value="342.54" />
-  <Tmax units="K"  value="506" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4083" />
-  <B value="-0.017071" />
-  <Tmin units="K"  value="152.6" />
-  <Tmax units="K"  value="392.08" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486909" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.554483E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="261.2871" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.46447" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.06101" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.709859" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.371" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16278" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8478" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.932" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004039" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.98948" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.371" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15180" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16278" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="589-81-1" />
-<Smiles name="SMILES"  value="CCC(C)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="30" />
-<CompoundID name="Name"  value="4-methylheptane" />
-<StructureFormula name="Structure"  value="CH3(CH2)2CH(CH3)(CH2)2CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="561.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2540000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.476" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="390.86" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="152.19" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="152.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000457034" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16306" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.371" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.52E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0887" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.233E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.1196E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.571E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="457390" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.08E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0902" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.07282E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8808" />
-  <B value="-0.0059952" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="60.88" />
-  <Tmax units="K"  value="152.2" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.41247" />
-  <B value="0.23007" />
-  <C value="561.76" />
-  <D value="0.23229" />
-  <Tmin units="K"  value="152.15" />
-  <Tmax units="K"  value="561.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="97.33843" />
-  <B value="-7742.706" />
-  <C value="-11.25952" />
-  <D value="7.843366E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="152.2" />
-  <Tmax units="K"  value="561.74" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.797167E+07" />
-  <B value="1.151616" />
-  <C value="-0.835173" />
-  <D value="-0.171743" />
-  <E value="0.314726" />
-  <Tmin units="K"  value="152.2" />
-  <Tmax units="K"  value="540.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="561.7" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="123600" />
-  <B value="-18.717" />
-  <C value="11.067" />
-  <D value="0.0020327" />
-  <E value="0.0000016218" />
-  <Tmin units="K"  value="152" />
-  <Tmax units="K"  value="530" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="100250" />
-  <B value="-569.74" />
-  <C value="13.266" />
-  <D value="0.000060406" />
-  <E value="-2.5661E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26872" />
-  <B value="-336.78" />
-  <C value="-55.297" />
-  <D value="-13650" />
-  <E value="26132" />
-  <Tmin units="K"  value="280.85" />
-  <Tmax units="K"  value="1792.87" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.11" />
-  <B value="1066.3" />
-  <C value="-0.039384" />
-  <D value="1.7455E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="152.2" />
-  <Tmax units="K"  value="390.86" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000043616" />
-  <B value="0.27023" />
-  <C value="695.06" />
-  <D value="-2959.1" />
-  <Tmin units="K"  value="152.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.096483" />
-  <B value="12.321" />
-  <C value="-1.3603" />
-  <D value="-0.00031289" />
-  <E value="-0.0000012186" />
-  <Tmin units="K"  value="152.15" />
-  <Tmax units="K"  value="503.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000040274" />
-  <B value="1.1204" />
-  <C value="-164.18" />
-  <D value="166050" />
-  <Tmin units="K"  value="390.86" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015124" />
-  <B value="11.813" />
-  <C value="-2.8959" />
-  <D value="-0.000703" />
-  <E value="-0.0000030068" />
-  <Tmin units="K"  value="152.2" />
-  <Tmax units="K"  value="540.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="18142" />
-  <B value="522.38" />
-  <C value="0.36742" />
-  <D value="-0.00083319" />
-  <E value="3.6234E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.935" />
-  <B value="3153.8" />
-  <C value="-55.685" />
-  <Tmin units="K"  value="341.5" />
-  <Tmax units="K"  value="503.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4371" />
-  <B value="-0.017141" />
-  <Tmin units="K"  value="152.2" />
-  <Tmax units="K"  value="390.86" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486849" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.370341E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="283.3328" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.46166" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0611736" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.710283" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.371" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16306" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8478" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.932" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.00287" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.95432" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.371" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15140" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16306" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="589-53-7" />
-<Smiles name="SMILES"  value="CCCC(C)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="31" />
-<CompoundID name="Name"  value="3-ethylhexane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(C2H5)CH2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="565.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2610000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4605" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="391.69" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16101" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.362" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.571E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15210" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08871" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.233E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.10874E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.68615E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="457860" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.02158" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.07398E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.46" />
-  <B value="-2.5002E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.46206" />
-  <B value="0.24436" />
-  <C value="565.51" />
-  <D value="0.22747" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="565.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="97.09596" />
-  <B value="-7733.566" />
-  <C value="-11.22583" />
-  <D value="7.810756E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="565.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.4799E+07" />
-  <B value="0.26737" />
-  <C value="0.81877" />
-  <D value="-1.2904" />
-  <E value="0.59915" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="550.05" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="565.4" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="80628" />
-  <B value="-64.909" />
-  <C value="11.186" />
-  <D value="0.0048319" />
-  <E value="-0.0000040172" />
-  <Tmin units="K"  value="166.11" />
-  <Tmax units="K"  value="391.69" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115160" />
-  <B value="-618.28" />
-  <C value="13.279" />
-  <D value="0.0000464" />
-  <E value="-2.6202E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27373" />
-  <B value="-345.24" />
-  <C value="-56.178" />
-  <D value="-8141.6" />
-  <E value="10145" />
-  <Tmin units="K"  value="282.7" />
-  <Tmax units="K"  value="1806.7" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.8742" />
-  <B value="897.68" />
-  <C value="-0.5066" />
-  <D value="2.0784E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="391.69" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.7627E-07" />
-  <B value="0.57415" />
-  <C value="196.9" />
-  <D value="-172.94" />
-  <Tmin units="K"  value="391.69" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.001637" />
-  <B value="-138.28" />
-  <C value="-0.62782" />
-  <D value="-0.0040963" />
-  <E value="8.9774E-07" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="391.69" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000056588" />
-  <B value="1.0789" />
-  <C value="-123.05" />
-  <D value="173090" />
-  <Tmin units="K"  value="391.69" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.044466" />
-  <B value="-81.024" />
-  <C value="-1.6153" />
-  <D value="-0.0032549" />
-  <E value="0.0000014934" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="550.05" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="59681" />
-  <B value="280.36" />
-  <C value="0.8618" />
-  <D value="-0.0012731" />
-  <E value="5.0619E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.025" />
-  <B value="3214.3" />
-  <C value="-53.307" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="565.5" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.7324" />
-  <B value="-0.010064" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="391.69" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486909" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.497393E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="262.1216" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0603593" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.716248" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.362" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16101" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8478" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.932" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.362" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15210" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16101" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="4" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="619-99-8" />
-<Smiles name="SMILES"  value="CCC(CC)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="32" />
-<CompoundID name="Name"  value="2,2-dimethylhexane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2CH2CH2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="549.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2530000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.478" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="379.99" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="151.97" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="151.97" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000215228" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16529" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.339" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.392E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14580" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.253E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.24723E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.0711E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="432710" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6778080" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0429" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06247E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8856" />
-  <B value="-0.0064827" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="60.79" />
-  <Tmax units="K"  value="151.97" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54681" />
-  <B value="0.26386" />
-  <C value="549.8" />
-  <D value="0.27774" />
-  <Tmin units="K"  value="151.97" />
-  <Tmax units="K"  value="549.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="94.06922" />
-  <B value="-7328.821" />
-  <C value="-10.84298" />
-  <D value="7.99047E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="151.97" />
-  <Tmax units="K"  value="549.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.211522E+07" />
-  <B value="1.000418" />
-  <C value="-0.588989" />
-  <D value="-0.277913" />
-  <E value="0.313577" />
-  <Tmin units="K"  value="151.97" />
-  <Tmax units="K"  value="549.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="549.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="125360" />
-  <B value="373.89" />
-  <C value="5.844" />
-  <D value="0.022419" />
-  <E value="-0.00002308" />
-  <Tmin units="K"  value="192.43" />
-  <Tmax units="K"  value="379.99" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97647" />
-  <B value="-528.4" />
-  <C value="13.112" />
-  <D value="0.00027844" />
-  <E value="-9.0187E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2681" />
-  <B value="-314.72" />
-  <C value="-51.398" />
-  <D value="-8276.4" />
-  <E value="13167" />
-  <Tmin units="K"  value="274.9" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.328" />
-  <B value="1166.6" />
-  <C value="-0.039718" />
-  <D value="2.6889E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="151.97" />
-  <Tmax units="K"  value="379.99" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000018535" />
-  <B value="0.38476" />
-  <C value="528.24" />
-  <D value="78.686" />
-  <Tmin units="K"  value="379.99" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.03878" />
-  <B value="5.2314" />
-  <C value="-1.6985" />
-  <D value="-0.00038448" />
-  <E value="-0.000001806" />
-  <Tmin units="K"  value="151.97" />
-  <Tmax units="K"  value="379.99" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000045965" />
-  <B value="1.1142" />
-  <C value="-113.91" />
-  <D value="162780" />
-  <Tmin units="K"  value="379.99" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011295" />
-  <B value="24.139" />
-  <C value="-3.1748" />
-  <D value="0.000033195" />
-  <E value="-0.0000045811" />
-  <Tmin units="K"  value="151.97" />
-  <Tmax units="K"  value="549.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="28702" />
-  <B value="459.14" />
-  <C value="0.50436" />
-  <D value="-0.00093712" />
-  <E value="3.9344E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.822" />
-  <B value="3046.8" />
-  <C value="-52.24" />
-  <Tmin units="K"  value="331.23" />
-  <Tmax units="K"  value="490.14" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.7156" />
-  <B value="-0.019243" />
-  <Tmin units="K"  value="151.97" />
-  <Tmax units="K"  value="379.99" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.180576E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="301.1639" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.265" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.47174" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.061412" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.700157" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.339" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16529" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8471" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.012" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000599" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.0203" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.339" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14580" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16529" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="590-73-8" />
-<Smiles name="SMILES"  value="CC(C)(C)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="33" />
-<CompoundID name="Name"  value="2,3-dimethylhexane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CH(CH3)CH2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="563.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2630000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4682" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="388.76" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16131" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.347" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.363E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15020" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.232E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.13886E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.50206E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="451960" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0586" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.07176E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.46" />
-  <B value="-2.5002E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.48655" />
-  <B value="0.24924" />
-  <C value="563.43" />
-  <D value="0.24533" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="563.42" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="106.31" />
-  <B value="-8083.9" />
-  <C value="-12.636" />
-  <D value="0.000008991" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="563.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.5877E+07" />
-  <B value="0.44475" />
-  <C value="0.4503" />
-  <D value="-0.98905" />
-  <E value="0.49662" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="548.16" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="563.4" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-256410" />
-  <B value="53.354" />
-  <C value="11.988" />
-  <D value="0.00458" />
-  <E value="-0.0000045457" />
-  <Tmin units="K"  value="138.5" />
-  <Tmax units="K"  value="388.76" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="55247" />
-  <B value="-379.2" />
-  <C value="12.913" />
-  <D value="0.00048944" />
-  <E value="-1.5722E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27351" />
-  <B value="-363.66" />
-  <C value="-49.524" />
-  <D value="-11049" />
-  <E value="21772" />
-  <Tmin units="K"  value="281.7" />
-  <Tmax units="K"  value="1799.7" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="8.0389" />
-  <B value="480.9" />
-  <C value="-3.1555" />
-  <D value="0.0000074225" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="388.76" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.4497E-07" />
-  <B value="0.56168" />
-  <C value="244.71" />
-  <D value="41.585" />
-  <Tmin units="K"  value="388.76" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0041864" />
-  <B value="-133.36" />
-  <C value="-0.65326" />
-  <D value="-0.003975" />
-  <E value="8.3867E-07" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="388.76" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000025619" />
-  <B value="1.1862" />
-  <C value="-177.9" />
-  <D value="153600" />
-  <Tmin units="K"  value="388.76" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="106" />
-  <A value="0.05024" />
-  <B value="1.1882" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="563.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-29882" />
-  <B value="839.62" />
-  <C value="-0.40575" />
-  <D value="-0.000028435" />
-  <E value="6.5601E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.01" />
-  <B value="3204.6" />
-  <C value="-50.852" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="563.5" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.8925" />
-  <B value="-0.0092431" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="388.76" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.196288E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="300.3107" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.263" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.50585" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0607317" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.715524" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.347" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16131" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.847" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.928" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002424" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.0396" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.347" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15020" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16131" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="584-94-1" />
-<Smiles name="SMILES"  value="CC(C)C(C)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="34" />
-<CompoundID name="Name"  value="2,4-dimethylhexane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CH2CH(CH3)CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="553.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2560000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.472" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="382.58" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16408" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.344" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.267E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14650" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.232E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.19409E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.17152E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="447600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0474" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06733E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.32" />
-  <B value="-8.5435E-17" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.49412" />
-  <B value="0.25086" />
-  <C value="553.5" />
-  <D value="0.26728" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="553.45" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="110.28" />
-  <B value="-8135.7" />
-  <C value="-13.268" />
-  <D value="0.0000097316" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="553.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.4006E+07" />
-  <B value="0.43973" />
-  <C value="0.30966" />
-  <D value="-0.70429" />
-  <E value="0.35515" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="538.69" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="553.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-373730" />
-  <B value="38.479" />
-  <C value="12.478" />
-  <D value="0.0035274" />
-  <E value="-0.0000034858" />
-  <Tmin units="K"  value="137.68" />
-  <Tmax units="K"  value="382.58" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68028" />
-  <B value="-390.94" />
-  <C value="12.9" />
-  <D value="0.00049032" />
-  <E value="-1.6117E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27345" />
-  <B value="-357.14" />
-  <C value="-46.872" />
-  <D value="-11112" />
-  <E value="22737" />
-  <Tmin units="K"  value="276.75" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.459" />
-  <B value="1208.2" />
-  <C value="0.16649" />
-  <D value="-2.1296E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="382.58" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000013835" />
-  <B value="0.41886" />
-  <C value="453.95" />
-  <D value="-1216.3" />
-  <Tmin units="K"  value="382.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.012272" />
-  <B value="-146.3" />
-  <C value="-0.49024" />
-  <D value="-0.0043592" />
-  <E value="0.0000013669" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="382.58" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000028277" />
-  <B value="1.1747" />
-  <C value="-150.01" />
-  <D value="140960" />
-  <Tmin units="K"  value="382.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.040538" />
-  <B value="-89.906" />
-  <C value="-1.6196" />
-  <D value="-0.0034572" />
-  <E value="0.0000015869" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="553.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-28036" />
-  <B value="903.33" />
-  <C value="-0.60421" />
-  <D value="0.00018092" />
-  <E value="-8.5639E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.948" />
-  <B value="3123.7" />
-  <C value="-51.012" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="553.5" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.1397" />
-  <B value="-0.011142" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="382.58" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.215704E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="295.0337" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.263" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.46325" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0616382" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.701075" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.344" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16408" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.847" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.928" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001943" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.99872" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.344" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14650" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16408" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="589-43-5" />
-<Smiles name="SMILES"  value="CC(C)CC(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="35" />
-<CompoundID name="Name"  value="2,5-dimethylhexane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CH2CH2CH(CH3)CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="550" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2490000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.482" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.262" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="382.26" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="182" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="182" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0683715" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1657" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.357" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.452E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14740" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.232E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.22631E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.046E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="442330" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.29537E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0696" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06398E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.6373" />
-  <B value="-0.0052793" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72.8" />
-  <Tmax units="K"  value="182" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.49779" />
-  <B value="0.2525" />
-  <C value="550" />
-  <D value="0.26429" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="550" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="87.65473" />
-  <B value="-7122.285" />
-  <C value="-9.843559" />
-  <D value="7.04047E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="550" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.2389E+07" />
-  <B value="1.0017" />
-  <C value="-0.72582" />
-  <D value="-0.024698" />
-  <E value="0.19155" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="550" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="550" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-51796" />
-  <B value="-110.09" />
-  <C value="12.759" />
-  <D value="0.00089408" />
-  <E value="-0.0000004354" />
-  <Tmin units="K"  value="208.7" />
-  <Tmax units="K"  value="382.26" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66542" />
-  <B value="-399.08" />
-  <C value="12.9" />
-  <D value="0.00049831" />
-  <E value="-1.6255E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27338" />
-  <B value="-354.69" />
-  <C value="-46.241" />
-  <D value="-8382" />
-  <E value="15583" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-2.9399" />
-  <B value="836.45" />
-  <C value="-1.3966" />
-  <D value="0.00000447" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="382.26" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.3872E-07" />
-  <B value="0.47833" />
-  <C value="344.26" />
-  <D value="27.957" />
-  <Tmin units="K"  value="382.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.074336" />
-  <B value="3.6543" />
-  <C value="-1.5091" />
-  <D value="-0.00039812" />
-  <E value="-0.0000013255" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="382.26" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000029331" />
-  <B value="1.1695" />
-  <C value="-138.07" />
-  <D value="145330" />
-  <Tmin units="K"  value="382.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0092168" />
-  <B value="46.652" />
-  <C value="-3.4804" />
-  <D value="0.0011019" />
-  <E value="-0.0000063095" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="550" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11366" />
-  <B value="725.73" />
-  <C value="-0.14958" />
-  <D value="-0.00027795" />
-  <E value="0.0000001544" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.777" />
-  <B value="3002.6" />
-  <C value="-57.773" />
-  <Tmin units="K"  value="333.13" />
-  <Tmax units="K"  value="491.89" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.9193" />
-  <B value="-0.01228" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="382.26" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.299601E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="289.1748" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.262" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.48407" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0616138" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.698238" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.357" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1657" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.847" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.928" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001621" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.0187" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.357" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14740" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1657" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="592-13-2" />
-<Smiles name="SMILES"  value="CC(C)CCC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="36" />
-<CompoundID name="Name"  value="3,3-dimethylhexane" />
-<StructureFormula name="Structure"  value="CH3CH2C(CH3)2CH2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="562" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2650000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4428" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="385.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="147.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="147.05" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000473645" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.16181" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.32" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.717E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14880" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.253E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.2012E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.32633E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="438230" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7112800" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.9621" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.06682E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9019" />
-  <B value="-0.006722" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="58.82" />
-  <Tmax units="K"  value="147.05" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.45959" />
-  <B value="0.24567" />
-  <C value="562" />
-  <D value="0.21162" />
-  <Tmin units="K"  value="147.05" />
-  <Tmax units="K"  value="561.95" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="109.95" />
-  <B value="-8119.3" />
-  <C value="-13.232" />
-  <D value="0.0000097251" />
-  <E value="2" />
-  <Tmin units="K"  value="147.05" />
-  <Tmax units="K"  value="562" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.8755E+07" />
-  <B value="0.81257" />
-  <C value="-0.27217" />
-  <D value="-0.51422" />
-  <E value="0.40803" />
-  <Tmin units="K"  value="147.05" />
-  <Tmax units="K"  value="540.16" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="562" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="130950" />
-  <B value="-54.41" />
-  <C value="9.7102" />
-  <D value="0.0098373" />
-  <E value="-0.0000089507" />
-  <Tmin units="K"  value="226.41" />
-  <Tmax units="K"  value="385.12" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="73854" />
-  <B value="-426.62" />
-  <C value="12.974" />
-  <D value="0.00044554" />
-  <E value="-1.4645E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26895" />
-  <B value="-323.28" />
-  <C value="-54.431" />
-  <D value="-10397" />
-  <E value="17361" />
-  <Tmin units="K"  value="281" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.0202" />
-  <B value="924.42" />
-  <C value="-0.69061" />
-  <D value="0.0000021821" />
-  <E value="2" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="385.12" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9286E-07" />
-  <B value="0.65784" />
-  <C value="75.166" />
-  <D value="8686.9" />
-  <Tmin units="K"  value="385.12" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.074777" />
-  <B value="3.6654" />
-  <C value="-1.4953" />
-  <D value="-0.00045709" />
-  <E value="-0.000001113" />
-  <Tmin units="K"  value="147.05" />
-  <Tmax units="K"  value="385.12" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000028072" />
-  <B value="1.1786" />
-  <C value="-168.43" />
-  <D value="151580" />
-  <Tmin units="K"  value="385.12" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013471" />
-  <B value="13.363" />
-  <C value="-2.98" />
-  <D value="-0.00049832" />
-  <E value="-0.0000034578" />
-  <Tmin units="K"  value="147.05" />
-  <Tmax units="K"  value="540.16" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-17402" />
-  <B value="785.55" />
-  <C value="-0.23347" />
-  <D value="-0.00023372" />
-  <E value="1.5099E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.871" />
-  <B value="3143.9" />
-  <C value="-48.698" />
-  <Tmin units="K"  value="343.14" />
-  <Tmax units="K"  value="503.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4713" />
-  <B value="-0.013535" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="385.12" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.470891E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="253.2065" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.251" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0599069" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.713866" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.32" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.16181" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8471" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.012" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001728" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.32" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14880" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.16181" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="563-16-6" />
-<Smiles name="SMILES"  value="CCC(C)(C)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="37" />
-<CompoundID name="Name"  value="3,4-dimethylhexane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)CH(CH3)CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="568.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2690000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4588" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="390.88" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15973" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.338" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.23E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.232E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.13007E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.674E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="451580" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0404" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.07251E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.54" />
-  <B value="-6.8305E-18" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.45439" />
-  <B value="0.24011" />
-  <C value="568.8" />
-  <D value="0.23618" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="568.78" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="93.68625" />
-  <B value="-7521.509" />
-  <C value="-10.73445" />
-  <D value="7.52569E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="568.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.4702E+07" />
-  <B value="0.45918" />
-  <C value="0.1856" />
-  <D value="-0.51513" />
-  <E value="0.26338" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="553.18" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="568.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-327870" />
-  <B value="47.226" />
-  <C value="12.229" />
-  <D value="0.0041484" />
-  <E value="-0.000004128" />
-  <Tmin units="K"  value="138.78" />
-  <Tmax units="K"  value="390.88" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="34075" />
-  <B value="-331.34" />
-  <C value="12.881" />
-  <D value="0.00054108" />
-  <E value="-1.7153E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27419" />
-  <B value="-368.34" />
-  <C value="-50.667" />
-  <D value="-11826" />
-  <E value="23331" />
-  <Tmin units="K"  value="284.4" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-41.742" />
-  <B value="2125.1" />
-  <C value="4.8163" />
-  <D value="-0.0000056466" />
-  <E value="2" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="390.88" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.4152E-07" />
-  <B value="0.51789" />
-  <C value="310.46" />
-  <D value="157.69" />
-  <Tmin units="K"  value="390.88" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0004002" />
-  <B value="-144.47" />
-  <C value="-0.57247" />
-  <D value="-0.0042745" />
-  <E value="0.0000010836" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="390.88" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000020807" />
-  <B value="1.2133" />
-  <C value="-200.76" />
-  <D value="152640" />
-  <Tmin units="K"  value="390.88" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.064052" />
-  <B value="-52.814" />
-  <C value="-1.681" />
-  <D value="-0.0023574" />
-  <E value="0.0000011157" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="553.18" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-51117" />
-  <B value="968.82" />
-  <C value="-0.69434" />
-  <D value="0.00024619" />
-  <E value="-2.8602E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.796538" />
-  <B value="-1200" />
-  <C value="-7.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.996" />
-  <B value="3219" />
-  <C value="-50.972" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="568.8" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.9827" />
-  <B value="-0.0089632" />
-  <Tmin units="K"  value="272.04" />
-  <Tmax units="K"  value="390.88" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.083117E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="311.5716" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.265" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.44525" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0603305" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.723382" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.338" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15973" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.847" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.928" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001744" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.91017" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.338" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15140" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15973" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="583-48-2" />
-<Smiles name="SMILES"  value="CCC(C)C(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="38" />
-<CompoundID name="Name"  value="2-methyl-3-ethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)CH(CH2CH3)CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="567" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2700000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4453" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="388.81" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="158.2" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="158.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000447428" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15972" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.331" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.181E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.232E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.11208E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.87861E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="443760" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.13386E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97631" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.07477E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9908" />
-  <B value="-0.0063143" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="63.28" />
-  <Tmax units="K"  value="158.2" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54567" />
-  <B value="0.26412" />
-  <C value="567.03" />
-  <D value="0.24308" />
-  <Tmin units="K"  value="158.2" />
-  <Tmax units="K"  value="567.02" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="92.12933" />
-  <B value="-7403.468" />
-  <C value="-10.51119" />
-  <D value="7.396006E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="158.2" />
-  <Tmax units="K"  value="567.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.9697E+07" />
-  <B value="0.73134" />
-  <C value="0.033175" />
-  <D value="-0.91459" />
-  <E value="0.58962" />
-  <Tmin units="K"  value="158.2" />
-  <Tmax units="K"  value="545.58" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="567" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="11076" />
-  <B value="-131.1" />
-  <C value="12.479" />
-  <D value="0.0013888" />
-  <E value="-7.3844E-07" />
-  <Tmin units="K"  value="173.57" />
-  <Tmax units="K"  value="388.8" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86476" />
-  <B value="-441" />
-  <C value="12.894" />
-  <D value="0.00051253" />
-  <E value="-1.9205E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2727" />
-  <B value="-363.94" />
-  <C value="-51.79" />
-  <D value="-4127.4" />
-  <E value="2402.8" />
-  <Tmin units="K"  value="283.5" />
-  <Tmax units="K"  value="1813.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.931" />
-  <B value="1059.8" />
-  <C value="-0.066598" />
-  <D value="1.3283E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="158.2" />
-  <Tmax units="K"  value="388.8" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.6587E-07" />
-  <B value="0.52506" />
-  <C value="255.1" />
-  <D value="-76.481" />
-  <Tmin units="K"  value="388.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.069311" />
-  <B value="4.0311" />
-  <C value="-1.5221" />
-  <D value="-0.00039448" />
-  <E value="-0.0000012799" />
-  <Tmin units="K"  value="158.2" />
-  <Tmax units="K"  value="388.8" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000026967" />
-  <B value="1.1845" />
-  <C value="-133.92" />
-  <D value="140280" />
-  <Tmin units="K"  value="388.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013529" />
-  <B value="15.88" />
-  <C value="-2.9699" />
-  <D value="-0.00045495" />
-  <E value="-0.0000035111" />
-  <Tmin units="K"  value="158.2" />
-  <Tmax units="K"  value="545.58" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-7258.5" />
-  <B value="791.48" />
-  <C value="-0.44225" />
-  <D value="0.000098111" />
-  <E value="0" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.899" />
-  <B value="3165.8" />
-  <C value="-51.044" />
-  <Tmin units="K"  value="343.26" />
-  <Tmax units="K"  value="503.21" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.6297" />
-  <B value="-0.016398" />
-  <Tmin units="K"  value="158.2" />
-  <Tmax units="K"  value="388.8" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.378964E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="266.623" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0599464" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.723932" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.331" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15972" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.847" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.928" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002499" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.331" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15140" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15972" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="609-26-7" />
-<Smiles name="SMILES"  value="CC(C)C(CC)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="39" />
-<CompoundID name="Name"  value="3-methyl-3-ethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH2C(CH3)(CH2CH3)CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="576.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2810000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4551" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="391.42" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="182.28" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="182.28" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0625263" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15788" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.305" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.928E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15060" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0886999" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.253E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.1485E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.288E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="432960" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.08E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93763" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.0716E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9635" />
-  <B value="-0.0054551" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72.91" />
-  <Tmax units="K"  value="182.28" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.59884" />
-  <B value="0.27253" />
-  <C value="576.5" />
-  <D value="0.28169" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="576.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="85.77668" />
-  <B value="-7097.92" />
-  <C value="-9.572218" />
-  <D value="6.70781E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="576.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.3775E+07" />
-  <B value="1.5194" />
-  <C value="-2.4569" />
-  <D value="2.0687" />
-  <E value="-0.69375" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="576.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="223200" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="576.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="77769" />
-  <B value="172.95" />
-  <C value="9.182" />
-  <D value="0.01021" />
-  <E value="-0.0000086615" />
-  <Tmin units="K"  value="201.78" />
-  <Tmax units="K"  value="381.78" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="89715" />
-  <B value="-509.11" />
-  <C value="13.135" />
-  <D value="0.00024858" />
-  <E value="-7.767E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28104" />
-  <B value="-352.27" />
-  <C value="-50.671" />
-  <D value="-6199.9" />
-  <E value="-111.85" />
-  <Tmin units="K"  value="249" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-18.59" />
-  <B value="1270.3" />
-  <C value="1.2467" />
-  <D value="-0.0000036226" />
-  <E value="2" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="391.42" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.5822E-07" />
-  <B value="0.50218" />
-  <C value="361.22" />
-  <D value="-3635.6" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.037427" />
-  <B value="7.7785" />
-  <C value="-1.7161" />
-  <D value="-0.00028317" />
-  <E value="-0.0000017728" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="391.42" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000021773" />
-  <B value="1.2197" />
-  <C value="-136.64" />
-  <D value="138470" />
-  <Tmin units="K"  value="391.42" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010536" />
-  <B value="39.464" />
-  <C value="-3.2983" />
-  <D value="0.00058327" />
-  <E value="-0.0000050348" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="576.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11225" />
-  <B value="736.53" />
-  <C value="-0.16305" />
-  <D value="-0.00026099" />
-  <E value="1.4875E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.91" />
-  <B value="3242" />
-  <C value="-45.986" />
-  <Tmin units="K"  value="348.27" />
-  <Tmax units="K"  value="514.25" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9795" />
-  <B value="-0.014829" />
-  <Tmin units="K"  value="182.28" />
-  <Tmax units="K"  value="391.42" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486848" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.000576E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="324.4539" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0603583" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.731726" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.305" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15788" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8471" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.012" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.004598" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.305" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15060" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15788" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="3" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1067-08-9" />
-<Smiles name="SMILES"  value="CCC(C)(CC)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="44" />
-<CompoundID name="Name"  value="2,2,3,3-tetramethylbutane" />
-<StructureFormula name="Structure"  value="(CH3)3CC(CH3)3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="567.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2870000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.482" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.28" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="379.44" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="373.84" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="373.96" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="86930.2" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.231" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13902" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.248" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.8146E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="12790" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08868" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.272E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.256E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.223E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="389360" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7540000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.85792" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.0558E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.4225" />
-  <B value="-0.0044705" />
-  <C value="0.0035846" />
-  <D value="-0.0000082784" />
-  <E value="7.021E-09" />
-  <Tmin units="K"  value="183.15" />
-  <Tmax units="K"  value="373.96" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61397" />
-  <B value="0.27674" />
-  <C value="567.8" />
-  <D value="0.28198" />
-  <Tmin units="K"  value="367.55" />
-  <Tmax units="K"  value="557.79" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="120.66" />
-  <B value="-8500.6" />
-  <C value="-14.863" />
-  <D value="0.000010649" />
-  <E value="2" />
-  <Tmin units="K"  value="373.96" />
-  <Tmax units="K"  value="568" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.3062E+07" />
-  <B value="0.30484" />
-  <C value="0.85323" />
-  <D value="-1.2161" />
-  <E value="0.48282" />
-  <Tmin units="K"  value="373.96" />
-  <Tmax units="K"  value="557.79" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-145070" />
-  <B value="3783.4" />
-  <C value="-18.811" />
-  <D value="0.04824" />
-  <E value="-0.000044479" />
-  <Tmin units="K"  value="130.05" />
-  <Tmax units="K"  value="365.79" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="239620" />
-  <B value="55.905" />
-  <C value="3.1054" />
-  <D value="0.027363" />
-  <E value="-0.000020376" />
-  <Tmin units="K"  value="373.96" />
-  <Tmax units="K"  value="426" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="73914" />
-  <B value="-415.76" />
-  <C value="12.897" />
-  <D value="0.00056384" />
-  <E value="-1.6707E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27451" />
-  <B value="-340.85" />
-  <C value="-44.213" />
-  <D value="-18.617" />
-  <E value="-11352" />
-  <Tmin units="K"  value="284" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-17.538" />
-  <B value="1603.5" />
-  <C value="0.8804" />
-  <D value="-0.0000034564" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="454" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.9099E-07" />
-  <B value="0.51128" />
-  <C value="412.18" />
-  <D value="-5389.1" />
-  <Tmin units="K"  value="373.96" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0058143" />
-  <B value="-354.88" />
-  <C value="0.79351" />
-  <D value="-0.0067293" />
-  <E value="0.0000023134" />
-  <Tmin units="K"  value="373.96" />
-  <Tmax units="K"  value="426" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000012508" />
-  <B value="1.3068" />
-  <C value="-132.52" />
-  <D value="121650" />
-  <Tmin units="K"  value="379.44" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0045024" />
-  <B value="622.88" />
-  <C value="-8.8445" />
-  <D value="0.017204" />
-  <E value="-0.000023129" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="557.79" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6385.5" />
-  <B value="606.54" />
-  <C value="0.13794" />
-  <D value="-0.00052564" />
-  <E value="2.3996E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.509" />
-  <B value="2922.6" />
-  <C value="-54.055" />
-  <Tmin units="K"  value="374" />
-  <Tmax units="K"  value="506.72" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.2178" />
-  <B value="-0.011395" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="454" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.486727" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.740172E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="379.208" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.28" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="168.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0605327" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.726041" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.248" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.13902" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8456" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.088" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.035734" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.248" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="12790" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.13902" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="4"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="6" />
-  <group id="4"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="6" />
-  <group id="4"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="6" />
-  <group id="4"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="6" />
-  <group id="4"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="4"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="594-82-1" />
-<Smiles name="SMILES"  value="CC(C)(C)C(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="47" />
-<CompoundID name="Name"  value="2,2,5-trimethylhexane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2CH2CH2CH(CH3)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="568.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2330000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.519" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="397.24" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="167.39" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="167.39" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000968629" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.255" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.18225" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.3571" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.658E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14380" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09892" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.387E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.533E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.38E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="461700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6200000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.047" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.66643E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.9031" />
-  <B value="-0.0051346" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="66.96" />
-  <Tmax units="K"  value="167.39" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.45081" />
-  <B value="0.25256" />
-  <C value="569.81" />
-  <D value="0.27357" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="569.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="133.84" />
-  <B value="-9023.578" />
-  <C value="-17.08913" />
-  <D value="0.0000169305" />
-  <E value="2" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="569.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.039801E+07" />
-  <B value="1.702411" />
-  <C value="-1.574913" />
-  <D value="0.0056916" />
-  <E value="0.373292" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="548.62" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="568.05" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84566" />
-  <B value="233.86" />
-  <C value="8.46" />
-  <D value="0.013452" />
-  <E value="-0.000012421" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="397.24" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="102010" />
-  <B value="-531.68" />
-  <C value="13.312" />
-  <D value="0.00017105" />
-  <E value="-4.7837E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30277" />
-  <B value="-381.25" />
-  <C value="-61.035" />
-  <D value="-9428.8" />
-  <E value="13429" />
-  <Tmin units="K"  value="247.39" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.084" />
-  <B value="1011.7" />
-  <C value="0.13186" />
-  <D value="-0.000000312" />
-  <E value="2" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="397.24" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.7588E-07" />
-  <B value="0.49876" />
-  <C value="301.49" />
-  <D value="-1437" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.13721" />
-  <B value="56.65" />
-  <C value="-1.9542" />
-  <D value="0.0024543" />
-  <E value="-0.0000043702" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="397.24" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000030176" />
-  <B value="1.1642" />
-  <C value="-156.95" />
-  <D value="161470" />
-  <Tmin units="K"  value="397.24" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010292" />
-  <B value="28.787" />
-  <C value="-3.249" />
-  <D value="0.00020541" />
-  <E value="-0.0000047205" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="548.62" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-11256" />
-  <B value="868.51" />
-  <C value="-0.4353" />
-  <D value="0.000083238" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.61" />
-  <B value="3036.5" />
-  <C value="-62.963" />
-  <Tmin units="K"  value="341.8" />
-  <Tmax units="K"  value="506.26" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.5103" />
-  <B value="-0.014267" />
-  <Tmin units="K"  value="167.39" />
-  <Tmax units="K"  value="397.24" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.5501" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.728927E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="270.9221" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.255" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.27819" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0679927" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.712422" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3571" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.18225" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5207" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.548" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000017" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.67699" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3571" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14380" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.18225" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="3522-94-9" />
-<Smiles name="SMILES"  value="CC(C)(C)CCC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="49" />
-<CompoundID name="Name"  value="2,4,4-trimethylhexane" />
-<StructureFormula name="Structure"  value="CH3CH2C(CH3)2CH2CH(CH3)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="583" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2500000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.509" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="403.81" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="159.78" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="159.78" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000306827" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.255" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.178125" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.352203" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.432E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14590" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09892" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.387E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.403E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.5E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="468400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.13E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.68E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.1808" />
-  <B value="-0.0064001" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="63.91" />
-  <Tmax units="K"  value="159.78" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.098546" />
-  <B value="0.11862" />
-  <C value="583" />
-  <D value="0.15161" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="581" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="143.1127" />
-  <B value="-9541.532" />
-  <C value="-18.4559" />
-  <D value="0.0000171318" />
-  <E value="2" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="581" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.5551E+07" />
-  <B value="0.63316" />
-  <C value="-0.60532" />
-  <D value="0.59593" />
-  <E value="-0.24062" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="581" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="583" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="36795" />
-  <B value="-79.414" />
-  <C value="11.689" />
-  <D value="0.0041098" />
-  <E value="-0.0000031494" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="403.81" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84170" />
-  <B value="-452.22" />
-  <C value="13.167" />
-  <D value="0.00035197" />
-  <E value="-1.1076E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33299" />
-  <B value="-391.8" />
-  <C value="-66.527" />
-  <D value="-6374" />
-  <E value="-5982.8" />
-  <Tmin units="K"  value="290.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-6.9748" />
-  <B value="1194.1" />
-  <C value="-0.75025" />
-  <D value="-2.9452E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="460" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000003308" />
-  <B value="0.60466" />
-  <C value="252.52" />
-  <D value="-7535.6" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.061213" />
-  <B value="3.6115" />
-  <C value="-1.5687" />
-  <D value="-0.00048198" />
-  <E value="-0.000001134" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="403.81" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000028131" />
-  <B value="1.1825" />
-  <C value="-103.57" />
-  <D value="142450" />
-  <Tmin units="K"  value="403.81" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016164" />
-  <B value="11.187" />
-  <C value="-2.915" />
-  <D value="-0.00065885" />
-  <E value="-0.0000025171" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="581" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-26639" />
-  <B value="942.63" />
-  <C value="-0.52031" />
-  <D value="0.00011267" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.68" />
-  <B value="3161.4" />
-  <C value="-58.474" />
-  <Tmin units="K"  value="351" />
-  <Tmax units="K"  value="514.49" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.6176" />
-  <B value="-0.017458" />
-  <Tmin units="K"  value="159.78" />
-  <Tmax units="K"  value="460" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.5501" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.502101E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="298.185" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0676501" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.728934" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.352203" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.178125" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5207" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.548" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.352203" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14590" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.178125" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="16747-30-1" />
-<Smiles name="SMILES"  value="CC(C)CC(C)(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="50" />
-<CompoundID name="Name"  value="3,3-diethylpentane" />
-<StructureFormula name="Structure"  value="CH3CH2C(C2H5)2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="610.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2674980" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.473" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.249" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="419.34" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="240.12" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="240.12" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="13.7918" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.255" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.171012" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.3379" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.314E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15220" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09893" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.388E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.31835E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.17E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="436500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9800000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97551" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.68438E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.812" />
-  <B value="-0.0035815" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="96.05" />
-  <Tmax units="K"  value="240.12" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61216" />
-  <B value="0.28967" />
-  <C value="610.05" />
-  <D value="0.29325" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="610.05" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="143.8917" />
-  <B value="-9842.666" />
-  <C value="-18.51396" />
-  <D value="0.000016514" />
-  <E value="2" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="610.05" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.0222E+07" />
-  <B value="-0.028455" />
-  <C value="0.90984" />
-  <D value="-0.78409" />
-  <E value="0.24027" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="610.05" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-6779" />
-  <B value="1486.6" />
-  <C value="-4.3383" />
-  <D value="0.0056081" />
-  <E value="0.000012002" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="240.1" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="167890" />
-  <B value="37.678" />
-  <C value="8.6605" />
-  <D value="0.012988" />
-  <E value="-0.000011813" />
-  <Tmin units="K"  value="240.1" />
-  <Tmax units="K"  value="419.34" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="120540" />
-  <B value="-563.25" />
-  <C value="13.32" />
-  <D value="0.00012473" />
-  <E value="-3.6626E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26457" />
-  <B value="-346.37" />
-  <C value="-88.76" />
-  <D value="-14602" />
-  <E value="15928" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.975" />
-  <B value="1131.8" />
-  <C value="0.25767" />
-  <D value="-3.4761E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="419.34" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.6575E-07" />
-  <B value="0.57536" />
-  <C value="184.44" />
-  <D value="2017.7" />
-  <Tmin units="K"  value="419.34" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.021495" />
-  <B value="-29.993" />
-  <C value="-1.4603" />
-  <D value="-0.0013716" />
-  <E value="-7.6272E-07" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="419.34" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000069723" />
-  <B value="1.0959" />
-  <C value="342.29" />
-  <D value="74930" />
-  <Tmin units="K"  value="419.34" />
-  <Tmax units="K"  value="999.34" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.09195" />
-  <B value="-27.641" />
-  <C value="-1.6687" />
-  <D value="-0.001559" />
-  <E value="7.4071E-07" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="610.05" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13160" />
-  <B value="797.17" />
-  <C value="-0.3726" />
-  <D value="0.000062998" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.726" />
-  <B value="3317.6" />
-  <C value="-58.699" />
-  <Tmin units="K"  value="373.64" />
-  <Tmax units="K"  value="532.17" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.5181" />
-  <B value="-0.010538" />
-  <Tmin units="K"  value="240.12" />
-  <Tmax units="K"  value="419.34" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550163" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.710682E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="267.0522" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.249" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0660643" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.757461" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3379" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.171012" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5215" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.552" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.009265" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3379" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15220" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.171012" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1067-20-5" />
-<Smiles name="SMILES"  value="CCC(CC)(CC)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="51" />
-<CompoundID name="Name"  value="2,2,3,3-tetramethylpentane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2C(CH3)2CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="607.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2740000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.478" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="413.44" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="263.26" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="263.26" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="133.839" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.258" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.17034" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.304" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.1E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15060" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09891" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.407E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.36856E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.74E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="436600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2300000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.93709" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.68149E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.7007" />
-  <B value="-0.0032505" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="105.3" />
-  <Tmax units="K"  value="263.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.58952" />
-  <B value="0.28267" />
-  <C value="607.6" />
-  <D value="0.29572" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="589.38" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="139.0487" />
-  <B value="-9535.451" />
-  <C value="-17.78617" />
-  <D value="0.0000157521" />
-  <E value="2" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="607.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.3713E+07" />
-  <B value="0.39899" />
-  <C value="-0.032998" />
-  <D value="0.06374" />
-  <E value="-0.0535" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="607.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-8132.5" />
-  <B value="1274" />
-  <C value="-2.5935" />
-  <D value="0.014873" />
-  <E value="-0.000051282" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="174.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116740" />
-  <B value="-86.104" />
-  <C value="11.13" />
-  <D value="0.0046308" />
-  <E value="-0.000003068" />
-  <Tmin units="K"  value="263.4" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="55048" />
-  <B value="-357.31" />
-  <C value="13.013" />
-  <D value="0.00055209" />
-  <E value="-1.6211E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30532" />
-  <B value="-388.69" />
-  <C value="-73.537" />
-  <D value="-25110" />
-  <E value="47691" />
-  <Tmin units="K"  value="303.75" />
-  <Tmax units="K"  value="1949.43" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.7597" />
-  <B value="1441.2" />
-  <C value="-0.37772" />
-  <D value="-0.000001226" />
-  <E value="2" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="486" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.1934E-07" />
-  <B value="0.48521" />
-  <C value="356.82" />
-  <D value="-1384.3" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0045701" />
-  <B value="-120.11" />
-  <C value="-0.775" />
-  <D value="-0.0036256" />
-  <E value="9.650699E-07" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="413.44" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000014917" />
-  <B value="1.2661" />
-  <C value="-211.67" />
-  <D value="155870" />
-  <Tmin units="K"  value="413.44" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.067505" />
-  <B value="-40.086" />
-  <C value="-1.7701" />
-  <D value="-0.0019128" />
-  <E value="8.1111E-07" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="607.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-50045" />
-  <B value="1093.4" />
-  <C value="-0.82446" />
-  <D value="0.00037581" />
-  <E value="-7.7657E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.567" />
-  <B value="3186.4" />
-  <C value="-60.994" />
-  <Tmin units="K"  value="368.1" />
-  <Tmax units="K"  value="535.03" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3449" />
-  <B value="-0.012915" />
-  <Tmin units="K"  value="263.26" />
-  <Tmax units="K"  value="486" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550036" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.052637E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="351.2684" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0661158" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.760702" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.304" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.17034" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.52" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.628" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.002328" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.304" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15060" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.17034" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="7154-79-2" />
-<Smiles name="SMILES"  value="CC(C)(C)C(C)(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="52" />
-<CompoundID name="Name"  value="2,2,3,4-tetramethylpentane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2CH(CH3)CH(CH3)CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="592.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2530000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.49" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.258" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="406.18" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="152.06" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="152.06" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000053591" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.258" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.179229" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.301" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.16E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09891" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.386E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.37358E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.26352E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="452834" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="500000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95146" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.68208E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.2756" />
-  <B value="-0.0060479" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="60.82" />
-  <Tmax units="K"  value="152.06" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.42889" />
-  <B value="0.24425" />
-  <C value="592.7" />
-  <D value="0.24983" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="592.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="137.07" />
-  <B value="-9700.5" />
-  <C value="-17.255" />
-  <D value="0.000012062" />
-  <E value="2" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="592.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.771831E+07" />
-  <B value="1.016576" />
-  <C value="-1.835135" />
-  <D value="2.12911" />
-  <E value="-0.921819" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="592.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="592.7" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="177720" />
-  <B value="-50.337" />
-  <C value="8.3416" />
-  <D value="0.015008" />
-  <E value="-0.000013849" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="406.18" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83946" />
-  <B value="-465.16" />
-  <C value="13.193" />
-  <D value="0.000328" />
-  <E value="-9.6189E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30123" />
-  <B value="-401.73" />
-  <C value="-67.509" />
-  <D value="-13419" />
-  <E value="21834" />
-  <Tmin units="K"  value="296.08" />
-  <Tmax units="K"  value="1892.08" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.182" />
-  <B value="1248.5" />
-  <C value="-0.55988" />
-  <D value="-2.1902E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="474.08" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.9083E-07" />
-  <B value="0.57522" />
-  <C value="220.52" />
-  <D value="-776.34" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.045924" />
-  <B value="4.3553" />
-  <C value="-1.6529" />
-  <D value="-0.00040588" />
-  <E value="-0.000001389" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="406.18" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000019408" />
-  <B value="1.2262" />
-  <C value="-198.62" />
-  <D value="159810" />
-  <Tmin units="K"  value="406.18" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012296" />
-  <B value="16.67" />
-  <C value="-3.0272" />
-  <D value="-0.00038099" />
-  <E value="-0.0000033807" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="592.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-45081" />
-  <B value="1026.9" />
-  <C value="-0.66774" />
-  <D value="0.00021534" />
-  <E value="-2.1701E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.558" />
-  <B value="3122" />
-  <C value="-60.513" />
-  <Tmin units="K"  value="360.74" />
-  <Tmax units="K"  value="523.04" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.3033" />
-  <B value="-0.017906" />
-  <Tmin units="K"  value="152.06" />
-  <Tmax units="K"  value="474.08" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550036" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.476529E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="294.835" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.258" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.066584" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.743261" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.301" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.179229" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5199" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.544" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002088" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.301" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14730" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.179229" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1186-53-4" />
-<Smiles name="SMILES"  value="CC(C)(C)C(C)C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="53" />
-<CompoundID name="Name"  value="2,2,4,4-tetramethylpentane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2CH2C(CH3)2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="571.35" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2360870" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.504" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="395.44" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="206.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="206.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.83952" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.255" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.17923" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.313609" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.86E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14150" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09891" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.407E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.41375E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.40159E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="431496" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9700000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95089" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.67978E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.7417" />
-  <B value="-0.0041681" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="82.78" />
-  <Tmax units="K"  value="206.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.47711" />
-  <B value="0.25904" />
-  <C value="574.61" />
-  <D value="0.26647" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="574.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="136.5701" />
-  <B value="-9035.55" />
-  <C value="-17.5287" />
-  <D value="0.0000167892" />
-  <E value="2" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="574.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.75823E+07" />
-  <B value="1.154086" />
-  <C value="-2.055247" />
-  <D value="2.209851" />
-  <E value="-0.923166" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="555.25" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-3662.8" />
-  <B value="1207.7" />
-  <C value="-1.0811" />
-  <D value="-0.016528" />
-  <E value="0.000094782" />
-  <Tmin units="K"  value="18" />
-  <Tmax units="K"  value="206.61" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119280" />
-  <B value="88.665" />
-  <C value="9.3063" />
-  <D value="0.010453" />
-  <E value="-0.0000091934" />
-  <Tmin units="K"  value="206.61" />
-  <Tmax units="K"  value="380" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122670" />
-  <B value="-599.26" />
-  <C value="13.402" />
-  <D value="0.000099085" />
-  <E value="-1.741E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30694" />
-  <B value="-369.96" />
-  <C value="-60.863" />
-  <D value="-20132" />
-  <E value="40675" />
-  <Tmin units="K"  value="285.68" />
-  <Tmax units="K"  value="1827.68" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.148" />
-  <B value="1468.8" />
-  <C value="-0.33327" />
-  <D value="-0.0000013179" />
-  <E value="2" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="459.68" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.8808E-07" />
-  <B value="0.52306" />
-  <C value="289.62" />
-  <D value="-2721.1" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.038909" />
-  <B value="-2.6455" />
-  <C value="-1.623" />
-  <D value="-0.0006558" />
-  <E value="-0.0000013711" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="395.44" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000015165" />
-  <B value="1.2696" />
-  <C value="-148.49" />
-  <D value="133700" />
-  <Tmin units="K"  value="395.44" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0065574" />
-  <B value="70.429" />
-  <C value="-3.7855" />
-  <D value="0.0020966" />
-  <E value="-0.0000079684" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="555.25" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="8603.1" />
-  <B value="793.17" />
-  <C value="-0.33044" />
-  <D value="0.000047239" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.498" />
-  <B value="3022.6" />
-  <C value="-58.531" />
-  <Tmin units="K"  value="343.77" />
-  <Tmax units="K"  value="497.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.9999" />
-  <B value="-0.016657" />
-  <Tmin units="K"  value="206.95" />
-  <Tmax units="K"  value="459.68" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550036" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.375219E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="304.5483" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.263" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0662001" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.725823" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.313609" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.17923" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.52" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.628" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001878" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.313609" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14150" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.17923" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="2"  value="1" />
-  <group id="4"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1070-87-7" />
-<Smiles name="SMILES"  value="CC(C)(C)CC(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="54" />
-<CompoundID name="Name"  value="2,3,3,4-tetramethylpentane" />
-<StructureFormula name="Structure"  value="(CH3)2CHC(CH3)2CH(CH3)2" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="607.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2670000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.493" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="414.71" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="171.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="171.03" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00089642" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.258" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.17076" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.313" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.2E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15110" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09891" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.386E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.361E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.8E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="436900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9000000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95099" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.6822E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.3777" />
-  <B value="-0.006123" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="68.41" />
-  <Tmax units="K"  value="171.03" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.49299" />
-  <B value="0.25927" />
-  <C value="607.51" />
-  <D value="0.27003" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="607.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="79.047" />
-  <B value="-7201.2" />
-  <C value="-8.4677" />
-  <D value="0.0000051332" />
-  <E value="2" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="607.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.5207E+07" />
-  <B value="0.63465" />
-  <C value="-0.82041" />
-  <D value="1.0175" />
-  <E value="-0.45604" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="584.53" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="607.1" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="61477" />
-  <B value="20.611" />
-  <C value="11.082" />
-  <D value="0.0041652" />
-  <E value="-0.0000014763" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="414.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="50811" />
-  <B value="-338.13" />
-  <C value="12.991" />
-  <D value="0.00056259" />
-  <E value="-1.7284E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30059" />
-  <B value="-410.94" />
-  <C value="-73.01" />
-  <D value="-15607" />
-  <E value="25044" />
-  <Tmin units="K"  value="303.75" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.4098" />
-  <B value="1217" />
-  <C value="-0.67198" />
-  <D value="-2.7904E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="486" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.7299E-07" />
-  <B value="0.59636" />
-  <C value="289.93" />
-  <D value="-9056.4" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.058699" />
-  <B value="3.5637" />
-  <C value="-1.5648" />
-  <D value="-0.000479" />
-  <E value="-0.0000010469" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="414.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000035577" />
-  <B value="1.1602" />
-  <C value="-50.424" />
-  <D value="142790" />
-  <Tmin units="K"  value="414.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015328" />
-  <B value="14.362" />
-  <C value="-2.9182" />
-  <D value="-0.00052501" />
-  <E value="-0.0000026764" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="584.53" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-76402" />
-  <B value="1346.3" />
-  <C value="-1.4905" />
-  <D value="0.001055" />
-  <E value="-3.2169E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.197557" />
-  <B value="-1450" />
-  <C value="-8.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.915" />
-  <B value="3420.9" />
-  <C value="-50.35" />
-  <Tmin units="K"  value="365" />
-  <Tmax units="K"  value="538.58" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0446" />
-  <B value="-0.015849" />
-  <Tmin units="K"  value="171.03" />
-  <Tmax units="K"  value="486" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550036" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.38854E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="314.8323" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.06644" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.758871" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.313" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.17076" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5199" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.544" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005733" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.313" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15110" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.17076" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="3"  value="2" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="16747-38-9" />
-<Smiles name="SMILES"  value="CC(C)C(C)(C)C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="91" />
-<CompoundID name="Name"  value="2-methyloctane" />
-<StructureFormula name="Structure"  value="(CH3)2CH(CH2)5CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="587" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2310000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.529" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="416.44" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="193.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="193.05" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0206" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.258" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.18075" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.423" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.973E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15310" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09894" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.368E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.348E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.21E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="496800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.8E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.15253" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.6791E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.7885" />
-  <B value="-0.0045145" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="68.52" />
-  <Tmax units="K"  value="193.05" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.048725" />
-  <B value="0.083928" />
-  <C value="587" />
-  <D value="0.13299" />
-  <Tmin units="K"  value="193.05" />
-  <Tmax units="K"  value="582.87" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="117.6637" />
-  <B value="-9065.067" />
-  <C value="-14.28093" />
-  <D value="0.0000101806" />
-  <E value="2" />
-  <Tmin units="K"  value="193.05" />
-  <Tmax units="K"  value="586.75" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.8687E+07" />
-  <B value="1.3406" />
-  <C value="-2.5809" />
-  <D value="2.7985" />
-  <E value="-1.1501" />
-  <Tmin units="K"  value="192.78" />
-  <Tmax units="K"  value="582.87" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-25158" />
-  <B value="2699" />
-  <C value="-23.134" />
-  <D value="0.12246" />
-  <E value="-0.00024281" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="160" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="69326" />
-  <B value="112.91" />
-  <C value="10.449" />
-  <D value="0.0058606" />
-  <E value="-0.0000035224" />
-  <Tmin units="K"  value="193" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="145390" />
-  <B value="-732.92" />
-  <C value="13.658" />
-  <D value="-0.00027343" />
-  <E value="8.6186E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.32232" />
-  <B value="-409.91" />
-  <C value="-67.241" />
-  <D value="-24500" />
-  <E value="45268" />
-  <Tmin units="K"  value="291.44" />
-  <Tmax units="K"  value="1877.38" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-14.31" />
-  <B value="1234.5" />
-  <C value="0.50422" />
-  <D value="-0.0000012054" />
-  <E value="2" />
-  <Tmin units="K"  value="192.78" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000005318" />
-  <B value="0.52649" />
-  <C value="272.37" />
-  <D value="-710.16" />
-  <Tmin units="K"  value="193.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.15278" />
-  <B value="14.586" />
-  <C value="-1.1974" />
-  <D value="-0.00013887" />
-  <E value="-9.4417E-07" />
-  <Tmin units="K"  value="193.05" />
-  <Tmax units="K"  value="466.03" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00002892" />
-  <B value="1.1595" />
-  <C value="-163.72" />
-  <D value="160440" />
-  <Tmin units="K"  value="416.43" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0095148" />
-  <B value="42.82" />
-  <C value="-3.2759" />
-  <D value="0.00028384" />
-  <E value="-0.0000047898" />
-  <Tmin units="K"  value="193.05" />
-  <Tmax units="K"  value="582.87" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="49172" />
-  <B value="391.1" />
-  <C value="0.86362" />
-  <D value="-0.0013874" />
-  <E value="5.6971E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.199" />
-  <B value="3477.2" />
-  <C value="-56.934" />
-  <Tmin units="K"  value="354.15" />
-  <Tmax units="K"  value="521.32" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3429" />
-  <B value="-0.012901" />
-  <Tmin units="K"  value="192.78" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550226" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.965301E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="260.6966" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0686142" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.717479" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.423" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.18075" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5222" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.472" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.423" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15310" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.18075" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="3221-61-2" />
-<Smiles name="SMILES"  value="CC(C)CCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="92" />
-<CompoundID name="Name"  value="3-methyloctane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)(CH2)4CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="590.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2340000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.529" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="417.38" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="165.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="165.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000898613" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.255" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.178944" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.412346" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.791E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15380" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09894" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.368E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.336E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.17E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="501660" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.7E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.68128E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.0428" />
-  <B value="-0.0054796" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="66.22" />
-  <Tmax units="K"  value="165.55" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.4999" />
-  <B value="0.26438" />
-  <C value="590.15" />
-  <D value="0.29155" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="567.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="169.345" />
-  <B value="-11170.36" />
-  <C value="-22.26865" />
-  <D value="0.0000190112" />
-  <E value="2" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="590.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.3378E+07" />
-  <B value="0.67667" />
-  <C value="-0.53996" />
-  <D value="0.45608" />
-  <E value="-0.18958" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="567.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="590.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="39163" />
-  <B value="25.328" />
-  <C value="11.626" />
-  <D value="0.0021572" />
-  <E value="2.6369E-07" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="560" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="118620" />
-  <B value="-596.81" />
-  <C value="13.418" />
-  <D value="0.0000088283" />
-  <E value="-1.2271E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30664" />
-  <B value="-390.98" />
-  <C value="-75.702" />
-  <D value="-18831" />
-  <E value="29822" />
-  <Tmin units="K"  value="295.07" />
-  <Tmax units="K"  value="1885.08" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.252" />
-  <B value="1147.6" />
-  <C value="-0.021999" />
-  <D value="4.3706E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="417.38" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.9482E-07" />
-  <B value="0.53152" />
-  <C value="245.99" />
-  <D value="4.1109" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1642" />
-  <B value="10.91" />
-  <C value="-1.1265" />
-  <D value="-0.00023366" />
-  <E value="-7.9637E-07" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="470" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000040968" />
-  <B value="1.1096" />
-  <C value="-178.72" />
-  <D value="180220" />
-  <Tmin units="K"  value="417.38" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011116" />
-  <B value="17.733" />
-  <C value="-2.999" />
-  <D value="-0.00046999" />
-  <E value="-0.0000037171" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="567.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="3693.9" />
-  <B value="812.59" />
-  <C value="-0.39408" />
-  <D value="0.000066664" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.613" />
-  <B value="3114.3" />
-  <C value="-74.619" />
-  <Tmin units="K"  value="355.15" />
-  <Tmax units="K"  value="523.11" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.5467" />
-  <B value="-0.015661" />
-  <Tmin units="K"  value="165.55" />
-  <Tmax units="K"  value="417.38" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550226" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.889501E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="269.7227" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.252" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0683818" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.724722" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.412346" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.178944" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5222" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.472" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.412346" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15380" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.178944" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2216-33-3" />
-<Smiles name="SMILES"  value="CCC(C)CCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="93" />
-<CompoundID name="Name"  value="4-methyloctane" />
-<StructureFormula name="Structure"  value="CH3(CH2)2CHCH3(CH2)3CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="587.65" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2340000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.523" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="415.59" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="159.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="159.95" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000317697" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.255" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.179037" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.412925" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.772E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15300" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09894" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.368E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.336E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.17E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="501660" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.6E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.68166E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.0556" />
-  <B value="-0.0055544" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="63.98" />
-  <Tmax units="K"  value="159.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.51336" />
-  <B value="0.26824" />
-  <C value="587.65" />
-  <D value="0.29075" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="587.65" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="168.4912" />
-  <B value="-11138.63" />
-  <C value="-22.13486" />
-  <D value="0.0000188399" />
-  <E value="2" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="587.65" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.2916E+07" />
-  <B value="0.7446" />
-  <C value="-0.80882" />
-  <D value="0.80228" />
-  <E value="-0.33895" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="587.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="587.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="71582" />
-  <B value="100.57" />
-  <C value="10.612" />
-  <D value="0.0050783" />
-  <E value="-0.0000024905" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="500" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116790" />
-  <B value="-588.34" />
-  <C value="13.412" />
-  <D value="0.000015201" />
-  <E value="-1.4561E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30648" />
-  <B value="-389" />
-  <C value="-74.826" />
-  <D value="-18071" />
-  <E value="28356" />
-  <Tmin units="K"  value="293.82" />
-  <Tmax units="K"  value="1877.83" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.837" />
-  <B value="1162" />
-  <C value="0.077237" />
-  <D value="-2.6336E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="415.59" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.2706E-07" />
-  <B value="0.5848" />
-  <C value="183.92" />
-  <D value="0.068678" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1663" />
-  <B value="9.2848" />
-  <C value="-1.1068" />
-  <D value="-0.00028405" />
-  <E value="-0.0000007408" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="470" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000038784" />
-  <B value="1.117" />
-  <C value="-185.06" />
-  <D value="177130" />
-  <Tmin units="K"  value="415.59" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0090133" />
-  <B value="27.989" />
-  <C value="-3.1772" />
-  <D value="0.00013817" />
-  <E value="-0.0000048752" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="587.65" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="1160.7" />
-  <B value="826.4" />
-  <C value="-0.41015" />
-  <D value="0.000072067" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.596" />
-  <B value="3082.6" />
-  <C value="-75.645" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="520.12" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.3456" />
-  <B value="-0.016308" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="415.59" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550226" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.935072E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="260.9853" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0683237" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.724328" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.412925" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.179037" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5222" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.472" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.412925" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15300" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.179037" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2216-34-4" />
-<Smiles name="SMILES"  value="CCCC(C)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="94" />
-<CompoundID name="Name"  value="3-ethylheptane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(C2H5)CH2(CH2)2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="594.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2430000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.5213" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="416.35" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="158.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="158.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000277743" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.255" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.177515" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.407991" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.953E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15300" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09894" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.368E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.3146E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.494E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="497400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.6E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.6838E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.1778" />
-  <B value="-0.0064596" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="63.3" />
-  <Tmax units="K"  value="158.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.38578" />
-  <B value="0.23273" />
-  <C value="594.3" />
-  <D value="0.25158" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="567.28" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="103.6653" />
-  <B value="-8269.445" />
-  <C value="-12.32292" />
-  <D value="0.000012256" />
-  <E value="2" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="590" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.3311E+07" />
-  <B value="1.0505" />
-  <C value="-1.9581" />
-  <D value="2.2955" />
-  <E value="-0.98973" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="590" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="594.3" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="29546" />
-  <B value="-3.2521" />
-  <C value="11.386" />
-  <D value="0.0045932" />
-  <E value="-0.0000035582" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="416.35" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="137360" />
-  <B value="-689.88" />
-  <C value="13.586" />
-  <D value="-0.00018791" />
-  <E value="5.2355E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30691" />
-  <B value="-394.25" />
-  <C value="-77.102" />
-  <D value="-21616" />
-  <E value="36748" />
-  <Tmin units="K"  value="297.15" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.279" />
-  <B value="1149.8" />
-  <C value="-0.019903" />
-  <D value="1.7111E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="416.35" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000007497" />
-  <B value="0.48637" />
-  <C value="340.94" />
-  <D value="-2876.9" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.038271" />
-  <B value="3.4169" />
-  <C value="-1.6847" />
-  <D value="-0.00052626" />
-  <E value="-0.0000013295" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="416.35" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000030963" />
-  <B value="1.1527" />
-  <C value="-150.17" />
-  <D value="156710" />
-  <Tmin units="K"  value="416.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011888" />
-  <B value="12.561" />
-  <C value="-2.9032" />
-  <D value="-0.00075797" />
-  <E value="-0.0000031904" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="590" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="28905" />
-  <B value="723.1" />
-  <C value="-0.30251" />
-  <D value="0.000037455" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.883" />
-  <B value="3285.8" />
-  <C value="-64.914" />
-  <Tmin units="K"  value="362.76" />
-  <Tmax units="K"  value="521.83" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.3411" />
-  <B value="-0.016316" />
-  <Tmin units="K"  value="158.25" />
-  <Tmax units="K"  value="416.35" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550226" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.668101E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="291.5266" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.257" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0682157" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.730456" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.407991" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.177515" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5222" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.472" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.407991" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15300" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.177515" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="15869-80-4" />
-<Smiles name="SMILES"  value="CCC(CC)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="96" />
-<CompoundID name="Name"  value="2,2-dimethylheptane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2(CH2)4CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="577.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2350000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.525" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="405.97" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="160.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="160.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000152983" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="128.258" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.18151" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.383" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.845E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14720" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09893" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.388E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.461E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.79E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="471800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8900000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.672E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.9753" />
-  <B value="-0.0055395" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="64.06" />
-  <Tmax units="K"  value="160.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.19929" />
-  <B value="0.16944" />
-  <C value="577.8" />
-  <D value="0.19098" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="576.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="173.1768" />
-  <B value="-10891.65" />
-  <C value="-23.04354" />
-  <D value="0.0000217483" />
-  <E value="2" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="576.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.677584E+07" />
-  <B value="0.420266" />
-  <C value="0.0606766" />
-  <D value="-0.058971" />
-  <E value="-0.0565229" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="576.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="249210" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="577.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="188490" />
-  <B value="-126.2" />
-  <C value="10.161" />
-  <D value="0.0065361" />
-  <E value="-0.0000033154" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="405.84" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119340" />
-  <B value="-582.53" />
-  <C value="13.386" />
-  <D value="0.000067675" />
-  <E value="-2.1229E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.29926" />
-  <B value="-360.95" />
-  <C value="-70.246" />
-  <D value="-13793" />
-  <E value="20867" />
-  <Tmin units="K"  value="288.35" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.654" />
-  <B value="1250.4" />
-  <C value="0.03445" />
-  <D value="-6.0618E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="405.84" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.0205E-07" />
-  <B value="0.4765" />
-  <C value="340.6" />
-  <D value="-3260.3" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.04961" />
-  <B value="4.5364" />
-  <C value="-1.657" />
-  <D value="-0.00038774" />
-  <E value="-0.0000014465" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="405.84" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000023582" />
-  <B value="1.1966" />
-  <C value="-148.34" />
-  <D value="144910" />
-  <Tmin units="K"  value="405.84" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.008025" />
-  <B value="40.938" />
-  <C value="-3.4014" />
-  <D value="0.00073554" />
-  <E value="-0.0000058206" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="576.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="5399.1" />
-  <B value="817.15" />
-  <C value="-0.38647" />
-  <D value="0.000065459" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.404923" />
-  <B value="-950" />
-  <C value="-5.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.532" />
-  <B value="3019.1" />
-  <C value="-70.648" />
-  <Tmin units="K"  value="346.85" />
-  <Tmax units="K"  value="510.93" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.5711" />
-  <B value="-0.018073" />
-  <Tmin units="K"  value="160.15" />
-  <Tmax units="K"  value="405.84" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.550163" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.686199E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="283.4327" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.257" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="189.3" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0677873" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.715257" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.383" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.18151" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5215" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.552" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.383" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14720" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.18151" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1071-26-7" />
-<Smiles name="SMILES"  value="CC(C)(C)CCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="48" />
-<CompoundID name="Name"  value="3,3,5-trimethylheptane" />
-<StructureFormula name="Structure"  value="CH3CH2C(CH3)2CH2CH(CH3)CH2CH3" />
-<Family name="Family"  value="4" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="609.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2320000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.564" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.258" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="428.83" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="165" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="165" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000151957" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.285" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.19248" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.383" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.886E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15010" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10915" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.522E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.588E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.23E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="513420" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.4E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.2911E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="7.4787" />
-  <B value="-0.0056657" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="66" />
-  <Tmax units="K"  value="165" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.32798" />
-  <B value="0.22465" />
-  <C value="609.6" />
-  <D value="0.2413" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="609.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="165.0702" />
-  <B value="-10873.83" />
-  <C value="-21.67781" />
-  <D value="0.0000174271" />
-  <E value="2" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="609.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.692041E+07" />
-  <B value="-0.369689" />
-  <C value="2.788348" />
-  <D value="-3.430471" />
-  <E value="1.37842" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="609.5" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="275220" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="609.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="181900" />
-  <B value="88.778" />
-  <C value="8.7398" />
-  <D value="0.011239" />
-  <E value="-0.0000078705" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="457.16" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="93450" />
-  <B value="-461.09" />
-  <C value="13.294" />
-  <D value="0.00031582" />
-  <E value="-1.0309E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33139" />
-  <B value="-440.19" />
-  <C value="-87.279" />
-  <D value="-20730" />
-  <E value="33410" />
-  <Tmin units="K"  value="304.75" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.8795" />
-  <B value="1294.8" />
-  <C value="-0.60549" />
-  <D value="-4.2086E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="487.64" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.7085E-07" />
-  <B value="0.52829" />
-  <C value="329.98" />
-  <D value="-4470.2" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0037809" />
-  <B value="-39.052" />
-  <C value="-1.5072" />
-  <D value="-0.0019367" />
-  <E value="-8.6862E-07" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="550" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000042493" />
-  <B value="1.1211" />
-  <C value="-89.298" />
-  <D value="167970" />
-  <Tmin units="K"  value="428.83" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0079018" />
-  <B value="47.103" />
-  <C value="-3.4097" />
-  <D value="0.00092865" />
-  <E value="-0.0000056403" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="609.5" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-24935" />
-  <B value="982.01" />
-  <C value="-0.34771" />
-  <D value="-0.00019639" />
-  <E value="1.4276E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.755" />
-  <B value="3365.2" />
-  <C value="-64.25" />
-  <Tmin units="K"  value="374.15" />
-  <Tmax units="K"  value="539.32" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.4461" />
-  <B value="-0.016988" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="487.64" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.615915" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.835398E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="303.2417" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.258" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.82" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0742386" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.747136" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.383" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.19248" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.1951" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.088" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.383" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15010" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.19248" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="5" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="5" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="5" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="5" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="5" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="7154-80-5" />
-<Smiles name="SMILES"  value="CCC(C)(C)CC(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="72" />
-<CompoundID name="Name"  value="2,2-dimethyloctane" />
-<StructureFormula name="Structure"  value="CH3C(CH3)2(CH2)5CH3" />
-<Family name="Family"  value="3" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="602.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2110000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.5897" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="430.05" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.282" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.197405" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.428759" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.223E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14870" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10916" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.523E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.67E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.6E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="511000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.7E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.281E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.35" />
-  <B value="2.3419E-17" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.27519" />
-  <B value="0.20873" />
-  <C value="602.4" />
-  <D value="0.22241" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="602" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="128.2162" />
-  <B value="-9736.787" />
-  <C value="-15.87938" />
-  <D value="0.0000121145" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="602" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.2139E+07" />
-  <B value="0.81955" />
-  <C value="-1.4728" />
-  <D value="1.7846" />
-  <E value="-0.74179" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="602" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="275220" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="602.4" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="130180" />
-  <B value="214" />
-  <C value="8.9638" />
-  <D value="0.010626" />
-  <E value="-0.0000085091" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="425" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="133300" />
-  <B value="-582.81" />
-  <C value="13.49" />
-  <D value="0.000049115" />
-  <E value="-1.5637E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33556" />
-  <B value="-413.18" />
-  <C value="-91.248" />
-  <D value="-27355" />
-  <E value="45691" />
-  <Tmin units="K"  value="301" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.132" />
-  <B value="1337.2" />
-  <C value="0.10372" />
-  <D value="-1.6576E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="430.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.6483E-07" />
-  <B value="0.48953" />
-  <C value="292.37" />
-  <D value="276.07" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.054905" />
-  <B value="-9.2849" />
-  <C value="-1.513" />
-  <D value="-0.00077582" />
-  <E value="-8.6839E-07" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="430.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000023992" />
-  <B value="1.186" />
-  <C value="-157.89" />
-  <D value="154490" />
-  <Tmin units="K"  value="430.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0081141" />
-  <B value="109.26" />
-  <C value="-3.9929" />
-  <D value="0.0023215" />
-  <E value="-0.0000066762" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="602" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="7717.8" />
-  <B value="904.09" />
-  <C value="-0.43608" />
-  <D value="0.00007608" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.447" />
-  <B value="3766.1" />
-  <C value="-50.805" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="602" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9662" />
-  <B value="-0.013254" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="430.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.615981" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.338988E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="259.9107" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.82" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0749304" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.728014" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.428759" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.197405" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.1959" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.092" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.428759" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14870" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.197405" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="15869-87-1" />
-<Smiles name="SMILES"  value="CC(C)(C)CCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="85" />
-<CompoundID name="Name"  value="3-methylnonane" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)(CH2)5CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="613.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2140000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.5904" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.247" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="440.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="188.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="188.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000565366" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.282" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.195076" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.464925" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.286E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15470" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10917" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.503E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.544E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.88E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="543900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.88E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.291E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.1736" />
-  <B value="-0.0042229" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="75.34" />
-  <Tmax units="K"  value="188.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.19012" />
-  <B value="0.17319" />
-  <C value="613.7" />
-  <D value="0.19349" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="613" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="90.738" />
-  <B value="-8476.8" />
-  <C value="-10.023" />
-  <D value="0.0000053448" />
-  <E value="2" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="613" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.354164E+07" />
-  <B value="1.024481" />
-  <C value="-0.0908156" />
-  <D value="-1.228122" />
-  <E value="0.762381" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="613" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="622690" />
-  <B value="-20288" />
-  <C value="276.93" />
-  <D value="-1.5699" />
-  <E value="0.0032518" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="180" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78506" />
-  <B value="74.892" />
-  <C value="11.023" />
-  <D value="0.0040568" />
-  <E value="-0.0000015927" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="580" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="133050" />
-  <B value="-599.42" />
-  <C value="13.53" />
-  <D value="-0.000017353" />
-  <E value="-3.363E-09" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33234" />
-  <B value="-422.27" />
-  <C value="-103.89" />
-  <D value="-20755" />
-  <E value="19060" />
-  <Tmin units="K"  value="306.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.922" />
-  <B value="1267.3" />
-  <C value="0.28159" />
-  <D value="-8.3807E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="440.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.1879E-07" />
-  <B value="0.49638" />
-  <C value="289.26" />
-  <D value="-877.62" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1781" />
-  <B value="10.557" />
-  <C value="-1.078" />
-  <D value="-0.00023148" />
-  <E value="-6.8221E-07" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="490" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000033407" />
-  <B value="1.1338" />
-  <C value="-162.76" />
-  <D value="171650" />
-  <Tmin units="K"  value="440.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01117" />
-  <B value="45.677" />
-  <C value="-3.2566" />
-  <D value="0.00030403" />
-  <E value="-0.0000040378" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="613" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="6363.2" />
-  <B value="899.08" />
-  <C value="-0.44378" />
-  <D value="0.000077366" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.006" />
-  <B value="3498.3" />
-  <C value="-71.962" />
-  <Tmin units="K"  value="370.15" />
-  <Tmax units="K"  value="545.95" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.7344" />
-  <B value="-0.013957" />
-  <Tmin units="K"  value="188.35" />
-  <Tmax units="K"  value="440.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.616046" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.382832E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="260.9626" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.247" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.82" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0754856" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.736955" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.464925" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.195076" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.196599" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.012" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.464925" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15470" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.195076" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="5911-04-6" />
-<Smiles name="SMILES"  value="CCC(C)CCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="86" />
-<CompoundID name="Name"  value="2-methylnonane" />
-<StructureFormula name="Structure"  value="(CH3)2CH(CH2)6CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="621" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2050000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.601" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="440.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="198.5" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="198.5" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00248675" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.282" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.196826" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.472342" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.429E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15380" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10917" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.503E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.5652E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.841E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="538020" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.75E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.2888E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.0875" />
-  <B value="-0.0039745" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="79.4" />
-  <Tmax units="K"  value="198.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.2243" />
-  <B value="0.18661" />
-  <C value="621" />
-  <D value="0.23259" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="588.34" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="133.13" />
-  <B value="-10462" />
-  <C value="-16.388" />
-  <D value="0.0000099287" />
-  <E value="2" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="610" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.023987E+07" />
-  <B value="-0.879246" />
-  <C value="6.371272" />
-  <D value="-9.404583" />
-  <E value="4.418702" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="610" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="581370" />
-  <B value="-18844" />
-  <C value="260.35" />
-  <D value="-1.4888" />
-  <E value="0.0031062" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="185" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-52606" />
-  <B value="80.981" />
-  <C value="11.786" />
-  <D value="0.0026831" />
-  <E value="-6.0448E-07" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="580" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="137030" />
-  <B value="-599.28" />
-  <C value="13.509" />
-  <D value="0.0000018563" />
-  <E value="-1.0781E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34066" />
-  <B value="-433.78" />
-  <C value="-97.746" />
-  <D value="-34416" />
-  <E value="59442" />
-  <Tmin units="K"  value="305" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-3.1519" />
-  <B value="949.54" />
-  <C value="-1.2725" />
-  <D value="0.0000012986" />
-  <E value="2" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.2127E-07" />
-  <B value="0.44292" />
-  <C value="352.44" />
-  <D value="-1163.9" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.16513" />
-  <B value="15.121" />
-  <C value="-1.1582" />
-  <D value="-0.00011252" />
-  <E value="-0.0000008534" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="488" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000030641" />
-  <B value="1.1437" />
-  <C value="-171.78" />
-  <D value="168770" />
-  <Tmin units="K"  value="440.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013266" />
-  <B value="8.6972" />
-  <C value="-2.8018" />
-  <D value="-0.0012779" />
-  <E value="-0.0000019818" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="610" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="12286" />
-  <B value="883.31" />
-  <C value="-0.42859" />
-  <D value="0.000072456" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.901" />
-  <B value="3427.2" />
-  <C value="-74.62" />
-  <Tmin units="K"  value="375.15" />
-  <Tmax units="K"  value="545.03" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.382" />
-  <B value="-0.011976" />
-  <Tmin units="K"  value="198.5" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.616046" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.557272E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="252.7017" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.244" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.82" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0765141" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.73091" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.472342" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.196826" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.196599" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.012" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.472342" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15380" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.196826" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="871-83-0" />
-<Smiles name="SMILES"  value="CC(C)CCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="87" />
-<CompoundID name="Name"  value="4-methylnonane" />
-<StructureFormula name="Structure"  value="CH3(CH2)2CH(CH3)(CH2)4CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="613.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2140000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.5904" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="438.85" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="174.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="174.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000108068" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.282" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.195426" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.465073" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.265E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15500" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10917" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.503E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.547E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.89E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="541900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.52E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.291E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.2988" />
-  <B value="-0.0046485" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="69.78" />
-  <Tmax units="K"  value="174.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.046753" />
-  <B value="0.085687" />
-  <C value="613.7" />
-  <D value="0.13909" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="610" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="143.6866" />
-  <B value="-10632.15" />
-  <C value="-18.17547" />
-  <D value="0.0000137486" />
-  <E value="2" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="610" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.2873E+07" />
-  <B value="0.39496" />
-  <C value="-0.054115" />
-  <D value="0.081779" />
-  <E value="-0.040701" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="610" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="1327700" />
-  <B value="-47867" />
-  <C value="675.59" />
-  <D value="-4.0824" />
-  <E value="0.0090781" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="160" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="41953" />
-  <B value="56.5" />
-  <C value="11.484" />
-  <D value="0.0029861" />
-  <E value="-0.0000006055" />
-  <Tmin units="K"  value="120" />
-  <Tmax units="K"  value="580" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="130820" />
-  <B value="-589.61" />
-  <C value="13.519" />
-  <D value="-0.0000013811" />
-  <E value="-1.0182E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34066" />
-  <B value="-433.78" />
-  <C value="-97.746" />
-  <D value="-34416" />
-  <E value="59442" />
-  <Tmin units="K"  value="305" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.7174" />
-  <B value="1148.5" />
-  <C value="-0.42278" />
-  <D value="0.000000818" />
-  <E value="2" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="438.85" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.0899E-07" />
-  <B value="0.5228" />
-  <C value="260.59" />
-  <D value="-971.93" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.16198" />
-  <B value="12.531" />
-  <C value="-1.1439" />
-  <D value="-0.00019006" />
-  <E value="-7.9079E-07" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="488" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000039332" />
-  <B value="1.1131" />
-  <C value="-152.11" />
-  <D value="174490" />
-  <Tmin units="K"  value="438.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0091915" />
-  <B value="41.648" />
-  <C value="-3.2196" />
-  <D value="0.0001215" />
-  <E value="-0.0000043751" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="610" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="3419.1" />
-  <B value="914.32" />
-  <C value="-0.46014" />
-  <D value="0.000082394" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.928" />
-  <B value="3434.7" />
-  <C value="-73.509" />
-  <Tmin units="K"  value="374.15" />
-  <Tmax units="K"  value="541.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4192" />
-  <B value="-0.015045" />
-  <Tmin units="K"  value="174.45" />
-  <Tmax units="K"  value="438.85" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.616046" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.342286E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="264.7862" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.82" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0754875" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.736664" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.465073" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.195426" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.196599" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.012" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.465073" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15500" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.195426" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="17301-94-9" />
-<Smiles name="SMILES"  value="CCCC(C)CCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="88" />
-<CompoundID name="Name"  value="5-methylnonane" />
-<StructureFormula name="Structure"  value="CH3(CH2)3CH(CH3)(CH2)3CH3" />
-<Family name="Family"  value="2" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="609.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2140000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.5904" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="438.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="186" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="185.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000438465" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.282" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.195298" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.456177" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.318E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15440" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10917" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.503E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.5472E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.06E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="536500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.66E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.291E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.2082" />
-  <B value="-0.0043126" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="74.18" />
-  <Tmax units="K"  value="185.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.41463" />
-  <B value="0.2529" />
-  <C value="610.01" />
-  <D value="0.28051" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="610" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="215.6392" />
-  <B value="-13712.31" />
-  <C value="-29.15861" />
-  <D value="0.0000236309" />
-  <E value="2" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="610" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.5588E+07" />
-  <B value="0.029762" />
-  <C value="1.6061" />
-  <D value="-2.0417" />
-  <E value="0.80324" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="587.66" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="759980" />
-  <B value="-25254" />
-  <C value="344.7" />
-  <D value="-1.9725" />
-  <E value="0.0041285" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="180" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="230160" />
-  <B value="-61.977" />
-  <C value="9.1603" />
-  <D value="0.0096645" />
-  <E value="-0.0000061376" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="550" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="131700" />
-  <B value="-594.98" />
-  <C value="13.529" />
-  <D value="-0.000014234" />
-  <E value="-5.0987E-09" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34066" />
-  <B value="-433.78" />
-  <C value="-97.746" />
-  <D value="-34416" />
-  <E value="59442" />
-  <Tmin units="K"  value="305" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-13.838" />
-  <B value="1303.8" />
-  <C value="0.41828" />
-  <D value="-8.7942E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="438.3" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.7631E-07" />
-  <B value="0.50736" />
-  <C value="283.05" />
-  <D value="-1279.5" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.183" />
-  <B value="10.49" />
-  <C value="-1.0698" />
-  <D value="-0.00021616" />
-  <E value="-6.8913E-07" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="488" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00003614" />
-  <B value="1.1239" />
-  <C value="-159.13" />
-  <D value="172680" />
-  <Tmin units="K"  value="438.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015552" />
-  <B value="22.28" />
-  <C value="-2.8961" />
-  <D value="-0.00075059" />
-  <E value="-0.0000023626" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="587.66" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="4321" />
-  <B value="909.02" />
-  <C value="-0.45451" />
-  <D value="0.000080712" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.621" />
-  <B value="3256.6" />
-  <C value="-80.185" />
-  <Tmin units="K"  value="367.15" />
-  <Tmax units="K"  value="542.97" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.6594" />
-  <B value="-0.014236" />
-  <Tmin units="K"  value="185.45" />
-  <Tmax units="K"  value="438.3" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.616046" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.342286E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="263.0172" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="209.82" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0758946" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.736351" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.456177" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.195298" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.196599" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.012" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.456177" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15440" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.195298" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="6" />
-  <group id="3"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="15869-85-9" />
-<Smiles name="SMILES"  value="CCCCC(C)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="217" />
-<CompoundID name="Name"  value="Cis-2-hexene" />
-<StructureFormula name="Structure"  value="CH3CHCH(CH2)2CH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="511.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3160000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.345" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="342.03" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="132" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="132.03" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000232" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.1595" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1234" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.287374" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.76E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15360" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.015E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06474" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.1E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.856E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="8.025E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="386500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8857530" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.90348" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.728E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.357" />
-  <B value="-0.010385" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="52.81" />
-  <Tmax units="K"  value="132.03" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77464" />
-  <B value="0.2672" />
-  <C value="511.4" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="132.03" />
-  <Tmax units="K"  value="511.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="104.3995" />
-  <B value="-6791.221" />
-  <C value="-12.84602" />
-  <D value="0.0000165576" />
-  <E value="2" />
-  <Tmin units="K"  value="132.03" />
-  <Tmax units="K"  value="511.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.9E+07" />
-  <B value="1.281" />
-  <C value="-2.4971" />
-  <D value="2.499" />
-  <E value="-0.86824" />
-  <Tmin units="K"  value="132" />
-  <Tmax units="K"  value="491.43" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-9903.7" />
-  <B value="833.78" />
-  <C value="12.723" />
-  <D value="-0.19752" />
-  <E value="0.00078189" />
-  <Tmin units="K"  value="11.37" />
-  <Tmax units="K"  value="121.04" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="135610" />
-  <B value="570.7" />
-  <C value="1.6392" />
-  <D value="0.033591" />
-  <E value="-0.000032605" />
-  <Tmin units="K"  value="132.03" />
-  <Tmax units="K"  value="342.03" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="88576" />
-  <B value="-789.82" />
-  <C value="13.286" />
-  <D value="-0.00034537" />
-  <E value="1.0091E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20114" />
-  <B value="-212.36" />
-  <C value="-29.612" />
-  <D value="-2416.2" />
-  <E value="3113.2" />
-  <Tmin units="K"  value="256.58" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.864" />
-  <B value="787.8" />
-  <C value="0.0025561" />
-  <D value="-7.6676E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="132" />
-  <Tmax units="K"  value="342.03" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.6061E-08" />
-  <B value="0.91362" />
-  <C value="-8.4415" />
-  <D value="1515.2" />
-  <Tmin units="K"  value="132.03" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.038625" />
-  <B value="3.4165" />
-  <C value="-1.4421" />
-  <D value="-0.00078927" />
-  <E value="-0.0000017176" />
-  <Tmin units="K"  value="132" />
-  <Tmax units="K"  value="342.03" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000053674" />
-  <B value="1.0887" />
-  <C value="-86.934" />
-  <D value="155330" />
-  <Tmin units="K"  value="342.03" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.022589" />
-  <B value="9.4677" />
-  <C value="-2.677" />
-  <D value="-0.0011032" />
-  <E value="-0.0000022065" />
-  <Tmin units="K"  value="132" />
-  <Tmax units="K"  value="491.43" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="4117" />
-  <B value="473.05" />
-  <C value="-0.20948" />
-  <D value="0.000030849" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.749" />
-  <B value="2696.8" />
-  <C value="-49.605" />
-  <Tmin units="K"  value="310.54" />
-  <Tmax units="K"  value="451.5" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3865" />
-  <B value="-0.016275" />
-  <Tmin units="K"  value="132" />
-  <Tmax units="K"  value="342.03" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.347104" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.713722E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="247.3648" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.256" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.14884" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.046217" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.691499" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.287374" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1234" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2677" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.643" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.003966" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.43397" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.287374" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15360" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1234" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="7688-21-3" />
-<Smiles name="SMILES"  value="C/C=C\CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="218" />
-<CompoundID name="Name"  value="Trans-2-hexene" />
-<StructureFormula name="Structure"  value="CH3CHCH(CH2)2CH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="509.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3168000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.345" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.258" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="341.02" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="140.17" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="140.17" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00179" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.1595" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.125" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.288635" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.616E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06474" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.1E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.381E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.675E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8255030" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.9628" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.72648E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.09" />
-  <B value="-0.0094736" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="56.07" />
-  <Tmax units="K"  value="140.17" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.7854" />
-  <B value="0.271" />
-  <C value="509.8" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="509.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="102.7613" />
-  <B value="-6858.249" />
-  <C value="-12.46469" />
-  <D value="0.0000134849" />
-  <E value="2" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="509.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.402196E+07" />
-  <B value="0.563356" />
-  <C value="-0.497314" />
-  <D value="0.306975" />
-  <E value="0.0161359" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="490.35" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="2070" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="140.17" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="145330" />
-  <B value="591.61" />
-  <C value="0.45085" />
-  <D value="0.040176" />
-  <E value="-0.000043449" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="341.02" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="96839" />
-  <B value="-758.81" />
-  <C value="13.112" />
-  <D value="-0.00018911" />
-  <E value="4.7057E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21635" />
-  <B value="-262.77" />
-  <C value="-18.97" />
-  <D value="-7202.8" />
-  <E value="15014" />
-  <Tmin units="K"  value="256.58" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.296" />
-  <B value="798.85" />
-  <C value="0.074688" />
-  <D value="-2.5765E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="341.02" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.5985E-08" />
-  <B value="0.91455" />
-  <C value="-9.2013" />
-  <D value="1687.6" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.091076" />
-  <B value="-0.14352" />
-  <C value="-1.1963" />
-  <D value="-0.00093801" />
-  <E value="-0.0000007123" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="341.02" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000094853" />
-  <B value="1.0175" />
-  <C value="2.8366" />
-  <D value="154410" />
-  <Tmin units="K"  value="341.02" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.024183" />
-  <B value="-0.32166" />
-  <C value="-2.4994" />
-  <D value="-0.0018373" />
-  <E value="-0.0000012135" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="490.35" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="19670" />
-  <B value="436.93" />
-  <C value="-0.1814" />
-  <D value="0.000023027" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.853" />
-  <B value="2752.4" />
-  <C value="-45.95" />
-  <Tmin units="K"  value="308.15" />
-  <Tmax units="K"  value="451.44" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.6015" />
-  <B value="-0.015521" />
-  <Tmin units="K"  value="140.17" />
-  <Tmax units="K"  value="341.02" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.347104" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.651318E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="253.5968" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.258" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.32659" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0459435" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.682799" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.288635" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.125" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2677" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.643" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.004891" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.67446" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.288635" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15250" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.125" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="4050-45-7" />
-<Smiles name="SMILES"  value="C/C=C/CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="250" />
-<CompoundID name="Name"  value="1-octene" />
-<StructureFormula name="Structure"  value="CH2CH(CH2)5CH3" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="567" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2680000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.468" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="394.44" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="171.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="171.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00298" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.215" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15785" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.393" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.457E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15540" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.4E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08523" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.181E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-8.194E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.057E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="463700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.531E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0842" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.961E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.1732" />
-  <B value="-0.0061137" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="68.58" />
-  <Tmax units="K"  value="171.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.44684" />
-  <B value="0.23463" />
-  <C value="567" />
-  <D value="0.24846" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="566.9" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="177.7155" />
-  <B value="-11137.29" />
-  <C value="-23.58923" />
-  <D value="0.000019592" />
-  <E value="2" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="566.9" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.7062E+07" />
-  <B value="0.3453" />
-  <C value="0.41628" />
-  <D value="-0.36125" />
-  <E value="-0.059539" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="566.9" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-18727" />
-  <B value="1711.3" />
-  <C value="-4.6191" />
-  <D value="-0.021907" />
-  <E value="0.00013331" />
-  <Tmin units="K"  value="12" />
-  <Tmax units="K"  value="171.48" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-24253" />
-  <B value="87.834" />
-  <C value="11.35" />
-  <D value="0.0032002" />
-  <E value="-0.0000012467" />
-  <Tmin units="K"  value="171" />
-  <Tmax units="K"  value="454" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="106430" />
-  <B value="-593.77" />
-  <C value="13.154" />
-  <D value="0.00006689" />
-  <E value="-2.6274E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26737" />
-  <B value="-340.49" />
-  <C value="-61.032" />
-  <D value="-4988.1" />
-  <E value="1129.3" />
-  <Tmin units="K"  value="264" />
-  <Tmax units="K"  value="1983.1" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-5.8042" />
-  <B value="945.32" />
-  <C value="-0.93827" />
-  <D value="0.0000032767" />
-  <E value="2" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="453.52" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000047664" />
-  <B value="0.084052" />
-  <C value="3514.6" />
-  <D value="21127" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.035226" />
-  <B value="40.754" />
-  <C value="-2.2668" />
-  <D value="0.00092297" />
-  <E value="-0.0000060301" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="513.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000014109" />
-  <B value="1.354" />
-  <C value="610.51" />
-  <D value="-30915" />
-  <Tmin units="K"  value="394.41" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.14483" />
-  <B value="-2.7807" />
-  <C value="-1.5504" />
-  <D value="-0.00091294" />
-  <E value="4.2416E-07" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="566.9" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="72710" />
-  <B value="110.08" />
-  <C value="1.2552" />
-  <D value="-0.0017373" />
-  <E value="6.9559E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.5046" />
-  <B value="-1050" />
-  <C value="-6.3" />
-  <Tmin units="K"  value="278.5945" />
-  <Tmax units="K"  value="448.5945" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.716" />
-  <B value="3032.4" />
-  <C value="-64.529" />
-  <Tmin units="K"  value="340.25" />
-  <Tmax units="K"  value="504.46" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.9394" />
-  <B value="-0.012055" />
-  <Tmin units="K"  value="171.45" />
-  <Tmax units="K"  value="453.52" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.465907" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.097994E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="314.8257" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.266" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.37034" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0596194" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.720816" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.393" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15785" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.6185" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.724" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.002307" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.78497" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.393" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15540" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15785" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-66-0" />
-<Smiles name="SMILES"  value="C=CCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="259" />
-<CompoundID name="Name"  value="1-nonene" />
-<StructureFormula name="Structure"  value="CH2CH(CH2)6CH3" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="594" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2330000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.526" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="420.03" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="191.91" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="191.91" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0204" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="126.242" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.17405" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.411" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.873E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15500" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09546" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.316E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.035E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.123E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="504100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.9359E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1406" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5716E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.0944" />
-  <B value="-0.0047703" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="76.76" />
-  <Tmax units="K"  value="191.91" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.18062" />
-  <B value="0.15802" />
-  <C value="594" />
-  <D value="0.18969" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="593.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="120.37" />
-  <B value="-9418.7" />
-  <C value="-14.583" />
-  <D value="0.0000094863" />
-  <E value="2" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="593.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.0729E+07" />
-  <B value="-0.72017" />
-  <C value="3.2276" />
-  <D value="-3.6347" />
-  <E value="1.4659" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="593.1" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16015" />
-  <B value="1468.8" />
-  <C value="2.0005" />
-  <D value="-0.064925" />
-  <E value="0.00021824" />
-  <Tmin units="K"  value="11" />
-  <Tmax units="K"  value="191.92" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="58309" />
-  <B value="119.15" />
-  <C value="10.75" />
-  <D value="0.0042025" />
-  <E value="-0.0000015805" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="475" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122350" />
-  <B value="-622.4" />
-  <C value="13.352" />
-  <D value="-0.000015236" />
-  <E value="-2.3169E-10" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21322" />
-  <B value="-235.69" />
-  <C value="-117.36" />
-  <D value="37005" />
-  <E value="-118360" />
-  <Tmin units="K"  value="297" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.296" />
-  <B value="1057.3" />
-  <C value="-0.12431" />
-  <D value="2.0281E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="420.02" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.2319E-08" />
-  <B value="0.81707" />
-  <C value="155.31" />
-  <D value="-12572" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.024602" />
-  <B value="-118.29" />
-  <C value="-0.40946" />
-  <D value="-0.0056136" />
-  <E value="0.0000021909" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="533.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000019761" />
-  <B value="1.2983" />
-  <C value="563.96" />
-  <D value="24829" />
-  <Tmin units="K"  value="400" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.13785" />
-  <B value="-6.5227" />
-  <C value="-1.5557" />
-  <D value="-0.00098337" />
-  <E value="4.6887E-07" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="593.1" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="82837" />
-  <B value="113.94" />
-  <C value="1.4559" />
-  <D value="-0.0020124" />
-  <E value="0.000000806" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.098" />
-  <B value="3433.4" />
-  <C value="-61.353" />
-  <Tmin units="K"  value="357.35" />
-  <Tmax units="K"  value="529.75" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.6813" />
-  <B value="-0.01221" />
-  <Tmin units="K"  value="191.91" />
-  <Tmax units="K"  value="420.02" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.528415" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.027215E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="256.2865" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="184.68" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.34446" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0667997" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.734403" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.411" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.17405" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.2929" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.264" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000564" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.80187" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.411" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15500" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.17405" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="124-11-8" />
-<Smiles name="SMILES"  value="C=CCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="261" />
-<CompoundID name="Name"  value="1-undecene" />
-<StructureFormula name="Structure"  value="CH3(CH2)8CHCH2" />
-<Family name="Family"  value="9" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="637.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2044000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.657" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="465.82" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="223.99" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="223.99" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0473" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="154.292" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.2065" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.522466" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.485E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15680" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.8E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1159" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.586E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.449E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.283E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="582180" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.699E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3343" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.7878E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.5724" />
-  <B value="-0.0032733" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="89.6" />
-  <Tmax units="K"  value="223.99" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.38001" />
-  <B value="0.24991" />
-  <C value="637.8" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="637.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="93.64799" />
-  <B value="-9306.494" />
-  <C value="-10.26144" />
-  <D value="4.149832E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="637.9" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.3696E+07" />
-  <B value="-6.3933" />
-  <C value="18.084" />
-  <D value="-19.033" />
-  <E value="7.4719" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="616.02" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-40578" />
-  <B value="-2250300" />
-  <C value="33508" />
-  <D value="-165.17" />
-  <E value="0.26994" />
-  <Tmin units="K"  value="217.3" />
-  <Tmax units="K"  value="226.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="99868" />
-  <B value="144.48" />
-  <C value="10.69" />
-  <D value="0.0042614" />
-  <E value="-0.0000010791" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="591.88" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="138670" />
-  <B value="-549.63" />
-  <C value="13.4" />
-  <D value="0.00014861" />
-  <E value="-5.2026E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.46674" />
-  <B value="-604.66" />
-  <C value="-91.632" />
-  <D value="-141600" />
-  <E value="329750" />
-  <Tmin units="K"  value="318.9" />
-  <Tmax units="K"  value="1773" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-49.01257" />
-  <B value="2643.166" />
-  <C value="5.957949" />
-  <D value="-8.451873E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="523.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.0406E-08" />
-  <B value="0.85093" />
-  <C value="112.38" />
-  <D value="-8900.1" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.067847" />
-  <B value="-250.41" />
-  <C value="0.40201" />
-  <D value="-0.0082828" />
-  <E value="0.0000014058" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="465.82" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000018335" />
-  <B value="1.3031" />
-  <C value="709.58" />
-  <D value="-2804.6" />
-  <Tmin units="K"  value="465.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0077397" />
-  <B value="78.944" />
-  <C value="-3.6355" />
-  <D value="0.0014924" />
-  <E value="-0.0000057786" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="616.02" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-7374.7" />
-  <B value="1015.1" />
-  <C value="-0.57607" />
-  <D value="0.00012723" />
-  <Tmin units="K"  value="273.16" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.051" />
-  <B value="3677.5" />
-  <C value="-79.724" />
-  <Tmin units="K"  value="383.57" />
-  <Tmax units="K"  value="573.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.5498" />
-  <B value="-0.01112" />
-  <Tmin units="K"  value="223.99" />
-  <Tmax units="K"  value="523.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.660788" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.440253E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="295.6865" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="225.72" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.793" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.080937" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.754663" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.522466" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.2065" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.6417" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.344" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.010786" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.6965" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.522466" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15680" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2065" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="8" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="821-95-4" />
-<Smiles name="SMILES"  value="C=CCCCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="221" />
-<CompoundID name="Name"  value="2-methyl-1-pentene" />
-<StructureFormula name="Structure"  value="CH2C(CH3)CH2CH2CH3" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="507" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3160000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.359" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="335.26" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="137.43" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="137.42" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000805463" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.1595" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.124649" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.261138" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.704E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15070" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.89E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06475" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.41E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.22581E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.2969E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="374000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7029120" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.94792" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.72209E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.183" />
-  <B value="-0.009706" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="54.97" />
-  <Tmax units="K"  value="137.42" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.13372" />
-  <B value="0.11276" />
-  <C value="507" />
-  <D value="0.1472" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="505" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="85.161" />
-  <B value="-6171.1" />
-  <C value="-9.6632" />
-  <D value="0.0000085639" />
-  <E value="2" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="505" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.397303E+07" />
-  <B value="1.23932" />
-  <C value="-1.433928" />
-  <D value="0.797889" />
-  <E value="-0.142823" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="505" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="156060" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="507" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="173630" />
-  <B value="-41311" />
-  <C value="386.78" />
-  <D value="-1.1602" />
-  <E value="0.0012063" />
-  <Tmin units="K"  value="177.45" />
-  <Tmax units="K"  value="335.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="92049" />
-  <B value="-683.66" />
-  <C value="13.009" />
-  <D value="-0.000089454" />
-  <E value="1.0969E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20427" />
-  <B value="-211.93" />
-  <C value="-28.323" />
-  <D value="-2202.1" />
-  <E value="2802.7" />
-  <Tmin units="K"  value="253.58" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.406" />
-  <B value="797.71" />
-  <C value="0.099228" />
-  <D value="-5.3373E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="335.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.3076E-07" />
-  <B value="0.52447" />
-  <C value="272.22" />
-  <D value="-3046.8" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.026056" />
-  <B value="4.3913" />
-  <C value="-1.6749" />
-  <D value="-0.00048682" />
-  <E value="-0.0000023385" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="335.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000074858" />
-  <B value="1.0485" />
-  <C value="-32.169" />
-  <D value="140340" />
-  <Tmin units="K"  value="335.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010227" />
-  <B value="29.367" />
-  <C value="-3.1888" />
-  <D value="0.00017808" />
-  <E value="-0.0000061262" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="505" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="12977" />
-  <B value="480.34" />
-  <C value="-0.23191" />
-  <D value="0.000039315" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.723" />
-  <B value="2655.1" />
-  <C value="-46.569" />
-  <Tmin units="K"  value="305.25" />
-  <Tmax units="K"  value="446.96" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.556" />
-  <B value="-0.015605" />
-  <Tmin units="K"  value="137.42" />
-  <Tmax units="K"  value="335.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.34716" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.647237E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="262.9221" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.45874" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0451328" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.686845" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.261138" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.124649" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2689" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.64" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.00519" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.95865" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.261138" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15070" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.124649" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="5"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="763-29-1" />
-<Smiles name="SMILES"  value="C=C(C)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="227" />
-<CompoundID name="Name"  value="4-methyl-cis-2-pentene" />
-<StructureFormula name="Structure"  value="CH3CHCHCH(CH3)2" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="499" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3220000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.346" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="329.53" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="138.72" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="138.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00215772" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.1595" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.126648" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.244178" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.621E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14610" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.18E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06473" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.09E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.03335E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.69856E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="373338" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7363840" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.72502E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.041" />
-  <B value="-0.0096786" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="55.32" />
-  <Tmax units="K"  value="138.3" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77793" />
-  <B value="0.27017" />
-  <C value="499" />
-  <D value="0.2861" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="480.02" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="83.573" />
-  <B value="-5993.9" />
-  <C value="-9.4501" />
-  <D value="0.0000085686" />
-  <E value="2" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="499" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.4227E+07" />
-  <B value="1.5628" />
-  <C value="-2.6171" />
-  <D value="2.4298" />
-  <E value="-0.92758" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="480.02" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="156060" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="499" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-59803" />
-  <B value="-16.203" />
-  <C value="11.773" />
-  <D value="0.0034333" />
-  <E value="-0.0000037581" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="329.53" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="101130" />
-  <B value="-861.95" />
-  <C value="13.463" />
-  <D value="-0.00060529" />
-  <E value="2.0212E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19352" />
-  <B value="-193.4" />
-  <C value="-26.471" />
-  <D value="-1593.9" />
-  <E value="1901.2" />
-  <Tmin units="K"  value="249.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.752" />
-  <B value="820.42" />
-  <C value="0.14056" />
-  <D value="-7.3435E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="329.53" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.3021E-07" />
-  <B value="0.52941" />
-  <C value="268.94" />
-  <D value="16.597" />
-  <Tmin units="K"  value="329.53" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.050868" />
-  <B value="4.0553" />
-  <C value="-1.554" />
-  <D value="-0.00045968" />
-  <E value="-0.000001981" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="329.53" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000052516" />
-  <B value="1.0978" />
-  <C value="-60.883" />
-  <D value="128130" />
-  <Tmin units="K"  value="329.53" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011598" />
-  <B value="20.102" />
-  <C value="-3.0908" />
-  <D value="-0.00038666" />
-  <E value="-0.0000050432" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="480.02" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="16890" />
-  <B value="454.86" />
-  <C value="-0.20446" />
-  <D value="0.000032855" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.651" />
-  <B value="2585.2" />
-  <C value="-46.215" />
-  <Tmin units="K"  value="299.87" />
-  <Tmax units="K"  value="442.05" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4146" />
-  <B value="-0.016461" />
-  <Tmin units="K"  value="138.3" />
-  <Tmax units="K"  value="329.53" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.347048" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.33239E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="288.4841" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0450895" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.674097" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.244178" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.126648" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2669" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.639" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.001675" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.244178" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14610" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.126648" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="691-38-3" />
-<Smiles name="SMILES"  value="C/C=C\C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="228" />
-<CompoundID name="Name"  value="4-methyl-trans-2-pentene" />
-<StructureFormula name="Structure"  value="CH3CHCHCH(CH3)2" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="501" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3220000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.346" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="331.76" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="132.36" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="132.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000344783" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="84.1595" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.126739" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.255237" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.766E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.63E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06473" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.09E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.43501E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7.43497E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="368390" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7154640" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.7205E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.074" />
-  <B value="-0.0099849" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="52.94" />
-  <Tmax units="K"  value="132.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77321" />
-  <B value="0.26966" />
-  <C value="501" />
-  <D value="0.28578" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="501" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.691" />
-  <B value="-5972.8" />
-  <C value="-9.1408" />
-  <D value="0.0000081285" />
-  <E value="2" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="501" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.3985E+07" />
-  <B value="1.4966" />
-  <C value="-2.4784" />
-  <D value="2.2857" />
-  <E value="-0.85991" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="501" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="156060" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="501" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="22279" />
-  <B value="6.5061" />
-  <C value="10.859" />
-  <D value="0.0058182" />
-  <E value="-0.000006387" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="331.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="95377" />
-  <B value="-622.83" />
-  <C value="12.814" />
-  <D value="0.000074545" />
-  <E value="-3.6318E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19736" />
-  <B value="-224.61" />
-  <C value="-21.903" />
-  <D value="488.25" />
-  <E value="-2649.6" />
-  <Tmin units="K"  value="250.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.038" />
-  <B value="805.55" />
-  <C value="0.01464" />
-  <D value="-7.2359E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="331.75" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.4971E-07" />
-  <B value="0.50587" />
-  <C value="292.11" />
-  <D value="780.77" />
-  <Tmin units="K"  value="331.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.02241" />
-  <B value="4.5423" />
-  <C value="-1.7038" />
-  <D value="-0.00048445" />
-  <E value="-0.0000024834" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="331.75" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000062348" />
-  <B value="1.0772" />
-  <C value="-17.479" />
-  <D value="116240" />
-  <Tmin units="K"  value="331.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.008865" />
-  <B value="28.019" />
-  <C value="-3.2795" />
-  <D value="0.00029139" />
-  <E value="-0.0000066732" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="501" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="23417" />
-  <B value="462.06" />
-  <C value="-0.22421" />
-  <D value="0.000039309" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.694" />
-  <B value="2614" />
-  <C value="-46.685" />
-  <Tmin units="K"  value="300.98" />
-  <Tmax units="K"  value="442.79" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.1984" />
-  <B value="-0.017331" />
-  <Tmin units="K"  value="132.35" />
-  <Tmax units="K"  value="331.75" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.347048" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.389352E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="281.9625" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="123.12" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0450719" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.673532" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.255237" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.126739" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2669" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.639" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.000704" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.255237" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14730" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.126739" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="674-76-0" />
-<Smiles name="SMILES"  value="C/C=C/C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="270" />
-<CompoundID name="Name"  value="Cyclohexene" />
-<StructureFormula name="Structure"  value="-CH2CHCHCH2CH2CH2-" />
-<Family name="Family"  value="13" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="560.42" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4350000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.291" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="356.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="169.67" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="169.67" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.103772" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="82.1436" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.101877" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.212302" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.157E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17420" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.83E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05672" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.99E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4520000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.077E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="310750" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3290000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.815753" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.532E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.172" />
-  <B value="-0.0093983" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="67.87" />
-  <Tmax units="K"  value="169.67" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.807" />
-  <B value="0.25253" />
-  <C value="560.42" />
-  <D value="0.26738" />
-  <Tmin units="K"  value="169.67" />
-  <Tmax units="K"  value="560.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="82.052" />
-  <B value="-6388.7" />
-  <C value="-9.1035" />
-  <D value="0.0000071317" />
-  <E value="2" />
-  <Tmin units="K"  value="169.67" />
-  <Tmax units="K"  value="560.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.794402E+07" />
-  <B value="1.587579" />
-  <C value="-2.225474" />
-  <D value="1.109627" />
-  <E value="0.041589" />
-  <Tmin units="K"  value="169.67" />
-  <Tmax units="K"  value="560.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-106910" />
-  <B value="3261.1" />
-  <C value="-17.561" />
-  <D value="0.022428" />
-  <E value="0.000070624" />
-  <Tmin units="K"  value="110" />
-  <Tmax units="K"  value="169.66" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97738" />
-  <B value="2.3363" />
-  <C value="7.7626" />
-  <D value="0.013772" />
-  <E value="-0.000011653" />
-  <Tmin units="K"  value="169.67" />
-  <Tmax units="K"  value="356.12" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="48919" />
-  <B value="-644.33" />
-  <C value="13.16" />
-  <D value="-0.0002758" />
-  <E value="9.0717E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17779" />
-  <B value="-223.3" />
-  <C value="-26.025" />
-  <D value="400.34" />
-  <E value="-7027.1" />
-  <Tmin units="K"  value="280.2" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.901" />
-  <B value="1159.3" />
-  <C value="0.11228" />
-  <D value="-1.9651E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000013322" />
-  <B value="0.45371" />
-  <C value="444.45" />
-  <D value="117.38" />
-  <Tmin units="K"  value="169.67" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11174" />
-  <B value="816.81" />
-  <C value="-14.373" />
-  <D value="0.055987" />
-  <E value="-0.00010104" />
-  <Tmin units="K"  value="169.67" />
-  <Tmax units="K"  value="383.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000094336" />
-  <B value="1.0783" />
-  <C value="568.3" />
-  <D value="34471" />
-  <Tmin units="K"  value="356.12" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011245" />
-  <B value="31.113" />
-  <C value="-2.988" />
-  <D value="0.00029997" />
-  <E value="-0.0000055654" />
-  <Tmin units="K"  value="169.67" />
-  <Tmax units="K"  value="560.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-29684" />
-  <B value="538" />
-  <C value="-0.28796" />
-  <D value="0.000056637" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.91" />
-  <B value="2943.1" />
-  <C value="-42.47" />
-  <Tmin units="K"  value="336.35" />
-  <Tmax units="K"  value="500" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.1149" />
-  <B value="-0.014108" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.302527" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.898296E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="337.1902" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="118.5" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0407571" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.816732" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.212302" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.101877" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.8143" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.027" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.212302" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17420" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.101877" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="4" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="4" />
-  <group id="6"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="4" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="6"  value="1" />
-  <group id="78"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-83-8" />
-<Smiles name="SMILES"  value="C1=CCCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="108" />
-<CompoundID name="Name"  value="1,1-dimethylcyclopentane" />
-<StructureFormula name="Structure"  value="-CH2C(CH3)2CH2CH2CH2-" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="547" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3445000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.36" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="361" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="203.36" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="203.68" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="9.04909" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.1861" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.130925" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.272354" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.43E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15460" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07045" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.07E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.3828E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.9037E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="359280" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1080000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.99405" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.2752E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.747" />
-  <B value="-0.0058701" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="81.34" />
-  <Tmax units="K"  value="203.36" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77031" />
-  <B value="0.27731" />
-  <C value="547" />
-  <D value="0.30161" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="547" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="80.69439" />
-  <B value="-6444.768" />
-  <C value="-8.840923" />
-  <D value="5.777915E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="547" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.4753E+07" />
-  <B value="1.835" />
-  <C value="-2.4221" />
-  <D value="1.0097" />
-  <E value="0.083052" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="547" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="182070" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="547" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63403" />
-  <B value="-76.912" />
-  <C value="11.112" />
-  <D value="0.0033685" />
-  <E value="-0.0000013786" />
-  <Tmin units="K"  value="213.87" />
-  <Tmax units="K"  value="361" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84040" />
-  <B value="-831.97" />
-  <C value="13.78" />
-  <D value="-0.00060484" />
-  <E value="0.0000001825" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22139" />
-  <B value="-197.51" />
-  <C value="-37.472" />
-  <D value="-7234" />
-  <E value="10587" />
-  <Tmin units="K"  value="273.5" />
-  <Tmax units="K"  value="1914.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.8132" />
-  <B value="901.76" />
-  <C value="-0.51373" />
-  <D value="0.0000011607" />
-  <E value="2" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="361" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000055348" />
-  <B value="0.28035" />
-  <C value="888.45" />
-  <D value="60.9" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.012548" />
-  <B value="-26.729" />
-  <C value="-1.3811" />
-  <D value="-0.0017046" />
-  <E value="-8.8213E-07" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="361" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0025566" />
-  <B value="0.60638" />
-  <C value="165.73" />
-  <D value="477660" />
-  <Tmin units="K"  value="361" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0074471" />
-  <B value="112.42" />
-  <C value="-4.128" />
-  <D value="0.0036419" />
-  <E value="-0.0000099747" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="547" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-40808" />
-  <B value="693.04" />
-  <C value="-0.36013" />
-  <D value="0.000068107" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.924" />
-  <B value="3024.7" />
-  <C value="-39.21" />
-  <Tmin units="K"  value="329.96" />
-  <Tmax units="K"  value="474.65" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.5541" />
-  <B value="-0.013334" />
-  <Tmin units="K"  value="203.36" />
-  <Tmax units="K"  value="361" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.379444" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.304016E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="333.4925" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.273" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.87279" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0500314" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.759292" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.272354" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.130925" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7193" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.856" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.013551" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.5932" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.272354" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15460" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.130925" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="4" />
-  <group id="80"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1638-26-2" />
-<Smiles name="SMILES"  value="C1(C)(C)CCCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="109" />
-<CompoundID name="Name"  value="Cis-1,2-dimethylcyclopentane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH(CH3)(CH2)3-" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="565.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3445050" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.37" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.271" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="372.68" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="219.26" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="219.26" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="24.1041" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.1861" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.127822" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2692" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.617E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16160" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07045" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.86E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.29453E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.58148E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="366142" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1657280" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.28203E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.765" />
-  <B value="-0.0054494" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="87.7" />
-  <Tmax units="K"  value="219.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.72465" />
-  <B value="0.26829" />
-  <C value="565.15" />
-  <D value="0.28378" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="565.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="88.755" />
-  <B value="-6920" />
-  <C value="-10.09" />
-  <D value="0.0000077797" />
-  <E value="2" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="565.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.8904E+07" />
-  <B value="1.2615" />
-  <C value="-1.6517" />
-  <D value="1.1747" />
-  <E value="-0.3566" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="565.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16020" />
-  <B value="3224.8" />
-  <C value="-26.696" />
-  <D value="0.09892" />
-  <E value="-0.00012985" />
-  <Tmin units="K"  value="146.85" />
-  <Tmax units="K"  value="213.09" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="91966" />
-  <B value="30.661" />
-  <C value="9.7483" />
-  <D value="0.0064492" />
-  <E value="-0.0000032985" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="372.68" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85421" />
-  <B value="-827.36" />
-  <C value="13.75" />
-  <D value="-0.00058187" />
-  <E value="1.7604E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19751" />
-  <B value="-161.53" />
-  <C value="-51.518" />
-  <D value="-2496.4" />
-  <E value="-2528.2" />
-  <Tmin units="K"  value="282.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-30.744" />
-  <B value="1578.9" />
-  <C value="3.2397" />
-  <D value="-0.0000069313" />
-  <E value="2" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="380.26" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.0794E-07" />
-  <B value="0.561" />
-  <C value="243.58" />
-  <D value="7280.5" />
-  <Tmin units="K"  value="372.68" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.014002" />
-  <B value="-51.607" />
-  <C value="-1.1286" />
-  <D value="-0.0024368" />
-  <E value="4.2617E-08" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="372.68" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.011269" />
-  <B value="0.40836" />
-  <C value="151.71" />
-  <D value="760020" />
-  <Tmin units="K"  value="372.68" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.12665" />
-  <B value="-13.427" />
-  <C value="-1.5337" />
-  <D value="-0.0012368" />
-  <E value="5.8475E-07" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="565.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-35696" />
-  <B value="676.86" />
-  <C value="-0.34653" />
-  <D value="0.000064464" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.883" />
-  <B value="3064.4" />
-  <C value="-45.216" />
-  <Tmin units="K"  value="344.26" />
-  <Tmax units="K"  value="492.33" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.0294" />
-  <B value="-0.011695" />
-  <Tmin units="K"  value="219.26" />
-  <Tmax units="K"  value="380.26" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.379444" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.418237E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="335.557" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.271" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0499538" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.777085" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2692" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.127822" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7192" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.772" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.006564" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2692" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16160" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.127822" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="3" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1192-18-3" />
-<Smiles name="SMILES"  value="C1[C@@](C)([H])([C@]([H])(C)(CC1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="110" />
-<CompoundID name="Name"  value="Trans-1,2-dimethylcyclopentane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH(CH3)(CH2)3-" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="553.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3445050" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.36" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.27" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="365.02" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="155.58" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="155.58" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00329595" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.1861" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.131474" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2692" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.607E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15760" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07045" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.86E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.36566E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.84928E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="366811" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7167190" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.27609E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.201" />
-  <B value="-0.0080527" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="62.23" />
-  <Tmax units="K"  value="155.58" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77149" />
-  <B value="0.27784" />
-  <C value="553.15" />
-  <D value="0.30964" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="532.23" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="89.97" />
-  <B value="-6815.6" />
-  <C value="-10.323" />
-  <D value="0.000008493" />
-  <E value="2" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="553.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.4143E+07" />
-  <B value="0.72069" />
-  <C value="0.072069" />
-  <D value="-0.93971" />
-  <E value="0.57146" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="532.23" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="182070" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="553.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-27570" />
-  <B value="-6.4733" />
-  <C value="11.325" />
-  <D value="0.0043522" />
-  <E value="-0.0000035776" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="365.02" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86316" />
-  <B value="-831.39" />
-  <C value="13.757" />
-  <D value="-0.0005975" />
-  <E value="1.8263E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19751" />
-  <B value="-158.14" />
-  <C value="-48.305" />
-  <D value="-2091.1" />
-  <E value="-2117" />
-  <Tmin units="K"  value="276.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.501" />
-  <B value="979.94" />
-  <C value="-0.073247" />
-  <D value="2.6464E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="365.02" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000015301" />
-  <B value="0.42849" />
-  <C value="479.07" />
-  <D value="3.9541" />
-  <Tmin units="K"  value="365.02" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.028286" />
-  <B value="5.044" />
-  <C value="-1.6594" />
-  <D value="-0.00043322" />
-  <E value="-0.000001941" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="365.02" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0087025" />
-  <B value="0.4463" />
-  <C value="190.1" />
-  <D value="689820" />
-  <Tmin units="K"  value="365.02" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013661" />
-  <B value="20.324" />
-  <C value="-2.8967" />
-  <D value="-0.0007348" />
-  <E value="-0.0000035142" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="532.23" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-34423" />
-  <B value="673.5" />
-  <C value="-0.34508" />
-  <D value="0.000064499" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.95" />
-  <B value="3051.5" />
-  <C value="-41.265" />
-  <Tmin units="K"  value="333.15" />
-  <Tmax units="K"  value="490.38" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.5731" />
-  <B value="-0.016451" />
-  <Tmin units="K"  value="155.58" />
-  <Tmax units="K"  value="365.02" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.379444" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.388162E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="324.0901" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.27" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0500017" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.75615" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2692" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.131474" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7192" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.772" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.009015" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2692" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15760" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.131474" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="3" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="3" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="822-50-4" />
-<Smiles name="SMILES"  value="C1[C@](C)([H])([C@]([H])(C)(CC1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="111" />
-<CompoundID name="Name"  value="Cis-1,3-dimethylcyclopentane" />
-<StructureFormula name="Structure"  value="-CH2CH(CH3)CH2CH(CH3)CH2-" />
-<Family name="Family"  value="3" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="551" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3633" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.277" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="364.71" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="139.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="139.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000172698" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.188" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13191" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.276" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.633E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15490" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07045" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.86E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.3585E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.9204E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="366810" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7397000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.2771E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.282" />
-  <B value="-0.0089936" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="55.78" />
-  <Tmax units="K"  value="139.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77224" />
-  <B value="0.27858" />
-  <C value="551" />
-  <D value="0.31293" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="551" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.262" />
-  <B value="-5561.3" />
-  <C value="-5.5932" />
-  <D value="0.0000039124" />
-  <E value="2" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="551" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.964754E+07" />
-  <B value="1.992198" />
-  <C value="-3.906039" />
-  <D value="3.442342" />
-  <E value="-1.064932" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="551" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="182070" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="551" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65786" />
-  <B value="-81.345" />
-  <C value="11.138" />
-  <D value="0.0032931" />
-  <E value="-0.0000013405" />
-  <Tmin units="K"  value="210.93" />
-  <Tmax units="K"  value="363.92" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86318" />
-  <B value="-831.43" />
-  <C value="13.758" />
-  <D value="-0.00059782" />
-  <E value="1.8276E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21788" />
-  <B value="-188.03" />
-  <C value="-39.482" />
-  <D value="-9836.4" />
-  <E value="17510" />
-  <Tmin units="K"  value="275.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.311" />
-  <B value="1000.6" />
-  <C value="0.063555" />
-  <D value="-2.0388E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="363.92" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.8359E-07" />
-  <B value="0.57388" />
-  <C value="271.6" />
-  <D value="-5017.7" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.041732" />
-  <B value="3.5995" />
-  <C value="-1.581" />
-  <D value="-0.00048911" />
-  <E value="-0.0000016476" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="363.92" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0021721" />
-  <B value="0.62882" />
-  <C value="203.61" />
-  <D value="446440" />
-  <Tmin units="K"  value="363.92" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0095794" />
-  <B value="29.018" />
-  <C value="-3.1051" />
-  <D value="-0.000049483" />
-  <E value="-0.00000529" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="551" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-20969" />
-  <B value="503.34" />
-  <C value="0.22474" />
-  <D value="-0.00062957" />
-  <E value="2.7945E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.065" />
-  <B value="3078.8" />
-  <C value="-41.512" />
-  <Tmin units="K"  value="332.1" />
-  <Tmax units="K"  value="486.02" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0328" />
-  <B value="-0.018355" />
-  <Tmin units="K"  value="139.45" />
-  <Tmax units="K"  value="363.92" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.379444" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.213806E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="353.9908" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.277" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0501818" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.750406" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.276" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.13191" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7192" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.772" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.001337" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.276" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15490" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.13191" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="3" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="3" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2532-58-3" />
-<Smiles name="SMILES"  value="C1[C@@](C)([H])(C[C@]([H])(C)(C1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="112" />
-<CompoundID name="Name"  value="Trans-1,3-dimethylcyclopentane" />
-<StructureFormula name="Structure"  value="-CH2CH(CH3)CH2CH(CH3)CH2-" />
-<Family name="Family"  value="3" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="553" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3633" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.276" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="363.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="139.18" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="139.18" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000437759" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.188" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13264" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.253" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.644E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15660" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07045" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.86E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.336E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.1463E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="366810" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7398000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.85958" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.279E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.285" />
-  <B value="-0.0090207" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="55.67" />
-  <Tmax units="K"  value="139.18" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77915" />
-  <B value="0.2805" />
-  <C value="553" />
-  <D value="0.30466" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="553" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="72.714" />
-  <B value="-6038.9" />
-  <C value="-7.709" />
-  <D value="0.0000063511" />
-  <E value="2" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="553" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.568557E+07" />
-  <B value="1.547069" />
-  <C value="-1.429715" />
-  <D value="-0.00159084" />
-  <E value="0.362451" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="553" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-20650" />
-  <B value="1946.2" />
-  <C value="-17.152" />
-  <D value="0.083188" />
-  <E value="-0.00011775" />
-  <Tmin units="K"  value="16.73" />
-  <Tmax units="K"  value="133.18" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="128140" />
-  <B value="215.87" />
-  <C value="5.2004" />
-  <D value="0.02446" />
-  <E value="-0.000024789" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="364.88" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86318" />
-  <B value="-831.43" />
-  <C value="13.758" />
-  <D value="-0.00059782" />
-  <E value="1.8276E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20356" />
-  <B value="-167.13" />
-  <C value="-48.07" />
-  <D value="-1089" />
-  <E value="-4751.1" />
-  <Tmin units="K"  value="276.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.152" />
-  <B value="996.91" />
-  <C value="0.036374" />
-  <D value="-1.1545E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="364.88" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000007023" />
-  <B value="0.52532" />
-  <C value="331.02" />
-  <D value="-5427.4" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.034026" />
-  <B value="3.551" />
-  <C value="-1.6156" />
-  <D value="-0.00049883" />
-  <E value="-0.0000017475" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="364.88" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0021472" />
-  <B value="0.63073" />
-  <C value="213.01" />
-  <D value="445470" />
-  <Tmin units="K"  value="364.88" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010805" />
-  <B value="26.324" />
-  <C value="-3.0571" />
-  <D value="-0.00014538" />
-  <E value="-0.0000048021" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="553" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-20969" />
-  <B value="503.34" />
-  <C value="0.22474" />
-  <D value="-0.00062957" />
-  <E value="2.7945E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.192" />
-  <B value="3238.2" />
-  <C value="-29.75" />
-  <Tmin units="K"  value="335.2" />
-  <Tmax units="K"  value="487.66" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0272" />
-  <B value="-0.018371" />
-  <Tmin units="K"  value="139.18" />
-  <Tmax units="K"  value="364.88" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.379444" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.240833E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="350.68" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.276" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.64" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0502618" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.753434" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.253" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.13264" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7192" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.772" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.017759" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.253" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15660" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.13264" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="3" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="3" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1759-58-6" />
-<Smiles name="SMILES"  value="C1[C@](C)([H])(C[C@]([H])(C)(C1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="115" />
-<CompoundID name="Name"  value="Isopropylcyclopentane" />
-<StructureFormula name="Structure"  value="(C5H9)CH(CH3)2" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="601" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.422" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="399.58" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="161.79" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="161.79" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000981869" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14527" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.302996" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.988E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15940" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07948" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.021E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.5071E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.305E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="407080" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.041E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.77168" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.8944E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.934" />
-  <B value="-0.007675" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="64.72" />
-  <Tmax units="K"  value="161.79" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.01997" />
-  <B value="0.048466" />
-  <C value="601" />
-  <D value="0.10484" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="593" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="70.74905" />
-  <B value="-6671.509" />
-  <C value="-7.204875" />
-  <D value="3.983606E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="593" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.807013E+07" />
-  <B value="1.420456" />
-  <C value="-3.256998" />
-  <D value="3.923183" />
-  <E value="-1.686337" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="593" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="208080" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="601" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="77318" />
-  <B value="-174.75" />
-  <C value="11.36" />
-  <D value="0.00375" />
-  <E value="-0.0000015189" />
-  <Tmin units="K"  value="296.5" />
-  <Tmax units="K"  value="444.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="31291" />
-  <B value="-392.29" />
-  <C value="12.88" />
-  <D value="0.0005799" />
-  <E value="-2.3026E-07" />
-  <Tmin units="K"  value="210" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27337" />
-  <B value="-340.23" />
-  <C value="-54.214" />
-  <D value="-3747.5" />
-  <E value="-9730.3" />
-  <Tmin units="K"  value="296.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.637" />
-  <B value="1116.2" />
-  <C value="0.10394" />
-  <D value="-3.9216E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="399.58" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.3283E-08" />
-  <B value="0.84204" />
-  <C value="92.528" />
-  <D value="-7299.5" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.057129" />
-  <B value="3.4704" />
-  <C value="-1.5201" />
-  <D value="-0.00050193" />
-  <E value="-0.0000011418" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="399.58" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.10336" />
-  <B value="0.072913" />
-  <C value="-474.32" />
-  <D value="1330800" />
-  <Tmin units="K"  value="399.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018773" />
-  <B value="0.51195" />
-  <C value="-2.5976" />
-  <D value="-0.001413" />
-  <E value="-0.0000015235" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="593" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-58984" />
-  <B value="846.07" />
-  <C value="-0.47718" />
-  <D value="0.000096903" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.93" />
-  <B value="3299.8" />
-  <C value="-48.694" />
-  <Tmin units="K"  value="362.52" />
-  <Tmax units="K"  value="530" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.3089" />
-  <B value="-0.016084" />
-  <Tmin units="K"  value="161.79" />
-  <Tmax units="K"  value="399.58" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.431762" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.080372E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="303.1565" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.58138" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.056894" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.781251" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.302996" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14527" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3936" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.008055" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.73788" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.302996" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15940" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14527" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="78"  value="4" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="3875-51-2" />
-<Smiles name="SMILES"  value="C1CCCC1(C(C)C)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="116" />
-<CompoundID name="Name"  value="1-methyl-1-ethylcyclopentane" />
-<StructureFormula name="Structure"  value="-C(CH3)(C2H5)CH2CH2CH2CH2-" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="582" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3020000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.428" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="394.672" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="129.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="129.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.16711E-07" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.144502" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.329811" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.773E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15840" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08182" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.099E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.549E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.067E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="401000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.88921E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="10.333" />
-  <B value="-0.0099857" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="51.74" />
-  <Tmax units="K"  value="129.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.62398" />
-  <B value="0.26553" />
-  <C value="582" />
-  <D value="0.28568" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="582" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="70.30095" />
-  <B value="-6628.265" />
-  <C value="-7.112201" />
-  <D value="3.497931E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="585" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.14848E+07" />
-  <B value="0.288357" />
-  <C value="0.487845" />
-  <D value="-0.669561" />
-  <E value="0.236062" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="582" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="208080" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="582" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="96111" />
-  <B value="-59.039" />
-  <C value="10.164" />
-  <D value="0.0078449" />
-  <E value="-0.0000067267" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="394.67" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="80936" />
-  <B value="-652.6" />
-  <C value="13.464" />
-  <D value="-0.00013102" />
-  <E value="2.6661E-08" />
-  <Tmin units="K"  value="152" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.040536" />
-  <B value="52.83" />
-  <C value="-127.64" />
-  <D value="96352" />
-  <E value="-263290" />
-  <Tmin units="K"  value="291" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.773" />
-  <B value="1099.9" />
-  <C value="-0.048343" />
-  <D value="1.7107E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="394.67" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.5602E-07" />
-  <B value="0.57042" />
-  <C value="274.82" />
-  <D value="-5055.3" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0033033" />
-  <B value="9.4359" />
-  <C value="-1.8646" />
-  <D value="-0.00027" />
-  <E value="-0.0000024258" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="394.67" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0026462" />
-  <B value="0.59802" />
-  <C value="270.85" />
-  <D value="473470" />
-  <Tmin units="K"  value="394.67" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012274" />
-  <B value="18.884" />
-  <C value="-2.9134" />
-  <D value="-0.00040243" />
-  <E value="-0.000003859" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="582" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-60886" />
-  <B value="871.1" />
-  <C value="-0.51466" />
-  <D value="0.00011578" />
-  <Tmin units="K"  value="152" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.867" />
-  <B value="3227" />
-  <C value="-49.268" />
-  <Tmin units="K"  value="350" />
-  <Tmax units="K"  value="520" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.1515" />
-  <B value="-0.01979" />
-  <Tmin units="K"  value="129.35" />
-  <Tmax units="K"  value="394.67" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.445576" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.858767E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="327.5493" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0567373" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.785294" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.329811" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.144502" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3937" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.396" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.014972" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.329811" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15840" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.144502" />
-<UnifacVLE name="UNIFAC" >
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-  <group id="4"  value="1" />
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-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
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-  <group id="4"  value="1" />
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-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="5" />
-  <group id="80"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="16747-50-5" />
-<Smiles name="SMILES"  value="C1CCCC1(C)(CC)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="122" />
-<CompoundID name="Name"  value="N-butylcyclopentane" />
-<StructureFormula name="Structure"  value="(C5H9)CH2CH2CH2CH3" />
-<Family name="Family"  value="6" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="621" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2710000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.482" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="429.75" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="165.165" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="165.18" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000370087" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="126.239" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.161572" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.37188" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.634E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16390" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09092" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.157E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.683E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.217E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="453800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.131E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5037E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.8832" />
-  <B value="-0.0067223" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="66.07" />
-  <Tmax units="K"  value="165.18" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.55321" />
-  <B value="0.26684" />
-  <C value="621" />
-  <D value="0.28873" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="597.01" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.57026" />
-  <B value="-7247.203" />
-  <C value="-5.051393" />
-  <D value="-2.973642E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="621" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.633912E+07" />
-  <B value="-0.222347" />
-  <C value="2.054738" />
-  <D value="-2.396364" />
-  <E value="0.924309" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="597.01" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15856" />
-  <B value="1577.6" />
-  <C value="-1.3452" />
-  <D value="-0.054207" />
-  <E value="0.00024372" />
-  <Tmin units="K"  value="14.41" />
-  <Tmax units="K"  value="154.28" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="165400" />
-  <B value="317.8" />
-  <C value="5.7051" />
-  <D value="0.0202" />
-  <E value="-0.000017103" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="429.75" />
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-  <eqno value="16" />
-  <A value="82154" />
-  <B value="-554.7" />
-  <C value="13.299" />
-  <D value="0.00015408" />
-  <E value="-5.7536E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.32315" />
-  <B value="-400.67" />
-  <C value="-80.571" />
-  <D value="-12802" />
-  <E value="-5984.5" />
-  <Tmin units="K"  value="310.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.446" />
-  <B value="1200.4" />
-  <C value="-0.12541" />
-  <D value="4.6316E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="429.75" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000029081" />
-  <B value="0.33269" />
-  <C value="700.46" />
-  <D value="-5220.4" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="1000" />
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-  <eqno value="16" />
-  <A value="-0.059329" />
-  <B value="3.6894" />
-  <C value="-1.5397" />
-  <D value="-0.00046539" />
-  <E value="-0.0000010217" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="429.75" />
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-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.001615" />
-  <B value="0.65033" />
-  <C value="212.05" />
-  <D value="447790" />
-  <Tmin units="K"  value="429.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
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-  <eqno value="16" />
-  <A value="-0.011464" />
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-  <C value="-3.0712" />
-  <D value="0.000095681" />
-  <E value="-0.000003989" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="597.01" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-39198" />
-  <B value="866.48" />
-  <C value="-0.45949" />
-  <D value="0.000092411" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.885" />
-  <B value="3420.5" />
-  <C value="-64.212" />
-  <Tmin units="K"  value="375.65" />
-  <Tmax units="K"  value="549.03" />
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-  <eqno value="12" />
-  <A value="-2.1614" />
-  <B value="-0.015728" />
-  <Tmin units="K"  value="165.18" />
-  <Tmax units="K"  value="429.75" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.500385" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.576352E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="292.0157" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="184.68" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0642821" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.789312" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.37188" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.161572" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.068799" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.856" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.37188" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16390" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.161572" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="7" />
-  <group id="3"  value="1" />
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-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
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-  </Umr>
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-<Smiles name="SMILES"  value="C1CCCC1(CCCC)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="141" />
-<CompoundID name="Name"  value="1,1-dimethylcyclohexane" />
-<StructureFormula name="Structure"  value="-C(CH3)2(CH2)5-" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="591.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2938430" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.45" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="392.69" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="239.66" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="239.66" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="60.5841" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.144469" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2376" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.668E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15670" />
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-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.042E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.81E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.52293E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="365012" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2020870" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.80822" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.8639E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
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-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="95.86" />
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-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.55073" />
-  <B value="0.24971" />
-  <C value="591.15" />
-  <D value="0.27534" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="591.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.518" />
-  <B value="-6942.5" />
-  <C value="-8.9" />
-  <D value="0.0000054941" />
-  <E value="2" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="591.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.5815E+07" />
-  <B value="2.7664" />
-  <C value="-6.0218" />
-  <D value="6.1598" />
-  <E value="-2.4093" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="591.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16424" />
-  <B value="1881.1" />
-  <C value="-20.206" />
-  <D value="0.13922" />
-  <E value="-0.00034887" />
-  <Tmin units="K"  value="12.31" />
-  <Tmax units="K"  value="141.61" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="108760" />
-  <B value="-1.4419" />
-  <C value="9.7271" />
-  <D value="0.0071596" />
-  <E value="-0.0000038148" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="392.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97627" />
-  <B value="-847.07" />
-  <C value="13.952" />
-  <D value="-0.00053736" />
-  <E value="1.4024E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2363" />
-  <B value="-268.25" />
-  <C value="-48.059" />
-  <D value="-9529.6" />
-  <E value="18562" />
-  <Tmin units="K"  value="295.58" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.7034" />
-  <B value="1042.4" />
-  <C value="-0.53177" />
-  <D value="8.3765E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="392.7" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.8141E-07" />
-  <B value="0.4995" />
-  <C value="371.04" />
-  <D value="124.2" />
-  <Tmin units="K"  value="392.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0057011" />
-  <B value="-80.549" />
-  <C value="-0.98212" />
-  <D value="-0.0030094" />
-  <E value="4.8733E-07" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="392.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.01079" />
-  <B value="0.39433" />
-  <C value="-74.36" />
-  <D value="805370" />
-  <Tmin units="K"  value="392.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.080643" />
-  <B value="-31.636" />
-  <C value="-1.6941" />
-  <D value="-0.0017816" />
-  <E value="8.0067E-07" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="591.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-48680" />
-  <B value="799.8" />
-  <C value="-0.38203" />
-  <D value="0.000059621" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.484" />
-  <B value="3005.4" />
-  <C value="-57.186" />
-  <Tmin units="K"  value="355.67" />
-  <Tmax units="K"  value="517.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4746" />
-  <B value="-0.012099" />
-  <Tmin units="K"  value="239.66" />
-  <Tmax units="K"  value="392.7" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438832" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.912149E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="341.7583" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.18749" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0567527" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.785287" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2376" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.144469" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3937" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.396" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.007389" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.07093" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2376" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15670" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.144469" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="5" />
-  <group id="80"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="590-66-9" />
-<Smiles name="SMILES"  value="C1CCCCC1(C)(C)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="142" />
-<CompoundID name="Name"  value="Cis-1,2-dimethylcyclohexane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH(CH3)(CH2)4-" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="606.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2938430" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.46" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="402.94" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="223.16" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="223.16" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.41394" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.141645" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2363" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.759E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16250" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08068" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.021E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.72172E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="4.12124E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="374510" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1645150" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.76657" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.87084E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.6128" />
-  <B value="-0.0047681" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="89.26" />
-  <Tmax units="K"  value="223.16" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.52003" />
-  <B value="0.24148" />
-  <C value="606.15" />
-  <D value="0.2655" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="606.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="79.675" />
-  <B value="-7110.6" />
-  <C value="-8.5422" />
-  <D value="0.0000045741" />
-  <E value="2" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="606.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.6247E+07" />
-  <B value="1.824" />
-  <C value="-3.744" />
-  <D value="3.9502" />
-  <E value="-1.5633" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="606.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13300" />
-  <B value="1529.1" />
-  <C value="-10.715" />
-  <D value="0.053025" />
-  <E value="-0.000098378" />
-  <Tmin units="K"  value="11.92" />
-  <Tmax units="K"  value="167.87" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="111710" />
-  <B value="52.625" />
-  <C value="9.3729" />
-  <D value="0.0077553" />
-  <E value="-0.0000040932" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="402.94" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="99210" />
-  <B value="-835.35" />
-  <C value="13.925" />
-  <D value="-0.00054754" />
-  <E value="1.5043E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23913" />
-  <B value="-321.51" />
-  <C value="-44.828" />
-  <D value="7459.3" />
-  <E value="-24725" />
-  <Tmin units="K"  value="303.08" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.312" />
-  <B value="1465.3" />
-  <C value="0.097955" />
-  <D value="-4.4792E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="484.92" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.4568E-07" />
-  <B value="0.48702" />
-  <C value="397.94" />
-  <D value="11.816" />
-  <Tmin units="K"  value="402.94" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.013234" />
-  <B value="-31.366" />
-  <C value="-1.3892" />
-  <D value="-0.0016087" />
-  <E value="-0.0000006162" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="402.94" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.015824" />
-  <B value="0.34516" />
-  <C value="-25.388" />
-  <D value="892770" />
-  <Tmin units="K"  value="402.94" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.11015" />
-  <B value="-24.856" />
-  <C value="-1.5182" />
-  <D value="-0.0015899" />
-  <E value="8.5396E-07" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="606.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-45273" />
-  <B value="798.91" />
-  <C value="-0.39513" />
-  <D value="0.000066999" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.431" />
-  <B value="3014.3" />
-  <C value="-64.403" />
-  <Tmin units="K"  value="364.26" />
-  <Tmax units="K"  value="525.52" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9831" />
-  <B value="-0.012867" />
-  <Tmin units="K"  value="223.16" />
-  <Tmax units="K"  value="484.92" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438832" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.994164E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="345.7631" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.268" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.52986" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0559709" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.800519" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2363" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.141645" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3936" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.014432" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.61866" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2363" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16250" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.141645" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="4" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2207-01-4" />
-<Smiles name="SMILES"  value="C1[C@@](C)([H])([C@]([H])(C)(CCC1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="143" />
-<CompoundID name="Name"  value="Trans-1,2-dimethylcyclohexane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH(CH3)(CH2)4-" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="596.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2938430" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.46" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="396.58" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="184.99" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="184.99" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0803872" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.145347" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2416" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.883E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15780" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08068" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.021E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.79996E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.44761E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="370912" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.04223E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.81029" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.86436E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.6758" />
-  <B value="-0.0058139" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="74" />
-  <Tmax units="K"  value="184.99" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54418" />
-  <B value="0.25029" />
-  <C value="596.15" />
-  <D value="0.26582" />
-  <Tmin units="K"  value="184.99" />
-  <Tmax units="K"  value="574.51" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="78.951" />
-  <B value="-6905.8" />
-  <C value="-8.4915" />
-  <D value="0.0000050406" />
-  <E value="2" />
-  <Tmin units="K"  value="184.99" />
-  <Tmax units="K"  value="596.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.3964E+07" />
-  <B value="1.6946" />
-  <C value="-3.2086" />
-  <D value="3.1663" />
-  <E value="-1.1947" />
-  <Tmin units="K"  value="184.99" />
-  <Tmax units="K"  value="574.51" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13403" />
-  <B value="1490.6" />
-  <C value="-9.8224" />
-  <D value="0.046599" />
-  <E value="-0.000082592" />
-  <Tmin units="K"  value="11.99" />
-  <Tmax units="K"  value="172.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="107760" />
-  <B value="95.278" />
-  <C value="8.9456" />
-  <D value="0.0091345" />
-  <E value="-0.000005166" />
-  <Tmin units="K"  value="183.68" />
-  <Tmax units="K"  value="396.58" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97739" />
-  <B value="-799.79" />
-  <C value="13.856" />
-  <D value="-0.00049041" />
-  <E value="1.3436E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23992" />
-  <B value="-317.9" />
-  <C value="-41.61" />
-  <D value="-1205.2" />
-  <E value="1133.9" />
-  <Tmin units="K"  value="298.08" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.8695" />
-  <B value="1124.4" />
-  <C value="-0.19468" />
-  <D value="4.6083E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="184.99" />
-  <Tmax units="K"  value="396.58" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000004616" />
-  <B value="0.56409" />
-  <C value="251.76" />
-  <D value="9969.9" />
-  <Tmin units="K"  value="396.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.096966" />
-  <B value="-4.6856" />
-  <C value="-1.2678" />
-  <D value="-0.00075424" />
-  <E value="-4.7962E-07" />
-  <Tmin units="K"  value="184.99" />
-  <Tmax units="K"  value="596.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.014659" />
-  <B value="0.3596" />
-  <C value="28.311" />
-  <D value="846250" />
-  <Tmin units="K"  value="396.58" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013995" />
-  <B value="21.416" />
-  <C value="-2.9689" />
-  <D value="-0.00029298" />
-  <E value="-0.0000033433" />
-  <Tmin units="K"  value="184.99" />
-  <Tmax units="K"  value="574.51" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-46666" />
-  <B value="819.31" />
-  <C value="-0.42362" />
-  <D value="0.000077591" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.538" />
-  <B value="3061.4" />
-  <C value="-56.887" />
-  <Tmin units="K"  value="358.11" />
-  <Tmax units="K"  value="531.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4752" />
-  <B value="-0.015117" />
-  <Tmin units="K"  value="184.99" />
-  <Tmax units="K"  value="396.58" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438832" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.840729E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="363.458" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.273" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.24932" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0569831" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.780271" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2416" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.145347" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3936" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.00729" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.23737" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2416" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15780" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.145347" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="4" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="6876-23-9" />
-<Smiles name="SMILES"  value="C1[C@](C)([H])([C@]([H])(C)(CCC1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="144" />
-<CompoundID name="Name"  value="Cis-1,3-dimethylcyclohexane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH2CH(CH3)(CH2)3-" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="591.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2938430" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.45" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="393.24" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="197.61" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="197.58" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.562747" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.147281" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2414" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.972E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15640" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08068" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.021E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.84765E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.98319E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="370451" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.08211E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91108" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.85972E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.4975" />
-  <B value="-0.0053365" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="79.03" />
-  <Tmax units="K"  value="197.58" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.56146" />
-  <B value="0.25431" />
-  <C value="591.15" />
-  <D value="0.28196" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="591.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="80.304" />
-  <B value="-6952.9" />
-  <C value="-8.6838" />
-  <D value="0.000005071" />
-  <E value="2" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="591.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.8345E+07" />
-  <B value="2.0984" />
-  <C value="-4.3187" />
-  <D value="4.4054" />
-  <E value="-1.7047" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="591.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12749" />
-  <B value="1536.3" />
-  <C value="-10.653" />
-  <D value="0.050633" />
-  <E value="-0.000085289" />
-  <Tmin units="K"  value="11.75" />
-  <Tmax units="K"  value="182.14" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="91638" />
-  <B value="67.51" />
-  <C value="9.6813" />
-  <D value="0.0069535" />
-  <E value="-0.0000034278" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="393.24" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="100690" />
-  <B value="-836.69" />
-  <C value="13.908" />
-  <D value="-0.00051206" />
-  <E value="1.3582E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24082" />
-  <B value="-317.36" />
-  <C value="-39.085" />
-  <D value="-11376" />
-  <E value="30465" />
-  <Tmin units="K"  value="295.58" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-19.068" />
-  <B value="1358.3" />
-  <C value="1.3526" />
-  <D value="-0.0000038202" />
-  <E value="2" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="393.24" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000012434" />
-  <B value="0.44274" />
-  <C value="472.75" />
-  <D value="75.213" />
-  <Tmin units="K"  value="393.24" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.04198" />
-  <B value="-3.8682" />
-  <C value="-1.5284" />
-  <D value="-0.00074068" />
-  <E value="-0.0000011056" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="393.24" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.015195" />
-  <B value="0.35206" />
-  <C value="-46.167" />
-  <D value="870770" />
-  <Tmin units="K"  value="393.24" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0081816" />
-  <B value="58.739" />
-  <C value="-3.5009" />
-  <D value="0.0012572" />
-  <E value="-0.0000062077" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="591.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-42404" />
-  <B value="786.83" />
-  <C value="-0.37657" />
-  <D value="0.000059811" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.487" />
-  <B value="2985.3" />
-  <C value="-60.096" />
-  <Tmin units="K"  value="356.47" />
-  <Tmax units="K"  value="529.01" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.696" />
-  <B value="-0.014492" />
-  <Tmin units="K"  value="197.58" />
-  <Tmax units="K"  value="393.24" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438832" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.912149E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="341.7583" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0570895" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.770374" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2414" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.147281" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3936" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.010622" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2414" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15640" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.147281" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="4" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="638-04-0" />
-<Smiles name="SMILES"  value="C1[C@@](C)([H])(C[C@]([H])(C)(CC1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="145" />
-<CompoundID name="Name"  value="Trans-1,3-dimethylcyclohexane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH2CH(CH3)(CH2)3-" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="598.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2938430" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.46" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="397.61" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="183.07" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="183.05" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0422148" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.143768" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2356" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.982E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16040" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08068" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.021E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.76565E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.63171E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="376225" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9865870" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.80546" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.86695E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.8511" />
-  <B value="-0.0059845" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="73.22" />
-  <Tmax units="K"  value="183.05" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.51304" />
-  <B value="0.23992" />
-  <C value="598.15" />
-  <D value="0.27441" />
-  <Tmin units="K"  value="183.05" />
-  <Tmax units="K"  value="576.16" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="80.341" />
-  <B value="-7070.2" />
-  <C value="-8.6503" />
-  <D value="0.0000047054" />
-  <E value="2" />
-  <Tmin units="K"  value="183.05" />
-  <Tmax units="K"  value="598" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.9382E+07" />
-  <B value="2.1184" />
-  <C value="-4.4766" />
-  <D value="4.6776" />
-  <E value="-1.8318" />
-  <Tmin units="K"  value="183.05" />
-  <Tmax units="K"  value="598" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-2368.7" />
-  <B value="925.58" />
-  <C value="0.83506" />
-  <D value="-0.035655" />
-  <E value="0.00013914" />
-  <Tmin units="K"  value="26.36" />
-  <Tmax units="K"  value="171.93" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="121960" />
-  <B value="76.643" />
-  <C value="8.8176" />
-  <D value="0.0095602" />
-  <E value="-0.0000057205" />
-  <Tmin units="K"  value="183.05" />
-  <Tmax units="K"  value="397.61" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="101700" />
-  <B value="-844.25" />
-  <C value="13.931" />
-  <D value="-0.00056374" />
-  <E value="1.5762E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24033" />
-  <B value="-319.57" />
-  <C value="-41.842" />
-  <D value="-2180.6" />
-  <E value="3918.4" />
-  <Tmin units="K"  value="299" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.854" />
-  <B value="1074.4" />
-  <C value="-0.03203" />
-  <D value="4.561E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="183.07" />
-  <Tmax units="K"  value="478.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000023976" />
-  <B value="0.3653" />
-  <C value="664.66" />
-  <D value="3836.7" />
-  <Tmin units="K"  value="397.61" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.046977" />
-  <B value="2.8897" />
-  <C value="-1.5646" />
-  <D value="-0.00046419" />
-  <E value="-0.0000013304" />
-  <Tmin units="K"  value="183.05" />
-  <Tmax units="K"  value="397.61" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.016485" />
-  <B value="0.34326" />
-  <C value="5.6687" />
-  <D value="894520" />
-  <Tmin units="K"  value="397.61" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0081604" />
-  <B value="50.552" />
-  <C value="-3.3636" />
-  <D value="0.0009936" />
-  <E value="-0.0000060087" />
-  <Tmin units="K"  value="183.05" />
-  <Tmax units="K"  value="598" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-40884" />
-  <B value="783.56" />
-  <C value="-0.38232" />
-  <D value="0.000063738" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.425" />
-  <B value="2962.4" />
-  <C value="-64.71" />
-  <Tmin units="K"  value="360.62" />
-  <Tmax units="K"  value="532.48" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.0122" />
-  <B value="-0.010989" />
-  <Tmin units="K"  value="183.07" />
-  <Tmax units="K"  value="478.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438832" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.87092E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="359.8914" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0565457" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.790566" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2356" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.143768" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3936" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.014903" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2356" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16040" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.143768" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="4" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2207-03-6" />
-<Smiles name="SMILES"  value="C1[C@](C)([H])(C[C@]([H])(C)(CC1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="146" />
-<CompoundID name="Name"  value="Cis-1,4-dimethylcyclohexane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH2CH2CH(CH3)(CH2)2-" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="598.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2938430" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.46" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="397.48" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="185.744" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="185.72" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0704204" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.144106" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2348" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.905E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15980" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08068" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.021E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.76648E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.79489E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="370451" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9307730" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.76732" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.86704E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.7979" />
-  <B value="-0.0058522" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="74.29" />
-  <Tmax units="K"  value="185.72" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53336" />
-  <B value="0.24533" />
-  <C value="598.15" />
-  <D value="0.2771" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="576.44" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="79.163" />
-  <B value="-7004.6" />
-  <C value="-8.4779" />
-  <D value="0.0000046053" />
-  <E value="2" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="598.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.1514E+07" />
-  <B value="2.3724" />
-  <C value="-5.2021" />
-  <D value="5.4751" />
-  <E value="-2.1521" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="576.44" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15617" />
-  <B value="1688.8" />
-  <C value="-13.402" />
-  <D value="0.071342" />
-  <E value="-0.00014259" />
-  <Tmin units="K"  value="19.17" />
-  <Tmax units="K"  value="173.61" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="110770" />
-  <B value="140.07" />
-  <C value="8.7617" />
-  <D value="0.0091373" />
-  <E value="-0.0000048302" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="397.47" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="101700" />
-  <B value="-844.25" />
-  <C value="13.931" />
-  <D value="-0.00056374" />
-  <E value="1.5762E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23973" />
-  <B value="-318.64" />
-  <C value="-42.246" />
-  <D value="-26.054" />
-  <E value="-2319.1" />
-  <Tmin units="K"  value="299.08" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-20.704" />
-  <B value="1391.4" />
-  <C value="1.6378" />
-  <D value="-0.0000047953" />
-  <E value="2" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="397.47" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000024207" />
-  <B value="0.36412" />
-  <C value="666.44" />
-  <D value="4231" />
-  <Tmin units="K"  value="397.47" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.063527" />
-  <B value="3.3026" />
-  <C value="-1.4941" />
-  <D value="-0.0004362" />
-  <E value="-0.0000011663" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="397.47" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.016747" />
-  <B value="0.34072" />
-  <C value="-1.7965" />
-  <D value="898230" />
-  <Tmin units="K"  value="397.47" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.013074" />
-  <B value="24.299" />
-  <C value="-3.0007" />
-  <D value="-0.00018331" />
-  <E value="-0.0000036266" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="576.44" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-40884" />
-  <B value="783.56" />
-  <C value="-0.38232" />
-  <D value="0.000063738" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.447" />
-  <B value="2982.9" />
-  <C value="-63.108" />
-  <Tmin units="K"  value="359.37" />
-  <Tmax units="K"  value="533.03" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4904" />
-  <B value="-0.015056" />
-  <Tmin units="K"  value="185.72" />
-  <Tmax units="K"  value="397.47" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438832" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.87092E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="359.8914" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.50855" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0569489" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.787298" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2348" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.144106" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3936" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.007723" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.55767" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2348" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15980" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.144106" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="4" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="624-29-3" />
-<Smiles name="SMILES"  value="C1[C@@](C)([H])(CC[C@]([H])(C)(C1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="147" />
-<CompoundID name="Name"  value="Trans-1,4-dimethylcyclohexane" />
-<StructureFormula name="Structure"  value="-CH(CH3)CH2CH2CH(CH3)(CH2)2-" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="590.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2940000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.45" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.271" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="392.51" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="236.21" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="236.21" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="44.9802" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.147921" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2429" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.907E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15490" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08068" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.021E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.84598E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.17147E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="364803" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.2332E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.732" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.86026E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.1298" />
-  <B value="-0.0043046" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="94.48" />
-  <Tmax units="K"  value="236.21" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.064652" />
-  <B value="0.087885" />
-  <C value="590.15" />
-  <D value="0.13093" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="587.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="85.56244" />
-  <B value="-7078.051" />
-  <C value="-9.547047" />
-  <D value="6.602527E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="587.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.5648E+07" />
-  <B value="0.9536" />
-  <C value="-1.3747" />
-  <D value="1.3927" />
-  <E value="-0.55606" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="587.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="27978" />
-  <B value="-360.95" />
-  <C value="18.399" />
-  <D value="-0.12928" />
-  <E value="0.00030483" />
-  <Tmin units="K"  value="42.39" />
-  <Tmax units="K"  value="220.61" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119770" />
-  <B value="186.95" />
-  <C value="7.9604" />
-  <D value="0.011554" />
-  <E value="-0.0000069633" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="392.51" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97979" />
-  <B value="-830.68" />
-  <C value="13.935" />
-  <D value="-0.00055238" />
-  <E value="1.5056E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24172" />
-  <B value="-316.33" />
-  <C value="-39.161" />
-  <D value="-2542.7" />
-  <E value="4823.9" />
-  <Tmin units="K"  value="293.85" />
-  <Tmax units="K"  value="1885.08" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.7946" />
-  <B value="1113.8" />
-  <C value="-0.41314" />
-  <D value="9.8767E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.6365E-07" />
-  <B value="0.52158" />
-  <C value="345.67" />
-  <D value="-1560.6" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0015458" />
-  <B value="-71.843" />
-  <C value="-1.1073" />
-  <D value="-0.0027831" />
-  <E value="1.5512E-07" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="392.51" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.012496" />
-  <B value="0.37939" />
-  <C value="-0.8405" />
-  <D value="811480" />
-  <Tmin units="K"  value="392.51" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.087781" />
-  <B value="-24.069" />
-  <C value="-1.6989" />
-  <D value="-0.0016706" />
-  <E value="8.2848E-07" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="587.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-49692" />
-  <B value="818.1" />
-  <C value="-0.41274" />
-  <D value="0.000071848" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.823" />
-  <B value="3222.8" />
-  <C value="-45.899" />
-  <Tmin units="K"  value="355" />
-  <Tmax units="K"  value="530" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.6989" />
-  <B value="-0.011979" />
-  <Tmin units="K"  value="236.21" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438832" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.850979E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="350.4008" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.271" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.9739" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0567868" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.766148" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2429" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.147921" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3936" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.021283" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.8685" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2429" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15490" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.147921" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="3"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="78"  value="4" />
-  <group id="79"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2207-04-7" />
-<Smiles name="SMILES"  value="C1[C@](C)([H])(CC[C@]([H])(C)(C1))" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="62" />
-<CompoundID name="Name"  value="Tert-butylcyclohexane" />
-<StructureFormula name="Structure"  value="C6H11C(CH3)3" />
-<Family name="Family"  value="7" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="652" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2660000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.51" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="444.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="231.98" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="231.98" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.2" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="140.266" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1734" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.299134" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.413E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16040" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1023" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.368E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.169E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5.695E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="445700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.12E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.091E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="7.857" />
-  <B value="-0.004234" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="92.79" />
-  <Tmax units="K"  value="231.98" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.52388" />
-  <B value="0.26705" />
-  <C value="652" />
-  <D value="0.32913" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="629.89" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="123.1664" />
-  <B value="-9675.557" />
-  <C value="-15.08186" />
-  <D value="0.0000105041" />
-  <E value="2" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="652" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.9454E+07" />
-  <B value="0.40915" />
-  <C value="1.6494" />
-  <D value="-3.4494" />
-  <E value="1.9573" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="629.89" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7696.3" />
-  <B value="1009" />
-  <C value="-1.0555" />
-  <D value="0.0022168" />
-  <E value="-0.0000028006" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="231.98" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="40996" />
-  <B value="-122.74" />
-  <C value="11.846" />
-  <D value="0.0032488" />
-  <E value="-0.0000015611" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="444.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="95339" />
-  <B value="-601.24" />
-  <C value="13.623" />
-  <D value="-0.000018521" />
-  <E value="-1.574E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.29828" />
-  <B value="-390.95" />
-  <C value="-86.65" />
-  <D value="-19290" />
-  <E value="30745" />
-  <Tmin units="K"  value="326" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.549" />
-  <B value="1445.9" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="444.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.6046E-08" />
-  <B value="0.87493" />
-  <C value="72.873" />
-  <D value="-5600.2" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.054405" />
-  <B value="-203.55" />
-  <C value="-0.50495" />
-  <D value="-0.0065818" />
-  <E value="0.0000029095" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="444.65" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.077607" />
-  <B value="0.14004" />
-  <C value="-91.94" />
-  <D value="1372500" />
-  <Tmin units="K"  value="444.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.089059" />
-  <B value="-24.697" />
-  <C value="-1.6764" />
-  <D value="-0.0015612" />
-  <E value="7.2073E-07" />
-  <Tmin units="K"  value="231.98" />
-  <Tmax units="K"  value="629.89" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-78018" />
-  <B value="1134.2" />
-  <C value="-0.67392" />
-  <D value="0.00015048" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.565" />
-  <B value="3373.6" />
-  <C value="-71.505" />
-  <Tmin units="K"  value="392.72" />
-  <Tmax units="K"  value="585.68" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.57156" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.868773E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="289.5641" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="205.2" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.069791" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.81854" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.299134" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1734" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.7417" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.472" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.000764" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.299134" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16040" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1734" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
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-<Asog name="ASOG" >
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-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
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-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="4"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="5" />
-  <group id="3"  value="1" />
-  <group id="4"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="78"  value="5" />
-  <group id="79"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="3178-22-1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="511" />
-<CompoundID name="Name"  value="O-ethyltoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="651.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3040000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.46" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="438.33" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="192.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="192.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00376669" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.192" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.136967" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2941" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.084E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18090" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.87E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08089" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.019E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1213360" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.31055E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="399350" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9962100" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.96524" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.94607E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.148" />
-  <B value="-0.0059039" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="76.94" />
-  <Tmax units="K"  value="192.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.37928" />
-  <B value="0.20513" />
-  <C value="651.15" />
-  <D value="0.23356" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="646.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="96.1971" />
-  <B value="-8650.261" />
-  <C value="-10.86209" />
-  <D value="5.918239E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="650" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.227273E+07" />
-  <B value="1.968046" />
-  <C value="-3.535916" />
-  <D value="3.107317" />
-  <E value="-1.061436" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="650" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="188730" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="651.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-102370" />
-  <B value="-26.419" />
-  <C value="12.162" />
-  <D value="0.0026059" />
-  <E value="-0.000002126" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="438.33" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85432" />
-  <B value="-569.61" />
-  <C value="13.054" />
-  <D value="0.000095945" />
-  <E value="-4.3717E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28121" />
-  <B value="-390.33" />
-  <C value="-73.261" />
-  <D value="-55800" />
-  <E value="123430" />
-  <Tmin units="K"  value="325" />
-  <Tmax units="K"  value="1953" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.303" />
-  <B value="1378.1" />
-  <C value="-0.24629" />
-  <D value="5.1436E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="613.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.4089E-07" />
-  <B value="0.56719" />
-  <C value="270.1" />
-  <D value="-4560.2" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.059289" />
-  <B value="4.2071" />
-  <C value="-1.4739" />
-  <D value="-0.00039236" />
-  <E value="-0.0000010623" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="438.33" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000092842" />
-  <B value="1.0422" />
-  <C value="544.16" />
-  <D value="63099" />
-  <Tmin units="K"  value="438.33" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0095325" />
-  <B value="42.422" />
-  <C value="-3.1128" />
-  <D value="0.0004594" />
-  <E value="-0.0000045591" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="650" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="1934.6" />
-  <B value="607.55" />
-  <C value="-0.29066" />
-  <D value="0.000046885" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.073" />
-  <B value="3576.5" />
-  <C value="-63.713" />
-  <Tmin units="K"  value="394.26" />
-  <Tmax units="K"  value="577.74" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.7738" />
-  <B value="-0.013269" />
-  <Tmin units="K"  value="192.35" />
-  <Tmax units="K"  value="613.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.440073" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.253199E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="333.0414" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0565227" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.885597" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2941" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.136967" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3322" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.076" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.047885" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2941" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18090" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.136967" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  <group id="2"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="611-14-3" />
-<Smiles name="SMILES"  value="c1(CC)c(C)cccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="512" />
-<CompoundID name="Name"  value="M-ethyltoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="637.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2840000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.49" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="434.48" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="177.61" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="177.61" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000664959" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.192" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.139685" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.3232" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.265E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17630" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.1E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08089" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.019E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1920000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.2643E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="404280" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7610000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.98305" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.94377E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.088" />
-  <B value="-0.0063302" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="71.04" />
-  <Tmax units="K"  value="177.61" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61007" />
-  <B value="0.26045" />
-  <C value="637.15" />
-  <D value="0.2946" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="612.96" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.906" />
-  <B value="-6895.5" />
-  <C value="-5.4176" />
-  <D value="0.00000211" />
-  <E value="2" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="637.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.562712E+07" />
-  <B value="1.251642" />
-  <C value="-2.311984" />
-  <D value="2.123485" />
-  <E value="-0.635116" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="612.96" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="188730" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="637.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="136340" />
-  <B value="-1484.6" />
-  <C value="20.724" />
-  <D value="-0.020829" />
-  <E value="0.000018949" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="434.48" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="77831" />
-  <B value="-586.35" />
-  <C value="13.16" />
-  <D value="0.0000010287" />
-  <E value="-1.3417E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30122" />
-  <B value="-402.05" />
-  <C value="-67.704" />
-  <D value="-53853" />
-  <E value="119410" />
-  <Tmin units="K"  value="318.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.732" />
-  <B value="1285.7" />
-  <C value="-0.12931" />
-  <D value="2.7444E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="434.48" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.7246E-07" />
-  <B value="0.55389" />
-  <C value="274.11" />
-  <D value="-5848.6" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.048117" />
-  <B value="4.2831" />
-  <C value="-1.5331" />
-  <D value="-0.00039971" />
-  <E value="-0.0000012216" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="434.48" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000091259" />
-  <B value="1.0513" />
-  <C value="653.39" />
-  <D value="40428" />
-  <Tmin units="K"  value="434.48" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.008518" />
-  <B value="41.345" />
-  <C value="-3.1089" />
-  <D value="0.00042327" />
-  <E value="-0.0000050765" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="612.96" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-22026" />
-  <B value="689.66" />
-  <C value="-0.38171" />
-  <D value="0.000078428" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.638772" />
-  <B value="-1100" />
-  <C value="-6.6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.48" />
-  <B value="3836.8" />
-  <C value="-48.994" />
-  <Tmin units="K"  value="383.15" />
-  <Tmax units="K"  value="564.59" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.9923" />
-  <B value="-0.016106" />
-  <Tmin units="K"  value="177.61" />
-  <Tmax units="K"  value="434.48" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.440073" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.618039E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="299.61" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0566058" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.869111" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3232" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.139685" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3322" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.076" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.036093" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3232" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17630" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.139685" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  <group id="2"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="620-14-4" />
-<Smiles name="SMILES"  value="c1(CC)cc(C)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="513" />
-<CompoundID name="Name"  value="P-ethyltoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH2CH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="640.2" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3230000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.44" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="435.13" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="210.83" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="210.83" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0782406" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.194" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1396" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.364" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.189E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17710" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08089" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.019E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3260000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.268E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="398900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.336E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.26912" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.94268E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.8403" />
-  <B value="-0.0052743" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="84.33" />
-  <Tmax units="K"  value="210.83" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.60155" />
-  <B value="0.25704" />
-  <C value="640.2" />
-  <D value="0.31664" />
-  <Tmin units="K"  value="210.83" />
-  <Tmax units="K"  value="617.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="21.19382" />
-  <B value="-5103.792" />
-  <C value="0.409026" />
-  <D value="-2.319216E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="210.83" />
-  <Tmax units="K"  value="640.23" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.1677E+07" />
-  <B value="1.0708" />
-  <C value="-1.1055" />
-  <D value="0.62044" />
-  <E value="-0.16372" />
-  <Tmin units="K"  value="210.83" />
-  <Tmax units="K"  value="617.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="188730" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="640.2" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="30748" />
-  <B value="-85.511" />
-  <C value="11.539" />
-  <D value="0.0037389" />
-  <E value="-0.0000030029" />
-  <Tmin units="K"  value="210.83" />
-  <Tmax units="K"  value="435.16" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="75636" />
-  <B value="-568.13" />
-  <C value="13.103" />
-  <D value="0.000082441" />
-  <E value="-4.4902E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25573" />
-  <B value="-344.8" />
-  <C value="-83.9" />
-  <D value="-25209" />
-  <E value="34327" />
-  <Tmin units="K"  value="320" />
-  <Tmax units="K"  value="1920" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-23.973" />
-  <B value="1681.2" />
-  <C value="1.9315" />
-  <D value="6.328E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="435.16" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.7075E-07" />
-  <B value="0.5347" />
-  <C value="318.96" />
-  <D value="-7211.9" />
-  <Tmin units="K"  value="210.83" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.065655" />
-  <B value="1.2156" />
-  <C value="-1.4285" />
-  <D value="-0.00047761" />
-  <E value="-9.6417E-07" />
-  <Tmin units="K"  value="210.83" />
-  <Tmax units="K"  value="435.16" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000095782" />
-  <B value="1.0471" />
-  <C value="660.61" />
-  <D value="40132" />
-  <Tmin units="K"  value="435.16" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0089903" />
-  <B value="31.501" />
-  <C value="-3.0152" />
-  <D value="0.00008036" />
-  <E value="-0.0000045289" />
-  <Tmin units="K"  value="210.83" />
-  <Tmax units="K"  value="617.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="42379" />
-  <B value="144.55" />
-  <C value="1.1308" />
-  <D value="-0.0016046" />
-  <E value="6.4994E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.064" />
-  <B value="3570" />
-  <C value="-60.902" />
-  <Tmin units="K"  value="385.57" />
-  <Tmax units="K"  value="573.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.0788" />
-  <B value="-0.01068" />
-  <Tmin units="K"  value="220" />
-  <Tmax units="K"  value="435.16" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.440073" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.179642E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="322.9297" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.68733" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0574321" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.866093" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.364" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1396" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3322" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.076" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.036093" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.75305" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.364" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17710" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1396" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  <group id="2"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="622-96-8" />
-<Smiles name="SMILES"  value="c1(CC)ccc(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="514" />
-<CompoundID name="Name"  value="1,2,3-trimethylbenzene" />
-<StructureFormula name="Structure"  value="(C6H3)(CH3)3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="664.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3454000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.435" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="449.23" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="247.79" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="247.79" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.70834" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.194" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13322" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.367" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.127E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18480" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.87E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08181" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.026E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9568810" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.244E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8170000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1114" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.93394E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.7697" />
-  <B value="-0.0043665" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="99.12" />
-  <Tmax units="K"  value="247.79" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.47081" />
-  <B value="0.22935" />
-  <C value="664.5" />
-  <D value="0.22914" />
-  <Tmin units="K"  value="243.15" />
-  <Tmax units="K"  value="664.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="103.4032" />
-  <B value="-9139.734" />
-  <C value="-11.94112" />
-  <D value="6.875135E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="664.5" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.897E+07" />
-  <B value="0.31296" />
-  <C value="0.11034" />
-  <D value="-0.18707" />
-  <E value="0.12203" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="642.57" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="165120" />
-  <B value="-5147.2" />
-  <C value="80.052" />
-  <D value="-0.45918" />
-  <E value="0.00093095" />
-  <Tmin units="K"  value="59.99" />
-  <Tmax units="K"  value="230.27" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="158190" />
-  <B value="-110.87" />
-  <C value="9.7005" />
-  <D value="0.0066246" />
-  <E value="-0.000003875" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97344" />
-  <B value="-642.53" />
-  <C value="13.123" />
-  <D value="0.000061931" />
-  <E value="-4.6438E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26373" />
-  <B value="-348.47" />
-  <C value="-92.015" />
-  <D value="-13079" />
-  <E value="-14420" />
-  <Tmin units="K"  value="332.23" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-13.622" />
-  <B value="1547.6" />
-  <C value="0.25604" />
-  <D value="-4.4218E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="449.27" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.8569E-07" />
-  <B value="0.49843" />
-  <C value="362.98" />
-  <D value="-102.15" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.066267" />
-  <B value="303.46" />
-  <C value="-5.2163" />
-  <D value="0.0092731" />
-  <E value="-0.000014825" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="603.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000093303" />
-  <B value="1.0419" />
-  <C value="539.24" />
-  <D value="56545" />
-  <Tmin units="K"  value="449.27" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0045939" />
-  <B value="547.15" />
-  <C value="-7.5443" />
-  <D value="0.012641" />
-  <E value="-0.000016044" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="642.57" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="33607" />
-  <B value="259.01" />
-  <C value="0.84683" />
-  <D value="-0.0013521" />
-  <E value="5.7553E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.569" />
-  <B value="4045.6" />
-  <C value="-46.375" />
-  <Tmin units="K"  value="399.82" />
-  <Tmax units="K"  value="595" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.023" />
-  <B value="-0.01311" />
-  <Tmin units="K"  value="247.79" />
-  <Tmax units="K"  value="449.27" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.445517" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.895957E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="373.9802" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.66379" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0557463" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.899219" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.367" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.13322" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3928" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.104" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.014458" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.1405" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.367" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18480" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.13322" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="11"  value="3" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="3" />
-  <group id="8"  value="3" />
-  <group id="1"  value="3" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="3" />
-  <group id="12"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="11"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="526-73-8" />
-<Smiles name="SMILES"  value="c1(C)c(C)c(C)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="515" />
-<CompoundID name="Name"  value="1,2,4-trimethylbenzene" />
-<StructureFormula name="Structure"  value="(C6H3)(CH3)3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="649.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3232000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.435" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="442.49" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="229.38" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="229.33" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.69347" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.194" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.136" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.377" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.199E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18090" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08181" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.026E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.392E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.17E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="395870" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.319E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1182" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.93067E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.7544" />
-  <B value="-0.0047176" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="91.73" />
-  <Tmax units="K"  value="229.38" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61782" />
-  <B value="0.26243" />
-  <C value="649.1" />
-  <D value="0.28053" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="627.01" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="60.23044" />
-  <B value="-7113.208" />
-  <C value="-5.408973" />
-  <D value="1.637451E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="649.17" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.6212E+07" />
-  <B value="0.612793" />
-  <C value="0.157992" />
-  <D value="-1.024462" />
-  <E value="0.66352" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="627.01" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11144" />
-  <B value="1377.6" />
-  <C value="-5.4631" />
-  <D value="0.013913" />
-  <E value="-0.000011765" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="229.33" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="159260" />
-  <B value="100.48" />
-  <C value="7.176" />
-  <D value="0.015511" />
-  <E value="-0.000013842" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="377.59" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86220" />
-  <B value="-588.22" />
-  <C value="13.049" />
-  <D value="0.00013217" />
-  <E value="-6.3042E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21967" />
-  <B value="-308.5" />
-  <C value="-93.453" />
-  <D value="-7582" />
-  <E value="-20640" />
-  <Tmin units="K"  value="324.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-22.655" />
-  <B value="1676.9" />
-  <C value="1.8204" />
-  <D value="-0.0000040799" />
-  <E value="2" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="442.53" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.0311E-07" />
-  <B value="0.47728" />
-  <C value="388.95" />
-  <D value="-1321.5" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.097311" />
-  <B value="-7.9329" />
-  <C value="-1.1933" />
-  <D value="-0.00075728" />
-  <E value="-4.2291E-07" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="442.53" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000071734" />
-  <B value="1.0715" />
-  <C value="503.12" />
-  <D value="48355" />
-  <Tmin units="K"  value="442.53" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011514" />
-  <B value="38.782" />
-  <C value="-3.0516" />
-  <D value="0.00024183" />
-  <E value="-0.0000039588" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="627.01" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="44225" />
-  <B value="166.9" />
-  <C value="1.0006" />
-  <D value="-0.0014029" />
-  <E value="5.5599E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.638772" />
-  <B value="-1100" />
-  <C value="-6.6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.398" />
-  <B value="3864.8" />
-  <C value="-51.014" />
-  <Tmin units="K"  value="392.48" />
-  <Tmax units="K"  value="583.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0344" />
-  <B value="-0.013005" />
-  <Tmin units="K"  value="229.33" />
-  <Tmax units="K"  value="442.53" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.445517" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.25304E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="313.9704" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.256" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.5894" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0565352" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.880542" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.377" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.136" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3928" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.104" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.010675" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.98594" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.377" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18090" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.136" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="11"  value="3" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="3" />
-  <group id="8"  value="3" />
-  <group id="1"  value="3" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="3" />
-  <group id="12"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="11"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="95-63-6" />
-<Smiles name="SMILES"  value="c1(C)c(C)cc(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="516" />
-<CompoundID name="Name"  value="Mesitylene" />
-<StructureFormula name="Structure"  value="(C6H3)(CH3)3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="637.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3127000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.43" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="437.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="228.46" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="228.42" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.742135" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="120.194" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14299" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.399" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.375E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17940" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08183" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.026E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.605E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.181E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="385410" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9514000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.05218" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.92904E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.6603" />
-  <B value="-0.004682" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="91.37" />
-  <Tmax units="K"  value="228.46" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.59019" />
-  <B value="0.25742" />
-  <C value="637.3" />
-  <D value="0.27724" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="637.3" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="118.5616" />
-  <B value="-9560.276" />
-  <C value="-14.30644" />
-  <D value="9.375247E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="637.3" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.9292E+07" />
-  <B value="1.0706" />
-  <C value="-1.5094" />
-  <D value="1.269" />
-  <E value="-0.42864" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="637.3" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-5866.5" />
-  <B value="1641.6" />
-  <C value="-10.768" />
-  <D value="0.042606" />
-  <E value="-0.000061561" />
-  <Tmin units="K"  value="40" />
-  <Tmax units="K"  value="228.42" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="152130" />
-  <B value="279.49" />
-  <C value="4.8304" />
-  <D value="0.024632" />
-  <E value="-0.000024309" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="350" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="76799" />
-  <B value="-561.49" />
-  <C value="13.016" />
-  <D value="0.00018488" />
-  <E value="-8.0041E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24882" />
-  <B value="-343.87" />
-  <C value="-78.688" />
-  <D value="-32243" />
-  <E value="54062" />
-  <Tmin units="K"  value="318.64" />
-  <Tmax units="K"  value="1911.84" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.283" />
-  <B value="1439.3" />
-  <C value="-0.15787" />
-  <D value="0.0000019934" />
-  <E value="2" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="437.89" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.4877E-07" />
-  <B value="0.61399" />
-  <C value="342.31" />
-  <D value="-16742" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.012521" />
-  <B value="77.398" />
-  <C value="-2.4912" />
-  <D value="0.0027181" />
-  <E value="-0.0000053908" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="437.89" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.3225" />
-  <B value="-0.079944" />
-  <C value="-464.54" />
-  <D value="1938200" />
-  <Tmin units="K"  value="437.89" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.055828" />
-  <B value="-26.825" />
-  <C value="-1.91" />
-  <D value="-0.0017202" />
-  <E value="3.8899E-07" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="637.3" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="44108" />
-  <B value="166.61" />
-  <C value="0.96498" />
-  <D value="-0.0013567" />
-  <E value="5.4069E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.468" />
-  <B value="3822" />
-  <C value="-53.453" />
-  <Tmin units="K"  value="383.15" />
-  <Tmax units="K"  value="573.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0703" />
-  <B value="-0.013286" />
-  <Tmin units="K"  value="228.42" />
-  <Tmax units="K"  value="437.89" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.445635" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.362983E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="291.2722" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.252" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.52" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.057193" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.869455" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.399" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14299" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3928" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.104" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.014912" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.399" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17940" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14299" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="11"  value="3" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="3" />
-  <group id="8"  value="3" />
-  <group id="1"  value="3" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="3" />
-  <group id="12"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="11"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-67-8" />
-<Smiles name="SMILES"  value="c1(C)cc(C)cc(C)c1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="519" />
-<CompoundID name="Name"  value="Isobutylbenzene" />
-<StructureFormula name="Structure"  value="(C6H5)CH2CH(CH3)2" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="650" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3050000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.48" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.271" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="445.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="221.7" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="221.7" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.289087" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.221" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15808" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.383" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.555E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16860" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09019" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.146E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.054E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.388E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="439700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.25E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0374" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.56974E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.6003" />
-  <B value="-0.0043101" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="88.68" />
-  <Tmax units="K"  value="221.7" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54967" />
-  <B value="0.26271" />
-  <C value="650" />
-  <D value="0.30807" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="627.46" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="97.24209" />
-  <B value="-8752.864" />
-  <C value="-11.04244" />
-  <D value="6.424651E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="650" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.0838E+07" />
-  <B value="0.30052" />
-  <C value="0.25612" />
-  <D value="-0.19969" />
-  <E value="-0.0011249" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="627.46" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6990.9" />
-  <B value="980.23" />
-  <C value="-2.1589" />
-  <D value="0.0063245" />
-  <E value="-0.0000082806" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="221.7" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116150" />
-  <B value="-36.608" />
-  <C value="10.189" />
-  <D value="0.0074074" />
-  <E value="-0.0000060747" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="445.94" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83364" />
-  <B value="-556.41" />
-  <C value="13.277" />
-  <D value="0.000016037" />
-  <E value="-2.0047E-08" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30201" />
-  <B value="-383.93" />
-  <C value="-94.545" />
-  <D value="-4562.5" />
-  <E value="-39381" />
-  <Tmin units="K"  value="325" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.546" />
-  <B value="1392.5" />
-  <C value="0.17362" />
-  <D value="-2.3672E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="445.94" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.8764E-07" />
-  <B value="0.58977" />
-  <C value="249.51" />
-  <D value="1034.4" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.033263" />
-  <B value="-23.962" />
-  <C value="-1.3695" />
-  <D value="-0.001338" />
-  <E value="-2.5251E-07" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="445.94" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000022162" />
-  <B value="1.2141" />
-  <C value="174.06" />
-  <D value="50162" />
-  <Tmin units="K"  value="445.94" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0096431" />
-  <B value="44.533" />
-  <C value="-3.1993" />
-  <D value="0.00043442" />
-  <E value="-0.0000043503" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="627.46" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-39186" />
-  <B value="861.97" />
-  <C value="-0.52789" />
-  <D value="0.00012235" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.764801" />
-  <B value="-1150" />
-  <C value="-6.9" />
-  <Tmin units="K"  value="270.8167" />
-  <Tmax units="K"  value="440.8167" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.694" />
-  <B value="4111.8" />
-  <C value="-41.494" />
-  <Tmin units="K"  value="390.04" />
-  <Tmax units="K"  value="582.37" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.7768" />
-  <B value="-0.013263" />
-  <Tmin units="K"  value="221.7" />
-  <Tmax units="K"  value="445.94" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.495922" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.99996E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="385.9366" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.271" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0641263" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.857681" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.383" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15808" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.9452" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.584" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.013419" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.383" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16860" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15808" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="10"  value="5" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="9"  value="5" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="2"  value="1" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="10"  value="5" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="9"  value="5" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="538-93-2" />
-<Smiles name="SMILES"  value="c1(CC(C)C)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="520" />
-<CompoundID name="Name"  value="Sec-butylbenzene" />
-<StructureFormula name="Structure"  value="(C6H5)CH(CH3)CH2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="664.54" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2930000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.478" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="446.48" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="197.717" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="197.717" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00180534" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.156497" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.279149" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.564E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17050" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09019" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.146E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.73E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.4523E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="439600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9830000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.87947" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.563E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.7924" />
-  <B value="-0.0049215" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="79.09" />
-  <Tmax units="K"  value="197.72" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.51273" />
-  <B value="0.25494" />
-  <C value="664.54" />
-  <D value="0.28096" />
-  <Tmin units="K"  value="197.72" />
-  <Tmax units="K"  value="664.54" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="222.2329" />
-  <B value="-13854.88" />
-  <C value="-30.30702" />
-  <D value="0.0000262583" />
-  <E value="2" />
-  <Tmin units="K"  value="197.72" />
-  <Tmax units="K"  value="664.54" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.1793E+07" />
-  <B value="-4.1563" />
-  <C value="12.591" />
-  <D value="-13.449" />
-  <E value="5.2588" />
-  <Tmin units="K"  value="197.72" />
-  <Tmax units="K"  value="664.54" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="664.54" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="163140" />
-  <B value="-1794.7" />
-  <C value="23.385" />
-  <D value="-0.029199" />
-  <E value="0.000028" />
-  <Tmin units="K"  value="197.72" />
-  <Tmax units="K"  value="498.4" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="118430" />
-  <B value="-784.79" />
-  <C value="13.745" />
-  <D value="-0.00050199" />
-  <E value="1.4393E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.32727" />
-  <B value="-453.4" />
-  <C value="-94.023" />
-  <D value="22089" />
-  <E value="-123210" />
-  <Tmin units="K"  value="289.72" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="10" />
-  <A value="-9.695648" />
-  <B value="-444.5934" />
-  <C value="-129.1082" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="161.3" />
-  <Tmax units="K"  value="446.48" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000001223" />
-  <B value="0.44278" />
-  <C value="495.81" />
-  <D value="151.45" />
-  <Tmin units="K"  value="197.72" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.042864" />
-  <B value="5.3464" />
-  <C value="-1.6033" />
-  <D value="-0.00035754" />
-  <E value="-0.0000011781" />
-  <Tmin units="K"  value="197.72" />
-  <Tmax units="K"  value="446.48" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000022" />
-  <B value="1.2101" />
-  <C value="186.5" />
-  <D value="49434" />
-  <Tmin units="K"  value="446.48" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0072678" />
-  <B value="56.315" />
-  <C value="-3.3559" />
-  <D value="0.00098625" />
-  <E value="-0.0000052989" />
-  <Tmin units="K"  value="197.72" />
-  <Tmax units="K"  value="664.54" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-13101" />
-  <B value="760.71" />
-  <C value="-0.41343" />
-  <D value="0.000082333" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.126" />
-  <B value="3014.6" />
-  <C value="-95.941" />
-  <Tmin units="K"  value="399.82" />
-  <Tmax units="K"  value="590.83" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="3.746" />
-  <B value="-0.031996" />
-  <Tmin units="K"  value="161.3" />
-  <Tmax units="K"  value="446.48" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.495922" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.180576E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="364.0151" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.265" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.37782" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0633935" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.86584" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.279149" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.156497" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.9452" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.584" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.01848" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.36042" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.279149" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17050" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.156497" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="5" />
-  <group id="14"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="9"  value="5" />
-  <group id="13"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="2"  value="1" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="5" />
-  <group id="14"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="9"  value="5" />
-  <group id="13"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="135-98-8" />
-<Smiles name="SMILES"  value="c1(C(C)CC)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="521" />
-<CompoundID name="Name"  value="Tert-butylbenzene" />
-<StructureFormula name="Structure"  value="(C6H5)C(CH3)2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="660" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2970000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.46" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="442.3" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="215.27" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="215.27" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0910321" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.155605" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.267406" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.318E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17130" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.33E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09018" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.166E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.26E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.4995E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="401400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8393000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.77053" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5547E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8005" />
-  <B value="-0.0046306" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="86.11" />
-  <Tmax units="K"  value="215.27" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50957" />
-  <B value="0.25071" />
-  <C value="660" />
-  <D value="0.30584" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="660" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="87.574" />
-  <B value="-8352.2" />
-  <C value="-9.5118" />
-  <D value="0.0000039953" />
-  <E value="2" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="660" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.3167E+07" />
-  <B value="0.45262" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="660" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="44844" />
-  <B value="-193.06" />
-  <C value="10.001" />
-  <D value="-0.051599" />
-  <E value="0.00010323" />
-  <Tmin units="K"  value="92.2" />
-  <Tmax units="K"  value="215.27" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="164930" />
-  <B value="701.24" />
-  <C value="1.184" />
-  <D value="0.037122" />
-  <E value="-0.000038006" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="325" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="113750" />
-  <B value="-776.86" />
-  <C value="13.825" />
-  <D value="-0.0005797" />
-  <E value="1.6467E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.31169" />
-  <B value="-443.18" />
-  <C value="-79.486" />
-  <D value="-14909" />
-  <E value="-8902.2" />
-  <Tmin units="K"  value="330" />
-  <Tmax units="K"  value="1815" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.7" />
-  <B value="1364.1" />
-  <C value="0.038741" />
-  <D value="-3.8013E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="442.3" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.2957E-07" />
-  <B value="0.50871" />
-  <C value="384.51" />
-  <D value="-23.513" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.052023" />
-  <B value="-143.3" />
-  <C value="-0.69673" />
-  <D value="-0.0057333" />
-  <E value="0.0000022627" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="442.3" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000018955" />
-  <B value="1.2291" />
-  <C value="130.74" />
-  <D value="53349" />
-  <Tmin units="K"  value="442.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0065659" />
-  <B value="74.035" />
-  <C value="-3.5401" />
-  <D value="0.001524" />
-  <E value="-0.0000060556" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="660" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-27299" />
-  <B value="830.02" />
-  <C value="-0.48525" />
-  <D value="0.00010401" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.362" />
-  <B value="3143.6" />
-  <C value="-86.505" />
-  <Tmin units="K"  value="398.09" />
-  <Tmax units="K"  value="589.78" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.5924" />
-  <B value="-0.013801" />
-  <Tmin units="K"  value="215.27" />
-  <Tmax units="K"  value="442.3" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.495861" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.057317E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="366.4637" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.266" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.84715" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0635105" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.871335" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.267406" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.155605" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.9452" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.584" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.018084" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-0.90376" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.267406" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17130" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.155605" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="5" />
-  <group id="14"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="9"  value="5" />
-  <group id="13"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="7"  value="5" />
-  <group id="8"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="10"  value="5" />
-  <group id="14"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="9"  value="5" />
-  <group id="13"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="98-06-6" />
-<Smiles name="SMILES"  value="c1(C(C)(C)C)ccccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="522" />
-<CompoundID name="Name"  value="O-cymene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="670.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2895870" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.478" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="451.33" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="201.64" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="201.64" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0177118" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.153824" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.2769" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.439E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17160" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09111" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.153E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.56061E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.37359E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="425500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.0E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.9" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.56053E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9396" />
-  <B value="-0.0049298" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="80.66" />
-  <Tmax units="K"  value="201.64" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.017298" />
-  <B value="0.046645" />
-  <C value="670.15" />
-  <D value="0.11526" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="657" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="47.323" />
-  <B value="-6536.6" />
-  <C value="-3.5074" />
-  <D value="6.0254E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="657" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.44827E+07" />
-  <B value="3.205721" />
-  <C value="-8.334975" />
-  <D value="9.055186" />
-  <E value="-3.399515" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="657" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="670.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="130330" />
-  <B value="-123.14" />
-  <C value="10.583" />
-  <D value="0.0062464" />
-  <E value="-0.0000049954" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="451.33" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="105060" />
-  <B value="-664.9" />
-  <C value="13.437" />
-  <D value="-0.00013826" />
-  <E value="2.1794E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.021656" />
-  <B value="-196.81" />
-  <C value="-126.59" />
-  <D value="-24488" />
-  <E value="23531" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.1679" />
-  <B value="885.64" />
-  <C value="-0.29176" />
-  <D value="-7.7161E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="529.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000020745" />
-  <B value="0.37852" />
-  <C value="642.92" />
-  <D value="259.27" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.06145" />
-  <B value="-173.56" />
-  <C value="-0.23519" />
-  <D value="-0.0077758" />
-  <E value="0.0000038715" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="451.33" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000020459" />
-  <B value="1.2217" />
-  <C value="183.94" />
-  <D value="51167" />
-  <Tmin units="K"  value="451.33" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012864" />
-  <B value="40.847" />
-  <C value="-2.9372" />
-  <D value="-0.0001363" />
-  <E value="-0.0000031711" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="657" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-31175" />
-  <B value="828.19" />
-  <C value="-0.48457" />
-  <D value="0.00010664" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.481" />
-  <B value="4002" />
-  <C value="-49.35" />
-  <Tmin units="K"  value="402.63" />
-  <Tmax units="K"  value="585.1" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.1517" />
-  <B value="-0.0089047" />
-  <Tmin units="K"  value="201.64" />
-  <Tmax units="K"  value="529.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.501549" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.346598E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="342.7593" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0648833" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.880891" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.2769" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.153824" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0058" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.612" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.2769" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17160" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.153824" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="14"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="527-84-4" />
-<Smiles name="SMILES"  value="c1(C(C)C)c(C)cccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="523" />
-<CompoundID name="Name"  value="M-cymene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="666.25" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2810000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.478" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="448.23" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="209.44" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="209.44" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0405569" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.156604" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.342" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.636E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17110" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09111" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.153E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.79909E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.301E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="432200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.37E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.88" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.55802E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.7359" />
-  <B value="-0.0046553" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="83.78" />
-  <Tmax units="K"  value="209.44" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.17699" />
-  <B value="0.14976" />
-  <C value="666.25" />
-  <D value="0.19922" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="625.87" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="72.132" />
-  <B value="-7676.5" />
-  <C value="-7.2263" />
-  <D value="0.0000031742" />
-  <E value="2" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="649" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.132017E+08" />
-  <B value="4.402749" />
-  <C value="-10.71693" />
-  <D value="11.0294" />
-  <E value="-4.113621" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="649" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="666.25" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="129560" />
-  <B value="-114.64" />
-  <C value="10.436" />
-  <D value="0.006807" />
-  <E value="-0.0000055776" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="448.23" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="118290" />
-  <B value="-808.58" />
-  <C value="13.818" />
-  <D value="-0.00057669" />
-  <E value="1.7291E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12974" />
-  <B value="-253.73" />
-  <C value="-121.92" />
-  <D value="-30910" />
-  <E value="33295" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.2582" />
-  <B value="1048.3" />
-  <C value="-0.41448" />
-  <D value="-1.0836E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="448.23" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000018208" />
-  <B value="0.39157" />
-  <C value="589.66" />
-  <D value="3771.8" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.042558" />
-  <B value="-18.046" />
-  <C value="-1.3081" />
-  <D value="-0.0015377" />
-  <E value="2.6414E-07" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="448.23" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000098162" />
-  <B value="1.3084" />
-  <C value="45.918" />
-  <D value="51418" />
-  <Tmin units="K"  value="448.23" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012208" />
-  <B value="47.367" />
-  <C value="-3.0587" />
-  <D value="0.000021368" />
-  <E value="-0.0000033062" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="649" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-18198" />
-  <B value="773.31" />
-  <C value="-0.42297" />
-  <D value="0.000085563" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.325" />
-  <B value="3857.2" />
-  <C value="-54.615" />
-  <Tmin units="K"  value="399.78" />
-  <Tmax units="K"  value="579.6" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4735" />
-  <B value="-0.011921" />
-  <Tmin units="K"  value="209.44" />
-  <Tmax units="K"  value="448.23" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.501549" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.449627E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="326.8208" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.257" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0649982" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.865347" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.342" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.156604" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0058" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.612" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.004533" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.342" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17110" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.156604" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="14"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="535-77-3" />
-<Smiles name="SMILES"  value="c1(C(C)C)cc(C)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="524" />
-<CompoundID name="Name"  value="P-cymene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH(CH3)2" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="652" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.497" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="450.26" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="205.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="205.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.010391" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.221" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15749" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.376" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.557E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17290" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09111" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.153E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.799E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.3352E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="426400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9661000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.03611" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.558E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.7239" />
-  <B value="-0.004728" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="82.1" />
-  <Tmax units="K"  value="205.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.44838" />
-  <B value="0.23842" />
-  <C value="653.16" />
-  <D value="0.26866" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="653.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="130.8986" />
-  <B value="-10357.88" />
-  <C value="-16.09943" />
-  <D value="9.850105E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="653.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.966039E+07" />
-  <B value="1.950064" />
-  <C value="-3.032433" />
-  <D value="2.16162" />
-  <E value="-0.588861" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="653.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-68366" />
-  <B value="2952.6" />
-  <C value="-17.388" />
-  <D value="0.036561" />
-  <E value="0.000036293" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="205.25" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="99148" />
-  <B value="48.442" />
-  <C value="10.281" />
-  <D value="0.006034" />
-  <E value="-0.0000045515" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="450.28" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119360" />
-  <B value="-822.32" />
-  <C value="13.841" />
-  <D value="-0.00060036" />
-  <E value="1.8085E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.075714" />
-  <B value="-202.54" />
-  <C value="-126.35" />
-  <D value="-27689" />
-  <E value="28143" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-29.824" />
-  <B value="1974.9" />
-  <C value="2.8359" />
-  <D value="-0.0000010565" />
-  <E value="2" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="522.53" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000032148" />
-  <B value="0.32014" />
-  <C value="730.34" />
-  <D value="10237" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.018679" />
-  <B value="-10.656" />
-  <C value="-1.722" />
-  <D value="-0.0015047" />
-  <E value="-7.6885E-07" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="593.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00010761" />
-  <B value="1.0275" />
-  <C value="670.75" />
-  <D value="67288" />
-  <Tmin units="K"  value="450.28" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.040455" />
-  <B value="32.653" />
-  <C value="-2.5051" />
-  <D value="-0.00081582" />
-  <E value="-0.0000005747" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="628.49" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-15629" />
-  <B value="759.85" />
-  <C value="-0.40811" />
-  <D value="0.000080721" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-1.756835" />
-  <B value="-1150" />
-  <C value="-6.9" />
-  <Tmin units="K"  value="271.3722" />
-  <Tmax units="K"  value="441.3722" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.164" />
-  <B value="3777.4" />
-  <C value="-58.088" />
-  <Tmin units="K"  value="393.15" />
-  <Tmax units="K"  value="581.46" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.2286" />
-  <B value="-0.0093756" />
-  <Tmin units="K"  value="205.25" />
-  <Tmax units="K"  value="522.53" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.501549" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.876896E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="281.3111" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0641258" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.860761" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.376" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15749" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0058" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.612" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.000849" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.376" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17290" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15749" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  <group id="3"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="14"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="13"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="99-87-6" />
-<Smiles name="SMILES"  value="c1(C(C)C)ccc(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="525" />
-<CompoundID name="Name"  value="O-diethylbenzene" />
-<StructureFormula name="Structure"  value="CH3CH2(C6H4)CH2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="668" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2880000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.502" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="456.573" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="241.91" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="241.929" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.04119" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.2182" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15328" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.3879" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.398E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17760" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.96803E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0911199" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.154E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.89535E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.41084E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="434800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.67778E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5596E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.6823" />
-  <B value="-0.0039819" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="96.77" />
-  <Tmax units="K"  value="241.93" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.52086" />
-  <B value="0.25389" />
-  <C value="668" />
-  <D value="0.28666" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="645.58" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="136.1844" />
-  <B value="-10760.78" />
-  <C value="-16.88233" />
-  <D value="0.0000109939" />
-  <E value="2" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="668" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.4827E+07" />
-  <B value="-1.9073" />
-  <C value="6.1295" />
-  <D value="-6.3772" />
-  <E value="2.4857" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="645.58" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7349.5" />
-  <B value="982.4" />
-  <C value="-2.0447" />
-  <D value="0.0056221" />
-  <E value="-0.0000068735" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="241.9" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="13731" />
-  <B value="7.9227" />
-  <C value="11.237" />
-  <D value="0.004718" />
-  <E value="-0.0000037106" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="456.61" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122330" />
-  <B value="-723.39" />
-  <C value="13.531" />
-  <D value="-0.00028953" />
-  <E value="7.2562E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.32238" />
-  <B value="-437.38" />
-  <C value="-102.19" />
-  <D value="33649" />
-  <E value="-188440" />
-  <Tmin units="K"  value="334" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-13.971" />
-  <B value="1608.7" />
-  <C value="0.32395" />
-  <D value="-5.0533E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="456.61" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.8451E-08" />
-  <B value="0.84013" />
-  <C value="-72.915" />
-  <D value="24855" />
-  <Tmin units="K"  value="456.61" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.047218" />
-  <B value="-11.073" />
-  <C value="-1.4189" />
-  <D value="-0.00077787" />
-  <E value="-7.5252E-07" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="456.61" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000087851" />
-  <B value="1.0397" />
-  <C value="505.4" />
-  <D value="47466" />
-  <Tmin units="K"  value="456.61" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.093807" />
-  <B value="-27.232" />
-  <C value="-1.5935" />
-  <D value="-0.0015645" />
-  <E value="6.8395E-07" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="645.58" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="1394.1" />
-  <B value="727.89" />
-  <C value="-0.38743" />
-  <D value="0.000075095" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.616" />
-  <B value="3368.2" />
-  <C value="-86.041" />
-  <Tmin units="K"  value="405.21" />
-  <Tmax units="K"  value="600.73" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.6125" />
-  <B value="-0.013599" />
-  <Tmin units="K"  value="241.93" />
-  <Tmax units="K"  value="456.61" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.501609" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.467551E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="341.6596" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0631774" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.884138" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3879" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15328" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0066" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.616" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.011193" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.3879" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17760" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15328" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="2"  value="2" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="135-01-3" />
-<Smiles name="SMILES"  value="c1(CC)c(CC)cccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="526" />
-<CompoundID name="Name"  value="M-diethylbenzene" />
-<StructureFormula name="Structure"  value="CH3CH2(C6H4)CH2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="663" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2880000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.488" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.255" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="454.252" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="189.23" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="189.259" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000664991" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.2182" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.156083" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.354019" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.742E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17460" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0911199" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.154E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.18E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.367E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="439500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.097E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.07091" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5546E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9123" />
-  <B value="-0.0052595" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="75.7" />
-  <Tmax units="K"  value="189.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.52578" />
-  <B value="0.25663" />
-  <C value="663" />
-  <D value="0.2955" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="638.07" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="153.5552" />
-  <B value="-11090.88" />
-  <C value="-19.79091" />
-  <D value="0.000016846" />
-  <E value="2" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="663" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.460804E+07" />
-  <B value="0.433681" />
-  <C value="-0.0244308" />
-  <D value="0.0154888" />
-  <E value="-0.0245419" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="638.07" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="663" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-15019" />
-  <B value="20.098" />
-  <C value="11.35" />
-  <D value="0.0044704" />
-  <E value="-0.0000034473" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="454.29" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115660" />
-  <B value="-734.22" />
-  <C value="13.598" />
-  <D value="-0.00034186" />
-  <E value="8.9326E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.31772" />
-  <B value="-425.84" />
-  <C value="-99.203" />
-  <D value="-21091" />
-  <E value="370.32" />
-  <Tmin units="K"  value="331.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.504" />
-  <B value="1313.6" />
-  <C value="0.03353" />
-  <D value="-9.5074E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="454.29" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000018496" />
-  <B value="0.38185" />
-  <C value="552.33" />
-  <D value="63.517" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.056303" />
-  <B value="5.6194" />
-  <C value="-1.5408" />
-  <D value="-0.00033118" />
-  <E value="-0.0000010873" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="454.29" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.25407" />
-  <B value="-0.039016" />
-  <C value="-216.19" />
-  <D value="1832400" />
-  <Tmin units="K"  value="454.29" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0080943" />
-  <B value="39.207" />
-  <C value="-3.1114" />
-  <D value="0.00028503" />
-  <E value="-0.0000046024" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="638.07" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-10213" />
-  <B value="753.93" />
-  <C value="-0.40768" />
-  <D value="0.00008049" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.511" />
-  <B value="3266.1" />
-  <C value="-90.749" />
-  <Tmin units="K"  value="398.51" />
-  <Tmax units="K"  value="588.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.2888" />
-  <B value="-0.01446" />
-  <Tmin units="K"  value="189.26" />
-  <Tmax units="K"  value="454.29" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.501609" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.571874E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="316.2069" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.255" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0633445" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.868204" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.354019" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.156083" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0066" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.616" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.01075" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.354019" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17460" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.156083" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="2"  value="2" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="141-93-5" />
-<Smiles name="SMILES"  value="c1(CC)cc(CC)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="527" />
-<CompoundID name="Name"  value="P-diethylbenzene" />
-<StructureFormula name="Structure"  value="CH3CH2(C6H4)CH2CH3" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="657.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2803000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4805" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.247" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="456.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="230.3" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="230.325" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.21291" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.2182" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15645" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.403" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.58E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17660" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09112" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.154E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.23E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.385E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="433100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.06E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1492" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5553E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.6072" />
-  <B value="-0.0041601" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="92.13" />
-  <Tmax units="K"  value="230.33" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50239" />
-  <B value="0.25108" />
-  <C value="657.9" />
-  <D value="0.28806" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="657.9" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="108.74" />
-  <B value="-9636.7" />
-  <C value="-12.656" />
-  <D value="0.000006664" />
-  <E value="2" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="657.9" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.468714E+07" />
-  <B value="-1.551219" />
-  <C value="6.621841" />
-  <D value="-8.199596" />
-  <E value="3.486311" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="657.9" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7197.6" />
-  <B value="988.33" />
-  <C value="-2.1237" />
-  <D value="0.0060518" />
-  <E value="-0.0000076904" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="230.33" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="42717" />
-  <B value="-14.138" />
-  <C value="11.106" />
-  <D value="0.0050234" />
-  <E value="-0.0000039715" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="456.94" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="117030" />
-  <B value="-755.24" />
-  <C value="13.637" />
-  <D value="-0.00037709" />
-  <E value="9.9721E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33339" />
-  <B value="-427.85" />
-  <C value="-102.98" />
-  <D value="-24864" />
-  <E value="-4016.1" />
-  <Tmin units="K"  value="328.95" />
-  <Tmax units="K"  value="1809" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.766" />
-  <B value="1322.3" />
-  <C value="0.075076" />
-  <D value="-1.4518E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="456.94" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.2136E-07" />
-  <B value="0.49617" />
-  <C value="343.97" />
-  <D value="-290.07" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.054323" />
-  <B value="-5.9143" />
-  <C value="-1.4413" />
-  <D value="-0.00065059" />
-  <E value="-8.3255E-07" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="456.94" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000023956" />
-  <B value="1.1969" />
-  <C value="213.51" />
-  <D value="48127" />
-  <Tmin units="K"  value="456.94" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.059365" />
-  <B value="-49.68" />
-  <C value="-1.6376" />
-  <D value="-0.0024385" />
-  <E value="0.000001123" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="657.9" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-2984.9" />
-  <B value="626.67" />
-  <C value="0.03675" />
-  <D value="-0.00047692" />
-  <E value="2.3139E-07" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.159" />
-  <B value="3770.1" />
-  <C value="-65.556" />
-  <Tmin units="K"  value="395.19" />
-  <Tmax units="K"  value="590.39" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.1726" />
-  <B value="-0.012096" />
-  <Tmin units="K"  value="230.32" />
-  <Tmax units="K"  value="456.94" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.50161" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.826599E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="279.7577" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.247" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.54175" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0635175" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.866273" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.403" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15645" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0066" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.616" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.006384" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.9778" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.403" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17660" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15645" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="7"  value="4" />
-  <group id="2"  value="2" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="13"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="9"  value="4" />
-  <group id="12"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="105-05-5" />
-<Smiles name="SMILES"  value="c1(CC)ccc(CC)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="530" />
-<CompoundID name="Name"  value="1,2,3,4-tetramethylbenzene" />
-<StructureFormula name="Structure"  value="(C6H2)(CH3)4" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="690" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2860000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.482" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="478.19" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="266.9" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="266.9" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.9878" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.149073" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.417172" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.402E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18860" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.66E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09296" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.168E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.305E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.324E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="416500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.123E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1163" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5376E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.8081" />
-  <B value="-0.0041252" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="106.76" />
-  <Tmax units="K"  value="266.9" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.62671" />
-  <B value="0.276" />
-  <C value="690" />
-  <D value="0.30501" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="670.57" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="103.3938" />
-  <B value="-9866.6" />
-  <C value="-11.74655" />
-  <D value="5.432648E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="693" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.827737E+07" />
-  <B value="0.20659" />
-  <C value="0.354625" />
-  <D value="0.156354" />
-  <E value="-0.400825" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="670.57" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="66629" />
-  <B value="-379.76" />
-  <C value="9.332" />
-  <D value="-0.039854" />
-  <E value="0.000072087" />
-  <Tmin units="K"  value="91" />
-  <Tmax units="K"  value="223.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="191090" />
-  <B value="-1527.7" />
-  <C value="20.231" />
-  <D value="-0.019977" />
-  <E value="0.000019333" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="519.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="108680" />
-  <B value="-536.06" />
-  <C value="13.006" />
-  <D value="0.00026578" />
-  <E value="-1.0197E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.31708" />
-  <B value="-424.09" />
-  <C value="-116.37" />
-  <D value="-38824" />
-  <E value="-120.02" />
-  <Tmin units="K"  value="346.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.555" />
-  <B value="1810.8" />
-  <C value="0.0032112" />
-  <D value="-3.0199E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="478.19" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.0975E-08" />
-  <B value="0.80432" />
-  <C value="144.14" />
-  <D value="-8326.5" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.046705" />
-  <B value="-31.572" />
-  <C value="-1.2356" />
-  <D value="-0.0012463" />
-  <E value="-2.6103E-07" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="478.19" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0001001" />
-  <B value="1.0331" />
-  <C value="653.92" />
-  <D value="21466" />
-  <Tmin units="K"  value="478.19" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0097807" />
-  <B value="201.26" />
-  <C value="-4.2769" />
-  <D value="0.0037572" />
-  <E value="-0.0000068682" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="670.57" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="14350" />
-  <B value="683.41" />
-  <C value="-0.34548" />
-  <D value="0.000063808" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.207" />
-  <B value="3942.9" />
-  <C value="-70.977" />
-  <Tmin units="K"  value="419.85" />
-  <Tmax units="K"  value="620" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.3745" />
-  <B value="-0.013807" />
-  <Tmin units="K"  value="266.9" />
-  <Tmax units="K"  value="478.19" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.512922" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.50538E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="333.7538" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.256" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.45969" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0648309" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.908473" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.417172" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.149073" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.1278" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.672" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.005169" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.84333" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.417172" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18860" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.149073" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="2" />
-  <group id="12"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="2" />
-  <group id="11"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="10"  value="2" />
-  <group id="11"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="2" />
-  <group id="8"  value="4" />
-  <group id="1"  value="4" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="2" />
-  <group id="12"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="2" />
-  <group id="11"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="488-23-3" />
-<Smiles name="SMILES"  value="c1(C)c(C)c(C)c(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="531" />
-<CompoundID name="Name"  value="1,2,3,5-tetramethylbenzene" />
-<StructureFormula name="Structure"  value="(C6H2)(CH3)4" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="679" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3220000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.436" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="471.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="249.46" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="249.46" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.886139" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.151385" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.459061" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.516E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18330" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09296" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.168E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.054E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.231E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="422500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.072E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.15" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.532E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.728" />
-  <B value="-0.0038845" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="99.78" />
-  <Tmax units="K"  value="249.46" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.5261" />
-  <B value="0.25428" />
-  <C value="679" />
-  <D value="0.28565" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="679" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="108.28" />
-  <B value="-9936.6" />
-  <C value="-12.519" />
-  <D value="0.0000062754" />
-  <E value="2" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="679" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.6549E+07" />
-  <B value="0.31372" />
-  <C value="0.25924" />
-  <D value="-0.3264" />
-  <E value="0.12301" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="679" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="88.391" />
-  <B value="1331.3" />
-  <C value="-5.2242" />
-  <D value="0.018095" />
-  <E value="-0.000025164" />
-  <Tmin units="K"  value="92.4" />
-  <Tmax units="K"  value="249.46" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="180380" />
-  <B value="-63.604" />
-  <C value="9.2496" />
-  <D value="0.0072443" />
-  <E value="-0.0000031051" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="480" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="109230" />
-  <B value="-579.21" />
-  <C value="13.116" />
-  <D value="0.00014705" />
-  <E value="-5.951E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.3267" />
-  <B value="-429.83" />
-  <C value="-108.17" />
-  <D value="-65519" />
-  <E value="104920" />
-  <Tmin units="K"  value="339.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-14.031" />
-  <B value="1747.6" />
-  <C value="0.263" />
-  <D value="-3.7653E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="471.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.7114E-07" />
-  <B value="0.50662" />
-  <C value="335.88" />
-  <D value="-402.07" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.064932" />
-  <B value="-8.9077" />
-  <C value="-1.3593" />
-  <D value="-0.00066705" />
-  <E value="-6.8372E-07" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="471.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000082384" />
-  <B value="1.0555" />
-  <C value="595.15" />
-  <D value="34335" />
-  <Tmin units="K"  value="471.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0077784" />
-  <B value="249.63" />
-  <C value="-4.8091" />
-  <D value="0.0051648" />
-  <E value="-0.0000085507" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="679" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="15661" />
-  <B value="655.05" />
-  <C value="-0.30287" />
-  <D value="0.000047023" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.323" />
-  <B value="3961.7" />
-  <C value="-66.892" />
-  <Tmin units="K"  value="407.71" />
-  <Tmax units="K"  value="610" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4676" />
-  <B value="-0.013966" />
-  <Tmin units="K"  value="249.46" />
-  <Tmax units="K"  value="471.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.512922" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.327233E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="319.2893" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0649311" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.894741" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.46" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.151385" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.1278" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.672" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.019944" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.426" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18330" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.151385" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="2" />
-  <group id="12"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="2" />
-  <group id="11"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="10"  value="2" />
-  <group id="11"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="2" />
-  <group id="8"  value="4" />
-  <group id="1"  value="4" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="2" />
-  <group id="12"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="2" />
-  <group id="11"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="527-53-7" />
-<Smiles name="SMILES"  value="c1(C)c(C)c(C)cc(C)c1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="532" />
-<CompoundID name="Name"  value="1,2,4,5-tetramethylbenzene" />
-<StructureFormula name="Structure"  value="(C6H2)(CH3)4" />
-<Family name="Family"  value="10" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="676" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2900000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.482" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.249" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="470" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="352.384" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="352.384" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1784.79" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.221" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15228" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.423" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.502E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09296" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.168E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.527E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.177E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="418500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.1E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.10541" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.507E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.6888" />
-  <B value="-1.9613E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.65779" />
-  <B value="0.28461" />
-  <C value="677.16" />
-  <D value="0.31429" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="677.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="96.028" />
-  <B value="-9355.7" />
-  <C value="-10.676" />
-  <D value="0.0000049509" />
-  <E value="2" />
-  <Tmin units="K"  value="346.75" />
-  <Tmax units="K"  value="676" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.607707E+08" />
-  <B value="4.915197" />
-  <C value="-10.37671" />
-  <D value="9.303886" />
-  <E value="-3.220797" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="658.97" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="1997.1" />
-  <B value="1178.3" />
-  <C value="-3.2722" />
-  <D value="0.0077475" />
-  <E value="-0.0000066937" />
-  <Tmin units="K"  value="92.2" />
-  <Tmax units="K"  value="352.38" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="139940" />
-  <B value="1169.1" />
-  <C value="1.2977" />
-  <D value="0.02859" />
-  <E value="-0.000023286" />
-  <Tmin units="K"  value="352.15" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="110940" />
-  <B value="-562.53" />
-  <C value="13.019" />
-  <D value="0.00027207" />
-  <E value="-1.0669E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33617" />
-  <B value="-444.13" />
-  <C value="-103.01" />
-  <D value="-89798" />
-  <E value="177990" />
-  <Tmin units="K"  value="337.58" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.4175" />
-  <B value="1452.8" />
-  <C value="-0.39341" />
-  <D value="2.9469E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="352.38" />
-  <Tmax units="K"  value="469.99" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.2635E-07" />
-  <B value="0.49106" />
-  <C value="324.48" />
-  <D value="3435.1" />
-  <Tmin units="K"  value="352.38" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.023024" />
-  <B value="-350.01" />
-  <C value="0.1946" />
-  <D value="-0.0044419" />
-  <E value="6.7822E-07" />
-  <Tmin units="K"  value="352.38" />
-  <Tmax units="K"  value="613.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000066062" />
-  <B value="1.0649" />
-  <C value="306.1" />
-  <D value="93850" />
-  <Tmin units="K"  value="469.99" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.022308" />
-  <B value="-40.303" />
-  <C value="-2.2467" />
-  <D value="-0.001602" />
-  <E value="-9.4735E-07" />
-  <Tmin units="K"  value="352.38" />
-  <Tmax units="K"  value="658.97" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="27870" />
-  <B value="560.2" />
-  <C value="0.043817" />
-  <D value="-0.000406" />
-  <E value="0.0000001904" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.278" />
-  <B value="3898.8" />
-  <C value="-70.102" />
-  <Tmin units="K"  value="412.75" />
-  <Tmax units="K"  value="607.87" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.2617" />
-  <B value="-0.0095155" />
-  <Tmin units="K"  value="352.38" />
-  <Tmax units="K"  value="469.99" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.512922" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.75928E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="295.9222" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.249" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0637472" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.89203" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.423" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15228" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.1278" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.672" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.014791" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.423" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17140" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15228" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="2" />
-  <group id="12"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="2" />
-  <group id="11"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="10"  value="2" />
-  <group id="11"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="7"  value="2" />
-  <group id="8"  value="4" />
-  <group id="1"  value="4" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="10"  value="2" />
-  <group id="12"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="2" />
-  <group id="11"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="95-93-2" />
-<Smiles name="SMILES"  value="c1(C)c(C)cc(C)c(C)c1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="576" />
-<CompoundID name="Name"  value="2-ethyl-m-xylene" />
-<StructureFormula name="Structure"  value="CH3CH2(C6H3)(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="670" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2960000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.446" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="463.19" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="257" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="256.89" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.81505" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.151424" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.405" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.415E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18140" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0920399" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.161E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.623E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.379E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="421000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.471E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2603" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.548E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.6854" />
-  <B value="-0.0037546" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="102.76" />
-  <Tmax units="K"  value="256.89" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.55372" />
-  <B value="0.25979" />
-  <C value="670" />
-  <D value="0.29804" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="649.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="101.54" />
-  <B value="-9425" />
-  <C value="-11.552" />
-  <D value="0.0000057989" />
-  <E value="2" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="671" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.2672E+07" />
-  <B value="1.1027" />
-  <C value="-0.68529" />
-  <D value="-0.33367" />
-  <E value="0.36103" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="649.2" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="23735" />
-  <B value="400.93" />
-  <C value="5.6" />
-  <D value="-0.033991" />
-  <E value="0.000064505" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="256.89" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="77646" />
-  <B value="-101.26" />
-  <C value="11.392" />
-  <D value="0.0045401" />
-  <E value="-0.0000038677" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="463.19" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="80902" />
-  <B value="-471.57" />
-  <C value="13.059" />
-  <D value="0.00022749" />
-  <E value="-9.0171E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.35368" />
-  <B value="-470.21" />
-  <C value="-86.839" />
-  <D value="-88080" />
-  <E value="193440" />
-  <Tmin units="K"  value="335" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.587" />
-  <B value="1737.4" />
-  <C value="0.54173" />
-  <D value="-0.0000007502" />
-  <E value="2" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="463.19" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000044354" />
-  <B value="0.29008" />
-  <C value="895.67" />
-  <D value="100.88" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.038284" />
-  <B value="-32.06" />
-  <C value="-1.2755" />
-  <D value="-0.0012699" />
-  <E value="-0.0000004068" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="463.19" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000097738" />
-  <B value="1.031" />
-  <C value="536.66" />
-  <D value="42862" />
-  <Tmin units="K"  value="463.19" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0078769" />
-  <B value="272" />
-  <C value="-4.9636" />
-  <D value="0.0055943" />
-  <E value="-0.0000090797" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="649.2" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-18638" />
-  <B value="815.63" />
-  <C value="-0.4908" />
-  <D value="0.00011128" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.219" />
-  <B value="3842.2" />
-  <C value="-66.846" />
-  <Tmin units="K"  value="406.45" />
-  <Tmax units="K"  value="600" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.7285" />
-  <B value="-0.013322" />
-  <Tmin units="K"  value="256.89" />
-  <Tmax units="K"  value="463.19" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.507256" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.145862E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="347.4512" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.0844" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0649154" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.894889" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.405" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.151424" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0672" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.644" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.8602" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.405" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18140" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.151424" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="12"  value="2" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
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-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
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-  <group id="7"  value="3" />
-  <group id="8"  value="3" />
-  <group id="2"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
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-  <group id="12"  value="2" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="2870-04-4" />
-<Smiles name="SMILES"  value="c1(C)c(CC)c(C)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="577" />
-<CompoundID name="Name"  value="2-ethyl-p-xylene" />
-<StructureFormula name="Structure"  value="CH3CH2(C6H3)(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="680" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3380000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.461" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="460.09" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="219" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="219.52" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0748611" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.153715" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.36" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.579E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17610" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0920399" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.161E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.218E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.273E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="436600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.519E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.03" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.543E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.829" />
-  <B value="-0.0044696" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="87.81" />
-  <Tmax units="K"  value="219.52" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.15639" />
-  <B value="0.13957" />
-  <C value="680" />
-  <D value="0.19566" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="639.66" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="51.35796" />
-  <B value="-7093.865" />
-  <C value="-3.98884" />
-  <D value="0.0000002143" />
-  <E value="2" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="680" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.269938E+07" />
-  <B value="2.580922" />
-  <C value="-6.4761" />
-  <D value="7.125795" />
-  <E value="-2.740318" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="663" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7232.9" />
-  <B value="1019.6" />
-  <C value="-2.26" />
-  <D value="0.006668" />
-  <E value="-0.0000087976" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="219.52" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115180" />
-  <B value="-69.179" />
-  <C value="10.574" />
-  <D value="0.0065199" />
-  <E value="-0.0000055164" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="459.98" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="90693" />
-  <B value="-533.27" />
-  <C value="13.139" />
-  <D value="0.00014143" />
-  <E value="-6.0863E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34598" />
-  <B value="-446.91" />
-  <C value="-99.564" />
-  <D value="-42376" />
-  <E value="51770" />
-  <Tmin units="K"  value="331.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.139" />
-  <B value="1509" />
-  <C value="0.050995" />
-  <D value="-2.3531E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="459.98" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000010483" />
-  <B value="0.4491" />
-  <C value="412.22" />
-  <D value="-1561.4" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.080449" />
-  <B value="4.7926" />
-  <C value="-1.4191" />
-  <D value="-0.00032019" />
-  <E value="-9.3368E-07" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="459.98" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000085732" />
-  <B value="1.0445" />
-  <C value="516.18" />
-  <D value="46622" />
-  <Tmin units="K"  value="459.98" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.025429" />
-  <B value="29.001" />
-  <C value="-2.5612" />
-  <D value="-0.001025" />
-  <E value="-0.0000010416" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="663" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-20399" />
-  <B value="799.64" />
-  <C value="-0.46931" />
-  <D value="0.00010452" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.962" />
-  <B value="3588.7" />
-  <C value="-79.823" />
-  <Tmin units="K"  value="413.35" />
-  <Tmax units="K"  value="600" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.3451" />
-  <B value="-0.014201" />
-  <Tmin units="K"  value="219.52" />
-  <Tmax units="K"  value="459.98" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.507256" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.535834E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="310.7879" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.252" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0654917" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.881517" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.36" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.153715" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0672" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.644" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.36" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17610" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.153715" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="12"  value="2" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="7"  value="3" />
-  <group id="8"  value="3" />
-  <group id="2"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="12"  value="2" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1758-88-9" />
-<Smiles name="SMILES"  value="c1(C)c(CC)cc(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="578" />
-<CompoundID name="Name"  value="4-ethyl-m-xylene" />
-<StructureFormula name="Structure"  value="CH3CH2(C6H3)(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="665" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2850000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.456" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="461.59" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="210" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="210.27" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0181496" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.153864" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.409" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.543E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17650" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0920399" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.161E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.08E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.286E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="436600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.293E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.09" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.544E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8871" />
-  <B value="-0.0047021" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="84.11" />
-  <Tmax units="K"  value="210.27" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53184" />
-  <B value="0.25635" />
-  <C value="665" />
-  <D value="0.29535" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="641.07" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="109.6" />
-  <B value="-9849.7" />
-  <C value="-12.73" />
-  <D value="0.0000063582" />
-  <E value="2" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="665" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.586476E+07" />
-  <B value="0.958711" />
-  <C value="-1.952194" />
-  <D value="2.240006" />
-  <E value="-0.865941" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="641.07" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="665" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="95699" />
-  <B value="-84.431" />
-  <C value="11.066" />
-  <D value="0.0051032" />
-  <E value="-0.0000041785" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="461.59" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="90693" />
-  <B value="-533.27" />
-  <C value="13.139" />
-  <D value="0.00014143" />
-  <E value="-6.0863E-08" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.33624" />
-  <B value="-432.23" />
-  <C value="-105.71" />
-  <D value="-27857" />
-  <E value="4073.5" />
-  <Tmin units="K"  value="332.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.665" />
-  <B value="1419.5" />
-  <C value="0.18354" />
-  <D value="-0.0000003451" />
-  <E value="2" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="461.59" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000037216" />
-  <B value="0.29591" />
-  <C value="752.65" />
-  <D value="-7.7443" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.081171" />
-  <B value="5.0587" />
-  <C value="-1.4195" />
-  <D value="-0.00031748" />
-  <E value="-9.1756E-07" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="461.59" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000083547" />
-  <B value="1.0482" />
-  <C value="520.64" />
-  <D value="45100" />
-  <Tmin units="K"  value="461.59" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015347" />
-  <B value="66.34" />
-  <C value="-3.091" />
-  <D value="0.00031864" />
-  <E value="-0.0000032686" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="641.07" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-20399" />
-  <B value="799.64" />
-  <C value="-0.46931" />
-  <D value="0.00010452" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.128" />
-  <B value="3744.2" />
-  <C value="-71.727" />
-  <Tmin units="K"  value="400" />
-  <Tmax units="K"  value="593.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.5864" />
-  <B value="-0.013635" />
-  <Tmin units="K"  value="210.27" />
-  <Tmax units="K"  value="461.59" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.507256" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.544402E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="299.6126" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.251" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0648944" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.880761" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.409" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.153864" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0672" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.644" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.409" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17650" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.153864" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
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-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
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-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
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-  <group id="7"  value="3" />
-  <group id="8"  value="3" />
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-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
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-  <group id="12"  value="2" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="874-41-9" />
-<Smiles name="SMILES"  value="c1(CC)c(C)cc(C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="579" />
-<CompoundID name="Name"  value="4-ethyl-o-xylene" />
-<StructureFormula name="Structure"  value="CH3CH2(C6H3)(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="666" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2890000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.452" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="462.93" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="206" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="206.22" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00343448" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.154172" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.42" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.552E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17990" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0920399" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.161E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.209E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.274E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="436600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.205E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.11" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.542E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.8776" />
-  <B value="-0.0047766" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="82.49" />
-  <Tmax units="K"  value="206.22" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54664" />
-  <B value="0.26088" />
-  <C value="666" />
-  <D value="0.29186" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="642.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="96.694" />
-  <B value="-9142.9" />
-  <C value="-10.852" />
-  <D value="0.0000055519" />
-  <E value="2" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="667" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.3714E+07" />
-  <B value="-2.7554" />
-  <C value="9.4578" />
-  <D value="-11.023" />
-  <E value="4.6307" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="642.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="666" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="89767" />
-  <B value="-77.889" />
-  <C value="11.113" />
-  <D value="0.0049399" />
-  <E value="-0.0000039958" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="462.93" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="90693" />
-  <B value="-533.27" />
-  <C value="13.139" />
-  <D value="0.00014143" />
-  <E value="-6.0863E-08" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.37792" />
-  <B value="-498.77" />
-  <C value="-87.527" />
-  <D value="-88381" />
-  <E value="187860" />
-  <Tmin units="K"  value="333" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.1159" />
-  <B value="1410.6" />
-  <C value="-0.43411" />
-  <D value="7.8135E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="462.93" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.8567E-07" />
-  <B value="0.52279" />
-  <C value="312.52" />
-  <D value="-1851" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.061613" />
-  <B value="4.0176" />
-  <C value="-1.4936" />
-  <D value="-0.00037218" />
-  <E value="-9.9721E-07" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="462.93" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000083697" />
-  <B value="1.0475" />
-  <C value="520.73" />
-  <D value="45665" />
-  <Tmin units="K"  value="462.93" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.021075" />
-  <B value="39.933" />
-  <C value="-2.7814" />
-  <D value="-0.00042216" />
-  <E value="-0.0000020214" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="642.75" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-20399" />
-  <B value="799.64" />
-  <C value="-0.46931" />
-  <D value="0.00010452" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.317" />
-  <B value="3913.1" />
-  <C value="-63.321" />
-  <Tmin units="K"  value="400.23" />
-  <Tmax units="K"  value="594.25" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0327" />
-  <B value="-0.015022" />
-  <Tmin units="K"  value="206.22" />
-  <Tmax units="K"  value="462.93" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.507256" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.415788E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="313.1763" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0648412" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.878797" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.42" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.154172" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0672" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.644" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.42" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17990" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.154172" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="12"  value="2" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="7"  value="3" />
-  <group id="8"  value="3" />
-  <group id="2"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="12"  value="2" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="9"  value="3" />
-  <group id="11"  value="2" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="934-80-5" />
-<Smiles name="SMILES"  value="c1(C)c(C)cc(CC)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="586" />
-<CompoundID name="Name"  value="1-methyl-3-n-propylbenzene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH2CH2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="656" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2860000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.482" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.249" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="455.13" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="190.57" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="190.57" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000721452" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.156623" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.412785" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.794E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17510" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.07E-31" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09112" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.154E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.414E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.352E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="436800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.06E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5516E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.0174" />
-  <B value="-0.0059147" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="76.23" />
-  <Tmax units="K"  value="190.57" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.18222" />
-  <B value="0.15152" />
-  <C value="656" />
-  <D value="0.20178" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="654" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="107.4588" />
-  <B value="-9508.773" />
-  <C value="-12.48918" />
-  <D value="6.776919E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="654" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.194565E+07" />
-  <B value="0.0524158" />
-  <C value="1.088831" />
-  <D value="-1.22236" />
-  <E value="0.439479" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="654" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="656" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="156110" />
-  <B value="-38.093" />
-  <C value="10.159" />
-  <D value="0.0050313" />
-  <E value="-0.0000015247" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="490.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97127" />
-  <B value="-599.11" />
-  <C value="13.273" />
-  <D value="0.000011665" />
-  <E value="-1.9003E-08" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34716" />
-  <B value="-445.08" />
-  <C value="-93.628" />
-  <D value="-50591" />
-  <E value="81753" />
-  <Tmin units="K"  value="327" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-17.301" />
-  <B value="1601.4" />
-  <C value="0.91018" />
-  <D value="-0.0000014707" />
-  <E value="2" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="603.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.3681E-08" />
-  <B value="0.81524" />
-  <C value="130.94" />
-  <D value="-9552" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.074198" />
-  <B value="4.023" />
-  <C value="-1.4364" />
-  <D value="-0.00042252" />
-  <E value="-0.0000008562" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="454.95" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000083513" />
-  <B value="1.0517" />
-  <C value="570.8" />
-  <D value="33790" />
-  <Tmin units="K"  value="454.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0086511" />
-  <B value="61.14" />
-  <C value="-3.1888" />
-  <D value="0.0004569" />
-  <E value="-0.0000046729" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="654" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-26053" />
-  <B value="805.01" />
-  <C value="-0.46803" />
-  <D value="0.00010355" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.2" />
-  <B value="3779.7" />
-  <C value="-64.304" />
-  <Tmin units="K"  value="395" />
-  <Tmax units="K"  value="590" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.1694" />
-  <B value="-0.011417" />
-  <Tmin units="K"  value="190.57" />
-  <Tmax units="K"  value="603.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.50161" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.75928E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="287.1671" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.249" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0643271" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.865762" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.412785" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.156623" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0066" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.616" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.412785" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17510" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.156623" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
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-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
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-<GCmethod name="PPR78" >
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-  <group id="2"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
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-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1074-43-7" />
-<Smiles name="SMILES"  value="c1(C)cc(CCC)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="587" />
-<CompoundID name="Name"  value="1-methyl-4-n-propylbenzene" />
-<StructureFormula name="Structure"  value="CH3(C6H4)CH2CH2CH3" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="658" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2860000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.482" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="456.53" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="209.455" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="209.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0171898" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="134.218" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.157097" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.413441" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.599E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17460" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09112" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.154E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.314E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.382E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="430400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.151E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.09" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.5528E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.8857" />
-  <B value="-0.0053004" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="83.82" />
-  <Tmax units="K"  value="209.55" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.48219" />
-  <B value="0.24259" />
-  <C value="658" />
-  <D value="0.32531" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="632.5" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="103.2332" />
-  <B value="-9321.423" />
-  <C value="-11.85346" />
-  <D value="6.228128E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="656" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.9632E+07" />
-  <B value="-0.13089" />
-  <C value="1.5769" />
-  <D value="-1.8325" />
-  <E value="0.74608" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="656" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="214740" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="658" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="128960" />
-  <B value="-102.23" />
-  <C value="11.269" />
-  <D value="0.0022913" />
-  <E value="5.0742E-07" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="492" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97127" />
-  <B value="-599.11" />
-  <C value="13.273" />
-  <D value="0.000011665" />
-  <E value="-1.9003E-08" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34983" />
-  <B value="-450.15" />
-  <C value="-93.925" />
-  <D value="-54544" />
-  <E value="91978" />
-  <Tmin units="K"  value="328" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-65.00531" />
-  <B value="3273.06" />
-  <C value="8.413079" />
-  <D value="-0.0000101347" />
-  <E value="2" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="553.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.8653E-08" />
-  <B value="0.80621" />
-  <C value="137.95" />
-  <D value="-9253.2" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.081049" />
-  <B value="3.2759" />
-  <C value="-1.4026" />
-  <D value="-0.00043634" />
-  <E value="-7.9035E-07" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="456.45" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000083347" />
-  <B value="1.0517" />
-  <C value="573.97" />
-  <D value="33136" />
-  <Tmin units="K"  value="456.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.19472" />
-  <B value="-2.8463" />
-  <C value="-1.2726" />
-  <D value="-0.000855" />
-  <E value="4.6239E-07" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="656" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-26053" />
-  <B value="805.01" />
-  <C value="-0.46803" />
-  <D value="0.00010355" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.139" />
-  <B value="3767" />
-  <C value="-64.622" />
-  <Tmin units="K"  value="397.53" />
-  <Tmax units="K"  value="590" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.52" />
-  <B value="-0.010859" />
-  <Tmin units="K"  value="209.55" />
-  <Tmax units="K"  value="553.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.50161" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.79684E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="283.8998" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="173.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0648127" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.863678" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.413441" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.157097" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0066" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.616" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.413441" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17460" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.157097" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="13"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1074-55-1" />
-<Smiles name="SMILES"  value="c1(C)ccc(CCC)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="544" />
-<CompoundID name="Name"  value="P-diisopropylbenzene" />
-<StructureFormula name="Structure"  value="(CH3)2CH(C6H4)CH(CH3)2" />
-<Family name="Family"  value="17" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="675" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2360000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.584" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="483.52" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="256.08" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="256.08" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.697953" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="162.271" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.190236" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.476415" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.178E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16930" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.101" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.404E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.76E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.47804E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="488000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3262" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.77E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.9021" />
-  <B value="-0.0029994" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="102.43" />
-  <Tmax units="K"  value="256.08" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77801" />
-  <B value="0.34547" />
-  <C value="675" />
-  <D value="0.38736" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="666.21" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="121.6259" />
-  <B value="-10711.76" />
-  <C value="-14.56272" />
-  <D value="8.944308E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="689" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.572101E+07" />
-  <B value="2.166143" />
-  <C value="-4.616074" />
-  <D value="4.777254" />
-  <E value="-1.852374" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="666.21" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34130" />
-  <B value="321.92" />
-  <C value="9.2079" />
-  <D value="-0.053989" />
-  <E value="0.00010157" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="256.08" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-70570" />
-  <B value="94.476" />
-  <C value="11.349" />
-  <D value="0.0048258" />
-  <E value="-0.0000034771" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="483.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="100830" />
-  <B value="-531.56" />
-  <C value="13.456" />
-  <D value="0.000043333" />
-  <E value="-2.4118E-08" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34296" />
-  <B value="-577.3" />
-  <C value="-147.03" />
-  <D value="-140880" />
-  <E value="339020" />
-  <Tmin units="K"  value="344.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.9912" />
-  <B value="1148.7" />
-  <C value="-0.35833" />
-  <D value="4.6037E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="483.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.0354E-07" />
-  <B value="0.48062" />
-  <C value="391.1" />
-  <D value="176.97" />
-  <Tmin units="K"  value="483.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.043466" />
-  <B value="-14.777" />
-  <C value="-1.4776" />
-  <D value="-0.00080068" />
-  <E value="-0.0000006904" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="483.65" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.31596" />
-  <B value="-0.074042" />
-  <C value="-318.59" />
-  <D value="1928600" />
-  <Tmin units="K"  value="483.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01271" />
-  <B value="60.745" />
-  <C value="-3.2229" />
-  <D value="0.00049535" />
-  <E value="-0.0000035281" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="666.21" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-44517" />
-  <B value="1071.8" />
-  <C value="-0.66372" />
-  <D value="0.00015645" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.599" />
-  <B value="3490" />
-  <C value="-98.353" />
-  <Tmin units="K"  value="407.05" />
-  <Tmax units="K"  value="597.86" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.216" />
-  <B value="-0.0097312" />
-  <Tmin units="K"  value="256.08" />
-  <Tmax units="K"  value="483.65" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.563273" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.001313E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="326.4983" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.256" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="214.08" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.118" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0776962" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.861206" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.390023" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.190236" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.3538" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.688" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.022869" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.0168" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.390023" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16930" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.190236" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="7"  value="4" />
-  <group id="8"  value="2" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="100-18-5" />
-<Smiles name="SMILES"  value="c1(C(C)C)ccc(C(C)C)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1054" />
-<CompoundID name="Name"  value="Methyl isobutyl ketone" />
-<StructureFormula name="Structure"  value="CH3COCH2CH(CH3)2" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="574.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3270000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.3406" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="389.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="189.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="189.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0698742" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.161" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12581" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.352" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.828E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17420" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06972" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.88E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.88E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.351E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="407000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9710000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.393" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.49E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.236" />
-  <B value="-0.0065382" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="75.66" />
-  <Tmax units="K"  value="189.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.70438" />
-  <B value="0.26215" />
-  <C value="574.6" />
-  <D value="0.2872" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="574.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="151.9969" />
-  <B value="-9958.63" />
-  <C value="-19.68914" />
-  <D value="0.0000167819" />
-  <E value="2" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="574.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.7929E+07" />
-  <B value="-4.5647" />
-  <C value="14.372" />
-  <D value="-16.097" />
-  <E value="6.5387" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="574.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="2120" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="189.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="93433" />
-  <B value="-8.9197" />
-  <C value="10.885" />
-  <D value="0.0029916" />
-  <E value="-6.6769E-07" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="97540" />
-  <B value="-634.68" />
-  <C value="12.939" />
-  <D value="0.000018497" />
-  <E value="-1.9665E-08" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="1500.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26403" />
-  <B value="-313.96" />
-  <C value="-40.054" />
-  <D value="-41014" />
-  <E value="79808" />
-  <Tmin units="K"  value="287.3" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.5441" />
-  <B value="1138.8" />
-  <C value="-0.34128" />
-  <D value="0.0000016581" />
-  <E value="2" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="389.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.9033E-07" />
-  <B value="0.63516" />
-  <C value="190.41" />
-  <D value="3013.2" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.05085" />
-  <B value="-96.32" />
-  <C value="-0.95078" />
-  <D value="-0.0031661" />
-  <E value="-0.0000020547" />
-  <Tmin units="K"  value="171.42" />
-  <Tmax units="K"  value="451.42" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-874190" />
-  <B value="0.020464" />
-  <C value="1.7911E+07" />
-  <D value="-8.1274E+12" />
-  <Tmin units="K"  value="276.09" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0053825" />
-  <B value="238.91" />
-  <C value="-5.4341" />
-  <D value="0.0080583" />
-  <E value="-0.000014754" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="574.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="10053" />
-  <B value="541.95" />
-  <C value="-0.29513" />
-  <D value="0.000061306" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="1500.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.464" />
-  <B value="3468.2" />
-  <C value="-40.674" />
-  <Tmin units="K"  value="348.15" />
-  <Tmax units="K"  value="513.74" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8866" />
-  <B value="-0.015149" />
-  <Tmin units="K"  value="189.15" />
-  <Tmax units="K"  value="389.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.375279" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.685059E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="277.9347" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.256" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="129.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-3.0405" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0492845" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.805767" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.352" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.12581" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5959" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.952" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="6.4011" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.352" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17420" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.12581" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-10-1" />
-<Smiles name="SMILES"  value="CC(C)CC(=O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1057" />
-<CompoundID name="Name"  value="3-heptanone" />
-<StructureFormula name="Structure"  value="CH3(CH2)3COC2H5" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="605" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3010000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.421" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="420.55" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="234.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="234.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.29921" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.185" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.140257" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.407565" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.539E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17940" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07996" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.124E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.01E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.196E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="448500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.81E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.13085" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.098E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.6961" />
-  <B value="-0.0051762" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="93.66" />
-  <Tmax units="K"  value="234.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.65544" />
-  <B value="0.26958" />
-  <C value="605" />
-  <D value="0.29059" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="587" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.93996" />
-  <B value="-7156.968" />
-  <C value="-5.201278" />
-  <D value="1.288938E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="606.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.726896E+07" />
-  <B value="0.830475" />
-  <C value="-1.256385" />
-  <D value="1.592723" />
-  <E value="-0.756362" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="587" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="2320" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="234.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="215140" />
-  <B value="447.78" />
-  <C value="3.9106" />
-  <D value="0.020539" />
-  <E value="-0.000013511" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="480" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="122140" />
-  <B value="-668.77" />
-  <C value="13.117" />
-  <D value="-0.0000064986" />
-  <E value="-3.4969E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.29056" />
-  <B value="-339.49" />
-  <C value="-76.497" />
-  <D value="-41160" />
-  <E value="60961" />
-  <Tmin units="K"  value="303.3" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.982" />
-  <B value="1284.2" />
-  <C value="0.095491" />
-  <D value="-8.1894E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="421.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4757E-07" />
-  <B value="0.71999" />
-  <C value="184.44" />
-  <D value="-6805" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.025728" />
-  <B value="-61.893" />
-  <C value="-0.97852" />
-  <D value="-0.0021604" />
-  <E value="1.2683E-07" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="553.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1201.8" />
-  <B value="1.0398" />
-  <C value="1.4113E+10" />
-  <D value="-9.6162E+10" />
-  <Tmin units="K"  value="420.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011218" />
-  <B value="48.92" />
-  <C value="-3.2612" />
-  <D value="0.00080836" />
-  <E value="-0.0000049917" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="587" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="35513" />
-  <B value="545.55" />
-  <C value="-0.2495" />
-  <D value="0.000035433" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.049" />
-  <B value="3293.7" />
-  <C value="-74.523" />
-  <Tmin units="K"  value="363.15" />
-  <Tmax units="K"  value="540" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.2585" />
-  <B value="-0.012873" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="421.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.434587" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.34622E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="272.5799" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.251" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="149.75" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.055992" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.823035" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.407565" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.140257" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2711" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.496" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.407565" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17940" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.140257" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="19"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-35-4" />
-<Smiles name="SMILES"  value="CCC(=O)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1058" />
-<CompoundID name="Name"  value="4-heptanone" />
-<StructureFormula name="Structure"  value="(CH3CH2CH2)2CO" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="595" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2920000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.421" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="417.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="240.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="240.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.95766" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.185" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.140625" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.471409" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.567E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17410" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.34E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07996" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.124E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.01E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.196E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="448600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.86E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.18" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.09E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.6566" />
-  <B value="-0.0050159" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="96.26" />
-  <Tmax units="K"  value="240.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.78297" />
-  <B value="0.29215" />
-  <C value="595" />
-  <D value="0.33209" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="582.98" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="121.5579" />
-  <B value="-9310.284" />
-  <C value="-14.85267" />
-  <D value="0.000010781" />
-  <E value="2" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="602" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.630562E+07" />
-  <B value="0.51436" />
-  <C value="0.600897" />
-  <D value="-1.414428" />
-  <E value="0.688564" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="582.98" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="2320" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="240.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="209750" />
-  <B value="222.65" />
-  <C value="6.403" />
-  <D value="0.014092" />
-  <E value="-0.0000084677" />
-  <Tmin units="K"  value="240" />
-  <Tmax units="K"  value="480" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="121670" />
-  <B value="-659.01" />
-  <C value="13.093" />
-  <D value="0.000016432" />
-  <E value="-4.1637E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12631" />
-  <B value="-98.502" />
-  <C value="-131.43" />
-  <D value="74661" />
-  <E value="-250200" />
-  <Tmin units="K"  value="287.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-29.013" />
-  <B value="1989.1" />
-  <C value="2.6786" />
-  <D value="-0.0000019943" />
-  <E value="2" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="417.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.5516E-07" />
-  <B value="0.71327" />
-  <C value="190.48" />
-  <D value="-6907.5" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.084176" />
-  <B value="-5.3333" />
-  <C value="-1.1753" />
-  <D value="-0.00094427" />
-  <E value="-3.0728E-07" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="553.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="2007.9" />
-  <B value="1.0403" />
-  <C value="2.325E+10" />
-  <D value="-1.556E+11" />
-  <Tmin units="K"  value="417.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.009316" />
-  <B value="8.2096" />
-  <C value="-3.0266" />
-  <D value="0.00040508" />
-  <E value="-0.0000054492" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="582.98" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="36724" />
-  <B value="544.28" />
-  <C value="-0.2504" />
-  <D value="0.000036307" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-11.21128" />
-  <B value="-5950" />
-  <C value="-35.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.277" />
-  <B value="3488.9" />
-  <C value="-59.687" />
-  <Tmin units="K"  value="358.41" />
-  <Tmax units="K"  value="529.73" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4939" />
-  <B value="-0.012328" />
-  <Tmin units="K"  value="240.65" />
-  <Tmax units="K"  value="417.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.434587" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.276587E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="275.8443" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="149.75" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0559243" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.821925" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.471409" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.140625" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2711" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.496" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.411976" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17410" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.140625" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="19"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="123-19-3" />
-<Smiles name="SMILES"  value="CCCC(=O)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1059" />
-<CompoundID name="Name"  value="3-hexanone" />
-<StructureFormula name="Structure"  value="CH3CH2CH2COCH2CH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="582.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3320000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.378" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.256" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="396.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="215" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="217.5" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.22016" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.161" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12343" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.38" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.009E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17930" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.57E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06973" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.89E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.777E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.253E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="409200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.11E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.04843" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.492E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.108" />
-  <B value="-0.0055955" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="87" />
-  <Tmax units="K"  value="217.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.60844" />
-  <B value="0.24303" />
-  <C value="582.83" />
-  <D value="0.26177" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="582.82" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="109.4591" />
-  <B value="-8520.55" />
-  <C value="-13.01531" />
-  <D value="9.019631E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="582.82" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.134266E+07" />
-  <B value="-0.294625" />
-  <C value="1.94188" />
-  <D value="-1.96318" />
-  <E value="0.653572" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="563.59" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-4123.3" />
-  <B value="428.48" />
-  <C value="26.855" />
-  <D value="-0.35338" />
-  <E value="0.0013463" />
-  <Tmin units="K"  value="12.52" />
-  <Tmax units="K"  value="140.13" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="185400" />
-  <B value="578.77" />
-  <C value="3.0261" />
-  <D value="0.02276" />
-  <E value="-0.000015777" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="108160" />
-  <B value="-675.23" />
-  <C value="12.973" />
-  <D value="-0.000036372" />
-  <E value="-1.5789E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21084" />
-  <B value="-230.63" />
-  <C value="-67.335" />
-  <D value="-10006" />
-  <E value="-4827.2" />
-  <Tmin units="K"  value="291.41" />
-  <Tmax units="K"  value="1863.41" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-3.119" />
-  <B value="957.18" />
-  <C value="-1.3764" />
-  <D value="0.0000033013" />
-  <E value="2" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="396.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7969E-07" />
-  <B value="0.70065" />
-  <C value="200.48" />
-  <D value="-7668.6" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0083801" />
-  <B value="80.808" />
-  <C value="-2.2377" />
-  <D value="0.00083175" />
-  <E value="-0.0000033028" />
-  <Tmin units="K"  value="174.85" />
-  <Tmax units="K"  value="533.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.24291" />
-  <B value="0.11759" />
-  <C value="-2306.6" />
-  <D value="-3681900" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.034741" />
-  <B value="-20.897" />
-  <C value="-2.185" />
-  <D value="-0.0017942" />
-  <E value="-3.1071E-07" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="563.59" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="77799" />
-  <B value="112.29" />
-  <C value="0.72627" />
-  <D value="-0.00099092" />
-  <E value="3.9161E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-15.27517" />
-  <B value="-7300" />
-  <C value="-43.8" />
-  <Tmin units="K"  value="269.15" />
-  <Tmax units="K"  value="439.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.18" />
-  <B value="3255.7" />
-  <C value="-59.439" />
-  <Tmin units="K"  value="350" />
-  <Tmax units="K"  value="520" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.2945" />
-  <B value="-0.013514" />
-  <Tmin units="K"  value="217.5" />
-  <Tmax units="K"  value="396.65" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.375336" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.921299E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="281.901" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.256" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="129.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0492727" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.819086" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.38" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.12343" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5967" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.956" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.38" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17930" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.12343" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="20"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="20"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="20"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="19"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="589-38-8" />
-<Smiles name="SMILES"  value="CCC(=O)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1060" />
-<CompoundID name="Name"  value="2-pentanone" />
-<StructureFormula name="Structure"  value="CH3CO(CH2)2CH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="561.1" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3690000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.301" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.238" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="375.39" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="196.29" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="196.29" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.752347" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10733" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.346" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.618E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18290" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0595" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.592E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.384E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="378600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.062E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.9943" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.88E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.184" />
-  <B value="-0.0073973" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="78.52" />
-  <Tmax units="K"  value="196.29" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.8193" />
-  <B value="0.25958" />
-  <C value="561.1" />
-  <D value="0.28941" />
-  <Tmin units="K"  value="196.29" />
-  <Tmax units="K"  value="561.08" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="92.01772" />
-  <B value="-7341.876" />
-  <C value="-10.45756" />
-  <D value="7.61086E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="196.29" />
-  <Tmax units="K"  value="561.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.074187E+07" />
-  <B value="1.097819" />
-  <C value="-1.350154" />
-  <D value="0.926065" />
-  <E value="-0.25017" />
-  <Tmin units="K"  value="196.29" />
-  <Tmax units="K"  value="561.08" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-21075" />
-  <B value="1836.3" />
-  <C value="-11.412" />
-  <D value="0.033399" />
-  <E value="-0.0000064676" />
-  <Tmin units="K"  value="20.74" />
-  <Tmax units="K"  value="180" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119520" />
-  <B value="155.09" />
-  <C value="9.2758" />
-  <D value="0.0038398" />
-  <E value="0.0000015236" />
-  <Tmin units="K"  value="196.29" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="86927" />
-  <B value="-727.52" />
-  <C value="12.986" />
-  <D value="-0.00023161" />
-  <E value="6.926E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25359" />
-  <B value="-304.06" />
-  <C value="-23.005" />
-  <D value="-48839" />
-  <E value="104690" />
-  <Tmin units="K"  value="280.54" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.4812" />
-  <B value="921.84" />
-  <C value="-0.40943" />
-  <D value="6.8984E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="375.46" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.4641E-07" />
-  <B value="0.66525" />
-  <C value="208.96" />
-  <D value="-62.76" />
-  <Tmin units="K"  value="196.29" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.010889" />
-  <B value="-36.658" />
-  <C value="-1.2206" />
-  <D value="-0.0022413" />
-  <E value="-2.5211E-07" />
-  <Tmin units="K"  value="196.29" />
-  <Tmax units="K"  value="513.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.017912" />
-  <B value="0.4825" />
-  <C value="-3887.7" />
-  <D value="-1296300" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.03956" />
-  <B value="2.1919" />
-  <C value="-2.4093" />
-  <D value="-0.0008791" />
-  <E value="-0.0000010614" />
-  <Tmin units="K"  value="196.29" />
-  <Tmax units="K"  value="561.08" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="65152" />
-  <B value="75.254" />
-  <C value="0.6704" />
-  <D value="-0.00090187" />
-  <E value="3.5611E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.291" />
-  <B value="3150.2" />
-  <C value="-52.754" />
-  <Tmin units="K"  value="339.46" />
-  <Tmax units="K"  value="503.48" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.6033" />
-  <B value="-0.010188" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="375.46" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.317875" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.001774E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="208.7519" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.238" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="108.71" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.042749" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.812771" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.346" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10733" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9223" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.416" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.346" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18290" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.10733" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-87-9" />
-<Smiles name="SMILES"  value="CC(=O)CCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1062" />
-<CompoundID name="Name"  value="2-hexanone" />
-<StructureFormula name="Structure"  value="CH3COCH2CH2CH2CH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="587" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3320000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.378" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.254" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="400.7" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="217.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="217.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.44559" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.161" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1241" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.393" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.093E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17600" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.94E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06973" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.89E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.79826E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.30081E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="417856" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.49E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.06376" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.49E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.083" />
-  <B value="-0.0056905" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="86.94" />
-  <Tmax units="K"  value="217.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.58528" />
-  <B value="0.23872" />
-  <C value="587.62" />
-  <D value="0.26191" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="587.61" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.22606" />
-  <B value="-7467.987" />
-  <C value="-8.650385" />
-  <D value="4.736711E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="587.61" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.140665E+07" />
-  <B value="1.724728" />
-  <C value="-1.991428" />
-  <D value="0.65901" />
-  <E value="0.10235" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="568.12" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5223.7" />
-  <B value="839.15" />
-  <C value="4.7323" />
-  <D value="-0.068211" />
-  <E value="0.00021333" />
-  <Tmin units="K"  value="39.76" />
-  <Tmax units="K"  value="217.69" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="171430" />
-  <B value="304.46" />
-  <C value="6.7554" />
-  <D value="0.010928" />
-  <E value="-0.0000044198" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="101950" />
-  <B value="-647" />
-  <C value="12.874" />
-  <D value="0.00017699" />
-  <E value="-1.3836E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24744" />
-  <B value="-284.68" />
-  <C value="-57.772" />
-  <D value="-30750" />
-  <E value="48339" />
-  <Tmin units="K"  value="293.8" />
-  <Tmax units="K"  value="1877.53" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.5407" />
-  <B value="1129.1" />
-  <C value="-0.30673" />
-  <D value="6.1273E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="400.7" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7562E-07" />
-  <B value="0.7037" />
-  <C value="196.23" />
-  <D value="-7085.8" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0056603" />
-  <B value="-27.398" />
-  <C value="-1.2811" />
-  <D value="-0.0017572" />
-  <E value="-3.9285E-07" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="400.85" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.96934" />
-  <B value="0.03859" />
-  <C value="-1883.3" />
-  <D value="-1.1142E+07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0081399" />
-  <B value="117.23" />
-  <C value="-3.9614" />
-  <D value="0.003099" />
-  <E value="-0.0000084515" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="568.12" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="76044" />
-  <B value="72.344" />
-  <C value="0.89264" />
-  <D value="-0.0012053" />
-  <E value="4.7958E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.044" />
-  <B value="3173.6" />
-  <C value="-67.224" />
-  <Tmin units="K"  value="353.76" />
-  <Tmax units="K"  value="525" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3896" />
-  <B value="-0.013212" />
-  <Tmin units="K"  value="217.35" />
-  <Tmax units="K"  value="400.7" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.375336" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.986748E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="276.0277" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="129.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0492648" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.81617" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.393" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1241" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5967" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.956" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.393" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17600" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1241" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="591-78-6" />
-<Smiles name="SMILES"  value="CC(=O)CCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1063" />
-<CompoundID name="Name"  value="2-heptanone" />
-<StructureFormula name="Structure"  value="CH3CO(CH2)4CH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="611.55" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2920000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.421" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="424.05" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="238.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="238.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.54477" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.185" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.140675" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.418982" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.498E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17400" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.71E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07996" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.124E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.00453E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.21796E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="456893" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.84E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1875" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.09952E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.5843" />
-  <B value="-0.0044928" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="95.26" />
-  <Tmax units="K"  value="238.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.42296" />
-  <B value="0.21673" />
-  <C value="611.55" />
-  <D value="0.2517" />
-  <Tmin units="K"  value="238.15" />
-  <Tmax units="K"  value="611.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="104.1321" />
-  <B value="-8934.299" />
-  <C value="-12.02629" />
-  <D value="6.758209E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="238.15" />
-  <Tmax units="K"  value="611.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.522658E+07" />
-  <B value="0.472207" />
-  <C value="0.238382" />
-  <D value="-0.54369" />
-  <E value="0.222217" />
-  <Tmin units="K"  value="238.15" />
-  <Tmax units="K"  value="611.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7238.3" />
-  <B value="975.88" />
-  <C value="-2.0519" />
-  <D value="0.0057069" />
-  <E value="-0.000007064" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="238.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="168580" />
-  <B value="759.37" />
-  <C value="3.3604" />
-  <D value="0.023088" />
-  <E value="-0.000017848" />
-  <Tmin units="K"  value="238.15" />
-  <Tmax units="K"  value="490" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119760" />
-  <B value="-702.71" />
-  <C value="13.229" />
-  <D value="-0.000074262" />
-  <E value="-4.5595E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28693" />
-  <B value="-334.98" />
-  <C value="-80.089" />
-  <D value="-38529" />
-  <E value="52793" />
-  <Tmin units="K"  value="305.7" />
-  <Tmax units="K"  value="1955.78" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.5709" />
-  <B value="1186.6" />
-  <C value="-0.30187" />
-  <D value="0.0000013185" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="424.18" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.5766E-07" />
-  <B value="0.71212" />
-  <C value="201.61" />
-  <D value="-8396.4" />
-  <Tmin units="K"  value="238.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.061916" />
-  <B value="-162.99" />
-  <C value="-0.59984" />
-  <D value="-0.0044095" />
-  <E value="-0.0000013415" />
-  <Tmin units="K"  value="238.15" />
-  <Tmax units="K"  value="424.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="2047.3" />
-  <B value="1.0324" />
-  <C value="2.297E+10" />
-  <D value="7.8096E+08" />
-  <Tmin units="K"  value="424.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.006816" />
-  <B value="130.1" />
-  <C value="-4.0853" />
-  <D value="0.0033192" />
-  <E value="-0.0000084854" />
-  <Tmin units="K"  value="238.15" />
-  <Tmax units="K"  value="611.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="53177" />
-  <B value="423.37" />
-  <C value="-0.032339" />
-  <D value="-0.000077198" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-11.272" />
-  <B value="-5975" />
-  <C value="-35.85" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.063" />
-  <B value="3363.5" />
-  <C value="-71.468" />
-  <Tmin units="K"  value="367" />
-  <Tmax units="K"  value="550" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.9476" />
-  <B value="-0.010818" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="424.18" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.434587" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.34622E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="275.531" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.251" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="149.75" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.64789" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0563666" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.820117" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.418982" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.140675" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2711" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.496" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.3304" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.418982" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17400" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.140675" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-43-0" />
-<Smiles name="SMILES"  value="CC(=O)CCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1064" />
-<CompoundID name="Name"  value="5-methyl-2-hexanone" />
-<StructureFormula name="Structure"  value="CH3CO(CH2)2CH(CH3)2" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="601" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2970000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.421" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="417.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="199.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="199.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0241997" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.185" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.141298" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.434398" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.329E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17740" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07995" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.123E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.04E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.22E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="446000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.1E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.8634" />
-  <B value="-0.0054919" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="79.7" />
-  <Tmax units="K"  value="199.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.59436" />
-  <B value="0.2568" />
-  <C value="601" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="199.25" />
-  <Tmax units="K"  value="601" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="114.12" />
-  <B value="-9180" />
-  <C value="-13.613" />
-  <D value="0.0000087656" />
-  <E value="2" />
-  <Tmin units="K"  value="199.25" />
-  <Tmax units="K"  value="601" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.005371E+07" />
-  <B value="1.17745" />
-  <C value="-0.708374" />
-  <D value="-0.221424" />
-  <E value="0.184955" />
-  <Tmin units="K"  value="199.25" />
-  <Tmax units="K"  value="601" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="195490" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="601" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="125240" />
-  <B value="163.14" />
-  <C value="9.1111" />
-  <D value="0.0074883" />
-  <E value="-0.0000035144" />
-  <Tmin units="K"  value="199.25" />
-  <Tmax units="K"  value="417.95" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="96832" />
-  <B value="-530.6" />
-  <C value="12.878" />
-  <D value="0.00028483" />
-  <E value="-1.1552E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23033" />
-  <B value="-274.58" />
-  <C value="-81.341" />
-  <D value="-10255" />
-  <E value="-37295" />
-  <Tmin units="K"  value="300.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.292" />
-  <B value="1388.7" />
-  <C value="0.61336" />
-  <D value="-0.0000015372" />
-  <E value="2" />
-  <Tmin units="K"  value="199.25" />
-  <Tmax units="K"  value="417.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.5504E-07" />
-  <B value="0.6089" />
-  <C value="292.03" />
-  <D value="-90.104" />
-  <Tmin units="K"  value="417.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.18233" />
-  <B value="17.124" />
-  <C value="-1.0595" />
-  <D value="-0.000040298" />
-  <E value="-9.9547E-07" />
-  <Tmin units="K"  value="180.3" />
-  <Tmax units="K"  value="480.3" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1467.4" />
-  <B value="1.0438" />
-  <C value="1.713E+10" />
-  <D value="-1.5385E+11" />
-  <Tmin units="K"  value="417.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010301" />
-  <B value="67.628" />
-  <C value="-3.3971" />
-  <D value="0.0010921" />
-  <E value="-0.0000054599" />
-  <Tmin units="K"  value="199.25" />
-  <Tmax units="K"  value="601" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="3468.2" />
-  <B value="653.98" />
-  <C value="-0.36734" />
-  <D value="0.000079674" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-12.70264" />
-  <B value="-6550" />
-  <C value="-39.3" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.335" />
-  <B value="3511.9" />
-  <C value="-59.958" />
-  <Tmin units="K"  value="367.25" />
-  <Tmax units="K"  value="537.57" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.5869" />
-  <B value="-0.015027" />
-  <Tmin units="K"  value="199.25" />
-  <Tmax units="K"  value="417.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.434528" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.381495E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="266.9142" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="149.75" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0563476" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.816947" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.434398" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.141298" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2703" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.492" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.434398" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17740" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.141298" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-12-3" />
-<Smiles name="SMILES"  value="CC(=O)CCC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1066" />
-<CompoundID name="Name"  value="3,3-dimethyl-2-butanone" />
-<StructureFormula name="Structure"  value="(CH3)3CCOCH3" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="567" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3470000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.368" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="379.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="221.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="221.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="14.4334" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.159" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.124869" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.327309" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.643E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16920" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06971" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.008E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.905E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.307E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="384400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.133E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.08969" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.4837E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="11.11" />
-  <B value="-0.0062798" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="88.46" />
-  <Tmax units="K"  value="221.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.050005" />
-  <B value="0.070782" />
-  <C value="567" />
-  <D value="0.11676" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="564" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="93.48771" />
-  <B value="-7385.263" />
-  <C value="-10.71444" />
-  <D value="7.878115E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="565" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.0163E+07" />
-  <B value="0.36416" />
-  <C value="-0.10654" />
-  <D value="0.27936" />
-  <E value="-0.16414" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="564" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12892" />
-  <B value="1715.9" />
-  <C value="-11.85" />
-  <D value="0.049444" />
-  <E value="-0.000066905" />
-  <Tmin units="K"  value="11.42" />
-  <Tmax units="K"  value="215.13" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="154180" />
-  <B value="195.77" />
-  <C value="7.7152" />
-  <D value="0.0092036" />
-  <E value="-0.0000029177" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="104260" />
-  <B value="-866.95" />
-  <C value="13.572" />
-  <D value="-0.00063607" />
-  <E value="2.0716E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21862" />
-  <B value="-246.98" />
-  <C value="-51.298" />
-  <D value="-13508" />
-  <E value="12998" />
-  <Tmin units="K"  value="282" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-19.254" />
-  <B value="1373.2" />
-  <C value="1.3346" />
-  <D value="-0.0000032641" />
-  <E value="2" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="379.45" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.8869E-07" />
-  <B value="0.70026" />
-  <C value="190.78" />
-  <D value="-6542.3" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.15399" />
-  <B value="9.8963" />
-  <C value="-1.0886" />
-  <D value="-0.00030883" />
-  <E value="-9.2007E-07" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="450" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1744.4" />
-  <B value="1.0305" />
-  <C value="1.6872E+10" />
-  <D value="-1.3896E+11" />
-  <Tmin units="K"  value="379.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0051063" />
-  <B value="135.01" />
-  <C value="-4.5681" />
-  <D value="0.0055635" />
-  <E value="-0.000012777" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="564" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-1641.8" />
-  <B value="551.82" />
-  <C value="-0.27948" />
-  <D value="0.000048732" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.806" />
-  <B value="2939.8" />
-  <C value="-62.476" />
-  <Tmin units="K"  value="343.57" />
-  <Tmax units="K"  value="509.87" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.2054" />
-  <B value="-0.013548" />
-  <Tmin units="K"  value="221.15" />
-  <Tmax units="K"  value="379.45" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.375222" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.702327E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="294.0371" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="129.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.91793" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0479897" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.810203" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.327309" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.124869" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5952" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.032" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.11079" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.327309" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16920" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.124869" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="19"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="19"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="18"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-97-8" />
-<Smiles name="SMILES"  value="CC(=O)C(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1068" />
-<CompoundID name="Name"  value="Diisobutyl ketone" />
-<StructureFormula name="Structure"  value="(CH3)2CHCH2COCH2CH(CH3)2" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="620" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2530000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.522" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="441.4" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="227" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="227.17" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.249815" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="142.239" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.177418" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.511608" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.614E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16450" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.87E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1004" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.392E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.576E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.13E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="509000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.31E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.6183" />
-  <B value="-0.0037318" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="90.87" />
-  <Tmax units="K"  value="227.17" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.3783" />
-  <B value="0.23231" />
-  <C value="620" />
-  <D value="0.24664" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="594.59" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="122.1783" />
-  <B value="-10064.3" />
-  <C value="-14.70184" />
-  <D value="8.652147E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="615" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.9161E+07" />
-  <B value="-1.6509" />
-  <C value="5.8937" />
-  <D value="-6.6307" />
-  <E value="2.7354" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="615" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="9143.1" />
-  <B value="1265" />
-  <C value="-2.7426" />
-  <D value="0.0078943" />
-  <E value="-0.000010141" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="227.17" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85834" />
-  <B value="-102.6" />
-  <C value="11.702" />
-  <D value="0.0033978" />
-  <E value="-0.0000021321" />
-  <Tmin units="K"  value="307.5" />
-  <Tmax units="K"  value="457.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="118320" />
-  <B value="-505.35" />
-  <C value="13.11" />
-  <D value="0.00028036" />
-  <E value="-1.0389E-07" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.35808" />
-  <B value="-394.11" />
-  <C value="-102.92" />
-  <D value="-39523" />
-  <E value="59420" />
-  <Tmin units="K"  value="307.5" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-74.692" />
-  <B value="4018.6" />
-  <C value="9.6018" />
-  <D value="-0.0000061216" />
-  <E value="2" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="492" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.3916E-07" />
-  <B value="0.72063" />
-  <C value="190.96" />
-  <D value="-7816.5" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.12088" />
-  <B value="22.25" />
-  <C value="-1.2974" />
-  <D value="0.0000088903" />
-  <E value="-0.0000012079" />
-  <Tmin units="K"  value="184.5" />
-  <Tmax units="K"  value="492" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-380230" />
-  <B value="0.02484" />
-  <C value="1.3363E+08" />
-  <D value="-3.9523E+12" />
-  <Tmin units="K"  value="441.41" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0094457" />
-  <B value="58.092" />
-  <C value="-3.5149" />
-  <D value="0.0011642" />
-  <E value="-0.0000051425" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="615" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="7717.8" />
-  <B value="827.5" />
-  <C value="-0.45679" />
-  <D value="0.000095765" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.348" />
-  <B value="3706.7" />
-  <C value="-63.996" />
-  <Tmin units="K"  value="373" />
-  <Tmax units="K"  value="553.76" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.7658" />
-  <B value="-0.010524" />
-  <Tmin units="K"  value="227.17" />
-  <Tmax units="K"  value="492" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.559462" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.817308E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="287.4344" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="190.79" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0689388" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.809782" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.511608" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.177418" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.6183" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.568" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.511608" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16450" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.177418" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  <group id="20"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  <group id="20"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  <group id="18"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  <group id="20"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  <group id="19"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-83-8" />
-<Smiles name="SMILES"  value="CC(C)CC(=O)CC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1069" />
-<CompoundID name="Name"  value="Diisopropyl ketone" />
-<StructureFormula name="Structure"  value="(CH3)2CHCOCH(CH3)2" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="582" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3380000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.416" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.262" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="397.5" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="204" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="204.81" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.820585" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.185" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.142561" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.404427" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.904E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16330" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.11E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07994" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.122E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.16E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.237E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="427000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.118E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1748" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.095E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.8299" />
-  <B value="-0.0059994" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="81.92" />
-  <Tmax units="K"  value="204.81" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.013793" />
-  <B value="0.039842" />
-  <C value="582" />
-  <D value="0.095675" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="576" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="107.12" />
-  <B value="-8385.7" />
-  <C value="-12.681" />
-  <D value="0.0000089823" />
-  <E value="2" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="580" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.205456E+07" />
-  <B value="3.802881" />
-  <C value="-9.83224" />
-  <D value="10.38407" />
-  <E value="-3.829124" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="576" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-4606.3" />
-  <B value="1087.6" />
-  <C value="3.3297" />
-  <D value="-0.060174" />
-  <E value="0.00019999" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="204.81" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="180230" />
-  <B value="-51.129" />
-  <C value="8.6687" />
-  <D value="0.010407" />
-  <E value="-0.0000076786" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="410" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="60064" />
-  <B value="-502.12" />
-  <C value="13.055" />
-  <D value="0.00012498" />
-  <E value="-3.7343E-08" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26243" />
-  <B value="-290.37" />
-  <C value="-61.044" />
-  <D value="-22979" />
-  <E value="26222" />
-  <Tmin units="K"  value="288" />
-  <Tmax units="K"  value="1842" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-5.6405" />
-  <B value="1129.7" />
-  <C value="-1.0122" />
-  <D value="0.0000027665" />
-  <E value="2" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="397.55" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7015E-07" />
-  <B value="0.70572" />
-  <C value="193.2" />
-  <D value="-7481.9" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.11955" />
-  <B value="20.681" />
-  <C value="-1.3034" />
-  <D value="0.0000051067" />
-  <E value="-0.0000013764" />
-  <Tmin units="K"  value="172.8" />
-  <Tmax units="K"  value="460" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-9.5076" />
-  <B value="-0.0072136" />
-  <C value="2380.8" />
-  <D value="-7.251E+07" />
-  <Tmin units="K"  value="397.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0095536" />
-  <B value="69.06" />
-  <C value="-3.5576" />
-  <D value="0.0014554" />
-  <E value="-0.0000061411" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="576" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-36824" />
-  <B value="754.57" />
-  <C value="-0.45548" />
-  <D value="0.00010732" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.12" />
-  <B value="3193.7" />
-  <C value="-64.256" />
-  <Tmin units="K"  value="350" />
-  <Tmax units="K"  value="520" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.6441" />
-  <B value="-0.015251" />
-  <Tmin units="K"  value="204.81" />
-  <Tmax units="K"  value="397.55" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.434469" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.949942E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="305.9995" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.262" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="133.85" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.68836" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0550018" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.724326" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.404427" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.142561" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.0493" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.568" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.95543" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.404427" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16330" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.142561" />
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="18"  value="1" />
-  </Asog>
-<CAS name="CAS number"  value="565-80-0" />
-<Smiles name="SMILES"  value="CC(C)C(=O)C(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1003" />
-<CompoundID name="Name"  value="Propanal" />
-<StructureFormula name="Structure"  value="CH3CH2CHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="493.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4650000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.223" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.239" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="321.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="193.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="170" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.31328" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="58.0791" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0734076" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.330077" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.6241E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19320" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.41E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03904" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.84E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.874E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.244E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="304700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8580000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.6857E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="20.081" />
-  <B value="-0.012081" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="68" />
-  <Tmax units="K"  value="193.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.81482" />
-  <B value="0.2126" />
-  <C value="493.15" />
-  <D value="0.21277" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="492.98" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="110.8631" />
-  <B value="-6856.828" />
-  <C value="-13.8218" />
-  <D value="0.0000173391" />
-  <E value="2" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="504.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.196909E+07" />
-  <B value="1.837694" />
-  <C value="-1.953499" />
-  <D value="-0.000443949" />
-  <E value="0.620394" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="486.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="91450" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="493.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116710" />
-  <B value="75.622" />
-  <C value="5.752" />
-  <D value="0.010877" />
-  <E value="0.0000042986" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="350.28" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-181030" />
-  <B value="9.3832" />
-  <C value="12.233" />
-  <D value="0.00079415" />
-  <E value="-2.4738E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12887" />
-  <B value="-136.56" />
-  <C value="-21.224" />
-  <D value="-4367.6" />
-  <E value="283.41" />
-  <Tmin units="K"  value="286.25" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.033" />
-  <B value="843.41" />
-  <C value="-0.14954" />
-  <D value="3.8846E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="321.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9173E-07" />
-  <B value="0.71905" />
-  <C value="111.91" />
-  <D value="4618.1" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.020248" />
-  <B value="-83.587" />
-  <C value="-0.55331" />
-  <D value="-0.0042681" />
-  <E value="0.0000015626" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="453.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="776.87" />
-  <B value="0.94095" />
-  <C value="4.8356E+09" />
-  <D value="-1.3358E+11" />
-  <Tmin units="K"  value="321.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.037283" />
-  <B value="-60.689" />
-  <C value="-1.5611" />
-  <D value="-0.0040346" />
-  <E value="0.0000015379" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="486.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="34187" />
-  <B value="159.05" />
-  <C value="0.0057665" />
-  <D value="-0.000022543" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.208" />
-  <B value="2686.9" />
-  <C value="-43.655" />
-  <Tmin units="K"  value="296.75" />
-  <Tmax units="K"  value="434" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.7237" />
-  <B value="-0.014511" />
-  <Tmin units="K"  value="170" />
-  <Tmax units="K"  value="321.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.20696" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.303801E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="186.2621" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.239" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="67.67" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0279786" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.804475" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.330077" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0734076" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.5735" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.336" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.255909" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19320" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0734076" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
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-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
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-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="20"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="21"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="20"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="123-38-6" />
-<Smiles name="SMILES"  value="CCC=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1005" />
-<CompoundID name="Name"  value="Butanal" />
-<StructureFormula name="Structure"  value="CH3CH2CH2CHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="521.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4000000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.263" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="347.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="176.75" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="176.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.316993" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.1057" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0904328" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.277417" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.185E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18660" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04927" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.19E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.07E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.1539E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="344900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.109E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1626" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.3035E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.988" />
-  <B value="-0.001057" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="78.15" />
-  <Tmax units="K"  value="176.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0715" />
-  <B value="0.2723" />
-  <C value="521.3" />
-  <D value="0.27225" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="521.29" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="99.51827" />
-  <B value="-7112.269" />
-  <C value="-11.7407" />
-  <D value="9.521179E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="537.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.118197E+07" />
-  <B value="-1.36073" />
-  <C value="5.949252" />
-  <D value="-7.213209" />
-  <E value="2.926745" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="518.23" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="9188.9" />
-  <B value="764.82" />
-  <C value="-3.4299" />
-  <D value="0.018702" />
-  <E value="-0.000037326" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="176.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="146790" />
-  <B value="-6569.4" />
-  <C value="41.653" />
-  <D value="-0.01116" />
-  <E value="-0.000075065" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="328.29" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84791" />
-  <B value="-954.83" />
-  <C value="13.167" />
-  <D value="-0.00050103" />
-  <E value="1.5222E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17145" />
-  <B value="-192.91" />
-  <C value="-29.941" />
-  <D value="-10155" />
-  <E value="12958" />
-  <Tmin units="K"  value="268.6" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-14.207" />
-  <B value="1014.9" />
-  <C value="0.55992" />
-  <D value="-0.0000018129" />
-  <E value="2" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="348.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.4037E-07" />
-  <B value="0.50713" />
-  <C value="464.89" />
-  <D value="-11049" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.054171" />
-  <B value="0.30189" />
-  <C value="-1.9042" />
-  <D value="-0.00054405" />
-  <E value="-0.0000037387" />
-  <Tmin units="K"  value="174.95" />
-  <Tmax units="K"  value="382.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="784.27" />
-  <B value="0.98392" />
-  <C value="6.406E+09" />
-  <D value="-1.3461E+11" />
-  <Tmin units="K"  value="347.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0074594" />
-  <B value="191.36" />
-  <C value="-4.9677" />
-  <D value="0.0077444" />
-  <E value="-0.000016096" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="518.23" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="30948" />
-  <B value="264.36" />
-  <C value="-0.061487" />
-  <D value="-0.0000068962" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.929" />
-  <B value="2779.4" />
-  <C value="-52.488" />
-  <Tmin units="K"  value="312.85" />
-  <Tmax units="K"  value="461.32" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4747" />
-  <B value="-0.014139" />
-  <Tmin units="K"  value="176.75" />
-  <Tmax units="K"  value="348.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.261872" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.31009E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="231.4515" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="88.19" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.4313" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0356078" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.806991" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.277417" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0904328" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.2479" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.876" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.654" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.277417" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18660" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0904328" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="21"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
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-  <group id="21"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
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-  <group id="20"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="21"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="20"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="123-72-8" />
-<Smiles name="SMILES"  value="CCCC=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1007" />
-<CompoundID name="Name"  value="Pentanal" />
-<StructureFormula name="Structure"  value="CH3(CH2)3CHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="554" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3500000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.316" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="376.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="190.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="182" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0522823" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.1323" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.107035" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.390803" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.516E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18440" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.57E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0595" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.2669E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.0711E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="382890" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.5E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.91E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.416" />
-  <B value="-0.0086288" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72.8" />
-  <Tmax units="K"  value="182" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.76227" />
-  <B value="0.25072" />
-  <C value="566.11" />
-  <D value="0.27912" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="566.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="92.63614" />
-  <B value="-7428.499" />
-  <C value="-10.51804" />
-  <D value="7.160109E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="566.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.99504E+07" />
-  <B value="0.991037" />
-  <C value="0.252443" />
-  <D value="-1.761713" />
-  <E value="0.936026" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="545.88" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-17544" />
-  <B value="1682.5" />
-  <C value="-12.848" />
-  <D value="0.067016" />
-  <E value="-0.00013817" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="150" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="156770" />
-  <B value="199.89" />
-  <C value="4.2571" />
-  <D value="0.024547" />
-  <E value="-0.000022679" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="424.57" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="101560" />
-  <B value="-929.74" />
-  <C value="13.391" />
-  <D value="-0.0005525" />
-  <E value="1.6606E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19709" />
-  <B value="-224.42" />
-  <C value="-40.148" />
-  <D value="-19532" />
-  <E value="30096" />
-  <Tmin units="K"  value="283.05" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.884" />
-  <B value="982.07" />
-  <C value="-0.00046989" />
-  <D value="2.2767E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="376.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.2718E-07" />
-  <B value="0.67661" />
-  <C value="192.16" />
-  <D value="-86.47" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.010965" />
-  <B value="-0.28239" />
-  <C value="-1.5585" />
-  <D value="-0.0012856" />
-  <E value="-0.0000013221" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="513.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-3901000" />
-  <B value="-0.05461" />
-  <C value="1.6551E+09" />
-  <D value="-2.4357E+13" />
-  <Tmin units="K"  value="376.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0058735" />
-  <B value="202.77" />
-  <C value="-5.1928" />
-  <D value="0.0083152" />
-  <E value="-0.00001616" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="545.88" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="31485" />
-  <B value="357.59" />
-  <C value="-0.11667" />
-  <D value="0.0000049337" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.106" />
-  <B value="3045.8" />
-  <C value="-58.174" />
-  <Tmin units="K"  value="337.15" />
-  <Tmax units="K"  value="485.24" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3505" />
-  <B value="-0.013773" />
-  <Tmin units="K"  value="182" />
-  <Tmax units="K"  value="376.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.317875" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.283707E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="299.3623" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.264" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="108.71" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.042492" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.814463" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.390803" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.107035" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9223" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.416" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.347159" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18440" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.107035" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="21"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="21"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="21"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="20"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-62-3" />
-<Smiles name="SMILES"  value="CCCCC=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1009" />
-<CompoundID name="Name"  value="Hexanal" />
-<StructureFormula name="Structure"  value="CH3(CH2)4CHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="579" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3110000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.369" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="401.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="217.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="217.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.24729" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.159" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.123708" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.439121" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.924E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18150" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.6E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06973" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.89E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.4732E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-9.882E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="422140" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.89E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.135951" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.52E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.093" />
-  <B value="-0.0058504" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="86.86" />
-  <Tmax units="K"  value="217.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3196" />
-  <B value="0.35571" />
-  <C value="579" />
-  <D value="0.38551" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="571.32" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="209.3738" />
-  <B value="-12430.59" />
-  <C value="-28.59364" />
-  <D value="0.0000281667" />
-  <E value="2" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="591" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.570251E+07" />
-  <B value="-0.000821879" />
-  <C value="0.788181" />
-  <D value="-0.0470431" />
-  <E value="-0.460389" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="571.32" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16038" />
-  <B value="1391.2" />
-  <C value="-4.6944" />
-  <D value="0.002827" />
-  <E value="0.000027528" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="214.94" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="175480" />
-  <B value="98.975" />
-  <C value="6.7267" />
-  <D value="0.013876" />
-  <E value="-0.0000081365" />
-  <Tmin units="K"  value="214.94" />
-  <Tmax units="K"  value="443.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115820" />
-  <B value="-867.39" />
-  <C value="13.422" />
-  <D value="-0.00036658" />
-  <E value="7.4569E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23651" />
-  <B value="-272.87" />
-  <C value="-57.26" />
-  <D value="-28587" />
-  <E value="42501" />
-  <Tmin units="K"  value="295.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.85" />
-  <B value="1055.4" />
-  <C value="0.17945" />
-  <D value="-3.4838E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="401.45" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.6626E-07" />
-  <B value="0.71206" />
-  <C value="185.2" />
-  <D value="-6483.1" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0039289" />
-  <B value="-19.957" />
-  <C value="-1.3588" />
-  <D value="-0.0017925" />
-  <E value="-6.0508E-07" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="533.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-5919900" />
-  <B value="-0.017833" />
-  <C value="2.2842E+09" />
-  <D value="-4.7916E+13" />
-  <Tmin units="K"  value="401.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0098512" />
-  <B value="146.83" />
-  <C value="-4.2826" />
-  <D value="0.0042701" />
-  <E value="-0.000009235" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="571.32" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29579" />
-  <B value="452.38" />
-  <C value="-0.16247" />
-  <D value="0.0000084363" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.836" />
-  <B value="3074" />
-  <C value="-71.172" />
-  <Tmin units="K"  value="352.15" />
-  <Tmax units="K"  value="512.29" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.7935" />
-  <B value="-0.011421" />
-  <Tmin units="K"  value="217.15" />
-  <Tmax units="K"  value="401.45" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.375336" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.739367E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="296.1391" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="129.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0492739" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.821257" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.439121" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.123708" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5967" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.956" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.387184" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18150" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.123708" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="21"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="21"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="20"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="21"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="20"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="66-25-1" />
-<Smiles name="SMILES"  value="CCCCCC=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1008" />
-<CompoundID name="Name"  value="Heptanal" />
-<StructureFormula name="Structure"  value="CH3(CH2)5CHO" />
-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="603" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.421" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="425.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="230.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="229.8" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.44979" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="114.185" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.140287" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.488466" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.314E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17780" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.6E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07996" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.124E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.6401E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-8.653E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="461380" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.359E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.136E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.6462" />
-  <B value="-0.004691" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="91.92" />
-  <Tmax units="K"  value="230.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53646" />
-  <B value="0.24452" />
-  <C value="616.81" />
-  <D value="0.26981" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="616.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="108.36" />
-  <B value="-9179.6" />
-  <C value="-12.655" />
-  <D value="0.0000073363" />
-  <E value="2" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="617" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.244116E+07" />
-  <B value="0.224744" />
-  <C value="0.949788" />
-  <D value="-1.500319" />
-  <E value="0.675167" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="596.43" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="11626" />
-  <B value="464.04" />
-  <C value="9.9687" />
-  <D value="-0.0854" />
-  <E value="0.0002123" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="210" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="200220" />
-  <B value="128.23" />
-  <C value="7.474" />
-  <D value="0.012008" />
-  <E value="-0.0000080423" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="462.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="131660" />
-  <B value="-858.87" />
-  <C value="13.596" />
-  <D value="-0.00041213" />
-  <E value="8.8955E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27254" />
-  <B value="-318.17" />
-  <C value="-77.952" />
-  <D value="-41429" />
-  <E value="58799" />
-  <Tmin units="K"  value="308.4" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="8.4077" />
-  <B value="475.87" />
-  <C value="-3.0758" />
-  <D value="0.0000053404" />
-  <E value="2" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="425.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4563E-07" />
-  <B value="0.72362" />
-  <C value="184.89" />
-  <D value="-7288.6" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.02754" />
-  <B value="-55.074" />
-  <C value="-1.243" />
-  <D value="-0.0022084" />
-  <E value="-0.0000010637" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="553.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1569.2" />
-  <B value="1.0102" />
-  <C value="1.4874E+10" />
-  <D value="2.7536E+11" />
-  <Tmin units="K"  value="425.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.073851" />
-  <B value="-32.28" />
-  <C value="-1.708" />
-  <D value="-0.0018301" />
-  <E value="6.9211E-07" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="596.43" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="28302" />
-  <B value="549.96" />
-  <C value="-0.22024" />
-  <D value="0.000020347" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-7.855" />
-  <B value="-4535" />
-  <C value="-27.21" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.509" />
-  <B value="3688.3" />
-  <C value="-56.603" />
-  <Tmin units="K"  value="364.15" />
-  <Tmax units="K"  value="535.33" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.691" />
-  <B value="-0.010949" />
-  <Tmin units="K"  value="229.8" />
-  <Tmax units="K"  value="425.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.434587" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.82117E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="339.3681" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="149.75" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0559389" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.822566" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.488466" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.140287" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2711" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.496" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.42794" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17780" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.140287" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="21"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="21"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="20"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="21"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="20"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-71-7" />
-<Smiles name="SMILES"  value="CCCCCCC=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1403" />
-<CompoundID name="Name"  value="Diisopropyl ether" />
-<StructureFormula name="Structure"  value="CH3CH(CH3)OCH(CH3)CH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="500.05" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2880000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.386" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="341.45" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="187.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="187.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.8582" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.175" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.141775" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.338683" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.906E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14450" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.77E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0719399" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.022E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.18988E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.248E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="382000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.103E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91199" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.70234E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.235" />
-  <B value="-0.0060556" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="75.06" />
-  <Tmax units="K"  value="187.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.72527" />
-  <B value="0.27594" />
-  <C value="500.05" />
-  <D value="0.29413" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="483.61" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="109.5333" />
-  <B value="-7120.297" />
-  <C value="-13.51365" />
-  <D value="0.0000143778" />
-  <E value="2" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="500.05" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.8041E+07" />
-  <B value="2.3385" />
-  <C value="-5.2086" />
-  <D value="5.0367" />
-  <E value="-1.6926" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="483.61" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12905" />
-  <B value="1581.3" />
-  <C value="-8.8913" />
-  <D value="0.036008" />
-  <E value="-0.000053243" />
-  <Tmin units="K"  value="10" />
-  <Tmax units="K"  value="187.77" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="161880" />
-  <B value="-2.8879" />
-  <C value="7.7638" />
-  <D value="0.014551" />
-  <E value="-0.000013251" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="341.45" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="69454" />
-  <B value="-410.18" />
-  <C value="12.642" />
-  <D value="0.00044085" />
-  <E value="-1.3595E-07" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20132" />
-  <B value="-190.66" />
-  <C value="-42.523" />
-  <D value="5178" />
-  <E value="-15257" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.064" />
-  <B value="932.47" />
-  <C value="-0.38815" />
-  <D value="0.0000010323" />
-  <E value="2" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="341.45" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.0782E-07" />
-  <B value="0.58517" />
-  <C value="121.4" />
-  <D value="19303" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.067752" />
-  <B value="-462.02" />
-  <C value="2.3997" />
-  <D value="-0.014453" />
-  <E value="0.0000029856" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="423.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00010149" />
-  <B value="1.0246" />
-  <C value="180.97" />
-  <D value="93179" />
-  <Tmin units="K"  value="328.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0092656" />
-  <B value="51.562" />
-  <C value="-3.4763" />
-  <D value="0.0012682" />
-  <E value="-0.000007923" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="483.61" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="7177.4" />
-  <B value="598.8" />
-  <C value="-0.32962" />
-  <D value="0.000071947" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.907471" />
-  <B value="-1950" />
-  <C value="-11.7" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.585" />
-  <B value="3179.8" />
-  <C value="-25.516" />
-  <Tmin units="K"  value="300.26" />
-  <Tmax units="K"  value="450" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4668" />
-  <B value="-0.015287" />
-  <Tmin units="K"  value="187.65" />
-  <Tmax units="K"  value="341.45" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.387973" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.626648E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="281.4279" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="133.85" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.82949" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0513038" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.730337" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.338683" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.141775" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7421" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.088" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="1.025312" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="-0.033494" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-2.1989" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.338683" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14450" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.141775" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="3"  value="1" />
-  <group id="29"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="3"  value="1" />
-  <group id="27"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="1" />
-  <group id="26"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-20-3" />
-<Smiles name="SMILES"  value="CC(C)OC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1404" />
-<CompoundID name="Name"  value="Di-n-butyl ether" />
-<StructureFormula name="Structure"  value="(C4H9)2O" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="580.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2380000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.511" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.247" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="415.35" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="177.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="175.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000714135" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="130.228" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.17041" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.447646" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.797E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15830" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.9E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09192" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.288E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.339E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-8.827E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="481200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.63E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.33492" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.94716E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.3732" />
-  <B value="-0.005226" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="70.12" />
-  <Tmax units="K"  value="177.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.22926" />
-  <B value="0.17412" />
-  <C value="584.11" />
-  <D value="0.21764" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="584.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="95.7043" />
-  <B value="-8294.241" />
-  <C value="-10.81822" />
-  <D value="6.127187E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="584.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.4859E+07" />
-  <B value="0.77992" />
-  <C value="-0.72383" />
-  <D value="0.38094" />
-  <E value="-0.025388" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="562.58" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="236620" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="580.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="198760" />
-  <B value="65.432" />
-  <C value="9.8123" />
-  <D value="0.0039694" />
-  <E value="8.4178E-07" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="152990" />
-  <B value="-805.71" />
-  <C value="13.605" />
-  <D value="-0.00024656" />
-  <E value="5.3497E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34998" />
-  <B value="-389.07" />
-  <C value="-72.95" />
-  <D value="-21323" />
-  <E value="26825" />
-  <Tmin units="K"  value="290.5" />
-  <Tmax units="K"  value="1856.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="20.743" />
-  <B value="-83.003" />
-  <C value="-4.9404" />
-  <D value="0.000004096" />
-  <E value="2" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="414.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000002113" />
-  <B value="0.66224" />
-  <C value="141.56" />
-  <D value="6932" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.067128" />
-  <B value="2.4703" />
-  <C value="-1.3291" />
-  <D value="-0.0010011" />
-  <E value="-2.5742E-07" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="523.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0036064" />
-  <B value="0.57918" />
-  <C value="1401.9" />
-  <D value="287150" />
-  <Tmin units="K"  value="280.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01167" />
-  <B value="44.906" />
-  <C value="-3.3567" />
-  <D value="0.00097712" />
-  <E value="-0.0000052216" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="562.58" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="34113" />
-  <B value="646.38" />
-  <C value="-0.25439" />
-  <D value="0.000025866" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.921" />
-  <B value="3199" />
-  <C value="-73.256" />
-  <Tmin units="K"  value="353.35" />
-  <Tmax units="K"  value="522.04" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3266" />
-  <B value="-0.013047" />
-  <Tmin units="K"  value="175.3" />
-  <Tmax units="K"  value="414.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.506519" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.988813E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="246.6962" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.247" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="174.89" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.87345" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0666012" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.77463" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.447646" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.17041" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0925" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.176" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.06222" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.447646" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15830" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.17041" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="6" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="142-96-1" />
-<Smiles name="SMILES"  value="CCCCOCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1406" />
-<CompoundID name="Name"  value="Di-sec-butyl ether" />
-<StructureFormula name="Structure"  value="C2H5(CH3)CHOCH(CH3)C2H5" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="562" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2556000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.487" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="394.2" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="173.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="173.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0027863" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="130.228" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.171577" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.329" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.373E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14950" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0924" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.292E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.609E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.157E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="501000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.9233E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.4542" />
-  <B value="-0.0061032" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="69.26" />
-  <Tmax units="K"  value="173.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.038135" />
-  <B value="0.072155" />
-  <C value="562" />
-  <D value="0.11862" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="559" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="102.5292" />
-  <B value="-8146.755" />
-  <C value="-11.97808" />
-  <D value="8.058954E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="560" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.5999E+07" />
-  <B value="0.34375" />
-  <C value="0.18962" />
-  <D value="-0.14755" />
-  <E value="-0.0040987" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="559" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="236620" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="562" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="102180" />
-  <B value="-37.551" />
-  <C value="10.606" />
-  <D value="0.0064949" />
-  <E value="-0.0000048029" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="420" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94528" />
-  <B value="-497.39" />
-  <C value="13.241" />
-  <D value="0.000057744" />
-  <E value="-1.2606E-09" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.31867" />
-  <B value="-341.87" />
-  <C value="-60.467" />
-  <D value="-9470.7" />
-  <E value="6002.4" />
-  <Tmin units="K"  value="281" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.318" />
-  <B value="1230.4" />
-  <C value="-0.20919" />
-  <D value="4.9411E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="394.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.1864E-07" />
-  <B value="0.74861" />
-  <C value="137.78" />
-  <D value="-4500.8" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.027499" />
-  <B value="27.604" />
-  <C value="-2.2754" />
-  <D value="0.00032105" />
-  <E value="-0.0000044406" />
-  <Tmin units="K"  value="167.7" />
-  <Tmax units="K"  value="453.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016749" />
-  <B value="0.96101" />
-  <C value="656.84" />
-  <D value="-691.7" />
-  <Tmin units="K"  value="394.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010066" />
-  <B value="43.992" />
-  <C value="-3.3461" />
-  <D value="0.00062354" />
-  <E value="-0.0000053912" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="559" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-28426" />
-  <B value="952.53" />
-  <C value="-0.64748" />
-  <D value="0.00017987" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.954" />
-  <B value="3141.6" />
-  <C value="-61.002" />
-  <Tmin units="K"  value="350" />
-  <Tmax units="K"  value="500" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.7138" />
-  <B value="-0.01814" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="394.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.509471" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.096626E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="324.9059" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="174.89" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0642045" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.769756" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.329" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.171577" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.0909" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.168" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.329" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14950" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.171577" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="29"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="27"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="26"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="6863-58-7" />
-<Smiles name="SMILES"  value="CCC(C)OC(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1407" />
-<CompoundID name="Name"  value="Methyl ethyl ether" />
-<StructureFormula name="Structure"  value="CH3CH2OCH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="437.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.221" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="280.5" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="160" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="160" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.85121" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="60.096" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.08585" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.236" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.594E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15370" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.1E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04127" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.19E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.164E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.177E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="308810" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7980000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.81612" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.9314E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.4" />
-  <B value="-5.0307E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1195" />
-  <B value="0.26367" />
-  <C value="437.86" />
-  <D value="0.25231" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="437.85" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="63.84" />
-  <B value="-4659.2" />
-  <C value="-6.4137" />
-  <D value="0.0000057727" />
-  <E value="2" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="437.85" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.3679E+08" />
-  <B value="9.4948" />
-  <C value="-25.655" />
-  <D value="28.424" />
-  <E value="-11.603" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="423.18" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="106570" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="437.8" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="109050" />
-  <B value="-31.645" />
-  <C value="7.7783" />
-  <D value="0.0084684" />
-  <E value="0.0000041202" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="291.87" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="60571" />
-  <B value="-557.18" />
-  <C value="12.079" />
-  <D value="0.00048084" />
-  <E value="-1.7581E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.11781" />
-  <B value="-82.964" />
-  <C value="-11.583" />
-  <D value="116.91" />
-  <E value="-410.44" />
-  <Tmin units="K"  value="218.9" />
-  <Tmax units="K"  value="1751.2" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.138" />
-  <B value="628.05" />
-  <C value="0.042345" />
-  <D value="-2.0281E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="300" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.9661E-07" />
-  <B value="0.6716" />
-  <C value="174.02" />
-  <D value="-2778.1" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.029003" />
-  <B value="34.124" />
-  <C value="-1.9356" />
-  <D value="0.0010295" />
-  <E value="-0.0000079939" />
-  <Tmin units="K"  value="123.15" />
-  <Tmax units="K"  value="393.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00021058" />
-  <B value="0.94472" />
-  <C value="515.36" />
-  <D value="8108.3" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010165" />
-  <B value="66.837" />
-  <C value="-3.7084" />
-  <D value="0.0031429" />
-  <E value="-0.000012741" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="423.18" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="33324" />
-  <B value="178.7" />
-  <C value="0.14991" />
-  <D value="-0.00027712" />
-  <E value="1.1067E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.812" />
-  <B value="2153.4" />
-  <C value="-48.579" />
-  <Tmin units="K"  value="265.35" />
-  <Tmax units="K"  value="393.94" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-5.3262" />
-  <B value="-0.012074" />
-  <Tmin units="K"  value="160" />
-  <Tmax units="K"  value="300" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.218857" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.502528E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="246.3936" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="72.28999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.44235" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0306623" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.705396" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.236" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.08585" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.7205" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.476" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.534" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.236" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15370" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.08585" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="25"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="24"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="540-67-0" />
-<Smiles name="SMILES"  value="COCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1408" />
-<CompoundID name="Name"  value="Methyl n-propyl ether" />
-<StructureFormula name="Structure"  value="CH3OCH2CH2CH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="472" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3801000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.274" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.265" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="312.29" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="123.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="133.97" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00289599" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.1216" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1032" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.276999" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.12326E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.14E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0515" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.379E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.108E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="352000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7670000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.89511" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.517E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="15.416" />
-  <B value="-0.014383" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="53.59" />
-  <Tmax units="K"  value="133.97" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1427" />
-  <B value="0.28927" />
-  <C value="472" />
-  <D value="0.3185" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="458.24" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.81269" />
-  <B value="-4968.626" />
-  <C value="-5.703041" />
-  <D value="3.962175E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="476.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.425282E+07" />
-  <B value="0.586164" />
-  <C value="-0.378014" />
-  <D value="0.582618" />
-  <E value="-0.440041" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="458.24" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-9510.5" />
-  <B value="1023.7" />
-  <C value="0.15873" />
-  <D value="-0.038206" />
-  <E value="0.00015489" />
-  <Tmin units="K"  value="15.99" />
-  <Tmax units="K"  value="127.29" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="136920" />
-  <B value="43.97" />
-  <C value="5.0864" />
-  <D value="0.024992" />
-  <E value="-0.000027384" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="312.2" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="93668" />
-  <B value="-926.82" />
-  <C value="13.189" />
-  <D value="-0.0004818" />
-  <E value="0.000000144" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17308" />
-  <B value="-175.69" />
-  <C value="-17.924" />
-  <D value="-525.83" />
-  <E value="-815.37" />
-  <Tmin units="K"  value="238.12" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.301" />
-  <B value="802.09" />
-  <C value="0.054938" />
-  <D value="-4.1844E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="312.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.0896E-07" />
-  <B value="0.78578" />
-  <C value="98.829" />
-  <D value="-6562.3" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0079788" />
-  <B value="3.9001" />
-  <C value="-1.4224" />
-  <D value="-0.0010693" />
-  <E value="-0.0000025315" />
-  <Tmin units="K"  value="123.15" />
-  <Tmax units="K"  value="423.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.010718" />
-  <B value="0.485" />
-  <C value="2083.9" />
-  <D value="283110" />
-  <Tmin units="K"  value="312.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012651" />
-  <B value="20.99" />
-  <C value="-2.9043" />
-  <D value="-0.00049586" />
-  <E value="-0.0000059519" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="458.24" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="29023" />
-  <B value="312.2" />
-  <C value="-0.087621" />
-  <D value="-0.0000082831" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.939" />
-  <B value="2550.9" />
-  <C value="-41.081" />
-  <Tmin units="K"  value="284.01" />
-  <Tmax units="K"  value="422.21" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3078" />
-  <B value="-0.017264" />
-  <Tmin units="K"  value="133.97" />
-  <Tmax units="K"  value="312.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.273974" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.964859E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="258.5475" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.265" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="92.81" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.72462" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0372251" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.733812" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.276999" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1032" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.3949" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.016" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-1.6721" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.276999" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15730" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1032" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="25"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="27"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="25"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="24"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="557-17-5" />
-<Smiles name="SMILES"  value="COCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1409" />
-<CompoundID name="Name"  value="Isopropyl butyl ether" />
-<StructureFormula name="Structure"  value="C4H9OCH(CH3)2" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="549" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2740000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.435" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="378.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="180" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="180" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0337504" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="116.201" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.155791" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.403229" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.475E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15260" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.24E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08218" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.158E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.269E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.071E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="450200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.22E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.324E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.3504" />
-  <B value="-0.0064933" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72" />
-  <Tmax units="K"  value="180" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.62258" />
-  <B value="0.27082" />
-  <C value="549" />
-  <D value="0.30735" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="549" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="85.99635" />
-  <B value="-7315.405" />
-  <C value="-9.426402" />
-  <D value="5.236755E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="549" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.2177E+07" />
-  <B value="0.38027" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="549" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="210610" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="549" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="200760" />
-  <B value="-0.77126" />
-  <C value="8.116" />
-  <D value="0.0093067" />
-  <E value="-0.00000176" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="411.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="76973" />
-  <B value="-443.41" />
-  <C value="12.925" />
-  <D value="0.00032949" />
-  <E value="-1.1644E-07" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28425" />
-  <B value="-304.18" />
-  <C value="-51.293" />
-  <D value="-5929.1" />
-  <E value="1171.2" />
-  <Tmin units="K"  value="274.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.496" />
-  <B value="1171.6" />
-  <C value="0.0066892" />
-  <D value="-1.6659E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="382.3" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000000176" />
-  <B value="0.70157" />
-  <C value="181.76" />
-  <D value="-5946.4" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.10095" />
-  <B value="17.355" />
-  <C value="-1.4146" />
-  <D value="-0.000082157" />
-  <E value="-0.0000014735" />
-  <Tmin units="K"  value="164.7" />
-  <Tmax units="K"  value="439.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016013" />
-  <B value="0.96562" />
-  <C value="574.46" />
-  <D value="18419" />
-  <Tmin units="K"  value="382.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0073125" />
-  <B value="68.441" />
-  <C value="-3.6554" />
-  <D value="0.0016795" />
-  <E value="-0.0000077692" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="549" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-16950" />
-  <B value="793.92" />
-  <C value="-0.50277" />
-  <D value="0.00012845" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.893" />
-  <B value="2954" />
-  <C value="-66.624" />
-  <Tmin units="K"  value="335.37" />
-  <Tmax units="K"  value="490.74" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4944" />
-  <B value="-0.016265" />
-  <Tmin units="K"  value="180" />
-  <Tmax units="K"  value="382.3" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.447711" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.086625E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="284.7026" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="154.37" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0580587" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.755446" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.403229" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.155791" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.4173" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.632" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.403229" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15260" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.155791" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="27"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="29"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="27"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="3" />
-  <group id="26"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="1860-27-1" />
-<Smiles name="SMILES"  value="CCCCOC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1410" />
-<CompoundID name="Name"  value="Methyl isobutyl ether" />
-<StructureFormula name="Structure"  value="CH3OCH2CH(CH3)CH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="497" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3410000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.329" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="331.7" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.1482" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.121242" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.307786" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.608E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15100" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.7E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06172" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.88E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.66E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.07E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="381000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.122E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.4" />
-  <B value="-2.3039E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.83514" />
-  <B value="0.27544" />
-  <C value="497" />
-  <D value="0.27525" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="497" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="67.83965" />
-  <B value="-5584.772" />
-  <C value="-6.90156" />
-  <D value="5.177794E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="497" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.281E+07" />
-  <B value="0.34436" />
-  <C value="0.050812" />
-  <D value="-0.029168" />
-  <E value="0.014527" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="497" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="158590" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="497" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="156890" />
-  <B value="481.87" />
-  <C value="3.1798" />
-  <D value="0.023292" />
-  <E value="-0.000015219" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="370" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84480" />
-  <B value="-573.48" />
-  <C value="12.645" />
-  <D value="0.00036001" />
-  <E value="-1.6026E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20282" />
-  <B value="-209.23" />
-  <C value="-25.747" />
-  <D value="-401.68" />
-  <E value="-2768.2" />
-  <Tmin units="K"  value="248.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-6.5049" />
-  <B value="776.05" />
-  <C value="-0.79051" />
-  <D value="0.0000029469" />
-  <E value="2" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="331.7" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.7344E-07" />
-  <B value="0.65828" />
-  <C value="203.42" />
-  <D value="-5560.1" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1664" />
-  <B value="6.1773" />
-  <C value="-1.0308" />
-  <D value="-0.0004394" />
-  <E value="-9.9213E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="390" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016088" />
-  <B value="0.97231" />
-  <C value="471.48" />
-  <D value="30281" />
-  <Tmin units="K"  value="331.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010965" />
-  <B value="36.367" />
-  <C value="-3.3144" />
-  <D value="0.00071793" />
-  <E value="-0.0000066621" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="497" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="9865.2" />
-  <B value="481.23" />
-  <C value="-0.22823" />
-  <D value="0.000035281" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.621" />
-  <B value="3058" />
-  <C value="-30.223" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="497" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.2832" />
-  <B value="-0.016308" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="331.7" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.330209" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.144609E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="299.032" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="113.33" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0437951" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.738166" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.307786" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.121242" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.0685" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.552" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.307786" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15100" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.121242" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="25"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="24"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="625-44-5" />
-<Smiles name="SMILES"  value="COCC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1411" />
-<CompoundID name="Name"  value="Methyl isopropyl ether" />
-<StructureFormula name="Structure"  value="CH3OCH(CH3)2" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="464.48" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3762000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.276" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="303.92" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="127.93" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="127.93" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00332352" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="74.1216" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1046" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.26555" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.125E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15160" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.16E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05149" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.53E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.52E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.209E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="338300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5850000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.88228" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.5311E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="15.275" />
-  <B value="-0.014925" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="51.17" />
-  <Tmax units="K"  value="127.93" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.82094" />
-  <B value="0.24798" />
-  <C value="464.48" />
-  <D value="0.26184" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="446.77" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="61.57822" />
-  <B value="-4874.158" />
-  <C value="-6.034163" />
-  <D value="5.097159E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="464.48" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.2811E+07" />
-  <B value="1.2196" />
-  <C value="-2.6572" />
-  <D value="3.1706" />
-  <E value="-1.3477" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="446.77" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14239" />
-  <B value="1522.1" />
-  <C value="-10.372" />
-  <D value="0.040411" />
-  <E value="-0.000026641" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="127.93" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="123760" />
-  <B value="190.2" />
-  <C value="5.9878" />
-  <D value="0.016259" />
-  <E value="-0.000010176" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="342.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84263" />
-  <B value="-798.1" />
-  <C value="12.945" />
-  <D value="-0.00018216" />
-  <E value="3.6316E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17001" />
-  <B value="-169.64" />
-  <C value="-16.164" />
-  <D value="-375.05" />
-  <E value="-728.91" />
-  <Tmin units="K"  value="232.24" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.884" />
-  <B value="730.8" />
-  <C value="-0.038881" />
-  <D value="2.6764E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="303.92" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9275E-07" />
-  <B value="0.70897" />
-  <C value="109.56" />
-  <D value="-107.54" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.21567" />
-  <B value="5.2547" />
-  <C value="-0.85956" />
-  <D value="-0.00045627" />
-  <E value="-9.7493E-07" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="370" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1.3675" />
-  <B value="-0.14071" />
-  <C value="1446.2" />
-  <D value="3030500" />
-  <Tmin units="K"  value="303.92" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012657" />
-  <B value="18.015" />
-  <C value="-2.9804" />
-  <D value="-0.00052011" />
-  <E value="-0.0000057032" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="446.77" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="23278" />
-  <B value="335.74" />
-  <C value="-0.1205" />
-  <D value="0.0000088148" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.025" />
-  <B value="2524.7" />
-  <C value="-38.36" />
-  <Tmin units="K"  value="287.35" />
-  <Tmax units="K"  value="411.34" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.5841" />
-  <B value="-0.01794" />
-  <Tmin units="K"  value="127.93" />
-  <Tmax units="K"  value="303.92" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.273919" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.872801E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="268.5273" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="92.81" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0366241" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.724137" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.26555" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1046" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.3941" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.012" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.26555" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15160" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1046" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="27"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="25"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="24"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="598-53-8" />
-<Smiles name="SMILES"  value="COC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1428" />
-<CompoundID name="Name"  value="Tert-butyl ethyl ether" />
-<StructureFormula name="Structure"  value="(CH3)3COCH2CH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="512" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3149000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.382" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="345.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="176.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="179.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.880264" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.175" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.138991" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.295672" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.825E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14800" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07194" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.043E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.165E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.217E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="397500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9530000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.96475" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.684E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="10.626" />
-  <B value="-0.0074141" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="71.66" />
-  <Tmax units="K"  value="179.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.74373" />
-  <B value="0.27619" />
-  <C value="512" />
-  <D value="0.30602" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="496.38" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="59.92213" />
-  <B value="-5564.171" />
-  <C value="-5.601322" />
-  <D value="3.389291E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="514" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.5825E+07" />
-  <B value="0.349787" />
-  <C value="0.137025" />
-  <D value="-0.301886" />
-  <E value="0.219717" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="496.38" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="184600" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="512" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="135520" />
-  <B value="9.8807" />
-  <C value="8.6914" />
-  <D value="0.01077" />
-  <E value="-0.0000076034" />
-  <Tmin units="K"  value="257" />
-  <Tmax units="K"  value="377" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78915" />
-  <B value="-487.03" />
-  <C value="12.843" />
-  <D value="0.00025385" />
-  <E value="-8.879E-08" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23521" />
-  <B value="-254.66" />
-  <C value="-30.796" />
-  <D value="-1091.5" />
-  <E value="-2460.3" />
-  <Tmin units="K"  value="257" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.011" />
-  <B value="1089.8" />
-  <C value="0.081011" />
-  <D value="-2.1688E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="345.95" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9715E-07" />
-  <B value="0.697" />
-  <C value="171.3" />
-  <D value="-4885.5" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1316" />
-  <B value="11.716" />
-  <C value="-1.2478" />
-  <D value="-0.00024672" />
-  <E value="-0.0000012519" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="404.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000058788" />
-  <B value="1.0907" />
-  <C value="235.7" />
-  <D value="33150" />
-  <Tmin units="K"  value="345.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0097534" />
-  <B value="59.145" />
-  <C value="-3.4319" />
-  <D value="0.0013727" />
-  <E value="-0.0000078881" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="496.38" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-8811.5" />
-  <B value="674.5" />
-  <C value="-0.41693" />
-  <D value="0.00010398" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.712" />
-  <B value="2624.2" />
-  <C value="-60.279" />
-  <Tmin units="K"  value="310" />
-  <Tmax units="K"  value="453.65" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8175" />
-  <B value="-0.016919" />
-  <Tmin units="K"  value="179.15" />
-  <Tmax units="K"  value="345.95" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.387974" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.458278E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="308.0571" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="133.85" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0518272" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.747248" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.295672" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.138991" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7422" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.172" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.886894" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.04628" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.295672" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14800" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.138991" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="4"  value="1" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="637-92-3" />
-<Smiles name="SMILES"  value="CCOC(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1430" />
-<CompoundID name="Name"  value="Ethyl tert-pentyl ether" />
-<StructureFormula name="Structure"  value="C2H5C(CH3)2OC2H5" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="544" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2740000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.435" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="374.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="190" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="190" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.729523" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="116.201" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.152635" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.338192" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.071E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14970" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.14E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08217" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.178E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.324E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.094E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="439200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.2E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.32E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.4008" />
-  <B value="-0.0061847" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="76" />
-  <Tmax units="K"  value="190" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.65888" />
-  <B value="0.27797" />
-  <C value="544" />
-  <D value="0.29227" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="527.26" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="47.12433" />
-  <B value="-5006.625" />
-  <C value="-3.892102" />
-  <D value="0.0000058438" />
-  <E value="2" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="546" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.448049E+07" />
-  <B value="2.475757" />
-  <C value="-5.830862" />
-  <D value="5.958177" />
-  <E value="-2.135539" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="527.26" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="210610" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="544" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-79604" />
-  <B value="-398.25" />
-  <C value="15.392" />
-  <D value="-0.0067505" />
-  <E value="0.0000071337" />
-  <Tmin units="K"  value="272" />
-  <Tmax units="K"  value="520" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="119820" />
-  <B value="-647.93" />
-  <C value="13.251" />
-  <D value="-0.00004893" />
-  <E value="2.8951E-09" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26473" />
-  <B value="-291.19" />
-  <C value="-50.413" />
-  <D value="-1429" />
-  <E value="-7779.1" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.435" />
-  <B value="1134.3" />
-  <C value="-0.0102" />
-  <D value="2.552E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="374.57" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2029E-07" />
-  <B value="0.7552" />
-  <C value="122.76" />
-  <D value="-2833.2" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.13805" />
-  <B value="13.252" />
-  <C value="-1.2618" />
-  <D value="-0.00018101" />
-  <E value="-0.0000010967" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="435.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013295" />
-  <B value="0.98504" />
-  <C value="431.52" />
-  <D value="34060" />
-  <Tmin units="K"  value="374.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012045" />
-  <B value="51.27" />
-  <C value="-3.2868" />
-  <D value="0.00081088" />
-  <E value="-0.0000057636" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="527.26" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="2299.7" />
-  <B value="719.3" />
-  <C value="-0.404" />
-  <D value="0.000086601" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.218" />
-  <B value="3203.1" />
-  <C value="-44.232" />
-  <Tmin units="K"  value="327.25" />
-  <Tmax units="K"  value="471.05" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9477" />
-  <B value="-0.015403" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="374.57" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.447652" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.714488E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="331.6635" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.273" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="154.37" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0585327" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.76996" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.338192" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.152635" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.4166" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.712" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.338192" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14970" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.152635" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="2"  value="2" />
-  <group id="4"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="919-94-8" />
-<Smiles name="SMILES"  value="CCC(C)(C)OCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1447" />
-<CompoundID name="Name"  value="Butyl vinyl ether" />
-<StructureFormula name="Structure"  value="C4H9OCHCH2" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="540.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3200000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.38362" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="367.131" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="181.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="181.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.134811" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.163" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.130251" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.358" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.806E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16460" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.16955E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0684699" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.71E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.83E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.61974E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="428000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.38E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.10759" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.59144E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.146" />
-  <B value="-0.0067994" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72.46" />
-  <Tmax units="K"  value="181.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.51202" />
-  <B value="0.22443" />
-  <C value="540.5" />
-  <D value="0.25269" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="517.32" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="80.48089" />
-  <B value="-6835.53" />
-  <C value="-8.641032" />
-  <D value="5.192611E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="536" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.9857E+07" />
-  <B value="1.4054" />
-  <C value="-2.9112" />
-  <D value="3.3585" />
-  <E value="-1.4378" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="536" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="177040" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="540.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="179060" />
-  <B value="294.15" />
-  <C value="4.464" />
-  <D value="0.023293" />
-  <E value="-0.000021892" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="366.97" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="70271" />
-  <B value="-440.11" />
-  <C value="12.531" />
-  <D value="0.00054467" />
-  <E value="-2.1666E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2416" />
-  <B value="-256" />
-  <C value="-40.57" />
-  <D value="859.83" />
-  <E value="-11281" />
-  <Tmin units="K"  value="268" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-13.973" />
-  <B value="1139.1" />
-  <C value="0.44727" />
-  <D value="-0.0000011861" />
-  <E value="2" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="366.97" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.4315E-08" />
-  <B value="0.78571" />
-  <C value="41.584" />
-  <D value="9100.4" />
-  <Tmin units="K"  value="366.97" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.13174" />
-  <B value="16.987" />
-  <C value="-1.2513" />
-  <D value="-0.000050242" />
-  <E value="-0.000001447" />
-  <Tmin units="K"  value="160.8" />
-  <Tmax units="K"  value="420.8" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00002407" />
-  <B value="1.1842" />
-  <C value="65.04" />
-  <D value="40153" />
-  <Tmin units="K"  value="366.97" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010113" />
-  <B value="61.945" />
-  <C value="-3.4261" />
-  <D value="0.0012947" />
-  <E value="-0.0000069057" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="536" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="6738" />
-  <B value="536.06" />
-  <C value="-0.27187" />
-  <D value="0.000047059" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.122" />
-  <B value="2983.4" />
-  <C value="-56.28" />
-  <Tmin units="K"  value="330.56" />
-  <Tmax units="K"  value="479.97" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9306" />
-  <B value="-0.015656" />
-  <Tmin units="K"  value="181.15" />
-  <Tmax units="K"  value="366.97" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.368168" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.438977E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="329.5296" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.273" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="131.54" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.78288" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0496357" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.791941" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.358" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.130251" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.7403" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.192" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.50681" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.358" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16460" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.130251" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="5"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="5"  value="1" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-34-2" />
-<Smiles name="SMILES"  value="CCCCOC=C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1461" />
-<CompoundID name="Name"  value="Anisole" />
-<StructureFormula name="Structure"  value="C6H5OCH3" />
-<Family name="Family"  value="62" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="642.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4180000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.337" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.267" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="426.95" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="235.85" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="235.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.44662" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="108.138" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.109167" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.350169" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.719E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20110" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.54E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06321" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.02E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.8E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.27E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="361000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9600000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.97849" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.6018E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.268" />
-  <B value="-0.0057985" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="94.26" />
-  <Tmax units="K"  value="235.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.67524" />
-  <B value="0.24431" />
-  <C value="645.61" />
-  <D value="0.26239" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="645.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="117.0581" />
-  <B value="-9318.991" />
-  <C value="-14.12565" />
-  <D value="9.850515E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="645.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.1782E+07" />
-  <B value="0.29654" />
-  <C value="0.81637" />
-  <D value="-1.3762" />
-  <E value="0.64684" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="624.02" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="25569" />
-  <B value="-54.962" />
-  <C value="8.9953" />
-  <D value="-0.053617" />
-  <E value="0.00010624" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="235.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="128070" />
-  <B value="-77.615" />
-  <C value="10.002" />
-  <D value="0.0059631" />
-  <E value="-0.0000043683" />
-  <Tmin units="K"  value="245.2" />
-  <Tmax units="K"  value="484.2" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-116340" />
-  <B value="-170.41" />
-  <C value="12.829" />
-  <D value="0.00034368" />
-  <E value="-1.0767E-07" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24272" />
-  <B value="-330.37" />
-  <C value="-37.811" />
-  <D value="-176890" />
-  <E value="557310" />
-  <Tmin units="K"  value="366.91" />
-  <Tmax units="K"  value="1760.88" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-16.864" />
-  <B value="1572.6" />
-  <C value="0.82898" />
-  <D value="-2.2828E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="426.73" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7587E-07" />
-  <B value="0.71998" />
-  <C value="171.18" />
-  <D value="1705.8" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
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-  <B value="21.142" />
-  <C value="-1.1373" />
-  <D value="-0.0000023738" />
-  <E value="-0.0000009757" />
-  <Tmin units="K"  value="192.5" />
-  <Tmax units="K"  value="512.5" />
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-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00055356" />
-  <B value="0.7624" />
-  <C value="342.48" />
-  <D value="235670" />
-  <Tmin units="K"  value="426.73" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01028" />
-  <B value="76.185" />
-  <C value="-3.3574" />
-  <D value="0.001879" />
-  <E value="-0.0000062433" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="624.02" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-76587" />
-  <B value="835.59" />
-  <C value="-0.72557" />
-  <D value="0.00024575" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-3.251956" />
-  <B value="-2150" />
-  <C value="-12.9" />
-  <Tmin units="K"  value="278.5945" />
-  <Tmax units="K"  value="448.5945" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.389" />
-  <B value="3602.4" />
-  <C value="-61.82" />
-  <Tmin units="K"  value="385.45" />
-  <Tmax units="K"  value="568.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.2274" />
-  <B value="-0.012042" />
-  <Tmin units="K"  value="235.65" />
-  <Tmax units="K"  value="426.73" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.338527" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.333466E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="361.4017" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.267" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="117.59" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0469574" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.999625" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.350169" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.109167" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.1667" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.208" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.350169" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20110" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.109167" />
-<UnifacVLE name="UNIFAC" >
-  <group id="25"  value="1" />
-  <group id="11"  value="1" />
-  <group id="10"  value="5" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="27"  value="1" />
-  <group id="10"  value="1" />
-  <group id="9"  value="5" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="25"  value="1" />
-  <group id="11"  value="1" />
-  <group id="10"  value="5" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="24"  value="1" />
-  <group id="10"  value="1" />
-  <group id="9"  value="5" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="100-66-3" />
-<Smiles name="SMILES"  value="c1ccccc1(OC)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1319" />
-<CompoundID name="Name"  value="Isopropyl acetate" />
-<StructureFormula name="Structure"  value="CH3COOCH(CH3)2" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="516.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3495640" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.343881" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="361.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="199.75" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="199.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.8692" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.132" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.117579" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.542817" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.679E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17150" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06299" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.13E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.817E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.337E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="390200" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8880000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.28" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.658E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.073" />
-  <B value="-0.0067629" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="79.9" />
-  <Tmax units="K"  value="199.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.7447" />
-  <B value="0.38746" />
-  <C value="516.15" />
-  <D value="0.46246" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="514.51" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="53.596" />
-  <B value="-5675.5" />
-  <C value="-4.5065" />
-  <D value="0.0000012831" />
-  <E value="2" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="532" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.852874E+07" />
-  <B value="0.139799" />
-  <C value="0.87492" />
-  <D value="-1.379465" />
-  <E value="0.721356" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="514.51" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="156890" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="516.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="131390" />
-  <B value="-46.486" />
-  <C value="8.1047" />
-  <D value="0.013597" />
-  <E value="-0.000010999" />
-  <Tmin units="K"  value="215.75" />
-  <Tmax units="K"  value="478.8" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="49388" />
-  <B value="-461.23" />
-  <C value="12.886" />
-  <D value="-0.00010674" />
-  <E value="6.959E-08" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="1200.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22372" />
-  <B value="-237.39" />
-  <C value="-36.602" />
-  <D value="-8696.2" />
-  <E value="11115" />
-  <Tmin units="K"  value="266" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.895" />
-  <B value="1115.7" />
-  <C value="-0.084451" />
-  <D value="4.8399E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="361.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.7177E-07" />
-  <B value="0.62086" />
-  <C value="249.31" />
-  <D value="-266.55" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.09612" />
-  <B value="7.576" />
-  <C value="-1.2028" />
-  <D value="-0.00070085" />
-  <E value="-9.2097E-07" />
-  <Tmin units="K"  value="161.4" />
-  <Tmax units="K"  value="421.4" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-5913400" />
-  <B value="-0.12076" />
-  <C value="3.6992E+09" />
-  <D value="-2.5996E+13" />
-  <Tmin units="K"  value="361.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0048741" />
-  <B value="363.65" />
-  <C value="-7.1258" />
-  <D value="0.0151" />
-  <E value="-0.000025128" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="514.51" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-29200" />
-  <B value="680.9" />
-  <C value="-0.52361" />
-  <D value="0.00016062" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="1200.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.384" />
-  <B value="3059.3" />
-  <C value="-51.328" />
-  <Tmin units="K"  value="312.04" />
-  <Tmax units="K"  value="462.05" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9628" />
-  <B value="-0.015227" />
-  <Tmin units="K"  value="199.75" />
-  <Tmax units="K"  value="361.65" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.337297" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.900063E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="229.2309" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="114.82" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0449492" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.881001" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.367774" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.117579" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.1522" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.652" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.367774" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17150" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.117579" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="3"  value="1" />
-  <group id="18"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-21-4" />
-<Smiles name="SMILES"  value="CC(=O)OC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1315" />
-<CompoundID name="Name"  value="N-butyl acetate" />
-<StructureFormula name="Structure"  value="CH3COO(CH2)3CH3" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="579" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3090000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4128" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="399.12" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="199.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="199.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0816516" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="116.16" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13251" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.407" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.28E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17670" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.14E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07323" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.049E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.856E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.123E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="442500" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.44E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.09" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.283E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.567" />
-  <B value="-0.0057964" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="79.86" />
-  <Tmax units="K"  value="199.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.13588" />
-  <B value="0.1193" />
-  <C value="579" />
-  <D value="0.16305" />
-  <Tmin units="K"  value="199.65" />
-  <Tmax units="K"  value="575.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="90.42793" />
-  <B value="-7625.342" />
-  <C value="-10.22284" />
-  <D value="8.987208E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="199.65" />
-  <Tmax units="K"  value="575.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.192574E+07" />
-  <B value="1.151594" />
-  <C value="0.0889674" />
-  <D value="-1.859865" />
-  <E value="1.113952" />
-  <Tmin units="K"  value="199.65" />
-  <Tmax units="K"  value="575.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="182900" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="579" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="201710" />
-  <B value="-19.025" />
-  <C value="8.0191" />
-  <D value="0.0068889" />
-  <E value="0.0000021505" />
-  <Tmin units="K"  value="202.7" />
-  <Tmax units="K"  value="461.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="92876" />
-  <B value="-666.17" />
-  <C value="13.432" />
-  <D value="-0.00066148" />
-  <E value="3.0678E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22835" />
-  <B value="-267.19" />
-  <C value="-64.731" />
-  <D value="-23119" />
-  <E value="30658" />
-  <Tmin units="K"  value="289.5" />
-  <Tmax units="K"  value="1737" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-17.008" />
-  <B value="1461.1" />
-  <C value="0.8424" />
-  <D value="1.1193E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="399.26" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.0488E-07" />
-  <B value="0.76809" />
-  <C value="52.337" />
-  <D value="8271.1" />
-  <Tmin units="K"  value="199.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.04366" />
-  <B value="-125.65" />
-  <C value="-0.40686" />
-  <D value="-0.0059305" />
-  <E value="0.0000024167" />
-  <Tmin units="K"  value="199.65" />
-  <Tmax units="K"  value="463.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="5.9364E-09" />
-  <B value="2.3739" />
-  <C value="-402.22" />
-  <D value="69606" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="800" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016732" />
-  <B value="17.559" />
-  <C value="-2.7905" />
-  <D value="-0.00064121" />
-  <E value="-0.0000029118" />
-  <Tmin units="K"  value="199.65" />
-  <Tmax units="K"  value="575.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-22630" />
-  <B value="742.91" />
-  <C value="-0.55184" />
-  <D value="0.0001701" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.114462" />
-  <B value="-2550" />
-  <C value="-15.3" />
-  <Tmin units="K"  value="273.0389" />
-  <Tmax units="K"  value="443.0389" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.225" />
-  <B value="3242.2" />
-  <C value="-64.854" />
-  <Tmin units="K"  value="349.03" />
-  <Tmax units="K"  value="516.07" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.8704" />
-  <B value="-0.011433" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="399.26" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.39539" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.229034E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="268.4266" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="135.34" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0528122" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.885234" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.407" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.13251" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.8274" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.196" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.407" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17670" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.13251" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="3" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="123-86-4" />
-<Smiles name="SMILES"  value="CC(=O)OCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1316" />
-<CompoundID name="Name"  value="Isobutyl acetate" />
-<StructureFormula name="Structure"  value="CH3COOCH2CH(CH3)2" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="561" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3160000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.413" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="389.72" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="174.3" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="174.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00622415" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="116.16" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.13387" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.456" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.276E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17050" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.24E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07322" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.048E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.93E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.222E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="441000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.24E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.16" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.319E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.68" />
-  <B value="-0.0067015" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="69.72" />
-  <Tmax units="K"  value="174.3" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.40843" />
-  <B value="0.20784" />
-  <C value="561" />
-  <D value="0.21394" />
-  <Tmin units="K"  value="174.3" />
-  <Tmax units="K"  value="560.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="28.45261" />
-  <B value="-5051.537" />
-  <C value="-0.615949" />
-  <D value="-1.95606E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="174.3" />
-  <Tmax units="K"  value="561.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.408651E+07" />
-  <B value="1.313221" />
-  <C value="-1.992233" />
-  <D value="1.203843" />
-  <E value="-0.0654865" />
-  <Tmin units="K"  value="174.3" />
-  <Tmax units="K"  value="560.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="182900" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="561" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="161610" />
-  <B value="660.76" />
-  <C value="3.3098" />
-  <D value="0.024476" />
-  <E value="-0.000019195" />
-  <Tmin units="K"  value="211.01" />
-  <Tmax units="K"  value="504.72" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="100140" />
-  <B value="-654.65" />
-  <C value="13.176" />
-  <D value="-0.00017464" />
-  <E value="3.2068E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1400.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25768" />
-  <B value="-273.28" />
-  <C value="-54.487" />
-  <D value="-16133" />
-  <E value="20909" />
-  <Tmin units="K"  value="280.4" />
-  <Tmax units="K"  value="1792.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.1351" />
-  <B value="566.94" />
-  <C value="-0.24427" />
-  <D value="-0.0000078548" />
-  <E value="2" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="389.8" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.0879E-07" />
-  <B value="0.78101" />
-  <C value="111.13" />
-  <D value="1059.5" />
-  <Tmin units="K"  value="174.3" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.070874" />
-  <B value="405.28" />
-  <C value="-7.1892" />
-  <D value="0.020474" />
-  <E value="-0.000033831" />
-  <Tmin units="K"  value="168.3" />
-  <Tmax units="K"  value="448.3" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.0010112" />
-  <B value="0.95292" />
-  <C value="-6813.9" />
-  <D value="270410" />
-  <Tmin units="K"  value="389.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01526" />
-  <B value="26.196" />
-  <C value="-3.0206" />
-  <D value="0.000089811" />
-  <E value="-0.0000040241" />
-  <Tmin units="K"  value="174.3" />
-  <Tmax units="K"  value="560.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-4262.4" />
-  <B value="646.34" />
-  <C value="-0.39482" />
-  <D value="0.000090736" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1400.15" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.532079" />
-  <B value="-2800" />
-  <C value="-16.8" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.759" />
-  <B value="3497.1" />
-  <C value="-48.009" />
-  <Tmin units="K"  value="337.04" />
-  <Tmax units="K"  value="503.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.9833" />
-  <B value="-0.011196" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="389.8" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.395333" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.808274E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="311.4942" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.266" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="135.34" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0520369" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.877796" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.456" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.13387" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.8266" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.192" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.456" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17050" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.13387" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-19-0" />
-<Smiles name="SMILES"  value="CC(=O)OCC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1357" />
-<CompoundID name="Name"  value="N-pentyl acetate" />
-<StructureFormula name="Structure"  value="CH3COOCH2(CH2)3CH3" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="605.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.442" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.245" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="422.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="202.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="202.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0185761" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="130.185" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.149382" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.413866" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.772E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17360" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.44E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08346" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.184E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.055E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.035E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="481800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.65E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.089933" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.89405E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.3057" />
-  <B value="-0.0050955" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="80.94" />
-  <Tmax units="K"  value="202.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.12608" />
-  <B value="0.12252" />
-  <C value="605.15" />
-  <D value="0.16886" />
-  <Tmin units="K"  value="202.35" />
-  <Tmax units="K"  value="599.9" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="168.7214" />
-  <B value="-11229.65" />
-  <C value="-22.11732" />
-  <D value="0.0000177213" />
-  <E value="2" />
-  <Tmin units="K"  value="202.35" />
-  <Tmax units="K"  value="600" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.883914E+07" />
-  <B value="0.946213" />
-  <C value="-0.171734" />
-  <D value="-0.730153" />
-  <E value="0.419139" />
-  <Tmin units="K"  value="202.35" />
-  <Tmax units="K"  value="599.9" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="208910" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="605.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="162580" />
-  <B value="80.092" />
-  <C value="8.5511" />
-  <D value="0.011513" />
-  <E value="-0.0000095523" />
-  <Tmin units="K"  value="209.3" />
-  <Tmax units="K"  value="439" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="47433" />
-  <B value="-339.24" />
-  <C value="12.756" />
-  <D value="0.0005476" />
-  <E value="-2.1862E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34111" />
-  <B value="-397.41" />
-  <C value="-63.466" />
-  <D value="-56487" />
-  <E value="116110" />
-  <Tmin units="K"  value="299" />
-  <Tmax units="K"  value="1913" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-24.376" />
-  <B value="1661.3" />
-  <C value="2.1378" />
-  <D value="-0.0000051198" />
-  <E value="2" />
-  <Tmin units="K"  value="202.35" />
-  <Tmax units="K"  value="480" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.6095E-07" />
-  <B value="0.57889" />
-  <C value="337.64" />
-  <D value="-259.28" />
-  <Tmin units="K"  value="202.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.08346" />
-  <B value="4.4855" />
-  <C value="-1.2866" />
-  <D value="-0.00064282" />
-  <E value="-6.6262E-07" />
-  <Tmin units="K"  value="179.4" />
-  <Tmax units="K"  value="469.4" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.014827" />
-  <B value="0.47704" />
-  <C value="-3337.4" />
-  <D value="-1003300" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012757" />
-  <B value="49.233" />
-  <C value="-3.1535" />
-  <D value="0.00024702" />
-  <E value="-0.000004004" />
-  <Tmin units="K"  value="202.35" />
-  <Tmax units="K"  value="599.9" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-18598" />
-  <B value="795.27" />
-  <C value="-0.51713" />
-  <D value="0.00013022" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.15" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.762874" />
-  <B value="-3450" />
-  <C value="-20.7" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.171" />
-  <B value="4226.8" />
-  <C value="-24.15" />
-  <Tmin units="K"  value="364.25" />
-  <Tmax units="K"  value="538.65" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0509" />
-  <B value="-0.012995" />
-  <Tmin units="K"  value="202.35" />
-  <Tmax units="K"  value="480" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.455324" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.686343E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="249.9046" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.245" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="155.86" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0596961" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.880404" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.413866" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.149382" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.5018" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.736" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.447773" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17360" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.149382" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="628-63-7" />
-<Smiles name="SMILES"  value="CC(=O)OCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1321" />
-<CompoundID name="Name"  value="Vinyl acetate" />
-<StructureFormula name="Structure"  value="CH3COOCHCH2" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="501.45" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4150000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.266" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="345.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="180.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="180.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.70586" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.0892" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0929486" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.529352" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.969E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18580" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.97E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04928" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.26E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.157E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.287E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="334400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5370000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.28" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.95E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.585" />
-  <B value="-0.0095513" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72.14" />
-  <Tmax units="K"  value="180.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.80837" />
-  <B value="0.2388" />
-  <C value="524.34" />
-  <D value="0.25151" />
-  <Tmin units="K"  value="180.35" />
-  <Tmax units="K"  value="524.33" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-28.90631" />
-  <B value="-2451.071" />
-  <C value="8.43748" />
-  <D value="-0.000014969" />
-  <E value="2" />
-  <Tmin units="K"  value="180.35" />
-  <Tmax units="K"  value="519.13" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.178411E+07" />
-  <B value="1.329393" />
-  <C value="-3.127105" />
-  <D value="3.542901" />
-  <E value="-1.384803" />
-  <Tmin units="K"  value="180.35" />
-  <Tmax units="K"  value="501.3" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="115760" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="501.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="104670" />
-  <B value="68.241" />
-  <C value="7.8309" />
-  <D value="0.01301" />
-  <E value="-0.00001011" />
-  <Tmin units="K"  value="213.41" />
-  <Tmax units="K"  value="389.35" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="50651" />
-  <B value="-432.89" />
-  <C value="12.118" />
-  <D value="0.00048734" />
-  <E value="-1.8964E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18283" />
-  <B value="-191.61" />
-  <C value="-27.209" />
-  <D value="-6457.2" />
-  <E value="8397.1" />
-  <Tmin units="K"  value="259.56" />
-  <Tmax units="K"  value="1890.57" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-20.187" />
-  <B value="1398" />
-  <C value="1.3362" />
-  <D value="8.2076E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="345.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4727E-07" />
-  <B value="0.76076" />
-  <C value="119.27" />
-  <D value="67.359" />
-  <Tmin units="K"  value="180.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.068153" />
-  <B value="28.848" />
-  <C value="-1.5016" />
-  <D value="0.00051317" />
-  <E value="-0.0000030057" />
-  <Tmin units="K"  value="180.35" />
-  <Tmax units="K"  value="410" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-5281900" />
-  <B value="-0.16154" />
-  <C value="2.8419E+09" />
-  <D value="-1.7045E+13" />
-  <Tmin units="K"  value="276.09" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0044907" />
-  <B value="310.64" />
-  <C value="-6.6728" />
-  <D value="0.014871" />
-  <E value="-0.000027076" />
-  <Tmin units="K"  value="180.35" />
-  <Tmax units="K"  value="501.3" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="21072" />
-  <B value="300.62" />
-  <C value="-0.12074" />
-  <D value="0.000010448" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.328" />
-  <B value="2885.8" />
-  <C value="-51.534" />
-  <Tmin units="K"  value="301.95" />
-  <Tmax units="K"  value="447.81" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.1171" />
-  <B value="-0.012291" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="345.65" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.261926" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.395338E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="216.355" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="89.68" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0355767" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.941" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.351307" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0929486" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.2485" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.904" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.351307" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18580" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0929486" />
-<UnifacVLE name="UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="5"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="5"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="5"  value="1" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-05-4" />
-<Smiles name="SMILES"  value="CC(=O)OC=C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1363" />
-<CompoundID name="Name"  value="N-hexyl acetate" />
-<StructureFormula name="Structure"  value="CH3COOCH2(CH2)4CH3" />
-<Family name="Family"  value="56" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="623.5" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2410000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.519" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="444.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="192.25" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="192.25" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000851561" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="144.211" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.166008" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.461433" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.16E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17200" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.09369" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.319E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.263E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.954E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="520900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.69E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.17" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.505E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.5065" />
-  <B value="-0.0055309" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="76.9" />
-  <Tmax units="K"  value="192.25" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.39801" />
-  <B value="0.22828" />
-  <C value="623.5" />
-  <D value="0.26879" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="595.59" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="135.2" />
-  <B value="-10778" />
-  <C value="-16.633" />
-  <D value="0.000010146" />
-  <E value="2" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="618" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.6365E+07" />
-  <B value="1.3535" />
-  <C value="-2.7266" />
-  <D value="3.0189" />
-  <E value="-1.2516" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="618" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="234920" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="623.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="152410" />
-  <B value="849.23" />
-  <C value="3.575" />
-  <D value="0.024024" />
-  <E value="-0.000019964" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="444.65" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="74275" />
-  <B value="-423.1" />
-  <C value="13.088" />
-  <D value="0.00020721" />
-  <E value="-5.6794E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26575" />
-  <B value="-251.71" />
-  <C value="-141.73" />
-  <D value="30213" />
-  <E value="-150230" />
-  <Tmin units="K"  value="309" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.853" />
-  <B value="1437.9" />
-  <C value="0.03568" />
-  <D value="-1.5887E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="444.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000001052" />
-  <B value="0.76244" />
-  <C value="141.7" />
-  <D value="-5217.3" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.076217" />
-  <B value="432.06" />
-  <C value="-6.6217" />
-  <D value="0.014354" />
-  <E value="-0.00002134" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="533.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-96.991" />
-  <B value="-0.0010535" />
-  <C value="51726" />
-  <D value="-1.0193E+09" />
-  <Tmin units="K"  value="444.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016381" />
-  <B value="19.416" />
-  <C value="-2.8226" />
-  <D value="-0.00062558" />
-  <E value="-0.000002447" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="618" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-13149" />
-  <B value="859.66" />
-  <C value="-0.53308" />
-  <D value="0.00012944" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.124" />
-  <B value="3454.4" />
-  <C value="-83.742" />
-  <Tmin units="K"  value="380.55" />
-  <Tmax units="K"  value="550.78" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.9193" />
-  <B value="-0.015758" />
-  <Tmin units="K"  value="192.25" />
-  <Tmax units="K"  value="444.65" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.517431" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.148912E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="253.719" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.244" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="176.38" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0672192" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.87832" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.461433" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.166008" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.1762" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.276" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.539588" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17200" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.166008" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="5" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="142-92-7" />
-<Smiles name="SMILES"  value="CCCCCCOC(=O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1109" />
-<CompoundID name="Name"  value="1-pentanol" />
-<StructureFormula name="Structure"  value="CH3(CH2)4OH" />
-<Family name="Family"  value="27" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="588.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3909000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.326" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.262" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="411.16" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="194.95" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="195.56" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000345245" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.15" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10863" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.579" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.679E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22520" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.67059E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06263" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.98E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.0016E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.46022E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="402501" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9790560" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3176" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.06051E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.8" />
-  <B value="7.9473E-09" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="195.56" />
-  <Tmax units="K"  value="205.06" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54137" />
-  <B value="0.21848" />
-  <C value="588.15" />
-  <D value="0.20812" />
-  <Tmin units="K"  value="195.56" />
-  <Tmax units="K"  value="588.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="150.9933" />
-  <B value="-11938.85" />
-  <C value="-18.59103" />
-  <D value="8.735585E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="195.56" />
-  <Tmax units="K"  value="588.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.1853E+08" />
-  <B value="1.9668" />
-  <C value="-2.5741" />
-  <D value="1.6268" />
-  <E value="-0.41037" />
-  <Tmin units="K"  value="195.56" />
-  <Tmax units="K"  value="588.1" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15533" />
-  <B value="1421.2" />
-  <C value="-4.9071" />
-  <D value="-0.013872" />
-  <E value="0.00011092" />
-  <Tmin units="K"  value="21.61" />
-  <Tmax units="K"  value="195.56" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="151460" />
-  <B value="721.52" />
-  <C value="-3.5691" />
-  <D value="0.059604" />
-  <E value="-0.000063767" />
-  <Tmin units="K"  value="200.14" />
-  <Tmax units="K"  value="390" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78144" />
-  <B value="-573.83" />
-  <C value="12.781" />
-  <D value="0.00015431" />
-  <E value="-6.6745E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24054" />
-  <B value="-258.72" />
-  <C value="-37.585" />
-  <D value="50573" />
-  <E value="-237590" />
-  <Tmin units="K"  value="294.05" />
-  <Tmax units="K"  value="1871.1" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-29.696" />
-  <B value="3126.2" />
-  <C value="2.4167" />
-  <D value="-0.0000024327" />
-  <E value="2" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="420" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9935E-07" />
-  <B value="0.70293" />
-  <C value="200.97" />
-  <D value="-2040.7" />
-  <Tmin units="K"  value="277.39" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.14679" />
-  <B value="201570" />
-  <C value="-2097.5" />
-  <D value="7.255" />
-  <E value="-0.0083973" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="373.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1221.5" />
-  <B value="0.95117" />
-  <C value="8.0014E+09" />
-  <D value="-2.8255E+11" />
-  <Tmin units="K"  value="324.42" />
-  <Tmax units="K"  value="990.95" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.066781" />
-  <B value="-45.948" />
-  <C value="-1.8289" />
-  <D value="-0.0013347" />
-  <E value="-5.553E-08" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="503.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="45979" />
-  <B value="140.41" />
-  <C value="0.78405" />
-  <D value="-0.0011412" />
-  <E value="4.6619E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-13.20079" />
-  <B value="-6950" />
-  <C value="-41.7" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.459" />
-  <B value="3044" />
-  <C value="-104.53" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="526.12" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="1.4416" />
-  <B value="-0.023533" />
-  <Tmin units="K"  value="253.15" />
-  <Tmax units="K"  value="420" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.335285" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.40751E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="309.2331" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.262" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="113.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.0103" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0436411" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.819862" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.579" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10863" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5987" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.208" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.3301" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.579" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22520" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.10863" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="71-41-0" />
-<Smiles name="SMILES"  value="CCCCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1110" />
-<CompoundID name="Name"  value="2-pentanol" />
-<StructureFormula name="Structure"  value="CH3(CH2)2CH(OH)CH3" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="552" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3880000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.327" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="392.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="200" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="200" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00596587" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.1482" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.109448" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.674371" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.619E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21700" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.39E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06262" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.97E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.138E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.593E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="396400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8480000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.47" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.0515E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.7" />
-  <B value="4.0224E-17" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.319" />
-  <B value="0.3371" />
-  <C value="552" />
-  <D value="0.32218" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="541.34" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="156.6278" />
-  <B value="-11701.22" />
-  <C value="-19.61134" />
-  <D value="0.0000119964" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="560.3" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.4515E+07" />
-  <B value="0.5603" />
-  <C value="0.52669" />
-  <D value="-1.3675" />
-  <E value="0.83639" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="541.34" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="158590" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="552" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="223900" />
-  <B value="2827.9" />
-  <C value="-24.806" />
-  <D value="0.11426" />
-  <E value="-0.00010479" />
-  <Tmin units="K"  value="276" />
-  <Tmax units="K"  value="420.22" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81533" />
-  <B value="-562.17" />
-  <C value="12.749" />
-  <D value="0.00015514" />
-  <E value="-6.2807E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24133" />
-  <B value="-247.23" />
-  <C value="-35.04" />
-  <D value="43362" />
-  <E value="-173350" />
-  <Tmin units="K"  value="280.15" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-161.5575" />
-  <B value="9388.477" />
-  <C value="22.02304" />
-  <D value="-0.0000121894" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="448.24" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.2586E-07" />
-  <B value="0.63457" />
-  <C value="242.49" />
-  <D value="-572.84" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.29342" />
-  <B value="50.682" />
-  <C value="-1.2923" />
-  <D value="0.0017888" />
-  <E value="-0.0000028966" />
-  <Tmin units="K"  value="165.6" />
-  <Tmax units="K"  value="435.6" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1300.2" />
-  <B value="0.95377" />
-  <C value="8.1158E+09" />
-  <D value="-2.9211E+11" />
-  <Tmin units="K"  value="392.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.024272" />
-  <B value="-6.3975" />
-  <C value="-2.6095" />
-  <D value="-0.0005545" />
-  <E value="-0.0000026816" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="541.34" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="5418.5" />
-  <B value="517.97" />
-  <C value="-0.28727" />
-  <D value="0.000060797" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500.15" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-12.96" />
-  <B value="-6855" />
-  <C value="-41.13" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.365" />
-  <B value="2787.1" />
-  <C value="-109.05" />
-  <Tmin units="K"  value="332.74" />
-  <Tmax units="K"  value="484.45" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="5.5268" />
-  <B value="-0.036204" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="448.24" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.335229" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.473307E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="282.3295" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="113.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0427674" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.813156" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.674371" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.109448" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5979" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.204" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.558707" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21700" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.109448" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="81"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="6032-29-7" />
-<Smiles name="SMILES"  value="CCCC(O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1112" />
-<CompoundID name="Name"  value="2-methyl-1-butanol" />
-<StructureFormula name="Structure"  value="CH3CH2CH(CH3)CH2OH" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="575.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3940000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.329" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.271" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="401.85" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="195" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="195" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000803" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.148" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1083" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.587733" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.437E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22080" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.27E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0593" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.484E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.0209E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.41E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="386900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7430000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.0182" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.062E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.886" />
-  <B value="-0.00826" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="78" />
-  <Tmax units="K"  value="195" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.88123" />
-  <B value="0.27569" />
-  <C value="576.16" />
-  <D value="0.26459" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="576.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="169.4054" />
-  <B value="-12535.91" />
-  <C value="-21.44821" />
-  <D value="0.000011664" />
-  <E value="2" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="575.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.7446E+08" />
-  <B value="5.4789" />
-  <C value="-13.886" />
-  <D value="15.653" />
-  <E value="-6.6531" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="560.91" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5555.3" />
-  <B value="806.4" />
-  <C value="-0.95225" />
-  <D value="0.0022801" />
-  <E value="-0.0000033301" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="195" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="64512" />
-  <B value="-115.41" />
-  <C value="11.54" />
-  <D value="0.0018322" />
-  <E value="0.0000027168" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="401.85" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="76232" />
-  <B value="-567.6" />
-  <C value="12.811" />
-  <D value="0.000074113" />
-  <E value="-1.3012E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17011" />
-  <B value="-182.68" />
-  <C value="-48.25" />
-  <D value="18476" />
-  <E value="-142510" />
-  <Tmin units="K"  value="287.7" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="0.00893998" />
-  <B value="2796.534" />
-  <C value="-2.732303" />
-  <D value="0.0000087109" />
-  <E value="2" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="453.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000000189" />
-  <B value="0.70643" />
-  <C value="185.92" />
-  <D value="-6046.6" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.080313" />
-  <B value="-215.29" />
-  <C value="-0.17577" />
-  <D value="-0.0076457" />
-  <E value="0.000003672" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="401.85" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1262.3" />
-  <B value="0.94565" />
-  <C value="7.7547E+09" />
-  <D value="-2.8418E+11" />
-  <Tmin units="K"  value="401.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.06667" />
-  <B value="21.081" />
-  <C value="-2.2968" />
-  <D value="-0.00031727" />
-  <E value="-8.1113E-07" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="555.38" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-1715" />
-  <B value="532.87" />
-  <C value="-0.30305" />
-  <D value="0.000069112" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-15.47" />
-  <B value="-7815" />
-  <C value="-46.89" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.051" />
-  <B value="2696.4" />
-  <C value="-119.16" />
-  <Tmin units="K"  value="345.65" />
-  <Tmax units="K"  value="515.34" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="4.7162" />
-  <B value="-0.0329" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="453.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.316767" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.171827E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="341.643" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.271" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="113.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="3.2374" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0430983" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.823885" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.587733" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1083" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5979" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.204" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-6.2448" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.587733" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22080" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1083" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="1" />
-  <group id="81"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="137-32-6" />
-<Smiles name="SMILES"  value="OCC(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1113" />
-<CompoundID name="Name"  value="2,2-dimethyl-1-propanol" />
-<StructureFormula name="Structure"  value="(CH3)3CCH2OH" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="552.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4078000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.327" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.29" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="386.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="328.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="328.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="8050" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.1482" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1255" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.595013" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.388E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19040" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.47E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06261" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.17E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.021E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.4E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="370000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3500000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1247" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.061E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.9642" />
-  <B value="-0.0024076" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="242.1" />
-  <Tmax units="K"  value="328.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.88741" />
-  <B value="0.29" />
-  <C value="552.7" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="328.15" />
-  <Tmax units="K"  value="552.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="192.4683" />
-  <B value="-12413.62" />
-  <C value="-25.59931" />
-  <D value="0.0000246643" />
-  <E value="2" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="552.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.5224E+07" />
-  <B value="-1.2435" />
-  <C value="2.138" />
-  <D value="0.13988" />
-  <E value="-0.73989" />
-  <Tmin units="K"  value="274.2" />
-  <Tmax units="K"  value="552.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="2.6373E+07" />
-  <B value="-380330" />
-  <C value="2052.3" />
-  <D value="-4.8887" />
-  <E value="0.004351" />
-  <Tmin units="K"  value="242.1" />
-  <Tmax units="K"  value="328.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="124850" />
-  <B value="368.96" />
-  <C value="4.9094" />
-  <D value="0.027472" />
-  <E value="-0.00002893" />
-  <Tmin units="K"  value="294.4" />
-  <Tmax units="K"  value="386.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="72294.67" />
-  <B value="-550.0374" />
-  <C value="12.86817" />
-  <D value="0.000039202" />
-  <E value="-1.255351E-08" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22295" />
-  <B value="-222.2" />
-  <C value="-30.28" />
-  <D value="12264" />
-  <E value="-130500" />
-  <Tmin units="K"  value="276.35" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.693" />
-  <B value="3446.8" />
-  <C value="-0.71456" />
-  <D value="0.0000011322" />
-  <E value="2" />
-  <Tmin units="K"  value="328.15" />
-  <Tmax units="K"  value="386.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000021696" />
-  <B value="0.15612" />
-  <C value="1926.2" />
-  <D value="5137.4" />
-  <Tmin units="K"  value="328.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.11602" />
-  <B value="10.416" />
-  <C value="-1.227" />
-  <D value="-0.00033355" />
-  <E value="-0.00000113" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="435" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="1.2842E-07" />
-  <B value="1.9773" />
-  <C value="-61.933" />
-  <D value="2946" />
-  <Tmin units="K"  value="386.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0041579" />
-  <B value="905.49" />
-  <C value="-11.129" />
-  <D value="0.02249" />
-  <E value="-0.000027579" />
-  <Tmin units="K"  value="327.15" />
-  <Tmax units="K"  value="552.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="56025" />
-  <B value="298.25" />
-  <C value="-0.0082083" />
-  <D value="-0.000042003" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.2" />
-  <B value="-4175" />
-  <C value="-25.05" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.192" />
-  <B value="2694.4" />
-  <C value="-107.63" />
-  <Tmin units="K"  value="333.15" />
-  <Tmax units="K"  value="490.57" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="3.1165" />
-  <B value="-0.028526" />
-  <Tmin units="K"  value="328.15" />
-  <Tmax units="K"  value="386.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.335173" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.678278E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="418.8277" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.29" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="113.33" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="2.4275" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0437982" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.735646" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.595013" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1255" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5972" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.284" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-4.9571" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.595013" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19040" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1255" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-84-3" />
-<Smiles name="SMILES"  value="OCC(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1114" />
-<CompoundID name="Name"  value="1-hexanol" />
-<StructureFormula name="Structure"  value="CH3(CH2)5OH" />
-<Family name="Family"  value="27" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="611.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3510000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.381" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.263" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="430.44" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="228.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="228.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0295499" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.177" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12519" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.58" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.144E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21830" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0728599" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.033E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.18E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.344E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="440000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.54E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.34" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.67439E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.939" />
-  <B value="-0.00020832" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="238.05" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.12172" />
-  <B value="0.11263" />
-  <C value="611.4" />
-  <D value="0.13194" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="610.3" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="140.4065" />
-  <B value="-11996.05" />
-  <C value="-16.8497" />
-  <D value="6.25688E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="610.3" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.9912E+07" />
-  <B value="1.0345" />
-  <C value="-0.71214" />
-  <D value="0.038869" />
-  <E value="0.22103" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="610.3" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19775" />
-  <B value="1482.2" />
-  <C value="-5.3111" />
-  <D value="0.0052486" />
-  <E value="0.000017593" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="200" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-13352" />
-  <B value="695.57" />
-  <C value="4.4864" />
-  <D value="0.026504" />
-  <E value="-0.000025444" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="93733" />
-  <B value="-618.92" />
-  <C value="13.098" />
-  <D value="-0.000028541" />
-  <E value="-8.6478E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28103" />
-  <B value="-313.61" />
-  <C value="-50.106" />
-  <D value="92563" />
-  <E value="-384560" />
-  <Tmin units="K"  value="305.15" />
-  <Tmax units="K"  value="1955.7" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-78.019" />
-  <B value="5186.5" />
-  <C value="9.8395" />
-  <D value="-0.0000094042" />
-  <E value="2" />
-  <Tmin units="K"  value="243.15" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.3121E-07" />
-  <B value="0.66402" />
-  <C value="127.06" />
-  <D value="17987" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.09203" />
-  <B value="1297.6" />
-  <C value="-15.712" />
-  <D value="0.045447" />
-  <E value="-0.000056017" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="575" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-2143900" />
-  <B value="-0.092957" />
-  <C value="1.682E+08" />
-  <D value="-1.0339E+13" />
-  <Tmin units="K"  value="290.96" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035783" />
-  <B value="66.822" />
-  <C value="-3.0656" />
-  <D value="0.00092964" />
-  <E value="-0.000002544" />
-  <Tmin units="K"  value="228.55" />
-  <Tmax units="K"  value="610.3" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="56405" />
-  <B value="141.84" />
-  <C value="0.99233" />
-  <D value="-0.0014257" />
-  <E value="5.8077E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-12.45024" />
-  <B value="-6650" />
-  <C value="-39.9" />
-  <Tmin units="K"  value="279.15" />
-  <Tmax units="K"  value="449.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.645" />
-  <B value="2705.5" />
-  <C value="-133.98" />
-  <Tmin units="K"  value="369.19" />
-  <Tmax units="K"  value="550.02" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="1.3202" />
-  <B value="-0.022361" />
-  <Tmin units="K"  value="243.15" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.393259" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.718511E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="325.8963" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.263" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="133.85" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0505795" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.822536" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.58" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.12519" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2731" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.748" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.58" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21830" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.12519" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-27-3" />
-<Smiles name="SMILES"  value="CCCCCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1125" />
-<CompoundID name="Name"  value="1-heptanol" />
-<StructureFormula name="Structure"  value="CH3(CH2)6OH" />
-<Family name="Family"  value="27" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="631.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3150000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.435" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="449.81" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="239.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="239.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0117728" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="116.203" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.14195" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.582" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.38E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21540" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.57E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0830899" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.168E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.32E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.253E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="480000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.322E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.1804" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.2887E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.68" />
-  <B value="1.2716E-08" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="248.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53584" />
-  <B value="0.24833" />
-  <C value="632.61" />
-  <D value="0.25556" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="632.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="251.8216" />
-  <B value="-17683.63" />
-  <C value="-33.48375" />
-  <D value="0.000017626" />
-  <E value="2" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="632.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.173181E+08" />
-  <B value="1.489028" />
-  <C value="-2.632241" />
-  <D value="3.547284" />
-  <E value="-1.892409" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="611.89" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-12012" />
-  <B value="1881.5" />
-  <C value="-12.305" />
-  <D value="0.047146" />
-  <E value="-0.000063007" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="239.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-85727" />
-  <B value="742.02" />
-  <C value="4.7157" />
-  <D value="0.026441" />
-  <E value="-0.000025674" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="460" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="106760" />
-  <B value="-598.85" />
-  <C value="13.165" />
-  <D value="0.000054117" />
-  <E value="-4.1018E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.37446" />
-  <B value="-455.4" />
-  <C value="-40.107" />
-  <D value="86814" />
-  <E value="-437570" />
-  <Tmin units="K"  value="312" />
-  <Tmax units="K"  value="1735.9" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-78.864" />
-  <B value="5896.7" />
-  <C value="9.4721" />
-  <D value="-3.3466E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="465.1" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.5718E-07" />
-  <B value="0.65021" />
-  <C value="248.54" />
-  <D value="12.534" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.090359" />
-  <B value="1107.5" />
-  <C value="-13.417" />
-  <D value="0.037115" />
-  <E value="-0.000045589" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="573.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.060066" />
-  <B value="0.28898" />
-  <C value="-3437.9" />
-  <D value="-1686200" />
-  <Tmin units="K"  value="449.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.043165" />
-  <B value="-13.275" />
-  <C value="-2.2347" />
-  <D value="-0.0011614" />
-  <E value="-3.9773E-07" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="611.89" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="65975" />
-  <B value="149.85" />
-  <C value="1.1826" />
-  <D value="-0.0016895" />
-  <E value="6.8694E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-11.03" />
-  <B value="-5875" />
-  <C value="-35.25" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.467" />
-  <B value="2769.6" />
-  <C value="-139.94" />
-  <Tmin units="K"  value="379.55" />
-  <Tmax units="K"  value="563.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="1.6144" />
-  <B value="-0.022444" />
-  <Tmin units="K"  value="239.15" />
-  <Tmax units="K"  value="465.1" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.453119" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.086625E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="327.6932" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="133.85" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.53641" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0577626" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.726944" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.582" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.14195" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2731" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.748" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.4631" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.582" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21540" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.14195" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="15"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="14"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="15"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="15"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="6" />
-  <group id="14"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-70-6" />
-<Smiles name="SMILES"  value="OCCCCCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1241" />
-<CompoundID name="Name"  value="1,4-butanediol" />
-<StructureFormula name="Structure"  value="HO(CH2)4OH" />
-<Family name="Family"  value="49" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="667" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4880000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.297" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="501.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="293.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="293.05" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.437872" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.121" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0888513" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.17696" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.582E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="28850" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.31E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.057" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.32E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.267E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.78E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="381000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.63E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.1" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.2801E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.325" />
-  <B value="-0.0054395" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="117.22" />
-  <Tmax units="K"  value="293.05" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.87669" />
-  <B value="0.26038" />
-  <C value="667" />
-  <D value="0.18382" />
-  <Tmin units="K"  value="293.05" />
-  <Tmax units="K"  value="667" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="273.87" />
-  <B value="-20688" />
-  <C value="-36.39" />
-  <D value="0.000020662" />
-  <E value="2" />
-  <Tmin units="K"  value="293.05" />
-  <Tmax units="K"  value="667" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.835E+07" />
-  <B value="0.2441" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="293.05" />
-  <Tmax units="K"  value="667" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="13695" />
-  <B value="403.81" />
-  <C value="2.0198" />
-  <D value="-0.012355" />
-  <E value="0.000021703" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="293.05" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-147300" />
-  <B value="-151.29" />
-  <C value="13.013" />
-  <D value="0.00082927" />
-  <E value="-4.8483E-07" />
-  <Tmin units="K"  value="290" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78857" />
-  <B value="-613.48" />
-  <C value="12.793" />
-  <D value="-0.00013274" />
-  <E value="6.7309E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.047517" />
-  <B value="224.57" />
-  <C value="-206.02" />
-  <D value="728640" />
-  <E value="-3209200" />
-  <Tmin units="K"  value="333" />
-  <Tmax units="K"  value="1833" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-135.2818" />
-  <B value="9167.078" />
-  <C value="18.06409" />
-  <D value="-0.0000115446" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="501.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.0592E-07" />
-  <B value="0.79673" />
-  <C value="195.38" />
-  <D value="-19182" />
-  <Tmin units="K"  value="293.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.17847" />
-  <B value="-272.57" />
-  <C value="-0.42428" />
-  <D value="-0.0080796" />
-  <E value="0.0000034419" />
-  <Tmin units="K"  value="290.15" />
-  <Tmax units="K"  value="501.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-0.69878" />
-  <B value="0.86746" />
-  <C value="-2810400" />
-  <D value="-7.1005E+07" />
-  <Tmin units="K"  value="500" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.16365" />
-  <B value="1.8545" />
-  <C value="-1.4959" />
-  <D value="-0.00012211" />
-  <E value="-5.0965E-07" />
-  <Tmin units="K"  value="293.05" />
-  <Tmax units="K"  value="667" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="7294.7" />
-  <B value="466.9" />
-  <C value="-0.2818" />
-  <D value="0.000069184" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500.15" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-17.49" />
-  <B value="-10000" />
-  <C value="-95.7" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="24.877" />
-  <B value="5782.7" />
-  <C value="-67.663" />
-  <Tmin units="K"  value="408.15" />
-  <Tmax units="K"  value="588.27" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="4.9232" />
-  <B value="-0.026397" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="501.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.304068" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.240152E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="345.8955" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="98.92" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0406687" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.021037" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.17696" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0888513" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.6976" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.56" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.17696" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="28850" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0888513" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="4" />
-  <group id="14"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="14"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-63-4" />
-<Smiles name="SMILES"  value="OCCCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1801" />
-<CompoundID name="Name"  value="Methyl mercaptan" />
-<StructureFormula name="Structure"  value="CH3SH" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="470" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7230000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.145" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="279.11" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="150.18" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="150.18" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.14785" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="48.109" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.05552" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.15" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.606E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19470" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.07E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02848" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.39E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.26E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-9920000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="255000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5904000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.89544" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.1517E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="27.366" />
-  <B value="-0.020311" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="60.07" />
-  <Tmax units="K"  value="150.18" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.954" />
-  <B value="0.28171" />
-  <C value="470" />
-  <D value="0.28737" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="453.12" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="115.1598" />
-  <B value="-6300.053" />
-  <C value="-14.66478" />
-  <D value="0.0000195265" />
-  <E value="2" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="469.95" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.221375E+07" />
-  <B value="-0.00310105" />
-  <C value="0.657759" />
-  <D value="-0.0249162" />
-  <E value="-0.340052" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="469.95" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-10842" />
-  <B value="883.79" />
-  <C value="1.0741" />
-  <D value="-0.071254" />
-  <E value="0.00032202" />
-  <Tmin units="K"  value="14.96" />
-  <Tmax units="K"  value="150" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="87318" />
-  <B value="-59222" />
-  <C value="550.29" />
-  <D value="-1.6599" />
-  <E value="0.001702" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="298.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="38535" />
-  <B value="-588.35" />
-  <C value="11.232" />
-  <D value="0.00044782" />
-  <E value="-1.6363E-07" />
-  <Tmin units="K"  value="100" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.086994" />
-  <B value="-107.34" />
-  <C value="-7.9703" />
-  <D value="-15.158" />
-  <E value="-109.37" />
-  <Tmin units="K"  value="235" />
-  <Tmax units="K"  value="1880" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.947" />
-  <B value="607.01" />
-  <C value="-0.26447" />
-  <D value="0.0000011807" />
-  <E value="2" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="279.11" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9969E-07" />
-  <B value="0.74097" />
-  <C value="130.67" />
-  <D value="-839.04" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.011242" />
-  <B value="-11.424" />
-  <C value="-1.1701" />
-  <D value="-0.0017729" />
-  <E value="-0.0000012043" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="279.11" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000024689" />
-  <B value="1.1702" />
-  <C value="4.7184" />
-  <D value="35466" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.01346" />
-  <B value="41.423" />
-  <C value="-3.0112" />
-  <D value="0.0013607" />
-  <E value="-0.000009249" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="469.95" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34247" />
-  <B value="10.917" />
-  <C value="0.21543" />
-  <D value="-0.00026706" />
-  <E value="1.0044E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.379" />
-  <B value="2532.6" />
-  <C value="-21.919" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="419.46" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.1431" />
-  <B value="-0.015082" />
-  <Tmin units="K"  value="150.18" />
-  <Tmax units="K"  value="279.11" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.150999" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.759988E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="268.0997" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.268" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="48.04" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.4449" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0220648" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.863192" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.877" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.676" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="0.529899" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0.141244" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.7511" />
-<UnifacVLE name="UNIFAC" >
-  <group id="60"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="55"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="60"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="59"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="74-93-1" />
-<Smiles name="SMILES"  value="CS" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1803" />
-<CompoundID name="Name"  value="N-propyl mercaptan" />
-<StructureFormula name="Structure"  value="CH3CH2CH2SH" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="536" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4520000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.254" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="340.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="159.85" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="160" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0651025" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="76.1606" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0911676" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.225" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.88328E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18020" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.17E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04894" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.1E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.75E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2700000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="336400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5477000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.82526" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.345E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="16.174" />
-  <B value="-0.011629" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="63.98" />
-  <Tmax units="K"  value="159.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.98491" />
-  <B value="0.2613" />
-  <C value="536.61" />
-  <D value="0.28105" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="536.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.44938" />
-  <B value="-6196.556" />
-  <C value="-9.018418" />
-  <D value="0.0000073391" />
-  <E value="2" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="536.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.183879E+07" />
-  <B value="-0.0306824" />
-  <C value="1.010385" />
-  <D value="-0.640892" />
-  <E value="-0.0194755" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="516.78" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15951" />
-  <B value="1376.4" />
-  <C value="-8.0131" />
-  <D value="0.022215" />
-  <E value="8.4808E-07" />
-  <Tmin units="K"  value="18.62" />
-  <Tmax units="K"  value="136.69" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="104970" />
-  <B value="204.83" />
-  <C value="8.2793" />
-  <D value="0.0048108" />
-  <E value="0.0000020317" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="440" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="69258" />
-  <B value="-718.05" />
-  <C value="12.587" />
-  <D value="-0.000090812" />
-  <E value="1.349E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16509" />
-  <B value="-214.88" />
-  <C value="-18.784" />
-  <D value="-1765.2" />
-  <E value="1192.4" />
-  <Tmin units="K"  value="266.5" />
-  <Tmax units="K"  value="1599" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.6328" />
-  <B value="806.3" />
-  <C value="-0.3609" />
-  <D value="0.0000011977" />
-  <E value="2" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="340.87" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.0609E-07" />
-  <B value="0.72623" />
-  <C value="217.41" />
-  <D value="-10810" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.061115" />
-  <B value="3.3836" />
-  <C value="-1.3478" />
-  <D value="-0.00049487" />
-  <E value="-0.0000016211" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="340.87" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0088953" />
-  <B value="0.51444" />
-  <C value="2337.9" />
-  <D value="345110" />
-  <Tmin units="K"  value="340.87" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0074449" />
-  <B value="194.68" />
-  <C value="-5.0277" />
-  <D value="0.0075386" />
-  <E value="-0.000015012" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="516.78" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="18723" />
-  <B value="294.36" />
-  <C value="-0.1308" />
-  <D value="0.000019418" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-5.047" />
-  <B value="-2970" />
-  <C value="-17.82" />
-  <Tmin units="K"  value="270" />
-  <Tmax units="K"  value="440" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.949" />
-  <B value="2807" />
-  <C value="-42.818" />
-  <Tmin units="K"  value="322.03" />
-  <Tmax units="K"  value="477.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3587" />
-  <B value="-0.015176" />
-  <Tmin units="K"  value="159.95" />
-  <Tmax units="K"  value="340.87" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.260086" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.842493E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="289.6357" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.264" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="83.03201" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.09328" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0359885" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.84534" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.225" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0911676" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.2265" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.756" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.326" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.225" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18020" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0911676" />
-<UnifacVLE name="UNIFAC" >
-  <group id="61"  value="1" />
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="55"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="61"  value="1" />
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="60"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-03-9" />
-<Smiles name="SMILES"  value="CCCS" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1804" />
-<CompoundID name="Name"  value="Tert-butyl mercaptan" />
-<StructureFormula name="Structure"  value="C(CH3)3SH" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="530" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4060000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.307" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.283" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="337.37" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="274.26" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="274.42" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7907.71" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.1872" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.113524" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.191395" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.185E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15790" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05915" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.45E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.096E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1006000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="338000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2482000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.89359" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.9396E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.536" />
-  <B value="-0.0047128" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="109.7" />
-  <Tmax units="K"  value="274.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.89711" />
-  <B value="0.27544" />
-  <C value="530" />
-  <D value="0.31359" />
-  <Tmin units="K"  value="274.26" />
-  <Tmax units="K"  value="530" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="107.5154" />
-  <B value="-7030.549" />
-  <C value="-13.1586" />
-  <D value="0.0000127338" />
-  <E value="2" />
-  <Tmin units="K"  value="274.26" />
-  <Tmax units="K"  value="530" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.3137E+07" />
-  <B value="1.4502" />
-  <C value="-2.4713" />
-  <D value="2.4297" />
-  <E value="-0.95458" />
-  <Tmin units="K"  value="274.26" />
-  <Tmax units="K"  value="530" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19552" />
-  <B value="2145.8" />
-  <C value="-26.593" />
-  <D value="0.17311" />
-  <E value="-0.00034631" />
-  <Tmin units="K"  value="12.35" />
-  <Tmax units="K"  value="176.87" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="154160" />
-  <B value="506.03" />
-  <C value="1.848" />
-  <D value="0.027991" />
-  <E value="-0.000021961" />
-  <Tmin units="K"  value="274.26" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81989" />
-  <B value="-677.66" />
-  <C value="12.907" />
-  <D value="-0.00021031" />
-  <E value="4.8543E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15748" />
-  <B value="-135.94" />
-  <C value="-33.617" />
-  <D value="1896.4" />
-  <E value="-6191.8" />
-  <Tmin units="K"  value="262" />
-  <Tmax units="K"  value="1834" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.3337" />
-  <B value="1214.8" />
-  <C value="-0.59208" />
-  <D value="0.0000022318" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="337.37" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.9123E-07" />
-  <B value="0.6395" />
-  <C value="316.74" />
-  <D value="-8533.3" />
-  <Tmin units="K"  value="274.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.031454" />
-  <B value="-260.91" />
-  <C value="0.599" />
-  <D value="-0.0079027" />
-  <E value="0.0000031638" />
-  <Tmin units="K"  value="274.26" />
-  <Tmax units="K"  value="337.37" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.032499" />
-  <B value="0.31482" />
-  <C value="1562.3" />
-  <D value="775320" />
-  <Tmin units="K"  value="337.37" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.003175" />
-  <B value="737.78" />
-  <C value="-10.123" />
-  <D value="0.022698" />
-  <E value="-0.000032367" />
-  <Tmin units="K"  value="274.26" />
-  <Tmax units="K"  value="530" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="11171" />
-  <B value="439.34" />
-  <C value="-0.24387" />
-  <D value="0.000049974" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.422" />
-  <B value="-2740" />
-  <C value="-16.44" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="445" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.619" />
-  <B value="2629" />
-  <C value="-48.233" />
-  <Tmin units="K"  value="318.35" />
-  <Tmax units="K"  value="476.97" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3141" />
-  <B value="-0.013773" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="337.37" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.315937" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.725508E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="367.8072" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.283" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="122.489" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.862" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0427884" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.80482" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.191395" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.113524" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.3543" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.912" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="2.2573" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.191395" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15790" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.113524" />
-<Asog name="ASOG" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="55"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<CAS name="CAS number"  value="75-66-1" />
-<Smiles name="SMILES"  value="CC(C)(C)S" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1805" />
-<CompoundID name="Name"  value="Isobutyl mercaptan" />
-<StructureFormula name="Structure"  value="(CH3)2CHCH2SH" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="557" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3900000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.307" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.268" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="361.64" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="128.31" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="128.3" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="4.75023E-06" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.1872" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.108751" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.25" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.455E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17240" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.1E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05916" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.4528E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.694E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6100000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="362840" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="4982300" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.91991" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.949E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.835" />
-  <B value="-0.012799" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="51.32" />
-  <Tmax units="K"  value="128.31" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.97433" />
-  <B value="0.28543" />
-  <C value="557" />
-  <D value="0.30684" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="536.33" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="94.36165" />
-  <B value="-7005.04" />
-  <C value="-10.97315" />
-  <D value="8.971409E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="559" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.696233E+07" />
-  <B value="0.280539" />
-  <C value="0.393074" />
-  <D value="-0.340509" />
-  <E value="0.0160184" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="536.33" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14787" />
-  <B value="1720.7" />
-  <C value="-15.027" />
-  <D value="0.082237" />
-  <E value="-0.00013773" />
-  <Tmin units="K"  value="12.41" />
-  <Tmax units="K"  value="128.31" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="113680" />
-  <B value="117.72" />
-  <C value="9.1822" />
-  <D value="0.0046628" />
-  <E value="2.8876E-09" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="470" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83649" />
-  <B value="-694.35" />
-  <C value="12.849" />
-  <D value="-0.00014111" />
-  <E value="3.1023E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.19029" />
-  <B value="-182.14" />
-  <C value="-34.378" />
-  <D value="-7197.6" />
-  <E value="12309" />
-  <Tmin units="K"  value="271.5" />
-  <Tmax units="K"  value="1629" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.885" />
-  <B value="935.58" />
-  <C value="0.015703" />
-  <D value="-1.4837E-10" />
-  <E value="2" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="361.64" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.5691E-08" />
-  <B value="0.8336" />
-  <C value="119.56" />
-  <D value="-8012" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.03575" />
-  <B value="3.5477" />
-  <C value="-1.4952" />
-  <D value="-0.00050318" />
-  <E value="-0.0000017356" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="361.64" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00014532" />
-  <B value="0.98673" />
-  <C value="557.5" />
-  <D value="22542" />
-  <Tmin units="K"  value="361.64" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.019478" />
-  <B value="11.024" />
-  <C value="-2.7575" />
-  <D value="-0.00056011" />
-  <E value="-0.0000029228" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="536.33" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="18204" />
-  <B value="396.93" />
-  <C value="-0.19558" />
-  <D value="0.000034612" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.932" />
-  <B value="2967.3" />
-  <C value="-46.193" />
-  <Tmin units="K"  value="338.12" />
-  <Tmax units="K"  value="500" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0171" />
-  <B value="-0.018678" />
-  <Tmin units="K"  value="128.31" />
-  <Tmax units="K"  value="361.64" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.315992" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.112178E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="317.7267" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.268" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="101.556" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.55718" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0427712" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.83847" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.25" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.108751" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9001" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.292" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2753" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.25" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17240" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.108751" />
-<UnifacVLE name="UNIFAC" >
-  <group id="61"  value="1" />
-  <group id="3"  value="1" />
-  <group id="1"  value="2" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="55"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="61"  value="1" />
-  <group id="3"  value="1" />
-  <group id="1"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="60"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="513-44-0" />
-<Smiles name="SMILES"  value="CC(C)CS" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1806" />
-<CompoundID name="Name"  value="Sec-butyl mercaptan" />
-<StructureFormula name="Structure"  value="CH3CH2CH(SH)CH3" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="551" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3970000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.307" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.271" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="358.13" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="133.01" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="133.01" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0000339902" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.1872" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10943" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.25" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.362E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17000" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.17E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05916" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.45E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.66E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="5200000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="366730" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6477000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.85933" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.95E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.628" />
-  <B value="-0.011085" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="53.21" />
-  <Tmax units="K"  value="133.02" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.81743" />
-  <B value="0.26237" />
-  <C value="554.01" />
-  <D value="0.28149" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="554" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="85.20348" />
-  <B value="-6580.804" />
-  <C value="-9.568603" />
-  <D value="0.0000075683" />
-  <E value="2" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="554" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.567571E+07" />
-  <B value="0.16352" />
-  <C value="0.885588" />
-  <D value="-1.131485" />
-  <E value="0.438377" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="531.84" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14348" />
-  <B value="1684.2" />
-  <C value="-14.306" />
-  <D value="0.073175" />
-  <E value="-0.00012364" />
-  <Tmin units="K"  value="12.44" />
-  <Tmax units="K"  value="133.02" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="132220" />
-  <B value="286.96" />
-  <C value="6.629" />
-  <D value="0.011753" />
-  <E value="-0.0000059086" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="470" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85634" />
-  <B value="-697.09" />
-  <C value="12.792" />
-  <D value="-0.00003836" />
-  <E value="-5.0229E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15286" />
-  <B value="-191.11" />
-  <C value="-37.033" />
-  <D value="3742.9" />
-  <E value="-12255" />
-  <Tmin units="K"  value="270.5" />
-  <Tmax units="K"  value="1623" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.718" />
-  <B value="953.76" />
-  <C value="0.15985" />
-  <D value="-4.5581E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="358.13" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.4539E-08" />
-  <B value="0.83594" />
-  <C value="117.21" />
-  <D value="-7872.1" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.032852" />
-  <B value="4.221" />
-  <C value="-1.5207" />
-  <D value="-0.0004702" />
-  <E value="-0.0000018598" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="358.13" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.97519" />
-  <B value="-0.11286" />
-  <C value="1130.7" />
-  <D value="3149700" />
-  <Tmin units="K"  value="358.13" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016327" />
-  <B value="13.06" />
-  <C value="-2.6627" />
-  <D value="-0.0011001" />
-  <E value="-0.0000030132" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="531.84" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="22301" />
-  <B value="378.69" />
-  <C value="-0.16891" />
-  <D value="0.000025206" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.77" />
-  <B value="-2825" />
-  <C value="-16.95" />
-  <Tmin units="K"  value="270" />
-  <Tmax units="K"  value="440" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.911" />
-  <B value="2934.9" />
-  <C value="-45.402" />
-  <Tmin units="K"  value="332.43" />
-  <Tmax units="K"  value="490" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.1814" />
-  <B value="-0.018144" />
-  <Tmin units="K"  value="133.02" />
-  <Tmax units="K"  value="358.13" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.315992" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.031073E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="327.1555" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.271" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="111.786" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.042761" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.83338" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.25" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10943" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.1276" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.604" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.25" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17000" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.10943" />
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="55"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<CAS name="CAS number"  value="513-53-1" />
-<Smiles name="SMILES"  value="CC(S)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1807" />
-<CompoundID name="Name"  value="N-hexyl mercaptan" />
-<StructureFormula name="Structure"  value="CH3(CH2)5SH" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="622" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3025000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.412" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.245" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="424.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="192.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="192.62" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0130959" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="118.24" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.141006" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.369" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.252E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17450" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.17E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07963" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.12E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.292E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.77E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="454600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.801E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.03043" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.176E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.9499" />
-  <B value="-0.0064569" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="77.05" />
-  <Tmax units="K"  value="192.62" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.60827" />
-  <B value="0.26212" />
-  <C value="623.01" />
-  <D value="0.27785" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="623" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="102.0208" />
-  <B value="-8530.272" />
-  <C value="-11.91139" />
-  <D value="8.521739E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="623" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.053718E+07" />
-  <B value="0.532372" />
-  <C value="-0.222059" />
-  <D value="0.0696209" />
-  <E value="-0.00101028" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="600.35" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19026" />
-  <B value="1622.7" />
-  <C value="-5.5711" />
-  <D value="-0.0016101" />
-  <E value="0.00005357" />
-  <Tmin units="K"  value="16.73" />
-  <Tmax units="K"  value="186.33" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="168110" />
-  <B value="243.92" />
-  <C value="7.741" />
-  <D value="0.0099925" />
-  <E value="-0.0000054522" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="510" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="116170" />
-  <B value="-711.75" />
-  <C value="13.18" />
-  <D value="-0.000044297" />
-  <E value="1.0562E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28791" />
-  <B value="-359.98" />
-  <C value="-70.803" />
-  <D value="-33240" />
-  <E value="54069" />
-  <Tmin units="K"  value="311.5" />
-  <Tmax units="K"  value="1991.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-35.723" />
-  <B value="1823.3" />
-  <C value="4.0853" />
-  <D value="-0.0000098564" />
-  <E value="2" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="425.81" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.7616E-08" />
-  <B value="0.85134" />
-  <C value="101.57" />
-  <D value="-4277.1" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.076932" />
-  <B value="5.5076" />
-  <C value="-1.3601" />
-  <D value="-0.00033003" />
-  <E value="-0.000001155" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="425.81" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.090806" />
-  <B value="0.27994" />
-  <C value="4707" />
-  <D value="1982000" />
-  <Tmin units="K"  value="425.81" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.043732" />
-  <B value="-13.608" />
-  <C value="-2.1183" />
-  <D value="-0.001643" />
-  <E value="5.7805E-08" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="600.35" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="23098" />
-  <B value="542.53" />
-  <C value="-0.23254" />
-  <D value="0.000032568" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.988" />
-  <B value="3419.8" />
-  <C value="-64.357" />
-  <Tmin units="K"  value="373.83" />
-  <Tmax units="K"  value="555.05" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0571" />
-  <B value="-0.013495" />
-  <Tmin units="K"  value="192.62" />
-  <Tmax units="K"  value="425.81" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.432645" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.508354E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="256.863" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.245" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="137.185" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0570385" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.84617" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.369" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.141006" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2497" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.376" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.369" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17450" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.141006" />
-<UnifacVLE name="UNIFAC" >
-  <group id="61"  value="1" />
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="55"  value="1" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="1"  value="1" />
-  <group id="2"  value="5" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="61"  value="1" />
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="60"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-31-9" />
-<Smiles name="SMILES"  value="CCCCCCS" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1813" />
-<CompoundID name="Name"  value="Methyl ethyl sulfide" />
-<StructureFormula name="Structure"  value="CH3SC2H5" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="533" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4260000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.26" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="339.8" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="167.24" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="167.23" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.224563" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="76.163" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.09102" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.208" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.846E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18010" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.34E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04837" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.89E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.93E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.19E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="332100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9761000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.78709" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.3531E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="16.219" />
-  <B value="-0.012123" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="66.89" />
-  <Tmax units="K"  value="167.23" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.067" />
-  <B value="0.27102" />
-  <C value="533" />
-  <D value="0.29364" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="533" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="84.44792" />
-  <B value="-6287.173" />
-  <C value="-9.497514" />
-  <D value="8.101952E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="533" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.1014E+07" />
-  <B value="1.045" />
-  <C value="-1.3834" />
-  <D value="1.1914" />
-  <E value="-0.41055" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="533" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-19284" />
-  <B value="1609.7" />
-  <C value="-10.685" />
-  <D value="0.036633" />
-  <E value="-0.000038883" />
-  <Tmin units="K"  value="17.79" />
-  <Tmax units="K"  value="161.43" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="128430" />
-  <B value="1340.2" />
-  <C value="-7.9347" />
-  <D value="0.062009" />
-  <E value="-0.00006022" />
-  <Tmin units="K"  value="147.21" />
-  <Tmax units="K"  value="339.8" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65018" />
-  <B value="-602.45" />
-  <C value="12.269" />
-  <D value="0.00023938" />
-  <E value="-9.0299E-08" />
-  <Tmin units="K"  value="273.16" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12321" />
-  <B value="-136.78" />
-  <C value="-37.817" />
-  <D value="13559" />
-  <E value="-38648" />
-  <Tmin units="K"  value="266.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.137" />
-  <B value="871.68" />
-  <C value="0.048227" />
-  <D value="-1.2198E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="339.8" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.5396E-07" />
-  <B value="0.76205" />
-  <C value="156.76" />
-  <D value="-5273.3" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.050172" />
-  <B value="-1.1207" />
-  <C value="-1.3208" />
-  <D value="-0.00082247" />
-  <E value="-0.0000013076" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="339.8" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0034168" />
-  <B value="0.62158" />
-  <C value="1811.6" />
-  <D value="162180" />
-  <Tmin units="K"  value="339.8" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010255" />
-  <B value="52.377" />
-  <C value="-3.2511" />
-  <D value="0.0012494" />
-  <E value="-0.0000074687" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="533" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="23414" />
-  <B value="242.67" />
-  <C value="0.067098" />
-  <D value="-0.00024012" />
-  <E value="1.1017E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.758" />
-  <B value="2662.3" />
-  <C value="-51.408" />
-  <Tmin units="K"  value="321.07" />
-  <Tmax units="K"  value="475.25" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.5661" />
-  <B value="-0.014639" />
-  <Tmin units="K"  value="167.23" />
-  <Tmax units="K"  value="339.8" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.257003" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.286005E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="236.7143" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="83.45" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.02863" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0358611" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.84695" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.208" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.09102" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.1885" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.756" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0.36781" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.208" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18010" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.09102" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="102"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="102"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="123"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="624-89-5" />
-<Smiles name="SMILES"  value="CSCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1814" />
-<CompoundID name="Name"  value="Methyl n-propyl sulfide" />
-<StructureFormula name="Structure"  value="CH3SCH2CH2CH3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="552" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.322" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="368.69" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="160.17" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="160.17" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00425588" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.1872" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.107699" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.356915" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.373E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17710" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0586" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.24E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-8.19E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.793E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="371700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9912000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.01" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.962E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="13.682" />
-  <B value="-0.010678" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="64.07" />
-  <Tmax units="K"  value="160.17" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.528" />
-  <B value="0.35328" />
-  <C value="552" />
-  <D value="0.39953" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="543.69" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="83.78969" />
-  <B value="-6786.538" />
-  <C value="-9.267875" />
-  <D value="6.742312E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="565" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.460643E+07" />
-  <B value="0.610381" />
-  <C value="0.183873" />
-  <D value="-0.864255" />
-  <E value="0.448129" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="543.69" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13278" />
-  <B value="1215" />
-  <C value="-0.30808" />
-  <D value="-0.046796" />
-  <E value="0.00019076" />
-  <Tmin units="K"  value="16.47" />
-  <Tmax units="K"  value="150.37" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="140680" />
-  <B value="477.81" />
-  <C value="3.8109" />
-  <D value="0.020949" />
-  <E value="-0.000014877" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="368.69" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="76201" />
-  <B value="-575.5" />
-  <C value="12.472" />
-  <D value="0.00030373" />
-  <E value="-1.0224E-07" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.08111" />
-  <B value="-68.911" />
-  <C value="-77.365" />
-  <D value="58267" />
-  <E value="-161420" />
-  <Tmin units="K"  value="282.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.683" />
-  <B value="983.43" />
-  <C value="0.11996" />
-  <D value="-4.1262E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="368.69" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.4928E-08" />
-  <B value="0.89154" />
-  <C value="78.07" />
-  <D value="-5628.6" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.062059" />
-  <B value="3.0814" />
-  <C value="-1.3629" />
-  <D value="-0.00055214" />
-  <E value="-0.0000012783" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="368.69" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0023304" />
-  <B value="0.67586" />
-  <C value="1803.3" />
-  <D value="153300" />
-  <Tmin units="K"  value="368.69" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0070237" />
-  <B value="92.745" />
-  <C value="-3.8705" />
-  <D value="0.0035687" />
-  <E value="-0.000010748" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="543.69" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="16136" />
-  <B value="391.22" />
-  <C value="-0.18441" />
-  <D value="0.000032898" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.984" />
-  <B value="3002.5" />
-  <C value="-51.221" />
-  <Tmin units="K"  value="331.82" />
-  <Tmax units="K"  value="479.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9627" />
-  <B value="-0.015623" />
-  <Tmin units="K"  value="160.17" />
-  <Tmax units="K"  value="368.69" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.312895" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.469994E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="278.4399" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="101.501" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0423566" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.84676" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.356915" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.107699" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.8629" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.296" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.273669" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17710" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.107699" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="102"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="102"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="123"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="3877-15-4" />
-<Smiles name="SMILES"  value="CSCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1815" />
-<CompoundID name="Name"  value="Methyl t-butyl sulfide" />
-<StructureFormula name="Structure"  value="CH3SC(CH3)3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="585" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.37" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="372.048" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="190.84" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="190.84" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.818336" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="104.214" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12697" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.107514" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.509E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16230" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06881" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.78E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.209E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="7400000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8414000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.67" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.558E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="11.206" />
-  <B value="-0.0073401" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="76.34" />
-  <Tmax units="K"  value="190.84" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.0025324" />
-  <B value="0.015967" />
-  <C value="585" />
-  <D value="0.080614" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="570" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="84.46516" />
-  <B value="-6786.586" />
-  <C value="-9.396892" />
-  <D value="6.668285E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="570" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.776086E+07" />
-  <B value="2.156989" />
-  <C value="-4.009149" />
-  <D value="3.630339" />
-  <E value="-1.236406" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="570" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-8544.9" />
-  <B value="1449.1" />
-  <C value="-8.766" />
-  <D value="0.039746" />
-  <E value="-0.000061947" />
-  <Tmin units="K"  value="20.74" />
-  <Tmax units="K"  value="180.54" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="141210" />
-  <B value="178.65" />
-  <C value="7.6994" />
-  <D value="0.011393" />
-  <E value="-0.0000080501" />
-  <Tmin units="K"  value="189.96" />
-  <Tmax units="K"  value="372.05" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="87862" />
-  <B value="-573.15" />
-  <C value="12.832" />
-  <D value="0.000097962" />
-  <E value="-4.8038E-08" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2108" />
-  <B value="-261.12" />
-  <C value="-41.45" />
-  <D value="-6872.1" />
-  <E value="24062" />
-  <Tmin units="K"  value="330.2" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.768" />
-  <B value="996.37" />
-  <C value="0.0046964" />
-  <D value="-1.0865E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="372.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4934E-07" />
-  <B value="0.74231" />
-  <C value="170.99" />
-  <D value="-8263.5" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.049324" />
-  <B value="-5.479" />
-  <C value="-1.3559" />
-  <D value="-0.00091706" />
-  <E value="-9.5073E-07" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="372.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016838" />
-  <B value="0.95767" />
-  <C value="599.31" />
-  <D value="12993" />
-  <Tmin units="K"  value="372.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.025531" />
-  <B value="-17.805" />
-  <C value="-2.276" />
-  <D value="-0.0022145" />
-  <E value="-2.4544E-07" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="570" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="7260" />
-  <B value="545.25" />
-  <C value="-0.30907" />
-  <D value="0.000066341" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.736" />
-  <B value="2954" />
-  <C value="-51.303" />
-  <Tmin units="K"  value="351.19" />
-  <Tmax units="K"  value="510.13" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.2409" />
-  <B value="-0.01354" />
-  <Tmin units="K"  value="190.84" />
-  <Tmax units="K"  value="372.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.3701" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.475542E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="338.2028" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="118.727" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0497028" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.82938" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.107514" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.12697" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5358" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.912" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.233365" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16230" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.12697" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="102"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="102"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="4"  value="1" />
-  <group id="122"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="6163-64-0" />
-<Smiles name="SMILES"  value="CSC(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1816" />
-<CompoundID name="Name"  value="Methyl t-pentyl sulfide" />
-<StructureFormula name="Structure"  value="CH3SC(CH3)(CH3)C2H5" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="632" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3130000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.412" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.259" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="401.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="195" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="195" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0547032" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="118.24" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.141236" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.283554" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.988E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16850" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07904" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.113E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.374E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.884E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="422900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8320000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.171E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.916" />
-  <B value="-0.0063564" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="78" />
-  <Tmax units="K"  value="195" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.59566" />
-  <B value="0.25918" />
-  <C value="632" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="632" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="71.41151" />
-  <B value="-7073.516" />
-  <C value="-7.244729" />
-  <D value="3.628693E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="632" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.4045E+07" />
-  <B value="0.37325" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="632" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-20380" />
-  <B value="1924" />
-  <C value="-10.285" />
-  <D value="0.022612" />
-  <E value="0.00003528" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="150" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="181970" />
-  <B value="283.58" />
-  <C value="5.3016" />
-  <D value="0.020294" />
-  <E value="-0.000016827" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="474" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="109660" />
-  <B value="-656.23" />
-  <C value="13.164" />
-  <D value="-0.000084618" />
-  <E value="-5.7336E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28156" />
-  <B value="-377.98" />
-  <C value="-67.102" />
-  <D value="-17004" />
-  <E value="6836.4" />
-  <Tmin units="K"  value="316" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.248" />
-  <B value="1169.1" />
-  <C value="-0.00088104" />
-  <D value="1.198E-09" />
-  <E value="2" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="423" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.9322E-08" />
-  <B value="0.79515" />
-  <C value="142.11" />
-  <D value="-9151.1" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.059845" />
-  <B value="-0.6973" />
-  <C value="-1.3681" />
-  <D value="-0.00062696" />
-  <E value="-0.0000008708" />
-  <Tmin units="K"  value="155" />
-  <Tmax units="K"  value="423" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00014528" />
-  <B value="0.96627" />
-  <C value="637.8" />
-  <D value="13351" />
-  <Tmin units="K"  value="423" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0084476" />
-  <B value="63" />
-  <C value="-3.4305" />
-  <D value="0.0011072" />
-  <E value="-0.0000054381" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="632" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="2393.4" />
-  <B value="652.33" />
-  <C value="-0.3793" />
-  <D value="0.000081492" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.825" />
-  <B value="3408.7" />
-  <C value="-56.194" />
-  <Tmin units="K"  value="402" />
-  <Tmax units="K"  value="563" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0728" />
-  <B value="-0.013528" />
-  <Tmin units="K"  value="195" />
-  <Tmax units="K"  value="423" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.429177" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.023997E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="318.7935" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="136.778" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0566345" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.84466" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.283554" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.141236" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2102" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.452" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.283554" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="16850" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.141236" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="102"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="3" />
-  <group id="2"  value="1" />
-  <group id="4"  value="1" />
-  <group id="102"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="13286-92-5" />
-<Smiles name="SMILES"  value="CSC(C)(C)CC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1817" />
-<CompoundID name="Name"  value="Di-n-propyl sulfide" />
-<StructureFormula name="Structure"  value="CH3CH2CH2SCH2CH2CH3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="608" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3080000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.412" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="415.978" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="170.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="170.44" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000440358" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="118.24" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.141918" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.374042" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.089E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17110" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07906" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.094E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.254E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.15E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="447000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.214E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.1801E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="10.099" />
-  <B value="-0.0074068" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="68.18" />
-  <Tmax units="K"  value="170.44" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.66296" />
-  <B value="0.27313" />
-  <C value="608" />
-  <D value="0.29224" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="584.97" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="149.6373" />
-  <B value="-10251.56" />
-  <C value="-19.3067" />
-  <D value="0.0000171365" />
-  <E value="2" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="608" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.7575E+07" />
-  <B value="0.38334" />
-  <C value="0.098397" />
-  <D value="-0.17233" />
-  <E value="0.065159" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="584.97" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-13983" />
-  <B value="1523.9" />
-  <C value="-1.9419" />
-  <D value="-0.047401" />
-  <E value="0.00023576" />
-  <Tmin units="K"  value="14.29" />
-  <Tmax units="K"  value="165.34" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="165300" />
-  <B value="330.45" />
-  <C value="6.4516" />
-  <D value="0.01426" />
-  <E value="-0.000009041" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="375" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="105470" />
-  <B value="-659.93" />
-  <C value="13.199" />
-  <D value="-0.00015" />
-  <E value="2.3041E-08" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27779" />
-  <B value="-335.64" />
-  <C value="-67.213" />
-  <D value="-19481" />
-  <E value="17068" />
-  <Tmin units="K"  value="304" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.285" />
-  <B value="1150.9" />
-  <C value="-0.17064" />
-  <D value="6.2281E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="415.98" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.5739E-08" />
-  <B value="0.838" />
-  <C value="116.99" />
-  <D value="-6475.6" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.078109" />
-  <B value="7.1733" />
-  <C value="-1.4231" />
-  <D value="-0.000097639" />
-  <E value="-0.0000015465" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="415.98" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0086151" />
-  <B value="0.48706" />
-  <C value="1648.6" />
-  <D value="489220" />
-  <Tmin units="K"  value="415.98" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016747" />
-  <B value="16.881" />
-  <C value="-2.7667" />
-  <D value="-0.00076737" />
-  <E value="-0.000002493" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="584.97" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="541.13" />
-  <B value="648.44" />
-  <C value="-0.38084" />
-  <D value="0.00008351" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.969" />
-  <B value="3327.3" />
-  <C value="-63.661" />
-  <Tmin units="K"  value="367.71" />
-  <Tmax units="K"  value="538.91" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4507" />
-  <B value="-0.015523" />
-  <Tmin units="K"  value="170.44" />
-  <Tmax units="K"  value="415.98" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.429295" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.293494E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="273.9316" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.251" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="140.034" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0565316" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.84105" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.374042" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.141918" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2117" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.376" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.374042" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17110" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.141918" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="103"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="103"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="123"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-47-7" />
-<Smiles name="SMILES"  value="CCCSCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1818" />
-<CompoundID name="Name"  value="Diethyl sulfide" />
-<StructureFormula name="Structure"  value="CH3CH2SCH2CH3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="557" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3960000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.318" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.269" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="365.25" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="169.22" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="169.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.099321" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.189" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.10851" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.295" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.212E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17490" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.14E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0586" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.24E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-8.347E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.778E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="368000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.19035E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.90128" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.9607E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.811" />
-  <B value="-3.1253E-09" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="83.15" />
-  <Tmax units="K"  value="92.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.71845" />
-  <B value="0.24674" />
-  <C value="557.16" />
-  <D value="0.25292" />
-  <Tmin units="K"  value="169.2" />
-  <Tmax units="K"  value="557.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="70.99138" />
-  <B value="-6108.92" />
-  <C value="-7.37143" />
-  <D value="5.835752E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="169.2" />
-  <Tmax units="K"  value="557.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.6317E+07" />
-  <B value="0.40563" />
-  <C value="-0.17525" />
-  <D value="0.12561" />
-  <E value="0.018959" />
-  <Tmin units="K"  value="169.2" />
-  <Tmax units="K"  value="536.73" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11543" />
-  <B value="1074.2" />
-  <C value="-1.061" />
-  <D value="-0.019344" />
-  <E value="0.000072553" />
-  <Tmin units="K"  value="15.97" />
-  <Tmax units="K"  value="159.4" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="145900" />
-  <B value="1485.7" />
-  <C value="-9.9348" />
-  <D value="0.077005" />
-  <E value="-0.000088463" />
-  <Tmin units="K"  value="181.95" />
-  <Tmax units="K"  value="322.08" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84916" />
-  <B value="-751.54" />
-  <C value="12.969" />
-  <D value="-0.00026179" />
-  <E value="6.4336E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16441" />
-  <B value="-234.17" />
-  <C value="-39.709" />
-  <D value="11874" />
-  <E value="-35686" />
-  <Tmin units="K"  value="278.5" />
-  <Tmax units="K"  value="1949.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-2.9987" />
-  <B value="606.92" />
-  <C value="-1.2077" />
-  <D value="8.2651E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="365.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.8477E-08" />
-  <B value="0.85168" />
-  <C value="55.152" />
-  <D value="236.99" />
-  <Tmin units="K"  value="169.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.07619" />
-  <B value="7.9978" />
-  <C value="-1.3835" />
-  <D value="-0.00020735" />
-  <E value="-0.0000016592" />
-  <Tmin units="K"  value="169.2" />
-  <Tmax units="K"  value="365.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0017352" />
-  <B value="0.67658" />
-  <C value="1116.5" />
-  <D value="181260" />
-  <Tmin units="K"  value="365.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014023" />
-  <B value="40.038" />
-  <C value="-3.1023" />
-  <D value="0.00060236" />
-  <E value="-0.0000051915" />
-  <Tmin units="K"  value="169.2" />
-  <Tmax units="K"  value="536.73" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="36043" />
-  <B value="216.86" />
-  <C value="0.32917" />
-  <D value="-0.00057212" />
-  <E value="2.4112E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.458" />
-  <B value="-2860" />
-  <C value="-17.16" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.747" />
-  <B value="3457.8" />
-  <C value="-26.458" />
-  <Tmin units="K"  value="337.07" />
-  <Tmax units="K"  value="495.89" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.6508" />
-  <B value="-0.01037" />
-  <Tmin units="K"  value="225" />
-  <Tmax units="K"  value="365.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.312895" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.156747E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="322.0153" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.269" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="103.932" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0429092" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.837" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.295" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.10851" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.8629" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.296" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.295" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17490" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.10851" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="103"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="103"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="123"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="352-93-2" />
-<Smiles name="SMILES"  value="CCSCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1824" />
-<CompoundID name="Name"  value="Diethyl disulfide" />
-<StructureFormula name="Structure"  value="C2H5SSC2H5" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="642" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3870000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.358" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="427.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="171.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="171.64" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000220562" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="122.252" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.12376" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.346925" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.615E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18630" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.54E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0705" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.47E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.301E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9406000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.257E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.385" />
-  <B value="-0.0073655" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="68.65" />
-  <Tmax units="K"  value="171.63" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77633" />
-  <B value="0.27774" />
-  <C value="642" />
-  <D value="0.3008" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="642" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="177.1651" />
-  <B value="-11358.16" />
-  <C value="-23.65597" />
-  <D value="0.0000232121" />
-  <E value="2" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="642" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.898575E+07" />
-  <B value="0.279736" />
-  <C value="0.523521" />
-  <D value="-0.500907" />
-  <E value="0.0214669" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="642" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16428" />
-  <B value="1949.1" />
-  <C value="-14.93" />
-  <D value="0.073624" />
-  <E value="-0.00014251" />
-  <Tmin units="K"  value="34.92" />
-  <Tmax units="K"  value="152.34" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="184820" />
-  <B value="1402.4" />
-  <C value="-9.485" />
-  <D value="0.072797" />
-  <E value="-0.00007939" />
-  <Tmin units="K"  value="168.17" />
-  <Tmax units="K"  value="299.3" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="100900" />
-  <B value="-621.21" />
-  <C value="12.713" />
-  <D value="-0.0000050655" />
-  <E value="-1.705E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22999" />
-  <B value="-298.83" />
-  <C value="-65.123" />
-  <D value="-33026" />
-  <E value="42588" />
-  <Tmin units="K"  value="321" />
-  <Tmax units="K"  value="1761" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-12.559" />
-  <B value="1373.4" />
-  <C value="0.15118" />
-  <D value="-3.7692E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="427.13" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.5143E-08" />
-  <B value="0.87157" />
-  <C value="110.73" />
-  <D value="-9132.4" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.047803" />
-  <B value="3.9799" />
-  <C value="-1.4697" />
-  <D value="-0.00042308" />
-  <E value="-0.0000011998" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="427.14" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00017171" />
-  <B value="0.93356" />
-  <C value="610.03" />
-  <D value="20030" />
-  <Tmin units="K"  value="427.14" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010614" />
-  <B value="45.537" />
-  <C value="-3.1313" />
-  <D value="0.00068508" />
-  <E value="-0.0000047035" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="642" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="35231" />
-  <B value="424.66" />
-  <C value="-0.23005" />
-  <D value="0.000046108" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.962" />
-  <B value="3433.2" />
-  <C value="-63.337" />
-  <Tmin units="K"  value="386.78" />
-  <Tmax units="K"  value="567.73" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.6558" />
-  <B value="-0.01741" />
-  <Tmin units="K"  value="171.63" />
-  <Tmax units="K"  value="427.13" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.379729" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.671723E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="328.3615" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="115.933" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0515886" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.997" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.346925" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.12376" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.5748" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.816" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.346925" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18630" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.12376" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="103"  value="2" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="103"  value="2" />
-  </Umr>
-<CAS name="CAS number"  value="110-81-6" />
-<Smiles name="SMILES"  value="CCSSCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1828" />
-<CompoundID name="Name"  value="Dimethyl disulfide" />
-<StructureFormula name="Structure"  value="CH3SSCH3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="606" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5360000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.252" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.264" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="382.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="188.44" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="188.44" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.207156" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="94.199" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0890926" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.266353" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.942E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20060" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.57E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05004" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.25E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.35978E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.53553E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="336686" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9192000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.88" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.04376E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.732" />
-  <B value="-0.0091284" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="75.38" />
-  <Tmax units="K"  value="188.44" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0289" />
-  <B value="0.26919" />
-  <C value="615.01" />
-  <D value="0.29771" />
-  <Tmin units="K"  value="188.44" />
-  <Tmax units="K"  value="615" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.238" />
-  <B value="-6951.5" />
-  <C value="-8.8055" />
-  <D value="0.0000055663" />
-  <E value="2" />
-  <Tmin units="K"  value="188.44" />
-  <Tmax units="K"  value="615" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.473869E+07" />
-  <B value="0.511523" />
-  <C value="0.456682" />
-  <D value="-1.152343" />
-  <E value="0.579651" />
-  <Tmin units="K"  value="188.43" />
-  <Tmax units="K"  value="592.55" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-15381" />
-  <B value="1506.8" />
-  <C value="-8.7556" />
-  <D value="0.024969" />
-  <E value="-0.000016391" />
-  <Tmin units="K"  value="18.3" />
-  <Tmax units="K"  value="181.17" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="143050" />
-  <B value="-21950" />
-  <C value="190.58" />
-  <D value="-0.51509" />
-  <E value="0.00050194" />
-  <Tmin units="K"  value="188.44" />
-  <Tmax units="K"  value="360" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="74603" />
-  <B value="-691.43" />
-  <C value="12.21" />
-  <D value="-0.0000028522" />
-  <E value="-1.9217E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="-0.27433" />
-  <B value="338.25" />
-  <C value="-157.11" />
-  <D value="213460" />
-  <E value="-611370" />
-  <Tmin units="K"  value="307.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.014" />
-  <B value="1197" />
-  <C value="-0.085106" />
-  <D value="2.8649E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="188.43" />
-  <Tmax units="K"  value="382.9" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.8221E-08" />
-  <B value="0.86272" />
-  <C value="109.17" />
-  <D value="-8364.4" />
-  <Tmin units="K"  value="188.43" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.035195" />
-  <B value="-0.25311" />
-  <C value="-1.4287" />
-  <D value="-0.00064815" />
-  <E value="-0.0000012773" />
-  <Tmin units="K"  value="188.43" />
-  <Tmax units="K"  value="382.9" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00022814" />
-  <B value="0.8901" />
-  <C value="687.63" />
-  <D value="4695.8" />
-  <Tmin units="K"  value="382.9" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012015" />
-  <B value="66.606" />
-  <C value="-3.1743" />
-  <D value="0.0012491" />
-  <E value="-0.0000059034" />
-  <Tmin units="K"  value="188.43" />
-  <Tmax units="K"  value="592.55" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="38217" />
-  <B value="216.65" />
-  <C value="-0.095516" />
-  <D value="0.00001376" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-8.22" />
-  <B value="-4800" />
-  <C value="-28.8" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.015" />
-  <B value="3141.5" />
-  <C value="-51.826" />
-  <Tmin units="K"  value="364.43" />
-  <Tmax units="K"  value="525.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.4373" />
-  <B value="-0.01633" />
-  <Tmin units="K"  value="188.43" />
-  <Tmax units="K"  value="382.9" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.266045" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.827118E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="327.4613" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.264" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="74.969" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0377667" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.06743" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.266353" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0890926" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.226" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.736" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.205916" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20060" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0890926" />
-<UnifacVLE name="UNIFAC" >
-  <group id="102"  value="2" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="102"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="201"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="624-92-0" />
-<Smiles name="SMILES"  value="CSSC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1829" />
-<CompoundID name="Name"  value="Di-n-propyl disulfide" />
-<StructureFormula name="Structure"  value="CH3CH2CH2SSCH2CH2CH3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="727.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3009350" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.518" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="466.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="187.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="187.66" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000767693" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="150.305" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.157229" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.142024" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.414E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17950" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.6E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08986" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.224E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.173E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.849E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="490000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.381E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.65" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.53027E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="8.9128" />
-  <B value="-0.0059368" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="75.06" />
-  <Tmax units="K"  value="187.66" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.0083051" />
-  <B value="0.032244" />
-  <C value="727.15" />
-  <D value="0.12866" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="675" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="37.30305" />
-  <B value="-7362.883" />
-  <C value="-1.323142" />
-  <D value="-8.891834E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="675" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.27924E+07" />
-  <B value="-0.627848" />
-  <C value="2.812662" />
-  <D value="-3.633008" />
-  <E value="1.997715" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="675" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-23050" />
-  <B value="2146.3" />
-  <C value="-10.296" />
-  <D value="0.017948" />
-  <E value="0.000028517" />
-  <Tmin units="K"  value="16.53" />
-  <Tmax units="K"  value="175.02" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="195280" />
-  <B value="206.99" />
-  <C value="8.2539" />
-  <D value="0.0083402" />
-  <E value="-0.0000036311" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="469" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="135200" />
-  <B value="-728.45" />
-  <C value="13.4" />
-  <D value="-0.00037376" />
-  <E value="9.4294E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30698" />
-  <B value="-389.94" />
-  <C value="-117.39" />
-  <D value="-56995" />
-  <E value="52423" />
-  <Tmin units="K"  value="337.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.576" />
-  <B value="1437.8" />
-  <C value="-0.35065" />
-  <D value="0.0000011166" />
-  <E value="2" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="469" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.2944E-08" />
-  <B value="0.86495" />
-  <C value="121.54" />
-  <D value="-9663.6" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.066065" />
-  <B value="4.827" />
-  <C value="-1.4132" />
-  <D value="-0.00039942" />
-  <E value="-9.1868E-07" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="469" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00015595" />
-  <B value="0.95139" />
-  <C value="651.61" />
-  <D value="14665" />
-  <Tmin units="K"  value="469" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010484" />
-  <B value="73.954" />
-  <C value="-3.3578" />
-  <D value="0.0010428" />
-  <E value="-0.0000040493" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="675" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="30077" />
-  <B value="631.46" />
-  <C value="-0.35924" />
-  <D value="0.000074548" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.097" />
-  <B value="4581.5" />
-  <C value="-35.467" />
-  <Tmin units="K"  value="439.75" />
-  <Tmax units="K"  value="649.35" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.6086" />
-  <B value="-0.01566" />
-  <Tmin units="K"  value="187.66" />
-  <Tmax units="K"  value="469" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.493908" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.909704E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="322.9395" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.035" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0694742" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.955" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.0836846" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.157229" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.9236" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.896" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.436981" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17950" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.157229" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="103"  value="2" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="103"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="201"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="629-19-6" />
-<Smiles name="SMILES"  value="CCCSSCCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="3801" />
-<CompoundID name="Name"  value="Di-tert-butyl disulfide" />
-<StructureFormula name="Structure"  value="(CH3)3CS2C(CH3)3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="689.7" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3159000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.518" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.285" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="473.6" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="268.2" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="268.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="9.12" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="178.359" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1947" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.402005" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.686E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15680" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1126" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.457E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.998E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.427E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="500100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.31E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.665E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="6.7119" />
-  <B value="-0.0031282" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="107.28" />
-  <Tmax units="K"  value="268.2" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.60778" />
-  <B value="0.31522" />
-  <C value="689.7" />
-  <D value="0.2884" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="689.7" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="113.63" />
-  <B value="-10180" />
-  <C value="-13.332" />
-  <D value="0.0000068178" />
-  <E value="2" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="689.7" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.0039E+07" />
-  <B value="-1.4285" />
-  <C value="5.5884" />
-  <D value="-6.8503" />
-  <E value="3.0089" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="689.7" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="3730" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="268.2" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="273850" />
-  <B value="-799.3" />
-  <C value="13.794" />
-  <D value="-0.001521" />
-  <E value="0.0000014598" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="689.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="171300" />
-  <B value="-806" />
-  <C value="13.98" />
-  <D value="-0.00069575" />
-  <E value="1.6372E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.3107" />
-  <B value="-418.41" />
-  <C value="-109.87" />
-  <D value="-34733" />
-  <E value="-2236.6" />
-  <Tmin units="K"  value="344.85" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.435" />
-  <B value="1172.7" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="473.65" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000001005" />
-  <B value="0.79652" />
-  <C value="148.51" />
-  <D value="-7648.2" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.019283" />
-  <B value="-53.989" />
-  <C value="-1.1745" />
-  <D value="-0.0017696" />
-  <E value="-1.3435E-07" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="473.65" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00018425" />
-  <B value="0.91582" />
-  <C value="448.35" />
-  <D value="58650" />
-  <Tmin units="K"  value="473.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.12216" />
-  <B value="-29.058" />
-  <C value="-1.4793" />
-  <D value="-0.001294" />
-  <E value="6.5007E-07" />
-  <Tmin units="K"  value="268.2" />
-  <Tmax units="K"  value="689.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-7365.9" />
-  <B value="999.61" />
-  <C value="-0.67127" />
-  <D value="0.00016012" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.558" />
-  <B value="4258.7" />
-  <C value="-49.2" />
-  <Tmin units="K"  value="423.49" />
-  <Tmax units="K"  value="600.96" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.638704" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.758875E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="490.9247" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.285" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="148.779" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0758034" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.922" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.402005" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1947" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.9221" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.972" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.402005" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15680" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1947" />
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="6" />
-  <group id="4"  value="2" />
-  <group id="201"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-06-5" />
-<Smiles name="SMILES"  value="CC(C)(C)SSC(C)(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="3813" />
-<CompoundID name="Name"  value="Ethyl methyl disulfide" />
-<StructureFormula name="Structure"  value="CH3CH2SSCH3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="628.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4615000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.312" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="407.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="183.22" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="183.22" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0416" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="108.226" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1066" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.301" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.411E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18730" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.25E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.061" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.365E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.94E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.709E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="381100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9210000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.65E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="13.215" />
-  <B value="-0.0090158" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="73.29" />
-  <Tmax units="K"  value="183.22" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.88258" />
-  <B value="0.27523" />
-  <C value="628.9" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="605.44" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="96.027" />
-  <B value="-8038.4" />
-  <C value="-10.972" />
-  <D value="0.0000070895" />
-  <E value="2" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="628.9" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.8216E+07" />
-  <B value="0.48633" />
-  <C value="-0.6279" />
-  <D value="0.476" />
-  <E value="0" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="628.9" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="2639" />
-  <B value="0.73245" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="183.22" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="187520" />
-  <B value="-208.62" />
-  <C value="0.55295" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="628.22" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="84149" />
-  <B value="-628.71" />
-  <C value="12.564" />
-  <D value="-0.0001652" />
-  <E value="8.9754E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18531" />
-  <B value="-341.47" />
-  <C value="-46.957" />
-  <D value="-9218.3" />
-  <E value="14306" />
-  <Tmin units="K"  value="314.45" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-74.45287" />
-  <B value="3204.964" />
-  <C value="10.10529" />
-  <D value="-0.0000144504" />
-  <E value="2" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="503.12" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.0201E-08" />
-  <B value="0.85571" />
-  <C value="90.077" />
-  <D value="-7385.7" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.21083" />
-  <B value="11.426" />
-  <C value="-1.0307" />
-  <D value="0.00012249" />
-  <E value="-0.0000010671" />
-  <Tmin units="K"  value="188.67" />
-  <Tmax units="K"  value="503.12" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00027958" />
-  <B value="0.86411" />
-  <C value="843.3" />
-  <D value="7471.1" />
-  <Tmin units="K"  value="407.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.019623" />
-  <B value="24.049" />
-  <C value="-2.6806" />
-  <D value="-0.0004209" />
-  <E value="-0.0000026778" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="605.44" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="28202" />
-  <B value="358.57" />
-  <C value="-0.21427" />
-  <D value="0.00005341" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.749" />
-  <B value="3877.4" />
-  <C value="-27.865" />
-  <Tmin units="K"  value="394.33" />
-  <Tmax units="K"  value="558.53" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.1439" />
-  <B value="-0.0099736" />
-  <Tmin units="K"  value="183.22" />
-  <Tmax units="K"  value="503.12" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.326201" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.957956E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="393.6339" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.275" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="95.451" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0449723" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.02" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.301" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1066" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9004" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.276" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.301" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18730" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1066" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="102"  value="1" />
-  <group id="103"  value="1" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="102"  value="1" />
-  <group id="103"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="201"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="20333-39-5" />
-<Smiles name="SMILES"  value="CCSSC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="3814" />
-<CompoundID name="Name"  value="Ethyl propyl disulfide" />
-<StructureFormula name="Structure"  value="CH3(CH2)2SSCH2CH3" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="660" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3612000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.417" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.274" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="446.85" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="165" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="165" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00002" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="136.279" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.1405" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.391" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.304E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17840" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.69E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0824" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.105E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.625E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.796E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="460300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.08E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.866E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="10.091" />
-  <B value="-0.0076445" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="66" />
-  <Tmax units="K"  value="165" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.65822" />
-  <B value="0.27459" />
-  <C value="660" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="660" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="110.6" />
-  <B value="-9574.8" />
-  <C value="-12.96" />
-  <D value="0.0000072115" />
-  <E value="2" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="660" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.9782E+07" />
-  <B value="0.63427" />
-  <C value="-0.74757" />
-  <D value="0.47275" />
-  <E value="0" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="660" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5554.7" />
-  <B value="1005.5" />
-  <C value="-1.3152" />
-  <D value="0.0022282" />
-  <E value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="165" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="223630" />
-  <B value="-139.83" />
-  <C value="0.57232" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="446.85" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="105720" />
-  <B value="-573.79" />
-  <C value="12.857" />
-  <D value="0.000058344" />
-  <E value="8.0803E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.24848" />
-  <B value="-451.31" />
-  <C value="-81.656" />
-  <D value="-23479" />
-  <E value="37883" />
-  <Tmin units="K"  value="330" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-37.87" />
-  <B value="2334.8" />
-  <C value="4.1564" />
-  <D value="-0.0000036099" />
-  <E value="2" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="528" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="6.9027E-08" />
-  <B value="0.8462" />
-  <C value="109.98" />
-  <D value="-9618.4" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.20064" />
-  <B value="12.059" />
-  <C value="-1.0757" />
-  <D value="0.00011826" />
-  <E value="-0.000000977" />
-  <Tmin units="K"  value="198" />
-  <Tmax units="K"  value="528" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00000124" />
-  <B value="1.5526" />
-  <C value="-137.7" />
-  <D value="30422" />
-  <Tmin units="K"  value="446.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.016218" />
-  <B value="22.019" />
-  <C value="-2.7492" />
-  <D value="-0.00041928" />
-  <E value="-0.0000026424" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="660" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="24558" />
-  <B value="549.61" />
-  <C value="-0.30995" />
-  <D value="0.000072708" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.677" />
-  <B value="4069.1" />
-  <C value="-45.972" />
-  <Tmin units="K"  value="399.47" />
-  <Tmax units="K"  value="581.84" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.8977" />
-  <B value="-0.013855" />
-  <Tmin units="K"  value="165" />
-  <Tmax units="K"  value="528" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.449017" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.591582E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="407.7173" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.274" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="133.984" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0590577" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.948" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.391" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1405" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2492" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.356" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.391" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17840" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.1405" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="103"  value="2" />
-  </UnifacVLE>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="103"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="201"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="30453-31-7" />
-<Smiles name="SMILES"  value="CCCSSCC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="3819" />
-<CompoundID name="Name"  value="Diphenyl disulfide" />
-<StructureFormula name="Structure"  value="(C6H5)SS(C6H5)" />
-<Family name="Family"  value="42" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="829.8" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3569000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.584" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.302" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="583.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="333.5" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="333.5" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.49" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="218.338" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.2076" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.569717" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.685E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20480" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.97E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.1193" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.447E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.628E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3.518E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="489300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.93E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.676E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="6.3025" />
-  <B value="-0.00053803" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="290" />
-  <Tmax units="K"  value="333.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.5173" />
-  <B value="0.302" />
-  <C value="829.8" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="829.8" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="927.5541" />
-  <B value="-59320.23" />
-  <C value="-131.1073" />
-  <D value="0.000060625" />
-  <E value="2" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="829.8" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.1805E+08" />
-  <B value="0.46278" />
-  <C value="0.25764" />
-  <D value="-0.22402" />
-  <E value="-0.0012437" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="829.8" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="13316" />
-  <B value="948.21" />
-  <C value="-1.198" />
-  <D value="0.0037219" />
-  <E value="-0.0000045845" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="333.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="267470" />
-  <B value="28.884" />
-  <C value="0.54728" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="583.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="50433" />
-  <B value="-472.23" />
-  <C value="13.469" />
-  <D value="-0.00011605" />
-  <E value="2.3877E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.32906" />
-  <B value="-464.91" />
-  <C value="-256.61" />
-  <D value="-253250" />
-  <E value="94392" />
-  <Tmin units="K"  value="414.9" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.832" />
-  <B value="1659.3" />
-  <C value="-0.039017" />
-  <D value="-1.1543E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="583.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.542E-08" />
-  <B value="0.87669" />
-  <C value="123.7" />
-  <D value="-14104" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.040762" />
-  <B value="-52.269" />
-  <C value="-1.2013" />
-  <D value="-0.001172" />
-  <E value="-1.6247E-07" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="583.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000021936" />
-  <B value="1.4453" />
-  <C value="-128.48" />
-  <D value="46604" />
-  <Tmin units="K"  value="583.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="106" />
-  <A value="0.086" />
-  <B value="1.222" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="829.8" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-72351" />
-  <B value="1102.3" />
-  <C value="-0.77741" />
-  <D value="0.00020116" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.007" />
-  <B value="3922.8" />
-  <C value="-169.93" />
-  <Tmin units="K"  value="516.35" />
-  <Tmax units="K"  value="725.32" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4659" />
-  <B value="-0.0085149" />
-  <Tmin units="K"  value="333.5" />
-  <Tmax units="K"  value="583.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.683837" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.562071E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="727.6315" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.302" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="143.191" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0940873" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.569717" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.2076" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.6308" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.496" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.569717" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20480" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.2076" />
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="10"  value="0" />
-  </UnifacLLE>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="10" />
-  <group id="10"  value="2" />
-  <group id="201"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="882-33-7" />
-<Smiles name="SMILES"  value="C1=CC=C(C=C1)SSC2=CC=CC=C2" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1723" />
-<CompoundID name="Name"  value="Monoethanolamine" />
-<StructureFormula name="Structure"  value="HOCH2CH2NH2" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="671.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="8030000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.225" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.284" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="444.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="283.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="283.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="13.3683" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="61.0831" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0603415" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.550815" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.826E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="31830" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.59E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03904" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.9E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.96E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.033E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="320000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.0496E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.289594" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.363E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="21.251" />
-  <B value="-0.0083183" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="113.46" />
-  <Tmax units="K"  value="283.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.648" />
-  <B value="0.18183" />
-  <C value="678.21" />
-  <D value="0.17947" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="678.2" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.09274" />
-  <B value="4319.625" />
-  <C value="-69.95024" />
-  <Tmin units="K"  value="283.65" />
-  <Tmax units="K"  value="678.2" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.012031E+08" />
-  <B value="1.976961" />
-  <C value="-4.399887" />
-  <D value="4.906054" />
-  <E value="-1.945886" />
-  <Tmin units="K"  value="283.65" />
-  <Tmax units="K"  value="595.14" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="15188" />
-  <B value="144.03" />
-  <C value="3.6142" />
-  <D value="-0.019701" />
-  <E value="0.000034165" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="283.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="78653.42" />
-  <B value="311.4162" />
-  <C value="-0.0607137" />
-  <D value="-2.713217E-06" />
-  <E value="-0.000017988" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="443.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="50668" />
-  <B value="-516.86" />
-  <C value="12.167" />
-  <D value="0.00008641" />
-  <E value="2.8656E-10" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.13635" />
-  <B value="-174.62" />
-  <C value="-48.233" />
-  <D value="-16405" />
-  <E value="4380.8" />
-  <Tmin units="K"  value="339.1" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-370.3" />
-  <B value="17780" />
-  <C value="54.624" />
-  <D value="-0.000051065" />
-  <E value="2" />
-  <Tmin units="K"  value="283.65" />
-  <Tmax units="K"  value="542.56" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.78881E-08" />
-  <B value="0.876532" />
-  <C value="75.00276" />
-  <D value="628.0161" />
-  <Tmin units="K"  value="283.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.37218" />
-  <B value="78.8" />
-  <C value="-1.5916" />
-  <D value="0.0043895" />
-  <E value="-0.0000053291" />
-  <Tmin units="K"  value="283.65" />
-  <Tmax units="K"  value="583.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-9539.9" />
-  <B value="0.39852" />
-  <C value="-1.7433E+09" />
-  <D value="-6.3715E+10" />
-  <Tmin units="K"  value="443.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.067139" />
-  <B value="-7.9" />
-  <C value="-1.90607" />
-  <D value="-0.0004719" />
-  <E value="-0.0000009533" />
-  <Tmin units="K"  value="270" />
-  <Tmax units="K"  value="600" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="11350" />
-  <B value="298.51" />
-  <C value="-0.17683" />
-  <D value="0.000043009" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-16.337" />
-  <B value="-10000" />
-  <C value="-113.16" />
-  <Tmin units="K"  value="283.65" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.027" />
-  <B value="3495.2" />
-  <C value="-109.62" />
-  <Tmin units="K"  value="370" />
-  <Tmax units="K"  value="545" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="1.9272" />
-  <B value="-0.020626" />
-  <Tmin units="K"  value="283.65" />
-  <Tmax units="K"  value="542.56" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.20696" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.140324E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="431.8628" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.284" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="51.539" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0284" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.01697" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.550815" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0603415" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.0436" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.976" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.446737" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="31830" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0603415" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  <group id="30"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  <group id="29"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  <group id="30"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="14"  value="1" />
-  <group id="29"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="141-43-5" />
-<Smiles name="SMILES"  value="NCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1724" />
-<CompoundID name="Name"  value="Diethanolamine" />
-<StructureFormula name="Structure"  value="(HOCH2CH2)2NH" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="736.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4720000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.349" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.243" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="542" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="301.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="301.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.102031" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="105.136" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.096244" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.991515" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.907E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="29260" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06508" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.31E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.73E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.2574E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="429000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.5104E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.85" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.4439E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.174" />
-  <B value="-0.0048077" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="120.46" />
-  <Tmax units="K"  value="301.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.5251" />
-  <B value="0.20924" />
-  <C value="736.61" />
-  <D value="0.18363" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="736.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.735" />
-  <B value="5441.7" />
-  <C value="-95.519" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="736.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.90134E+07" />
-  <B value="-1.865152" />
-  <C value="6.820965" />
-  <D value="-7.963053" />
-  <E value="3.251551" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="713.68" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5726.4" />
-  <B value="678.12" />
-  <C value="-1.2202" />
-  <D value="0.0028487" />
-  <E value="-0.0000029189" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="301.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="88234.68" />
-  <B value="483.2566" />
-  <C value="0.294569" />
-  <D value="-0.000214761" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="715" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="92216" />
-  <B value="-624.1" />
-  <C value="12.938" />
-  <D value="-0.00014779" />
-  <E value="6.6337E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500.1" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25716" />
-  <B value="-224.15" />
-  <C value="-187.3" />
-  <D value="-175320" />
-  <E value="231800" />
-  <Tmin units="K"  value="368.3" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-0.28702" />
-  <B value="6080.5" />
-  <C value="-3.8708" />
-  <D value="0.00001517" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="589.28" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.7852E-08" />
-  <B value="0.89857" />
-  <C value="99.058" />
-  <D value="-7265.2" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.91328" />
-  <B value="16.824" />
-  <C value="-0.15997" />
-  <D value="0.0011516" />
-  <E value="-0.0000013756" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="673.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-10221" />
-  <B value="0.42596" />
-  <C value="-2.5172E+09" />
-  <D value="-7.9932E+10" />
-  <Tmin units="K"  value="541.54" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.146398" />
-  <B value="45.86264" />
-  <C value="-1.696703" />
-  <D value="-0.000291273" />
-  <E value="-1.334366E-07" />
-  <Tmin units="K"  value="301.15" />
-  <Tmax units="K"  value="736.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="9793.4" />
-  <B value="530.15" />
-  <C value="-0.31974" />
-  <D value="0.000077668" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500.1" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-13.04345" />
-  <B value="-12719.43" />
-  <C value="32.79742" />
-  <Tmin units="K"  value="303" />
-  <Tmax units="K"  value="715" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.735" />
-  <B value="5441.7" />
-  <C value="-95.519" />
-  <Tmin units="K"  value="430" />
-  <Tmax units="K"  value="640" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="8.1033" />
-  <B value="-0.031788" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="589.28" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.349015" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.174515E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="286.6829" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.243" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="105.77" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0453451" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.101108" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.991515" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.096244" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.2302" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.956" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.952882" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="29260" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.096244" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="3" />
-  <group id="15"  value="2" />
-  <group id="33"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  <group id="30"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="3" />
-  <group id="15"  value="2" />
-  <group id="33"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="3" />
-  <group id="14"  value="2" />
-  <group id="32"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-42-2" />
-<Smiles name="SMILES"  value="OCCNCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1725" />
-<CompoundID name="Name"  value="Triethanolamine" />
-<StructureFormula name="Structure"  value="(HOCH2CH2)3N" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="787" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3590000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.472" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.202" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="613" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="294.35" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="294.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000287009" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="149.188" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.132992" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.28411" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.219E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="27430" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.6E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08983" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.271E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.54E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.994E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="538000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.7191E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="2.21" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.5025E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.5621" />
-  <B value="-0.0036262" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="117.74" />
-  <Tmax units="K"  value="294.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.028938" />
-  <B value="0.058014" />
-  <C value="787" />
-  <D value="0.099632" />
-  <Tmin units="K"  value="283.15" />
-  <Tmax units="K"  value="772.1" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="283.76" />
-  <B value="-24672" />
-  <C value="-37.048" />
-  <D value="0.000015689" />
-  <E value="2" />
-  <Tmin units="K"  value="294.35" />
-  <Tmax units="K"  value="772.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.354875E+08" />
-  <B value="0.343894" />
-  <C value="0.961738" />
-  <D value="-1.466285" />
-  <E value="0.442687" />
-  <Tmin units="K"  value="294.35" />
-  <Tmax units="K"  value="772.1" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="8095.9" />
-  <B value="970.95" />
-  <C value="-1.7742" />
-  <D value="0.0042146" />
-  <E value="-0.0000044001" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="294.35" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="285560" />
-  <B value="313.35" />
-  <C value="6.351" />
-  <D value="0.016374" />
-  <E value="-0.000012842" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="633.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="114870" />
-  <B value="-616.04" />
-  <C value="13.509" />
-  <D value="-0.00048074" />
-  <E value="2.2464E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.40996" />
-  <B value="-214.21" />
-  <C value="-459.31" />
-  <D value="-488000" />
-  <E value="535120" />
-  <Tmin units="K"  value="386.1" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="33.605" />
-  <B value="4399.7" />
-  <C value="-8.9203" />
-  <D value="0.000021038" />
-  <E value="2" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="617.68" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.0013E-08" />
-  <B value="0.95199" />
-  <C value="45.139" />
-  <D value="-3355.9" />
-  <Tmin units="K"  value="294.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.76863" />
-  <B value="26.11" />
-  <C value="-0.3374" />
-  <D value="0.0010847" />
-  <E value="-0.0000011937" />
-  <Tmin units="K"  value="294.35" />
-  <Tmax units="K"  value="723.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.043843" />
-  <B value="0.38395" />
-  <C value="6681.4" />
-  <D value="1202500" />
-  <Tmin units="K"  value="608.54" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.151321" />
-  <B value="49.37161" />
-  <C value="-1.697977" />
-  <D value="-0.00029278" />
-  <E value="-3.656577E-08" />
-  <Tmin units="K"  value="294.35" />
-  <Tmax units="K"  value="787" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-21521" />
-  <B value="918.12" />
-  <C value="-0.68139" />
-  <D value="0.00020714" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.15" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-17.59" />
-  <B value="-10000" />
-  <C value="-84.33" />
-  <Tmin units="K"  value="294.35" />
-  <Tmax units="K"  value="450" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="24.348" />
-  <B value="6603" />
-  <C value="-93.899" />
-  <Tmin units="K"  value="475.15" />
-  <Tmax units="K"  value="696.67" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="6.6572" />
-  <B value="-0.027285" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="617.68" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.493725" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="9.903848E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="162.2381" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.202" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="152.92" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.063602" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.131188" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.28411" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.132992" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="7.3317" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.932" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.28411" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="27430" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.132992" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="5" />
-  <group id="15"  value="3" />
-  <group id="36"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="2"  value="6" />
-  <group id="15"  value="3" />
-  <group id="31"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="5" />
-  <group id="15"  value="3" />
-  <group id="36"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="5" />
-  <group id="14"  value="3" />
-  <group id="35"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="102-71-6" />
-<Smiles name="SMILES"  value="OCCN(CCO)CCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1741" />
-<CompoundID name="Name"  value="Ethylenediamine" />
-<StructureFormula name="Structure"  value="H2NCH2CH2NH2" />
-<Family name="Family"  value="37" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="592.95" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6290000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.206" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.337" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="390.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="281.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="284.29" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="677.511" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="60.0983" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0672757" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.472367" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.7605E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="25200" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.34E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04154" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.54E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.78E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.032E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="321833" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="109700" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.3873" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.691E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="19.105" />
-  <B value="-0.007483" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="113.72" />
-  <Tmax units="K"  value="284.29" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77469" />
-  <B value="0.20588" />
-  <C value="592.95" />
-  <D value="0.20098" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="576.75" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="133.543" />
-  <B value="-9787.615" />
-  <C value="-16.57909" />
-  <D value="0.0000129717" />
-  <E value="2" />
-  <Tmin units="K"  value="262.15" />
-  <Tmax units="K"  value="593" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.5708E+07" />
-  <B value="1.0826" />
-  <C value="-0.65481" />
-  <D value="-0.27019" />
-  <E value="0.25065" />
-  <Tmin units="K"  value="284.29" />
-  <Tmax units="K"  value="576.75" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-16264" />
-  <B value="987.11" />
-  <C value="-4.4926" />
-  <D value="0.011566" />
-  <E value="-0.0000088487" />
-  <Tmin units="K"  value="25.91" />
-  <Tmax units="K"  value="265.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="143860" />
-  <B value="434.68" />
-  <C value="4.2425" />
-  <D value="0.021662" />
-  <E value="-0.000021123" />
-  <Tmin units="K"  value="284.29" />
-  <Tmax units="K"  value="390.41" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="58340" />
-  <B value="-554.75" />
-  <C value="12.205" />
-  <D value="0.00022368" />
-  <E value="-7.8562E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.12638" />
-  <B value="-182.9" />
-  <C value="-38.105" />
-  <D value="-22568" />
-  <E value="37297" />
-  <Tmin units="K"  value="296.5" />
-  <Tmax units="K"  value="1899.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.2076" />
-  <B value="2247.2" />
-  <C value="-0.93509" />
-  <D value="0.0000071501" />
-  <E value="2" />
-  <Tmin units="K"  value="284.29" />
-  <Tmax units="K"  value="483.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.0005E-07" />
-  <B value="0.70929" />
-  <C value="192.67" />
-  <D value="-6383.4" />
-  <Tmin units="K"  value="284.29" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.020715" />
-  <B value="-158.25" />
-  <C value="0.1953" />
-  <D value="-0.004385" />
-  <E value="0.0000010035" />
-  <Tmin units="K"  value="284.29" />
-  <Tmax units="K"  value="390.41" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.16528" />
-  <B value="0.18013" />
-  <C value="3835.1" />
-  <D value="1598900" />
-  <Tmin units="K"  value="390.41" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.031818" />
-  <B value="-71.601" />
-  <C value="-1.8001" />
-  <D value="-0.00127" />
-  <E value="-0.0000022345" />
-  <Tmin units="K"  value="284.29" />
-  <Tmax units="K"  value="576.75" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13229" />
-  <B value="307.67" />
-  <C value="-0.16317" />
-  <D value="0.000033422" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-16.9316" />
-  <B value="-8000" />
-  <C value="-48" />
-  <Tmin units="K"  value="271.9278" />
-  <Tmax units="K"  value="441.9278" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.176" />
-  <B value="3547.8" />
-  <C value="-57.244" />
-  <Tmin units="K"  value="356.35" />
-  <Tmax units="K"  value="528.01" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9318" />
-  <B value="-0.012454" />
-  <Tmin units="K"  value="284.29" />
-  <Tmax units="K"  value="483.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.2203" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.064853E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="771.612" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.337" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="56.533" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.7134" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0304359" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.17431" />
-<Charge name="Charge"  units="_"  value="0" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.7384" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.472" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.1081" />
-<UnifacVLE name="UNIFAC" >
-  <group id="30"  value="2" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="2"  value="2" />
-  <group id="29"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="30"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="29"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="107-15-3" />
-<Smiles name="SMILES"  value="NCCN" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1743" />
-<CompoundID name="Name"  value="Diisopropylamine" />
-<StructureFormula name="Structure"  value="((CH3)2CH)2NH" />
-<Family name="Family"  value="35" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="522.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3200000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.031" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.308" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="357.05" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="176.85" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="176.85" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00447237" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="101.19" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.141919" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.388315" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.806E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15060" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07632" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.061E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.5E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="6.42E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="412000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6530000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.98503" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.99E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.219" />
-  <B value="-0.0064246" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="70.74" />
-  <Tmax units="K"  value="176.85" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.72754" />
-  <B value="0.27918" />
-  <C value="522.15" />
-  <D value="0.29458" />
-  <Tmin units="K"  value="176.85" />
-  <Tmax units="K"  value="504.88" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="237.36" />
-  <B value="-12403" />
-  <C value="-33.276" />
-  <D value="0.000035165" />
-  <E value="2" />
-  <Tmin units="K"  value="176.85" />
-  <Tmax units="K"  value="523.1" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.537039E+07" />
-  <B value="-2.459337" />
-  <C value="14.73933" />
-  <D value="-19.70849" />
-  <E value="7.844199" />
-  <Tmin units="K"  value="176.85" />
-  <Tmax units="K"  value="504.88" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="197480" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="522.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="150380" />
-  <B value="276.56" />
-  <C value="5.7411" />
-  <D value="0.021881" />
-  <E value="-0.000021998" />
-  <Tmin units="K"  value="275" />
-  <Tmax units="K"  value="357.05" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="61641" />
-  <B value="-432.93" />
-  <C value="12.839" />
-  <D value="0.00037342" />
-  <E value="-1.4329E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.23056" />
-  <B value="-237.06" />
-  <C value="-36.183" />
-  <D value="970.06" />
-  <E value="-9593.3" />
-  <Tmin units="K"  value="261.55" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-7.0105" />
-  <B value="766.59" />
-  <C value="-0.57101" />
-  <D value="-0.0000016173" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="357.05" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.4462E-07" />
-  <B value="0.56686" />
-  <C value="334.62" />
-  <D value="-4787.5" />
-  <Tmin units="K"  value="357.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.046488" />
-  <B value="-113.84" />
-  <C value="-0.63846" />
-  <D value="-0.0065631" />
-  <E value="0.0000029442" />
-  <Tmin units="K"  value="176.85" />
-  <Tmax units="K"  value="357.05" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00048482" />
-  <B value="0.81453" />
-  <C value="349.64" />
-  <D value="151910" />
-  <Tmin units="K"  value="357.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.007975" />
-  <B value="58.206" />
-  <C value="-3.5469" />
-  <D value="0.0016772" />
-  <E value="-0.0000085096" />
-  <Tmin units="K"  value="176.85" />
-  <Tmax units="K"  value="504.88" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-15354" />
-  <B value="697.81" />
-  <C value="-0.39592" />
-  <D value="0.000082987" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.374" />
-  <B value="2622.7" />
-  <C value="-60.838" />
-  <Tmin units="K"  value="313.77" />
-  <Tmax units="K"  value="468.43" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.4791" />
-  <B value="-0.011177" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="357.05" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.41328" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="2.408637E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="491.4633" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.308" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="134.59" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0523754" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.722239" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.388315" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.1" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.0308" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.244" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="1" />
-  <group id="34"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="4" />
-  <group id="3"  value="2" />
-  <group id="30"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="4" />
-  <group id="3"  value="1" />
-  <group id="34"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="4" />
-  <group id="3"  value="1" />
-  <group id="33"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-18-9" />
-<Smiles name="SMILES"  value="CC(C)NC(C)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1750" />
-<CompoundID name="Name"  value="N-aminoethyl piperazine" />
-<StructureFormula name="Structure"  value="H2NC2H4(NCH2CH2NHCH2CH2)" />
-<Family name="Family"  value="37" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="708" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3850000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.475" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="495.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="254.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="254.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0694812" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="129.203" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.132257" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.557243" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.225E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21520" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08433" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.106E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.51E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.79E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="451000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.135E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.9891" />
-  <B value="-0.004913" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="101.66" />
-  <Tmax units="K"  value="254.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.66681" />
-  <B value="0.27137" />
-  <C value="708" />
-  <D value="0.27214" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="708" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="127.7429" />
-  <B value="-12067.23" />
-  <C value="-15.04915" />
-  <D value="6.424073E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="708" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.785579E+07" />
-  <B value="0.814708" />
-  <C value="0.0237006" />
-  <D value="-0.690218" />
-  <E value="0.260899" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="708" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="1710" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="254.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="259220" />
-  <B value="331.04" />
-  <C value="3.608" />
-  <D value="0.023605" />
-  <E value="-0.000018248" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="524" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="70888" />
-  <B value="-450.73" />
-  <C value="13.066" />
-  <D value="0.00018285" />
-  <E value="-6.5268E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26459" />
-  <B value="-324.05" />
-  <C value="-122" />
-  <D value="-62238" />
-  <E value="41430" />
-  <Tmin units="K"  value="354" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-497.9054" />
-  <B value="22666.52" />
-  <C value="74.36022" />
-  <D value="-0.0000702789" />
-  <E value="2" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="566.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.7705E-08" />
-  <B value="0.8233" />
-  <C value="132.06" />
-  <D value="-8963.7" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.089882" />
-  <B value="-7.0061" />
-  <C value="-1.0711" />
-  <D value="-0.00065668" />
-  <E value="-0.0000005629" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="493.55" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00012973" />
-  <B value="0.99814" />
-  <C value="630.8" />
-  <D value="21962" />
-  <Tmin units="K"  value="493.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.017548" />
-  <B value="79.8" />
-  <C value="-3.1218" />
-  <D value="0.00097678" />
-  <E value="-0.0000034661" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="708" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-21376" />
-  <B value="821.45" />
-  <C value="-0.51136" />
-  <D value="0.00012139" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.46" />
-  <B value="4725.8" />
-  <C value="-61.815" />
-  <Tmin units="K"  value="425.35" />
-  <Tmax units="K"  value="636.34" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="0.7273" />
-  <B value="-0.017627" />
-  <Tmin units="K"  value="254.15" />
-  <Tmax units="K"  value="566.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.460517" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.133208E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="393.1157" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.266" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="125.591" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0587237" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.9852" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.557243" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.132257" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.5591" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.424" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.557243" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21520" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.132257" />
-<UnifacVLE name="UNIFAC" >
-  <group id="36"  value="1" />
-  <group id="33"  value="1" />
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-<Umr name="UMR" >
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-  <group id="33"  value="1" />
-  <group id="2"  value="3" />
-  <group id="30"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="35"  value="1" />
-  <group id="32"  value="1" />
-  <group id="2"  value="3" />
-  <group id="29"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="140-31-8" />
-<Smiles name="SMILES"  value="C1CNCCN1CCN" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2717" />
-<CompoundID name="Name"  value="Diethylenetriamine" />
-<StructureFormula name="Structure"  value="(H2NCH2CH2)2NH" />
-<Family name="Family"  value="37" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="676" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4220000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.426" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.257" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="480" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="234" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="234.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0524649" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="103.166" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.108088" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.70022" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.865E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22210" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07008" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.87E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5860000" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.07293E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="444000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.97E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.15789" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.08E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.376" />
-  <B value="-0.005886" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="93.66" />
-  <Tmax units="K"  value="234.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.75082" />
-  <B value="0.25686" />
-  <C value="676" />
-  <D value="0.285" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="676" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="100.1854" />
-  <B value="-10608.36" />
-  <C value="-10.96201" />
-  <D value="4.74905E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="676" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.200873E+07" />
-  <B value="-0.521717" />
-  <C value="2.922507" />
-  <D value="-3.785965" />
-  <E value="1.591946" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="676" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="4677.2" />
-  <B value="636.48" />
-  <C value="-1.3531" />
-  <D value="0.0038102" />
-  <E value="-0.0000047797" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="234.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="42291" />
-  <B value="-130.86" />
-  <C value="11.696" />
-  <D value="0.0024243" />
-  <E value="-0.0000011576" />
-  <Tmin units="K"  value="338" />
-  <Tmax units="K"  value="498" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="73737" />
-  <B value="-451.7" />
-  <C value="12.705" />
-  <D value="0.00030197" />
-  <E value="-1.0181E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20692" />
-  <B value="-343.64" />
-  <C value="-96.031" />
-  <D value="-90293" />
-  <E value="176600" />
-  <Tmin units="K"  value="338" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.117" />
-  <B value="2075.7" />
-  <C value="-0.40711" />
-  <D value="6.9322E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="480.25" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.7285E-08" />
-  <B value="0.85783" />
-  <C value="72.519" />
-  <D value="-3817.5" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.078667" />
-  <B value="1.4114" />
-  <C value="-1.3167" />
-  <D value="-0.00041656" />
-  <E value="-8.7844E-07" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="480.25" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00017737" />
-  <B value="0.94914" />
-  <C value="591.08" />
-  <D value="27011" />
-  <Tmin units="K"  value="480.25" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.021703" />
-  <B value="47.519" />
-  <C value="-2.6592" />
-  <D value="-0.000080847" />
-  <E value="-0.0000026267" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="676" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="5303.6" />
-  <B value="589.73" />
-  <C value="-0.34089" />
-  <D value="0.000076082" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.134" />
-  <B value="5149.9" />
-  <C value="-36.704" />
-  <Tmin units="K"  value="420.19" />
-  <Tmax units="K"  value="606.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="0.32144" />
-  <B value="-0.01858" />
-  <Tmin units="K"  value="234.15" />
-  <Tmax units="K"  value="480.25" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.377332" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.169053E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="331.6035" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.257" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="100.082" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.048963" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.880407" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.70022" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.108088" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.6198" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.948" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.70022" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22210" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.108088" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="30"  value="2" />
-  <group id="33"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="2"  value="4" />
-  <group id="29"  value="2" />
-  <group id="30"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="1" />
-  <group id="30"  value="2" />
-  <group id="33"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="29"  value="2" />
-  <group id="32"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-40-0" />
-<Smiles name="SMILES"  value="NCCNCCN" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2732" />
-<CompoundID name="Name"  value="N-aminoethyl ethanolamine" />
-<StructureFormula name="Structure"  value="H2NCH2CH2NHCH2CH2OH" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="698" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4460000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.387" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.252" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="517" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="104.151" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.101519" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.04726" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.821E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="29230" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06758" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.59E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.91E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="3810000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="447000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.9" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.74E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.8" />
-  <B value="-1.6252E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.76828" />
-  <B value="0.25238" />
-  <C value="698" />
-  <D value="0.28565" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="675.64" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="214.43" />
-  <B value="-18769" />
-  <C value="-27.15" />
-  <D value="0.00001141" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="698" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.2005E+08" />
-  <B value="0.3465" />
-  <C value="0.971" />
-  <D value="-1.7132" />
-  <E value="0.81091" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="675.64" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="65604" />
-  <B value="-121.74" />
-  <C value="11.802" />
-  <D value="0.0023485" />
-  <E value="-7.9478E-07" />
-  <Tmin units="K"  value="349" />
-  <Tmax units="K"  value="519" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="75533" />
-  <B value="-495.37" />
-  <C value="12.77" />
-  <D value="0.00015714" />
-  <E value="-4.9852E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.088651" />
-  <B value="-82.595" />
-  <C value="-177.94" />
-  <D value="449510" />
-  <E value="-2249800" />
-  <Tmin units="K"  value="349" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-27.66295" />
-  <B value="5326.5" />
-  <C value="1.362383" />
-  <D value="-1.706454E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="517" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2606E-07" />
-  <B value="0.76222" />
-  <C value="173.4" />
-  <D value="-8594.2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1257" />
-  <B value="-10.607" />
-  <C value="-0.88928" />
-  <D value="-0.00060102" />
-  <E value="-5.9478E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="517" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00019261" />
-  <B value="0.93731" />
-  <C value="615.43" />
-  <D value="23918" />
-  <Tmin units="K"  value="517" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.046419" />
-  <B value="12.352" />
-  <C value="-2.0792" />
-  <D value="-0.001082" />
-  <E value="-0.0000005495" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="675.64" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="2031.6" />
-  <B value="577.66" />
-  <C value="-0.34597" />
-  <D value="0.000080678" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-8.924" />
-  <B value="-9007" />
-  <C value="0" />
-  <Tmin units="K"  value="223.15" />
-  <Tmax units="K"  value="698" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="24.561" />
-  <B value="5615.5" />
-  <C value="-88.315" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="698" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="7.9594" />
-  <B value="-0.034824" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="517" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.363122" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.108882E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="319.0146" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.252" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="95.088" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.04649" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.0254" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.04726" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.101519" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.925" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.452" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.04726" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="29230" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.101519" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
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-  <group id="33"  value="1" />
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-<Asog name="ASOG" >
-  <group id="2"  value="4" />
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-<Umr name="UMR" >
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-  <group id="33"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="14"  value="1" />
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-  <group id="32"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="111-41-1" />
-<Smiles name="SMILES"  value="NCCNCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2750" />
-<CompoundID name="Name"  value="P-phenylenediamine" />
-<StructureFormula name="Structure"  value="(C6H4)(NH2)2" />
-<Family name="Family"  value="36" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="796" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5180000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.377" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="540" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="419" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="413" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1388.21" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="108.141" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.102198" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.53864" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.733E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24810" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.1E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0644" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.08E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="9.12E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.1E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="349000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.68E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.33E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.426" />
-  <B value="-0.0033838" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="165.2" />
-  <Tmax units="K"  value="413" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.78274" />
-  <B value="0.24798" />
-  <C value="796" />
-  <D value="0.28573" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="775.84" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="120.7365" />
-  <B value="-13060.28" />
-  <C value="-13.71648" />
-  <D value="4.333592E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="796" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.0783E+08" />
-  <B value="1.6408" />
-  <C value="-3.3392" />
-  <D value="3.5461" />
-  <E value="-1.4179" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="775.84" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5535.8" />
-  <B value="549.11" />
-  <C value="-0.79398" />
-  <D value="0.0014488" />
-  <E value="-0.0000011393" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="413" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="199750" />
-  <B value="494.23" />
-  <C value="5.1045" />
-  <D value="0.015817" />
-  <E value="-0.000010858" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="588" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="58132" />
-  <B value="-482.33" />
-  <C value="12.882" />
-  <D value="-0.000085339" />
-  <E value="9.0492E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22693" />
-  <B value="-318.73" />
-  <C value="-138.3" />
-  <D value="-255620" />
-  <E value="535900" />
-  <Tmin units="K"  value="398" />
-  <Tmax units="K"  value="1830" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.9816" />
-  <B value="2291" />
-  <C value="-0.53494" />
-  <D value="2.8717E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.4679E-07" />
-  <B value="0.74191" />
-  <C value="224.79" />
-  <D value="-11478" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0030572" />
-  <B value="-268.6" />
-  <C value="0.38244" />
-  <D value="-0.0036549" />
-  <E value="8.2114E-07" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="540" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000070276" />
-  <B value="1.0203" />
-  <C value="189.91" />
-  <D value="62690" />
-  <Tmin units="K"  value="540" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012384" />
-  <B value="521.02" />
-  <C value="-5.5892" />
-  <D value="0.0063731" />
-  <E value="-0.0000072097" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="775.84" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-13543" />
-  <B value="616.65" />
-  <C value="-0.42898" />
-  <D value="0.00010942" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.019" />
-  <B value="4568.9" />
-  <C value="-104.99" />
-  <Tmin units="K"  value="489.6" />
-  <Tmax units="K"  value="715.37" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0631" />
-  <B value="-0.011145" />
-  <Tmin units="K"  value="413" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.345195" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.183731E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="343.4411" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="104.66" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0460999" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.164317" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.53864" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.102198" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2452" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.232" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.53864" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24810" />
-<UnifacVLE name="UNIFAC" >
-  <group id="37"  value="2" />
-  <group id="10"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="43"  value="2" />
-  <group id="9"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="29"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="37"  value="2" />
-  <group id="10"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="36"  value="2" />
-  <group id="9"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="106-50-3" />
-<Smiles name="SMILES"  value="c1(N)ccc(N)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2752" />
-<CompoundID name="Name"  value="Piperazine" />
-<StructureFormula name="Structure"  value="-NHCH2CH2NHCH2CH2-" />
-<Family name="Family"  value="37" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="656.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5420000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.267" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.2652" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="419.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="379.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="379.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="26372.2" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.1356" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.129371" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.269668" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.035E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17960" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.90339E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05708" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.38E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.26E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.7E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="321000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.17E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.9" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.76E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.576" />
-  <B value="-0.0026896" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="302.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.4074" />
-  <B value="0.323" />
-  <C value="638" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="379.15" />
-  <Tmax units="K"  value="638" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="143.27" />
-  <B value="-11245" />
-  <C value="-17.657" />
-  <D value="0.0000096236" />
-  <E value="2" />
-  <Tmin units="K"  value="379.15" />
-  <Tmax units="K"  value="638" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.6945E+07" />
-  <B value="0.99602" />
-  <C value="-2.0069" />
-  <D value="2.4018" />
-  <E value="-0.97129" />
-  <Tmin units="K"  value="379.15" />
-  <Tmax units="K"  value="638" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-377150" />
-  <B value="4505.5" />
-  <C value="-17.799" />
-  <D value="0.035442" />
-  <E value="-0.000026404" />
-  <Tmin units="K"  value="295" />
-  <Tmax units="K"  value="384.6" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="32886.27" />
-  <B value="346.6189" />
-  <C value="0.473406" />
-  <D value="-0.000434168" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="638" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68463" />
-  <B value="-744.16" />
-  <C value="13.556" />
-  <D value="-0.00073698" />
-  <E value="1.7652E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16381" />
-  <B value="-201.87" />
-  <C value="-47.429" />
-  <D value="-2534.9" />
-  <E value="-24066" />
-  <Tmin units="K"  value="319" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="24.341" />
-  <B value="105.42" />
-  <C value="-5.6537" />
-  <D value="0.0000060109" />
-  <E value="2" />
-  <Tmin units="K"  value="379.15" />
-  <Tmax units="K"  value="419.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.0000022951" />
-  <B value="0.42453" />
-  <C value="937.27" />
-  <D value="-18307" />
-  <Tmin units="K"  value="379.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.029211" />
-  <B value="-334.85" />
-  <C value="0.86034" />
-  <D value="-0.0073343" />
-  <E value="0.0000029317" />
-  <Tmin units="K"  value="379.15" />
-  <Tmax units="K"  value="419.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0014866" />
-  <B value="0.6319" />
-  <C value="-11.551" />
-  <D value="345800" />
-  <Tmin units="K"  value="419.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="106" />
-  <A value="0.0533278" />
-  <B value="1.232" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="656.3" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-51888" />
-  <B value="720.62" />
-  <C value="-0.52354" />
-  <D value="0.00013324" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.737" />
-  <B value="3535.7" />
-  <C value="-73.202" />
-  <Tmin units="K"  value="392.09" />
-  <Tmax units="K"  value="573.29" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.2893" />
-  <B value="-0.010036" />
-  <Tmin units="K"  value="379.15" />
-  <Tmax units="K"  value="419.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.304509" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.901426E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="712.6282" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.323" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="95.78" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0290647" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.720588" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.41376" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.129371" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.7628" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.952" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.41376" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17960" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.129371" />
-<UnifacVLE name="UNIFAC" >
-  <group id="33"  value="2" />
-  <group id="2"  value="2" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="13"  value="4" />
-  <group id="30"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="33"  value="2" />
-  <group id="2"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="32"  value="2" />
-  <group id="2"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-85-0" />
-<Smiles name="SMILES"  value="N1CCNCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="6862" />
-<CompoundID name="Name"  value="Methylethanolamine" />
-<StructureFormula name="Structure"  value="CH3NHCH2CH2OH" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="630" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5300000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.25901" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.262" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="432.388" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="268.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="268.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="11.1091" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="75.112" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.082206" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.604" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.035E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="25930" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.2E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05025" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.27E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.98E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-6.11E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="344000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8760000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.36403" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.01E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="16.367" />
-  <B value="-0.0076153" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="107.46" />
-  <Tmax units="K"  value="268.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.982868" />
-  <B value="0.255663" />
-  <C value="630" />
-  <D value="0.231239" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="610.98" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="101.1268" />
-  <B value="-9896.461" />
-  <C value="-11.12231" />
-  <D value="4.333878E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="630" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.3715E+07" />
-  <B value="1.1304" />
-  <C value="-1.7736" />
-  <D value="1.7333" />
-  <E value="-0.66961" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="610.98" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="1490" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="268.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="65879.9" />
-  <B value="415.0007" />
-  <C value="0.00004583" />
-  <D value="2.109E-09" />
-  <E value="-0.0000030816" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="465" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="50351" />
-  <B value="-464.92" />
-  <C value="12.353" />
-  <D value="0.00032078" />
-  <E value="-1.1521E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16573" />
-  <B value="-171.59" />
-  <C value="-61.863" />
-  <D value="-10326" />
-  <E value="-8446.2" />
-  <Tmin units="K"  value="315" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.8113" />
-  <B value="2947" />
-  <C value="-0.99316" />
-  <D value="4.0603E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="431.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.1919E-07" />
-  <B value="0.70935" />
-  <C value="211" />
-  <D value="-8775.4" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.011378" />
-  <B value="-96.849" />
-  <C value="-0.47605" />
-  <D value="-0.0029428" />
-  <E value="4.7129E-07" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="431.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00021463" />
-  <B value="0.94857" />
-  <C value="622.07" />
-  <D value="15372" />
-  <Tmin units="K"  value="431.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011359" />
-  <B value="194.04" />
-  <C value="-4.2168" />
-  <D value="0.0039447" />
-  <E value="-0.0000077857" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="610.98" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-3617.1" />
-  <B value="432.68" />
-  <C value="-0.26594" />
-  <D value="0.000065752" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.175" />
-  <B value="3679.7" />
-  <C value="-85.876" />
-  <Tmin units="K"  value="382.76" />
-  <Tmax units="K"  value="557.73" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="3.6732" />
-  <B value="-0.027534" />
-  <Tmin units="K"  value="268.65" />
-  <Tmax units="K"  value="431.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.267184" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.934566E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="331.2366" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.262" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="51.847" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0337966" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.94" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.604" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.082206" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.7825" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.524" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.604" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="25930" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.082206" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  <group id="32"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  <group id="30"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  <group id="32"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="14"  value="1" />
-  <group id="31"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-83-1" />
-<Smiles name="SMILES"  value="CNCCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="6863" />
-<CompoundID name="Name"  value="Dimethylethanolamine" />
-<StructureFormula name="Structure"  value="HOCH2CH2N(CH3)2" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="571.82" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4140000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.331" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="404.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="214.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="214.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0376223" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="89.1362" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.101094" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.710963" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.46249E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22790" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06017" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.63E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.02E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.64E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="384000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.65E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="13.805" />
-  <B value="-0.0080578" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="85.66" />
-  <Tmax units="K"  value="214.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.87166" />
-  <B value="0.26133" />
-  <C value="571.82" />
-  <D value="0.28585" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="571.82" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="121.6094" />
-  <B value="-10451.37" />
-  <C value="-14.23754" />
-  <D value="0.000006927" />
-  <E value="2" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="571.82" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.9011E+07" />
-  <B value="0.56455" />
-  <C value="-0.031757" />
-  <D value="-0.28621" />
-  <E value="0.17191" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="571.82" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="1800" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="214.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="66692" />
-  <B value="-55.489" />
-  <C value="10.897" />
-  <D value="0.0047237" />
-  <E value="-0.0000030382" />
-  <Tmin units="K"  value="299.91" />
-  <Tmax units="K"  value="425.91" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="71203" />
-  <B value="-582.55" />
-  <C value="12.891" />
-  <D value="-0.000082299" />
-  <E value="3.2172E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21155" />
-  <B value="-189.81" />
-  <C value="-51.091" />
-  <D value="-19900" />
-  <E value="29045" />
-  <Tmin units="K"  value="285.91" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-15.376" />
-  <B value="3350.8" />
-  <C value="-0.34232" />
-  <D value="9.4723E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="457.46" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2904E-07" />
-  <B value="0.77955" />
-  <C value="165.36" />
-  <D value="-6888.3" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.083559" />
-  <B value="-10.945" />
-  <C value="-0.99458" />
-  <D value="-0.00097463" />
-  <E value="-8.1342E-07" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="407.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00023136" />
-  <B value="0.92757" />
-  <C value="412.5" />
-  <D value="95357" />
-  <Tmin units="K"  value="407.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0127" />
-  <B value="89.713" />
-  <C value="-3.389" />
-  <D value="0.0019204" />
-  <E value="-0.0000065659" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="571.82" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-13496" />
-  <B value="570.3" />
-  <C value="-0.37223" />
-  <D value="0.000097254" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.242" />
-  <B value="3423.1" />
-  <C value="-87.75" />
-  <Tmin units="K"  value="345.92" />
-  <Tmax units="K"  value="500.29" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="4.354" />
-  <B value="-0.033071" />
-  <Tmin units="K"  value="214.15" />
-  <Tmax units="K"  value="457.46" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.32159" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.469723E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="296.5367" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="99.66" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0423961" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.892" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.710963" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.101094" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.4363" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.068" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.710963" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22790" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.101094" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  <group id="36"  value="1" />
-  <group id="1"  value="2" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="15"  value="1" />
-  <group id="31"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="1" />
-  <group id="15"  value="1" />
-  <group id="36"  value="1" />
-  <group id="1"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="14"  value="1" />
-  <group id="35"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-01-0" />
-<Smiles name="SMILES"  value="CN(C)CCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1760" />
-<CompoundID name="Name"  value="Nitromethane" />
-<StructureFormula name="Structure"  value="CH3NO2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="588" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5870000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.173" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.208" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="374.35" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="244.6" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="244.6" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="146.529" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="61.04" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.05396" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.348026" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.3544E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="25700" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.15E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03047" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.69E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.48E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-6940000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="275000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9703000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.13877" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-6.432E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="24.924" />
-  <B value="-0.011419" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="97.84" />
-  <Tmax units="K"  value="244.6" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.2195" />
-  <B value="0.22476" />
-  <C value="588.16" />
-  <D value="0.2787" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="588.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="93.27" />
-  <B value="-7345.1" />
-  <C value="-10.689" />
-  <D value="0.0000086998" />
-  <E value="2" />
-  <Tmin units="K"  value="244.15" />
-  <Tmax units="K"  value="588.15" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.160998E+07" />
-  <B value="-0.662124" />
-  <C value="2.67118" />
-  <D value="-2.702805" />
-  <E value="0.931262" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="570.07" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="24756" />
-  <B value="206.1" />
-  <C value="2.378" />
-  <D value="-0.021867" />
-  <E value="0.000053521" />
-  <Tmin units="K"  value="59.98" />
-  <Tmax units="K"  value="235.46" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="80588" />
-  <B value="345.48" />
-  <C value="6.7575" />
-  <D value="0.0084794" />
-  <E value="-0.0000031326" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="38681" />
-  <B value="-615.84" />
-  <C value="11.895" />
-  <D value="0.000023118" />
-  <E value="-2.9677E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.09758" />
-  <B value="-168.84" />
-  <C value="-42.71" />
-  <D value="-11412" />
-  <E value="-9713.2" />
-  <Tmin units="K"  value="294" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.411" />
-  <B value="1047.6" />
-  <C value="-0.095445" />
-  <D value="6.9198E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="374.35" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.2141E-07" />
-  <B value="0.64539" />
-  <C value="383.4" />
-  <D value="-1344.5" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.050889" />
-  <B value="-150.55" />
-  <C value="-0.2952" />
-  <D value="-0.0028403" />
-  <E value="-0.0000022109" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="374.35" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000031393" />
-  <B value="1.1117" />
-  <C value="-91.903" />
-  <D value="128140" />
-  <Tmin units="K"  value="374.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.04012" />
-  <B value="-18.606" />
-  <C value="-1.9227" />
-  <D value="-0.0017487" />
-  <E value="-7.2781E-07" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="570.07" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="34888" />
-  <B value="-9.1625" />
-  <C value="0.42886" />
-  <D value="-0.00055882" />
-  <E value="2.2116E-07" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="1000" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-17.75919" />
-  <B value="-10000" />
-  <C value="-118.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.699" />
-  <B value="3368.7" />
-  <C value="-43.222" />
-  <Tmin units="K"  value="353.09" />
-  <Tmax units="K"  value="515.82" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.171" />
-  <B value="-0.01068" />
-  <Tmin units="K"  value="244.6" />
-  <Tmax units="K"  value="374.35" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.16151" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.84307E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="134.6848" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.208" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="39.59" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.9816" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0238563" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.141871" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.348026" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.05396" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.0086" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.868" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.02291" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.348026" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="257" />
-<UnifacVLE name="UNIFAC" >
-  <group id="55"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="44"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="33"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="55"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="54"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-52-5" />
-<Smiles name="SMILES"  value="CN(=O)=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1761" />
-<CompoundID name="Name"  value="Nitroethane" />
-<StructureFormula name="Structure"  value="CH3CH2NO2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="557.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5160000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.236" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.247" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="387.22" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="183.63" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="183.63" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0317711" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="75.0666" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0720005" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.672348" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.7949E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23090" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.22E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0407" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.02E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.022E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4900000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="315400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9853000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.53" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.25E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="19.737" />
-  <B value="-0.01194" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="73.45" />
-  <Tmax units="K"  value="183.63" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.90007" />
-  <B value="0.22451" />
-  <C value="593.01" />
-  <D value="0.26359" />
-  <Tmin units="K"  value="183.63" />
-  <Tmax units="K"  value="593" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.03385" />
-  <B value="-7188.308" />
-  <C value="-8.680357" />
-  <D value="0.0000053196" />
-  <E value="2" />
-  <Tmin units="K"  value="183.63" />
-  <Tmax units="K"  value="595" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.428692E+07" />
-  <B value="0.314015" />
-  <C value="-0.225443" />
-  <D value="1.068645" />
-  <E value="-0.953684" />
-  <Tmin units="K"  value="183.63" />
-  <Tmax units="K"  value="549.91" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="5490.6" />
-  <B value="767.61" />
-  <C value="-3.7362" />
-  <D value="0.014315" />
-  <E value="-0.000017981" />
-  <Tmin units="K"  value="80" />
-  <Tmax units="K"  value="180" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="67990" />
-  <B value="798.52" />
-  <C value="2.4874" />
-  <D value="0.02816" />
-  <E value="-0.000027001" />
-  <Tmin units="K"  value="183.63" />
-  <Tmax units="K"  value="387.22" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="48198" />
-  <B value="-581.79" />
-  <C value="12.283" />
-  <D value="0.000023838" />
-  <E value="-2.2739E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.15234" />
-  <B value="-172.56" />
-  <C value="-45.201" />
-  <D value="-57753" />
-  <E value="108450" />
-  <Tmin units="K"  value="296.5" />
-  <Tmax units="K"  value="1892.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="15.403" />
-  <B value="194.75" />
-  <C value="-4.2217" />
-  <D value="0.0000078126" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="387.22" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.4631E-07" />
-  <B value="0.70062" />
-  <C value="285.76" />
-  <D value="-1030.8" />
-  <Tmin units="K"  value="183.63" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1486" />
-  <B value="6.324" />
-  <C value="-1.0708" />
-  <D value="0.00009663" />
-  <E value="-0.0000015981" />
-  <Tmin units="K"  value="183.63" />
-  <Tmax units="K"  value="387.22" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0011064" />
-  <B value="0.69186" />
-  <C value="675.03" />
-  <D value="236860" />
-  <Tmin units="K"  value="387.22" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0024376" />
-  <B value="342.16" />
-  <C value="-7.0402" />
-  <D value="0.016727" />
-  <E value="-0.000027883" />
-  <Tmin units="K"  value="183.63" />
-  <Tmax units="K"  value="549.91" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="10768" />
-  <B value="271.27" />
-  <C value="-0.13688" />
-  <D value="0.000024329" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-22.38503" />
-  <B value="-9850" />
-  <C value="-59.1" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.48" />
-  <B value="3381.9" />
-  <C value="-47.509" />
-  <Tmin units="K"  value="334.45" />
-  <Tmax units="K"  value="500" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.6566" />
-  <B value="-0.011965" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="387.22" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.215813" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.175128E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="236.916" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.247" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="60.11" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0298367" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.054543" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.380324" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0720005" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.6829" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.408" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.380324" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23090" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0720005" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="56"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="45"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="33"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="56"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="55"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-24-3" />
-<Smiles name="SMILES"  value="CCN(=O)=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1762" />
-<CompoundID name="Name"  value="1-nitropropane" />
-<StructureFormula name="Structure"  value="CH3CH2CH2NO2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="605" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4350000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.288" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.249" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="404.33" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="169.16" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="169.16" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.000688982" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="89.0932" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0894679" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.412773" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.359E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21290" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.22E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05093" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.37E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.24E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="335000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="355600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9220000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.09" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.859E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.957" />
-  <B value="-0.010505" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="67.66" />
-  <Tmax units="K"  value="169.16" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.85075" />
-  <B value="0.24483" />
-  <C value="605" />
-  <D value="0.27413" />
-  <Tmin units="K"  value="169.16" />
-  <Tmax units="K"  value="605" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="38.65807" />
-  <B value="-5750.644" />
-  <C value="-2.115655" />
-  <D value="-1.225423E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="169.16" />
-  <Tmax units="K"  value="605" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.6307E+07" />
-  <B value="0.47767" />
-  <C value="-0.18338" />
-  <D value="0.057255" />
-  <E value="-0.028311" />
-  <Tmin units="K"  value="169.16" />
-  <Tmax units="K"  value="605" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="131170" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="605" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-8835.6" />
-  <B value="176.43" />
-  <C value="9.53" />
-  <D value="0.0096176" />
-  <E value="-0.0000099253" />
-  <Tmin units="K"  value="169.16" />
-  <Tmax units="K"  value="404.33" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="57745" />
-  <B value="-538.37" />
-  <C value="12.483" />
-  <D value="0.00011202" />
-  <E value="-5.1502E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.18935" />
-  <B value="-215.56" />
-  <C value="-56.681" />
-  <D value="-61127" />
-  <E value="111790" />
-  <Tmin units="K"  value="302.5" />
-  <Tmax units="K"  value="1934.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-19.997" />
-  <B value="1653" />
-  <C value="1.2605" />
-  <D value="0.0000015194" />
-  <E value="2" />
-  <Tmin units="K"  value="240" />
-  <Tmax units="K"  value="404.33" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7108E-07" />
-  <B value="0.7401" />
-  <C value="220.03" />
-  <D value="-15.073" />
-  <Tmin units="K"  value="169.16" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.068381" />
-  <B value="13.221" />
-  <C value="-1.3628" />
-  <D value="-0.00024357" />
-  <E value="-0.0000012535" />
-  <Tmin units="K"  value="169.16" />
-  <Tmax units="K"  value="404.33" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0022117" />
-  <B value="0.61538" />
-  <C value="875.34" />
-  <D value="312410" />
-  <Tmin units="K"  value="404.33" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035529" />
-  <B value="0.58517" />
-  <C value="-2.3314" />
-  <D value="-0.00099947" />
-  <E value="-0.0000011138" />
-  <Tmin units="K"  value="169.16" />
-  <Tmax units="K"  value="605" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="8797.2" />
-  <B value="373.51" />
-  <C value="-0.1991" />
-  <D value="0.000038609" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.552" />
-  <B value="3564.5" />
-  <C value="-49.073" />
-  <Tmin units="K"  value="363.15" />
-  <Tmax units="K"  value="536.18" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.6872" />
-  <B value="-0.011404" />
-  <Tmin units="K"  value="240" />
-  <Tmax units="K"  value="404.33" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.270875" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.535366E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="264.8416" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.249" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="80.63" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0376918" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.006497" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.412773" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0894679" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.3573" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.948" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.412773" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21290" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0894679" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="56"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="45"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="33"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="56"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="55"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="108-03-2" />
-<Smiles name="SMILES"  value="CCCN(=O)=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1763" />
-<CompoundID name="Name"  value="2-nitropropane" />
-<StructureFormula name="Structure"  value="CH3CH(NO2)CH3" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="595" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4450000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.288" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.26" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="393.4" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="181.83" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="181.83" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.021584" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="89.0932" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0905535" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.383568" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.273E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20530" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.24E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05092" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.36E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.39E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.2803E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="347700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="7790000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.846E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.679" />
-  <B value="-0.0096732" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72.73" />
-  <Tmax units="K"  value="181.83" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.27031" />
-  <B value="0.13967" />
-  <C value="595" />
-  <D value="0.17588" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="594" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="57.04038" />
-  <B value="-6262.318" />
-  <C value="-4.993807" />
-  <D value="1.61213E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="594" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.543435E+07" />
-  <B value="0.377393" />
-  <C value="0.18894" />
-  <D value="-0.0391329" />
-  <E value="-0.243258" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="594" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="131170" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="595" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="67863" />
-  <B value="138.63" />
-  <C value="8.8679" />
-  <D value="0.01051" />
-  <E value="-0.00001051" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="393.4" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="58543" />
-  <B value="-558.36" />
-  <C value="12.559" />
-  <D value="0.000040137" />
-  <E value="-3.1383E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17935" />
-  <B value="-204.53" />
-  <C value="-50.86" />
-  <D value="-56062" />
-  <E value="103000" />
-  <Tmin units="K"  value="297" />
-  <Tmax units="K"  value="1899" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-26.48" />
-  <B value="1441.6" />
-  <C value="2.6439" />
-  <D value="-0.0000074647" />
-  <E value="2" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="393.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000005644" />
-  <B value="0.32789" />
-  <C value="1291.7" />
-  <D value="6279.8" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.085284" />
-  <B value="-50.915" />
-  <C value="-1.467" />
-  <D value="-0.0035856" />
-  <E value="-0.000001687" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="393.4" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0042281" />
-  <B value="0.52696" />
-  <C value="790.25" />
-  <D value="431610" />
-  <Tmin units="K"  value="393.4" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015626" />
-  <B value="18.663" />
-  <C value="-2.7222" />
-  <D value="-0.00050234" />
-  <E value="-0.0000033626" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="594" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="7449" />
-  <B value="381.45" />
-  <C value="-0.20531" />
-  <D value="0.000039841" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.572" />
-  <B value="3562.3" />
-  <C value="-38.858" />
-  <Tmin units="K"  value="363.15" />
-  <Tmax units="K"  value="528.92" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9011" />
-  <B value="-0.014208" />
-  <Tmin units="K"  value="181.83" />
-  <Tmax units="K"  value="393.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.270821" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.20499E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="304.3226" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.26" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="80.63" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0372943" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.994733" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.383568" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0905535" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.3573" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.948" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.383568" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20530" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0905535" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="56"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
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-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
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-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="55"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-46-9" />
-<Smiles name="SMILES"  value="CC(N(=O)=O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1769" />
-<CompoundID name="Name"  value="1-nitrobutane" />
-<StructureFormula name="Structure"  value="CH3(CH2)3NO2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="623" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3600000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.338" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.248" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="425.92" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="191.82" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="191.82" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00329301" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="103.12" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.106476" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.454584" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.558E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20780" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.13E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06116" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.72E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.439E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.5E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="379100" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.27E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.08195" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.46965E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="13.265" />
-  <B value="-0.0086439" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="76.73" />
-  <Tmax units="K"  value="191.82" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.709" />
-  <B value="0.24401" />
-  <C value="623" />
-  <D value="0.28339" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="600.31" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="275.2044" />
-  <B value="-15483.84" />
-  <C value="-38.70231" />
-  <D value="0.0000386" />
-  <E value="2" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="623" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.525605E+07" />
-  <B value="-1.025854" />
-  <C value="4.47262" />
-  <D value="-4.675607" />
-  <E value="1.466497" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="600.31" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="1900" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="191.82" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="56152" />
-  <B value="6.6387" />
-  <C value="10.762" />
-  <D value="0.003942" />
-  <E value="-0.0000013791" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="467.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="69545" />
-  <B value="-548.77" />
-  <C value="12.729" />
-  <D value="0.0001233" />
-  <E value="-6.7656E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.22917" />
-  <B value="-262.47" />
-  <C value="-73.827" />
-  <D value="-67561" />
-  <E value="117970" />
-  <Tmin units="K"  value="311.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.4776" />
-  <B value="1274.9" />
-  <C value="-0.51437" />
-  <D value="0.0000019485" />
-  <E value="2" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="425.92" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.0308E-08" />
-  <B value="0.82266" />
-  <C value="144.36" />
-  <D value="-9193.7" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.088752" />
-  <B value="4.014" />
-  <C value="-1.2388" />
-  <D value="-0.00043694" />
-  <E value="-0.0000009691" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="425.92" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013665" />
-  <B value="0.98745" />
-  <C value="630.3" />
-  <D value="15608" />
-  <Tmin units="K"  value="425.92" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.043136" />
-  <B value="2.5171" />
-  <C value="-2.3094" />
-  <D value="-0.00084543" />
-  <E value="-8.2017E-07" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="600.31" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-1162" />
-  <B value="505.07" />
-  <C value="-0.28865" />
-  <D value="0.000060633" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.871" />
-  <B value="3253.5" />
-  <C value="-77.411" />
-  <Tmin units="K"  value="383.15" />
-  <Tmax units="K"  value="554.92" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.177" />
-  <B value="-0.015145" />
-  <Tmin units="K"  value="191.82" />
-  <Tmax units="K"  value="425.92" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.327091" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.926947E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="268.7988" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.248" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="101.15" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0450147" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.978442" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.454584" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.106476" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.0317" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.488" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.454584" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20780" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.106476" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="56"  value="1" />
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-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
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-  <group id="45"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
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-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="56"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="2" />
-  <group id="55"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="627-05-4" />
-<Smiles name="SMILES"  value="CCCCN(=O)=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1778" />
-<CompoundID name="Name"  value="O-nitrotoluene" />
-<StructureFormula name="Structure"  value="C6H4(NO2)(CH3)" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="720" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.441" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.28" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="494.85" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="269.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="269.98" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.72928" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="137.136" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.118442" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.487824" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.309E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21420" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.25E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07379" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.27E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="4.71E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.715E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.148E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2029" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.5914E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.967" />
-  <B value="-0.0045272" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="107.99" />
-  <Tmax units="K"  value="269.98" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.49527" />
-  <B value="0.21852" />
-  <C value="720" />
-  <D value="0.27202" />
-  <Tmin units="K"  value="269.98" />
-  <Tmax units="K"  value="720" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="110.496" />
-  <B value="-10356.21" />
-  <C value="-12.86215" />
-  <D value="7.080827E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="265" />
-  <Tmax units="K"  value="720" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.853006E+07" />
-  <B value="0.959622" />
-  <C value="-1.263212" />
-  <D value="1.073123" />
-  <E value="-0.436452" />
-  <Tmin units="K"  value="269.98" />
-  <Tmax units="K"  value="720" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="23321" />
-  <B value="179.27" />
-  <C value="6.0748" />
-  <D value="-0.034038" />
-  <E value="0.000061259" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="269.98" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="167320" />
-  <B value="675.67" />
-  <C value="2.8482" />
-  <D value="0.023742" />
-  <E value="-0.00001748" />
-  <Tmin units="K"  value="269.98" />
-  <Tmax units="K"  value="540" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="126830" />
-  <B value="-1053.5" />
-  <C value="13.982" />
-  <D value="-0.0011308" />
-  <E value="3.2272E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25342" />
-  <B value="-324.82" />
-  <C value="-137.34" />
-  <D value="-228340" />
-  <E value="439210" />
-  <Tmin units="K"  value="360" />
-  <Tmax units="K"  value="1980" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-227.78" />
-  <B value="9560.6" />
-  <C value="33.954" />
-  <D value="-0.00004379" />
-  <E value="2" />
-  <Tmin units="K"  value="269.98" />
-  <Tmax units="K"  value="576" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.9111E-08" />
-  <B value="0.92063" />
-  <C value="61.279" />
-  <D value="-2619.3" />
-  <Tmin units="K"  value="269.98" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.28005" />
-  <B value="20.455" />
-  <C value="-0.90478" />
-  <D value="0.000049377" />
-  <E value="-4.8022E-07" />
-  <Tmin units="K"  value="216" />
-  <Tmax units="K"  value="576" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013501" />
-  <B value="0.95252" />
-  <C value="632.43" />
-  <D value="27080" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.07846" />
-  <B value="-32.848" />
-  <C value="-1.5968" />
-  <D value="-0.0015031" />
-  <E value="3.3724E-07" />
-  <Tmin units="K"  value="269.98" />
-  <Tmax units="K"  value="720" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13539" />
-  <B value="550.05" />
-  <C value="-0.32279" />
-  <D value="0.000069576" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-20.0046" />
-  <B value="-10000" />
-  <C value="-82.2" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.718" />
-  <B value="4428.1" />
-  <C value="-60.639" />
-  <Tmin units="K"  value="435.78" />
-  <Tmax units="K"  value="645" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.2034" />
-  <B value="-0.01309" />
-  <Tmin units="K"  value="269.98" />
-  <Tmax units="K"  value="576" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.398619" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.543371E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="480.8555" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.28" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="107.72" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-0.61215" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.054527" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.057273" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.487824" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.118442" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2801" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.272" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="1.2945" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.487824" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21420" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.118442" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
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-  <group id="58"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
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-<Umr name="UMR" >
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-  <group id="12"  value="1" />
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-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="57"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="88-72-2" />
-<Smiles name="SMILES"  value="c1(C)c(N(=O)=O)cccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1779" />
-<CompoundID name="Name"  value="P-nitrotoluene" />
-<StructureFormula name="Structure"  value="C6H4(NO2)(CH3)" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="736" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.441" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.229" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="511.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="325.05" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="324.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="40.4829" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="137.136" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.121894" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.542405" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.371E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21110" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.48E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07379" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.27E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="3.1E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.554E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.6676E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.178424" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.553E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.955" />
-  <B value="-0.0051608" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="324.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.76802" />
-  <B value="0.27463" />
-  <C value="736" />
-  <D value="0.3126" />
-  <Tmin units="K"  value="320.15" />
-  <Tmax units="K"  value="720.99" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="115.4618" />
-  <B value="-11239.6" />
-  <C value="-13.3636" />
-  <D value="5.387653E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="324.75" />
-  <Tmax units="K"  value="743" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.550237E+08" />
-  <B value="1.89329" />
-  <C value="-1.014085" />
-  <D value="-0.0168324" />
-  <E value="-0.442436" />
-  <Tmin units="K"  value="324.75" />
-  <Tmax units="K"  value="720.99" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="8048.3" />
-  <B value="609060" />
-  <C value="-6008.8" />
-  <D value="19.783" />
-  <E value="-0.021716" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="307.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="90280" />
-  <B value="945.96" />
-  <C value="3.9359" />
-  <D value="0.019415" />
-  <E value="-0.000013352" />
-  <Tmin units="K"  value="324.75" />
-  <Tmax units="K"  value="557.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="126830" />
-  <B value="-1053.5" />
-  <C value="13.982" />
-  <D value="-0.0011308" />
-  <E value="3.2272E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.3096" />
-  <B value="-430.56" />
-  <C value="-175.46" />
-  <D value="-349500" />
-  <E value="685920" />
-  <Tmin units="K"  value="371.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-164.01" />
-  <B value="7455.2" />
-  <C value="23.73" />
-  <D value="-0.000026464" />
-  <E value="2" />
-  <Tmin units="K"  value="320.15" />
-  <Tmax units="K"  value="594.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.1207E-08" />
-  <B value="0.91154" />
-  <C value="64.997" />
-  <D value="-92.66" />
-  <Tmin units="K"  value="324.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.1404" />
-  <B value="23.385" />
-  <C value="-1.2743" />
-  <D value="-0.000067534" />
-  <E value="-5.8708E-07" />
-  <Tmin units="K"  value="220.8" />
-  <Tmax units="K"  value="580.8" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000064675" />
-  <B value="1.0353" />
-  <C value="391.41" />
-  <D value="37904" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.017488" />
-  <B value="-28.223" />
-  <C value="-2.4034" />
-  <D value="-0.00054634" />
-  <E value="-0.0000022569" />
-  <Tmin units="K"  value="324.75" />
-  <Tmax units="K"  value="720.99" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13539" />
-  <B value="550.05" />
-  <C value="-0.32279" />
-  <D value="0.000069576" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-21.94037" />
-  <B value="-10000" />
-  <C value="-66.6" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.068" />
-  <B value="4086.9" />
-  <C value="-83.592" />
-  <Tmin units="K"  value="445" />
-  <Tmax units="K"  value="654.95" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.6317" />
-  <B value="-0.0093276" />
-  <Tmin units="K"  value="320.15" />
-  <Tmax units="K"  value="594.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.398619" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.328918E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="238.341" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.229" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="107.72" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.054156" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.050112" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.542405" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.121894" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2801" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.272" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.425222" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21110" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.121894" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="58"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="47"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="34"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="58"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="57"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="99-99-0" />
-<Smiles name="SMILES"  value="c1(C)ccc(N(=O)=O)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1780" />
-<CompoundID name="Name"  value="M-nitrotoluene" />
-<StructureFormula name="Structure"  value="C6H4(NO2)(CH3)" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="734" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.441" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="504" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="288.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="289.2" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="6.84272" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="137.136" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.118913" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.491987" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.468E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21470" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.41E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07379" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.27E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.58E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.502E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="380800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.406E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.21" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.5696E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.744" />
-  <B value="-0.0041348" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="115.68" />
-  <Tmax units="K"  value="289.2" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50673" />
-  <B value="0.22353" />
-  <C value="734" />
-  <D value="0.25642" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="734" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="174.0974" />
-  <B value="-13266.49" />
-  <C value="-22.50751" />
-  <D value="0.0000146534" />
-  <E value="2" />
-  <Tmin units="K"  value="289.2" />
-  <Tmax units="K"  value="734" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.23147E+08" />
-  <B value="2.991682" />
-  <C value="-5.10633" />
-  <D value="3.432299" />
-  <E value="-0.844633" />
-  <Tmin units="K"  value="289.2" />
-  <Tmax units="K"  value="734" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="13048" />
-  <B value="562.7" />
-  <C value="1.2374" />
-  <D value="-0.0092642" />
-  <E value="0.000017191" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="289.2" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="165480" />
-  <B value="678.6" />
-  <C value="2.6976" />
-  <D value="0.024579" />
-  <E value="-0.000018568" />
-  <Tmin units="K"  value="289.2" />
-  <Tmax units="K"  value="550.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="126830" />
-  <B value="-1053.5" />
-  <C value="13.982" />
-  <D value="-0.0011308" />
-  <E value="3.2272E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.2479" />
-  <B value="-319.54" />
-  <C value="-155.56" />
-  <D value="-309650" />
-  <E value="619890" />
-  <Tmin units="K"  value="367" />
-  <Tmax units="K"  value="1687" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-219.04" />
-  <B value="9323.8" />
-  <C value="32.506" />
-  <D value="-0.000040609" />
-  <E value="2" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="587.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.6657E-08" />
-  <B value="0.9283" />
-  <C value="56.912" />
-  <D value="-1935.8" />
-  <Tmin units="K"  value="289.2" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.16653" />
-  <B value="2.5129" />
-  <C value="-1.0577" />
-  <D value="-0.0003596" />
-  <E value="-3.0249E-07" />
-  <Tmin units="K"  value="289.2" />
-  <Tmax units="K"  value="587.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013182" />
-  <B value="0.95336" />
-  <C value="611.68" />
-  <D value="32295" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.028468" />
-  <B value="-35.938" />
-  <C value="-2.0197" />
-  <D value="-0.0016065" />
-  <E value="-6.1813E-07" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="710.53" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13539" />
-  <B value="550.05" />
-  <C value="-0.32279" />
-  <D value="0.000069576" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-21.29583" />
-  <B value="-10000" />
-  <C value="-71.4" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.046" />
-  <B value="4823.7" />
-  <C value="-47.238" />
-  <Tmin units="K"  value="444.4" />
-  <Tmax units="K"  value="645" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.7259" />
-  <B value="-0.011764" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="587.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.398619" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.686394E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="459.4169" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.275" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="107.72" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0536831" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.052241" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.491987" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.118913" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.2801" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.272" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.491987" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21470" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.118913" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="58"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="47"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="34"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="12"  value="1" />
-  <group id="58"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="11"  value="1" />
-  <group id="57"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="99-08-1" />
-<Smiles name="SMILES"  value="c1(C)cc(N(=O)=O)ccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2743" />
-<CompoundID name="Name"  value="2,4-dinitrotoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H3)(NO2)2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="814" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.487" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.245" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="553" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="333" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="342.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.8719" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="182.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.137448" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.712571" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.07E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21470" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.44E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08807" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.112E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="3.36E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.18E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.0126E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.416E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.4055" />
-  <B value="-0.00020398" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="297.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.5108" />
-  <B value="0.24037" />
-  <C value="814" />
-  <D value="0.26806" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="789.19" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="128.9329" />
-  <B value="-13393.44" />
-  <C value="-15.15736" />
-  <D value="5.597038E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="814" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.2919E+08" />
-  <B value="1.3248" />
-  <C value="1.0872" />
-  <D value="-4.8737" />
-  <E value="2.858" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="789.19" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="48.36" />
-  <B value="3539.4" />
-  <C value="-18.134" />
-  <D value="0.041289" />
-  <E value="-0.000035254" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="297.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="88958" />
-  <B value="1324.4" />
-  <C value="2.7528" />
-  <D value="0.019721" />
-  <E value="-0.000011079" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="590" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94512" />
-  <B value="-582.56" />
-  <C value="13.27" />
-  <D value="-0.00026587" />
-  <E value="5.3735E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.31157" />
-  <B value="-359" />
-  <C value="-324.62" />
-  <D value="-771130" />
-  <E value="1449700" />
-  <Tmin units="K"  value="407" />
-  <Tmax units="K"  value="1871.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-41.408" />
-  <B value="3947.7" />
-  <C value="4.2203" />
-  <D value="-0.0000035178" />
-  <E value="2" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="590" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9809E-08" />
-  <B value="1.0159" />
-  <C value="22.316" />
-  <D value="-3670.3" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.057001" />
-  <B value="-67.01" />
-  <C value="-0.90194" />
-  <D value="-0.0013614" />
-  <E value="-3.0209E-08" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="590" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00011852" />
-  <B value="0.95914" />
-  <C value="734.05" />
-  <D value="13896" />
-  <Tmin units="K"  value="590" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.076326" />
-  <B value="-4.6299" />
-  <C value="-1.6478" />
-  <D value="-0.0012028" />
-  <E value="7.9965E-08" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="789.19" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14258" />
-  <B value="768.51" />
-  <C value="-0.52986" />
-  <D value="0.00013246" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="24.142" />
-  <B value="7851.3" />
-  <C value="30.661" />
-  <Tmin units="K"  value="490" />
-  <Tmax units="K"  value="714.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.46" />
-  <B value="-0.013192" />
-  <Tmin units="K"  value="342.65" />
-  <Tmax units="K"  value="590" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.483027" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.938808E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="336.1519" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.245" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="122.08" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.065157" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.376363" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.712571" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.137448" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.7" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.376" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.712571" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21470" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.137448" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="47"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  <group id="34"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="57"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="121-14-2" />
-<Smiles name="SMILES"  value="c1(C)c(N(=O)=O)cc(N(=O)=O)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2744" />
-<CompoundID name="Name"  value="2,6-dinitrotoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H3)(NO2)2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="780" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.487" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.242" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="553" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="339" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="337.85" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="24.9565" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="182.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.136568" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.714206" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.887E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20760" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.37E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08807" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.112E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.86E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.32E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.12E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.429E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.4498" />
-  <B value="-1.9264E-08" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="297.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.27332" />
-  <B value="0.17415" />
-  <C value="780" />
-  <D value="0.22386" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="747.26" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="115.7657" />
-  <B value="-12082.2" />
-  <C value="-13.31782" />
-  <D value="5.09858E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="770" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.041715E+08" />
-  <B value="1.247529" />
-  <C value="0.0309575" />
-  <D value="-2.851863" />
-  <E value="1.938855" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="770" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="8264.5" />
-  <B value="917.86" />
-  <C value="-1.527" />
-  <D value="0.0032636" />
-  <E value="-0.0000030408" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="337.85" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="163490" />
-  <B value="785.69" />
-  <C value="5.0684" />
-  <D value="0.014589" />
-  <E value="-0.0000070833" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="558" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94512" />
-  <B value="-582.56" />
-  <C value="13.27" />
-  <D value="-0.00026587" />
-  <E value="5.3735E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.5317" />
-  <B value="-704.49" />
-  <C value="-124.14" />
-  <D value="-895340" />
-  <E value="2377800" />
-  <Tmin units="K"  value="385" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-70.386" />
-  <B value="5310.9" />
-  <C value="8.6262" />
-  <D value="-0.0000081126" />
-  <E value="2" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="558" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.9592E-08" />
-  <B value="0.88167" />
-  <C value="135.78" />
-  <D value="-11605" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.039901" />
-  <B value="-99.466" />
-  <C value="-0.76681" />
-  <D value="-0.0019329" />
-  <E value="1.8512E-07" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="558" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00015932" />
-  <B value="0.92355" />
-  <C value="690.15" />
-  <D value="19720" />
-  <Tmin units="K"  value="558" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012803" />
-  <B value="255.04" />
-  <C value="-4.0121" />
-  <D value="0.0034159" />
-  <E value="-0.0000055401" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="770" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14258" />
-  <B value="768.51" />
-  <C value="-0.52986" />
-  <D value="0.00013246" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="26.68" />
-  <B value="10368" />
-  <C value="125.19" />
-  <Tmin units="K"  value="470" />
-  <Tmax units="K"  value="701.77" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-0.49935" />
-  <B value="-0.0153" />
-  <Tmin units="K"  value="337.85" />
-  <Tmax units="K"  value="558" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.483027" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.057052E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="308.1365" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.242" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="122.08" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0654633" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.383668" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.714206" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.136568" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.7" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.376" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.714206" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20760" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.136568" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="47"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
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-  </Asog>
-<Umr name="UMR" >
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-  <group id="12"  value="1" />
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-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="57"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="606-20-2" />
-<Smiles name="SMILES"  value="c1c(N(=O)=O)c(C)c(N(=O)=O)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2745" />
-<CompoundID name="Name"  value="3,4-dinitrotoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H3)(NO2)2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="842" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.487" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.237" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="610" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="331.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="331.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2.66366" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="182.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.139231" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.709209" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.859E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21410" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.13E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08807" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.112E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="3.58E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.59E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.08E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.466E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.1125" />
-  <B value="-0.0030536" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="132.58" />
-  <Tmax units="K"  value="332" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.48567" />
-  <B value="0.23619" />
-  <C value="842" />
-  <D value="0.28583" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="842" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="62.33838" />
-  <B value="-11025.98" />
-  <C value="-5.109566" />
-  <D value="1.997931E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="842" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.888359E+07" />
-  <B value="-1.153409" />
-  <C value="5.750305" />
-  <D value="-8.495374" />
-  <E value="4.124815" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="842" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="8196.6" />
-  <B value="920.11" />
-  <C value="-1.551" />
-  <D value="0.0033644" />
-  <E value="-0.0000031849" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="331.45" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="144440" />
-  <B value="677.88" />
-  <C value="6.2554" />
-  <D value="0.011911" />
-  <E value="-0.000005235" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="610" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94512" />
-  <B value="-582.56" />
-  <C value="13.27" />
-  <D value="-0.00026587" />
-  <E value="5.3735E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.28426" />
-  <B value="-305.85" />
-  <C value="-425.92" />
-  <D value="-1893800" />
-  <E value="4300100" />
-  <Tmin units="K"  value="421" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-13.817" />
-  <B value="2734.2" />
-  <C value="0.029663" />
-  <D value="-2.4471E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="610" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.8655E-08" />
-  <B value="0.96106" />
-  <C value="104.06" />
-  <D value="-10189" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.082395" />
-  <B value="-25.284" />
-  <C value="-1.0996" />
-  <D value="-0.00075328" />
-  <E value="-2.6136E-07" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="610" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0001043" />
-  <B value="0.96342" />
-  <C value="702.61" />
-  <D value="22699" />
-  <Tmin units="K"  value="610" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.012927" />
-  <B value="157.29" />
-  <C value="-3.3747" />
-  <D value="0.0014221" />
-  <E value="-0.000003365" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="842" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14258" />
-  <B value="768.51" />
-  <C value="-0.52986" />
-  <D value="0.00013246" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="26.341" />
-  <B value="10770" />
-  <C value="116.96" />
-  <Tmin units="K"  value="519.55" />
-  <Tmax units="K"  value="740" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.4661" />
-  <B value="-0.013088" />
-  <Tmin units="K"  value="331.45" />
-  <Tmax units="K"  value="610" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.483027" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.261456E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="308.5456" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.237" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="122.08" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0651537" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.348237" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.709209" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.139231" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.7" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.376" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.709209" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21410" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.139231" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="47"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  <group id="34"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="57"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="610-39-9" />
-<Smiles name="SMILES"  value="c1c(N(=O)=O)c(N(=O)=O)cc(C)c1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2748" />
-<CompoundID name="Name"  value="2,5-dinitrotoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H3)(NO2)2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="814" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.487" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.237" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="590" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="325.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="323.48" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="3.04164" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="182.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.135666" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.712285" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.997E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21390" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.93E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08807" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.112E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.71E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.36E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.03E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.446E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.3517" />
-  <B value="-0.0032112" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="129.39" />
-  <Tmax units="K"  value="325.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50237" />
-  <B value="0.23693" />
-  <C value="814" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="814" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="90.89499" />
-  <B value="-12036.13" />
-  <C value="-9.395524" />
-  <D value="2.853055E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="814" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.5817E+07" />
-  <B value="-1.8578" />
-  <C value="6.6656" />
-  <D value="-8.4526" />
-  <E value="3.8136" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="814" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="8111.1" />
-  <B value="922.97" />
-  <C value="-1.582" />
-  <D value="0.0034965" />
-  <E value="-0.0000033776" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="323.48" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="152220" />
-  <B value="711.2" />
-  <C value="5.8598" />
-  <D value="0.012789" />
-  <E value="-0.0000058246" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="590" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94512" />
-  <B value="-582.56" />
-  <C value="13.27" />
-  <D value="-0.00026587" />
-  <E value="5.3735E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.34331" />
-  <B value="-415.02" />
-  <C value="-293.07" />
-  <D value="-272710" />
-  <E value="53719" />
-  <Tmin units="K"  value="407" />
-  <Tmax units="K"  value="1871" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-10.391" />
-  <B value="2604.7" />
-  <C value="-0.5024" />
-  <D value="5.1688E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="590" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="3.8924E-08" />
-  <B value="0.93015" />
-  <C value="82.835" />
-  <D value="-8099.3" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.078898" />
-  <B value="-29.065" />
-  <C value="-1.0796" />
-  <D value="-0.00084649" />
-  <E value="-2.5074E-07" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="590" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0001568" />
-  <B value="0.92031" />
-  <C value="704.11" />
-  <D value="20197" />
-  <Tmin units="K"  value="590" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.014691" />
-  <B value="149.15" />
-  <C value="-3.2422" />
-  <D value="0.0014191" />
-  <E value="-0.0000035371" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="814" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14258" />
-  <B value="768.51" />
-  <C value="-0.52986" />
-  <D value="0.00013246" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="25.215" />
-  <B value="8927.2" />
-  <C value="62.336" />
-  <Tmin units="K"  value="489.39" />
-  <Tmax units="K"  value="710.73" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.0809" />
-  <B value="-0.013945" />
-  <Tmin units="K"  value="323.48" />
-  <Tmax units="K"  value="590" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.483027" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.261456E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="298.2852" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.237" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="122.08" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0651127" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.377369" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.712285" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.135666" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.7" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.376" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.712285" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21390" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.135666" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
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-  <group id="47"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
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-  </Asog>
-<Umr name="UMR" >
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-  <group id="58"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
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-  <group id="57"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="619-15-8" />
-<Smiles name="SMILES"  value="c1(N(=O)=O)c(C)cc(N(=O)=O)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2749" />
-<CompoundID name="Name"  value="3,5-dinitrotoluene" />
-<StructureFormula name="Structure"  value="CH3(C6H3)(NO2)2" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="800" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2150000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.487" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.238" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="588" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="366.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="365.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="35.4684" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="182.134" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.140577" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.702302" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.314E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21440" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.44E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08807" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.112E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.71E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.34E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="414000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.29E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.437E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.0259" />
-  <B value="-0.0027445" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="146.26" />
-  <Tmax units="K"  value="365.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.45727" />
-  <B value="0.227" />
-  <C value="814.01" />
-  <D value="0.27155" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="814" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="63.61855" />
-  <B value="-10355.64" />
-  <C value="-5.423477" />
-  <D value="2.374318E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="814" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.989509E+07" />
-  <B value="-0.991558" />
-  <C value="3.414071" />
-  <D value="-4.448985" />
-  <E value="2.238465" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="790.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="8551.8" />
-  <B value="908.56" />
-  <C value="-1.4311" />
-  <D value="0.0028756" />
-  <E value="-0.0000025075" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="365.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="211860" />
-  <B value="-5.3058" />
-  <C value="8.1208" />
-  <D value="0.009225" />
-  <E value="-0.0000034389" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="588" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="94512" />
-  <B value="-582.56" />
-  <C value="13.27" />
-  <D value="-0.00026587" />
-  <E value="5.3735E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.31159" />
-  <B value="-362.24" />
-  <C value="-319.87" />
-  <D value="-785450" />
-  <E value="1509600" />
-  <Tmin units="K"  value="407" />
-  <Tmax units="K"  value="1871" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-0.25652" />
-  <B value="2097.7" />
-  <C value="-2.0147" />
-  <D value="0.0000014987" />
-  <E value="2" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="588" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.7633E-08" />
-  <B value="0.90246" />
-  <C value="116.57" />
-  <D value="-8469.6" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.029795" />
-  <B value="-134.57" />
-  <C value="-0.63203" />
-  <D value="-0.0021751" />
-  <E value="3.0388E-07" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="588" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00014433" />
-  <B value="0.92815" />
-  <C value="684.42" />
-  <D value="24021" />
-  <Tmin units="K"  value="588" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.02022" />
-  <B value="191.13" />
-  <C value="-3.4062" />
-  <D value="0.001628" />
-  <E value="-0.0000032376" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="790.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14258" />
-  <B value="768.51" />
-  <C value="-0.52986" />
-  <D value="0.00013246" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="24.061" />
-  <B value="7289.5" />
-  <C value="-7.1177" />
-  <Tmin units="K"  value="483.64" />
-  <Tmax units="K"  value="719.61" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.8766" />
-  <B value="-0.012458" />
-  <Tmin units="K"  value="365.65" />
-  <Tmax units="K"  value="588" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.483027" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.219819E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="297.6324" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.238" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="122.08" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0647636" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.370051" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.702302" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.140577" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.7" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.376" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.702302" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21440" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.140577" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="47"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="3" />
-  <group id="11"  value="3" />
-  <group id="34"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="3" />
-  <group id="12"  value="1" />
-  <group id="58"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="3" />
-  <group id="11"  value="1" />
-  <group id="57"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="618-85-9" />
-<Smiles name="SMILES"  value="c1(C)cc(N(=O)=O)cc(N(=O)=O)c1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2747" />
-<CompoundID name="Name"  value="2,4,6-trinitrotoluene" />
-<StructureFormula name="Structure"  value="(CH3)C6H2(NO2)3" />
-<Family name="Family"  value="39" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="795" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3040000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.48" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="573" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="355" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="354" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.936248" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="227.131" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.154989" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.897249" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.914E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="23070" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.87E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10235" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.217E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.64E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="2.844E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="460700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.12E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.2919E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.6459" />
-  <B value="-0.0046892" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="352.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.99663" />
-  <B value="0.34261" />
-  <C value="803.06" />
-  <D value="0.50647" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="803.05" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="245.81" />
-  <B value="-20425" />
-  <C value="-32.225" />
-  <D value="0.00001503" />
-  <E value="2" />
-  <Tmin units="K"  value="354" />
-  <Tmax units="K"  value="828" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="2.111008E+07" />
-  <B value="-12.33056" />
-  <C value="37.27643" />
-  <D value="-41.67226" />
-  <E value="16.622" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="778.11" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-337310" />
-  <B value="4588.5" />
-  <C value="-14.24" />
-  <D value="0.030526" />
-  <E value="-0.000030713" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="353.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="188750" />
-  <B value="750.94" />
-  <C value="4.5661" />
-  <D value="0.019107" />
-  <E value="-0.00001348" />
-  <Tmin units="K"  value="354" />
-  <Tmax units="K"  value="625" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="209680" />
-  <B value="-1410.9" />
-  <C value="14.902" />
-  <D value="-0.0017672" />
-  <E value="4.5403E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.37998" />
-  <B value="-379.85" />
-  <C value="-418.42" />
-  <D value="-567110" />
-  <E value="576970" />
-  <Tmin units="K"  value="414" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="92.002" />
-  <B value="-1238.6" />
-  <C value="-16.127" />
-  <D value="0.000013297" />
-  <E value="2" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="625" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.1205E-08" />
-  <B value="0.89283" />
-  <C value="134.66" />
-  <D value="-13583" />
-  <Tmin units="K"  value="354" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.10196" />
-  <B value="-488.31" />
-  <C value="0.35873" />
-  <D value="-0.0039133" />
-  <E value="0.0000039064" />
-  <Tmin units="K"  value="357.2" />
-  <Tmax units="K"  value="393.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00015986" />
-  <B value="0.89621" />
-  <C value="647.63" />
-  <D value="36973" />
-  <Tmin units="K"  value="625" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015319" />
-  <B value="-305.07" />
-  <C value="-0.19869" />
-  <D value="-0.0050479" />
-  <E value="5.8446E-07" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="778.11" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="63628" />
-  <B value="610.44" />
-  <C value="-0.32626" />
-  <D value="0.000055813" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-21.91636" />
-  <B value="-10000" />
-  <C value="-66" />
-  <Tmin units="K"  value="274.7056" />
-  <Tmax units="K"  value="444.7056" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.3" />
-  <B value="5815.6" />
-  <C value="-83.892" />
-  <Tmin units="K"  value="478.74" />
-  <Tmax units="K"  value="703.26" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="0.72019" />
-  <B value="-0.015685" />
-  <Tmin units="K"  value="353.15" />
-  <Tmax units="K"  value="625" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.571879" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.601759E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="368.565" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="136.53" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.070597" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.543387" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.897249" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.154989" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5886" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.08" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.897249" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="23070" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.154989" />
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-  <group id="10"  value="2" />
-  <group id="12"  value="1" />
-  <group id="58"  value="3" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="2" />
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-<Umr name="UMR" >
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-  <group id="58"  value="3" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="2" />
-  <group id="11"  value="1" />
-  <group id="57"  value="3" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="118-96-7" />
-<Smiles name="SMILES"  value="c1(N(=O)=O)c(C)c(N(=O)=O)cc(N(=O)=O)c1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1255" />
-<CompoundID name="Name"  value="Oxalic acid" />
-<StructureFormula name="Structure"  value="HOOCCOOH" />
-<Family name="Family"  value="52" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="804" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7020000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.205" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.215" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="569" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="462.65" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="462.65" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2152.34" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.0349" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0614585" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.917597" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.22E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="35980" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.77E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03948" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.12E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.338E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-6.614E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="343300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.01E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="19.12" />
-  <B value="-0.0026428" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="85.15" />
-  <Tmax units="K"  value="462.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.0501" />
-  <B value="0.215" />
-  <C value="804" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="462.65" />
-  <Tmax units="K"  value="804" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="216.92" />
-  <B value="-20979" />
-  <C value="-27.004" />
-  <D value="0.0000086326" />
-  <E value="2" />
-  <Tmin units="K"  value="462.65" />
-  <Tmax units="K"  value="804" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.2079E+08" />
-  <B value="0.30321" />
-  <C value="0.62049" />
-  <D value="-0.9257" />
-  <E value="0.38682" />
-  <Tmin units="K"  value="462.65" />
-  <Tmax units="K"  value="786.03" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-11394" />
-  <B value="847.14" />
-  <C value="-3.3297" />
-  <D value="0.0084208" />
-  <E value="-0.0000077485" />
-  <Tmin units="K"  value="40.35" />
-  <Tmax units="K"  value="323" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="81965" />
-  <B value="-1.9623" />
-  <C value="9.0826" />
-  <D value="0.0038828" />
-  <E value="2.1663E-07" />
-  <Tmin units="K"  value="462.65" />
-  <Tmax units="K"  value="603" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="25231" />
-  <B value="-1473.6" />
-  <C value="15.259" />
-  <D value="-0.0058042" />
-  <E value="0.0000026122" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.1" />
-  </IdealGasHeatCapacityCp>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.3016E-07" />
-  <B value="0.7814" />
-  <C value="154.56" />
-  <D value="-3949.8" />
-  <Tmin units="K"  value="462.65" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.088775" />
-  <B value="-213.56" />
-  <C value="0.1118" />
-  <D value="-0.0022725" />
-  <E value="3.5301E-07" />
-  <Tmin units="K"  value="462.65" />
-  <Tmax units="K"  value="643.2" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.084868" />
-  <B value="0.23486" />
-  <C value="15441" />
-  <D value="507600" />
-  <Tmin units="K"  value="569" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.011612" />
-  <B value="847.01" />
-  <C value="-7.1508" />
-  <D value="0.0093795" />
-  <E value="-0.0000092018" />
-  <Tmin units="K"  value="462.65" />
-  <Tmax units="K"  value="786.03" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-17972" />
-  <B value="229.76" />
-  <C value="-0.24007" />
-  <D value="0.000093102" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.1" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.465" />
-  <B value="5198.7" />
-  <C value="-133.88" />
-  <Tmin units="K"  value="496.79" />
-  <Tmax units="K"  value="718.66" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.209305" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.959373E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="207.4664" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.215" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="60.86" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0276727" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.703223" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.917597" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0614585" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.6026" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.448" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.917597" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="35980" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0614585" />
-<UnifacVLE name="UNIFAC" >
-  <group id="43"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="23"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="24"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="43"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="42"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="144-62-7" />
-<Smiles name="SMILES"  value="C(=O)(O)C(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1277" />
-<CompoundID name="Name"  value="Acrylic acid" />
-<StructureFormula name="Structure"  value="CH2CHCOOH" />
-<Family name="Family"  value="51" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="654.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5664070" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.210712" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.23" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="414.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="286.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="286.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="257.117" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="72.0627" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.068927" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.220736" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.978E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19230" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.87E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04015" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.0E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.371E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.861E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="315000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.117E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.86" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.28022E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="17.984" />
-  <B value="-4.7488E-17" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.11535" />
-  <B value="0.078693" />
-  <C value="654.15" />
-  <D value="0.16945" />
-  <Tmin units="K"  value="285.15" />
-  <Tmax units="K"  value="597.69" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="55.86645" />
-  <B value="-7062.889" />
-  <C value="-4.564151" />
-  <D value="1.238643E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="276.65" />
-  <Tmax units="K"  value="615" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.9258E+07" />
-  <B value="1.9796" />
-  <C value="2.7587" />
-  <D value="-12.283" />
-  <E value="8.2823" />
-  <Tmin units="K"  value="286.15" />
-  <Tmax units="K"  value="615" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="4218.5" />
-  <B value="513.93" />
-  <C value="-0.95712" />
-  <D value="0.0023227" />
-  <E value="-0.0000024814" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="286.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="142250" />
-  <B value="1837.1" />
-  <C value="-38.373" />
-  <D value="0.21763" />
-  <E value="-0.00027035" />
-  <Tmin units="K"  value="252.65" />
-  <Tmax units="K"  value="375" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="49916" />
-  <B value="-589.6" />
-  <C value="12.259" />
-  <D value="-0.00013536" />
-  <E value="3.0855E-08" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-113.67" />
-  <B value="5526.6" />
-  <C value="15.75" />
-  <D value="-0.000015983" />
-  <E value="2" />
-  <Tmin units="K"  value="286.15" />
-  <Tmax units="K"  value="460" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.4666E-07" />
-  <B value="0.69704" />
-  <C value="207.66" />
-  <D value="-6104.4" />
-  <Tmin units="K"  value="286.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.40695" />
-  <B value="33.472" />
-  <C value="-0.79449" />
-  <D value="0.00078306" />
-  <E value="-0.0000013868" />
-  <Tmin units="K"  value="184.5" />
-  <Tmax units="K"  value="484.5" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00092475" />
-  <B value="0.70367" />
-  <C value="626.1" />
-  <D value="112700" />
-  <Tmin units="K"  value="414.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="0.00036116" />
-  <B value="2216" />
-  <C value="-21.799" />
-  <D value="0.051947" />
-  <E value="-0.000052793" />
-  <Tmin units="K"  value="286.15" />
-  <Tmax units="K"  value="615" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="8237.7" />
-  <B value="284.59" />
-  <C value="-0.1807" />
-  <D value="0.00004331" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.386" />
-  <B value="3741" />
-  <C value="-69.977" />
-  <Tmin units="K"  value="393.15" />
-  <Tmax units="K"  value="582.16" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.8047" />
-  <B value="-0.010482" />
-  <Tmin units="K"  value="286.15" />
-  <Tmax units="K"  value="460" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.212878" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.477409E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="215.1844" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.23" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="69.16" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0296714" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.058208" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.220736" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.068927" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.6467" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.4" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.538324" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19230" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.068927" />
-<UnifacVLE name="UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="5"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="5"  value="1" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="5"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="5"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-10-7" />
-<Smiles name="SMILES"  value="C=CC(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1278" />
-<CompoundID name="Name"  value="Methacrylic acid" />
-<StructureFormula name="Structure"  value="CH2C(CH3)COOH" />
-<Family name="Family"  value="51" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="643" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4700000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.27" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.244" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="433.65" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="288.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="288.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="58.5615" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="86.0892" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0852843" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.331817" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.412E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21000" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.5E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05036" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.65E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.68E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.88E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="350000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.75969" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.93E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.003" />
-  <B value="-0.0057166" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="115.26" />
-  <Tmax units="K"  value="288.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="2.1083" />
-  <B value="0.37321" />
-  <C value="643" />
-  <D value="0.47743" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="642.32" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="9.843112" />
-  <B value="-6238.161" />
-  <C value="2.965581" />
-  <D value="-0.0000105952" />
-  <E value="2" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="662" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7009500" />
-  <B value="-12.334" />
-  <C value="36.335" />
-  <D value="-42.263" />
-  <E value="18.248" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="642.32" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6059" />
-  <B value="735.3" />
-  <C value="-1.363" />
-  <D value="0.0032903" />
-  <E value="-0.0000034953" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="288.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="130480" />
-  <B value="265.42" />
-  <C value="3.971" />
-  <D value="0.026507" />
-  <E value="-0.000026858" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="434.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="48894" />
-  <B value="-560.59" />
-  <C value="12.692" />
-  <D value="-0.00031458" />
-  <E value="1.4407E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.1" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="0.054722" />
-  <B value="968.88" />
-  <C value="-1.7788" />
-  <D value="0.0000031087" />
-  <E value="2" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="434.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.4671E-08" />
-  <B value="0.81582" />
-  <C value="92.397" />
-  <D value="383.72" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.067603" />
-  <B value="29.398" />
-  <C value="-1.512" />
-  <D value="0.00016774" />
-  <E value="-0.0000015769" />
-  <Tmin units="K"  value="192.9" />
-  <Tmax units="K"  value="530" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000065218" />
-  <B value="1.0555" />
-  <C value="299.46" />
-  <D value="29315" />
-  <Tmin units="K"  value="434.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0048338" />
-  <B value="515.9" />
-  <C value="-7.199" />
-  <D value="0.011548" />
-  <E value="-0.000015481" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="642.32" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-15268" />
-  <B value="462.54" />
-  <C value="-0.34541" />
-  <D value="0.00010342" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.1" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.957" />
-  <B value="2984.3" />
-  <C value="-118.31" />
-  <Tmin units="K"  value="386.53" />
-  <Tmax units="K"  value="572.03" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4335" />
-  <B value="-0.010614" />
-  <Tmin units="K"  value="280" />
-  <Tmax units="K"  value="434.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.267781" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.553879E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="261.6541" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.244" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="89.68" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="3.6523" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0349816" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.021898" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.331817" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0852843" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.3197" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.06" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="-6.7774" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.331817" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21000" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0852843" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="7"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="8"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="7"  value="1" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="7"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="7"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="79-41-4" />
-<Smiles name="SMILES"  value="C=C(C)C(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1281" />
-<CompoundID name="Name"  value="Benzoic acid" />
-<StructureFormula name="Structure"  value="(C6H5)COOH" />
-<Family name="Family"  value="53" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="751" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4470000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.344" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.246" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="523.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="395.55" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="395.45" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="795.501" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="122.121" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.112442" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.602794" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.059E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24590" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.34E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.06558" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.41E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.902E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.142E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="369000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.807E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.41302" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.0951E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.523" />
-  <B value="-0.0023742" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="78.15" />
-  <Tmax units="K"  value="395.45" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.7147" />
-  <B value="0.24811" />
-  <C value="751" />
-  <D value="0.28445" />
-  <Tmin units="K"  value="394.65" />
-  <Tmax units="K"  value="751" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="444.4847" />
-  <B value="-30166.81" />
-  <C value="-61.25117" />
-  <D value="0.000029739" />
-  <E value="2" />
-  <Tmin units="K"  value="373.15" />
-  <Tmax units="K"  value="751" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.7437E+07" />
-  <B value="0.13946" />
-  <C value="-2.3071" />
-  <D value="5.0416" />
-  <E value="-2.5138" />
-  <Tmin units="K"  value="395.45" />
-  <Tmax units="K"  value="751" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="1801.4" />
-  <B value="920.19" />
-  <C value="-4.2178" />
-  <D value="0.013624" />
-  <E value="-0.000014613" />
-  <Tmin units="K"  value="30" />
-  <Tmax units="K"  value="395.52" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78008" />
-  <B value="1056.8" />
-  <C value="2.5621" />
-  <D value="0.02421" />
-  <E value="-0.000017579" />
-  <Tmin units="K"  value="395.45" />
-  <Tmax units="K"  value="450" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="71253" />
-  <B value="-905.31" />
-  <C value="13.682" />
-  <D value="-0.00087786" />
-  <E value="2.5351E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-204.19" />
-  <B value="11713" />
-  <C value="28.642" />
-  <D value="-0.000020228" />
-  <E value="2" />
-  <Tmin units="K"  value="395.52" />
-  <Tmax units="K"  value="600.8" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.426E-08" />
-  <B value="0.8289" />
-  <C value="91.171" />
-  <D value="5.6616" />
-  <Tmin units="K"  value="395.45" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.26694" />
-  <B value="24.352" />
-  <C value="-0.89204" />
-  <D value="0.00010336" />
-  <E value="-5.9141E-07" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="596" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000021559" />
-  <B value="1.1593" />
-  <C value="126.16" />
-  <D value="64371" />
-  <Tmin units="K"  value="522.4" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018071" />
-  <B value="-333.25" />
-  <C value="-0.48157" />
-  <D value="-0.0043141" />
-  <E value="2.3966E-07" />
-  <Tmin units="K"  value="395.45" />
-  <Tmax units="K"  value="751" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-22579" />
-  <B value="512.65" />
-  <C value="-0.28424" />
-  <D value="0.000055985" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.577" />
-  <B value="4593.4" />
-  <C value="-107.46" />
-  <Tmin units="K"  value="451.59" />
-  <Tmax units="K"  value="657.43" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.0682" />
-  <B value="-0.011311" />
-  <Tmin units="K"  value="395.52" />
-  <Tmax units="K"  value="600.8" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.351828" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.035727E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="314.7165" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.246" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="119.08" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0475472" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.185846" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.602794" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.112442" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.323" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.344" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.602794" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24590" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.112442" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="5" />
-  <group id="10"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="65-85-0" />
-<Smiles name="SMILES"  value="c1ccccc1(C(=O)O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1282" />
-<CompoundID name="Name"  value="O-toluic acid" />
-<StructureFormula name="Structure"  value="CH3(C6H4)COOH" />
-<Family name="Family"  value="53" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="751" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3860000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.397" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.245" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="532" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="376.85" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="376.85" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="237.832" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="136.148" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.126888" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.657237" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.387E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22920" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.67059E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07673" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.78E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.22796E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.13346E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="406141" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.01774E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.69902E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.4748" />
-  <B value="4.5776E-09" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="386.35" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.61816" />
-  <B value="0.24687" />
-  <C value="751" />
-  <D value="0.2856" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="751" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="133.1988" />
-  <B value="-13740.37" />
-  <C value="-15.5105" />
-  <D value="5.245068E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="370" />
-  <Tmax units="K"  value="751" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="9.9956E+07" />
-  <B value="0.80217" />
-  <C value="-0.93427" />
-  <D value="0.8805" />
-  <E value="-0.3406" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="751" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="30.552" />
-  <B value="2311.3" />
-  <C value="-11.456" />
-  <D value="0.025236" />
-  <E value="-0.000020846" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="307.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="129490" />
-  <B value="18.011" />
-  <C value="10.105" />
-  <D value="0.0057419" />
-  <E value="-0.000003975" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="532.35" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85949" />
-  <B value="-929.05" />
-  <C value="14.065" />
-  <D value="-0.0013145" />
-  <E value="5.0858E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.7015" />
-  <B value="1473.1" />
-  <C value="-0.25079" />
-  <D value="0.0000003109" />
-  <E value="2" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="600.8" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.2379E-07" />
-  <B value="0.7551" />
-  <C value="177.89" />
-  <D value="-5611.1" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.13162" />
-  <B value="29.195" />
-  <C value="-1.2663" />
-  <D value="0.000070644" />
-  <E value="-8.4448E-07" />
-  <Tmin units="K"  value="225.3" />
-  <Tmax units="K"  value="595.3" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000027427" />
-  <B value="1.1315" />
-  <C value="204.73" />
-  <D value="55122" />
-  <Tmin units="K"  value="532" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.088963" />
-  <B value="33.057" />
-  <C value="-2.0549" />
-  <D value="-0.00011701" />
-  <E value="-5.6887E-07" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="751" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-36255" />
-  <B value="643.38" />
-  <C value="-0.35936" />
-  <D value="0.000063647" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.059" />
-  <B value="4456.2" />
-  <C value="-109.65" />
-  <Tmin units="K"  value="455.62" />
-  <Tmax units="K"  value="674" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.9168" />
-  <B value="-0.0065457" />
-  <Tmin units="K"  value="376.85" />
-  <Tmax units="K"  value="600.8" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.415667" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.416104E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="310.1352" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.245" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="139.6" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0563975" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.153456" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.657237" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.126888" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.058" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.912" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.657237" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22920" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.126888" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="11"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="11"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="118-90-1" />
-<Smiles name="SMILES"  value="c1(C)ccccc1(C(=O)O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1283" />
-<CompoundID name="Name"  value="P-toluic acid" />
-<StructureFormula name="Structure"  value="CH3(C6H4)COOH" />
-<Family name="Family"  value="53" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="773" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3860000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.397" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.238" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="548.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="452.75" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="452.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="5208.62" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="136.148" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.129817" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.661017" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.35E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22040" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07673" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.78E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.22796E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.13346E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="406141" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.2737E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.69222E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.1884" />
-  <B value="-1.9667E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.60059" />
-  <B value="0.238" />
-  <C value="773" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="452.75" />
-  <Tmax units="K"  value="773" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="180.79" />
-  <B value="-16901" />
-  <C value="-22.327" />
-  <D value="0.0000079041" />
-  <E value="2" />
-  <Tmin units="K"  value="450" />
-  <Tmax units="K"  value="773" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.0299E+08" />
-  <B value="0.94653" />
-  <C value="-1.474" />
-  <D value="1.5504" />
-  <E value="-0.62044" />
-  <Tmin units="K"  value="452.75" />
-  <Tmax units="K"  value="756.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="29.528" />
-  <B value="2233.9" />
-  <C value="-11.072" />
-  <D value="0.024391" />
-  <E value="-0.000020147" />
-  <Tmin units="K"  value="298" />
-  <Tmax units="K"  value="307.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="204240" />
-  <B value="558.58" />
-  <C value="5.081" />
-  <D value="0.015699" />
-  <E value="-0.000010465" />
-  <Tmin units="K"  value="452.75" />
-  <Tmax units="K"  value="548.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85949" />
-  <B value="-929.05" />
-  <C value="14.065" />
-  <D value="-0.0013145" />
-  <E value="5.0858E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-16.393" />
-  <B value="2717.5" />
-  <C value="0.51437" />
-  <D value="-3.3608E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="452.75" />
-  <Tmax units="K"  value="598" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.0828E-08" />
-  <B value="0.81038" />
-  <C value="114.97" />
-  <D value="-489.3" />
-  <Tmin units="K"  value="452.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.14095" />
-  <B value="29.118" />
-  <C value="-1.2124" />
-  <D value="0.000049104" />
-  <E value="-7.6374E-07" />
-  <Tmin units="K"  value="231.9" />
-  <Tmax units="K"  value="611.9" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00002977" />
-  <B value="1.1214" />
-  <C value="206.56" />
-  <D value="62002" />
-  <Tmin units="K"  value="548.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0093429" />
-  <B value="992.57" />
-  <C value="-8.4763" />
-  <D value="0.011892" />
-  <E value="-0.000011231" />
-  <Tmin units="K"  value="452.75" />
-  <Tmax units="K"  value="756.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-36255" />
-  <B value="643.38" />
-  <C value="-0.35936" />
-  <D value="0.000063647" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.085" />
-  <B value="4607.3" />
-  <C value="-112.28" />
-  <Tmin units="K"  value="469.61" />
-  <Tmax units="K"  value="688.72" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0746" />
-  <B value="-0.0094981" />
-  <Tmin units="K"  value="452.75" />
-  <Tmax units="K"  value="598" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.415667" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.678613E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="287.5873" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.238" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="139.6" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0546655" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.207575" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.661017" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.129817" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.058" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.912" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.661017" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22040" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.129817" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="11"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="12"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="11"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="99-94-5" />
-<Smiles name="SMILES"  value="c1cc(C)ccc1(C(=O)O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1284" />
-<CompoundID name="Name"  value="Salicylic acid" />
-<StructureFormula name="Structure"  value="HO(C6H4)COOH" />
-<Family name="Family"  value="43" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="739" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5180000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.364" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.275" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="529" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="431.75" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="431.75" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="2802.65" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="138.121" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.119591" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.851182" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.251E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="24210" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.84E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0711" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="9.12E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.948E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.954E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="399800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.959E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.8901E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="10.991" />
-  <B value="-0.0020281" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="78.15" />
-  <Tmax units="K"  value="431.75" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.8432" />
-  <B value="0.27522" />
-  <C value="739" />
-  <D value="0.28574" />
-  <Tmin units="K"  value="426.15" />
-  <Tmax units="K"  value="722.53" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="252.5417" />
-  <B value="-21148.9" />
-  <C value="-32.63925" />
-  <D value="0.0000130693" />
-  <E value="2" />
-  <Tmin units="K"  value="429.95" />
-  <Tmax units="K"  value="739" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.3325E+08" />
-  <B value="-0.11849" />
-  <C value="3.6062" />
-  <D value="-5.1635" />
-  <E value="2.13" />
-  <Tmin units="K"  value="431.75" />
-  <Tmax units="K"  value="722.83" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="47862" />
-  <B value="1.3021" />
-  <C value="2.8451" />
-  <D value="-0.0074793" />
-  <E value="0.0000077542" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="350" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="129500" />
-  <B value="160.82" />
-  <C value="8.5105" />
-  <D value="0.0092921" />
-  <E value="-0.0000057493" />
-  <Tmin units="K"  value="431.75" />
-  <Tmax units="K"  value="551.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83388" />
-  <B value="-879.57" />
-  <C value="13.917" />
-  <D value="-0.0013499" />
-  <E value="0.0000005122" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-50.743" />
-  <B value="5203.6" />
-  <C value="5.2837" />
-  <D value="2.047E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="426.15" />
-  <Tmax units="K"  value="591.2" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.0029E-07" />
-  <B value="0.78423" />
-  <C value="131.87" />
-  <D value="-154.53" />
-  <Tmin units="K"  value="431.75" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0043799" />
-  <B value="-391.31" />
-  <C value="0.63544" />
-  <D value="-0.0048323" />
-  <E value="0.0000010995" />
-  <Tmin units="K"  value="431.75" />
-  <Tmax units="K"  value="529" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000028337" />
-  <B value="1.1043" />
-  <C value="106.43" />
-  <D value="67783" />
-  <Tmin units="K"  value="529" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.025399" />
-  <B value="35.561" />
-  <C value="-2.635" />
-  <D value="0.00026914" />
-  <E value="-0.0000023783" />
-  <Tmin units="K"  value="431.75" />
-  <Tmax units="K"  value="722.83" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-33229" />
-  <B value="646.66" />
-  <C value="-0.44103" />
-  <D value="0.00010904" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.591" />
-  <B value="4389.8" />
-  <C value="-131.93" />
-  <Tmin units="K"  value="445.35" />
-  <Tmax units="K"  value="662.19" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.3875" />
-  <B value="-0.010056" />
-  <Tmin units="K"  value="426.15" />
-  <Tmax units="K"  value="591.2" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.38316" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.272098E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="462.5464" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.275" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="125.19" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0500667" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.298112" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.851182" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.119591" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.6869" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.624" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.851182" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="24210" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.119591" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="18"  value="1" />
-  <group id="43"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="18"  value="1" />
-  <group id="23"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="16"  value="1" />
-  <group id="24"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="11"  value="1" />
-  <group id="18"  value="1" />
-  <group id="43"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="10"  value="1" />
-  <group id="17"  value="1" />
-  <group id="42"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="69-72-7" />
-<Smiles name="SMILES"  value="c1(O)ccccc1(C(=O)O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1285" />
-<CompoundID name="Name"  value="Adipic acid" />
-<StructureFormula name="Structure"  value="HOOC(CH2)4COOH" />
-<Family name="Family"  value="52" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="809" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3530000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.21" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="611" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="426.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="425.5" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="78.0827" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="146.141" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.133942" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.05065" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.976E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="25370" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.74E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.07996" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.15E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-8.65E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-6.82E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="482000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.67E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.58E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.2095" />
-  <B value="0.000041964" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="285.65" />
-  <Tmax units="K"  value="425.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.64797" />
-  <B value="0.25918" />
-  <C value="809" />
-  <D value="0.28198" />
-  <Tmin units="K"  value="425.5" />
-  <Tmax units="K"  value="809" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="255.2237" />
-  <B value="-23233.92" />
-  <C value="-32.83085" />
-  <D value="0.000013435" />
-  <E value="2" />
-  <Tmin units="K"  value="425.5" />
-  <Tmax units="K"  value="809" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.949255E+08" />
-  <B value="0.823008" />
-  <C value="2.518159" />
-  <D value="-5.646327" />
-  <E value="2.784565" />
-  <Tmin units="K"  value="425.5" />
-  <Tmax units="K"  value="809" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="40.553" />
-  <B value="3069.4" />
-  <C value="-15.206" />
-  <D value="0.033481" />
-  <E value="-0.000027642" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="307.65" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="235940" />
-  <B value="-32.997" />
-  <C value="10.809" />
-  <D value="0.0032672" />
-  <E value="-0.0000019456" />
-  <Tmin units="K"  value="425.5" />
-  <Tmax units="K"  value="611" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="85474" />
-  <B value="-423.41" />
-  <C value="12.745" />
-  <D value="0.00026178" />
-  <E value="-1.1462E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.4738" />
-  <B value="3093.2" />
-  <C value="-0.68319" />
-  <D value="4.5668E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="433.15" />
-  <Tmax units="K"  value="466.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.6397E-08" />
-  <B value="0.79699" />
-  <C value="129.04" />
-  <D value="-83.45" />
-  <Tmin units="K"  value="425.5" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.15138" />
-  <B value="31.723" />
-  <C value="-1.1417" />
-  <D value="0.000072402" />
-  <E value="-7.2467E-07" />
-  <Tmin units="K"  value="242.7" />
-  <Tmax units="K"  value="642.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00019846" />
-  <B value="0.87712" />
-  <C value="520.45" />
-  <D value="62013" />
-  <Tmin units="K"  value="611" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018266" />
-  <B value="123.31" />
-  <C value="-3.4148" />
-  <D value="0.00050163" />
-  <E value="-0.0000017596" />
-  <Tmin units="K"  value="425.5" />
-  <Tmax units="K"  value="809" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="18304" />
-  <B value="636.31" />
-  <C value="-0.40132" />
-  <D value="0.0000928" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.687" />
-  <B value="5175.2" />
-  <C value="-145.76" />
-  <Tmin units="K"  value="486.05" />
-  <Tmax units="K"  value="708.08" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="1.714" />
-  <B value="-0.016424" />
-  <Tmin units="K"  value="433.15" />
-  <Tmax units="K"  value="466.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.434587" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.945443E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="191.8011" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.21" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="142.94" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0512838" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.204857" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.05065" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.133942" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.3002" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.608" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.05065" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="25370" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.133942" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="43"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="4" />
-  <group id="23"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="4" />
-  <group id="24"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="4" />
-  <group id="43"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="42"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="124-04-9" />
-<Smiles name="SMILES"  value="OC(=O)CCCCC(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1287" />
-<CompoundID name="Name"  value="Phthalic acid" />
-<StructureFormula name="Structure"  value="COOH(C6H4)COOH" />
-<Family name="Family"  value="53" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="943.0648" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4492234" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4235" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.242627" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="651.424" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="483.15" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="166.131" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.115821" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.16031" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.162787E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="29038.44" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.67E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0828" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.072E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.63E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5.42E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="442000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.0915E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.5506" />
-  <B value="0.0031229" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="302.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.59385" />
-  <B value="0.252" />
-  <C value="800" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="800" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="214.6186" />
-  <B value="-21678.73" />
-  <C value="-26.54136" />
-  <D value="7.94063E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="800" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.16446E+08" />
-  <B value="0.325842" />
-  <C value="-0.000233021" />
-  <D value="0.00216992" />
-  <E value="0.484323" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="800" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="22693" />
-  <B value="550.36" />
-  <C value="-0.074278" />
-  <D value="0.00058694" />
-  <E value="-9.7751E-07" />
-  <Tmin units="K"  value="90" />
-  <Tmax units="K"  value="350" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="126080" />
-  <B value="73.955" />
-  <C value="9.4222" />
-  <D value="0.0070682" />
-  <E value="-0.0000039598" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="600" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78972" />
-  <B value="-814.12" />
-  <C value="13.621" />
-  <D value="-0.00057909" />
-  <E value="1.2469E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-20.315" />
-  <B value="4089.4" />
-  <C value="0.87699" />
-  <D value="-5.3713E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="598" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.1978E-08" />
-  <B value="0.86126" />
-  <C value="68.544" />
-  <D value="-136.86" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.13007" />
-  <B value="40.261" />
-  <C value="-1.3314" />
-  <D value="0.00027982" />
-  <E value="-9.4309E-07" />
-  <Tmin units="K"  value="240" />
-  <Tmax units="K"  value="640" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00011576" />
-  <B value="0.91053" />
-  <C value="351.24" />
-  <D value="130660" />
-  <Tmin units="K"  value="598" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035541" />
-  <B value="-4.5485" />
-  <C value="-2.2151" />
-  <D value="-0.00053178" />
-  <E value="-1.9436E-07" />
-  <Tmin units="K"  value="464.15" />
-  <Tmax units="K"  value="800" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-52622.52" />
-  <B value="719.7759" />
-  <C value="-0.465185" />
-  <D value="0.000108418" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.903144" />
-  <B value="-3000" />
-  <C value="-18" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<RacketParameter name="Rackett parameter"  units="_"  value="0.242627" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="147.2" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0493" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.451" />
-<Charge name="Charge"  units="_"  value="0" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.456" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.288" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="43"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="23"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="24"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="43"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="42"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="88-99-3" />
-<Smiles name="SMILES"  value="c1(C(=O)O)c(C(=O)O)cccc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1286" />
-<CompoundID name="Name"  value="Maleic acid" />
-<StructureFormula name="Structure"  value="HOOCCHCHCOOH" />
-<Family name="Family"  value="52" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="773" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4990000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.297" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.231" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="411" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="403.45" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="403.8" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="98.6734" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="116.072" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.090835" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.997587" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.221E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="30550" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.06E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05642" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.28E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.794E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5.96E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="416000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3.47E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.2684E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="13.698" />
-  <B value="-1.103E-09" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="302.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.77641" />
-  <B value="0.231" />
-  <C value="773" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="403.8" />
-  <Tmax units="K"  value="773" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="187.4602" />
-  <B value="-19104.39" />
-  <C value="-22.78106" />
-  <D value="6.967225E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="403.8" />
-  <Tmax units="K"  value="773" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.16446E+08" />
-  <B value="0.325842" />
-  <C value="-0.000233021" />
-  <D value="0.00216992" />
-  <E value="0.484323" />
-  <Tmin units="K"  value="403.8" />
-  <Tmax units="K"  value="773" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="21794" />
-  <B value="494.53" />
-  <C value="-0.98012" />
-  <D value="0.002955" />
-  <E value="-0.00000306" />
-  <Tmin units="K"  value="60" />
-  <Tmax units="K"  value="350" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="148240" />
-  <B value="706.52" />
-  <C value="4.046" />
-  <D value="0.018422" />
-  <E value="-0.000011933" />
-  <Tmin units="K"  value="403.8" />
-  <Tmax units="K"  value="579.75" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="60872" />
-  <B value="-493.34" />
-  <C value="12.58" />
-  <D value="-0.00028606" />
-  <E value="0.0000001493" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-11.993" />
-  <B value="2508.3" />
-  <C value="0.079857" />
-  <D value="-1.8766E-08" />
-  <E value="2" />
-  <Tmin units="K"  value="403.45" />
-  <Tmax units="K"  value="565" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.0189E-08" />
-  <B value="0.80995" />
-  <C value="111.91" />
-  <D value="-70.22" />
-  <Tmin units="K"  value="403" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.061944" />
-  <B value="-160.86" />
-  <C value="-0.25643" />
-  <D value="-0.0021458" />
-  <E value="2.3954E-07" />
-  <Tmin units="K"  value="403.8" />
-  <Tmax units="K"  value="612" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0000021963" />
-  <B value="1.4191" />
-  <C value="-285.03" />
-  <D value="84199" />
-  <Tmin units="K"  value="469" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010076" />
-  <B value="568.91" />
-  <C value="-6.0243" />
-  <D value="0.0070715" />
-  <E value="-0.0000080291" />
-  <Tmin units="K"  value="403.45" />
-  <Tmax units="K"  value="773" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="13513" />
-  <B value="415.8" />
-  <C value="-0.29766" />
-  <D value="0.000084426" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.374" />
-  <B value="5133" />
-  <C value="-132.2" />
-  <Tmin units="K"  value="477.36" />
-  <Tmax units="K"  value="695.27" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.0564" />
-  <B value="-0.010763" />
-  <Tmin units="K"  value="403.45" />
-  <Tmax units="K"  value="565" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.300877" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.224859E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="258.283" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.231" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="97.28" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0397792" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.407506" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.997587" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.090835" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.7193" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.315" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.997587" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="30550" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.090835" />
-<UnifacVLE name="UNIFAC" >
-  <group id="43"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="23"  value="2" />
-  <group id="6"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="6"  value="1" />
-  <group id="24"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="43"  value="2" />
-  <group id="6"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="42"  value="2" />
-  <group id="6"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-16-7" />
-<Smiles name="SMILES"  value="C(=O)(O)/C=C\C(=O)O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1289" />
-<CompoundID name="Name"  value="Terephthalic acid" />
-<StructureFormula name="Structure"  value="1,4-COOH(C6H4)COOH" />
-<Family name="Family"  value="53" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="943.0648" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4492234" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4235" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.242627" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="665.55" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="573.15" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="166.131" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.115821" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.16031" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.162787E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="29038.44" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0828" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.062E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.179E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-5.99E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="448000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.0576E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="9.0891" />
-  <B value="-4.8319E-09" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="307.65" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.42685" />
-  <B value="0.181" />
-  <C value="1113" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="700.15" />
-  <Tmax units="K"  value="1113" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="215.8574" />
-  <B value="-29586.64" />
-  <C value="-25.50026" />
-  <D value="3.863371E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="700.15" />
-  <Tmax units="K"  value="1113" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="8.9802E+07" />
-  <B value="0.189" />
-  <C value="-0.50305" />
-  <D value="-1.1074" />
-  <E value="4.311" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="307.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-6542500" />
-  <B value="74970" />
-  <C value="-317.47" />
-  <D value="0.6016" />
-  <E value="-0.0004268" />
-  <Tmin units="K"  value="318" />
-  <Tmax units="K"  value="398" />
-  </SolidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83070" />
-  <B value="-852.74" />
-  <C value="13.689" />
-  <D value="-0.000643" />
-  <E value="1.4167E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="2.4248E-08" />
-  <B value="0.96894" />
-  <C value="40.456" />
-  <D value="-14256" />
-  <Tmin units="K"  value="700.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016184" />
-  <B value="0.88608" />
-  <C value="624.29" />
-  <D value="90960" />
-  <Tmin units="K"  value="832" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-47902" />
-  <B value="696.58" />
-  <C value="-0.43325" />
-  <D value="0.000095385" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="24.733" />
-  <B value="9708.2" />
-  <C value="-96.745" />
-  <Tmin units="K"  value="844.65" />
-  <Tmax units="K"  value="1113" />
-  </AntoineVaporPressure>
-<RacketParameter name="Rackett parameter"  units="_"  value="0.242627" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="147.2" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.049" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.51" />
-<Charge name="Charge"  units="_"  value="0" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.456" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.288" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="43"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="23"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="24"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="43"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="42"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="100-21-0" />
-<Smiles name="SMILES"  value="c1(C(=O)O)ccc(C(=O)O)cc1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1291" />
-<CompoundID name="Name"  value="Acetic anhydride" />
-<StructureFormula name="Structure"  value="CH3COOOCCH3" />
-<Family name="Family"  value="54" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="569.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4280000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.29" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.23" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="413.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="200.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="200.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.0219995" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.089" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0949602" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.809524" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.579E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="22010" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0544" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.06E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.735E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4.767E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="389900" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.05E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.65" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.675E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.778" />
-  <B value="-0.0082423" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="80.06" />
-  <Tmax units="K"  value="200.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.3543" />
-  <B value="0.3062" />
-  <C value="584.65" />
-  <D value="0.43334" />
-  <Tmin units="K"  value="200.15" />
-  <Tmax units="K"  value="584.64" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="94.79499" />
-  <B value="-8627.117" />
-  <C value="-10.49847" />
-  <D value="0.0000051448" />
-  <E value="2" />
-  <Tmin units="K"  value="200.15" />
-  <Tmax units="K"  value="606" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.787557E+07" />
-  <B value="-0.639261" />
-  <C value="1.651354" />
-  <D value="-0.778133" />
-  <E value="-0.0411955" />
-  <Tmin units="K"  value="200.15" />
-  <Tmax units="K"  value="563.28" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-76055" />
-  <B value="674.26" />
-  <C value="4.7415" />
-  <D value="0.026829" />
-  <E value="-0.000028167" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="413.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="63862" />
-  <B value="-716.36" />
-  <C value="13.016" />
-  <D value="-0.00041944" />
-  <E value="1.1702E-07" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.21833" />
-  <B value="-249.69" />
-  <C value="-53.999" />
-  <D value="-19108" />
-  <E value="27047" />
-  <Tmin units="K"  value="303" />
-  <Tmax units="K"  value="2000" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-13.196" />
-  <B value="1321.3" />
-  <C value="0.29135" />
-  <D value="3.1938E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="210" />
-  <Tmax units="K"  value="412.7" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.3132E-07" />
-  <B value="0.7781" />
-  <C value="96.036" />
-  <D value="3593.8" />
-  <Tmin units="K"  value="200.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0017236" />
-  <B value="-11.978" />
-  <C value="-1.3413" />
-  <D value="-0.0012823" />
-  <E value="-6.1388E-07" />
-  <Tmin units="K"  value="200.15" />
-  <Tmax units="K"  value="412.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0003967" />
-  <B value="0.81349" />
-  <C value="426.6" />
-  <D value="140300" />
-  <Tmin units="K"  value="412.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0012765" />
-  <B value="252.13" />
-  <C value="-6.1499" />
-  <D value="0.014601" />
-  <E value="-0.000027747" />
-  <Tmin units="K"  value="200.15" />
-  <Tmax units="K"  value="563.28" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-5437.1" />
-  <B value="428.12" />
-  <C value="-0.25005" />
-  <D value="0.000054067" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.597" />
-  <B value="3463.7" />
-  <C value="-68.344" />
-  <Tmin units="K"  value="342.2" />
-  <Tmax units="K"  value="510" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.3258" />
-  <B value="-0.012352" />
-  <Tmin units="K"  value="210" />
-  <Tmax units="K"  value="412.7" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.289796" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.205059E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="187.2234" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.23" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0382651" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.08656" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.453" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0949602" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.586025" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.224" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.453" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="22010" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0949602" />
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="18"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<CAS name="CAS number"  value="108-24-7" />
-<Smiles name="SMILES"  value="CC(=O)OC(=O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1298" />
-<CompoundID name="Name"  value="Maleic anhydride" />
-<StructureFormula name="Structure"  value="-CHCOOCOCH-" />
-<Family name="Family"  value="54" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="721" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="7280000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.219" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.266" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="473.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="325.927" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="325.72" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="289.837" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="98.0569" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0741215" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.54629" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.312E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="25870" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.31E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04404" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.96E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.167E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.55E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="317000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.15E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.06669" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.38E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.277" />
-  <B value="-6.3556E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.1934" />
-  <B value="0.26153" />
-  <C value="721" />
-  <D value="0.35499" />
-  <Tmin units="K"  value="325.65" />
-  <Tmax units="K"  value="721" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="181.7423" />
-  <B value="-13070.32" />
-  <C value="-23.83155" />
-  <D value="0.0000182982" />
-  <E value="2" />
-  <Tmin units="K"  value="323.15" />
-  <Tmax units="K"  value="721" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.7421E+07" />
-  <B value="0.064434" />
-  <C value="0.35394" />
-  <D value="-0.39596" />
-  <E value="0.19018" />
-  <Tmin units="K"  value="325.72" />
-  <Tmax units="K"  value="721" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="29806" />
-  <B value="250.42" />
-  <C value="0.11616" />
-  <D value="-0.000014644" />
-  <E value="6.1402E-07" />
-  <Tmin units="K"  value="88.51" />
-  <Tmax units="K"  value="320.3" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="7374.3" />
-  <B value="412.68" />
-  <C value="8.4647" />
-  <D value="0.0086559" />
-  <E value="-0.0000060424" />
-  <Tmin units="K"  value="325.72" />
-  <Tmax units="K"  value="540.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-39596" />
-  <B value="-169.57" />
-  <C value="12.496" />
-  <D value="6.0181E-08" />
-  <E value="4.1214E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.1" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.1425" />
-  <B value="-178.8" />
-  <C value="-68.898" />
-  <D value="-34417" />
-  <E value="12399" />
-  <Tmin units="K"  value="360.5" />
-  <Tmax units="K"  value="1980.5" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="93.459" />
-  <B value="-2744.1" />
-  <C value="-16.078" />
-  <D value="0.000015825" />
-  <E value="2" />
-  <Tmin units="K"  value="325.72" />
-  <Tmax units="K"  value="475.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.5282E-08" />
-  <B value="0.87275" />
-  <C value="168.46" />
-  <D value="-10784" />
-  <Tmin units="K"  value="325.72" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0050361" />
-  <B value="-137.05" />
-  <C value="-0.46443" />
-  <D value="-0.0029116" />
-  <E value="3.9472E-07" />
-  <Tmin units="K"  value="325.72" />
-  <Tmax units="K"  value="475.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00030053" />
-  <B value="0.85542" />
-  <C value="634.55" />
-  <D value="21624" />
-  <Tmin units="K"  value="473.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.010279" />
-  <B value="305" />
-  <C value="-4.7222" />
-  <D value="0.0047657" />
-  <E value="-0.0000071881" />
-  <Tmin units="K"  value="325.72" />
-  <Tmax units="K"  value="721" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-7976.2" />
-  <B value="560.7" />
-  <C value="-0.59917" />
-  <D value="0.00024312" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.1" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-4.509298" />
-  <B value="-10000" />
-  <C value="-153" />
-  <Tmin units="K"  value="314.15" />
-  <Tmax units="K"  value="484.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="25.037" />
-  <B value="7200.5" />
-  <C value="56.284" />
-  <Tmin units="K"  value="434" />
-  <Tmax units="K"  value="637.78" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.9417" />
-  <B value="-0.010534" />
-  <Tmin units="K"  value="325.72" />
-  <Tmax units="K"  value="475.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.233687" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.510636E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="400.3339" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.266" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0337942" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.32293" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.54629" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0741215" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.903098" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.384" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.54629" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="25870" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0741215" />
-<Asog name="ASOG" >
-  <group id="6"  value="1" />
-  <group id="18"  value="2" />
-  <group id="19"  value="1" />
-  </Asog>
-<CAS name="CAS number"  value="108-31-6" />
-<Smiles name="SMILES"  value="O1C(=O)C=CC1(=O)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1100" />
-<CompoundID name="Name"  value="Ketene" />
-<StructureFormula name="Structure"  value="CH2CO" />
-<Family name="Family"  value="26" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="370" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5810000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.144" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.272" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="217.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="122.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="122" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="7.19493" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="42.0367" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.06374" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.125656" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="1.605E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="13820" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="4.74E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.02571" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.02733E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.11E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-6.02914E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="241800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-9.67759E+08" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="28.127" />
-  <B value="-0.025457" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="48.8" />
-  <Tmax units="K"  value="122" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.8886" />
-  <B value="0.272" />
-  <C value="370" />
-  <D value="0.28571" />
-  <Tmin units="K"  value="122" />
-  <Tmax units="K"  value="370" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="58.628" />
-  <B value="-3467" />
-  <C value="-5.9337" />
-  <D value="0.000010248" />
-  <E value="2" />
-  <Tmin units="K"  value="122" />
-  <Tmax units="K"  value="370" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.6158E+07" />
-  <B value="4.5264" />
-  <C value="-12.408" />
-  <D value="14.257" />
-  <E value="-5.881" />
-  <Tmin units="K"  value="122" />
-  <Tmax units="K"  value="356.95" />
-  </HeatOfVaporization>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="41971" />
-  <B value="267.01" />
-  <C value="4.7755" />
-  <D value="0.029953" />
-  <E value="-0.000037749" />
-  <Tmin units="K"  value="162.53" />
-  <Tmax units="K"  value="277.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="33110" />
-  <B value="-414.32" />
-  <C value="10.968" />
-  <D value="0.00041237" />
-  <E value="-1.3222E-07" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.084441" />
-  <B value="-73.911" />
-  <C value="-3.4543" />
-  <D value="-184.05" />
-  <E value="165.87" />
-  <Tmin units="K"  value="185" />
-  <Tmax units="K"  value="1845" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-18.659" />
-  <B value="731.69" />
-  <C value="1.5497" />
-  <D value="-0.000011288" />
-  <E value="2" />
-  <Tmin units="K"  value="120" />
-  <Tmax units="K"  value="223.33" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="0.000001285" />
-  <B value="0.50552" />
-  <C value="367.45" />
-  <D value="-2188.3" />
-  <Tmin units="K"  value="122" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.007072" />
-  <B value="-11.763" />
-  <C value="-0.74777" />
-  <D value="-0.0024777" />
-  <E value="-0.0000018714" />
-  <Tmin units="K"  value="122" />
-  <Tmax units="K"  value="223.33" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.000028519" />
-  <B value="1.1477" />
-  <C value="-97.436" />
-  <D value="37387" />
-  <Tmin units="K"  value="223.34" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0092911" />
-  <B value="36.086" />
-  <C value="-3.4694" />
-  <D value="0.0016382" />
-  <E value="-0.000014409" />
-  <Tmin units="K"  value="122" />
-  <Tmax units="K"  value="356.95" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="21695" />
-  <B value="109.1" />
-  <C value="-0.059305" />
-  <D value="0.000012442" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.165" />
-  <B value="1969.1" />
-  <C value="-19.227" />
-  <Tmin units="K"  value="223" />
-  <Tmax units="K"  value="330.84" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.0718" />
-  <B value="-0.020835" />
-  <Tmin units="K"  value="120" />
-  <Tmax units="K"  value="223.33" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.136385" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="4.665338E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="222.6194" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.272" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0190563" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.678908" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.125656" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.06374" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="1.694792" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.610932" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.125656" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="13820" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.06374" />
-<CAS name="CAS number"  value="463-51-4" />
-<Smiles name="SMILES"  value="C=C=O" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1351" />
-<CompoundID name="Name"  value="Methyl methacrylate" />
-<StructureFormula name="Structure"  value="CH2C(CH3)COOCH3" />
-<Family name="Family"  value="59" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="563.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3670000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.324" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.253" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="374.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="225.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="225.6" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="19.0855" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="100.116" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.106736" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.280233" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.62E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18530" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.57E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05949" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="8.91E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.6E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.54E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="401000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.44348E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.27622" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.54E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="12.912" />
-  <B value="-0.0063843" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="89.98" />
-  <Tmax units="K"  value="224.95" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.91648" />
-  <B value="0.27205" />
-  <C value="563.15" />
-  <D value="0.3201" />
-  <Tmin units="K"  value="224.95" />
-  <Tmax units="K"  value="548.05" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="129.5007" />
-  <B value="-8907.818" />
-  <C value="-16.17497" />
-  <D value="0.000012098" />
-  <E value="2" />
-  <Tmin units="K"  value="224.95" />
-  <Tmax units="K"  value="566" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.397285E+07" />
-  <B value="-0.0862845" />
-  <C value="1.857786" />
-  <D value="-2.127696" />
-  <E value="0.775243" />
-  <Tmin units="K"  value="224.95" />
-  <Tmax units="K"  value="548.05" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-22371" />
-  <B value="1615.2" />
-  <C value="-7.3896" />
-  <D value="0.0056281" />
-  <E value="0.000054354" />
-  <Tmin units="K"  value="20" />
-  <Tmax units="K"  value="210" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="45251" />
-  <B value="733.56" />
-  <C value="4.0201" />
-  <D value="0.024183" />
-  <E value="-0.000020347" />
-  <Tmin units="K"  value="224.95" />
-  <Tmax units="K"  value="373.45" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="40862.92" />
-  <B value="-408.0793" />
-  <C value="12.53452" />
-  <D value="0.000265188" />
-  <E value="-1.105927E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.20274" />
-  <B value="-240.84" />
-  <C value="-40.536" />
-  <D value="6484.6" />
-  <E value="-27053" />
-  <Tmin units="K"  value="282" />
-  <Tmax units="K"  value="1800" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.2342" />
-  <B value="780.75" />
-  <C value="-0.30393" />
-  <D value="-0.0000019127" />
-  <E value="2" />
-  <Tmin units="K"  value="260" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.0508E-07" />
-  <B value="0.64362" />
-  <C value="435.99" />
-  <D value="-25064" />
-  <Tmin units="K"  value="224.95" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.093744" />
-  <B value="-51.297" />
-  <C value="-0.18289" />
-  <D value="-0.0078351" />
-  <E value="-0.0000030405" />
-  <Tmin units="K"  value="290.15" />
-  <Tmax units="K"  value="363.45" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0023506" />
-  <B value="0.61168" />
-  <C value="848.43" />
-  <D value="252520" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.035425" />
-  <B value="-58.877" />
-  <C value="-1.5763" />
-  <D value="-0.0037063" />
-  <E value="0.0000012939" />
-  <Tmin units="K"  value="224.95" />
-  <Tmax units="K"  value="548.05" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-10357" />
-  <B value="514.6" />
-  <C value="-0.32166" />
-  <D value="0.000073928" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.565" />
-  <B value="2703.4" />
-  <C value="-74.211" />
-  <Tmin units="K"  value="340" />
-  <Tmax units="K"  value="494.2" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.6879" />
-  <B value="-0.0094364" />
-  <Tmin units="K"  value="260" />
-  <Tmax units="K"  value="400" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.31782" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.668304E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="261.0785" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.253" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="110.2" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0432757" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.94966" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.280233" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.106736" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.9215" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.564" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.280233" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="18530" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.106736" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="7"  value="1" />
-  <group id="22"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="8"  value="1" />
-  <group id="25"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="7"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="7"  value="1" />
-  <group id="22"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="7"  value="1" />
-  <group id="21"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="80-62-6" />
-<Smiles name="SMILES"  value="C=C(C)C(=O)OC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1381" />
-<CompoundID name="Name"  value="Dimethyl terephthalate" />
-<StructureFormula name="Structure"  value="C6H4(COOCH3)2" />
-<Family name="Family"  value="60" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="772" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2780000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.529" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.229" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="555.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="413.8" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="413.8" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1257.73" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="194.184" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.180564" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.637086" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="5.394E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17710" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="7.3E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.10106" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.324E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.37E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4.74E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="550000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="3.09E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.43085" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.4115E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="7.4567" />
-  <B value="-1.8182E-16" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="9.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.50864" />
-  <B value="0.26895" />
-  <C value="772" />
-  <D value="0.26133" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="753.15" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="87.35202" />
-  <B value="-11061.82" />
-  <C value="-8.88269" />
-  <D value="1.566691E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="772" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.927268E+07" />
-  <B value="-0.826644" />
-  <C value="0.840569" />
-  <D value="0.547723" />
-  <E value="-0.373819" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="753.15" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-784670" />
-  <B value="8890.9" />
-  <C value="-28.57" />
-  <D value="0.040933" />
-  <E value="-0.000019452" />
-  <Tmin units="K"  value="317.35" />
-  <Tmax units="K"  value="403.68" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="306140" />
-  <B value="1151.8" />
-  <C value="1.8179" />
-  <D value="0.019226" />
-  <E value="-0.0000087371" />
-  <Tmin units="K"  value="423.15" />
-  <Tmax units="K"  value="466.35" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="95546" />
-  <B value="-944.26" />
-  <C value="15.059" />
-  <D value="-0.0027373" />
-  <E value="0.0000012901" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.40094" />
-  <B value="-498.08" />
-  <C value="-263.19" />
-  <D value="-218660" />
-  <E value="171700" />
-  <Tmin units="K"  value="386" />
-  <Tmax units="K"  value="1774" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-9.6027" />
-  <B value="1845.8" />
-  <C value="-0.28991" />
-  <D value="2.7867E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="561.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.5497E-10" />
-  <B value="1.62" />
-  <C value="-527.6" />
-  <D value="101960" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="1550" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.015206" />
-  <B value="-275.63" />
-  <C value="0.058569" />
-  <D value="-0.0035078" />
-  <E value="7.3745E-07" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="561.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="-21938" />
-  <B value="0.32202" />
-  <C value="-4.3275E+09" />
-  <D value="-1.5265E+11" />
-  <Tmin units="K"  value="561.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.058913" />
-  <B value="-26.714" />
-  <C value="-1.9282" />
-  <D value="-0.0011887" />
-  <E value="8.1672E-08" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="753.15" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-135990" />
-  <B value="1367.3" />
-  <C value="-1.3275" />
-  <D value="0.00050832" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1000.15" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.619" />
-  <B value="6772" />
-  <C value="-1.4218" />
-  <Tmin units="K"  value="470.36" />
-  <Tmax units="K"  value="677.74" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-3.4624" />
-  <B value="-0.008305" />
-  <Tmin units="K"  value="413.8" />
-  <Tmax units="K"  value="561.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.563654" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.849681E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="249.999" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.229" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="169.94" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0718832" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.174947" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.637086" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.180564" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.6618" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.296" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.637086" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17710" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.180564" />
-<UnifacVLE name="UNIFAC" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="22"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="25"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="22"  value="2" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="10"  value="4" />
-  <group id="11"  value="2" />
-  <group id="22"  value="2" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="9"  value="4" />
-  <group id="10"  value="2" />
-  <group id="21"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="120-61-6" />
-<Smiles name="SMILES"  value="c1c(C(=O)OC)ccc(C(=O)OC)c1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1442" />
-<CompoundID name="Name"  value="1,2-propylene oxide" />
-<StructureFormula name="Structure"  value="CH3-CHCH2O-" />
-<Family name="Family"  value="63" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="482.25" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4920000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.186" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.228" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="307.05" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="161.22" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="161.22" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.965624" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="58.0791" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0705481" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.268304" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.66E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19050" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="6.7E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0344" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.64E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.372E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.58E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="286700" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="6531000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.95094" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.79E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="21.358" />
-  <B value="-0.014706" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="64.49" />
-  <Tmax units="K"  value="161.22" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.5769" />
-  <B value="0.28598" />
-  <C value="482.25" />
-  <D value="0.29139" />
-  <Tmin units="K"  value="161.22" />
-  <Tmax units="K"  value="482.25" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="83.693" />
-  <B value="-5715.8" />
-  <C value="-9.522" />
-  <D value="0.00001033" />
-  <E value="2" />
-  <Tmin units="K"  value="161.22" />
-  <Tmax units="K"  value="482.25" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.241305E+07" />
-  <B value="1.339985" />
-  <C value="-1.496096" />
-  <D value="0.72766" />
-  <E value="-0.151947" />
-  <Tmin units="K"  value="161.22" />
-  <Tmax units="K"  value="482.25" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-22780" />
-  <B value="1901.9" />
-  <C value="-20.601" />
-  <D value="0.11819" />
-  <E value="-0.00025907" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="161.25" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="78704" />
-  <B value="274.26" />
-  <C value="7.2963" />
-  <D value="0.0088641" />
-  <E value="-0.0000023407" />
-  <Tmin units="K"  value="161.22" />
-  <Tmax units="K"  value="433.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="42195" />
-  <B value="-578.73" />
-  <C value="12.252" />
-  <D value="0.00010777" />
-  <E value="-4.7082E-08" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.068785" />
-  <B value="-9.8409" />
-  <C value="-37.616" />
-  <D value="14983" />
-  <E value="-36794" />
-  <Tmin units="K"  value="241.12" />
-  <Tmax units="K"  value="1543.13" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="20.905" />
-  <B value="283.5" />
-  <C value="-5.5156" />
-  <D value="0.000016261" />
-  <E value="2" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="313.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.1059E-07" />
-  <B value="0.81831" />
-  <C value="109.91" />
-  <D value="-5863.4" />
-  <Tmin units="K"  value="161.22" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.10066" />
-  <B value="294.75" />
-  <C value="-5.9561" />
-  <D value="0.019433" />
-  <E value="-0.000039547" />
-  <Tmin units="K"  value="161.22" />
-  <Tmax units="K"  value="385.8" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00022671" />
-  <B value="0.95467" />
-  <C value="579.31" />
-  <D value="32798" />
-  <Tmin units="K"  value="307.05" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.015763" />
-  <B value="49.046" />
-  <C value="-3.1007" />
-  <D value="0.001104" />
-  <E value="-0.0000073634" />
-  <Tmin units="K"  value="161.22" />
-  <Tmax units="K"  value="482.25" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="8474.7" />
-  <B value="248.13" />
-  <C value="-0.09863" />
-  <D value="0.0000096523" />
-  <Tmin units="K"  value="150" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.382" />
-  <B value="2709.9" />
-  <C value="-32.425" />
-  <Tmin units="K"  value="290.2" />
-  <Tmax units="K"  value="433.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.8854" />
-  <B value="-0.017723" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="313.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.182307" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.279053E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="153.7272" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.228" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="67.67" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-1.02" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0273464" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.836764" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.268304" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0705481" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.2663" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="1.856" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.24763" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.268304" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19050" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0705481" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="26"  value="1" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="28"  value="1" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="19"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="26"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="25"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="75-56-9" />
-<Smiles name="SMILES"  value="CC1OC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1472" />
-<CompoundID name="Name"  value="Cumene hydroperoxide" />
-<StructureFormula name="Structure"  value="(C6H5)C(CH3)2OOH" />
-<Family name="Family"  value="64" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="605" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3340000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.463" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.278" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="442.7" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="264.26" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="264.26" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00236574" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="152.19" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.145892" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.995" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.532E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21500" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.95412E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08825" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.162E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.84E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.6E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="455000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.8444E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="8.9801" />
-  <B value="-0.0037758" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="105.7" />
-  <Tmax units="K"  value="264.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.6643" />
-  <B value="0.27801" />
-  <C value="605" />
-  <D value="0.28637" />
-  <Tmin units="K"  value="264.26" />
-  <Tmax units="K"  value="605" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="156.523" />
-  <B value="-16668.56" />
-  <C value="-17.98221" />
-  <D value="0.0000113017" />
-  <E value="2" />
-  <Tmin units="K"  value="264.26" />
-  <Tmax units="K"  value="494.28" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="7.2836E+07" />
-  <B value="0.18056" />
-  <C value="-0.22381" />
-  <D value="-0.21673" />
-  <E value="0.35898" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="307.65" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7404" />
-  <B value="942.63" />
-  <C value="-1.8511" />
-  <D value="0.0047682" />
-  <E value="-0.0000054326" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="264.26" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="83403" />
-  <B value="-35.074" />
-  <C value="9.3262" />
-  <D value="0.010979" />
-  <E value="-0.00001071" />
-  <Tmin units="K"  value="264.26" />
-  <Tmax units="K"  value="442.7" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="70090" />
-  <B value="-408.89" />
-  <C value="12.927" />
-  <D value="0.00036839" />
-  <E value="-1.5886E-07" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.9678E-07" />
-  <B value="0.71936" />
-  <C value="203.36" />
-  <D value="-7639" />
-  <Tmin units="K"  value="264.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.022189" />
-  <B value="-77.144" />
-  <C value="-1.2225" />
-  <D value="-0.0023354" />
-  <E value="4.0588E-08" />
-  <Tmin units="K"  value="264.26" />
-  <Tmax units="K"  value="442.7" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00018194" />
-  <B value="0.94296" />
-  <C value="592.69" />
-  <D value="22533" />
-  <Tmin units="K"  value="442.7" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.045171" />
-  <B value="4.6642" />
-  <C value="-2.3249" />
-  <D value="-0.0010841" />
-  <E value="-3.4989E-07" />
-  <Tmin units="K"  value="264.26" />
-  <Tmax units="K"  value="442.7" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-20463" />
-  <B value="844.33" />
-  <C value="-0.56023" />
-  <D value="0.00014275" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="33.2" />
-  <B value="8625.8" />
-  <C value="-44.733" />
-  <Tmin units="K"  value="367.57" />
-  <Tmax units="K"  value="494.28" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.484118" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.707874E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="393.7584" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.278" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0577525" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.053372" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.995" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.145892" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.817402" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.648" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.995" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21500" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.145892" />
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="10"  value="5" />
-  <group id="11"  value="1" />
-  <group id="15"  value="1" />
-  <group id="18"  value="1" />
-  </Asog>
-<CAS name="CAS number"  value="80-15-9" />
-<Smiles name="SMILES"  value="c1ccccc1(C(C)(C)OO)" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1773" />
-<CompoundID name="Name"  value="Propionitrile" />
-<StructureFormula name="Structure"  value="CH3CH2CN" />
-<Family name="Family"  value="38" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="564.4" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4180000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.229" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.204" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="370.5" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="180.26" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="180.26" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.169356" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="55.0785" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0708565" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.324267" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.652E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="21760" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.34E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0386" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.66E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="5.15E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.74949E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="286600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5029170" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.2586" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.8007E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="20.345" />
-  <B value="-0.012638" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="72.1" />
-  <Tmax units="K"  value="180.26" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.90359" />
-  <B value="0.2211" />
-  <C value="564.4" />
-  <D value="0.26246" />
-  <Tmin units="K"  value="180.26" />
-  <Tmax units="K"  value="564.4" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="81.601" />
-  <B value="-6646.8" />
-  <C value="-8.9882" />
-  <D value="0.0000074443" />
-  <E value="2" />
-  <Tmin units="K"  value="180.26" />
-  <Tmax units="K"  value="564.4" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.633259E+07" />
-  <B value="-2.107222" />
-  <C value="8.013128" />
-  <D value="-9.747514" />
-  <E value="4.114254" />
-  <Tmin units="K"  value="180.26" />
-  <Tmax units="K"  value="564.4" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-14960" />
-  <B value="1312.1" />
-  <C value="-7.69" />
-  <D value="0.017079" />
-  <E value="0.000015678" />
-  <Tmin units="K"  value="15" />
-  <Tmax units="K"  value="170" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="105770" />
-  <B value="154.89" />
-  <C value="4.5843" />
-  <D value="0.018329" />
-  <E value="-0.000011984" />
-  <Tmin units="K"  value="180.26" />
-  <Tmax units="K"  value="370.5" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="47947" />
-  <B value="-544.83" />
-  <C value="11.91" />
-  <D value="0.00026005" />
-  <E value="-9.1233E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.088354" />
-  <B value="-183.35" />
-  <C value="-90.512" />
-  <D value="-32289" />
-  <E value="-55646" />
-  <Tmin units="K"  value="338.64" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.0958" />
-  <B value="775.57" />
-  <C value="-0.393" />
-  <D value="-7.9624E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="370.5" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="9.8851E-08" />
-  <B value="0.79377" />
-  <C value="155.28" />
-  <D value="-11568" />
-  <Tmin units="K"  value="180.26" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.13846" />
-  <B value="2645.2" />
-  <C value="-37.177" />
-  <D value="0.15078" />
-  <E value="-0.00022598" />
-  <Tmin units="K"  value="180.26" />
-  <Tmax units="K"  value="413.15" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00048871" />
-  <B value="1.327" />
-  <C value="43042" />
-  <D value="-3226700" />
-  <Tmin units="K"  value="370.5" />
-  <Tmax units="K"  value="990.5" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.018019" />
-  <B value="28.207" />
-  <C value="-2.8898" />
-  <D value="0.00012339" />
-  <E value="-0.0000039362" />
-  <Tmin units="K"  value="180.26" />
-  <Tmax units="K"  value="564.4" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="17680" />
-  <B value="218.52" />
-  <C value="-0.10368" />
-  <D value="0.000017753" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-19.90771" />
-  <B value="-10000" />
-  <C value="-83.1" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.537" />
-  <B value="3368.2" />
-  <C value="-34.373" />
-  <Tmin units="K"  value="342" />
-  <Tmax units="K"  value="503.75" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.9156" />
-  <B value="-0.0096282" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="370.5" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.204617" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.690725E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="120.5504" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.204" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="63.79" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="-2.1562" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0289561" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.786785" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.324267" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0708565" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.5445" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.264" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="3.5161" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.324267" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="21760" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0708565" />
-<UnifacVLE name="UNIFAC" >
-  <group id="42"  value="1" />
-  <group id="1"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="28"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="42"  value="1" />
-  <group id="1"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="107-12-0" />
-<Smiles name="SMILES"  value="CCC#N" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2391" />
-<CompoundID name="Name"  value="Dimethyl carbonate" />
-<StructureFormula name="Structure"  value="(CH3O)2CO" />
-<Family name="Family"  value="45" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="557" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4800000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.25163" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.261" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="363.24" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="276.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="273.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1825.53" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="90.084" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.084825" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.337" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.247E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="20240" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="3.0E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04624" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.04E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.701E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4.524E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="321600" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.2E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.98328" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.295E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="15.551" />
-  <B value="-0.0071164" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="109.26" />
-  <Tmax units="K"  value="273.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.0073625" />
-  <B value="0.022214" />
-  <C value="557" />
-  <D value="0.083013" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="548" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="127.2975" />
-  <B value="-8353.984" />
-  <C value="-16.14514" />
-  <D value="0.0000181933" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="548" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.291764E+07" />
-  <B value="1.146922" />
-  <C value="-2.489366" />
-  <D value="2.898325" />
-  <E value="-1.182726" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="548" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="1690" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="273.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="170430" />
-  <B value="-2560.3" />
-  <C value="-9.9628" />
-  <D value="-0.012169" />
-  <E value="0.000014736" />
-  <Tmin units="K"  value="292.95" />
-  <Tmax units="K"  value="361.15" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="62577" />
-  <B value="-594.2" />
-  <C value="12.53" />
-  <D value="-0.000022352" />
-  <E value="-2.2803E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.17199" />
-  <B value="-186.08" />
-  <C value="-30.494" />
-  <D value="-4242.1" />
-  <E value="2158.1" />
-  <Tmin units="K"  value="274" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-235.18" />
-  <B value="9633.9" />
-  <C value="34.904" />
-  <D value="-0.000038795" />
-  <E value="2" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="438.4" />
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-  <Tmax units="K"  value="1000" />
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-  <eqno value="16" />
-  <A value="0.011223" />
-  <B value="-183.44" />
-  <C value="0.22279" />
-  <D value="-0.0056614" />
-  <E value="0.0000021056" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="363.4" />
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-  <B value="0.89541" />
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-  <D value="19356" />
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-  <Tmax units="K"  value="1000" />
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-  <C value="-8.4539" />
-  <D value="0.016647" />
-  <E value="-0.000022126" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="548" />
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-  <B value="384.59" />
-  <C value="-0.2325" />
-  <D value="0.000052013" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
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-  <B value="-1545" />
-  <C value="-9.27" />
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-  <Tmax units="K"  value="450" />
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-  <eqno value="10" />
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-  <B value="3264.5" />
-  <C value="-42.989" />
-  <Tmin units="K"  value="335.2" />
-  <Tmax units="K"  value="490.14" />
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-  <A value="-5.3228" />
-  <B value="-0.0072352" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="438.4" />
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-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.904691E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="288.8513" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.261" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="79.89" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0350959" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.075345" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.337" />
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-<UniquacR  name="UNIQUAC r"  units="_"  value="3.3822" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.086" />
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-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="20240" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.084825" />
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-<CriticalPressure name="Critical pressure"  units="Pa"  value="3420000" />
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-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="4.443408E+07" />
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-<VaporPressure name="Vapour pressure"  units="Pa" >
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-  <eqno value="1" />
-  <A value="170310" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="423.12" />
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-  <eqno value="4" />
-  <A value="-748.0008" />
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-  <C value="-0.1938" />
-  <D value="0.0000364" />
-  <Tmin units="K"  value="126.9366" />
-  <Tmax units="K"  value="1500" />
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-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="2" />
-  <A value="-0.0000012839" />
-  <B value="1.9951E-08" />
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-  <Tmax units="K"  value="1000" />
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-  <eqno value="4" />
-  <A value="8394.8" />
-  <B value="358.12" />
-  <C value="-0.17146" />
-  <D value="0.000031221" />
-  <Tmin units="K"  value="126.94" />
-  <Tmax units="K"  value="1500" />
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-  <eqno value="120" />
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-  <B value="-1410" />
-  <C value="-8.46" />
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-  <Tmax units="K"  value="450" />
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-  <eqno value="10" />
-  <A value="21.72793" />
-  <B value="3499.52" />
-  <C value="-55.48797" />
-  <Tmin units="K"  value="263" />
-  <Tmax units="K"  value="577" />
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-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="5.206992E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="327.1211" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254676" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="120.93" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0.3544" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0445" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.975" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.3544" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.09721" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="4.731" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.166" />
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-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.12721" />
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-  <Tmax units="K"  value="1500" />
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-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.9825" />
-  <B value="3769.291" />
-  <C value="-93.16374" />
-  <Tmin units="K"  value="393.408" />
-  <Tmax units="K"  value="711.76" />
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-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.988531E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="257.1649" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.244961" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="145.71" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.05" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.14" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.41299" />
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-<compound>
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-<CompoundID name="Name"  value="Ethyl Phenyl Carbonate" />
-<StructureFormula name="Structure"  value="CH3CH2(OCOO)C6H5" />
-<Family name="Family"  value="45" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="729.29" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2529800" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.55209" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.230336" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="522.67" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="166.1762" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.18105" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.54406" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="18670.52" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.0937081" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.2245E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.138466E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.263844E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="970006.4" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.867867" />
-<VaporPressure name="Vapour pressure"  units="Pa" >
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-  <eqno value="4" />
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-  <Tmax units="K"  value="1500" />
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-  <eqno value="2" />
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-  <Tmin units="K"  value="427.89" />
-  <Tmax units="K"  value="1000" />
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-  <eqno value="4" />
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-  <B value="643.04" />
-  <C value="-0.37254" />
-  <D value="0.000089182" />
-  <Tmin units="K"  value="198.34" />
-  <Tmax units="K"  value="1500" />
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-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.03089" />
-  <B value="3977.417" />
-  <C value="-104.2059" />
-  <Tmin units="K"  value="418.136" />
-  <Tmax units="K"  value="729.29" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.517543" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.279963E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="274.1277" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.230336" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="166.23" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0644" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.108" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.54406" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.18105" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.1772" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.898" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.54406" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.18105" />
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-<compound>
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-<CompoundID name="Name"  value="DiPhenyl Carbonate" />
-<StructureFormula name="Structure"  value="(C6H5)2(OCOO)" />
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-<CriticalTemperature name="Critical temperature"  units="K"  value="799.32" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2796500" />
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-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.251145" />
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-<AcentricityFactor name="Acentric factor"  units="_"  value="0.55805" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.600808E-10" />
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-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.115626" />
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-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="1.832592E+08" />
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-<VaporPressure name="Vapour pressure"  units="Pa" >
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-  <E value="0" />
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-  <Tmin units="K"  value="273" />
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-  <D value="0" />
-  <E value="0" />
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-  <E value="0" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="760.5541" />
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-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="273" />
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-  <Tmin units="K"  value="458.392" />
-  <Tmax units="K"  value="799.32" />
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-<Smiles name="SMILES"  value="C1=CC=C(C=C1)OC(=O)OC2=CC=CC=C2" />
-</compound>
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-<compound>
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-<CriticalTemperature name="Critical temperature"  units="K"  value="806" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6770000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.193" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.195" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="521.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="309.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="309.55" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="8.01004" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="88.0621" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0664942" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.442272" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.841E-10" />
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-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.5E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.03822" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="4.93E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.069E+08" />
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-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="260000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.0E+07" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.09004" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.083E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
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-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
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-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
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-  <eqno value="101" />
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-  <E value="2.9631" />
-  <Tmin units="K"  value="309.55" />
-  <Tmax units="K"  value="779.87" />
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-  <eqno value="100" />
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-  <B value="304010" />
-  <C value="-3104" />
-  <D value="10.582" />
-  <E value="-0.012029" />
-  <Tmin units="K"  value="288.15" />
-  <Tmax units="K"  value="298.15" />
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-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
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-  <B value="-17.021" />
-  <C value="11.366" />
-  <D value="0.0033817" />
-  <E value="-0.0000020646" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="511.15" />
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-  <eqno value="16" />
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-  <C value="12.288" />
-  <D value="0.000013893" />
-  <E value="-2.689E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
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-  <eqno value="104" />
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-  <D value="-699130" />
-  <E value="1646500" />
-  <Tmin units="K"  value="403" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.7402" />
-  <B value="1424.5" />
-  <C value="-0.45708" />
-  <D value="0.0000005934" />
-  <E value="2" />
-  <Tmin units="K"  value="310.93" />
-  <Tmax units="K"  value="372.04" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="8.5517E-08" />
-  <B value="0.85448" />
-  <C value="116.16" />
-  <D value="-3914.9" />
-  <Tmin units="K"  value="309.55" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.00091342" />
-  <B value="-110.82" />
-  <C value="-0.51748" />
-  <D value="-0.0023793" />
-  <E value="3.9376E-07" />
-  <Tmin units="K"  value="309.55" />
-  <Tmax units="K"  value="521.35" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.030823" />
-  <B value="0.34958" />
-  <C value="3003.2" />
-  <D value="830800" />
-  <Tmin units="K"  value="521.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.069239" />
-  <B value="49.575" />
-  <C value="-2.2485" />
-  <D value="-0.0002049" />
-  <E value="-5.0141E-07" />
-  <Tmin units="K"  value="309.55" />
-  <Tmax units="K"  value="779.87" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="5956" />
-  <B value="338.31" />
-  <C value="-0.21843" />
-  <D value="0.000052329" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="0.204056" />
-  <B value="-18366.46" />
-  <C value="-107.1818" />
-  <Tmin units="K"  value="309" />
-  <Tmax units="K"  value="806" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="22.69" />
-  <B value="5599.1" />
-  <C value="-19.097" />
-  <Tmin units="K"  value="492.45" />
-  <Tmax units="K"  value="701.48" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-2.6347" />
-  <B value="-0.013224" />
-  <Tmin units="K"  value="310.93" />
-  <Tmax units="K"  value="372.04" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.202594" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.668715E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="146.3433" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.195" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="75.27" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0299348" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.343115" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.442272" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0664942" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.9288" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.47" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.442272" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="29660" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0664942" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="2" />
-  <group id="120"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="2"  value="1" />
-  <group id="21"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="2" />
-  <group id="120"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="96-49-1" />
-<Smiles name="SMILES"  value="C1OC(=O)OC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2367" />
-<CompoundID name="Name"  value="Propylene carbonate" />
-<StructureFormula name="Structure"  value="-OCH(CH3)CH2OCO-" />
-<Family name="Family"  value="45" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="778" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="5410000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.246" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.206" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="514.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="218.62" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="224.85" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00116652" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="102.089" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0852768" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.449764" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.413E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="27300" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.65E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04519" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.7E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-6.0116E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4.555E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="296300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="9617000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="1.09674" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.6678E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="15.979" />
-  <B value="-0.0088829" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="89.94" />
-  <Tmax units="K"  value="224.85" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.122" />
-  <B value="0.27599" />
-  <C value="778" />
-  <D value="0.40344" />
-  <Tmin units="K"  value="224.85" />
-  <Tmax units="K"  value="778" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="102.32" />
-  <B value="-10530" />
-  <C value="-11.489" />
-  <D value="0.0000052921" />
-  <E value="2" />
-  <Tmin units="K"  value="224.85" />
-  <Tmax units="K"  value="778" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.145898E+08" />
-  <B value="9.998207" />
-  <C value="-26.2884" />
-  <D value="28.38292" />
-  <E value="-11.49051" />
-  <Tmin units="K"  value="224.85" />
-  <Tmax units="K"  value="778" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="3041.6" />
-  <B value="908.81" />
-  <C value="-3.5669" />
-  <D value="0.00717" />
-  <E value="8.8712E-08" />
-  <Tmin units="K"  value="55" />
-  <Tmax units="K"  value="224.5" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="121750" />
-  <B value="105.89" />
-  <C value="6.5083" />
-  <D value="0.016964" />
-  <E value="-0.000014577" />
-  <Tmin units="K"  value="298.15" />
-  <Tmax units="K"  value="425" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="51696" />
-  <B value="-502.59" />
-  <C value="12.655" />
-  <D value="-0.000076494" />
-  <E value="1.3781E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16441" />
-  <B value="-219.89" />
-  <C value="-163.04" />
-  <D value="-737950" />
-  <E value="1715100" />
-  <Tmin units="K"  value="389" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-818.33" />
-  <B value="28057" />
-  <C value="129.62" />
-  <D value="-0.00022812" />
-  <E value="2" />
-  <Tmin units="K"  value="219" />
-  <Tmax units="K"  value="622.4" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.7119E-08" />
-  <B value="0.92676" />
-  <C value="86.628" />
-  <D value="-9783.8" />
-  <Tmin units="K"  value="224.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.096241" />
-  <B value="6.7832" />
-  <C value="-1.0385" />
-  <D value="-0.00032841" />
-  <E value="-6.9782E-07" />
-  <Tmin units="K"  value="224.85" />
-  <Tmax units="K"  value="514.85" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00017416" />
-  <B value="0.94857" />
-  <C value="659.28" />
-  <D value="16364" />
-  <Tmin units="K"  value="514.85" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0051901" />
-  <B value="69.321" />
-  <C value="-3.1157" />
-  <D value="0.00082804" />
-  <E value="-0.0000049222" />
-  <Tmin units="K"  value="224.85" />
-  <Tmax units="K"  value="778" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-6737.7" />
-  <B value="477.48" />
-  <C value="-0.32123" />
-  <D value="0.000080589" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="0.412687" />
-  <B value="-16994.83" />
-  <C value="-34.01907" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="778" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.845" />
-  <B value="4552.5" />
-  <C value="-73.662" />
-  <Tmin units="K"  value="471.91" />
-  <Tmax units="K"  value="690.66" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-1.8879" />
-  <B value="-0.012915" />
-  <Tmin units="K"  value="219" />
-  <Tmax units="K"  value="622.4" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.239863" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.784834E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="172.1134" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.206" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="95.79" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0381263" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.208416" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.449764" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0852768" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.6024" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="3.006" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.449764" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="27300" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0852768" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="120"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="3"  value="1" />
-  <group id="21"  value="1" />
-  <group id="22"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="1" />
-  <group id="2"  value="1" />
-  <group id="3"  value="1" />
-  <group id="120"  value="1" />
-  </Umr>
-<CAS name="CAS number"  value="108-32-7" />
-<Smiles name="SMILES"  value="C1C(C)OC(=O)O1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="2252" />
-<CompoundID name="Name"  value="2-methyl-1-heptene" />
-<StructureFormula name="Structure"  value="CH2C(CH3)CH2(CH2)3CH3" />
-<Family name="Family"  value="11" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="564" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2400000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.497" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.25" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="392.37" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="185.78" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="185.77" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.113498" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="112.213" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.156655" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.35513" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.51E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="15180" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08521" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.211E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9.699E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="9.32E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="457800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.44E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.948E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.1821" />
-  <B value="-0.0061784" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="74.31" />
-  <Tmax units="K"  value="185.77" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.53765" />
-  <B value="0.25476" />
-  <C value="567.01" />
-  <D value="0.28376" />
-  <Tmin units="K"  value="185.77" />
-  <Tmax units="K"  value="567" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="108.46" />
-  <B value="-8257.2" />
-  <C value="-12.941" />
-  <D value="0.0000091062" />
-  <E value="2" />
-  <Tmin units="K"  value="185.77" />
-  <Tmax units="K"  value="567" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="5.8021E+07" />
-  <B value="1.4711" />
-  <C value="-3.336" />
-  <D value="3.8018" />
-  <E value="-1.5579" />
-  <Tmin units="K"  value="185.77" />
-  <Tmax units="K"  value="546.94" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="1" />
-  <A value="208080" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="564" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="88257" />
-  <B value="855.11" />
-  <C value="3.1929" />
-  <D value="0.026245" />
-  <E value="-0.000022451" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="425.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="92500" />
-  <B value="-450.54" />
-  <C value="12.712" />
-  <D value="0.00068864" />
-  <E value="-3.0334E-07" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.26129" />
-  <B value="-298.53" />
-  <C value="-61.563" />
-  <D value="-2356.6" />
-  <E value="-3540.3" />
-  <Tmin units="K"  value="283.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-34.674" />
-  <B value="1655.3" />
-  <C value="3.8693" />
-  <D value="-0.0000085602" />
-  <E value="2" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="473.15" />
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-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="5.7686E-07" />
-  <B value="0.51551" />
-  <C value="255.32" />
-  <D value="-429.98" />
-  <Tmin units="K"  value="185.77" />
-  <Tmax units="K"  value="1000" />
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-  <eqno value="16" />
-  <A value="-0.0714" />
-  <B value="1.7767" />
-  <C value="-1.4729" />
-  <D value="-0.00055517" />
-  <E value="-0.0000010492" />
-  <Tmin units="K"  value="185.77" />
-  <Tmax units="K"  value="392.37" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00085233" />
-  <B value="0.71803" />
-  <C value="81.386" />
-  <D value="330930" />
-  <Tmin units="K"  value="392.37" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
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-  <eqno value="16" />
-  <A value="-0.01103" />
-  <B value="38.104" />
-  <C value="-3.171" />
-  <D value="0.000054009" />
-  <E value="-0.0000046411" />
-  <Tmin units="K"  value="185.77" />
-  <Tmax units="K"  value="546.94" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="6589.8" />
-  <B value="674.58" />
-  <C value="-0.32408" />
-  <D value="0.00004613" />
-  <Tmin units="K"  value="250" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.992" />
-  <B value="3231.9" />
-  <C value="-50.935" />
-  <Tmin units="K"  value="342.45" />
-  <Tmax units="K"  value="506.81" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.0096" />
-  <B value="-0.012148" />
-  <Tmin units="K"  value="173.15" />
-  <Tmax units="K"  value="473.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.465787" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.801338E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="250.4819" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.25" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="164.16" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0593532" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.724648" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.35513" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.156655" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.6171" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.844" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.35513" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="15180" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.156655" />
-<UnifacVLE name="UNIFAC" >
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-  </ModifiedUnifac>
-<CAS name="CAS number"  value="15870-10-7" />
-<Smiles name="SMILES"  value="C=C(C)CCCCC" />
-</compound>
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-<compound>
-<LibraryIndex name="Index"  value="22158" />
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-<StructureFormula name="Structure"  value="(CH3O)(CH3)2 C(CH2)4 CH3" />
-<Family name="Family"  value="61" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="618.2025" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2357849" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.53093" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.24355" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="446.7301" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="144.2564" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.18511" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.433286" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="14871.82" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.102631" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.448E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-9790565" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-6.029269" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="1629362" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.95423E+09" />
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="200" />
-  <A value="-8.2705" />
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-  <D value="-3.7256" />
-  <E value="2357800" />
-  <Tmin units="K"  value="312.71" />
-  <Tmax units="K"  value="618.2" />
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-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
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-  <D value="0" />
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-  <Tmin units="K"  value="312.71" />
-  <Tmax units="K"  value="618.2" />
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-  <eqno value="1" />
-  <A value="262630" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="618.2" />
-  </SolidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-4265.999" />
-  <B value="921.48" />
-  <C value="-0.5266" />
-  <D value="0.000113" />
-  <Tmin units="K"  value="185.4608" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="2" />
-  <A value="-4.0287E-08" />
-  <B value="1.4474E-08" />
-  <Tmin units="K"  value="446.73" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="4302" />
-  <B value="902.18" />
-  <C value="-0.49999" />
-  <D value="0.00010387" />
-  <Tmin units="K"  value="185.46" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="20.91" />
-  <B value="3457.7" />
-  <C value="-78.254" />
-  <Tmin units="K"  value="312.71" />
-  <Tmax units="K"  value="618.2" />
-  </AntoineVaporPressure>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.573677" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="8.229094E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="249.8964" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.24355" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="195.41" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0641327" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.433286" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.18511" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.7654" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.792" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.433286" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="14871.82" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.18511" />
-<UnifacVLE name="UNIFAC" >
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-</compound>
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-<compound>
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-<StructureFormula name="Structure"  value="(CH3)2(OH)C(CH2)4CH3" />
-<Family name="Family"  value="46" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="636.6534" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2716180" />
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-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.247551" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="467.6976" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="130.2296" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.15788" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.723562" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17397.3" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.100431" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.476E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-1.238045" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.233886" />
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-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-5.204435" />
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="200" />
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-  <Tmin units="K"  value="327.39" />
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-  <eqno value="106" />
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-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="327.39" />
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-  <eqno value="1" />
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-  <eqno value="4" />
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-  <D value="0.0001657" />
-  <Tmin units="K"  value="190.996" />
-  <Tmax units="K"  value="1500" />
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-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="2" />
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-  <B value="1.4972E-08" />
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-  <Tmax units="K"  value="1000" />
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-  <eqno value="4" />
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-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
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-  <eqno value="120" />
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-  <Tmin units="K"  value="327.39" />
-  <Tmax units="K"  value="636.65" />
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-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0547474" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.82" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.723562" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.15788" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.6204" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.904" />
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-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.15788" />
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-
-<compound>
-<LibraryIndex name="Index"  value="1431" />
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-<Family name="Family"  value="25" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="480.6" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3950000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.213" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.211" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="315" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="168" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="168.35" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="1.13284" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="76.0944" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0891275" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.285565" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.891E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="17430" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="2.47E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04497" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="6.79E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.482E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.263E+08" />
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-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="8330000" />
-<MatthiasCopemanC1 name="Mathias-Copeman C1"  units="_"  value="0.82106" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.7998E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
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-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="67.34" />
-  <Tmax units="K"  value="168.35" />
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-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.4351" />
-  <B value="0.30572" />
-  <C value="480.6" />
-  <D value="0.31739" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="480.6" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="62.15058" />
-  <B value="-5217.94" />
-  <C value="-5.982976" />
-  <D value="3.491239E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="480.6" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.956236E+07" />
-  <B value="0.517705" />
-  <C value="0.708214" />
-  <D value="-1.530256" />
-  <E value="0.744705" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="480.6" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="-23498" />
-  <B value="1741.5" />
-  <C value="-11.164" />
-  <D value="0.04279" />
-  <E value="-0.000078511" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="168.03" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="134330" />
-  <B value="575.02" />
-  <C value="0.73414" />
-  <D value="0.035906" />
-  <E value="-0.00003541" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="315" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="73387" />
-  <B value="-1249" />
-  <C value="14.774" />
-  <D value="-0.0029552" />
-  <E value="0.0000012399" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="1000.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.16872" />
-  <B value="-171.97" />
-  <C value="-17.875" />
-  <D value="-56.611" />
-  <E value="-1706.7" />
-  <Tmin units="K"  value="240.3" />
-  <Tmax units="K"  value="1968.3" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-8.4058" />
-  <B value="722.36" />
-  <C value="-0.36572" />
-  <D value="2.4819E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="378.5" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="4.8512E-07" />
-  <B value="0.60235" />
-  <C value="248.43" />
-  <D value="-1208.9" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.11543" />
-  <B value="-776.65" />
-  <C value="7.882" />
-  <D value="-0.041206" />
-  <E value="0.000038121" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="315" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0014869" />
-  <B value="0.65846" />
-  <C value="470.64" />
-  <D value="206460" />
-  <Tmin units="K"  value="315" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.027396" />
-  <B value="-6.2054" />
-  <C value="-2.2451" />
-  <D value="-0.0022104" />
-  <E value="-0.0000012647" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="480.6" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-11636" />
-  <B value="411.45" />
-  <C value="-0.24227" />
-  <D value="0.000049287" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="1000.15" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-2.036011" />
-  <B value="-1350" />
-  <C value="-8.1" />
-  <Tmin units="K"  value="274.15" />
-  <Tmax units="K"  value="444.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21" />
-  <B value="2534.2" />
-  <C value="-47.822" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="431.3" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="-4.1816" />
-  <B value="-0.012718" />
-  <Tmin units="K"  value="168.35" />
-  <Tmax units="K"  value="378.5" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.23868" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.209402E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="115.9081" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.211" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="78.39999" />
-<MatthiasCopemanC2 name="Mathias-Copeman C2"  units="_"  value="0" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0337574" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.865971" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.285565" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.0891275" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="2.964403" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.716" />
-<MatthiasCopemanC3 name="Mathias-Copeman C3"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.285565" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="17430" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.0891275" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="25"  value="2" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="1" />
-  <group id="27"  value="2" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="19"  value="2" />
-  </Asog>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="1" />
-  <group id="24"  value="2" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="109-87-5" />
-<Smiles name="SMILES"  value="COCOC" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1722" />
-<CompoundID name="Name"  value="Methyl DiEthanolAmine" />
-<StructureFormula name="Structure"  value="CH3N(CH2CH2OH)2" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="741.9" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4160000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.365" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.246154" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="520.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="252.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="252.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00203612" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="119.162" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.115302" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.1649" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.366E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="28140" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="9.53993E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.075" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.067E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-3.8E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-1.69E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="469000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="0" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.06E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="11.449" />
-  <B value="-0.0051119" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="100.86" />
-  <Tmax units="K"  value="252.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.69135" />
-  <B value="0.25418" />
-  <C value="675" />
-  <D value="0.2857" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="675" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="-0.352098" />
-  <B value="-4812.65" />
-  <C value="3.121045" />
-  <D value="6.605463E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="678" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.40201E+08" />
-  <B value="0.632751" />
-  <C value="0.350924" />
-  <D value="-0.633597" />
-  <E value="0.0584955" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="675" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="6425.8" />
-  <B value="839.54" />
-  <C value="-1.7005" />
-  <D value="0.0045352" />
-  <E value="-0.0000053648" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="252.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="181326" />
-  <B value="26.21689" />
-  <C value="0.880838" />
-  <D value="0" />
-  <E value="-0.00001581" />
-  <Tmin units="K"  value="290" />
-  <Tmax units="K"  value="506.25" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="89777" />
-  <B value="-550.24" />
-  <C value="13.01" />
-  <D value="0.000045139" />
-  <E value="-3.2024E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.25763" />
-  <B value="-148.02" />
-  <C value="-177.99" />
-  <D value="-169010" />
-  <E value="271570" />
-  <Tmin units="K"  value="337.5" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-162.0804" />
-  <B value="9995.149" />
-  <C value="22.49076" />
-  <D value="-0.0000361184" />
-  <E value="1.932506" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="7.7364E-08" />
-  <B value="0.84268" />
-  <C value="140.24" />
-  <D value="-9063.1" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.869" />
-  <B value="15" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="518" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00016443" />
-  <B value="0.97072" />
-  <C value="595.54" />
-  <D value="41960" />
-  <Tmin units="K"  value="518" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0388377" />
-  <B value="-28.75677" />
-  <C value="-2.216016" />
-  <D value="-0.00048763" />
-  <E value="-1.144892E-06" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="742" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-4949.1" />
-  <B value="671.33" />
-  <C value="-0.40892" />
-  <D value="0.00009394" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1500" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-11.07032" />
-  <B value="-9774.9" />
-  <C value="-6.426155" />
-  <Tmin units="K"  value="303" />
-  <Tmax units="K"  value="675" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="26.512" />
-  <B value="8069.9" />
-  <C value="21.545" />
-  <Tmin units="K"  value="407.94" />
-  <Tmax units="K"  value="592.83" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="6.0457" />
-  <B value="-0.029282" />
-  <Tmin units="K"  value="252.15" />
-  <Tmax units="K"  value="540" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.405616" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.125674E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="317.4084" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.254" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="126.29" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0511332" />
-<SpecificGravity name="Specific gravity"  units="_"  value="1.04" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.1649" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.115302" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.8841" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="5.5" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.1649" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="28140" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.115302" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  <group id="35"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="1" />
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  <group id="31"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="2"  value="4" />
-  <group id="15"  value="2" />
-  <group id="35"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="2"  value="4" />
-  <group id="14"  value="2" />
-  <group id="34"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="105-59-9" />
-<Smiles name="SMILES"  value="CN(CCO)CCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="6861" />
-<CompoundID name="Name"  value="Diethylethanolamine" />
-<StructureFormula name="Structure"  value="HOCH2CH2N(CH2CH3)2" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="616" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="2650000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.4231" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.218914" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="434.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="235.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="253" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="4.85244" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="117.189" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.132864" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.781757" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.407E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="19100" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="8.11E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08063" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.133E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-2.575E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-3.323E+07" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="459800" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.84E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-4.03338E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="10.088" />
-  <B value="-0.0049843" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="101.2" />
-  <Tmax units="K"  value="253" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.63795" />
-  <B value="0.25988" />
-  <C value="592" />
-  <D value="0.27186" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="592" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="442.3122" />
-  <B value="-22650.03" />
-  <C value="-64.35227" />
-  <D value="0.0000641088" />
-  <E value="2" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="592" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="6.442525E+07" />
-  <B value="-0.590881" />
-  <C value="4.028331" />
-  <D value="-5.586056" />
-  <E value="2.388691" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="592" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="102" />
-  <A value="2220" />
-  <B value="0.79267" />
-  <C value="0" />
-  <D value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="253" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="28933.37" />
-  <B value="738.1104" />
-  <C value="-0.669126" />
-  <D value="0.000593149" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="592" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="91061" />
-  <B value="-562.7" />
-  <C value="13.172" />
-  <D value="-0.000023606" />
-  <E value="6.7111E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.27423" />
-  <B value="-227.63" />
-  <C value="-93.133" />
-  <D value="-46929" />
-  <E value="69828" />
-  <Tmin units="K"  value="296" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-83.307" />
-  <B value="6061.8" />
-  <C value="10.089" />
-  <D value="-1.4583E-07" />
-  <E value="2" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="436.15" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.3335E-07" />
-  <B value="0.7599" />
-  <C value="186.08" />
-  <D value="-6648.4" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.0045149" />
-  <B value="-46.605" />
-  <C value="-1.1875" />
-  <D value="-0.0019723" />
-  <E value="-5.2781E-08" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="443" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00013877" />
-  <B value="0.99774" />
-  <C value="582.26" />
-  <D value="23748" />
-  <Tmin units="K"  value="436.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="2" />
-  <A value="0.065" />
-  <B value="-0.00011" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="592" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-23633" />
-  <B value="791.71" />
-  <C value="-0.51703" />
-  <D value="0.00013437" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="23.092" />
-  <B value="4628.3" />
-  <C value="-36.082" />
-  <Tmin units="K"  value="360.05" />
-  <Tmax units="K"  value="520.63" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="6.4" />
-  <B value="-0.04" />
-  <Tmin units="K"  value="253" />
-  <Tmax units="K"  value="436.15" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.438537" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="7.157819E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="298.6167" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.259" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="140.7" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.05675" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.884" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="0.781757" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.132864" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="5.315095" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="4.532" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="1.602722" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="0.781757" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="19100" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.132864" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="15"  value="1" />
-  <group id="36"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="4" />
-  <group id="15"  value="1" />
-  <group id="31"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="15"  value="1" />
-  <group id="36"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="3" />
-  <group id="14"  value="1" />
-  <group id="35"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="100-37-8" />
-<Smiles name="SMILES"  value="CCN(CC)CCO" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="6864" />
-<CompoundID name="Name"  value="Diisopropanolamine" />
-<StructureFormula name="Structure"  value="CH3CH(OH)CH2NHCH2CH(OH)CH3" />
-<Family name="Family"  value="68" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="672" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="3600000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.454" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.293" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="521.9" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="315" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="318.15" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.217912" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="133.189" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.134763" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.38914" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="4.694E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="26610" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.08552" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="1.199E+09" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-4.54E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2.15E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="513000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="2.636E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-3.82E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="100" />
-  <A value="9.4982" />
-  <B value="-0.0037318" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="127.26" />
-  <Tmax units="K"  value="318.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.54022" />
-  <B value="0.24621" />
-  <C value="672" />
-  <D value="0.22052" />
-  <Tmin units="K"  value="293.15" />
-  <Tmax units="K"  value="672" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="339.329" />
-  <B value="-25910.98" />
-  <C value="-45.42461" />
-  <D value="0.0000223088" />
-  <E value="2" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="672" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.4113E+08" />
-  <B value="0.38119" />
-  <C value="1.0156" />
-  <D value="-1.8242" />
-  <E value="0.83437" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="672" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="100" />
-  <A value="7629.4" />
-  <B value="876.24" />
-  <C value="-1.519" />
-  <D value="0.0034005" />
-  <E value="-0.0000033304" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="318.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="119382.9" />
-  <B value="778.3072" />
-  <C value="-0.00245385" />
-  <D value="-1.190941E-06" />
-  <E value="-0.0000013464" />
-  <Tmin units="K"  value="300" />
-  <Tmax units="K"  value="400" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="104010" />
-  <B value="-559.93" />
-  <C value="13.272" />
-  <D value="-0.00018865" />
-  <E value="9.0295E-08" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.30241" />
-  <B value="-139.52" />
-  <C value="-203.79" />
-  <D value="-134000" />
-  <E value="160130" />
-  <Tmin units="K"  value="336" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="101" />
-  <A value="-158.9768" />
-  <B value="13684.82" />
-  <C value="19.79212" />
-  <D value="0.0000178855" />
-  <E value="1.442815" />
-  <Tmin units="K"  value="303.15" />
-  <Tmax units="K"  value="537.6" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="102" />
-  <A value="1.7289E-07" />
-  <B value="0.71286" />
-  <C value="205.1" />
-  <D value="-6089.6" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="-0.070378" />
-  <B value="-101.18" />
-  <C value="-0.46641" />
-  <D value="-0.0021528" />
-  <E value="2.0992E-07" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="521.9" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.0002313" />
-  <B value="0.90558" />
-  <C value="651.81" />
-  <D value="18136" />
-  <Tmin units="K"  value="521.9" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.091653" />
-  <B value="26.019" />
-  <C value="-2.0608" />
-  <D value="-0.00014789" />
-  <E value="-5.9445E-07" />
-  <Tmin units="K"  value="318.15" />
-  <Tmax units="K"  value="672" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-15774" />
-  <B value="849.72" />
-  <C value="-0.60159" />
-  <D value="0.00017226" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200" />
-  </RPPHeatCapacityCp>
-<RelativeStaticPermittivity name="Relative static permittivity"  units="_" >
-  <eqno value="120" />
-  <A value="-12.64602" />
-  <B value="-6935" />
-  <C value="-41.61" />
-  <Tmin units="K"  value="284.15" />
-  <Tmax units="K"  value="454.15" />
-  </RelativeStaticPermittivity>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="24.415" />
-  <B value="5143.2" />
-  <C value="-123.48" />
-  <Tmin units="K"  value="406.61" />
-  <Tmax units="K"  value="601.23" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="12" />
-  <A value="8.486" />
-  <B value="-0.034714" />
-  <Tmin units="K"  value="303.15" />
-  <Tmax units="K"  value="537.6" />
-  </LiquidViscosityRPS>
-<COSTALDVolume name="COSTLD characteristic volume (V*)"  units="m3/kmol"  value="0.467647" />
-<DiameterLJ name="Lennard Jones diameter"  units="m"  value="6.25685E-10" />
-<EnergyLJ name="Lennard Jones energy"  units="K"  value="528.4525" />
-<RacketParameter name="Rackett parameter"  units="_"  value="0.293" />
-<FullerVolume name="Fuller et al. diffusion volume"  units="_"  value="146.81" />
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.057223" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.999" />
-<Charge name="Charge"  units="_"  value="0" />
-<CostaldAcentricFactor name="SRK acentric factor"  units="_"  value="1.38914" />
-<WilsonVolume name="Wilson volume"  units="m3/kmol"  value="0.134763" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="6.5774" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="6.028" />
-<ApiSrkS1 name="API-SRK s1"  units="_"  value="2.339337" />
-<ApiSrkS2 name="API-SRK s2"  units="_"  value="0" />
-<ChaoSeaderAcentricFactor name="Chao-Seader acentric factor"  units="_"  value="1.38914" />
-<ChaoSeaderSolubilityParameter name="Chao-Seader solubility parameter"  units="J0.5/m1.5"  value="26610" />
-<ChaoSeaderLiquidVolume name="Chao-Seader liquid volume"  units="m3/kmol"  value="0.134763" />
-<UnifacVLE name="UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  <group id="15"  value="2" />
-  <group id="33"  value="1" />
-  </UnifacVLE>
-<Asog name="ASOG" >
-  <group id="1"  value="2" />
-  <group id="2"  value="2" />
-  <group id="3"  value="2" />
-  <group id="15"  value="2" />
-  <group id="30"  value="1" />
-  </Asog>
-<Umr name="UMR" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  <group id="15"  value="2" />
-  <group id="33"  value="1" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="1"  value="2" />
-  <group id="2"  value="1" />
-  <group id="3"  value="2" />
-  <group id="14"  value="2" />
-  <group id="32"  value="1" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="110-97-4" />
-<Smiles name="SMILES"  value="CC(O)CNCC(O)C" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="102" />
-<CompoundID name="Name"  value="Cyclobutane" />
-<StructureFormula name="Structure"  value="-(CH2)4-" />
-<Family name="Family"  value="5" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="459.93" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4980000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.21" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.273" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="285.66" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="182.48" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="182.48" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="180.101" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="56.1063" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0814243" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.18474" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.45E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16020" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="0" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04092" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="5.4E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="2.85E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="1.122E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="265400" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1088000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.5678E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="14.96111" />
-  <B value="0.0000555916" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="173" />
-  <Tmax units="K"  value="182.5" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.407691" />
-  <B value="0.295395" />
-  <C value="459.93" />
-  <D value="0.248729" />
-  <E value="0" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="459.93" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="60.70694" />
-  <B value="-4389.85" />
-  <C value="-6.086364" />
-  <D value="7.387074E-06" />
-  <E value="2" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="459.93" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="3.344974E+07" />
-  <B value="0.35995" />
-  <C value="-0.0547115" />
-  <D value="0.0583309" />
-  <E value="-0.0233634" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="459.93" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-24126" />
-  <B value="1646.5" />
-  <C value="-13.114" />
-  <D value="0.043967" />
-  <E value="0" />
-  <Tmin units="K"  value="25" />
-  <Tmax units="K"  value="120" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-3355.973" />
-  <B value="25.71519" />
-  <C value="11.14976" />
-  <D value="-0.0000199586" />
-  <E value="4.55626E-06" />
-  <Tmin units="K"  value="190" />
-  <Tmax units="K"  value="298.1501" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="37380.05" />
-  <B value="-673.6637" />
-  <C value="12.72112" />
-  <D value="-0.000063263" />
-  <E value="1.539025E-09" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.130037" />
-  <B value="-132.3643" />
-  <C value="-8.684027" />
-  <D value="-204.0061" />
-  <E value="215.6664" />
-  <Tmin units="K"  value="230" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="16" />
-  <A value="0.0000263799" />
-  <B value="486.4199" />
-  <C value="-9.034853" />
-  <D value="-0.00420404" />
-  <E value="4.708051E-07" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="367.9399" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="16" />
-  <A value="2.344771E-06" />
-  <B value="-353.1514" />
-  <C value="-11.15186" />
-  <D value="0.000996526" />
-  <E value="-0.0000002755" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="999.9998" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.0169674" />
-  <B value="14.7154" />
-  <C value="-1.831383" />
-  <D value="-0.000155026" />
-  <E value="-0.0000048849" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="285.6601" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.00541541" />
-  <B value="-765.5803" />
-  <C value="-2.581507" />
-  <D value="0.00174448" />
-  <E value="-3.307726E-07" />
-  <Tmin units="K"  value="285.66" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.00834272" />
-  <B value="113.8985" />
-  <C value="-4.119698" />
-  <D value="0.00522719" />
-  <E value="-0.00001579" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="459.93" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="37226.21" />
-  <B value="-77.82548" />
-  <C value="0.815135" />
-  <D value="-0.000593048" />
-  <E value="0" />
-  <Tmin units="K"  value="50" />
-  <Tmax units="K"  value="400" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.94339" />
-  <B value="3076.728" />
-  <C value="10.52672" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="204.95" />
-  <Tmax units="K"  value="433.15" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="10" />
-  <A value="-11.36515" />
-  <B value="-1019.814" />
-  <C value="55.89796" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="182.48" />
-  <Tmax units="K"  value="367.94" />
-  </LiquidViscosityRPS>
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0308894" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.698393" />
-<UnifacVLE name="UNIFAC" >
-  <group id="2"  value="4" />
-  </UnifacVLE>
-<UnifacLLE name="UNIFAC-LLE" >
-  <group id="2"  value="4" />
-  </UnifacLLE>
-<Asog name="ASOG" >
-  <group id="2"  value="4" />
-  </Asog>
-<GCmethod name="PPR78" >
-  <group id="2"  value="4" />
-  </GCmethod>
-<Umr name="UMR" >
-  <group id="2"  value="4" />
-  </Umr>
-<ModifiedUnifac name="Modified UNIFAC" >
-  <group id="78"  value="4" />
-  </ModifiedUnifac>
-<CAS name="CAS number"  value="287-23-0" />
-<Smiles name="SMILES"  value="C1CCC1" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1810" />
-<CompoundID name="Name"  value="Isopropyl mercaptan" />
-<StructureFormula name="Structure"  value="(CH3)2CHSH" />
-<Family name="Family"  value="41" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="517.3" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="4750000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.254" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.281" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="325.75" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="142.61" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="142.64" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00973089" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="76.1606" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0941865" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="0.21381" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="2.993E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="16970" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="5.47E-30" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.04893" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.1E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-7.59E+07" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-2180000" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="324300" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="5736000" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-2.3684E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="0" />
-  <B value="0" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="0" />
-  <Tmax units="K"  value="1" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="1.093001" />
-  <B value="0.27762" />
-  <C value="517" />
-  <D value="0.29781" />
-  <E value="0" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="497.2953" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="52.49398" />
-  <B value="-5018.813" />
-  <C value="-4.414151" />
-  <D value="1.969036E-13" />
-  <E value="2" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="517.0001" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="4.07186E+07" />
-  <B value="0.189905" />
-  <C value="0.420769" />
-  <D value="-0.0231137" />
-  <E value="-0.258009" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="517.0001" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-18220" />
-  <B value="1882.6" />
-  <C value="-19.293" />
-  <D value="0.0884" />
-  <E value="0" />
-  <Tmin units="K"  value="14.62" />
-  <Tmax units="K"  value="110.2699" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="-4182.09" />
-  <B value="11.57821" />
-  <C value="11.69322" />
-  <D value="0.0000133303" />
-  <E value="0.0000020152" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="350" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="68588.92" />
-  <B value="-673.2911" />
-  <C value="12.50044" />
-  <D value="1.486465E-06" />
-  <E value="-1.964897E-08" />
-  <Tmin units="K"  value="200" />
-  <Tmax units="K"  value="1500" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.153422" />
-  <B value="-199.5338" />
-  <C value="-18.99653" />
-  <D value="1144.562" />
-  <E value="-4039.504" />
-  <Tmin units="K"  value="257" />
-  <Tmax units="K"  value="1542" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="16" />
-  <A value="0.0000158085" />
-  <B value="630.9957" />
-  <C value="-8.670452" />
-  <D value="-0.006493" />
-  <E value="5.676279E-06" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="325.71" />
-  </LiquidViscosity>
-<VaporViscosity name="Vapour viscosity"  units="Pa.s" >
-  <eqno value="16" />
-  <A value="2.562672E-06" />
-  <B value="-300.3637" />
-  <C value="-11.49051" />
-  <D value="0.00155043" />
-  <E value="-4.080467E-07" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="1000" />
-  </VaporViscosity>
-<LiquidThermalConductivity name="Liquid thermal conductivity"  units="W/m/K" >
-  <eqno value="16" />
-  <A value="0.019346" />
-  <B value="8.361977" />
-  <C value="-1.76982" />
-  <D value="-0.000539416" />
-  <E value="-3.287583E-06" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="325.71" />
-  </LiquidThermalConductivity>
-<VaporThermalConductivity name="Vapour thermal conductivity"  units="W/m/K" >
-  <eqno value="102" />
-  <A value="0.00018367" />
-  <B value="0.9627" />
-  <C value="646.01" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="325.71" />
-  <Tmax units="K"  value="1000" />
-  </VaporThermalConductivity>
-<SurfaceTension name="Surface tension"  units="N/m" >
-  <eqno value="16" />
-  <A value="-0.0111776" />
-  <B value="26.63325" />
-  <C value="-3.053494" />
-  <D value="0.000331969" />
-  <E value="-0.0000062853" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="517.0001" />
-  </SurfaceTension>
-<RPPHeatCapacityCp name="Ideal gas heat capacity (RPP)"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="46207.41" />
-  <B value="65.01495" />
-  <C value="0.499267" />
-  <D value="-0.000522701" />
-  <E value="0" />
-  <Tmin units="K"  value="273.15" />
-  <Tmax units="K"  value="487.2" />
-  </RPPHeatCapacityCp>
-<AntoineVaporPressure name="Antoine"  units="Pa" >
-  <eqno value="10" />
-  <A value="21.08291" />
-  <B value="2786.592" />
-  <C value="-34.12406" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="168.7" />
-  <Tmax units="K"  value="457.97" />
-  </AntoineVaporPressure>
-<LiquidViscosityRPS name="Liquid viscosity (RPS)"  units="Pa.s" >
-  <eqno value="10" />
-  <A value="-10.66501" />
-  <B value="-828.3052" />
-  <C value="4.074317" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="142.61" />
-  <Tmax units="K"  value="323.15" />
-  </LiquidViscosityRPS>
-<Parachor name="Parachor"  units="kg0.25.m3/s0.5/kmol"  value="0.0360599" />
-<SpecificGravity name="Specific gravity"  units="_"  value="0.81887" />
-<UniquacR  name="UNIQUAC r"  units="_"  value="3.225445" />
-<UniquacQ  name="UNIQUAC q"  units="_"  value="2.84" />
-<GCmethod name="PPR78" >
-  <group id="1"  value="2" />
-  <group id="3"  value="1" />
-  <group id="15"  value="1" />
-  </GCmethod>
-<CAS name="CAS number"  value="75-33-2" />
-<Smiles name="SMILES"  value="CC(C)S" />
-</compound>
-
-<compound>
-<LibraryIndex name="Index"  value="1231" />
-<CompoundID name="Name"  value="Glycerol" />
-<StructureFormula name="Structure"  value="HOCH2CH(OH)CH2OH" />
-<Family name="Family"  value="49" />
-<CriticalTemperature name="Critical temperature"  units="K"  value="725.15" />
-<CriticalPressure name="Critical pressure"  units="Pa"  value="6660000" />
-<CriticalVolume name="Critical volume"  units="m3/kmol"  value="0.264" />
-<CriticalCompressibility name="Critical compressibility factor"  units="_"  value="0.28" />
-<NormalBoilingPointTemperature name="Normal boiling point"  units="K"  value="563.15" />
-<NormalMeltingPointTemperature name="Melting point"  units="K"  value="291.15" />
-<TriplePointTemperature name="Triple point temperature"  units="K"  value="291.33" />
-<TriplePointPressure name="Triple point pressure"  units="Pa"  value="0.00952225" />
-<MolecularWeight name="Molecular weight"  units="kg/kmol"  value="92.0938" />
-<LiquidVolumeAtNormalBoilingPoint name="Liquid molar volume at normal boiling point"  units="m3/kmol"  value="0.0732027" />
-<AcentricityFactor name="Acentric factor"  units="_"  value="1.544133" />
-<RadiusOfGyration name="Radius of gyration"  units="m"  value="3.52E-10" />
-<SolubilityParameter name="Solubility parameter"  units="J0.5/m1.5"  value="34540" />
-<DipoleMoment name="Dipole moment"  units="Coulomb.m"  value="1.4E-29" />
-<VanDerWaalsVolume name="Van der Waals volume"  units="m3/kmol"  value="0.05136" />
-<VanDerWaalsArea name="Van der Waals area"  units="m2/kmol"  value="7.65E+08" />
-<HeatOfFormation name="IG heat of formation"  units="J/kmol"  value="-5.828E+08" />
-<GibbsEnergyOfFormation name="IG Gibbs energy of formation"  units="J/kmol"  value="-4.471E+08" />
-<AbsEntropy name="IG absolute entropy"  units="J/kmol/K"  value="396000" />
-<HeatOfFusionAtMeltingPoint name="Heat of fusion at melting point"  units="J/kmol"  value="1.831E+07" />
-<HeatOfCombustion name="Standard net heat of combustion"  units="J/kmol"  value="-1.477E+09" />
-<SolidDensity name="Solid density"  units="kmol/m3" >
-  <eqno value="2" />
-  <A value="15.131" />
-  <B value="-0.002161" />
-  <C value="0" />
-  <D value="0" />
-  <E value="0" />
-  <Tmin units="K"  value="90.15" />
-  <Tmax units="K"  value="291.15" />
-  </SolidDensity>
-<LiquidDensity name="Liquid density"  units="kmol/m3" >
-  <eqno value="105" />
-  <A value="0.933664" />
-  <B value="0.246209" />
-  <C value="850" />
-  <D value="0.220672" />
-  <E value="0" />
-  <Tmin units="K"  value="291.33" />
-  <Tmax units="K"  value="850" />
-  </LiquidDensity>
-<VaporPressure name="Vapour pressure"  units="Pa" >
-  <eqno value="101" />
-  <A value="99.57469" />
-  <B value="-13673.87" />
-  <C value="-10.09699" />
-  <D value="1.227718E-11" />
-  <E value="2" />
-  <Tmin units="K"  value="291.33" />
-  <Tmax units="K"  value="850" />
-  </VaporPressure>
-<HeatOfVaporization name="Heat of vaporization"  units="J/kmol" >
-  <eqno value="106" />
-  <A value="1.1E+08" />
-  <B value="1" />
-  <C value="-2.5" />
-  <D value="3.4" />
-  <E value="-1.65" />
-  <Tmin units="K"  value="291.33" />
-  <Tmax units="K"  value="765" />
-  </HeatOfVaporization>
-<SolidHeatCapacityCp name="Solid heat capacity"  units="J/kmol/K" >
-  <eqno value="4" />
-  <A value="-14764.07" />
-  <B value="1034.972" />
-  <C value="-4.074509" />
-  <D value="0.00802715" />
-  <E value="0" />
-  <Tmin units="K"  value="25.25" />
-  <Tmax units="K"  value="273.15" />
-  </SolidHeatCapacityCp>
-<LiquidHeatCapacityCp name="Liquid heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="115.6361" />
-  <B value="-33.33621" />
-  <C value="11.80006" />
-  <D value="0.00238285" />
-  <E value="-0.0000010098" />
-  <Tmin units="K"  value="187.4" />
-  <Tmax units="K"  value="560.9999" />
-  </LiquidHeatCapacityCp>
-<IdealGasHeatCapacityCp name="Ideal gas heat capacity"  units="J/kmol/K" >
-  <eqno value="16" />
-  <A value="31366.31" />
-  <B value="-311.2541" />
-  <C value="12.31511" />
-  <D value="0.000195602" />
-  <E value="1.752076E-09" />
-  <Tmin units="K"  value="273" />
-  <Tmax units="K"  value="1200.15" />
-  </IdealGasHeatCapacityCp>
-<SecondVirialCoefficient name="Second virial coefficient"  units="m3/kmol" >
-  <eqno value="104" />
-  <A value="0.151103" />
-  <B value="-224.6228" />
-  <C value="-138.7965" />
-  <D value="-370017.6" />
-  <E value="689661.3" />
-  <Tmin units="K"  value="425" />
-  <Tmax units="K"  value="1500" />
-  </SecondVirialCoefficient>
-<LiquidViscosity name="Liquid viscosity"  units="Pa.s" >
-  <eqno value="10" />
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-	border-style: inset;
-	border-color: rgb(150,150,150);
-	background-color:rgb(221,221,219);
-}
-QProgressBar::chunk:horizontal {
-	background-color: qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(225, 108, 54, 255), stop:1 rgba(246, 134, 86, 255));
-	border-style: solid;
-	border-radius:8px;
-	border-width:1px;
-	border-bottom-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(175,85,48,255), stop:1 rgba(236,114,67, 255));
-	border-top-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-	border-right-color:qlineargradient(spread:pad, x1:0, y1:0.5, x2:1, y2:0.5, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-	border-left-color:qlineargradient(spread:pad, x1:1, y1:0.5, x2:0, y2:0.5, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-}
-QTabWidget {
-	color:rgb(0,0,0);
-	background-color:rgb(247,246,246);
-}
-QTabWidget::pane {
-	border-color: rgb(180,180,180);
-	background-color:rgb(247,246,246);
-	border-style: solid;
-	border-width: 1px;
-  	border-radius: 6px;
-}
-QTabBar::tab {
-	padding-left:4px;
-	padding-right:4px;
-	padding-bottom:2px;
-	padding-top:2px;
-	color:rgb(81,72,65);
-  	background-color: qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(221,218,217,255), stop:1 rgba(240,239,238,255));
-	border-style: solid;
-	border-width: 1px;
-  	border-top-right-radius:4px;
-	border-top-left-radius:4px;
-	border-top-color: rgb(180,180,180);
-	border-left-color: rgb(180,180,180);
-	border-right-color: rgb(180,180,180);
-	border-bottom-color: transparent;
-}
-QTabBar::tab:selected, QTabBar::tab:last:selected, QTabBar::tab:hover {
-  	background-color:rgb(247,246,246);
-  	margin-left: 0px;
-  	margin-right: 1px;
-}
-QTabBar::tab:!selected {
-	margin-top: 1px;
-	margin-right: 1px;
-}
-QMenuBar {
-	color:rgb(223,219,210);
-	background-color:rgb(0,90,90);
-}
-QMenuBar::item {
-	padding-top:4px;
-	padding-left:4px;
-	padding-right:4px;
-	color:rgb(223,219,210);
-	background-color:rgb(0,90,90);
-}
-QMenuBar::item:selected {
-	color:rgb(255,255,255);
-	padding-top:2px;
-	padding-left:2px;
-	padding-right:2px;
-	border-top-width:2px;
-	border-left-width:2px;
-	border-right-width:2px;
-	border-top-right-radius:4px;
-	border-top-left-radius:4px;
-	border-style:solid;
-	background-color:rgb(0,207,207);
-	border-top-color: rgb(0, 129, 129);
-	border-right-color: qlineargradient(spread:pad, x1:0, y1:1, x2:1, y2:0, stop:0 rgba(0, 188, 188, 255), stop:1 rgba(0, 129, 129, 255));
-	border-left-color:  qlineargradient(spread:pad, x1:1, y1:0, x2:0, y2:0, stop:0 rgba(0, 188, 188, 255), stop:1 rgba(0, 129, 129, 255));
-}
-QMenu::item:selected {
-	color:rgb(255,255,255);
-	background-color: qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(0, 109, 109, 255), stop:1 rgba(0, 168, 168, 255));
-	border-style:solid;
-	border-width:3px;
-	padding-left:17px;
-	padding-top:4px;
-	padding-bottom:4px;
-	padding-right:7px;
-	border-bottom-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(175,85,48,255), stop:1 rgba(236,114,67, 255));
-	border-top-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-	border-right-color:qlineargradient(spread:pad, x1:0, y1:0.5, x2:1, y2:0.5, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-	border-left-color:qlineargradient(spread:pad, x1:1, y1:0.5, x2:0, y2:0.5, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-}
-QMenu::item {
-	color:rgb(223,219,210);
-	padding-left:20px;
-	padding-top:4px;
-	padding-bottom:4px;
-	padding-right:10px;
-}
-QMenu {
-	color:rgb(223,219,210);
-	background-color:rgb(65,64,59);
-}
-QCheckBox {
-	padding:2px;
-}
-QCheckBox:hover {
-	border-radius:4px;
-	border-style:solid;
-	border-width:1px;
-	padding-left: 1px;
-	padding-right: 1px;
-	padding-bottom: 1px;
-	padding-top: 1px;
-	border-color: rgb(0,148,148);
-	background-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(0, 109, 109, 50), stop:1 rgba(0, 207, 207, 50));
-}
-QCheckBox::indicator:checked {
-	border-radius:4px;
-	border-style:solid;
-	border-width:1px;
-	border-color: rgb(246, 134, 86);
-  	background-color:rgb(246, 134, 86)
-}
-QCheckBox::indicator:unchecked {
-	border-radius:4px;
-	border-style:solid;
-	border-width:1px;
-	border-color:rgb(246, 134, 86);
-  	background-color:rgb(255,255,255);
-}
-QRadioButton {
-	padding: 1px;
-}
-QRadioButton::indicator:checked {
-	height: 10px;
-	width: 10px;
-	border-style:solid;
-	border-radius:5px;
-	border-width: 1px;
-	border-color: rgba(246, 134, 86, 255);
-	color: #a9b7c6;
-	background-color:rgba(246, 134, 86, 255);
-}
-QRadioButton::indicator:!checked {
-	height: 10px;
-	width: 10px;
-	border-style:solid;
-	border-radius:5px;
-	border-width: 1px;
-	border-color: rgb(246, 134, 86);
-	color: #a9b7c6;
-	background-color: transparent;
-}
-QStatusBar {
-	color:rgb(81,72,65);
-}
-QSpinBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QDoubleSpinBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QTimeEdit {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QDateTimeEdit {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QDateEdit {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QComboBox {
-	color:rgb(81,72,65);
-	background: #ffffff;
-}
-QComboBox:editable {
-	background: #ffffff;
-	color: rgb(81,72,65);
-	selection-color:rgb(81,72,65);
-	selection-background-color: #ffffff;
-}
-QComboBox QAbstractItemView {
-	color:rgb(81,72,65);
-	background: #ffffff;
-	selection-color: #ffffff;
-	selection-background-color: rgb(0, 207, 207);
-}
-QComboBox:!editable:on, QComboBox::drop-down:editable:on {
-	color:  #1e1d23;
-	background: #ffffff;
-}
-QFontComboBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QToolBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QToolBox::tab {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QToolBox::tab:selected {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QScrollArea {
-	color: #FFFFFF;
-	background-color:#f0f0f0;
-}
-QSlider::groove {
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-}
-QSlider::groove:horizontal {
-	height: 5px;
-	background: rgb(246, 134, 86);
-}
-QSlider::groove:vertical {
-	width: 5px;
-	background: rgb(246, 134, 86);
-}
-QSlider::handle:horizontal {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	width: 12px;
-	margin: -5px 0;
-	border-radius: 7px;
-}
-QSlider::handle:vertical {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	height: 12px;
-	margin: 0 -5px;
-	border-radius: 7px;
-}
-QSlider::add-page:horizontal {
- 	background: white;
-}
-QSlider::add-page:vertical {
-	background: white;
-}
-QSlider::sub-page:horizontal {
-	background: rgb(246, 134, 86);
-}
-QSlider::sub-page:vertical {
-  	background: rgb(246, 134, 86);
-}
-QScrollBar:horizontal {
-	max-height: 20px;
-	border: 1px transparent grey;
-	margin: 0px 20px 0px 20px;
-}
-QScrollBar::handle:horizontal {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	border-radius: 7px;
-	min-width: 25px;
-}
-QScrollBar::handle:horizontal:hover {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(0,207,207);
-	border-radius: 7px;
-	min-width: 25px;
-}
-QScrollBar::add-line:horizontal {
-  	border: 1px solid;
-  	border-color: rgb(207, 207, 207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: right;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:horizontal:hover {
-  	border: 1px solid;
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	border-color: rgb(0, 207, 207);
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: right;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:horizontal:pressed {
-  	border: 1px solid grey;
-  	border-top-left-radius: 7px;
-  	border-top-right-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	background: rgb(231,231,231);
-  	width: 20px;
-  	subcontrol-position: right;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:horizontal {
-  	border: 1px solid;
-  	border-color: rgb(207,207,207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: left;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:horizontal:hover {
-  	border: 1px solid;
-  	border-color: rgb(0, 207, 207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: left;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:horizontal:pressed {
-  	border: 1px solid grey;
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(231,231,231);
-  	width: 20px;
-  	subcontrol-position: left;
-  	subcontrol-origin: margin;
-}
-QScrollBar::left-arrow:horizontal {
-  	border: 1px transparent grey;
-  	border-top-left-radius: 3px;
-  	border-bottom-left-radius: 3px;
-  	width: 6px;
-  	height: 6px;
-  	background: rgb(0,188,188);
-}
-QScrollBar::right-arrow:horizontal {
-	border: 1px transparent grey;
-	border-top-right-radius: 3px;
-
-	border-bottom-right-radius: 3px;
-  	width: 6px;
-  	height: 6px;
- 	background: rgb(0,188,188);
-}
-QScrollBar::add-page:horizontal, QScrollBar::sub-page:horizontal {
- 	background: none;
-}
-QScrollBar:vertical {
-	max-width: 20px;
-	border: 1px transparent grey;
-	margin: 20px 0px 20px 0px;
-}
-QScrollBar::add-line:vertical {
-	border: 1px solid;
-	border-color: rgb(207,207,207);
-	border-bottom-right-radius: 7px;
-	border-bottom-left-radius: 7px;
-	border-top-left-radius: 7px;
-	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: bottom;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:vertical:hover {
-  	border: 1px solid;
-  	border-color: rgb(0, 207, 207);
-  	border-bottom-right-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	border-top-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: bottom;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:vertical:pressed {
-  	border: 1px solid grey;
-  	border-bottom-left-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	background: rgb(231,231,231);
-  	height: 20px;
-  	subcontrol-position: bottom;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:vertical {
-  	border: 1px solid;
-  	border-color: rgb(207,207,207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: top;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:vertical:hover {
-  	border: 1px solid;
-  	border-color: rgb(0, 207, 207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: top;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:vertical:pressed {
-  	border: 1px solid grey;
-  	border-top-left-radius: 7px;
-  	border-top-right-radius: 7px;
-  	background: rgb(231,231,231);
- 	height: 20px;
-  	subcontrol-position: top;
-  	subcontrol-origin: margin;
-}
-	QScrollBar::handle:vertical {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	border-radius: 7px;
-	min-height: 25px;
-}
-QScrollBar::handle:vertical:hover {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(0,207,207);
-	border-radius: 7px;
-	min-height: 25px;
-}
-QScrollBar::up-arrow:vertical {
-	border: 1px transparent grey;
-  	border-top-left-radius: 3px;
-	border-top-right-radius: 3px;
-  	width: 6px;
-  	height: 6px;
-  	background: rgb(0,188,188);
-}
-QScrollBar::down-arrow:vertical {
-  	border: 1px transparent grey;
-  	border-bottom-left-radius: 3px;
-  	border-bottom-right-radius: 3px;
-  	width: 6px;
-  	height: 6px;
-  	background: rgb(0,188,188);
-}
-QScrollBar::add-page:vertical, QScrollBar::sub-page:vertical {
-  	background: none;
-}
-QToolTip
-{
-     border: 1px solid black;
-     background-color: rgb(0, 207, 207);
-     padding: 1px;
-     border-radius: 3px;
-     opacity: 100;
-}
-QTableView
-{
-    border: 1px solid #76797C;
-    gridline-color: #004646;
-    background-color: #f0f0f0;
-}
-QTableView, QHeaderView
-{
-    border-radius: 0px;
-}
-QTableView::item:pressed, QListView::item:pressed, QTreeView::item:pressed  {
-    background: rgb(150, 255, 255);
-    color: black;
-}
-QTableView::item:selected:active, QTreeView::item:selected:active, QListView::item:selected:active  {
-    background: rgb(150, 255, 255);
-    color: black;
-}
-QHeaderView
-{
-    background-color: #f0f0f0;
-    border: 1px transparent;
-    border-radius: 0px;
-    margin: 0px;
-    padding: 0px;
-
-}
-QHeaderView::section {
-	padding:3px;
-	margin:0px;
-	color:#f0f0f0;
-	border: 1px solid #004646;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 rgb(0, 148, 148), stop:1 rgb(0, 148, 148));
-}
-QHeaderView::section::vertical::first, QHeaderView::section::vertical::only-one
-{
-    border-top: 1px rgb(150, 247, 247);
-}
-QHeaderView::section::vertical
-{
-    border-top: transparent;
-}
-QHeaderView::section::horizontal::first, QHeaderView::section::horizontal::only-one
-{
-    border-left: 1px rgb(150, 247, 247);
-}
-QHeaderView::section::horizontal
-{
-    border-left: transparent;
-}
-QHeaderView::section:checked
-{
-    color: white;
-    background-color:rgb(150, 247, 247);
-}
-QLabel {
-    background-color: #f0f0f0;
-    border: 0px solid #32414B;
-    padding: 2px;
-    margin: 0px;
-    color: rgb(17, 17, 17);
-}
-QLabel::disabled {
-    background-color: #f0f0f0;
-    border: 0px solid #32414B;
-    color: rgb(17, 17, 17);
-}
-QDockWidget.QWidget.QScrollArea.QWidget.QLabel{
-    color : red;
-}
-QFrame {
-    border-radius: 4px;
-    border: 1px solid #32414B;
-}
-QFrame[frameShape="0"] {
-    border-radius: 4px;
-    border: 1px transparent #32414B;
-}
-QFrame[height="3"],
-QFrame[width="3"] {
-    background-color: #19232D;
-}
-
diff --git a/darkgray.css b/darkgray.css
deleted file mode 100644
index 69e4eef..0000000
--- a/darkgray.css
+++ /dev/null
@@ -1,1281 +0,0 @@
-
-QToolTip
-{
-     border: 1px solid black;
-     background-color: #D1DBCB;
-     padding: 1px;
-     border-radius: 3px;
-     opacity: 100;
-}
-
-QWidget
-{
-    color: #b1b1b1;
-    background-color: #323232;
-    selection-background-color:#323232;
-    selection-color: black;
-    background-clip: border;
-    border-image: none;
-    border: 0px transparent black;
-    outline: 0;
-}
-
-QWidget:item:hover
-{
-    background-color: #D1DBCB;
-    color: black;
-}
-
-QWidget:item:selected
-{
-    background-color: #D1DBCB;
-    border: 0px
-}
-
-QCheckBox
-{
-    spacing: 5px;
-    outline: none;
-    color: #eff0f1;
-    margin-bottom: 2px;
-}
-
-QCheckBox:disabled
-{
-    color: #76797C;
-}
-
-QCheckBox::indicator,QGroupBox::indicator
-{
-    width: 18px;
-    height: 18px;
-}
-
-QGroupBox::indicator
-{
-    margin-left: 2px;
-}
-
-QCheckBox::indicator:unchecked
-{
-    image: url(:/qss_icons/rc/checkbox_unchecked.png);
-}
-
-QCheckBox::indicator:unchecked:hover,
-QCheckBox::indicator:unchecked:focus,
-QCheckBox::indicator:unchecked:pressed,
-QGroupBox::indicator:unchecked:hover,
-QGroupBox::indicator:unchecked:focus,
-QGroupBox::indicator:unchecked:pressed
-{
-  border: none;
-    image: url(:/qss_icons/rc/checkbox_unchecked_focus.png);
-}
-
-QCheckBox::indicator:checked
-{
-    image: url(:/qss_icons/rc/checkbox_checked.png);
-}
-
-QCheckBox::indicator:checked:hover,
-QCheckBox::indicator:checked:focus,
-QCheckBox::indicator:checked:pressed,
-QGroupBox::indicator:checked:hover,
-QGroupBox::indicator:checked:focus,
-QGroupBox::indicator:checked:pressed
-{
-    border: none;
-    image: url(:/qss_icons/rc/checkbox_checked_focus.png);
-}
-
-
-QCheckBox::indicator:indeterminate
-{
-    image: url(:/qss_icons/rc/checkbox_indeterminate.png);
-}
-
-QCheckBox::indicator:indeterminate:focus,
-QCheckBox::indicator:indeterminate:hover,
-QCheckBox::indicator:indeterminate:pressed
-{
-    image: url(:/qss_icons/rc/checkbox_indeterminate_focus.png);
-}
-
-QCheckBox::indicator:checked:disabled,
-QGroupBox::indicator:checked:disabled
-{
-    image: url(:/qss_icons/rc/checkbox_checked_disabled.png);
-}
-
-QCheckBox::indicator:unchecked:disabled,
-QGroupBox::indicator:unchecked:disabled
-{
-    image: url(:/qss_icons/rc/checkbox_unchecked_disabled.png);
-}
-
-QRadioButton
-{
-    spacing: 5px;
-    outline: none;
-    color: #eff0f1;
-    margin-bottom: 2px;
-}
-
-QRadioButton:disabled
-{
-    color: #76797C;
-}
-QRadioButton::indicator
-{
-    width: 21px;
-    height: 21px;
-}
-
-QRadioButton::indicator:unchecked
-{
-    image: url(:/qss_icons/rc/radio_unchecked.png);
-}
-
-
-QRadioButton::indicator:unchecked:hover,
-QRadioButton::indicator:unchecked:focus,
-QRadioButton::indicator:unchecked:pressed
-{
-    border: none;
-    outline: none;
-    image: url(:/qss_icons/rc/radio_unchecked_focus.png);
-}
-
-QRadioButton::indicator:checked
-{
-    border: none;
-    outline: none;
-    image: url(:/qss_icons/rc/radio_checked.png);
-}
-
-QRadioButton::indicator:checked:hover,
-QRadioButton::indicator:checked:focus,
-QRadioButton::indicator:checked:pressed
-{
-    border: none;
-    outline: none;
-    image: url(:/qss_icons/rc/radio_checked_focus.png);
-}
-
-QRadioButton::indicator:checked:disabled
-{
-    outline: none;
-    image: url(:/qss_icons/rc/radio_checked_disabled.png);
-}
-
-QRadioButton::indicator:unchecked:disabled
-{
-    image: url(:/qss_icons/rc/radio_unchecked_disabled.png);
-}
-
-
-QMenuBar
-{
-    background-color: #323232;
-    color: #D1DBCB;
-}
-
-QMenuBar::item
-{
-    background-color: #323232;
-    background: transparent;
-    /* padding: 2px 20px 2px 20px; */
-}
-
-QMenuBar::item:selected
-{
-    background: transparent;
-    /* border: 1px solid #76797C; */
-}
-
-QMenuBar::item:pressed
-{
-    border: 0px solid #76797C;
-    background-color: #D1DBCB;
-    color: #000;
-    margin-bottom:-1px;
-    padding-bottom:1px;
-}
-
-QMenu
-{
-    background-color: #323232;
-    /* border: 1px solid #76797C; */
-    color: #eff0f1;
-    /*margin: 2px; */
-}
-
-QMenu::icon
-{
-    /*margin: 5px;*/
-}
-
-QMenu::item
-{
-    padding: 2px 30px 2px 30px;
-    /*margin-left: 5px;*/
-    border: 1px solid transparent; /* reserve space for selection border */
-}
-
-QMenu::item:selected
-{
-    color: #000000;
-}
-
-QMenu::separator {
-    height: 2px;
-    background: #D1DBCB;
-    margin-left: 10px;
-    margin-right: 5px;
-}
-
-QMenu::indicator {
-    width: 18px;
-    height: 18px;
-}
-
-/* non-exclusive indicator = check box style indicator
-   (see QActionGroup::setExclusive) */
-QMenu::indicator:non-exclusive:unchecked {
-    image: url(:/qss_icons/rc/checkbox_unchecked.png);
-}
-
-QMenu::indicator:non-exclusive:unchecked:selected {
-    image: url(:/qss_icons/rc/checkbox_unchecked_disabled.png);
-}
-
-QMenu::indicator:non-exclusive:checked {
-    image: url(:/qss_icons/rc/checkbox_checked.png);
-}
-
-QMenu::indicator:non-exclusive:checked:selected {
-    image: url(:/qss_icons/rc/checkbox_checked_disabled.png);
-}
-
-/* exclusive indicator = radio button style indicator (see QActionGroup::setExclusive) */
-QMenu::indicator:exclusive:unchecked {
-    image: url(:/qss_icons/rc/radio_unchecked.png);
-}
-
-QMenu::indicator:exclusive:unchecked:selected {
-    image: url(:/qss_icons/rc/radio_unchecked_disabled.png);
-}
-
-QMenu::indicator:exclusive:checked {
-    image: url(:/qss_icons/rc/radio_checked.png);
-}
-
-QMenu::indicator:exclusive:checked:selected {
-    image: url(:/qss_icons/rc/radio_checked_disabled.png);
-}
-
-QMenu::right-arrow {
-    margin: 5px;
-    image: url(:/qss_icons/rc/right_arrow.png)
-}
-
-
-QWidget:disabled
-{
-    color: #454545;
-    background-color: #323232;
-}
-
-QAbstractItemView
-{
-    alternate-background-color: #323232;
-    color: #eff0f1;
-    border: 1px solid 3A3939;
-    border-radius: 2px;
-}
-
-QWidget:focus, QMenuBar:focus,QToolBar:focus,QScrollAreaViewer:focus
-{
-    /* border: 2px solid #D1DBCB; */
-}
-
-QTabWidget:focus, QCheckBox:focus, QRadioButton:focus, QSlider:focus
-{
-    border: none;
-}
-
-QLineEdit
-{
-    background-color: #1e1e1e;
-    selection-background-color: #D1DBCB;
-    selection-color: black;
-    padding: 5px;
-    border-style: solid;
-    border: 1px solid #76797C;
-    border-radius: 2px;
-    color: #eff0f1;
-}
-
-QGroupBox {
-    border:1px solid #76797C;
-    border-radius: 2px;
-    margin-top: 20px;
-}
-
-QGroupBox::title {
-    subcontrol-origin: margin;
-    subcontrol-position: top center;
-    padding-left: 10px;
-    padding-right: 10px;
-    padding-top: 10px;
-}
-
-QAbstractScrollArea
-{
-    border-radius: 0px;
-    border: 0px solid #76797C;
-    background-color: transparent;
-}
-
-QScrollBar:horizontal
-{
-    height: 15px;
-    margin: 3px 15px 3px 15px;
-    border: 1px transparent #2A2929;
-    border-radius: 4px;
-    background-color: #2A2929;
-}
-
-QScrollBar::handle:horizontal
-{
-    background-color: #605F5F;
-    min-width: 5px;
-    border-radius: 4px;
-}
-
-QScrollBar::add-line:horizontal
-{
-    margin: 0px 3px 0px 3px;
-    border-image: url(:/qss_icons/rc/right_arrow_disabled.png);
-    width: 10px;
-    height: 10px;
-    subcontrol-position: right;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::sub-line:horizontal
-{
-    margin: 0px 3px 0px 3px;
-    border-image: url(:/qss_icons/rc/left_arrow_disabled.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: left;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::add-line:horizontal:hover,QScrollBar::add-line:horizontal:on
-{
-    border-image: url(:/qss_icons/rc/right_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: right;
-    subcontrol-origin: margin;
-}
-
-
-QScrollBar::sub-line:horizontal:hover, QScrollBar::sub-line:horizontal:on
-{
-    border-image: url(:/qss_icons/rc/left_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: left;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::up-arrow:horizontal, QScrollBar::down-arrow:horizontal
-{
-    background: none;
-}
-
-
-QScrollBar::add-page:horizontal, QScrollBar::sub-page:horizontal
-{
-    background: none;
-}
-
-QScrollBar:vertical
-{
-    background-color: #2A2929;
-    width: 15px;
-    margin: 15px 3px 15px 3px;
-    border: 1px transparent #2A2929;
-    border-radius: 4px;
-}
-
-QScrollBar::handle:vertical
-{
-    background-color: #605F5F;
-    min-height: 5px;
-    border-radius: 4px;
-}
-
-QScrollBar::sub-line:vertical
-{
-    margin: 3px 0px 3px 0px;
-    border-image: url(:/qss_icons/rc/up_arrow_disabled.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: top;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::add-line:vertical
-{
-    margin: 3px 0px 3px 0px;
-    border-image: url(:/qss_icons/rc/down_arrow_disabled.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: bottom;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::sub-line:vertical:hover,QScrollBar::sub-line:vertical:on
-{
-
-    border-image: url(:/qss_icons/rc/up_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: top;
-    subcontrol-origin: margin;
-}
-
-
-QScrollBar::add-line:vertical:hover, QScrollBar::add-line:vertical:on
-{
-    border-image: url(:/qss_icons/rc/down_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: bottom;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::up-arrow:vertical, QScrollBar::down-arrow:vertical
-{
-    background: none;
-}
-
-
-QScrollBar::add-page:vertical, QScrollBar::sub-page:vertical
-{
-    background: none;
-}
-
-QTextEdit
-{
-    background-color: #1e1e1e;
-    color: #eff0f1;
-    border: 1px solid #76797C;
-}
-
-QPlainTextEdit
-{
-    background-color: #1e1e1e;;
-    color: #eff0f1;
-    border-radius: 2px;
-    border: 1px solid #76797C;
-}
-
-QHeaderView::section
-{
-    background-color: #76797C;
-    color: #eff0f1;
-    padding: 5px;
-    border: 1px solid #76797C;
-}
-
-QSizeGrip {
-    image: url(:/qss_icons/rc/sizegrip.png);
-    width: 12px;
-    height: 12px;
-}
-
-
-QMainWindow::separator
-{
-    background-color: #323232;
-    color: white;
-    padding-left: 4px;
-    spacing: 2px;
-    border: 1px dashed #76797C;
-}
-
-QMainWindow::separator:hover
-{
-
-    background-color: #787876;
-    color: white;
-    padding-left: 4px;
-    border: 1px solid #76797C;
-    spacing: 2px;
-}
-
-
-QMenu::separator
-{
-    height: 1px;
-    background-color: #76797C;
-    color: white;
-    padding-left: 4px;
-    margin-left: 10px;
-    margin-right: 5px;
-}
-
-QFrame
-{
-    border-radius: 0px;
-    /*border: 1px solid #76797C;*/
-}
-
-
-QFrame[frameShape="0"]
-{
-    border-radius: 0px;
-    border: 0px transparent #76797C;
-}
-
-QStackedWidget
-{
-    border: 1px transparent black;
-}
-
-QToolBar {
-    border: 0px transparent #393838;
-    background: 0px solid #323232;
-    font-weight: bold;
-}
-
-QToolBar::handle:horizontal {
-    image: url(:/qss_icons/rc/Hmovetoolbar.png);
-}
-QToolBar::handle:vertical {
-    image: url(:/qss_icons/rc/Vmovetoolbar.png);
-}
-QToolBar::separator:horizontal {
-    image: url(:/qss_icons/rc/Hsepartoolbar.png);
-}
-QToolBar::separator:vertical {
-    image: url(:/qss_icons/rc/Vsepartoolbar.png);
-}
-QToolButton#qt_toolbar_ext_button {
-    background: #58595a
-}
-
-QPushButton
-{
-    color: #eff0f1;
-    background-color: #323232;
-    border-width: 1px;
-    border-color: #76797C;
-    border-style: solid;
-    padding: 5px;
-    border-radius: 0px;
-    outline: none;
-}
-
-QPushButton:disabled
-{
-    background-color: #323232;
-    border-width: 1px;
-    border-color: #454545;
-    border-style: solid;
-    padding-top: 5px;
-    padding-bottom: 5px;
-    padding-left: 10px;
-    padding-right: 10px;
-    border-radius: 2px;
-    color: #454545;
-}
-
-QPushButton:focus {
-    background-color: #D1DBCB;
-    color: black;
-}
-
-QPushButton:pressed
-{
-    color: black;
-    background-color: #D1DBCB;
-    padding-top: -15px;
-    padding-bottom: -17px;
-}
-
-QComboBox
-{
-    selection-background-color: #D1DBCB;
-    background-color: #31363B;
-    border-style: solid;
-    border: 1px solid #76797C;
-    border-radius: 2px;
-    padding: 5px;
-    min-width: 75px;
-}
-
-QPushButton:checked{
-    background-color: #76797C;
-    border-color: #6A6969;
-}
-
-QComboBox:hover,QPushButton:hover,QAbstractSpinBox:hover,QLineEdit:hover,QTextEdit:hover,QPlainTextEdit:hover,QAbstractView:hover,QTreeView:hover
-{
-    border: 1px solid #D1DBCB;
-}
-
-QComboBox:on
-{
-    padding-top: 0px;
-    padding-left: 4px;
-    selection-background-color: #4a4a4a;
-}
-
-QComboBox QAbstractItemView
-{
-    background-color: #1e1e1e;
-    border-radius: 2px;
-    border: 1px solid #76797C;
-    selection-background-color: #D1DBCB;
-}
-
-QComboBox::drop-down
-{
-    subcontrol-origin: padding;
-    subcontrol-position: top right;
-    width: 15px;
-
-    border-left-width: 0px;
-    border-left-color: darkgray;
-    border-left-style: solid;
-    border-top-right-radius: 3px;
-    border-bottom-right-radius: 3px;
-}
-
-QComboBox::down-arrow
-{
-    image: url(:/qss_icons/rc/down_arrow_disabled.png);
-}
-
-QComboBox::down-arrow:on, QComboBox::down-arrow:hover,
-QComboBox::down-arrow:focus
-{
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-QAbstractSpinBox {
-    padding: 2px;
-    margin: 2px;
-    background-color: #1e1e1e;
-    color: #eff0f1;
-    border-radius: 0px;
-    min-width: 75px;
-    selection-background-color: #D1DBCB;
-    selection-color: black;
-}
-
-QAbstractSpinBox:up-button
-{
-    background-color: transparent;
-    subcontrol-origin: border;
-    subcontrol-position: center right;
-}
-
-QAbstractSpinBox:down-button
-{
-    background-color: transparent;
-    subcontrol-origin: border;
-    subcontrol-position: center left;
-}
-
-QAbstractSpinBox::up-arrow,QAbstractSpinBox::up-arrow:disabled,QAbstractSpinBox::up-arrow:off {
-    image: url(:/qss_icons/rc/up_arrow_disabled.png);
-    width: 10px;
-    height: 10px;
-}
-QAbstractSpinBox::up-arrow:hover
-{
-    image: url(:/qss_icons/rc/up_arrow.png);
-}
-
-
-QAbstractSpinBox::down-arrow,QAbstractSpinBox::down-arrow:disabled,QAbstractSpinBox::down-arrow:off
-{
-    image: url(:/qss_icons/rc/down_arrow_disabled.png);
-    width: 10px;
-    height: 10px;
-}
-QAbstractSpinBox::down-arrow:hover
-{
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-
-QLabel
-{
-    border: 0px solid black;
-    margin-left: 2px;
-    margin-right: 2px;
-    color: #D1DBCB;
-}
-
-QTabWidget{
-    border: 0px transparent black;
-}
-
-QTabWidget::pane {
-    border: 1px solid #76797C;
-    padding: 5px;
-    margin: 0px;
-}
-
-QTabWidget::tab-bar {
-    left: 5px; /* move to the right by 5px */
-}
-
-QTabBar
-{
-    qproperty-drawBase: 0;
-    border-radius: 3px;
-}
-
-QTabBar::focus
-{
-    border: 0px transparent black;
-    color: black;
-}
-
-QTabBar::hover
-{
-    border: 0px transparent black;
-    color: black;
-}
-
-QTabBar::close-button  {
-    image: url(:/qss_icons/rc/close.png);
-    background: transparent;
-}
-
-QTabBar::close-button:hover
-{
-    image: url(:/qss_icons/rc/close-hover.png);
-    background: transparent;
-}
-
-QTabBar::close-button:pressed {
-    image: url(:/qss_icons/rc/close-pressed.png);
-    background: transparent;
-}
-
-/* TOP TABS */
-QTabBar::tab:top {
-    color: #eff0f1;
-    border: 1px solid #76797C;
-    border-bottom: 1px transparent black;
-    background-color: #323232;
-    padding: 5px;
-    min-width: 50px;
-    border-top-left-radius: 2px;
-    border-top-right-radius: 2px;
-}
-
-QTabBar::tab:top:!selected
-{
-    color: #eff0f1;
-    background-color: #54575B;
-    border: 1px solid #76797C;
-    border-bottom: 1px transparent black;
-    border-top-left-radius: 2px;
-    border-top-right-radius: 2px;
-}
-
-QTabBar::tab:top:!selected:hover {
-    background-color: #D1DBCB;
-    color: black;
-}
-
-/* BOTTOM TABS */
-QTabBar::tab:bottom {
-    color: #eff0f1;
-    border: 1px solid #76797C;
-    border-top: 1px transparent black;
-    background-color: #323232;
-    padding: 5px;
-    border-bottom-left-radius: 2px;
-    border-bottom-right-radius: 2px;
-    min-width: 50px;
-}
-
-QTabBar::tab:bottom:!selected
-{
-    color: #eff0f1;
-    background-color: #54575B;
-    border: 1px solid #76797C;
-    border-top: 1px transparent black;
-    border-bottom-left-radius: 2px;
-    border-bottom-right-radius: 2px;
-}
-
-QTabBar::tab:bottom:!selected:hover {
-    background-color: #D1DBCB;
-    color: black;
-}
-
-/* LEFT TABS */
-QTabBar::tab:left {
-    color: #eff0f1;
-    border: 1px solid #76797C;
-    border-left: 1px transparent black;
-    background-color: #323232;
-    padding: 5px;
-    border-top-right-radius: 2px;
-    border-bottom-right-radius: 2px;
-    min-height: 50px;
-}
-
-QTabBar::tab:left:!selected
-{
-    color: #eff0f1;
-    background-color: #54575B;
-    border: 1px solid #76797C;
-    border-left: 1px transparent black;
-    border-top-right-radius: 2px;
-    border-bottom-right-radius: 2px;
-}
-
-QTabBar::tab:left:!selected:hover {
-    background-color: #D1DBCB;
-    color: black;
-}
-
-
-/* RIGHT TABS */
-QTabBar::tab:right {
-    color: #eff0f1;
-    border: 1px solid #76797C;
-    border-right: 1px transparent black;
-    background-color: #323232;
-    padding: 5px;
-    border-top-left-radius: 2px;
-    border-bottom-left-radius: 2px;
-    min-height: 50px;
-}
-
-QTabBar::tab:right:!selected
-{
-    color: #eff0f1;
-    background-color: #54575B;
-    border: 1px solid #76797C;
-    border-right: 1px transparent black;
-    border-top-left-radius: 2px;
-    border-bottom-left-radius: 2px;
-}
-
-QTabBar::tab:right:!selected:hover {
-    background-color: #D1DBCB;
-    color: black;
-}
-
-QTabBar QToolButton::right-arrow:enabled {
-     image: url(:/qss_icons/rc/right_arrow.png);
- }
-
- QTabBar QToolButton::left-arrow:enabled {
-     image: url(:/qss_icons/rc/left_arrow.png);
- }
-
-QTabBar QToolButton::right-arrow:disabled {
-     image: url(:/qss_icons/rc/right_arrow_disabled.png);
- }
-
- QTabBar QToolButton::left-arrow:disabled {
-     image: url(:/qss_icons/rc/left_arrow_disabled.png);
- }
-
-
-QDockWidget {
-    background: #323232;
-    border: 1px solid #403F3F;
-    titlebar-close-icon: url(:/qss_icons/rc/close.png);
-    titlebar-normal-icon: url(:/qss_icons/rc/undock.png);
-}
-
-QDockWidget::close-button, QDockWidget::float-button {
-    border: 1px solid transparent;
-    border-radius: 2px;
-    background: transparent;
-}
-
-QDockWidget::close-button:hover, QDockWidget::float-button:hover {
-    background: rgba(255, 255, 255, 10);
-}
-
-QDockWidget::close-button:pressed, QDockWidget::float-button:pressed {
-    padding: 1px -1px -1px 1px;
-    background: rgba(255, 255, 255, 10);
-}
-
-QTreeView, QListView
-{
-    border: 1px solid #76797C;
-    background-color: #1e1e1e;
-}
-
-QTreeView:branch:selected, QTreeView:branch:hover
-{
-    background: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:has-siblings:!adjoins-item {
-    border-image: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:has-siblings:adjoins-item {
-    border-image: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:!has-children:!has-siblings:adjoins-item {
-    border-image: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:has-children:!has-siblings:closed,
-QTreeView::branch:closed:has-children:has-siblings {
-    image: url(:/qss_icons/rc/branch_closed.png);
-}
-
-QTreeView::branch:open:has-children:!has-siblings,
-QTreeView::branch:open:has-children:has-siblings  {
-    image: url(:/qss_icons/rc/branch_open.png);
-}
-
-QTreeView::branch:has-children:!has-siblings:closed:hover,
-QTreeView::branch:closed:has-children:has-siblings:hover {
-    image: url(:/qss_icons/rc/branch_closed-on.png);
-    }
-
-QTreeView::branch:open:has-children:!has-siblings:hover,
-QTreeView::branch:open:has-children:has-siblings:hover  {
-    image: url(:/qss_icons/rc/branch_open-on.png);
-    }
-
-QListView::item:!selected:hover, QTreeView::item:!selected:hover  {
-    background: #848383;
-    outline: 0;
-    color: #eff0f1;
-}
-
-QListView::item:selected:hover, QTreeView::item:selected:hover  {
-    background: #D1DBCB;
-}
-
-QSlider::groove:horizontal {
-    border: 1px solid #565a5e;
-    height: 4px;
-    background: #565a5e;
-    margin: 0px;
-    border-radius: 2px;
-}
-
-QSlider::handle:horizontal {
-    background: #D1DBCB;
-    border: 1px solid #999999;
-    width: 10px;
-    height: 10px;
-    margin: -5px 0;
-}
-
-QSlider::add-page:qlineargradient {
-    background: #595858;
-    border-top-right-radius: 5px;
-    border-bottom-right-radius: 5px;
-    border-top-left-radius: 0px;
-    border-bottom-left-radius: 0px;
-}
-
-QSlider::sub-page::qlineargradient:horizontal {
-    background:  #D1DBCB;
-    border-top-right-radius: 0px;
-    border-bottom-right-radius: 0px;
-    border-top-left-radius: 5px;
-    border-bottom-left-radius: 5px;
-}
-
-QSlider::groove:vertical {
-    border: 1px solid #565a5e;
-    width: 4px;
-    background: #565a5e;
-    margin: 0px;
-    border-radius: 3px;
-}
-
-QSlider::handle:vertical {
-    background: #D1DBCB;
-    border: 1px solid #999999;
-    width: 10px;
-    height: 10px;
-    margin: 0 -5px;
-}
-
-QToolButton {
-    color: #D1DBCB;
-    background-color: transparent;
-    border: 0px transparent #76797C;
-    border-radius: 0px;
-    padding: 1px;
-    margin-right: 5px;
-}
-
-QToolButton[popupMode="1"] { /* only for MenuButtonPopup */
- padding-right: 20px; /* make way for the popup button */
- border: 1px #76797C;
- border-radius: 0px;
-}
-
-QToolButton[popupMode="2"] { /* only for InstantPopup */
- padding-right: 10px; /* make way for the popup button */
- border: 0px #76797C;
-}
-
-
-QToolButton:hover, QToolButton::menu-button:hover {
-    background-color: transparent;
-    border: 1px solid #D1DBCB;
-    padding: 2px;
-}
-
-QToolButton:checked, QToolButton:pressed,
-        QToolButton::menu-button:pressed {
-    color: black;
-    background-color: #D1DBCB;
-    border: 0px solid #D1DBCB;
-    padding: 2px;
-}
-
-/* the subcontrol below is used only in the InstantPopup or DelayedPopup mode */
-QToolButton::menu-indicator {
-    image: url(:/qss_icons/rc/down_arrow.png);
-    top: -7px; left: -2px; /* shift it a bit */
-}
-
-/* the subcontrols below are used only in the MenuButtonPopup mode */
-QToolButton::menu-button {
-    border: 1px transparent #76797C;
-    border-top-right-radius: 6px;
-    border-bottom-right-radius: 6px;
-    /* 16px width + 4px for border = 20px allocated above */
-    width: 16px;
-    outline: none;
-}
-
-QToolButton::menu-arrow {
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-QToolButton::menu-arrow:open {
-    border: 1px solid #76797C;
-}
-
-QPushButton::menu-indicator  {
-    subcontrol-origin: padding;
-    subcontrol-position: bottom right;
-    left: 8px;
-}
-
-QTableView
-{
-    border: 1px solid #76797C;
-    gridline-color: #323232;
-    background-color: #1e1e1e;
-}
-
-
-QTableView, QHeaderView
-{
-    border-radius: 0px;
-}
-
-QTableView::item:pressed, QListView::item:pressed, QTreeView::item:pressed  {
-    background: #D1DBCB;
-    color: black;
-}
-
-QTableView::item:selected:active, QTreeView::item:selected:active, QListView::item:selected:active  {
-    background: #D1DBCB;
-    color: black;
-}
-
-QHeaderView
-{
-    background-color: #323232;
-    border: 1px transparent;
-    border-radius: 0px;
-    margin: 0px;
-    padding: 0px;
-
-}
-
-QHeaderView::section  {
-    background-color: #323232;
-    color: #eff0f1;
-    padding: 5px;
-    border: 1px solid #76797C;
-    border-radius: 0px;
-    text-align: center;
-}
-
-QHeaderView::section::vertical::first, QHeaderView::section::vertical::only-one
-{
-    border-top: 1px solid #76797C;
-}
-
-QHeaderView::section::vertical
-{
-    border-top: transparent;
-}
-
-QHeaderView::section::horizontal::first, QHeaderView::section::horizontal::only-one
-{
-    border-left: 1px solid #76797C;
-}
-
-QHeaderView::section::horizontal
-{
-    border-left: transparent;
-}
-
-
-QHeaderView::section:checked
- {
-    color: white;
-    background-color: #848383;
- }
-
- /* style the sort indicator */
-QHeaderView::down-arrow {
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-QHeaderView::up-arrow {
-    image: url(:/qss_icons/rc/up_arrow.png);
-}
-
-
-QTableCornerButton::section {
-    background-color: #323232;
-    border: 1px transparent #76797C;
-    border-radius: 0px;
-}
-
-QToolBox  {
-    padding: 5px;
-    border: 1px transparent black;
-}
-
-QToolBox::tab {
-    color: #eff0f1;
-    background-color: #323232;
-    border: 1px solid #76797C;
-    border-bottom: 1px transparent #323232;
-    border-top-left-radius: 5px;
-    border-top-right-radius: 5px;
-}
-
-QToolBox::tab:selected { /* italicize selected tabs */
-    font: italic;
-    background-color: #323232;
-    border-color: #D1DBCB;
- }
-
-QStatusBar::item {
-    border: 0px transparent dark;
-    margin: 0px;
-    border: 0px;
- }
-
-
-QFrame[height="3"], QFrame[width="3"] {
-    background-color: #76797C;
-}
-
-
-QSplitter::handle {
-    border: 1px dashed #76797C;
-}
-
-QSplitter::handle:hover {
-    background-color: #787876;
-    border: 1px solid #76797C;
-}
-
-QSplitter::handle:horizontal {
-    width: 1px;
-}
-
-QSplitter::handle:vertical {
-    height: 1px;
-}
-
-QProgressBar {
-    border: 1px solid #76797C;
-    border-radius: 5px;
-    text-align: center;
-}
-
-QProgressBar::chunk {
-    background-color: #D1DBCB;
-}
-
-QDateEdit
-{
-    selection-background-color: #D1DBCB;
-    border-style: solid;
-    border: 1px solid #CEE343;
-    border-radius: 2px;
-    padding: 1px;
-    min-width: 75px;
-}
-
-QDateEdit:on
-{
-    padding-top: 3px;
-    padding-left: 4px;
-    selection-background-color: #4a4a4a;
-}
-
-QDateEdit QAbstractItemView
-{
-    background-color: #1e1e1e;
-    border-radius: 2px;
-    border: 1px solid #3375A3;
-    selection-background-color: #D1DBCB;
-}
-
-QDateEdit::drop-down
-{
-    subcontrol-origin: padding;
-    subcontrol-position: top right;
-    width: 15px;
-    border-left-width: 0px;
-    border-left-color: darkgray;
-    border-left-style: solid;
-    border-top-right-radius: 3px;
-    border-bottom-right-radius: 3px;
-}
-
-QDateEdit::down-arrow
-{
-    image: url(:/qss_icons/rc/down_arrow_disabled.png);
-}
-
-QDateEdit::down-arrow:on, QDateEdit::down-arrow:hover,
-QDateEdit::down-arrow:focus
-{
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
diff --git a/darkorange.css b/darkorange.css
deleted file mode 100644
index 9df2ee8..0000000
--- a/darkorange.css
+++ /dev/null
@@ -1,520 +0,0 @@
-QToolTip
-{
-     border: 1px solid black;
-     background-color: #ffa02f;
-     padding: 1px;
-     border-radius: 3px;
-     opacity: 100;
-}
-
-QWidget
-{
-    color: #b1b1b1;
-    background-color: #323232;
-}
-
-QTreeView, QListView
-{
-    background-color: silver;
-    margin-left: 5px;
-}
-
-QWidget:item:hover
-{
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #ffa02f, stop: 1 #ca0619);
-    color: #000000;
-}
-
-QWidget:item:selected
-{
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #ffa02f, stop: 1 #d7801a);
-}
-
-QMenuBar::item
-{
-    background: transparent;
-}
-
-QMenuBar::item:selected
-{
-    background: transparent;
-    border: 1px solid #ffaa00;
-}
-
-QMenuBar::item:pressed
-{
-    background: #444;
-    border: 1px solid #000;
-    background-color: QLinearGradient(
-        x1:0, y1:0,
-        x2:0, y2:1,
-        stop:1 #212121,
-        stop:0.4 #343434/*,
-        stop:0.2 #343434,
-        stop:0.1 #ffaa00*/
-    );
-    margin-bottom:-1px;
-    padding-bottom:1px;
-}
-
-QMenu
-{
-    border: 1px solid #000;
-}
-
-QMenu::item
-{
-    padding: 2px 20px 2px 20px;
-}
-
-QMenu::item:selected
-{
-    color: #000000;
-}
-
-QWidget:disabled
-{
-    color: #808080;
-    background-color: #323232;
-}
-
-QAbstractItemView
-{
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #4d4d4d, stop: 0.1 #646464, stop: 1 #5d5d5d);
-}
-
-QWidget:focus
-{
-    /*border: 1px solid darkgray;*/
-}
-
-QLineEdit
-{
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #4d4d4d, stop: 0 #646464, stop: 1 #5d5d5d);
-    padding: 1px;
-    border-style: solid;
-    border: 1px solid #1e1e1e;
-    border-radius: 5;
-}
-
-QPushButton
-{
-    color: #b1b1b1;
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #565656, stop: 0.1 #525252, stop: 0.5 #4e4e4e, stop: 0.9 #4a4a4a, stop: 1 #464646);
-    border-width: 1px;
-    border-color: #1e1e1e;
-    border-style: solid;
-    border-radius: 6;
-    padding: 3px;
-    font-size: 12px;
-    padding-left: 5px;
-    padding-right: 5px;
-    min-width: 40px;
-}
-
-QPushButton:pressed
-{
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #2d2d2d, stop: 0.1 #2b2b2b, stop: 0.5 #292929, stop: 0.9 #282828, stop: 1 #252525);
-}
-
-QComboBox
-{
-    selection-background-color: #ffaa00;
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #565656, stop: 0.1 #525252, stop: 0.5 #4e4e4e, stop: 0.9 #4a4a4a, stop: 1 #464646);
-    border-style: solid;
-    border: 1px solid #1e1e1e;
-    border-radius: 5;
-}
-
-QComboBox:hover,QPushButton:hover
-{
-    border: 2px solid QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #ffa02f, stop: 1 #d7801a);
-}
-
-
-QComboBox:on
-{
-    padding-top: 3px;
-    padding-left: 4px;
-    background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #2d2d2d, stop: 0.1 #2b2b2b, stop: 0.5 #292929, stop: 0.9 #282828, stop: 1 #252525);
-    selection-background-color: #ffaa00;
-}
-
-QComboBox QAbstractItemView
-{
-    border: 2px solid darkgray;
-    selection-background-color: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #ffa02f, stop: 1 #d7801a);
-}
-
-QComboBox::drop-down
-{
-     subcontrol-origin: padding;
-     subcontrol-position: top right;
-     width: 15px;
-
-     border-left-width: 0px;
-     border-left-color: darkgray;
-     border-left-style: solid; /* just a single line */
-     border-top-right-radius: 3px; /* same radius as the QComboBox */
-     border-bottom-right-radius: 3px;
- }
-
-QComboBox::down-arrow
-{
-     image: url(:/dark_orange/img/down_arrow.png);
-}
-
-QGroupBox
-{
-    border: 1px solid darkgray;
-    margin-top: 10px;
-}
-
-QGroupBox:focus
-{
-    border: 1px solid darkgray;
-}
-
-QTextEdit:focus
-{
-    border: 1px solid darkgray;
-}
-
-QScrollBar:horizontal {
-     border: 1px solid #222222;
-     background: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0.0 #121212, stop: 0.2 #282828, stop: 1 #484848);
-     height: 7px;
-     margin: 0px 16px 0 16px;
-}
-
-QScrollBar::handle:horizontal
-{
-      background: QLinearGradient( x1: 0, y1: 0, x2: 1, y2: 0, stop: 0 #ffa02f, stop: 0.5 #d7801a, stop: 1 #ffa02f);
-      min-height: 20px;
-      border-radius: 2px;
-}
-
-QScrollBar::add-line:horizontal {
-      border: 1px solid #1b1b19;
-      border-radius: 2px;
-      background: QLinearGradient( x1: 0, y1: 0, x2: 1, y2: 0, stop: 0 #ffa02f, stop: 1 #d7801a);
-      width: 14px;
-      subcontrol-position: right;
-      subcontrol-origin: margin;
-}
-
-QScrollBar::sub-line:horizontal {
-      border: 1px solid #1b1b19;
-      border-radius: 2px;
-      background: QLinearGradient( x1: 0, y1: 0, x2: 1, y2: 0, stop: 0 #ffa02f, stop: 1 #d7801a);
-      width: 14px;
-     subcontrol-position: left;
-     subcontrol-origin: margin;
-}
-
-QScrollBar::right-arrow:horizontal, QScrollBar::left-arrow:horizontal
-{
-      border: 1px solid black;
-      width: 1px;
-      height: 1px;
-      background: white;
-}
-
-QScrollBar::add-page:horizontal, QScrollBar::sub-page:horizontal
-{
-      background: none;
-}
-
-QScrollBar:vertical
-{
-      background: QLinearGradient( x1: 0, y1: 0, x2: 1, y2: 0, stop: 0.0 #121212, stop: 0.2 #282828, stop: 1 #484848);
-      width: 7px;
-      margin: 16px 0 16px 0;
-      border: 1px solid #222222;
-}
-
-QScrollBar::handle:vertical
-{
-      background: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #ffa02f, stop: 0.5 #d7801a, stop: 1 #ffa02f);
-      min-height: 20px;
-      border-radius: 2px;
-}
-
-QScrollBar::add-line:vertical
-{
-      border: 1px solid #1b1b19;
-      border-radius: 2px;
-      background: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #ffa02f, stop: 1 #d7801a);
-      height: 14px;
-      subcontrol-position: bottom;
-      subcontrol-origin: margin;
-}
-
-QScrollBar::sub-line:vertical
-{
-      border: 1px solid #1b1b19;
-      border-radius: 2px;
-      background: QLinearGradient( x1: 0, y1: 0, x2: 0, y2: 1, stop: 0 #d7801a, stop: 1 #ffa02f);
-      height: 14px;
-      subcontrol-position: top;
-      subcontrol-origin: margin;
-}
-
-QScrollBar::up-arrow:vertical, QScrollBar::down-arrow:vertical
-{
-      border: 1px solid black;
-      width: 1px;
-      height: 1px;
-      background: white;
-}
-
-
-QScrollBar::add-page:vertical, QScrollBar::sub-page:vertical
-{
-      background: none;
-}
-
-QTextEdit
-{
-    background-color: #242424;
-}
-
-QPlainTextEdit
-{
-    background-color: #242424;
-}
-
-QHeaderView::section
-{
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:0 #616161, stop: 0.5 #505050, stop: 0.6 #434343, stop:1 #656565);
-    color: white;
-    padding-left: 4px;
-    border: 1px solid #6c6c6c;
-}
-
-QCheckBox:disabled
-{
-color: #414141;
-}
-
-QDockWidget::title
-{
-    text-align: center;
-    spacing: 3px; /* spacing between items in the tool bar */
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:0 #323232, stop: 0.5 #242424, stop:1 #323232);
-}
-
-QDockWidget::close-button, QDockWidget::float-button
-{
-    text-align: center;
-    spacing: 1px; /* spacing between items in the tool bar */
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:0 #323232, stop: 0.5 #242424, stop:1 #323232);
-}
-
-QDockWidget::close-button:hover, QDockWidget::float-button:hover
-{
-    background: #242424;
-}
-
-QDockWidget::close-button:pressed, QDockWidget::float-button:pressed
-{
-    padding: 1px -1px -1px 1px;
-}
-
-QMainWindow::separator
-{
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:0 #161616, stop: 0.5 #151515, stop: 0.6 #212121, stop:1 #343434);
-    color: white;
-    padding-left: 4px;
-    border: 1px solid #4c4c4c;
-    spacing: 3px; /* spacing between items in the tool bar */
-}
-
-QMainWindow::separator:hover
-{
-
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:0 #d7801a, stop:0.5 #b56c17 stop:1 #ffa02f);
-    color: white;
-    padding-left: 4px;
-    border: 1px solid #6c6c6c;
-    spacing: 3px; /* spacing between items in the tool bar */
-}
-
-QToolBar::handle
-{
-     spacing: 3px; /* spacing between items in the tool bar */
-     background: url(:/dark_orange/img/handle.png);
-}
-
-QMenu::separator
-{
-    height: 2px;
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:0 #161616, stop: 0.5 #151515, stop: 0.6 #212121, stop:1 #343434);
-    color: white;
-    padding-left: 4px;
-    margin-left: 10px;
-    margin-right: 5px;
-}
-
-QProgressBar
-{
-    border: 2px solid grey;
-    border-radius: 5px;
-    text-align: center;
-}
-
-QProgressBar::chunk
-{
-    background-color: #d7801a;
-    width: 2.15px;
-    margin: 0.5px;
-}
-
-QTabBar::tab {
-    color: #b1b1b1;
-    border: 1px solid #444;
-    border-bottom-style: none;
-    background-color: #323232;
-    padding-left: 10px;
-    padding-right: 10px;
-    padding-top: 3px;
-    padding-bottom: 2px;
-    margin-right: -1px;
-}
-
-QTabWidget::pane {
-    border: 1px solid #444;
-    top: 1px;
-}
-
-QTabBar::tab:last
-{
-    margin-right: 0; /* the last selected tab has nothing to overlap with on the right */
-    border-top-right-radius: 3px;
-}
-
-QTabBar::tab:first:!selected
-{
- margin-left: 0px; /* the last selected tab has nothing to overlap with on the right */
-
-
-    border-top-left-radius: 3px;
-}
-
-QTabBar::tab:!selected
-{
-    color: #b1b1b1;
-    border-bottom-style: solid;
-    margin-top: 3px;
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:1 #212121, stop:.4 #343434);
-}
-
-QTabBar::tab:selected
-{
-    border-top-left-radius: 3px;
-    border-top-right-radius: 3px;
-    margin-bottom: 0px;
-}
-
-QTabBar::tab:!selected:hover
-{
-    /*border-top: 2px solid #ffaa00;
-    padding-bottom: 3px;*/
-    border-top-left-radius: 3px;
-    border-top-right-radius: 3px;
-    background-color: QLinearGradient(x1:0, y1:0, x2:0, y2:1, stop:1 #212121, stop:0.4 #343434, stop:0.2 #343434, stop:0.1 #ffaa00);
-}
-
-QRadioButton::indicator:checked, QRadioButton::indicator:unchecked{
-    color: #b1b1b1;
-    background-color: #323232;
-    border: 1px solid #b1b1b1;
-    border-radius: 6px;
-}
-
-QRadioButton::indicator:checked
-{
-    background-color: qradialgradient(
-        cx: 0.5, cy: 0.5,
-        fx: 0.5, fy: 0.5,
-        radius: 1.0,
-        stop: 0.25 #ffaa00,
-        stop: 0.3 #323232
-    );
-}
-
-QCheckBox::indicator{
-    color: #b1b1b1;
-    background-color: #323232;
-    border: 1px solid #b1b1b1;
-    width: 9px;
-    height: 9px;
-}
-
-QRadioButton::indicator
-{
-    border-radius: 6px;
-}
-
-QRadioButton::indicator:hover, QCheckBox::indicator:hover
-{
-    border: 1px solid #ffaa00;
-}
-
-QCheckBox::indicator:checked
-{
-    image:url(:/dark_orange/img/checkbox.png);
-}
-
-QCheckBox::indicator:disabled, QRadioButton::indicator:disabled
-{
-    border: 1px solid #444;
-}
-
-
-QSlider::groove:horizontal {
-    border: 1px solid #3A3939;
-    height: 8px;
-    background: #201F1F;
-    margin: 2px 0;
-    border-radius: 2px;
-}
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diff --git a/icon/plus.png b/icon/plus.png
deleted file mode 100644
index 08a6564..0000000
--- a/icon/plus.png
+++ /dev/null
diff --git a/icon/zoomIn.png b/icon/zoomIn.png
deleted file mode 100644
index b10c61a..0000000
--- a/icon/zoomIn.png
+++ /dev/null
diff --git a/icon/zoomOut.png b/icon/zoomOut.png
deleted file mode 100644
index 6c60a02..0000000
--- a/icon/zoomOut.png
+++ /dev/null
diff --git a/icon/zoomReset.png b/icon/zoomReset.png
deleted file mode 100644
index 62fc917..0000000
--- a/icon/zoomReset.png
+++ /dev/null
diff --git a/info/build/windows/build.txt b/info/build/windows/build.txt
new file mode 100644
index 0000000..7066da7
--- /dev/null
+++ b/info/build/windows/build.txt
@@ -0,0 +1,23 @@
+Steps to create .exe for Chemical Simulator GUI
+1. Go to dir=> src/main/python/
+2. Run the command=> pyinstaller --onefile -windowed --icon=..\resources\base\icons\logo.ico --name="Chemical Simulator GUI" --add-data="..\..\*;." --hidden-import=csv --hidden-import=pandas --hidden-import=PyQt5.uic --hidden-import=xml.dom --hidden-import=pyqtgraph mainApp.py
+3. Move the .exe in 'src/main/python/dist/' to 'src/main/python/'
+4. Delete the file and folders after moving the .exe
+	File to delete
+		1. src/main/python/Chemical Simulator GUI.spec
+	Folders to delete
+		1. src/main/python/dist
+		2. src/main/python/build
+Steps to create installer for Chemical Simulator GUI
+1. Go to dir=> Chemical-Simulator-GUI/
+2. Zip the contents in the folder
+3. Name the zipped folder 'Chemical-Simulator-GUI'
+4. Launch NSIS
+5. Click on the option 'Installer based on .ZIP file' in NSIS
+6. Select the zipped folder created in Step 2 and 3.
+7. Options in NSIS
+	i)	Installer Name - Chemical-Simulator-GUI
+	ii)	Interface - Modern
+	iii)	Default Folder - $PROGRAMFILES\Chemical-Simulator-GUI
+	iv)	Compression - LZMA
+8. Click Generate
\ No newline at end of file
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index 851904b..851904b 100644
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+++ b/info/structure/DiagramRepresentation_Component[dot]py_2019work.uxf
diff --git a/class_diagram.pdf b/info/structure/class_diagram.pdf
index c2c1134..c2c1134 100644
--- a/class_diagram.pdf
+++ b/info/structure/class_diagram.pdf
diff --git a/umlet.uxf b/info/structure/umlet.uxf
index 89f794e..89f794e 100644
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-	color:rgb(255,255,255);
-	padding-top:2px;
-	padding-left:2px;
-	padding-right:2px;
-	border-top-width:2px;
-	border-left-width:2px;
-	border-right-width:2px;
-	border-top-right-radius:4px;
-	border-top-left-radius:4px;
-	border-style:solid;
-	background-color:rgb(65,64,59);
-	border-top-color: rgb(47,47,44);
-	border-right-color: qlineargradient(spread:pad, x1:0, y1:1, x2:1, y2:0, stop:0 rgba(90, 87, 78, 255), stop:1 rgba(47,47,44, 255));
-	border-left-color:  qlineargradient(spread:pad, x1:1, y1:0, x2:0, y2:0, stop:0 rgba(90, 87, 78, 255), stop:1 rgba(47,47,44, 255));
-}
-QMenu::item:selected {
-	color:rgb(255,255,255);
-	background-color: qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(225, 108, 54, 255), stop:1 rgba(246, 134, 86, 255));
-	border-style:solid;
-	border-width:3px;
-	padding-left:17px;
-	padding-top:4px;
-	padding-bottom:4px;
-	padding-right:7px;
-	border-bottom-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(175,85,48,255), stop:1 rgba(236,114,67, 255));
-	border-top-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-	border-right-color:qlineargradient(spread:pad, x1:0, y1:0.5, x2:1, y2:0.5, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-	border-left-color:qlineargradient(spread:pad, x1:1, y1:0.5, x2:0, y2:0.5, stop:0 rgba(253,156,113,255), stop:1 rgba(205,90,46, 255));
-}
-QMenu::item {
-	color:rgb(223,219,210);
-	padding-left:20px;
-	padding-top:4px;
-	padding-bottom:4px;
-	padding-right:10px;
-}
-QMenu {
-	color:rgb(223,219,210);
-	background-color:rgb(65,64,59);
-}
-QCheckBox {
-	padding:2px;
-}
-QCheckBox:hover {
-	border-radius:4px;
-	border-style:solid;
-	border-width:1px;
-	padding-left: 1px;
-	padding-right: 1px;
-	padding-bottom: 1px;
-	padding-top: 1px;
-	border-color: rgb(255,150,60);
-	background-color:qlineargradient(spread:pad, x1:0.5, y1:1, x2:0.5, y2:0, stop:0 rgba(190, 90, 50, 50), stop:1 rgba(250, 130, 40, 50));
-}
-QCheckBox::indicator:checked {
-	border-radius:4px;
-	border-style:solid;
-	border-width:1px;
-	border-color: rgb(246, 134, 86);
-  	background-color:rgb(246, 134, 86)
-}
-QCheckBox::indicator:unchecked {
-	border-radius:4px;
-	border-style:solid;
-	border-width:1px;
-	border-color:rgb(246, 134, 86);
-  	background-color:rgb(255,255,255);
-}
-QRadioButton {
-	padding: 1px;
-}
-QRadioButton::indicator:checked {
-	height: 10px;
-	width: 10px;
-	border-style:solid;
-	border-radius:5px;
-	border-width: 1px;
-	border-color: rgba(246, 134, 86, 255);
-	color: #a9b7c6;
-	background-color:rgba(246, 134, 86, 255);
-}
-QRadioButton::indicator:!checked {
-	height: 10px;
-	width: 10px;
-	border-style:solid;
-	border-radius:5px;
-	border-width: 1px;
-	border-color: rgb(246, 134, 86);
-	color: #a9b7c6;
-	background-color: transparent;
-}
-QStatusBar {
-	color:rgb(81,72,65);
-}
-QSpinBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QDoubleSpinBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QTimeEdit {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QDateTimeEdit {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QDateEdit {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QComboBox {
-	color:rgb(81,72,65);
-	background: #ffffff;
-}
-QComboBox:editable {
-	background: #ffffff;
-	color: rgb(81,72,65);
-	selection-color:rgb(81,72,65);
-	selection-background-color: #ffffff;
-}
-QComboBox QAbstractItemView {
-	color:rgb(81,72,65);	
-	background: #ffffff;
-	selection-color: #ffffff;
-	selection-background-color: rgb(246, 134, 86);
-}
-QComboBox:!editable:on, QComboBox::drop-down:editable:on {
-	color:  #1e1d23;	
-	background: #ffffff;
-}
-QFontComboBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QHeaderView::section {
-	padding:3px;
-	margin:0px;
-	color:#F0F0F0;
-	border: 1px solid #F0F0F0;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 rgb(222,192,222), stop:1 rgb(222,192,242));
-}
-QToolBox {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QToolBox::tab {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QToolBox::tab:selected {
-	color:rgb(81,72,65);
-	background-color: #ffffff;
-}
-QScrollArea {
-	color: #FFFFFF;
-	background-color:#f0f0f0;
-}
-QSlider::groove {
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-}
-QSlider::groove:horizontal {
-	height: 5px;
-	background: rgb(246, 134, 86);
-}
-QSlider::groove:vertical {
-	width: 5px;
-	background: rgb(246, 134, 86);
-}
-QSlider::handle:horizontal {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	width: 12px;
-	margin: -5px 0;
-	border-radius: 7px;
-}
-QSlider::handle:vertical {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	height: 12px;
-	margin: 0 -5px;
-	border-radius: 7px;
-}
-QSlider::add-page:horizontal {
- 	background: white;
-}
-QSlider::add-page:vertical {
-	background: white;
-}
-QSlider::sub-page:horizontal {
-	background: rgb(246, 134, 86);
-}
-QSlider::sub-page:vertical {
-  	background: rgb(246, 134, 86);
-}
-QScrollBar:horizontal {
-	max-height: 20px;
-	border: 1px transparent grey;
-	margin: 0px 20px 0px 20px;
-}
-QScrollBar::handle:horizontal {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	border-radius: 7px;
-	min-width: 25px;
-}
-QScrollBar::handle:horizontal:hover {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(255,150,60);
-	border-radius: 7px;
-	min-width: 25px;
-}
-QScrollBar::add-line:horizontal {
-  	border: 1px solid;
-  	border-color: rgb(207,207,207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: right;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:horizontal:hover {
-  	border: 1px solid;
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	border-color: rgb(255,150,60);
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: right;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:horizontal:pressed {
-  	border: 1px solid grey;
-  	border-top-left-radius: 7px;
-  	border-top-right-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	background: rgb(231,231,231);
-  	width: 20px;
-  	subcontrol-position: right;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:horizontal {
-  	border: 1px solid;
-  	border-color: rgb(207,207,207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: left;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:horizontal:hover {
-  	border: 1px solid;
-  	border-color: rgb(255,150,60);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	width: 20px;
-  	subcontrol-position: left;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:horizontal:pressed {
-  	border: 1px solid grey;
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(231,231,231);
-  	width: 20px;
-  	subcontrol-position: left;
-  	subcontrol-origin: margin;
-}
-QScrollBar::left-arrow:horizontal {
-  	border: 1px transparent grey;
-  	border-top-left-radius: 3px;
-  	border-bottom-left-radius: 3px;
-  	width: 6px;
-  	height: 6px;
-  	background: rgb(230,230,230);
-}
-QScrollBar::right-arrow:horizontal {
-	border: 1px transparent grey;
-	border-top-right-radius: 3px;
-	border-bottom-right-radius: 3px;
-  	width: 6px;
-  	height: 6px;
- 	background: rgb(230,230,230);
-}
-QScrollBar::add-page:horizontal, QScrollBar::sub-page:horizontal {
- 	background: none;
-} 
-QScrollBar:vertical {
-	max-width: 20px;
-	border: 1px transparent grey;
-	margin: 20px 0px 20px 0px;
-}
-QScrollBar::add-line:vertical {
-	border: 1px solid;
-	border-color: rgb(207,207,207);
-	border-bottom-right-radius: 7px;
-	border-bottom-left-radius: 7px;
-	border-top-left-radius: 7px;
-	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: bottom;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:vertical:hover {
-  	border: 1px solid;
-  	border-color: rgb(255,150,60);
-  	border-bottom-right-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	border-top-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: bottom;
-  	subcontrol-origin: margin;
-}
-QScrollBar::add-line:vertical:pressed {
-  	border: 1px solid grey;
-  	border-bottom-left-radius: 7px;
-  	border-bottom-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	background: rgb(231,231,231);
-  	height: 20px;
-  	subcontrol-position: bottom;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:vertical {
-  	border: 1px solid;
-  	border-color: rgb(207,207,207);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-  	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: top;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:vertical:hover {
-  	border: 1px solid;
-  	border-color: rgb(255,150,60);
-  	border-top-right-radius: 7px;
-  	border-top-left-radius: 7px;
-  	border-bottom-left-radius: 7px;
-	background: rgb(255, 255, 255);
-  	height: 20px;
-  	subcontrol-position: top;
-  	subcontrol-origin: margin;
-}
-QScrollBar::sub-line:vertical:pressed {
-  	border: 1px solid grey;
-  	border-top-left-radius: 7px;
-  	border-top-right-radius: 7px;
-  	background: rgb(231,231,231);
- 	height: 20px;
-  	subcontrol-position: top;
-  	subcontrol-origin: margin;
-}
-	QScrollBar::handle:vertical {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(207,207,207);
-	border-radius: 7px;
-	min-height: 25px;
-}
-QScrollBar::handle:vertical:hover {
-	background: rgb(253,253,253);
-	border-style: solid;
-	border-width: 1px;
-	border-color: rgb(255,150,60);
-	border-radius: 7px;
-	min-height: 25px;
-}
-QScrollBar::up-arrow:vertical {
-	border: 1px transparent grey;
-  	border-top-left-radius: 3px;
-	border-top-right-radius: 3px;
-  	width: 6px;
-  	height: 6px;
-  	background: rgb(230,230,230);
-}
-QScrollBar::down-arrow:vertical {
-  	border: 1px transparent grey;
-  	border-bottom-left-radius: 3px;
-  	border-bottom-right-radius: 3px;
-  	width: 6px;
-  	height: 6px;
-  	background: rgb(230,230,230);
-}
-QScrollBar::add-page:vertical, QScrollBar::sub-page:vertical {
-  	background: none;
-}
\ No newline at end of file
diff --git a/new.css b/new.css
deleted file mode 100644
index a193833..0000000
--- a/new.css
+++ /dev/null
@@ -1,347 +0,0 @@
-QWidget#frmLogin,QWidget#frmPopup,QWidget#frmHostInfo,QWidget#frmLogout,QWidget#frmConfig,QWidget#frmData,QWidget#frmDefence,QWidget#frmHost,QWidget#frmMain,QWidget#frmPwd,QWidget#frmSelect,QWidget#frmMessageBox{
-	border:1px solid #454648;
-	border-radius:0px;	
-}
-
-.QFrame{
-	border:1px solid #B8B8B8;
-	border-radius:5px;
-}
-
-QWidget#widget_title{
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A);
-}
-
-QLabel#lab_Ico,QLabel#lab_Title{
-	border-radius:0px;
-	color: #F0F0F0;
-	background-color:rgba(0,0,0,0);
-	border-style:none;
-}
-
-QLineEdit {
-	border: 1px solid #B8B8B8;
-	border-radius: 5px;
-	padding: 2px;
-	background: none;
-	selection-background-color: #454648;
-}
-
-QLineEdit[echoMode="2"] { 
-	lineedit-password-character: 9679; 
-}
-
-.QGroupBox{
-	border: 1px solid #B8B8B8;
-	border-radius: 5px;
-}
-
-.QPushButton{
-	border-style: none;
-	border: 0px;
-	color: #F0F0F0;
-	padding: 5px;	
-	min-height: 20px;
-	border-radius:5px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-.QPushButton[focusPolicy="0"] {
-	border-style: none;
-	border: 0px;
-	color: #F0F0F0;
-	padding: 0px;	
-	min-height: 10px;
-	border-radius:3px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-.QPushButton:hover{ 
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #B8B8B8, stop:1 #D6D6D6);
-}
-
-.QPushButton:pressed{ 
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A);
-}
-
-QPushButton#btnMenu,QPushButton#btnMenu_Min,QPushButton#btnMenu_Max,QPushButton#btnMenu_Close{
-	border-radius:0px;
-	color: #F0F0F0;
-	background-color:rgba(0,0,0,0);
-	border-style:none;
-}
-
-QPushButton#btnMenu:hover,QPushButton#btnMenu_Min:hover,QPushButton#btnMenu_Max:hover{
-	background-color: qlineargradient(spread:pad, x1:0, y1:1, x2:0, y2:0, stop:0 rgba(25, 134, 199, 0), stop:1 #B8B8B8);
-}
-
-QPushButton#btnMenu_Close:hover{
-	background-color: qlineargradient(spread:pad, x1:0, y1:1, x2:0, y2:0, stop:0 rgba(238, 0, 0, 128), stop:1 rgba(238, 44, 44, 255));
-}
-
-QCheckBox {
-	spacing: 2px; 
-}
-
-QCheckBox::indicator {
-	width: 20px;
-	height: 20px;
-}
-
-QCheckBox::indicator:unchecked {
-	image: url(:/qss_icons/img_rc/checkbox_unchecked.png);
-}
-
-QCheckBox::indicator:checked {
-	image: url(:/qss_icons/img_rc/checkbox_checked.png); 
-}
-
-QRadioButton {
-	spacing: 2px;
-}
-
-QRadioButton::indicator {
-	width: 15px; 
-	height: 15px; 
-}
-
-QRadioButton::indicator::unchecked {
-	image: url(:/qss_icons/img_rc/radio_normal.png); 
-}
-
-QRadioButton::indicator::checked {
-	image: url(:/qss_icons/img_rc/radio_selected.png); 
-}
-
-QComboBox,QDateEdit{
-	border-radius: 3px;
-	padding: 1px 10px 1px 5px;
-	border: 1px solid #B8B8B8;
-}
-
-QComboBox::drop-down,QDateEdit::drop-down {
-	subcontrol-origin: padding;
-	subcontrol-position: top right;
-	width: 15px; 
-	border-left-width: 1px;
-	border-left-style: solid;
-	border-top-right-radius: 3px;
-	border-bottom-right-radius: 3px;
-	border-left-color: #B8B8B8;
-}
-
-QComboBox::down-arrow,QDateEdit::down-arrow {
-	image: url(:/qss_icons/img_rc/array_down.png); 
-}
-
-QMenu {
-	background-color:#F0F0F0;
-	margin: 2px;
-}
-
-QMenu::item {	
-	padding: 2px 12px 2px 12px;
-}
-
-QMenu::indicator {
-	width: 13px;
-	height: 13px;
-}
-
-QMenu::item:selected {
-	color: #F0F0F0;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-QMenu::separator {
-	height: 1px;
-	background: #B8B8B8;
-}
-
-QProgressBar {
-	border-radius: 5px;
-	text-align: center;
-	border: 1px solid #B8B8B8;
-}
-
-QProgressBar::chunk {
-	width: 5px; 
-	margin: 0.5px;
-	background-color: #454648;
-}
-
-QSlider::groove:horizontal,QSlider::add-page:horizontal { 
-	background: #808080; 
-	height: 8px; 
-	border-radius: 3px; 
-}
-
-QSlider::sub-page:horizontal {
-	height: 8px; 
-	border-radius: 3px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-QSlider::handle:horizontal {
-	width: 13px; 
-	margin-top: -3px; 
-	margin-bottom: -3px; 
-	border-radius: 6px;
-	background: qradialgradient(spread:pad, cx:0.5, cy:0.5, radius:0.5, fx:0.5, fy:0.5,stop:0.6 #F0F0F0, stop:0.778409 #B8B8B8);
-}
-
-QSlider::handle:horizontal:hover {
-	background: qradialgradient(spread: pad, cx: 0.5, cy: 0.5, radius: 0.5, fx: 0.5, fy: 0.5, stop: 0.6 #F0F0F0,stop:0.778409 #454648);
-}
-
-QSlider::groove:vertical,QSlider::sub-page:vertical {
-	background:#808080; 
-	width: 8px; 
-	border-radius: 3px;
-}
-
-QSlider::add-page:vertical {
-	width: 8px;
-	border-radius: 3px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-QSlider::handle:vertical {
-	height: 14px; 
-	margin-left: -3px;
-	margin-right: -3px;
-	border-radius: 6px;
-	background: qradialgradient(spread: pad, cx: 0.5, cy: 0.5, radius: 0.5, fx: 0.5, fy: 0.5, stop: 0.6 #F0F0F0, stop:0.778409 #B8B8B8);
-}
-
-QSlider::handle:vertical:hover {
-	background: qradialgradient(spread: pad, cx: 0.5, cy: 0.5, radius: 0.5, fx: 0.5, fy: 0.5, stop: 0.6 #F0F0F0,stop:0.778409 #454648);
-}
-
-QScrollBar:vertical {
-	width:10px; 
-	background-color:rgba(0,0,0,0%); 
-	padding-top:10px; 
-	padding-bottom:10px;
-}
-
-QScrollBar:horizontal {
-	height:10px; 
-	background-color:rgba(0,0,0,0%); 
-	padding-left:10px; padding-right:10px;
-}
-
-QScrollBar::handle:vertical {
-	width:10px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #B8B8B8, stop:1 #D6D6D6); 
-}
-
-QScrollBar::handle:horizontal {
-	height:10px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #B8B8B8, stop:1 #D6D6D6); 
-}
-
-QScrollBar::handle:vertical:hover {
-	width:10px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-QScrollBar::handle:horizontal:hover {
-	height:10px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-QScrollBar::add-line:vertical {
-	height:10px;
-	width:10px;
-	subcontrol-position: bottom; 
-	subcontrol-origin: margin;
-	border-image:url(:/qss_icons/img_rc/add-line_vertical.png);
-}
-
-QScrollBar::add-line:horizontal {
-	height:10px;
-	width:10px;
-	subcontrol-position: right;
-	subcontrol-origin: margin;
-	border-image:url(:/qss_icons/img_rc/add-line_horizontal.png);
-}
-
-QScrollBar::sub-line:vertical {
-	height:10px;
-	width:10px;
-	subcontrol-position: top; 
-	subcontrol-origin: margin;
-	border-image:url(:/qss_icons/img_rc/sub-line_vertical.png);
-}
-
-QScrollBar::sub-line:horizontal {
-	height:10px;
-	width:10px;
-	subcontrol-position: left;
-	subcontrol-origin: margin;
-	border-image:url(:/qss_icons/img_rc/sub-line_horizontal.png);
-}
-
-QScrollBar::add-page:vertical,QScrollBar::sub-page:vertical {
-	width:10px;
-	background: #C0C0C0;
-}
-
-QScrollBar::add-page:horizontal,QScrollBar::sub-page:horizontal {
-	height:10px;
-	background: #C0C0C0;
-}
-
-QScrollArea {
-	border: 0px ; 
-}
-
-QTreeView,QListView,QTableView{
-	border: 1px solid #B8B8B8; 
-	selection-background-color: #454648;
-	selection-color: #F0F0F0;
-}
-
-QTableView::item:selected, QListView::item:selected, QTreeView::item:selected {
-	color: #F0F0F0;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-QTableView::item:hover, QListView::item:hover, QTreeView::item:hover {
-	color: #F0F0F0;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #B8B8B8, stop:1 #D6D6D6); 
-}
-
-QTableView::item, QListView::item, QTreeView::item {
-	padding: 5px; 
-	margin: 0px; 
-}
-
-QHeaderView::section {
-	padding:3px;
-	margin:0px;
-	color:#F0F0F0;
-	border: 1px solid #F0F0F0;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #B8B8B8, stop:1 #D6D6D6);
-}
-
-QTabBar::tab {
-	border-bottom-left-radius:0px;
-	border-bottom-right-radius:0px;
-	color: #F0F0F0;
-	min-width: 60px;
-	min-height: 20px;
-	padding: 3px 8px 3px 8px;
-	margin:1px;
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #B8B8B8, stop:1 #D6D6D6); 
-}
-
-QTabBar::tab:selected, QTabBar::tab:hover {
-	background: qlineargradient(spread:pad, x1:0, y1:0, x2:0, y2:1, stop:0 #454648, stop:1 #7A7A7A); 
-}
-
-QStatusBar::item {
-     border: 1px solid #B8B8B8;
-     border-radius: 3px;
-}
\ No newline at end of file
diff --git a/pycflags b/pycflags
deleted file mode 100644
index e69de29..0000000
--- a/pycflags
+++ /dev/null
diff --git a/pyldflags b/pyldflags
deleted file mode 100644
index e69de29..0000000
--- a/pyldflags
+++ /dev/null
diff --git a/qdark.css b/qdark.css
deleted file mode 100644
index 0ca3c73..0000000
--- a/qdark.css
+++ /dev/null
@@ -1,1898 +0,0 @@
-/* QDarkStyleSheet --------------------------------------------------------
-
-This is the main style sheet, the palette has nine main colors.
-It is based on three selecting colors, three greyish (background) colors
-plus three whitish (foreground) colors. Each set of widgets of the same
-type have a header like this:
-
-    ------------------
-    GroupName --------
-    ------------------
-
-And each widget is separated with a header like this:
-
-    QWidgetName ------
-
-This makes more easy to find and change some css field. The basic
-configuration is described bellow.
-
-    SELECTION ------------
-
-        sel_light  #179AE0 #148CD2 (selection/hover/active)
-        sel_normal #3375A3 #1464A0 (selected)
-        sel_dark   #18465D #14506E (selected disabled)
-
-    FOREGROUND -----------
-
-        for_light  #EFF0F1 #F0F0F0 (texts/labels)
-        for_dark   #505F69 #787878 (disabled texts)
-
-    BACKGROUND -----------
-
-        bac_light  #4D545B #505F69 (unpressed)
-        bac_normal #31363B #32414B (border, disabled, pressed, checked, toolbars, menus)
-        bac_dark   #232629 #19232D (background)
-
-If a stranger configuration is required because of a bugfix or anything
-else, keep the comment on that line to nobodys changed it, including the
-issue number.
---------------------------------------------------------------------------- */
-
-
-
-/* QWidget ---------------------------------------------------------------- */
-
-QWidget {
-    background-color: #19232D;
-    border: 0px solid #32414B;
-    padding: 0px;
-    color: #F0F0F0;
-    selection-background-color: #1464A0;
-    selection-color: #F0F0F0;
-}
-
-QWidget:disabled {
-    background-color: #19232D;
-    color: #787878;
-    selection-background-color: #14506E;
-    selection-color: #787878;
-}
-
-QWidget:item:selected {
-    background-color: #1464A0;
-}
-
-QWidget:item:hover {
-    background-color: #148CD2;
-    color: #32414B;
-}
-
-/* QMainWindow ------------------------------------------------------------ */
-/* This adjusts the splitter in the dock widget, not qsplitter              */
-
-
-QMainWindow::separator {
-    background-color: #32414B;
-    border: 0 solid #19232D;
-    spacing: 0;
-    padding: 2px;
-}
-
-QMainWindow::separator:hover {
-    background-color: #505F69;
-    border: 0px solid #148CD2;
-}
-
-QMainWindow::separator:horizontal {
-    width: 5px;
-    margin-top: 2px;
-    margin-bottom: 2px;
-    image: url(:/qss_icons/rc/Vsepartoolbar.png);
-}
-
-QMainWindow::separator:vertical {
-    height: 5px;
-    margin-left: 2px;
-    margin-right: 2px;
-    image: url(:/qss_icons/rc/Hsepartoolbar.png);
-}
-
-/* QToolTip --------------------------------------------------------------- */
-
-QToolTip {
-    background-color: #148CD2;
-    border: 1px solid #19232D;
-    color: #19232D;
-    padding: 0;   /*remove padding, for fix combo box tooltip*/
-    opacity: 230; /*reducing transparency to read better*/
-}
-
-/* QStatusBar ------------------------------------------------------------- */
-
-QStatusBar {
-    border: 1px solid #32414B;
-}
-
-QStatusBar QToolTip {
-    background-color: #148CD2;
-    border: 1px solid #19232D;
-    color: #19232D;
-    padding: 0;   /*remove padding, for fix combo box tooltip*/
-    opacity: 230; /*reducing transparency to read better*/
-}
-
-/* QCheckBox -------------------------------------------------------------- */
-
-QCheckBox {
-    background-color: #19232D;
-    color: #F0F0F0;
-    spacing: 4px;
-    outline: none;
-    padding-top: 4px;
-    padding-bottom: 4px;
-}
-
-QCheckBox:focus {
-    border: none;
-}
-
-QCheckBox QWidget:disabled {
-    background-color: #19232D;
-    color: #787878;
-}
-
-QCheckBox::indicator {
-    margin-left: 4px;
-    width: 16px;
-    height: 16px;
-}
-
-QCheckBox::indicator:unchecked {
-    image: url(:/qss_icons/rc/checkbox_unchecked.png);
-}
-
-QCheckBox::indicator:unchecked:hover,
-QCheckBox::indicator:unchecked:focus,
-QCheckBox::indicator:unchecked:pressed {
-    border: none;
-    image: url(:/qss_icons/rc/checkbox_unchecked_focus.png);
-}
-
-QCheckBox::indicator:unchecked:disabled {
-    image: url(:/qss_icons/rc/checkbox_unchecked_disabled.png);
-}
-
-QCheckBox::indicator:checked {
-    image: url(:/qss_icons/rc/checkbox_checked.png);
-}
-
-QCheckBox::indicator:checked:hover,
-QCheckBox::indicator:checked:focus,
-QCheckBox::indicator:checked:pressed {
-    border: none;
-    image: url(:/qss_icons/rc/checkbox_checked_focus.png);
-}
-
-QCheckBox::indicator:checked:disabled{
-    image: url(:/qss_icons/rc/checkbox_checked_disabled.png);
-}
-
-QCheckBox::indicator:indeterminate {
-    image: url(:/qss_icons/rc/checkbox_indeterminate.png);
-}
-
-QCheckBox::indicator:indeterminate:disabled {
-    image: url(:/qss_icons/rc/checkbox_indeterminate_disabled.png);
-}
-
-QCheckBox::indicator:indeterminate:focus,
-QCheckBox::indicator:indeterminate:hover,
-QCheckBox::indicator:indeterminate:pressed {
-    image: url(:/qss_icons/rc/checkbox_indeterminate_focus.png);
-}
-
-/* QGroupBox -------------------------------------------------------------- */
-
-QGroupBox {
-    font-weight: bold;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    padding: 4px;
-    margin-top: 16px;
-}
-
-
-
-QGroupBox::title {
-    subcontrol-origin: margin;
-    subcontrol-position: top left;
-    left: 3px;
-    padding-left: 3px;
-    padding-right: 5px;
-    padding-top: 8px;
-    padding-bottom: 16px;
-}
-
-QGroupBox::indicator {
-    margin-left: 4px;
-    width: 16px;
-    height: 16px;
-}
-
-QGroupBox::indicator {
-    margin-left: 2px;
-}
-
-QGroupBox::indicator:unchecked:hover,
-QGroupBox::indicator:unchecked:focus,
-QGroupBox::indicator:unchecked:pressed {
-    border: none;
-    image: url(:/qss_icons/rc/checkbox_unchecked_focus.png);
-}
-
-QGroupBox::indicator:checked:hover,
-QGroupBox::indicator:checked:focus,
-QGroupBox::indicator:checked:pressed {
-    border: none;
-    image: url(:/qss_icons/rc/checkbox_checked_focus.png);
-}
-
-QGroupBox::indicator:checked:disabled {
-    image: url(:/qss_icons/rc/checkbox_checked_disabled.png);
-}
-
-QGroupBox::indicator:unchecked:disabled {
-    image: url(:/qss_icons/rc/checkbox_unchecked_disabled.png);
-}
-
-/* QRadioButton ----------------------------------------------------------- */
-
-QRadioButton {
-    background-color: #19232D;
-    color: #F0F0F0;
-    spacing: 0;
-    padding: 0;
-    border: none;
-    outline: none;
-}
-
-QRadioButton:focus {
-    border: none;
-}
-
-QRadioButton:disabled {
-    background-color: #19232D;
-    color: #787878;
-    border: none;
-    outline: none;
-}
-
-QRadioButton QWidget {
-    background-color: #19232D;
-    color: #F0F0F0;
-    spacing: 0px;
-    padding: 0px;
-    outline: none;
-    border: none;
-}
-
-QRadioButton::indicator {
-    border: none;
-    outline: none;
-    margin-bottom: 2px;
-    width: 25px;
-    height: 25px;
-}
-
-QRadioButton::indicator:unchecked {
-    image: url(:/qss_icons/rc/radio_unchecked.png);
-}
-
-QRadioButton::indicator:unchecked:hover,
-QRadioButton::indicator:unchecked:focus,
-QRadioButton::indicator:unchecked:pressed {
-    border: none;
-    outline: none;
-    image: url(:/qss_icons/rc/radio_unchecked_focus.png);
-}
-
-QRadioButton::indicator:checked {
-    border: none;
-    outline: none;
-    image: url(:/qss_icons/rc/radio_checked.png);
-}
-
-QRadioButton::indicator:checked:hover,
-QRadioButton::indicator:checked:focus,
-QRadioButton::indicator:checked:pressed {
-    border: none;
-    outline: none;
-    image: url(:/qss_icons/rc/radio_checked_focus.png);
-}
-
-QRadioButton::indicator:checked:disabled {
-    outline: none;
-    image: url(:/qss_icons/rc/radio_checked_disabled.png);
-}
-
-QRadioButton::indicator:unchecked:disabled {
-    image: url(:/qss_icons/rc/radio_unchecked_disabled.png);
-}
-
-/* QMenuBar --------------------------------------------------------------- */
-
-QMenuBar {
-    background-color: #32414B;
-    padding: 2px;
-    border: 1px solid #19232D;
-    color: #F0F0F0;
-}
-
-QMenuBar:focus {
-    border: 1px solid #148CD2;
-}
-
-QMenuBar::item {
-    background: transparent;
-    padding: 4px;
-}
-
-QMenuBar::item:selected {
-    padding: 4px;
-    background: transparent;
-    border: 0px solid #32414B;
-}
-
-QMenuBar::item:pressed {
-    padding: 4px;
-    border: 0px solid #32414B;
-    background-color: #148CD2;
-    color: #F0F0F0;
-    margin-bottom: 0px;
-    padding-bottom: 0px;
-}
-
-/* QMenu ------------------------------------------------------------------ */
-
-QMenu {
-    border: 0px solid #32414B;
-    color: #F0F0F0;
-    margin: 0px;
-}
-
-QMenu::separator {
-    height: 2px;
-    background-color: #505F69;
-    color: #F0F0F0;
-    padding-left: 4px;
-    margin-left: 2px;
-    margin-right: 2px;
-}
-
-QMenu::icon {
-    margin: 0px;
-    padding-left:4px;
-}
-
-QMenu::item {
-    padding: 4px 24px 4px 24px;
-    border: 1px transparent #32414B;  /* reserve space for selection border */
-}
-
-QMenu::item:selected {
-    color: #F0F0F0;
-}
-
-
-
-QMenu::indicator {
-    width: 12px;
-    height: 12px;
-    padding-left:6px;
-}
-
-/* non-exclusive indicator = check box style indicator (see QActionGroup::setExclusive) */
-
-QMenu::indicator:non-exclusive:unchecked {
-    image: url(:/qss_icons/rc/checkbox_unchecked.png);
-}
-
-QMenu::indicator:non-exclusive:unchecked:selected {
-    image: url(:/qss_icons/rc/checkbox_unchecked_disabled.png);
-}
-
-QMenu::indicator:non-exclusive:checked {
-    image: url(:/qss_icons/rc/checkbox_checked.png);
-}
-
-QMenu::indicator:non-exclusive:checked:selected {
-    image: url(:/qss_icons/rc/checkbox_checked_disabled.png);
-}
-
-/* exclusive indicator = radio button style indicator (see QActionGroup::setExclusive) */
-
-QMenu::indicator:exclusive:unchecked {
-    image: url(:/qss_icons/rc/radio_unchecked.png);
-}
-
-QMenu::indicator:exclusive:unchecked:selected {
-    image: url(:/qss_icons/rc/radio_unchecked_disabled.png);
-}
-
-QMenu::indicator:exclusive:checked {
-    image: url(:/qss_icons/rc/radio_checked.png);
-}
-
-QMenu::indicator:exclusive:checked:selected {
-    image: url(:/qss_icons/rc/radio_checked_disabled.png);
-}
-
-QMenu::right-arrow {
-    margin: 5px;
-    image: url(:/qss_icons/rc/right_arrow.png)
-}
-
-/* QAbstractItemView ------------------------------------------------------ */
-
-QAbstractItemView {
-    alternate-background-color: #19232D;
-    color: #F0F0F0;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-}
-
-QAbstractItemView QLineEdit {
-    padding: 2px;
-}
-
-/* QAbstractScrollArea ---------------------------------------------------- */
-
-QAbstractScrollArea {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    padding: 4px;
-    color: #F0F0F0;
-}
-
-QAbstractScrollArea:disabled {
-    color: #787878;
-}
-
-/* QScrollArea ------------------------------------------------------------ */
-
-QScrollArea QWidget QWidget:disabled {
-    background-color: #19232D;
-}
-
-/* QScrollBar ------------------------------------------------------------- */
-
-QScrollBar:horizontal {
-    height: 16px;
-    margin: 2px 16px 2px 16px;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    background-color: #19232D;
-}
-
-QScrollBar::handle:horizontal {
-    background-color: #787878;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    min-width: 8px;
-
-}
-
-QScrollBar::handle:horizontal:hover {
-    background-color: #148CD2;
-    border: 1px solid #148CD2;
-    border-radius: 4px;
-    min-width: 8px;
-}
-
-QScrollBar::add-line:horizontal {
-    margin: 0px 0px 0px 0px;
-    border-image: url(:/qss_icons/rc/right_arrow_disabled.png);
-    width: 10px;
-    height: 10px;
-    subcontrol-position: right;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::sub-line:horizontal {
-    margin: 0px 3px 0px 3px;
-    border-image: url(:/qss_icons/rc/left_arrow_disabled.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: left;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::add-line:horizontal:hover,
-QScrollBar::add-line:horizontal:on {
-    border-image: url(:/qss_icons/rc/right_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: right;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::sub-line:horizontal:hover,
-QScrollBar::sub-line:horizontal:on {
-    border-image: url(:/qss_icons/rc/left_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: left;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::up-arrow:horizontal,
-QScrollBar::down-arrow:horizontal {
-    background: none;
-}
-
-QScrollBar::add-page:horizontal,
-QScrollBar::sub-page:horizontal {
-    background: none;
-}
-
-QScrollBar:vertical {
-    background-color: #19232D;
-    width: 16px;
-    margin: 16px 2px 16px 2px;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-}
-
-QScrollBar::handle:vertical {
-    background-color: #787878;
-    border: 1px solid #32414B;
-    min-height: 8px;
-    border-radius: 4px;
-}
-
-QScrollBar::handle:vertical:hover {
-    background-color: #148CD2;
-    border: 1px solid #148CD2;
-    border-radius: 4px;
-    min-height: 8px;
-
-}
-
-QScrollBar::sub-line:vertical {
-    margin: 3px 0px 3px 0px;
-    border-image: url(:/qss_icons/rc/up_arrow_disabled.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: top;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::add-line:vertical {
-    margin: 3px 0px 3px 0px;
-    border-image: url(:/qss_icons/rc/down_arrow_disabled.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: bottom;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::sub-line:vertical:hover,
-QScrollBar::sub-line:vertical:on {
-    border-image: url(:/qss_icons/rc/up_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: top;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::add-line:vertical:hover,
-QScrollBar::add-line:vertical:on {
-    border-image: url(:/qss_icons/rc/down_arrow.png);
-    height: 10px;
-    width: 10px;
-    subcontrol-position: bottom;
-    subcontrol-origin: margin;
-}
-
-QScrollBar::up-arrow:vertical,
-QScrollBar::down-arrow:vertical {
-    background: none;
-}
-
-QScrollBar::add-page:vertical,
-QScrollBar::sub-page:vertical {
-    background: none;
-}
-
-/* QTextEdit--------------------------------------------------------------- */
-
-QTextEdit {
-    background-color: #19232D;
-    color: #F0F0F0;
-    border: 1px solid #32414B;
-}
-
-QTextEdit:hover {
-    border: 1px solid #148CD2;
-    color: #F0F0F0;
-}
-
-QTextEdit:selected {
-    background: #1464A0;
-    color: #32414B;
-}
-
-/* QPlainTextEdit --------------------------------------------------------- */
-
-QPlainTextEdit {
-    background-color: #19232D;
-    color: #F0F0F0;
-    border-radius: 4px;
-    border: 1px solid #32414B;
-}
-
-QPlainTextEdit:hover {
-    border: 1px solid #148CD2;
-    color: #F0F0F0;
-}
-
-QPlainTextEdit:selected {
-    background: #1464A0;
-    color: #32414B;
-}
-
-/* QSizeGrip --------------------------------------------------------------- */
-
-QSizeGrip {
-    image: url(:/qss_icons/rc/sizegrip.png);
-    width: 12px;
-    height: 12px;
-}
-
-/* QStackedWidget --------------------------------------------------------- */
-
-QStackedWidget {
-    padding: 4px;
-    border: 1px solid #32414B;
-    border: 1px solid #19232D;
-}
-
-/* QToolBar --------------------------------------------------------------- */
-
-QToolBar {
-    background-color: #32414B;
-    border-bottom: 1px solid #19232D;
-    padding: 2px;
-    font-weight: bold;
-}
-
-QToolBar QToolButton{
-    background-color: #32414B;
-}
-
-QToolBar::handle:horizontal {
-    width: 6px;
-    image: url(:/qss_icons/rc/Hmovetoolbar.png);
-}
-
-QToolBar::handle:vertical {
-    height: 6px;
-    image: url(:/qss_icons/rc/Vmovetoolbar.png);
-}
-
-QToolBar::separator:horizontal {
-    width: 3px;
-    image: url(:/qss_icons/rc/Hsepartoolbar.png);
-}
-
-QToolBar::separator:vertical {
-    height: 3px;
-    image: url(:/qss_icons/rc/Vsepartoolbar.png);
-}
-
-QToolButton#qt_toolbar_ext_button {
-    background: #32414B;
-    border: 0px;
-    color: #F0F0F0;
-    image: url(:/qss_icons/rc/right_arrow.png);
-}
-
-/* QAbstractSpinBox ------------------------------------------------------- */
-
-QAbstractSpinBox {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    padding-top: 2px;     /* This fix  103, 111*/
-    padding-bottom: 2px;  /* This fix  103, 111*/
-    padding-left: 4px;
-    padding-right: 4px;
-    border-radius: 4px;
-    /* min-width: 5px; removed to fix 109 */
-}
-
-QAbstractSpinBox:up-button {
-    background-color: transparent #19232D;
-    subcontrol-origin: border;
-    subcontrol-position: top right;
-    border-left: 1px solid #32414B;
-    margin: 1px;
-}
-
-QAbstractSpinBox::up-arrow,
-QAbstractSpinBox::up-arrow:disabled,
-QAbstractSpinBox::up-arrow:off {
-    image: url(:/qss_icons/rc/up_arrow_disabled.png);
-    width: 9px;
-    height: 9px;
-}
-
-QAbstractSpinBox::up-arrow:hover {
-    image: url(:/qss_icons/rc/up_arrow.png);
-}
-
-QAbstractSpinBox:down-button {
-    background-color: transparent #19232D;
-    subcontrol-origin: border;
-    subcontrol-position: bottom right;
-    border-left: 1px solid #32414B;
-    margin: 1px;
-}
-
-QAbstractSpinBox::down-arrow,
-QAbstractSpinBox::down-arrow:disabled,
-QAbstractSpinBox::down-arrow:off {
-    image: url(:/qss_icons/rc/down_arrow_disabled.png);
-    width: 9px;
-    height: 9px;
-}
-
-QAbstractSpinBox::down-arrow:hover {
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-QAbstractSpinBox:hover{
-    border: 1px solid #148CD2;
-    color: #F0F0F0;
-}
-
-QAbstractSpinBox:selected {
-    background: #1464A0;
-    color: #32414B;
-}
-
-/* ------------------------------------------------------------------------ */
-/* DISPLAYS --------------------------------------------------------------- */
-/* ------------------------------------------------------------------------ */
-
-/* QLabel ----------------------------------------------------------------- */
-
-QLabel {
-    background-color: #19232D;
-    border: 0px solid #32414B;
-    padding: 2px;
-    margin: 0px;
-    color: #F0F0F0
-}
-
-QLabel::disabled {
-    background-color: #19232D;
-    border: 0px solid #32414B;
-    color: #787878;
-}
-
-/* QTextBrowser ----------------------------------------------------------- */
-
-QTextBrowser {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    border-radius: 4px;
-}
-
-QTextBrowser:disabled {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #787878;
-    border-radius: 4px;
-}
-
-QTextBrowser:hover,
-QTextBrowser:!hover,
-QTextBrowser::selected,
-QTextBrowser::pressed {
-    border: 1px solid #32414B;
-}
-
-/* QGraphicsView --------------------------------------------------------- */
-
-QGraphicsView {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    border-radius: 4px;
-}
-
-QGraphicsView:disabled {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #787878;
-    border-radius: 4px;
-}
-
-QGraphicsView:hover,
-QGraphicsView:!hover,
-QGraphicsView::selected,
-QGraphicsView::pressed {
-    border: 1px solid #32414B;
-}
-
-/* QCalendarWidget -------------------------------------------------------- */
-
-QCalendarWidget {
-    border: 1px solid #32414B;
-    border-radius: 4px;
-}
-
-QCalendarWidget:disabled {
-    background-color: #19232D;
-    color: #787878;
-}
-
-/* QLCDNumber ------------------------------------------------------------- */
-
-QLCDNumber {
-    background-color: #19232D;
-    color: #F0F0F0;
-}
-
-QLCDNumber:disabled {
-    background-color: #19232D;
-    color: #787878;
-}
-
-/* QProgressBar ----------------------------------------------------------- */
-
-QProgressBar {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    border-radius: 4px;
-    text-align: center;
-}
-
-QProgressBar:disabled {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #787878;
-    border-radius: 4px;
-    text-align: center;
-}
-
-QProgressBar::chunk {
-    background-color: #1464A0;
-    color: #19232D;
-    border-radius: 4px;
-}
-
-QProgressBar::chunk:disabled {
-    background-color: #14506E;
-    color: #787878;
-    border-radius: 4px;
-}
-
-
-/* ------------------------------------------------------------------------ */
-/* BUTTONS ---------------------------------------------------------------- */
-/* ------------------------------------------------------------------------ */
-
-/* QPushButton ------------------------------------------------------------ */
-
-QPushButton {
-    background-color: #505F69 ;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    border-radius: 4px;
-    padding: 3px;
-    outline: none;
-}
-
-QPushButton:disabled {
-    background-color: #32414B;
-    border: 1px solid #32414B;
-    color: #787878;
-    border-radius: 4px;
-    padding: 3px;
-}
-
-
-QPushButton:checked {
-    background-color: #32414B;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    padding: 3px;
-    outline: none;
-}
-
-QPushButton:checked:disabled {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #787878;
-    border-radius: 4px;
-    padding: 3px;
-    outline: none;
-}
-
-QPushButton::menu-indicator {
-    subcontrol-origin: padding;
-    subcontrol-position: bottom right;
-    bottom: 4px;
-}
-
-QPushButton:pressed {
-    background-color: #19232D;
-    border: 1px solid #19232D;
-}
-
-QPushButton:hover,
-QPushButton:checked:hover{
-    border: 1px solid #148CD2;
-    color: #F0F0F0;
-}
-
-QPushButton:selected,
-QPushButton:checked:selected{
-    background: #1464A0;
-    color: #32414B;
-}
-
-/* QToolButton ------------------------------------------------------------ */
-
-QToolButton {
-    background-color: transparent;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    margin: 0px;
-    padding: 2px;
-}
-
-QToolButton:checked {
-    background-color: #19232D;
-    border: 1px solid #19232D;
-}
-
-QToolButton:disabled {
-    border: 1px solid #32414B;
-}
-
-QToolButton:hover,
-QToolButton:checked:hover{
-    border: 1px solid #148CD2;
-}
-
-/* the subcontrols below are used only in the MenuButtonPopup mode */
-
-QToolButton[popupMode="1"] {
-    padding: 2px;
-    padding-right: 12px;     /* only for MenuButtonPopup */
-    border: 1px solid #32414B;   /* make way for the popup button */
-    border-radius: 4px;
-}
-
-/* The subcontrol below is used only in the InstantPopup or DelayedPopup mode */
-
-QToolButton[popupMode="2"] {
-    padding: 2px;
-    padding-right: 12px;      /* only for InstantPopup */
-    border: 1px solid #32414B;    /* make way for the popup button */
-}
-
-QToolButton::menu-button {
-    padding: 2px;
-    border-radius: 4px;
-    border: 1px solid #32414B;
-    border-top-right-radius: 4px;
-    border-bottom-right-radius: 4px;
-    /* 16px width + 4px for border = 20px allocated above */
-    width: 16px;
-    outline: none;
-}
-
-QToolButton::menu-button:hover,
-QToolButton::menu-button:checked:hover {
-    border: 1px solid #148CD2;
-}
-
-QToolButton::menu-indicator {
-    image: url(:/qss_icons/rc/down_arrow.png);
-    top: -8px;     /* shift it a bit */
-    left: -4px;    /* shift it a bit */
-}
-
-QToolButton::menu-arrow {
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-QToolButton::menu-arrow:open {
-    border: 1px solid #32414B;
-}
-
-/* QCommandLinkButton ----------------------------------------------------- */
-
-QCommandLinkButton {
-    background-color: transparent;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    border-radius: 4px;
-    padding: 0px;
-    margin: 0px;
-}
-
-QCommandLinkButton:disabled {
-    background-color: transparent;
-    color: #787878;
-}
-
-/* ------------------------------------------------------------------------ */
-/* INPUTS - NO FIELDS ----------------------------------------------------- */
-/* ------------------------------------------------------------------------ */
-
-/* QCombobox -------------------------------------------------------------- */
-
-QComboBox {
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    selection-background-color: #1464A0;
-    padding-top: 2px;     /* This fix  #103, #111*/
-    padding-bottom: 2px;  /* This fix  #103, #111*/
-    padding-left: 4px;
-    padding-right: 4px;
-    /* min-width: 75px;  removed to fix 109 */
-}
-
-QComboBox:disabled {
-    background-color: #19232D;
-    color: #787878;
-}
-
-QComboBox:hover{
-    border: 1px solid #148CD2;
-}
-
-QComboBox:on {
-    selection-background-color: #19232D;
-}
-
-QComboBox QAbstractItemView {
-    background-color: #19232D;
-    border-radius: 4px;
-    border: 1px solid #32414B;
-    selection-color: #148CD2;
-    selection-background-color: #32414B;
-}
-
-QComboBox::drop-down {
-    subcontrol-origin: padding;
-    subcontrol-position: top right;
-    width: 20px;
-    border-left-width: 0px;
-    border-left-color: #32414B;
-    border-left-style: solid;
-    border-top-right-radius: 3px;
-    border-bottom-right-radius: 3px;
-}
-
-QComboBox::down-arrow {
-    image: url(:/qss_icons/rc/down_arrow_disabled.png);
-}
-
-QComboBox::down-arrow:on,
-QComboBox::down-arrow:hover,
-QComboBox::down-arrow:focus {
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-/* QSlider ---------------------------------------------------------------- */
-
-QSlider:disabled {
-    background: #19232D;
-}
-
-QSlider:focus {
-    border: none;
-}
-
-QSlider::groove:horizontal {
-    background: #32414B;
-    border: 1px solid #32414B;
-    height: 4px;
-    margin: 0px;
-    border-radius: 4px;
-}
-
-QSlider::sub-page:horizontal {
-    background: #1464A0;
-    border: 1px solid #32414B;
-    height: 4px;
-    margin: 0px;
-    border-radius: 4px;
-}
-
-QSlider::sub-page:horizontal:disabled {
-    background: #14506E;
-}
-
-QSlider::handle:horizontal {
-    background: #787878;
-    border: 1px solid #32414B;
-    width: 8px;
-    height: 8px;
-    margin: -8px 0;
-    border-radius: 4px;
-}
-
-QSlider::handle:horizontal:hover {
-    background: #148CD2;
-    border: 1px solid #148CD2;
-}
-
-QSlider::groove:vertical {
-    background: #32414B;
-    border: 1px solid #32414B;
-    width: 4px;
-    margin: 0px;
-    border-radius: 4px;
-}
-
-QSlider::sub-page:vertical {
-    background: #1464A0;
-    border: 1px solid #32414B;
-    width: 4px;
-    margin: 0px;
-    border-radius: 4px;
-}
-
-QSlider::sub-page:vertical:disabled {
-    background: #14506E;
-}
-
-QSlider::handle:vertical {
-    background: #787878;
-    border: 1px solid #32414B;
-    width: 8px;
-    height: 8px;
-    margin: 0 -8px;
-    border-radius: 4px;
-}
-
-QSlider::handle:vertical:hover {
-    background: #148CD2;
-    border: 1px solid #148CD2;
-}
-
-/* QLine ------------------------------------------------------------------ */
-
-QLineEdit {
-    background-color: #19232D;
-    padding-top: 2px;     /* This QLineEdit fix  103, 111 */
-    padding-bottom: 2px;  /* This QLineEdit fix  103, 111 */
-    padding-left: 4px;
-    padding-right: 4px;
-    border-style: solid;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    color: #F0F0F0;
-}
-
-QLineEdit:disabled {
-    background-color: #19232D;
-    color: #787878;
-}
-
-QLineEdit:hover{
-    border: 1px solid #148CD2;
-    color: #F0F0F0;
-}
-
-QLineEdit:selected{
-    background: #1464A0;
-    color: #32414B;
-}
-
-/* QTabWiget -------------------------------------------------------------- */
-
-QTabWidget {
-    padding: 2px;
-    selection-background-color: #32414B;
-}
-
-QTabWidget QFrame{
-    border: 0;
-}
-
-QTabWidget::pane {
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    padding: 2px;
-    margin: 0px;
-}
-
-QTabWidget::pane:selected {
-    background-color: #32414B;
-    border: 1px solid #1464A0;
-}
-
-/* QTabBar ---------------------------------------------------------------- */
-
-QTabBar {
-    qproperty-drawBase: 0;
-    border-radius: 4px;
-    margin: 0px;
-    padding: 2px;
-    border: 0;
-
-    /* left: 5px; move to the right by 5px - removed for fix */
-    }
-
-QTabBar::close-button {
-    border: 0;
-    margin: 2px;
-    padding: 0;
-    image: url(:/qss_icons/rc/close.png);
-}
-
-QTabBar::close-button:hover {
-    image: url(:/qss_icons/rc/close-hover.png);
-}
-
-QTabBar::close-button:pressed {
-    image: url(:/qss_icons/rc/close-pressed.png);
-}
-
-/* QTabBar::tab - selected ----------------------------------------------- */
-
-QTabBar::tab:top:selected:disabled {
-    border-bottom: 3px solid #14506E;
-    color: #787878;
-    background-color: #32414B;
-}
-
-QTabBar::tab:bottom:selected:disabled {
-    border-top: 3px solid #14506E;
-    color: #787878;
-    background-color: #32414B;
-}
-
-QTabBar::tab:left:selected:disabled {
-    border-left: 3px solid #14506E;
-    color: #787878;
-    background-color: #32414B;
-}
-
-QTabBar::tab:right:selected:disabled {
-    border-right: 3px solid #14506E;
-    color: #787878;
-    background-color: #32414B;
-}
-
-/* QTabBar::tab - !selected and disabled ---------------------------------- */
-
-QTabBar::tab:top:!selected:disabled {
-    border-bottom: 3px solid #19232D;
-    color: #787878;
-    background-color: #19232D;
-}
-
-QTabBar::tab:bottom:!selected:disabled {
-    border-top: 3px solid #19232D;
-    color: #787878;
-    background-color: #19232D;
-}
-
-QTabBar::tab:left:!selected:disabled {
-    border-right: 3px solid #19232D;
-    color: #787878;
-    background-color: #19232D;
-}
-
-QTabBar::tab:right:!selected:disabled {
-    border-left: 3px solid #19232D;
-    color: #787878;
-    background-color: #19232D;
-}
-
-/* QTabBar::tab - selected ----------------------------------------------- */
-
-QTabBar::tab:top:!selected {
-    border-bottom: 2px solid #19232D;
-    margin-top: 2px;
-}
-
-QTabBar::tab:bottom:!selected {
-    border-top: 2px solid #19232D;
-    margin-bottom: 3px;
-}
-
-QTabBar::tab:left:!selected {
-    border-left: 2px solid #19232D;
-    margin-right: 2px;
-}
-
-QTabBar::tab:right:!selected {
-    border-right: 2px solid #19232D;
-    margin-left: 2px;
-}
-
-
-QTabBar::tab:top {
-    background-color: #32414B;
-    color: #F0F0F0;
-    margin-left: 2px;
-    padding-left: 4px;
-    padding-right: 4px;
-    padding-top: 2px;
-    padding-bottom: 2px;
-    min-width: 5px;
-    border-bottom: 3px solid #32414B;
-    border-top-left-radius: 3px;
-    border-top-right-radius: 3px;
-}
-
-QTabBar::tab:top:selected {
-    background-color: #505F69;
-    color: #F0F0F0;
-    border-bottom: 3px solid #1464A0;
-    border-top-left-radius: 3px;
-    border-top-right-radius: 3px;
-}
-
-QTabBar::tab:top:!selected:hover {
-    border: 1px solid #148CD2;
-    border-bottom: 3px solid #148CD2;
-    padding: 0px;
-}
-
-QTabBar::tab:bottom {
-    color: #F0F0F0;
-    border-top: 3px solid #32414B;
-    background-color: #32414B;
-    margin-left: 2px;
-    padding-left: 4px;
-    padding-right: 4px;
-    padding-top: 2px;
-    padding-bottom: 2px;
-    border-bottom-left-radius: 3px;
-    border-bottom-right-radius: 3px;
-    min-width: 5px;
-}
-
-QTabBar::tab:bottom:selected {
-    color: #F0F0F0;
-    background-color: #505F69;
-    border-top: 3px solid #1464A0;
-    border-bottom-left-radius: 3px;
-    border-bottom-right-radius: 3px;
-}
-
-QTabBar::tab:bottom:!selected:hover {
-    border: 1px solid #148CD2;
-    border-top: 3px solid #148CD2;
-    padding: 0px;
-}
-
-QTabBar::tab:left {
-    color: #F0F0F0;
-    background-color: #32414B;
-    margin-top: 2px;
-    padding-left: 2px;
-    padding-right: 2px;
-    padding-top: 4px;
-    padding-bottom: 4px;
-    border-top-right-radius: 3px;
-    border-bottom-right-radius: 3px;
-    min-height: 5px;
-}
-
-QTabBar::tab:left:selected {
-    color: #F0F0F0;
-    background-color: #505F69;
-    border-left: 3px solid #1464A0;
-    border-top-right-radius: 3px;
-    border-bottom-right-radius: 3px;
-}
-
-QTabBar::tab:left:!selected:hover {
-    border: 1px solid #148CD2;
-    border-left: 3px solid #148CD2;
-    padding: 0px;
-}
-
-QTabBar::tab:right {
-    color: #F0F0F0;
-    background-color: #32414B;
-    margin-top: 2px;
-    padding-left: 2px;
-    padding-right: 2px;
-    padding-top: 4px;
-    padding-bottom: 4px;
-    border-top-left-radius: 3px;
-    border-bottom-left-radius: 3px;
-    min-height: 5px;
-}
-
-QTabBar::tab:right:selected {
-    color: #F0F0F0;
-    background-color: #505F69;
-    border-right: 3px solid #1464A0;
-    border-top-left-radius: 3px;
-    border-bottom-left-radius: 3px;
-}
-
-QTabBar::tab:right:!selected:hover {
-    border: 1px solid #148CD2;
-    border-right: 3px solid #148CD2;
-    padding: 0px;
-}
-
-QTabBar QToolButton::right-arrow:enabled {
-    image: url(:/qss_icons/rc/right_arrow.png);
-}
-
-QTabBar QToolButton::left-arrow:enabled {
-    image: url(:/qss_icons/rc/left_arrow.png);
-}
-
-QTabBar QToolButton::right-arrow:disabled {
-    image: url(:/qss_icons/rc/right_arrow_disabled.png);
-}
-
-QTabBar QToolButton::left-arrow:disabled {
-    image: url(:/qss_icons/rc/left_arrow_disabled.png);
-}
-
-
-/*  Some examples from internet to check
-
-QTabBar::tabButton() and QTabBar::tabIcon()
-QTabBar::tear {width: 0px; border: none;}
-QTabBar::tear {image: url(tear_indicator.png);}
-QTabBar::scroller{width:85pix;}
-QTabBar QToolbutton{background-color:"light blue";}
-
-But that left the buttons transparant.
-Looked confusing as the tab buttons migrated behind the scroller buttons.
-So we had to color the back ground of the scroller buttons
-*/
-
-/* QDockWiget ------------------------------------------------------------- */
-
-QDockWidget {
-    outline: 1px solid #32414B;
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    titlebar-close-icon: url(:/qss_icons/rc/close.png);
-    titlebar-normal-icon: url(:/qss_icons/rc/undock.png);
-}
-
-QDockWidget::title {
-    padding: 6px;   /* better size for title bar */
-    border: none;
-    background-color: #32414B;
-}
-
-QDockWidget::close-button {
-    background-color: #32414B;
-    border-radius: 4px;
-    border: none;
-}
-
-QDockWidget::close-button:hover {
-    border: 1px solid #32414B;
-}
-
-QDockWidget::close-button:pressed {
-    border: 1px solid #32414B;
-}
-
-QDockWidget::float-button {
-    background-color: #32414B;
-    border-radius: 4px;
-    border: none;
-}
-
-QDockWidget::float-button:hover {
-    border: 1px solid #32414B;
-}
-
-QDockWidget::float-button:pressed {
-    border: 1px solid #32414B;
-}
-
-
-/* QTreeView QTableView QListView ----------------------------------------- */
-
-QTreeView:branch:selected,
-QTreeView:branch:hover {
-    background: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:has-siblings:!adjoins-item {
-    border-image: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:has-siblings:adjoins-item {
-    border-image: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:!has-children:!has-siblings:adjoins-item {
-    border-image: url(:/qss_icons/rc/transparent.png);
-}
-
-QTreeView::branch:has-children:!has-siblings:closed,
-QTreeView::branch:closed:has-children:has-siblings {
-    image: url(:/qss_icons/rc/branch_closed.png);
-}
-
-QTreeView::branch:open:has-children:!has-siblings,
-QTreeView::branch:open:has-children:has-siblings {
-    image: url(:/qss_icons/rc/branch_open.png);
-}
-
-QTreeView::branch:has-children:!has-siblings:closed:hover,
-QTreeView::branch:closed:has-children:has-siblings:hover {
-    image: url(:/qss_icons/rc/branch_closed-on.png);
-}
-
-QTreeView::branch:open:has-children:!has-siblings:hover,
-QTreeView::branch:open:has-children:has-siblings:hover {
-    image: url(:/qss_icons/rc/branch_open-on.png);
-}
-
-QListView::item:!selected:hover,
-QTreeView::item:!selected:hover,
-QTableView::item:!selected:hover,
-QColumnView::item:!selected:hover {
-    outline: 0;
-    color: #148CD2;
-    background-color: #32414B;
-}
-
-QListView::item:selected:hover,
-QTreeView::item:selected:hover,
-QTableView::item:selected:hover,
-QColumnView::item:selected:hover {
-    background: #1464A0;
-    color:  #19232D;
-}
-
-QTreeView::indicator:checked,
-QListView::indicator:checked {
-    image: url(:/qss_icons/rc/checkbox_checked.png);
-}
-
-QTreeView::indicator:unchecked,
-QListView::indicator:unchecked {
-    image: url(:/qss_icons/rc/checkbox_unchecked.png);
-}
-
-QTreeView::indicator:checked:hover,
-QTreeView::indicator:checked:focus,
-QTreeView::indicator:checked:pressed,
-QListView::indicator:checked:hover,
-QListView::indicator:checked:focus,
-QListView::indicator:checked:pressed {
-    image: url(:/qss_icons/rc/checkbox_checked_focus.png);
-}
-
-QTreeView::indicator:unchecked:hover,
-QTreeView::indicator:unchecked:focus,
-QTreeView::indicator:unchecked:pressed,
-QListView::indicator:unchecked:hover,
-QListView::indicator:unchecked:focus,
-QListView::indicator:unchecked:pressed {
-    image: url(:/qss_icons/rc/checkbox_unchecked_focus.png);
-}
-
-QTreeView::indicator:indeterminate:hover,
-QTreeView::indicator:indeterminate:focus,
-QTreeView::indicator:indeterminate:pressed,
-QListView::indicator:indeterminate:hover,
-QListView::indicator:indeterminate:focus,
-QListView::indicator:indeterminate:pressed {
-    image: url(:/qss_icons/rc/checkbox_indeterminate_focus.png);
-}
-
-QTreeView::indicator:indeterminate,
-QListView::indicator:indeterminate {
-    image: url(:/qss_icons/rc/checkbox_indeterminate.png);
-}
-
-QListView,
-QTreeView,
-QTableView,
-QColumnView {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    gridline-color: #32414B;
-    border-radius: 4px;
-}
-
-QListView:disabled,
-QTreeView:disabled,
-QTableView:disabled,
-QColumnView:disabled {
-    background-color: #19232D;
-    color: #787878;
-}
-
-QListView:selected,
-QTreeView:selected,
-QTableView:selected,
-QColumnView:selected {
-    background: #1464A0;
-    color: #32414B;
-}
-
-QListView:hover,
-QTreeView::hover,
-QTableView::hover,
-QColumnView::hover {
-    background-color: #19232D;
-    border: 1px solid #148CD2;
-}
-
-QListView::item:pressed,
-QTreeView::item:pressed,
-QTableView::item:pressed,
-QColumnView::item:pressed {
-    background-color: #1464A0;
-}
-
-QListView::item:selected:active,
-QTreeView::item:selected:active,
-QTableView::item:selected:active,
-QColumnView::item:selected:active {
-    background-color: #1464A0;
-}
-
-QTableCornerButton::section {
-    background-color: #19232D;
-    border: 1px transparent #32414B;
-    border-radius: 0px;
-}
-
-/* QHeaderView ------------------------------------------------------------ */
-
-QHeaderView {
-    background-color: #32414B;
-    border: 0px transparent #32414B;
-    padding: 0px;
-    margin: 0px;
-    border-radius: 0px;
-}
-
-QHeaderView:disabled {
-    background-color: #32414B;
-    border: 1px transparent #32414B;
-    padding: 2px;
-}
-
-QHeaderView::section {
-    background-color: #32414B;
-    color: #F0F0F0;
-    padding: 2px;
-    border-radius: 0px;
-    text-align: left;
-}
-
-QHeaderView::section:checked {
-    color: #F0F0F0;
-    background-color: #1464A0;
-}
-
-QHeaderView::section:checked:disabled {
-    color: #787878;
-    background-color: #14506E;
-}
-
-QHeaderView::section::horizontal:disabled,
-QHeaderView::section::vertical:disabled {
-    color: #787878;
-}
-
-QHeaderView::section::vertical::first,
-QHeaderView::section::vertical::only-one {
-    border-top: 1px solid #32414B;
-}
-
-QHeaderView::section::vertical {
-    border-top: 1px solid #19232D;
-}
-
-QHeaderView::section::horizontal::first,
-QHeaderView::section::horizontal::only-one {
-    border-left: 1px solid #32414B;
-}
-
-QHeaderView::section::horizontal {
-    border-left: 1px solid #19232D;
-}
-
-/* Those settings (border/width/height/background-color) solve bug */
-/* transparent arrow background and size */
-
-QHeaderView::down-arrow {
-    background-color: #32414B;
-    width: 16px;
-    height: 16px;
-    border-right: 1px solid #19232D;
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-QHeaderView::up-arrow {
-    background-color: #32414B;
-    width: 16px;
-    height: 16px;
-    border-right: 1px solid #19232D;
-    image: url(:/qss_icons/rc/up_arrow.png);
-}
-
-/* QToolBox -------------------------------------------------------------- */
-
-QToolBox {
-    padding: 0px;
-    border: 1px solid #32414B;
-}
-
-QToolBox::selected {
-    padding: 0px;
-    border: 2px solid #1464A0;
-}
-
-QToolBox::tab {
-    background-color: #19232D;
-    border: 1px solid #32414B;
-    color: #F0F0F0;
-    border-top-left-radius: 4px;
-    border-top-right-radius: 4px;
-}
-
-QToolBox::tab:disabled {
-    color: #787878;
-}
-
-QToolBox::tab:selected {
-    background-color: #505F69;
-    border-bottom: 2px solid #1464A0;
-}
-
-QToolBox::tab:!selected {
-    background-color: #32414B;
-    border-bottom: 2px solid #32414B;
-}
-
-QToolBox::tab:selected:disabled {
-    background-color: #32414B;
-    border-bottom: 2px solid #14506E;
-}
-
-QToolBox::tab:!selected:disabled {
-    background-color: #19232D;
-}
-
-QToolBox::tab:hover {
-    border-color: #148CD2;
-    border-bottom: 2px solid #148CD2;
-}
-
-QToolBox QScrollArea QWidget QWidget {
-    padding: 0px;
-    background-color: #19232D;
-}
-
-/* QFrame ----------------------------------------------------------------- */
-
-QFrame {
-    border-radius: 4px;
-    border: 1px solid #32414B;
-}
-
-QFrame[frameShape="0"] {
-    border-radius: 4px;
-    border: 1px transparent #32414B;
-}
-
-QFrame[height="3"],
-QFrame[width="3"] {
-    background-color: #19232D;
-}
-
-/* QSplitter -------------------------------------------------------------- */
-
-QSplitter {
-    background-color: #32414B;
-    spacing: 0;
-    padding: 0;
-    margin: 0;
-}
-
-QSplitter::separator {
-    background-color: #32414B;
-    border: 0 solid #19232D;
-    spacing: 0;
-    padding: 1px;
-    margin: 0;
-}
-
-QSplitter::separator:hover {
-    background-color: #787878;
-}
-
-QSplitter::separator:horizontal {
-    width: 5px;
-    image: url(:/qss_icons/rc/Vsepartoolbar.png);
-}
-
-QSplitter::separator:vertical {
-    height: 5px;
-    image: url(:/qss_icons/rc/Hsepartoolbar.png);
-}
-
-
-/* QDateEdit-------------------------------------------------------------- */
-
-QDateEdit {
-    selection-background-color: #1464A0;
-    border-style: solid;
-    border: 1px solid #32414B;
-    border-radius: 4px;
-    padding-top: 2px;     /* This fix  #103, #111*/
-    padding-bottom: 2px;  /* This fix  #103, #111*/
-    padding-left: 4px;
-    padding-right: 4px;
-    min-width: 10px;
-}
-
-QDateEdit:on {
-    selection-background-color: #1464A0;
-}
-
-QDateEdit::drop-down {
-    subcontrol-origin: padding;
-    subcontrol-position: top right;
-    width: 20px;
-    border-top-right-radius: 3px;
-    border-bottom-right-radius: 3px;
-}
-
-QDateEdit::down-arrow {
-    image: url(:/qss_icons/rc/down_arrow_disabled.png);
-}
-
-QDateEdit::down-arrow:on,
-QDateEdit::down-arrow:hover,
-QDateEdit::down-arrow:focus {
-    image: url(:/qss_icons/rc/down_arrow.png);
-}
-
-QDateEdit QAbstractItemView {
-    background-color: #19232D;
-    border-radius: 4px;
-    border: 1px solid #32414B;
-    selection-background-color: #1464A0;
-}
-
-QAbstractView:hover{
-    border: 1px solid #148CD2;
-    color: #F0F0F0;
-}
-
-QAbstractView:selected {
-    background: #1464A0;
-    color: #32414B;
-}
-
-
diff --git a/requirements.txt b/requirements.txt
index 14e451a..8183dcf 100644
--- a/requirements.txt
+++ b/requirements.txt
@@ -2,3 +2,5 @@ pyqtgraph==0.10.0
 pandas==1.0.1
 numpy==1.17.3
 PyQt5==5.15.1
+pyuac
+pywin32
diff --git a/Simulator/BinaryEnvelopes.mo b/src/main/Simulator/BinaryEnvelopes.mo
index 590888d..590888d 100644
--- a/Simulator/BinaryEnvelopes.mo
+++ b/src/main/Simulator/BinaryEnvelopes.mo
diff --git a/Simulator/Databases/Databases.py b/src/main/Simulator/Databases/Databases.py
index d6e0b46..f6e6584 100644
--- a/Simulator/Databases/Databases.py
+++ b/src/main/Simulator/Databases/Databases.py
@@ -6,7 +6,9 @@ Created on Wed Dec 25 17:41:56 2019
 """
 
 import xml.dom.minidom
-DOMTree = xml.dom.minidom.parse("chemsep1.xml")
+import os
+current = os.path.dirname(os.path.realpath(__file__))
+DOMTree = xml.dom.minidom.parse(current+"/chemsep1.xml")
 compounds = DOMTree.documentElement
 compound = compounds.getElementsByTagName("compound")
        
diff --git a/src/main/Simulator/Databases/__pycache__/Databases.cpython-36.pyc b/src/main/Simulator/Databases/__pycache__/Databases.cpython-36.pyc
new file mode 100644
index 0000000..fd10705
--- /dev/null
+++ b/src/main/Simulator/Databases/__pycache__/Databases.cpython-36.pyc
diff --git a/src/main/Simulator/Databases/__pycache__/Databases.cpython-37.pyc b/src/main/Simulator/Databases/__pycache__/Databases.cpython-37.pyc
new file mode 100644
index 0000000..861284c
--- /dev/null
+++ b/src/main/Simulator/Databases/__pycache__/Databases.cpython-37.pyc
diff --git a/Simulator/Databases/chemsep1.xml b/src/main/Simulator/Databases/chemsep1.xml
index 547e246..547e246 100644
--- a/Simulator/Databases/chemsep1.xml
+++ b/src/main/Simulator/Databases/chemsep1.xml
diff --git a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeNRTL.mo b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeNRTL.mo
index 212e013..212e013 100644
--- a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeNRTL.mo
+++ b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeNRTL.mo
diff --git a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopePR.mo b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopePR.mo
index be47c1c..be47c1c 100644
--- a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopePR.mo
+++ b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopePR.mo
diff --git a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIFAC.mo b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIFAC.mo
index ba6ab71..ba6ab71 100644
--- a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIFAC.mo
+++ b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIFAC.mo
diff --git a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIQUAC.mo b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIQUAC.mo
index 1679004..1679004 100644
--- a/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIQUAC.mo
+++ b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/BinaryPhaseEnvelopeUNIQUAC.mo
diff --git a/Simulator/Simulator/BinaryPhaseEnvelope/package.mo b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/package.mo
index 463d7b1..463d7b1 100644
--- a/Simulator/Simulator/BinaryPhaseEnvelope/package.mo
+++ b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/package.mo
diff --git a/Simulator/Simulator/BinaryPhaseEnvelope/package.order b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/package.order
index 9e3f81f..9e3f81f 100644
--- a/Simulator/Simulator/BinaryPhaseEnvelope/package.order
+++ b/src/main/Simulator/Simulator/BinaryPhaseEnvelope/package.order
diff --git a/Simulator/Simulator/Examples/Absorption.mo b/src/main/Simulator/Simulator/Examples/Absorption.mo
index f958807..f958807 100644
--- a/Simulator/Simulator/Examples/Absorption.mo
+++ b/src/main/Simulator/Simulator/Examples/Absorption.mo
diff --git a/Simulator/Simulator/Examples/CR.mo b/src/main/Simulator/Simulator/Examples/CR.mo
index e9c755e..e9c755e 100644
--- a/Simulator/Simulator/Examples/CR.mo
+++ b/src/main/Simulator/Simulator/Examples/CR.mo
diff --git a/Simulator/Simulator/Examples/CompositeMS.mo b/src/main/Simulator/Simulator/Examples/CompositeMS.mo
index 0fdb681..0fdb681 100644
--- a/Simulator/Simulator/Examples/CompositeMS.mo
+++ b/src/main/Simulator/Simulator/Examples/CompositeMS.mo
diff --git a/Simulator/Simulator/Examples/CompoundSeparator.mo b/src/main/Simulator/Simulator/Examples/CompoundSeparator.mo
index eeec442..eeec442 100644
--- a/Simulator/Simulator/Examples/CompoundSeparator.mo
+++ b/src/main/Simulator/Simulator/Examples/CompoundSeparator.mo
diff --git a/Simulator/Simulator/Examples/Compressor.mo b/src/main/Simulator/Simulator/Examples/Compressor.mo
index c3e9e6e..c3e9e6e 100644
--- a/Simulator/Simulator/Examples/Compressor.mo
+++ b/src/main/Simulator/Simulator/Examples/Compressor.mo
diff --git a/Simulator/Simulator/Examples/Cooler.mo b/src/main/Simulator/Simulator/Examples/Cooler.mo
index e6c7af3..e6c7af3 100644
--- a/Simulator/Simulator/Examples/Cooler.mo
+++ b/src/main/Simulator/Simulator/Examples/Cooler.mo
diff --git a/Simulator/Simulator/Examples/Distillation.mo b/src/main/Simulator/Simulator/Examples/Distillation.mo
index fab504a..fab504a 100644
--- a/Simulator/Simulator/Examples/Distillation.mo
+++ b/src/main/Simulator/Simulator/Examples/Distillation.mo
diff --git a/Simulator/Simulator/Examples/EquilibriumReactor.mo b/src/main/Simulator/Simulator/Examples/EquilibriumReactor.mo
index 36f51bb..36f51bb 100644
--- a/Simulator/Simulator/Examples/EquilibriumReactor.mo
+++ b/src/main/Simulator/Simulator/Examples/EquilibriumReactor.mo
diff --git a/Simulator/Simulator/Examples/Expander.mo b/src/main/Simulator/Simulator/Examples/Expander.mo
index 28c5655..28c5655 100644
--- a/Simulator/Simulator/Examples/Expander.mo
+++ b/src/main/Simulator/Simulator/Examples/Expander.mo
diff --git a/Simulator/Simulator/Examples/Flash.mo b/src/main/Simulator/Simulator/Examples/Flash.mo
index e128397..e128397 100644
--- a/Simulator/Simulator/Examples/Flash.mo
+++ b/src/main/Simulator/Simulator/Examples/Flash.mo
diff --git a/Simulator/Simulator/Examples/HeatExchanger.mo b/src/main/Simulator/Simulator/Examples/HeatExchanger.mo
index 29fd96f..29fd96f 100644
--- a/Simulator/Simulator/Examples/HeatExchanger.mo
+++ b/src/main/Simulator/Simulator/Examples/HeatExchanger.mo
diff --git a/Simulator/Simulator/Examples/Heater.mo b/src/main/Simulator/Simulator/Examples/Heater.mo
index dd28183..dd28183 100644
--- a/Simulator/Simulator/Examples/Heater.mo
+++ b/src/main/Simulator/Simulator/Examples/Heater.mo
diff --git a/Simulator/Simulator/Examples/MaterialStream.mo b/src/main/Simulator/Simulator/Examples/MaterialStream.mo
index 73d749c..73d749c 100644
--- a/Simulator/Simulator/Examples/MaterialStream.mo
+++ b/src/main/Simulator/Simulator/Examples/MaterialStream.mo
diff --git a/Simulator/Simulator/Examples/Mixer.mo b/src/main/Simulator/Simulator/Examples/Mixer.mo
index 1f4b19c..1f4b19c 100644
--- a/Simulator/Simulator/Examples/Mixer.mo
+++ b/src/main/Simulator/Simulator/Examples/Mixer.mo
diff --git a/Simulator/Simulator/Examples/PFR.mo b/src/main/Simulator/Simulator/Examples/PFR.mo
index b89f5f4..b89f5f4 100644
--- a/Simulator/Simulator/Examples/PFR.mo
+++ b/src/main/Simulator/Simulator/Examples/PFR.mo
diff --git a/Simulator/Simulator/Examples/Pump.mo b/src/main/Simulator/Simulator/Examples/Pump.mo
index 939ab5a..939ab5a 100644
--- a/Simulator/Simulator/Examples/Pump.mo
+++ b/src/main/Simulator/Simulator/Examples/Pump.mo
diff --git a/Simulator/Simulator/Examples/ShortcutColumn.mo b/src/main/Simulator/Simulator/Examples/ShortcutColumn.mo
index ebcd218..ebcd218 100644
--- a/Simulator/Simulator/Examples/ShortcutColumn.mo
+++ b/src/main/Simulator/Simulator/Examples/ShortcutColumn.mo
diff --git a/Simulator/Simulator/Examples/Splitter.mo b/src/main/Simulator/Simulator/Examples/Splitter.mo
index cd39347..cd39347 100644
--- a/Simulator/Simulator/Examples/Splitter.mo
+++ b/src/main/Simulator/Simulator/Examples/Splitter.mo
diff --git a/Simulator/Simulator/Examples/Valve.mo b/src/main/Simulator/Simulator/Examples/Valve.mo
index a1f3766..a1f3766 100644
--- a/Simulator/Simulator/Examples/Valve.mo
+++ b/src/main/Simulator/Simulator/Examples/Valve.mo
diff --git a/Simulator/Simulator/Examples/package.mo b/src/main/Simulator/Simulator/Examples/package.mo
index 8be84f5..8be84f5 100644
--- a/Simulator/Simulator/Examples/package.mo
+++ b/src/main/Simulator/Simulator/Examples/package.mo
diff --git a/Simulator/Simulator/Examples/package.order b/src/main/Simulator/Simulator/Examples/package.order
index 7e198d6..7e198d6 100644
--- a/Simulator/Simulator/Examples/package.order
+++ b/src/main/Simulator/Simulator/Examples/package.order
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acenaphthene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acenaphthene.mo
index 9eaf293..9eaf293 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acenaphthene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acenaphthene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acetaldehyde.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetaldehyde.mo
index 2dfb3e9..2dfb3e9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acetaldehyde.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetaldehyde.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Aceticacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Aceticacid.mo
index 33cadcf..33cadcf 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Aceticacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Aceticacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Aceticanhydride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Aceticanhydride.mo
index 6218d86..6218d86 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Aceticanhydride.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Aceticanhydride.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acetone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetone.mo
index 81c392a..81c392a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acetone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acetonitrile.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetonitrile.mo
index 767102b..767102b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acetonitrile.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetonitrile.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acetylchloride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetylchloride.mo
index 4b14708..4b14708 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acetylchloride.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetylchloride.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acetylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetylene.mo
index 9991dc1..9991dc1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acetylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acetylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acrylicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acrylicacid.mo
index f8f90b4..f8f90b4 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acrylicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acrylicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Acrylonitrile.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acrylonitrile.mo
index 558c0c3..558c0c3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Acrylonitrile.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Acrylonitrile.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Adipicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Adipicacid.mo
index 09b05d3..09b05d3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Adipicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Adipicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Air.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Air.mo
index 2b397f4..2b397f4 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Air.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Air.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ammonia.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ammonia.mo
index 055eefc..055eefc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ammonia.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ammonia.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Aniline.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Aniline.mo
index 9ea052b..9ea052b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Aniline.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Aniline.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Anisole.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Anisole.mo
index 8628dc6..8628dc6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Anisole.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Anisole.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Argon.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Argon.mo
index 3241716..3241716 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Argon.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Argon.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Benzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Benzene.mo
index 73a5082..73a5082 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Benzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Benzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Benzoicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Benzoicacid.mo
index 561a8a9..561a8a9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Benzoicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Benzoicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Biphenyl.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Biphenyl.mo
index 1aa21e6..1aa21e6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Biphenyl.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Biphenyl.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Bromine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Bromine.mo
index 1503635..1503635 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Bromine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Bromine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Bromobenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Bromobenzene.mo
index 7d9ec50..7d9ec50 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Bromobenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Bromobenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Butanal.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Butanal.mo
index 2c2a578..2c2a578 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Butanal.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Butanal.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Butylvinylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Butylvinylether.mo
index 592ef17..592ef17 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Butylvinylether.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Butylvinylether.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Carbondioxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbondioxide.mo
index 21e9927..21e9927 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Carbondioxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbondioxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Carbondisulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbondisulfide.mo
index 020c77b..020c77b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Carbondisulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbondisulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Carbonmonoxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbonmonoxide.mo
index 306c5c8..306c5c8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Carbonmonoxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbonmonoxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Carbontetrachloride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbontetrachloride.mo
index 262543d..262543d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Carbontetrachloride.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbontetrachloride.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Carbonylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbonylsulfide.mo
index 8c50c86..8c50c86 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Carbonylsulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Carbonylsulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Chlorine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Chlorine.mo
index f097352..f097352 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Chlorine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Chlorine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Chloroform.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Chloroform.mo
index 4f21713..4f21713 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Chloroform.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Chloroform.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Chrysene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Chrysene.mo
index d35c72d..d35c72d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Chrysene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Chrysene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisOneFourdimethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisOneFourdimethylcyclohexane.mo
index c0e931f..c0e931f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisOneFourdimethylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisOneFourdimethylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisOneThreedimethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisOneThreedimethylcyclohexane.mo
index 4b17200..4b17200 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisOneThreedimethylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisOneThreedimethylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisOneThreedimethylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisOneThreedimethylcyclopentane.mo
index 0fae579..0fae579 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisOneThreedimethylcyclopentane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisOneTwodimethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisOneTwodimethylcyclohexane.mo
index bea2d5b..bea2d5b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisOneTwodimethylcyclohexane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisOneTwodimethylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisOneTwodimethylcyclopentane.mo
index 60002c2..60002c2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisOneTwodimethylcyclopentane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisTwobutene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisTwobutene.mo
index 9bd8d97..9bd8d97 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisTwobutene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisTwobutene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisTwohexene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisTwohexene.mo
index 9a146b2..9a146b2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisTwohexene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisTwohexene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/CisTwopentene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisTwopentene.mo
index 8a535f1..8a535f1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/CisTwopentene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/CisTwopentene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cisdecahydronaphthalene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cisdecahydronaphthalene.mo
index b5e9e47..b5e9e47 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cisdecahydronaphthalene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cisdecahydronaphthalene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cumene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cumene.mo
index a8b9af8..a8b9af8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cumene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cumene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cumenehydroperoxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cumenehydroperoxide.mo
index 6eb1e89..6eb1e89 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cumenehydroperoxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cumenehydroperoxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cyclobutane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclobutane.mo
index 3608bfc..3608bfc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cyclobutane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclobutane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexane.mo
index 518f5b7..518f5b7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanol.mo
index bad1870..bad1870 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanone.mo
index 1c791b1..1c791b1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexanone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexene.mo
index 10208f1..10208f1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclohexene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Cyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclopentane.mo
index 12394f3..12394f3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Cyclopentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Cyclopentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/DiButylCarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/DiButylCarbonate.mo
index ae5d2ab..ae5d2ab 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/DiButylCarbonate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/DiButylCarbonate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/DiEthylCarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/DiEthylCarbonate.mo
index 571b504..571b504 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/DiEthylCarbonate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/DiEthylCarbonate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/DiPhenylCarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/DiPhenylCarbonate.mo
index 407a754..407a754 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/DiPhenylCarbonate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/DiPhenylCarbonate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetaldehyde.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetaldehyde.mo
index 13877e8..13877e8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetaldehyde.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetaldehyde.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetylchloride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetylchloride.mo
index 915e539..915e539 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetylchloride.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dichloroacetylchloride.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dicyclopentadiene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dicyclopentadiene.mo
index 618e864..618e864 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dicyclopentadiene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dicyclopentadiene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethanolamine.mo
index 46bcf60..46bcf60 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethanolamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethanolamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethylamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylamine.mo
index d5e23cc..d5e23cc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethylamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethyldisulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethyldisulfide.mo
index 98ec750..98ec750 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethyldisulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethyldisulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethyleneglycol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethyleneglycol.mo
index 816243e..816243e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethyleneglycol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethyleneglycol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethylenetriamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylenetriamine.mo
index 36c1b7b..36c1b7b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethylenetriamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylenetriamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethylethanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylethanolamine.mo
index de1fbfd..de1fbfd 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethylethanolamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylethanolamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylether.mo
index 25ae98d..25ae98d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethylether.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylether.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diethylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylsulfide.mo
index a7076ed..a7076ed 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diethylsulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diethylsulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diisobutylketone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisobutylketone.mo
index 65a2e4f..65a2e4f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diisobutylketone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisobutylketone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropanolamine.mo
index aedf05f..aedf05f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropanolamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropanolamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylamine.mo
index 626097d..626097d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylether.mo
index 8e41855..8e41855 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylether.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylether.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylketone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylketone.mo
index eba753f..eba753f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylketone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diisopropylketone.mo
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index 4c994c1..4c994c1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylacetylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylacetylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylcarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylcarbonate.mo
index 364855c..364855c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylcarbonate.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dimethyldisulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethyldisulfide.mo
index 35fe9e2..35fe9e2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethyldisulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethyldisulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylethanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylethanolamine.mo
index 2ee7c08..2ee7c08 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylethanolamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylethanolamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylether.mo
index de11e5f..de11e5f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylether.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylether.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfide.mo
index c8b4829..c8b4829 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfoxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfoxide.mo
index 379d1a9..379d1a9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfoxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylsulfoxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylterephthalate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylterephthalate.mo
index 5bc9beb..5bc9beb 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dimethylterephthalate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dimethylterephthalate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dinbutylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dinbutylether.mo
index 2299125..2299125 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dinbutylether.mo
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index bc8597c..bc8597c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dinpropyldisulfide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Dinpropylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dinpropylsulfide.mo
index 2ee51fc..2ee51fc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Dinpropylsulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Dinpropylsulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Diphenyldisulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Diphenyldisulfide.mo
index 54ea3fe..54ea3fe 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Diphenyldisulfide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Disecbutylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Disecbutylether.mo
index 9dc1a65..9dc1a65 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Disecbutylether.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ditertbutyldisulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ditertbutyldisulfide.mo
index a97b481..a97b481 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ditertbutyldisulfide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethane.mo
index 40dc07a..40dc07a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethanol.mo
index a579c60..a579c60 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethanol.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/EthylPhenylCarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/EthylPhenylCarbonate.mo
index 18fc5ce..18fc5ce 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/EthylPhenylCarbonate.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylacetate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylacetate.mo
index 35001f3..35001f3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylacetate.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylacetylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylacetylene.mo
index f88fa8f..f88fa8f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylacetylene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylamine.mo
index e7bc131..e7bc131 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylamine.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylbenzene.mo
index 46dd319..46dd319 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylbenzene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylchloride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylchloride.mo
index 3b740d4..3b740d4 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylchloride.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylcyclohexane.mo
index e16085d..e16085d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylcyclohexane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylcyclopentane.mo
index ca2f5a3..ca2f5a3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylcyclopentane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylene.mo
index de776b0..de776b0 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylenecarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylenecarbonate.mo
index adafe6d..adafe6d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylenecarbonate.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylenediamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylenediamine.mo
index a550252..a550252 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylenediamine.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethyleneglycol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethyleneglycol.mo
index f82bc3a..f82bc3a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethyleneglycol.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethyleneoxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethyleneoxide.mo
index 5e897ef..5e897ef 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethyleneoxide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylformate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylformate.mo
index 59275e0..59275e0 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylformate.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylmercaptan.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylmercaptan.mo
index 5a445b2..5a445b2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylmercaptan.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylmethyldisulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylmethyldisulfide.mo
index 2fc4c0c..2fc4c0c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylmethyldisulfide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethylpropyldisulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethylpropyldisulfide.mo
index c8cbe38..c8cbe38 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethylpropyldisulfide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ethyltertpentylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ethyltertpentylether.mo
index d765062..d765062 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ethyltertpentylether.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/FivemethylTwohexanone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/FivemethylTwohexanone.mo
index 70c5587..70c5587 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/FivemethylTwohexanone.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fivemethylnonane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fivemethylnonane.mo
index 562f228..562f228 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fluoranthene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fluoranthene.mo
index 336cf45..336cf45 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fluorene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fluorene.mo
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--- a/Simulator/Simulator/Files/ChemsepDatabase/Fluorene.mo
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index f0be735..f0be735 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fourethylmxylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fourethylmxylene.mo
index 0cbf032..0cbf032 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Fourethylmxylene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fourethyloxylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fourethyloxylene.mo
index d8e670d..d8e670d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Fourethyloxylene.mo
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index a6318e7..a6318e7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Fourheptanone.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/FourmethylcisTwopentene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/FourmethylcisTwopentene.mo
index 4e0964f..4e0964f 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fourmethylheptane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fourmethylheptane.mo
index 07a85b5..07a85b5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Fourmethylheptane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fourmethylnonane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fourmethylnonane.mo
index c2c4a1f..c2c4a1f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Fourmethylnonane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Fourmethyloctane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Fourmethyloctane.mo
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--- a/Simulator/Simulator/Files/ChemsepDatabase/Fourmethyloctane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/FourmethyltransTwopentene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/FourmethyltransTwopentene.mo
index 554e90b..554e90b 100644
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index 3db0b42..3db0b42 100644
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index ffb7889..ffb7889 100644
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index 8117a99..8117a99 100644
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index 21e8fdf..21e8fdf 100644
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index c62806f..c62806f 100644
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index 87bf5d6..87bf5d6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Hydrogenchloride.mo
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index 60700e3..60700e3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Hydrogencyanide.mo
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index 1a896fd..1a896fd 100644
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index c810e25..c810e25 100644
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index 7e08ab6..7e08ab6 100644
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index 5205512..5205512 100644
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index 850f478..850f478 100644
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index 64dc9b6..64dc9b6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Isobutylbenzene.mo
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index 16d2964..16d2964 100644
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index 8987f12..8987f12 100644
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index 7e155cd..7e155cd 100644
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index 0e6bec3..0e6bec3 100644
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index 8ce488e..8ce488e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Isopropylbutylether.mo
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index b5e316d..b5e316d 100644
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index 841c729..841c729 100644
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index c6b5aa8..c6b5aa8 100644
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index 00ea733..00ea733 100644
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index c349169..c349169 100644
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index c7984d4..c7984d4 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Mdichlorobenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mdichlorobenzene.mo
index 07a1bb0..07a1bb0 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Mdichlorobenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mdichlorobenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Mdiethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mdiethylbenzene.mo
index 010b0fa..010b0fa 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Mdiethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mdiethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Mesitylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mesitylene.mo
index ef633f8..ef633f8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Mesitylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mesitylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methacrylicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methacrylicacid.mo
index 422ddb4..422ddb4 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methacrylicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methacrylicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methacrylonitrile.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methacrylonitrile.mo
index 5c93234..5c93234 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methacrylonitrile.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methacrylonitrile.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methane.mo
index 243a9e1..243a9e1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methanol.mo
index b8a9f21..b8a9f21 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/MethylDiEthanolAmine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/MethylDiEthanolAmine.mo
index 05309ce..05309ce 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/MethylDiEthanolAmine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/MethylDiEthanolAmine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/MethylEthylCarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/MethylEthylCarbonate.mo
index 00c84fa..00c84fa 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/MethylEthylCarbonate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/MethylEthylCarbonate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/MethylPhenylCarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/MethylPhenylCarbonate.mo
index 7a7626a..7a7626a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/MethylPhenylCarbonate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/MethylPhenylCarbonate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylacetate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylacetate.mo
index 0031373..0031373 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylacetate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylacetate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylacetylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylacetylene.mo
index aafab53..aafab53 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylacetylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylacetylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylal.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylal.mo
index c963f49..c963f49 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylal.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylal.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylamine.mo
index e7057fb..e7057fb 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylchloride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylchloride.mo
index fdf9c0e..fdf9c0e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylchloride.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylchloride.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylcyclohexane.mo
index a00ae9e..a00ae9e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylcyclopentane.mo
index 1870844..1870844 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylcyclopentane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylethanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylethanolamine.mo
index 85484b6..85484b6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylethanolamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylethanolamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylethylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylethylether.mo
index 91bfc74..91bfc74 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylethylether.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylethylketone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylethylketone.mo
index 7504498..7504498 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylethylketone.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylethylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylethylsulfide.mo
index 8cfc9eb..8cfc9eb 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylethylsulfide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylformate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylformate.mo
index eabf212..eabf212 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylformate.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methyliodide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyliodide.mo
index 8a69e97..8a69e97 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methyliodide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylisobutylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylisobutylether.mo
index 7f3ed92..7f3ed92 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylisobutylether.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylisobutylketone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylisobutylketone.mo
index caa4c39..caa4c39 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylisobutylketone.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylisopropylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylisopropylether.mo
index 385e46b..385e46b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylisopropylether.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylisopropylketone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylisopropylketone.mo
index 0f4e085..0f4e085 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylisopropylketone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylisopropylketone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylmercaptan.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylmercaptan.mo
index 2974755..2974755 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylmercaptan.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylmethacrylate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylmethacrylate.mo
index bb79c4d..bb79c4d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylmethacrylate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylmethacrylate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylnpropylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylnpropylether.mo
index bfb965f..bfb965f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylnpropylether.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylnpropylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylnpropylsulfide.mo
index 747e29e..747e29e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylnpropylsulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylnpropylsulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methylpropionate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylpropionate.mo
index 227651d..227651d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methylpropionate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methylpropionate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methyltbutylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltbutylsulfide.mo
index ca44e24..ca44e24 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methyltbutylsulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltbutylsulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methyltertbutylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltertbutylether.mo
index 322e3f9..322e3f9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methyltertbutylether.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltertbutylether.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methyltertpentylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltertpentylether.mo
index 4bf09de..4bf09de 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methyltertpentylether.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltertpentylether.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methyltoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltoluene.mo
index 4b0f5ca..4b0f5ca 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methyltoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Methyltpentylsulfide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltpentylsulfide.mo
index e56820e..e56820e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Methyltpentylsulfide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Methyltpentylsulfide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Mnitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mnitrotoluene.mo
index 1f0209b..1f0209b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Mnitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mnitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Monochlorobenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Monochlorobenzene.mo
index cd756a9..cd756a9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Monochlorobenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Monochlorobenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Monoethanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Monoethanolamine.mo
index 32a078d..32a078d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Monoethanolamine.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Mxylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mxylene.mo
index 67e1aa1..67e1aa1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Mxylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Mxylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Naminoethylethanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Naminoethylethanolamine.mo
index 8a2133a..8a2133a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Naminoethylethanolamine.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Naminoethylpiperazine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Naminoethylpiperazine.mo
index 073fb91..073fb91 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Naminoethylpiperazine.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Naphthalene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Naphthalene.mo
index cfb53bc..cfb53bc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Naphthalene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nbutane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutane.mo
index 69d6a45..69d6a45 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nbutane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nbutylacetate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutylacetate.mo
index 2dfd14a..2dfd14a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nbutylacetate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutylacetate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nbutylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutylbenzene.mo
index b4359a1..b4359a1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nbutylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nbutylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutylcyclohexane.mo
index 14bf8ee..14bf8ee 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nbutylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutylcyclohexane.mo
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index 1d3a35d..1d3a35d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nbutylcyclopentane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nbutyricacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nbutyricacid.mo
index 4101cd1..4101cd1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nbutyricacid.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ndecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ndecane.mo
index 75d986c..75d986c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ndecane.mo
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index c940ae2..c940ae2 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ndodecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ndodecane.mo
index 5940462..5940462 100644
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index 1b87710..1b87710 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Neicosane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Neon.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Neon.mo
index 7646be5..7646be5 100644
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index 15ef270..15ef270 100644
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index 56e4525..56e4525 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nheptadecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nheptadecane.mo
index bd752e7..bd752e7 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nheptane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nheptane.mo
index e43fcdf..e43fcdf 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nhexacosane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nhexacosane.mo
index 5ef8184..5ef8184 100644
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index a9c0eb3..a9c0eb3 100644
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nhexane.mo
index 8c93e2b..8c93e2b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nhexane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nhexylacetate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nhexylacetate.mo
index fd6d2d6..fd6d2d6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nhexylacetate.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nhexylmercaptan.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nhexylmercaptan.mo
index 4c993d2..4c993d2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nhexylmercaptan.mo
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index 975802c..975802c 100644
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index 5dda407..5dda407 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitricoxide.mo
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index 1e5aaaf..1e5aaaf 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitrobenzene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nitroethane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitroethane.mo
index 599836b..599836b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitroethane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitroethane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogen.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogen.mo
index 9307612..9307612 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogen.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogen.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogendioxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogendioxide.mo
index ef4f943..ef4f943 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogendioxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogendioxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentetroxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentetroxide.mo
index f5436ef..f5436ef 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentetroxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentetroxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentrioxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentrioxide.mo
index 50408ca..50408ca 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentrioxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrogentrioxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nitromethane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitromethane.mo
index 0a35893..0a35893 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitromethane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitromethane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nitrousoxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrousoxide.mo
index d1fa2c7..d1fa2c7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nitrousoxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nitrousoxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylacetamide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylacetamide.mo
index 2076137..2076137 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylacetamide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylacetamide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylformamide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylformamide.mo
index e53a885..e53a885 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylformamide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nndimethylformamide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nnonacosane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nnonacosane.mo
index 44bf7be..44bf7be 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nnonacosane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nnonacosane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nnonadecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nnonadecane.mo
index 83570d1..83570d1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nnonadecane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nnonadecane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nnonane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nnonane.mo
index 30d8613..30d8613 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nnonane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nnonane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Noctacosane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Noctacosane.mo
index b958679..b958679 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Noctacosane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Noctacosane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Noctadecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Noctadecane.mo
index 3319b94..3319b94 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Noctadecane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Noctadecane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Noctane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Noctane.mo
index 46a955d..46a955d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Noctane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Noctane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npentacosane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentacosane.mo
index ee96957..ee96957 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npentacosane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentacosane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npentadecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentadecane.mo
index 61ff718..61ff718 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npentadecane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentadecane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentane.mo
index 3bb71b8..3bb71b8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npentylacetate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentylacetate.mo
index 0fcb9dc..0fcb9dc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npentylacetate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npentylacetate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npropylacetate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylacetate.mo
index def17c0..def17c0 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npropylacetate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylacetate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npropylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylbenzene.mo
index b5b16c6..b5b16c6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npropylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclohexane.mo
index 32e7163..32e7163 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclopentane.mo
index 72dd7ef..72dd7ef 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclopentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylcyclopentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npropylformate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylformate.mo
index 08182bc..08182bc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npropylformate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylformate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Npropylmercaptan.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylmercaptan.mo
index 9943133..9943133 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Npropylmercaptan.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Npropylmercaptan.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ntetracosane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntetracosane.mo
index 6de997b..6de997b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ntetracosane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntetracosane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ntetradecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntetradecane.mo
index b4b83f5..b4b83f5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ntetradecane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntetradecane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ntricosane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntricosane.mo
index 3309bf9..3309bf9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ntricosane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntricosane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ntridecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntridecane.mo
index 3f6ed9f..3f6ed9f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ntridecane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ntridecane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Nundecane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nundecane.mo
index 0cba17f..0cba17f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Nundecane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Nundecane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ocresol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ocresol.mo
index 9d6b6f8..9d6b6f8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ocresol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ocresol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ocymene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ocymene.mo
index 44dec09..44dec09 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ocymene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ocymene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Odichlorobenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Odichlorobenzene.mo
index 4ad7a9b..4ad7a9b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Odichlorobenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Odichlorobenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Odiethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Odiethylbenzene.mo
index 8b57d56..8b57d56 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Odiethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Odiethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oethyltoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oethyltoluene.mo
index 5cd133c..5cd133c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oethyltoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oethyltoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneFourbutanediol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneFourbutanediol.mo
index 39d501d..39d501d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneFourbutanediol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneFourbutanediol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneFourdioxane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneFourdioxane.mo
index 3e03ca9..3e03ca9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneFourdioxane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneFourdioxane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneOneTwotrichloroethane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOneTwotrichloroethane.mo
index 02a3601..02a3601 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneOneTwotrichloroethane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOneTwotrichloroethane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneOnedichloroethane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOnedichloroethane.mo
index b1c0ee8..b1c0ee8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneOnedichloroethane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOnedichloroethane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclohexane.mo
index 9ee60ce..9ee60ce 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclopentane.mo
index 0456ca3..0456ca3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclopentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneOnedimethylcyclopentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneThreebutadiene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneThreebutadiene.mo
index 6e36414..6e36414 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneThreebutadiene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneThreebutadiene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourFivetetramethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourFivetetramethylbenzene.mo
index b015054..b015054 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourFivetetramethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourFivetetramethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrichlorobenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrichlorobenzene.mo
index 98c07ba..98c07ba 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrichlorobenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrichlorobenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrimethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrimethylbenzene.mo
index 5d0bfdf..5d0bfdf 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrimethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoFourtrimethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFivetetramethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFivetetramethylbenzene.mo
index 5b816f0..5b816f0 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFivetetramethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFivetetramethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFourtetramethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFourtetramethylbenzene.mo
index 02c7769..02c7769 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFourtetramethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreeFourtetramethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreetrimethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreetrimethylbenzene.mo
index fb73be8..fb73be8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreetrimethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwoThreetrimethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwobutadiene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwobutadiene.mo
index 01253e9..01253e9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwobutadiene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwobutadiene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwodichloroethane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwodichloroethane.mo
index 9ffd6e9..9ffd6e9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwodichloroethane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwodichloroethane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OneTwopropyleneoxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwopropyleneoxide.mo
index 4c71ffc..4c71ffc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OneTwopropyleneoxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OneTwopropyleneoxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onebutanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onebutanol.mo
index ec9e3d6..ec9e3d6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onebutanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onebutanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onebutene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onebutene.mo
index a9c09ba..a9c09ba 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onebutene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onebutene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oneheptanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneheptanol.mo
index f9eb7f2..f9eb7f2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oneheptanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneheptanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oneheptene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneheptene.mo
index 28725a9..28725a9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oneheptene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneheptene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onehexanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onehexanol.mo
index cc02ddd..cc02ddd 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onehexanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onehexanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onehexene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onehexene.mo
index 866627d..866627d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onehexene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onehexene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OnemethylFournpropylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OnemethylFournpropylbenzene.mo
index 12cd40c..12cd40c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OnemethylFournpropylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OnemethylFournpropylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OnemethylOneethylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OnemethylOneethylcyclopentane.mo
index ea6203c..ea6203c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OnemethylOneethylcyclopentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OnemethylOneethylcyclopentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/OnemethylThreenpropylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OnemethylThreenpropylbenzene.mo
index 8fee3bb..8fee3bb 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/OnemethylThreenpropylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/OnemethylThreenpropylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onemethylindene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onemethylindene.mo
index 182dbbb..182dbbb 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onemethylindene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onemethylindene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onemethylnaphthalene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onemethylnaphthalene.mo
index a52d2e1..a52d2e1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onemethylnaphthalene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onemethylnaphthalene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onenitrobutane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onenitrobutane.mo
index 33d160e..33d160e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onenitrobutane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onenitrobutane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onenitropropane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onenitropropane.mo
index 1c2f8c9..1c2f8c9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onenitropropane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onenitropropane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onenonene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onenonene.mo
index 4e35cee..4e35cee 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onenonene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onenonene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oneoctene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneoctene.mo
index 50b5541..50b5541 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oneoctene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneoctene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onepentanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onepentanol.mo
index ddab692..ddab692 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onepentanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onepentanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onepentene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onepentene.mo
index 08c50da..08c50da 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onepentene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onepentene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onephenylnaphthalene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onephenylnaphthalene.mo
index c8ba09f..c8ba09f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onephenylnaphthalene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onephenylnaphthalene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onepropanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onepropanol.mo
index 9f4362f..9f4362f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onepropanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onepropanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oneundecene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneundecene.mo
index a4b95fd..a4b95fd 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oneundecene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oneundecene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Onitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onitrotoluene.mo
index 43bc7a7..43bc7a7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Onitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Onitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Otoluicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Otoluicacid.mo
index 11415df..11415df 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Otoluicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Otoluicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oxalicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oxalicacid.mo
index 480d8c3..480d8c3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oxalicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oxalicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oxygen.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oxygen.mo
index 6b7214b..6b7214b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oxygen.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oxygen.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Oxylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oxylene.mo
index b8c30e1..b8c30e1 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Oxylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Oxylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ozone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ozone.mo
index c3cecfc..c3cecfc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ozone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ozone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pcresol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pcresol.mo
index 0ca548c..0ca548c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pcresol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pcresol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pcymene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pcymene.mo
index fbf9a9d..fbf9a9d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pcymene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pcymene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pdichlorobenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pdichlorobenzene.mo
index f2b6c3c..f2b6c3c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pdichlorobenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pdichlorobenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pdiethylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pdiethylbenzene.mo
index 1901268..1901268 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pdiethylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pdiethylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pdiisopropylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pdiisopropylbenzene.mo
index f65d202..f65d202 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pdiisopropylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pdiisopropylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pentanal.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pentanal.mo
index 9efbbc4..9efbbc4 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pentanal.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pentanal.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pethyltoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pethyltoluene.mo
index 4dd8eb2..4dd8eb2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pethyltoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pethyltoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Phenanthrene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phenanthrene.mo
index d8ece64..d8ece64 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Phenanthrene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phenanthrene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Phenol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phenol.mo
index 02830f2..02830f2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Phenol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phenol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Phosgene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phosgene.mo
index 57e5b1e..57e5b1e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Phosgene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phosgene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Phthalicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phthalicacid.mo
index 09872f2..09872f2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Phthalicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Phthalicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Piperazine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Piperazine.mo
index d9c6ab7..d9c6ab7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Piperazine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Piperazine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pnitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pnitrotoluene.mo
index 0b0d219..0b0d219 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pnitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pnitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pphenylenediamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pphenylenediamine.mo
index 4ae8d9d..4ae8d9d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pphenylenediamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pphenylenediamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Propadiene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propadiene.mo
index 37723c3..37723c3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Propadiene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propadiene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Propanal.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propanal.mo
index 9c32f53..9c32f53 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Propanal.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Propane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propane.mo
index b7853f5..b7853f5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Propane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Propionicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propionicacid.mo
index 5b5ef8c..5b5ef8c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Propionicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propionicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Propionitrile.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propionitrile.mo
index 65f59f3..65f59f3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Propionitrile.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Propylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propylene.mo
index eb70cfe..eb70cfe 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Propylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Propylenecarbonate.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propylenecarbonate.mo
index 5a8fc57..5a8fc57 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Propylenecarbonate.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Propylenecarbonate.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Ptoluicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Ptoluicacid.mo
index aa17309..aa17309 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Ptoluicacid.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pxylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pxylene.mo
index cdca150..cdca150 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pxylene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pyrene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pyrene.mo
index 17a8a18..17a8a18 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pyrene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Pyridine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Pyridine.mo
index ee8911c..ee8911c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Pyridine.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Salicylicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Salicylicacid.mo
index 8f98ddc..8f98ddc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Salicylicacid.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Salicylicacid.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Secbutylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Secbutylbenzene.mo
index 1c57c49..1c57c49 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Secbutylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Secbutylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Secbutylmercaptan.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Secbutylmercaptan.mo
index 003d873..003d873 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Secbutylmercaptan.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Secbutylmercaptan.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Squalane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Squalane.mo
index d9c7436..d9c7436 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Squalane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Styrene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Styrene.mo
index 0ede9ff..0ede9ff 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Styrene.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Sulfolane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Sulfolane.mo
index 536aa84..536aa84 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Sulfolane.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Sulfurdioxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Sulfurdioxide.mo
index 4415dda..4415dda 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Sulfurdioxide.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Sulfurhexafluoride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Sulfurhexafluoride.mo
index 31d178d..31d178d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Sulfurhexafluoride.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Sulfurtrioxide.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Sulfurtrioxide.mo
index 67b2a75..67b2a75 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Sulfurtrioxide.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Sulfurtrioxide.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Terephthalicacid.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Terephthalicacid.mo
index 104abc7..104abc7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Terephthalicacid.mo
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diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylbenzene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylbenzene.mo
index bc6cdd2..bc6cdd2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylbenzene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylbenzene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylcyclohexane.mo
index 01204d8..01204d8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylethylether.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylethylether.mo
index 63cf565..63cf565 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylethylether.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylethylether.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylmercaptan.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylmercaptan.mo
index 2c8394b..2c8394b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylmercaptan.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tertbutylmercaptan.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Tetraethyleneglycol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tetraethyleneglycol.mo
index 6326775..6326775 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Tetraethyleneglycol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tetraethyleneglycol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Tetrahydrofuran.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Tetrahydrofuran.mo
index 2c7451a..2c7451a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Tetrahydrofuran.mo
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index a28a4a8..a28a4a8 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Thiophene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Thiophene.mo
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index 8835e68..8835e68 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeFivedinitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeFivedinitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdimethylhexane.mo
index f597507..f597507 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdinitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdinitrotoluene.mo
index 4d62a57..4d62a57 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdinitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeFourdinitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreeFivetrimethylheptane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreeFivetrimethylheptane.mo
index e5a020b..e5a020b 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreeFivetrimethylheptane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreeFivetrimethylheptane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreediethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreediethylpentane.mo
index 3702b87..3702b87 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreediethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreediethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylTwobutanone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylTwobutanone.mo
index 3296937..3296937 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylTwobutanone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylTwobutanone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylhexane.mo
index c11b666..c11b666 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylpentane.mo
index 2c7b4d5..2c7b4d5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/ThreeThreedimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Threeethylheptane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threeethylheptane.mo
index 47db976..47db976 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threeethylheptane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threeethylheptane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Threeethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threeethylhexane.mo
index 9ed8a76..9ed8a76 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threeethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threeethylhexane.mo
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index 47d2f57..47d2f57 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threeethylpentane.mo
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index f30c3f1..f30c3f1 100644
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index 906769a..906769a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threehexanone.mo
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index e2e7166..e2e7166 100644
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index 09477f2..09477f2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/ThreemethylThreeethylpentane.mo
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index df57ec2..df57ec2 100644
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index b9f731c..b9f731c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threemethylhexane.mo
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index a659db0..a659db0 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threemethylnonane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threemethylnonane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Threemethyloctane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threemethyloctane.mo
index 212e598..212e598 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threemethyloctane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threemethyloctane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Threemethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threemethylpentane.mo
index 53fed46..53fed46 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threemethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threemethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Threepentanone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threepentanone.mo
index 9185013..9185013 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Threepentanone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Threepentanone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Toluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Toluene.mo
index b70b061..b70b061 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Toluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Toluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransOneFourdimethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneFourdimethylcyclohexane.mo
index dc5313f..dc5313f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransOneFourdimethylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneFourdimethylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclohexane.mo
index 9ec7491..9ec7491 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclopentane.mo
index 62794a9..62794a9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclopentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneThreedimethylcyclopentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclohexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclohexane.mo
index f546751..f546751 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclohexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclohexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclopentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclopentane.mo
index e0b8fce..e0b8fce 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclopentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransOneTwodimethylcyclopentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransTwobutene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransTwobutene.mo
index 6e6cac5..6e6cac5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransTwobutene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransTwobutene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransTwohexene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransTwohexene.mo
index 15af60f..15af60f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransTwohexene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransTwohexene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TransTwopentene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransTwopentene.mo
index 1c0284d..1c0284d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TransTwopentene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TransTwopentene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Transdecahydronaphthalene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Transdecahydronaphthalene.mo
index cbdab71..cbdab71 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Transdecahydronaphthalene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Transdecahydronaphthalene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetaldehyde.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetaldehyde.mo
index 0ea0c30..0ea0c30 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetaldehyde.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetaldehyde.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetylchloride.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetylchloride.mo
index 78b5289..78b5289 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetylchloride.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trichloroacetylchloride.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Trichloroethylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trichloroethylene.mo
index 79b096d..79b096d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Trichloroethylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trichloroethylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Triethanolamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Triethanolamine.mo
index 09e85ce..09e85ce 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Triethanolamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Triethanolamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Triethylamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Triethylamine.mo
index 0d349c6..0d349c6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Triethylamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Triethylamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Triethyleneglycol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Triethyleneglycol.mo
index a65879e..a65879e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Triethyleneglycol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Triethyleneglycol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Trimethylamine.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trimethylamine.mo
index 54355e2..54355e2 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Trimethylamine.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Trimethylamine.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Two6dinitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Two6dinitrotoluene.mo
index 8241f6f..8241f6f 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Two6dinitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Two6dinitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedimethylhexane.mo
index d986f6c..d986f6c 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedinitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedinitrotoluene.mo
index 7f36c18..7f36c18 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedinitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFivedinitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoFour6trinitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFour6trinitrotoluene.mo
index 3c75510..3c75510 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoFour6trinitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFour6trinitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourFourtrimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourFourtrimethylhexane.mo
index b09ee4a..b09ee4a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourFourtrimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourFourtrimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylhexane.mo
index b5fdf78..b5fdf78 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylpentane.mo
index cf6cb1d..cf6cb1d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdinitrotoluene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdinitrotoluene.mo
index e8a45d3..e8a45d3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdinitrotoluene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoFourdinitrotoluene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoMethoxyTwoMethylHeptane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoMethoxyTwoMethylHeptane.mo
index 6e628ac..6e628ac 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoMethoxyTwoMethylHeptane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoMethoxyTwoMethylHeptane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoMethylTwoHeptanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoMethylTwoHeptanol.mo
index c31a10e..c31a10e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoMethylTwoHeptanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoMethylTwoHeptanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeFourtrimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeFourtrimethylpentane.mo
index 4f008d3..4f008d3 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeFourtrimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeFourtrimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreeFourtetramethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreeFourtetramethylpentane.mo
index 4eddcda..4eddcda 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreeFourtetramethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreeFourtetramethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreetrimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreetrimethylpentane.mo
index e19b6ce..e19b6ce 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreetrimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreeThreetrimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylbutane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylbutane.mo
index f60f1b9..f60f1b9 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylbutane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylbutane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylhexane.mo
index df7f159..df7f159 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylpentane.mo
index a2e4522..a2e4522 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoThreedimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFivetrimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFivetrimethylhexane.mo
index 4db7536..4db7536 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFivetrimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFivetrimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourFourtetramethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourFourtetramethylpentane.mo
index 3c89a27..3c89a27 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourFourtetramethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourFourtetramethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourtrimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourtrimethylpentane.mo
index 8dc5c60..8dc5c60 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourtrimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoFourtrimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeFourtetramethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeFourtetramethylpentane.mo
index 1397fab..1397fab 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeFourtetramethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeFourtetramethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylbutane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylbutane.mo
index 79aafae..79aafae 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylbutane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylbutane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylpentane.mo
index f70ccf5..f70ccf5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreeThreetetramethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylbutane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylbutane.mo
index 66c2166..66c2166 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylbutane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylbutane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylpentane.mo
index 4de4b54..4de4b54 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwoThreetrimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylOnepropanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylOnepropanol.mo
index 67284b7..67284b7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylOnepropanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylOnepropanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylbutane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylbutane.mo
index 5d1803a..5d1803a 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylbutane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylbutane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylheptane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylheptane.mo
index 2beb166..2beb166 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylheptane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylheptane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylhexane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylhexane.mo
index 36918fc..36918fc 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylhexane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylhexane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethyloctane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethyloctane.mo
index a0ab019..a0ab019 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethyloctane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethyloctane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylpentane.mo
index 6099fd5..6099fd5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwoTwodimethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Twobutanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twobutanol.mo
index c7c8c29..c7c8c29 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Twobutanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twobutanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Twoethylmxylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twoethylmxylene.mo
index 37d65d7..37d65d7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Twoethylmxylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twoethylmxylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Twoethylpxylene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twoethylpxylene.mo
index d8711d5..d8711d5 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Twoethylpxylene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twoethylpxylene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Twoheptanone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twoheptanone.mo
index a0d8421..a0d8421 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Twoheptanone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twoheptanone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Twohexanone.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twohexanone.mo
index 4f5aa7e..4f5aa7e 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/Twohexanone.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twohexanone.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutanol.mo
index 936adc6..936adc6 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutene.mo
index 23aafdf..23aafdf 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnebutene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOneheptene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOneheptene.mo
index 7ad5923..7ad5923 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOneheptene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOneheptene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepentene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepentene.mo
index b669495..b669495 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepentene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepentene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepropanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepropanol.mo
index 94e5950..94e5950 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepropanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylOnepropanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylThreeethylpentane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylThreeethylpentane.mo
index 1a53aeb..1a53aeb 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylThreeethylpentane.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylThreeethylpentane.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutanol.mo
index db17c4d..db17c4d 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutene.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutene.mo
index fc800c7..fc800c7 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutene.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwobutene.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwopropanol.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwopropanol.mo
index 7bcb845..7bcb845 100644
--- a/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwopropanol.mo
+++ b/src/main/Simulator/Simulator/Files/ChemsepDatabase/TwomethylTwopropanol.mo
diff --git a/Simulator/Simulator/Files/ChemsepDatabase/Twomethylheptane.mo b/src/main/Simulator/Simulator/Files/ChemsepDatabase/Twomethylheptane.mo
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--- a/Simulator/Simulator/Files/ThermodynamicFunctions/PoyntingCF.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/PoyntingCF.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/Psat.mo b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/Psat.mo
index 2b779ae..2b779ae 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/Psat.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/Psat.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/SId.mo b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/SId.mo
index bc94e61..bc94e61 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/SId.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/SId.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/SolublityParameter.mo b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/SolublityParameter.mo
index 15d2afd..15d2afd 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/SolublityParameter.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/SolublityParameter.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/TowUNIQUAC.mo b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/TowUNIQUAC.mo
index 60209d3..60209d3 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/TowUNIQUAC.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/TowUNIQUAC.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/VapCpId.mo b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/VapCpId.mo
index 5042d02..5042d02 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/VapCpId.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/VapCpId.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/index.mo b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/index.mo
index a076f3a..a076f3a 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/index.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/index.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/package.mo b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/package.mo
index 543d5bf..543d5bf 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/package.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/package.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicFunctions/package.order b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/package.order
index 1ef0048..1ef0048 100644
--- a/Simulator/Simulator/Files/ThermodynamicFunctions/package.order
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicFunctions/package.order
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/GraysonStreed.mo b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/GraysonStreed.mo
index 5fbc14b..5fbc14b 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/GraysonStreed.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/GraysonStreed.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/NRTL.mo b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/NRTL.mo
index cf4eba1..cf4eba1 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/NRTL.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/NRTL.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/PengRobinson.mo b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/PengRobinson.mo
index e0f3ce9..e0f3ce9 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/PengRobinson.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/PengRobinson.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/RaoultsLaw.mo b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/RaoultsLaw.mo
index c318000..c318000 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/RaoultsLaw.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/RaoultsLaw.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/UNIFAC.mo b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/UNIFAC.mo
index e64210f..e64210f 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/UNIFAC.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/UNIFAC.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/UNIQUAC.mo b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/UNIQUAC.mo
index 932c692..932c692 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/UNIQUAC.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/UNIQUAC.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/package.mo b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/package.mo
index 95bd58e..95bd58e 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/package.mo
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/package.mo
diff --git a/Simulator/Simulator/Files/ThermodynamicPackages/package.order b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/package.order
index 8f1c507..8f1c507 100644
--- a/Simulator/Simulator/Files/ThermodynamicPackages/package.order
+++ b/src/main/Simulator/Simulator/Files/ThermodynamicPackages/package.order
diff --git a/Simulator/Simulator/Files/TransportProperties/LiqK.mo b/src/main/Simulator/Simulator/Files/TransportProperties/LiqK.mo
index e6886d9..e6886d9 100644
--- a/Simulator/Simulator/Files/TransportProperties/LiqK.mo
+++ b/src/main/Simulator/Simulator/Files/TransportProperties/LiqK.mo
diff --git a/Simulator/Simulator/Files/TransportProperties/LiqVis.mo b/src/main/Simulator/Simulator/Files/TransportProperties/LiqVis.mo
index 825174b..825174b 100644
--- a/Simulator/Simulator/Files/TransportProperties/LiqVis.mo
+++ b/src/main/Simulator/Simulator/Files/TransportProperties/LiqVis.mo
diff --git a/Simulator/Simulator/Files/TransportProperties/VapK.mo b/src/main/Simulator/Simulator/Files/TransportProperties/VapK.mo
index bcb5ed3..bcb5ed3 100644
--- a/Simulator/Simulator/Files/TransportProperties/VapK.mo
+++ b/src/main/Simulator/Simulator/Files/TransportProperties/VapK.mo
diff --git a/Simulator/Simulator/Files/TransportProperties/VapVisc.mo b/src/main/Simulator/Simulator/Files/TransportProperties/VapVisc.mo
index 31e3dbd..31e3dbd 100644
--- a/Simulator/Simulator/Files/TransportProperties/VapVisc.mo
+++ b/src/main/Simulator/Simulator/Files/TransportProperties/VapVisc.mo
diff --git a/Simulator/Simulator/Files/TransportProperties/package.mo b/src/main/Simulator/Simulator/Files/TransportProperties/package.mo
index 7bafb58..7bafb58 100644
--- a/Simulator/Simulator/Files/TransportProperties/package.mo
+++ b/src/main/Simulator/Simulator/Files/TransportProperties/package.mo
diff --git a/Simulator/Simulator/Files/TransportProperties/package.order b/src/main/Simulator/Simulator/Files/TransportProperties/package.order
index c109137..c109137 100644
--- a/Simulator/Simulator/Files/TransportProperties/package.order
+++ b/src/main/Simulator/Simulator/Files/TransportProperties/package.order
diff --git a/Simulator/Simulator/Files/package.mo b/src/main/Simulator/Simulator/Files/package.mo
index 361b84f..361b84f 100644
--- a/Simulator/Simulator/Files/package.mo
+++ b/src/main/Simulator/Simulator/Files/package.mo
diff --git a/Simulator/Simulator/Files/package.order b/src/main/Simulator/Simulator/Files/package.order
index 2d8ff2f..2d8ff2f 100644
--- a/Simulator/Simulator/Files/package.order
+++ b/src/main/Simulator/Simulator/Files/package.order
diff --git a/Simulator/Simulator/GuessModels/GuessInput.mo b/src/main/Simulator/Simulator/GuessModels/GuessInput.mo
index fb27ad8..fb27ad8 100644
--- a/Simulator/Simulator/GuessModels/GuessInput.mo
+++ b/src/main/Simulator/Simulator/GuessModels/GuessInput.mo
diff --git a/Simulator/Simulator/GuessModels/InitialGuess.mo b/src/main/Simulator/Simulator/GuessModels/InitialGuess.mo
index a52288b..a52288b 100644
--- a/Simulator/Simulator/GuessModels/InitialGuess.mo
+++ b/src/main/Simulator/Simulator/GuessModels/InitialGuess.mo
diff --git a/Simulator/Simulator/GuessModels/package.mo b/src/main/Simulator/Simulator/GuessModels/package.mo
index 585e061..585e061 100644
--- a/Simulator/Simulator/GuessModels/package.mo
+++ b/src/main/Simulator/Simulator/GuessModels/package.mo
diff --git a/Simulator/Simulator/GuessModels/package.order b/src/main/Simulator/Simulator/GuessModels/package.order
index 846e250..846e250 100644
--- a/Simulator/Simulator/GuessModels/package.order
+++ b/src/main/Simulator/Simulator/GuessModels/package.order
diff --git a/Simulator/Simulator/Streams/EnergyStream.mo b/src/main/Simulator/Simulator/Streams/EnergyStream.mo
index b7cfa29..b7cfa29 100644
--- a/Simulator/Simulator/Streams/EnergyStream.mo
+++ b/src/main/Simulator/Simulator/Streams/EnergyStream.mo
diff --git a/Simulator/Simulator/Streams/MaterialStream.mo b/src/main/Simulator/Simulator/Streams/MaterialStream.mo
index 6d78e99..6d78e99 100644
--- a/Simulator/Simulator/Streams/MaterialStream.mo
+++ b/src/main/Simulator/Simulator/Streams/MaterialStream.mo
diff --git a/Simulator/Simulator/Streams/package.mo b/src/main/Simulator/Simulator/Streams/package.mo
index 74a32da..74a32da 100644
--- a/Simulator/Simulator/Streams/package.mo
+++ b/src/main/Simulator/Simulator/Streams/package.mo
diff --git a/Simulator/Simulator/Streams/package.order b/src/main/Simulator/Simulator/Streams/package.order
index 4d1c5ab..4d1c5ab 100644
--- a/Simulator/Simulator/Streams/package.order
+++ b/src/main/Simulator/Simulator/Streams/package.order
diff --git a/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsCol.mo b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsCol.mo
index 6f962ec..6f962ec 100644
--- a/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsCol.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsCol.mo
diff --git a/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsTray.mo b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsTray.mo
index 25b9baf..25b9baf 100644
--- a/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsTray.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/AbsTray.mo
diff --git a/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.mo b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.mo
index 5afa5fc..5afa5fc 100644
--- a/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.mo
diff --git a/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.order b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.order
index 8322d9c..8322d9c 100644
--- a/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.order
+++ b/src/main/Simulator/Simulator/UnitOperations/AbsorptionColumn/package.order
diff --git a/Simulator/Simulator/UnitOperations/AdiabaticCompressor.mo b/src/main/Simulator/Simulator/UnitOperations/AdiabaticCompressor.mo
index 19e4248..19e4248 100644
--- a/Simulator/Simulator/UnitOperations/AdiabaticCompressor.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/AdiabaticCompressor.mo
diff --git a/Simulator/Simulator/UnitOperations/AdiabaticExpander.mo b/src/main/Simulator/Simulator/UnitOperations/AdiabaticExpander.mo
index b5fdaf6..b5fdaf6 100644
--- a/Simulator/Simulator/UnitOperations/AdiabaticExpander.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/AdiabaticExpander.mo
diff --git a/Simulator/Simulator/UnitOperations/CentrifugalPump.mo b/src/main/Simulator/Simulator/UnitOperations/CentrifugalPump.mo
index 6b5934b..6b5934b 100644
--- a/Simulator/Simulator/UnitOperations/CentrifugalPump.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/CentrifugalPump.mo
diff --git a/Simulator/Simulator/UnitOperations/CompoundSeparator.mo b/src/main/Simulator/Simulator/UnitOperations/CompoundSeparator.mo
index 577551a..577551a 100644
--- a/Simulator/Simulator/UnitOperations/CompoundSeparator.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/CompoundSeparator.mo
diff --git a/Simulator/Simulator/UnitOperations/ConversionReactor.mo b/src/main/Simulator/Simulator/UnitOperations/ConversionReactor.mo
index 78a18a9..78a18a9 100644
--- a/Simulator/Simulator/UnitOperations/ConversionReactor.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/ConversionReactor.mo
diff --git a/Simulator/Simulator/UnitOperations/Cooler.mo b/src/main/Simulator/Simulator/UnitOperations/Cooler.mo
index 945f38d..945f38d 100644
--- a/Simulator/Simulator/UnitOperations/Cooler.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/Cooler.mo
diff --git a/Simulator/Simulator/UnitOperations/DistillationColumn/Cond.mo b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/Cond.mo
index 29fc163..29fc163 100644
--- a/Simulator/Simulator/UnitOperations/DistillationColumn/Cond.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/Cond.mo
diff --git a/Simulator/Simulator/UnitOperations/DistillationColumn/DistCol.mo b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/DistCol.mo
index 64e1cc9..64e1cc9 100644
--- a/Simulator/Simulator/UnitOperations/DistillationColumn/DistCol.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/DistCol.mo
diff --git a/Simulator/Simulator/UnitOperations/DistillationColumn/DistTray.mo b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/DistTray.mo
index f308a73..f308a73 100644
--- a/Simulator/Simulator/UnitOperations/DistillationColumn/DistTray.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/DistTray.mo
diff --git a/Simulator/Simulator/UnitOperations/DistillationColumn/Reb.mo b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/Reb.mo
index 21383aa..21383aa 100644
--- a/Simulator/Simulator/UnitOperations/DistillationColumn/Reb.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/Reb.mo
diff --git a/Simulator/Simulator/UnitOperations/DistillationColumn/package.mo b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/package.mo
index 66cc267..66cc267 100644
--- a/Simulator/Simulator/UnitOperations/DistillationColumn/package.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/package.mo
diff --git a/Simulator/Simulator/UnitOperations/DistillationColumn/package.order b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/package.order
index 5a8f2be..5a8f2be 100644
--- a/Simulator/Simulator/UnitOperations/DistillationColumn/package.order
+++ b/src/main/Simulator/Simulator/UnitOperations/DistillationColumn/package.order
diff --git a/Simulator/Simulator/UnitOperations/EquilibriumReactor.mo b/src/main/Simulator/Simulator/UnitOperations/EquilibriumReactor.mo
index 73672e5..73672e5 100644
--- a/Simulator/Simulator/UnitOperations/EquilibriumReactor.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/EquilibriumReactor.mo
diff --git a/Simulator/Simulator/UnitOperations/Flash.mo b/src/main/Simulator/Simulator/UnitOperations/Flash.mo
index 6cd2b24..6cd2b24 100644
--- a/Simulator/Simulator/UnitOperations/Flash.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/Flash.mo
diff --git a/Simulator/Simulator/UnitOperations/HeatExchanger.mo b/src/main/Simulator/Simulator/UnitOperations/HeatExchanger.mo
index f1d5847..f1d5847 100644
--- a/Simulator/Simulator/UnitOperations/HeatExchanger.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/HeatExchanger.mo
diff --git a/Simulator/Simulator/UnitOperations/Heater.mo b/src/main/Simulator/Simulator/UnitOperations/Heater.mo
index 1f2d10a..1f2d10a 100644
--- a/Simulator/Simulator/UnitOperations/Heater.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/Heater.mo
diff --git a/Simulator/Simulator/UnitOperations/Mixer.mo b/src/main/Simulator/Simulator/UnitOperations/Mixer.mo
index ae0a1d9..ae0a1d9 100644
--- a/Simulator/Simulator/UnitOperations/Mixer.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/Mixer.mo
diff --git a/Simulator/Simulator/UnitOperations/PFR/Integral.mo b/src/main/Simulator/Simulator/UnitOperations/PFR/Integral.mo
index bd03e89..bd03e89 100644
--- a/Simulator/Simulator/UnitOperations/PFR/Integral.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/PFR/Integral.mo
diff --git a/Simulator/Simulator/UnitOperations/PFR/PFR.mo b/src/main/Simulator/Simulator/UnitOperations/PFR/PFR.mo
index d8bcf59..d8bcf59 100644
--- a/Simulator/Simulator/UnitOperations/PFR/PFR.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/PFR/PFR.mo
diff --git a/Simulator/Simulator/UnitOperations/PFR/PerformancePFR.mo b/src/main/Simulator/Simulator/UnitOperations/PFR/PerformancePFR.mo
index b1deb43..b1deb43 100644
--- a/Simulator/Simulator/UnitOperations/PFR/PerformancePFR.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/PFR/PerformancePFR.mo
diff --git a/Simulator/Simulator/UnitOperations/PFR/package.mo b/src/main/Simulator/Simulator/UnitOperations/PFR/package.mo
index d057566..d057566 100644
--- a/Simulator/Simulator/UnitOperations/PFR/package.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/PFR/package.mo
diff --git a/Simulator/Simulator/UnitOperations/PFR/package.order b/src/main/Simulator/Simulator/UnitOperations/PFR/package.order
index e6992a1..e6992a1 100644
--- a/Simulator/Simulator/UnitOperations/PFR/package.order
+++ b/src/main/Simulator/Simulator/UnitOperations/PFR/package.order
diff --git a/Simulator/Simulator/UnitOperations/RecycleBlock.mo b/src/main/Simulator/Simulator/UnitOperations/RecycleBlock.mo
index 6957b2d..6957b2d 100644
--- a/Simulator/Simulator/UnitOperations/RecycleBlock.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/RecycleBlock.mo
diff --git a/Simulator/Simulator/UnitOperations/ShortcutColumn.mo b/src/main/Simulator/Simulator/UnitOperations/ShortcutColumn.mo
index 3bdfd36..3bdfd36 100644
--- a/Simulator/Simulator/UnitOperations/ShortcutColumn.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/ShortcutColumn.mo
diff --git a/Simulator/Simulator/UnitOperations/Splitter.mo b/src/main/Simulator/Simulator/UnitOperations/Splitter.mo
index 9871ea7..9871ea7 100644
--- a/Simulator/Simulator/UnitOperations/Splitter.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/Splitter.mo
diff --git a/Simulator/Simulator/UnitOperations/Valve.mo b/src/main/Simulator/Simulator/UnitOperations/Valve.mo
index 658d52a..658d52a 100644
--- a/Simulator/Simulator/UnitOperations/Valve.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/Valve.mo
diff --git a/Simulator/Simulator/UnitOperations/package.mo b/src/main/Simulator/Simulator/UnitOperations/package.mo
index 0b39662..0b39662 100644
--- a/Simulator/Simulator/UnitOperations/package.mo
+++ b/src/main/Simulator/Simulator/UnitOperations/package.mo
diff --git a/Simulator/Simulator/UnitOperations/package.order b/src/main/Simulator/Simulator/UnitOperations/package.order
index 95fe9a1..95fe9a1 100644
--- a/Simulator/Simulator/UnitOperations/package.order
+++ b/src/main/Simulator/Simulator/UnitOperations/package.order
diff --git a/Simulator/Simulator/package.mo b/src/main/Simulator/Simulator/package.mo
index 8e6e1da..8e6e1da 100644
--- a/Simulator/Simulator/package.mo
+++ b/src/main/Simulator/Simulator/package.mo
diff --git a/Simulator/Simulator/package.order b/src/main/Simulator/Simulator/package.order
index b0723ec..b0723ec 100644
--- a/Simulator/Simulator/package.order
+++ b/src/main/Simulator/Simulator/package.order
diff --git a/DockWidgets/DistillationColumnStagewiseResults.py b/src/main/python/DockWidgets/DistillationColumnStagewiseResults.py
index c5bd67d..65527dc 100644
--- a/DockWidgets/DistillationColumnStagewiseResults.py
+++ b/src/main/python/DockWidgets/DistillationColumnStagewiseResults.py
@@ -1,7 +1,13 @@
+import os, sys
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.uic import loadUiType
 from PyQt5.QtWidgets import QWidget
 
-ui_dialog,_ = loadUiType('DockWidgets/DistillationColumnStagewiseResults.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DistillationColumnStagewiseResults.ui')
 
 
 class DistillationColumnStagewiseResults(QWidget,ui_dialog):
diff --git a/DockWidgets/DockWidget.py b/src/main/python/DockWidgets/DockWidget.py
index bb8ddf5..764d8fb 100644
--- a/DockWidgets/DockWidget.py
+++ b/src/main/python/DockWidgets/DockWidget.py
@@ -1,11 +1,18 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
-from ComponentSelector import *
-from Graphics import *
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidget.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidget.ui')
 
 class DockWidget(QDockWidget,ui_dialog):
     
@@ -20,7 +27,7 @@ class DockWidget(QDockWidget,ui_dialog):
         self.modes()
         self.comboBox.currentIndexChanged.connect(self.mode_selection)
        
-        print("constructor ", self.input_dict)
+        #print("constructor ", self.input_dict)
         self.pushButton_2.clicked.connect(self.param)
 
         self.dict = {}          # a dictionary
@@ -44,27 +51,28 @@ class DockWidget(QDockWidget,ui_dialog):
         self.input_dict= {}
         for i in reversed(range(self.formLayout.count())):
             self.formLayout.removeRow(i) 
-        print(self.comboBox.currentText())
+        #print(self.comboBox.currentText())
         for i in self.obj.variables:
             if self.obj.variables[i]['name'] == self.comboBox.currentText():
                 currentText = i
                 break
         self.input_dict = self.obj.param_getter(currentText)
-        print('mode selection ', self.input_dict)
+        #print('mode selection ', self.input_dict)
         self.input_params_list()
             
     def input_params_list(self):
         try:
-            print("input_params_list ", self.input_dict)
+            #print("input_params_list ", self.input_dict)
             for c,i in enumerate(self.input_dict):
                 #print(i)
                 if i == None:
                     continue
                 l = QLineEdit(str(self.obj.variables[i]['value']))
+                l.setFixedWidth(80)
                 lay = QGridLayout()
                 lay.addWidget(QLabel(self.obj.variables[i]['name']+":"),0,0, alignment=Qt.AlignLeft)
                 lay.addWidget(l,0,1, alignment=Qt.AlignCenter)
-                lay.addWidget(QLabel(self.obj.variables[i]['unit']),0,2, alignment=Qt.AlignCenter)
+                lay.addWidget(QLabel(self.obj.variables[i]['unit']),0,2, alignment=Qt.AlignLeft)
                 self.formLayout.addRow(lay)
                 self.input_dict[i] = l
         except Exception as e:
diff --git a/DockWidgets/DockWidgetCompoundSeparator.py b/src/main/python/DockWidgets/DockWidgetCompoundSeparator.py
index 57b1339..26f8fd4 100644
--- a/DockWidgets/DockWidgetCompoundSeparator.py
+++ b/src/main/python/DockWidgets/DockWidgetCompoundSeparator.py
@@ -1,14 +1,21 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
 import pandas as pd
 from functools import partial
-from ComponentSelector import *
+from python.utils.ComponentSelector import *
 from collections import defaultdict
-from Graphics import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetCompoundSeparator.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetCompoundSeparator.ui')
 
 class DockWidgetCompoundSeparator(QDockWidget,ui_dialog):
 
@@ -56,6 +63,7 @@ class DockWidgetCompoundSeparator(QDockWidget,ui_dialog):
                     combo.setCurrentText(self.obj.variables['SepFact_c']['value'][k])
                     combo.setSizePolicy(QSizePolicy.Fixed, QSizePolicy.Fixed)
                     l = QLineEdit(str(self.obj.variables['SepVal_c']['value'][k]))
+                    l.setFixedWidth(80)
                     l.setSizePolicy(QSizePolicy.Fixed, QSizePolicy.Fixed)
                     self.calculationLayout.addWidget(QLabel(val+" :"), k+1,0, alignment=Qt.AlignLeft)
                     self.calculationLayout.addWidget(combo, k+1, 1, alignment=Qt.AlignCenter)
diff --git a/DockWidgets/DockWidgetCompressorExpander.py b/src/main/python/DockWidgets/DockWidgetCompressorExpander.py
index e8e2b31..9a8cb07 100644
--- a/DockWidgets/DockWidgetCompressorExpander.py
+++ b/src/main/python/DockWidgets/DockWidgetCompressorExpander.py
@@ -1,11 +1,18 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
-from ComponentSelector import *
-from Graphics import *
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetCompressorExpander.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetCompressorExpander.ui')
 
 class DockWidgetCompressorExpander(QDockWidget,ui_dialog):
 
@@ -44,18 +51,18 @@ class DockWidgetCompressorExpander(QDockWidget,ui_dialog):
         self.input_dict= {}
         for i in reversed(range(self.formLayout.count())):
             self.formLayout.removeRow(i) 
-        print(self.comboBox.currentText())
+        #print(self.comboBox.currentText())
         for i in self.obj.variables:
             if self.obj.variables[i]['name'] == self.comboBox.currentText():
                 currentText = i
                 break
         self.input_dict = self.obj.param_getter(currentText)
-        print('mode selection ', self.input_dict)
+        #print('mode selection ', self.input_dict)
         self.input_params_list()
             
     def input_params_list(self):
         try:
-            print("input_params_list ", self.input_dict)
+            #print("input_params_list ", self.input_dict)
             for c,i in enumerate(self.input_dict):
                 if i == None:
                     continue
@@ -63,15 +70,16 @@ class DockWidgetCompressorExpander(QDockWidget,ui_dialog):
                 l = QLineEdit()
                 if self.input_dict[i] != None:
                     l.setText(str(self.input_dict[i]))
+                l.setFixedWidth(80)
                 lay = QGridLayout()
                 lay.addWidget(QLabel(self.obj.variables[i]['name']+":"),0,0, alignment=Qt.AlignLeft) 
                 lay.addWidget(l,0,1, alignment=Qt.AlignCenter)
-                lay.addWidget(QLabel(self.obj.variables[i]['unit']),0,2, alignment=Qt.AlignCenter)
+                lay.addWidget(QLabel(self.obj.variables[i]['unit']),0,2, alignment=Qt.AlignLeft)
               
                 self.formLayout.addRow(lay)
                 self.input_dict[i] = l
             
-            self.lines = [line.rstrip('\n') for line in open('thermopackage.txt')]
+            self.lines = [line.rstrip('\n') for line in open(parentPath+'/python/utils/thermopackage.txt')]
             for j in self.lines:
                 self.cbTP.addItem(str(j))
             self.input_dict['Thermo Package'] = self.cbTP
@@ -91,11 +99,11 @@ class DockWidgetCompressorExpander(QDockWidget,ui_dialog):
                 elif (i == "Thermo Package"):
                     self.dict[i] = self.input_dict[i].currentText()
                 else:
-                    print(self.input_dict[i], i, self.obj.type)
+                    #print(self.input_dict[i], i, self.obj.type)
                     if (self.input_dict[i].text()):
                         self.dict[i] = self.input_dict[i].text()
                     else:
-                        print(self.input_dict[i].text())
+                        #print(self.input_dict[i].text())
                         self.show_error()
                         break
             
@@ -130,19 +138,19 @@ class DockWidgetCompressorExpander(QDockWidget,ui_dialog):
     def results_category(self,name):
         flag = True
         try:
-            print("Under result category name ", name)
+            #print("Under result category name ", name)
             result=self.container.result
             obj = self.container.fetch_object(name)
             self.tableWidget.setRowCount(0)
             variKeys = list(obj.variables.keys())
-            print(variKeys)
+            #print(variKeys)
             for i, val in enumerate(variKeys):
                 propertyname = name + '.' + val
-                print(i,val, propertyname)
+                #print(i,val, propertyname)
                 if propertyname in result[0]:
                     ind = result[0].index(propertyname)
                     resultval = str(result[-1][ind])
-                    print("######Resultsfetch####",val,resultval)
+                    #print("######Resultsfetch####",val,resultval)
                     rowPosition = self.tableWidget.rowCount()
                     self.tableWidget.insertRow(rowPosition)
                     self.tableWidget.setItem(rowPosition , 0, QTableWidgetItem(obj.variables[val]['name']))
diff --git a/DockWidgets/DockWidgetDistillationColumn.py b/src/main/python/DockWidgets/DockWidgetDistillationColumn.py
index e2e1031..7895b32 100644
--- a/DockWidgets/DockWidgetDistillationColumn.py
+++ b/src/main/python/DockWidgets/DockWidgetDistillationColumn.py
@@ -1,15 +1,23 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
 import pandas as pd
 from functools import partial
-from ComponentSelector import *
 from collections import defaultdict
-from DockWidgets.DistillationColumnStagewiseResults import DistillationColumnStagewiseResults
-from Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetDistillationColumn.ui')
+from python.utils.ComponentSelector import *
+from python.DockWidgets.DistillationColumnStagewiseResults import DistillationColumnStagewiseResults
+from python.utils.Graphics import *
+
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetDistillationColumn.ui')
 
 
 class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
@@ -39,6 +47,7 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
             # tab 1
             
             l1 = QLineEdit()
+            l1.setFixedWidth(80)
             l1.setText(str(self.obj.variables['Nt']['value']))
             self.lay1.addWidget(QLabel(self.obj.variables['Nt']['name'] + " :"), 0 ,0, alignment=Qt.AlignLeft)
             self.lay1.addWidget(l1,0,1, alignment=Qt.AlignLeft)
@@ -47,6 +56,7 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
             for i in range(self.obj.variables['Ni']['value']):
                 print(i)
                 l = QLineEdit()
+                l.setFixedWidth(80)
                 if len(self.obj.variables['InT_s']['value']) is not 0:
                     l.setText(str(self.obj.variables['InT_s']['value'][i]))
                 self.lay1.addWidget(QLabel(self.obj.variables['InT_s']['name'] +" " + str(i+1) + " location :"),2*(i+1),0, alignment=Qt.AlignLeft)
@@ -67,6 +77,7 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
             self.cb5.addItem("Total")
             self.cb5.addItem("Partial")
             self.cb5.setCurrentText(self.obj.variables['Ctype']['value'])
+            
             for j in self.obj.Cspec_list:
                 self.cb1.addItem(str(j))
             self.cb1.setCurrentText(self.obj.variables['C_Spec']['type'])
@@ -77,6 +88,18 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
             self.cb2.setDisabled(True)  
             self.cb1.currentIndexChanged.connect(self.fun2) 
 
+            self.le5.setFixedWidth(80)
+            self.le6.setFixedWidth(80)
+            self.le7.setFixedWidth(80)
+            self.le8.setFixedWidth(80)
+            self.cb1.setFixedWidth(180)
+            self.cb2.setFixedWidth(80)
+            self.cb3.setFixedWidth(180)
+            self.cb4.setFixedWidth(80)
+            self.cb5.setFixedWidth(80)
+            self.u2.setAlignment(Qt.AlignLeft)
+            self.u3.setAlignment(Qt.AlignLeft)
+
             self.input_dict.append(self.cb5)
             self.input_dict.append(self.le5)
             self.input_dict.append(self.cb1) 
@@ -105,7 +128,7 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
             self.input_dict.append(self.cb4) 
             self.input_dict.append(self.le8)
 
-            self.lines = [line.rstrip('\n') for line in open('thermopackage.txt')]
+            self.lines = [line.rstrip('\n') for line in open(parentPath+'/python/utils/thermopackage.txt')]
             for j in self.lines:
                 self.cbTP.addItem(str(j))
             self.cbTP.setCurrentText(self.obj.variables['thermo_package']['value'])
@@ -154,30 +177,30 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
                 temp = i + 1
                 print(temp)
 
-            print(temp)
-            print(self.input_dict[temp+1])
+            # print(temp)
+            # print(self.input_dict[temp+1])
             self.dict.append(self.input_dict[temp+1].currentText())
-            print(temp+1)
+            # print(temp+1)
             self.dict.append(int(self.input_dict[temp+2].text()))
-            print(temp+2)
+            #print(temp+2)
             self.dict.append(self.input_dict[temp+3].currentText())
-            print(temp+3)
+            #print(temp+3)
             self.dict.append(self.input_dict[temp+4].currentText())
-            print(temp+4)
+            #print(temp+4)
             self.dict.append(int(self.input_dict[temp+5].text()))
-            print(temp+5)
+            #print(temp+5)
             self.dict.append(int(self.input_dict[temp+6].text()))
-            print(temp+6)
+            #print(temp+6)
             self.dict.append(self.input_dict[temp+7].currentText())
-            print(temp+7)
+            #print(temp+7)
             self.dict.append(self.input_dict[temp+8].currentText())
-            print(temp+8)
+            #print(temp+8)
             self.dict.append(int(self.input_dict[temp+9].text()))
-            print(temp+9)
+            #print(temp+9)
             self.dict.append(self.input_dict[temp+10].currentText())
-            print(temp + 10)
+            #print(temp + 10)
 
-            print("param ", self.dict)
+            #print("param ", self.dict)
             self.obj.param_setter(self.dict)
             if(self.isVisible()):
                 currentVal = self.parent().container.graphics.graphicsView.horizontalScrollBar().value()
@@ -210,20 +233,20 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
     def results_category(self,name):
         flag = True
         try:
-            print("Under result category name ", name)
+            #print("Under result category name ", name)
             result = self.container.result
             obj = self.container.fetch_object(name)
             self.tableWidget.setRowCount(0)
             variKeys = obj.result_parameters
-            print(variKeys)
+            #print(variKeys)
             for i, val in enumerate(variKeys):
                 propertyname = name + '.' + val
-                print(i, val, propertyname)
+                #print(i, val, propertyname)
                 if propertyname in result[0]:
                     ind = result[0].index(propertyname)
                     resultval = str(result[-1][ind])
                     obj.variables[val]['value'] = result[-1][ind]
-                    print("######Resultsfetch####", val, resultval)
+                    #print("######Resultsfetch####", val, resultval)
                     rowPosition = self.tableWidget.rowCount()
                     self.tableWidget.insertRow(rowPosition)
                     self.tableWidget.setItem(rowPosition, 0, QTableWidgetItem(obj.variables[val]['name']))
@@ -261,7 +284,7 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
                     #     else:
                     #         Stages_F_p[0][2] = result[-1][ind]
                     else:
-                        print(ind)
+                        #print(ind)
                         phase_no = int(result[0][ind][result[0][ind].index('[') + 1])
                         comp_no = int(result[0][ind][result[0][ind].index(']') - 1])
                         Stages_x_pc[0][comp_no - 1][phase_no - 1] = result[-1][ind]
@@ -286,8 +309,8 @@ class DockWidgetDistillationColumn(QDockWidget, ui_dialog):
                         #     else:
                         #         Stages_F_p[i][2] = result[-1][ind]
                         else:
-                            print(ind)
-                            print(result[0][ind])
+                            # print(ind)
+                            # print(result[0][ind])
                             phase_no = int(result[0][ind].split('.')[-1][result[0][ind].split('.')[-1].index('[') + 1])
                             comp_no = int(result[0][ind].split('.')[-1][result[0][ind].split('.')[-1].index(']') - 1])
                             Stages_x_pc[i][comp_no - 1][phase_no - 1] = result[-1][ind]
diff --git a/DockWidgets/DockWidgetFlash.py b/src/main/python/DockWidgets/DockWidgetFlash.py
index c75f950..c001fe2 100644
--- a/DockWidgets/DockWidgetFlash.py
+++ b/src/main/python/DockWidgets/DockWidgetFlash.py
@@ -1,11 +1,18 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
-from ComponentSelector import *
-from Graphics import *
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetFlash.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetFlash.ui')
 
 class DockWidgetFlash(QDockWidget,ui_dialog):
 
@@ -24,7 +31,7 @@ class DockWidgetFlash(QDockWidget,ui_dialog):
     def input_params_list(self):
         try:        
             self.l1.setText(self.obj.variables['thermo_package']['name']+":")
-            self.lines = [line.rstrip('\n') for line in open('thermopackage.txt')]
+            self.lines = [line.rstrip('\n') for line in open(parentPath+'/python/utils/thermopackage.txt')]
             for j in self.lines:
                 self.cb1.addItem(str(j))
             self.cb1.setCurrentText(self.obj.variables['thermo_package']['value'])
@@ -40,6 +47,10 @@ class DockWidgetFlash(QDockWidget,ui_dialog):
             self.check2.toggled.connect(self.fun)
             self.check2.setChecked(self.obj.variables['BPdef']['value'])
 
+            self.le2.setFixedWidth(80)
+            self.le3.setFixedWidth(80)
+            self.cb1.setFixedWidth(80)
+
             self.input_dict = [self.cb1, self.check1, self.le2, self.check2, self.le3]
  
         except Exception as e:
@@ -61,9 +72,9 @@ class DockWidgetFlash(QDockWidget,ui_dialog):
     def param(self):
         try:
             self.dict = []
-            print("param.input_dict ", self.input_dict)
+            #print("param.input_dict ", self.input_dict)
             self.dict = [self.input_dict[0].currentText(),self.input_dict[1].isChecked(), float(self.input_dict[2].text()), self.input_dict[3].isChecked(), float(self.input_dict[4].text())]
-            print("param ", self.dict)
+            #print("param ", self.dict)
             self.obj.param_setter(self.dict)
             if(self.isVisible()):
                 currentVal = self.parent().container.graphics.graphicsView.horizontalScrollBar().value()
diff --git a/DockWidgets/DockWidgetMaterialStream.py b/src/main/python/DockWidgets/DockWidgetMaterialStream.py
index 422119e..d2aefb6 100644
--- a/DockWidgets/DockWidgetMaterialStream.py
+++ b/src/main/python/DockWidgets/DockWidgetMaterialStream.py
@@ -1,11 +1,17 @@
+import os, sys
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
-from ComponentSelector import *
-from Graphics import *
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetMaterialStream.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetMaterialStream.ui')
 
 class DockWidgetMaterialStream(QDockWidget,ui_dialog):
 
@@ -31,7 +37,7 @@ class DockWidgetMaterialStream(QDockWidget,ui_dialog):
         self.mTreeWidget.setHeaderItem(header)
         self.lTreeWidget.setHeaderItem(header)
         self.vTreeWidget.setHeaderItem(header)
-        lines = [line.rstrip('\n') for line in open('thermopackage.txt')]
+        lines = [line.rstrip('\n') for line in open(parentPath+'/python/utils/thermopackage.txt')]
         for j in lines:
             self.cbTP.addItem(str(j))
         self.modes()
@@ -75,10 +81,7 @@ class DockWidgetMaterialStream(QDockWidget,ui_dialog):
                             l = QLineEdit(str(self.obj.variables['x_pc']['value'][j]))
                         except:
                             l = QLineEdit()
-                        # if self.input_dict[i] != '':
-                        #     l.setText(str(self.obj.variables['x_pc']['value'][j]))
-                        #     print('l = ', str(self.obj.variables['x_pc']['value'][j]))
-
+                        l.setFixedWidth(100)
                         self.input_dict[i] = "x_pc"
                         lay.addWidget(QLabel(str(compound_selected[j])+":"),j,0, alignment= Qt.AlignLeft)
                         lay.addWidget(l,j,1, alignment=Qt.AlignCenter)
@@ -93,7 +96,7 @@ class DockWidgetMaterialStream(QDockWidget,ui_dialog):
                     l = QLineEdit()
                     if self.input_dict[i] != None:
                         l.setText(str(self.input_dict[i]))
-
+                    l.setFixedWidth(80)
                     lay = QGridLayout()
                     if i !='MolFlow':
                         lay.addWidget(QLabel(self.obj.variables[i]['name']+":"),0,0, alignment=Qt.AlignLeft)
@@ -101,9 +104,9 @@ class DockWidgetMaterialStream(QDockWidget,ui_dialog):
                         lay.addWidget(QLabel(i+":"),0,0, alignment=Qt.AlignLeft)
                     lay.addWidget(l,0,1, alignment=Qt.AlignCenter)
                     if(i != 'MolFlow'):
-                        lay.addWidget(QLabel(self.obj.variables[i]['unit']),0,2, alignment=Qt.AlignCenter)
+                        lay.addWidget(QLabel(self.obj.variables[i]['unit']),0,2, alignment=Qt.AlignLeft)
                     else:
-                        lay.addWidget(QLabel("mol/s"),0,2, alignment=Qt.AlignCenter)
+                        lay.addWidget(QLabel("mol/s"),0,2, alignment=Qt.AlignLeft)
                     self.formLayout.addRow(lay)
                     self.input_dict[i] = l
 
@@ -333,8 +336,6 @@ class DockWidgetMaterialStream(QDockWidget,ui_dialog):
             self.input_dict = {}
             self.input_dict = self.obj.param_getter(self.comboBox.currentText())
             # print("before", self.input_dict)
-            #self.input_dict.pop("x_pc")
-            # temp = self.input_dict.pop('thermo_package')
             for i in range(len(compound_selected)):
                 #print(i)
                 self.input_dict['x_pc[1,' + str(i+1) + ']'] = self.obj.variables['x_pc[1,' + str(i+1) +']']['value']
diff --git a/DockWidgets/DockWidgetMixer.py b/src/main/python/DockWidgets/DockWidgetMixer.py
index 2d02f8c..5d89589 100644
--- a/DockWidgets/DockWidgetMixer.py
+++ b/src/main/python/DockWidgets/DockWidgetMixer.py
@@ -1,11 +1,18 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
-from ComponentSelector import *
-from Graphics import *
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetMixer.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetMixer.ui')
 
 class DockWidgetMixer(QDockWidget,ui_dialog):
 
diff --git a/DockWidgets/DockWidgetShortcutColumn.py b/src/main/python/DockWidgets/DockWidgetShortcutColumn.py
index 9b65021..b627e9d 100644
--- a/DockWidgets/DockWidgetShortcutColumn.py
+++ b/src/main/python/DockWidgets/DockWidgetShortcutColumn.py
@@ -1,11 +1,18 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
-from ComponentSelector import *
-from Graphics import *
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetShortcutColumn.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetShortcutColumn.ui')
 
 class DockWidgetShortcutColumn(QDockWidget,ui_dialog):
 
@@ -61,7 +68,7 @@ class DockWidgetShortcutColumn(QDockWidget,ui_dialog):
 
             self.l9.setText("Thermo Package :")
 
-            self.lines = [line.rstrip('\n') for line in open('thermopackage.txt')]
+            self.lines = [line.rstrip('\n') for line in open(parentPath+'/python/utils/thermopackage.txt')]
             for j in self.lines:
                 self.cb6.addItem(str(j))
             self.cb6.setCurrentText(self.obj.variables['thermo_package']['value'])
@@ -113,20 +120,20 @@ class DockWidgetShortcutColumn(QDockWidget,ui_dialog):
     def results_category(self,name):
         flag = True
         try:
-            print("Under result category name ", name)
+            #print("Under result category name ", name)
             result=self.container.result
             obj = self.container.fetch_object(name)
             self.tableWidget.setRowCount(0)
             variKeys = obj.result_parameters
-            print(variKeys)
+            #print(variKeys)
             for i, val in enumerate(variKeys):
                 propertyname = name + '.' + val
-                print(i,val, propertyname)
+                #print(i,val, propertyname)
                 if propertyname in result[0]:
                     ind = result[0].index(propertyname)
                     resultval = str(result[-1][ind])
                     obj.variables[val]['value']= result[-1][ind]
-                    print("######Resultsfetch####",val,resultval)
+                    #print("######Resultsfetch####",val,resultval)
                     rowPosition = self.tableWidget.rowCount()
                     self.tableWidget.insertRow(rowPosition)
                     self.tableWidget.setItem(rowPosition , 0, QTableWidgetItem(obj.variables[val]['name']))
diff --git a/DockWidgets/DockWidgetSplitter.py b/src/main/python/DockWidgets/DockWidgetSplitter.py
index 24a8ee2..296e111 100644
--- a/DockWidgets/DockWidgetSplitter.py
+++ b/src/main/python/DockWidgets/DockWidgetSplitter.py
@@ -1,11 +1,18 @@
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
 from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
-from ComponentSelector import *
-from Graphics import *
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import *
 
-ui_dialog,_ = loadUiType('DockWidgets/DockWidgetSplitter.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/DockWidgets/DockWidgetSplitter.ui')
 
 class DockWidgetSplitter(QDockWidget,ui_dialog):
 
diff --git a/venv/Lib/site-packages/astroid/interpreter/__init__.py b/src/main/python/DockWidgets/__init__.py
index e69de29..e69de29 100644
--- a/venv/Lib/site-packages/astroid/interpreter/__init__.py
+++ b/src/main/python/DockWidgets/__init__.py
diff --git a/src/main/python/DockWidgets/__pycache__/DistillationColumnStagewiseResults.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DistillationColumnStagewiseResults.cpython-36.pyc
new file mode 100644
index 0000000..0feb70b
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DistillationColumnStagewiseResults.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DistillationColumnStagewiseResults.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DistillationColumnStagewiseResults.cpython-37.pyc
new file mode 100644
index 0000000..d8c43f1
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DistillationColumnStagewiseResults.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidget.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidget.cpython-36.pyc
new file mode 100644
index 0000000..853e89a
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidget.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidget.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidget.cpython-37.pyc
new file mode 100644
index 0000000..90c3ef9
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidget.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetCompoundSeparator.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetCompoundSeparator.cpython-36.pyc
new file mode 100644
index 0000000..355cf3a
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetCompoundSeparator.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetCompoundSeparator.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetCompoundSeparator.cpython-37.pyc
new file mode 100644
index 0000000..eed70e1
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetCompoundSeparator.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetCompressorExpander.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetCompressorExpander.cpython-36.pyc
new file mode 100644
index 0000000..88102aa
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetCompressorExpander.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetCompressorExpander.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetCompressorExpander.cpython-37.pyc
new file mode 100644
index 0000000..05d0157
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetCompressorExpander.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetDistillationColumn.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetDistillationColumn.cpython-36.pyc
new file mode 100644
index 0000000..f5eccbb
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetDistillationColumn.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetDistillationColumn.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetDistillationColumn.cpython-37.pyc
new file mode 100644
index 0000000..a3cba32
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetDistillationColumn.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetFlash.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetFlash.cpython-36.pyc
new file mode 100644
index 0000000..34d90b2
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetFlash.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetFlash.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetFlash.cpython-37.pyc
new file mode 100644
index 0000000..08f6dae
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetFlash.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetMaterialStream.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetMaterialStream.cpython-36.pyc
new file mode 100644
index 0000000..1181e13
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetMaterialStream.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetMaterialStream.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetMaterialStream.cpython-37.pyc
new file mode 100644
index 0000000..abc5f50
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetMaterialStream.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetMixer.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetMixer.cpython-36.pyc
new file mode 100644
index 0000000..1fc6df4
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetMixer.cpython-36.pyc
diff --git a/DockWidgets/__pycache__/DockWidgetMixer.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetMixer.cpython-37.pyc
index ce2d5af..2974d48 100644
--- a/DockWidgets/__pycache__/DockWidgetMixer.cpython-37.pyc
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetMixer.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetShortcutColumn.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetShortcutColumn.cpython-36.pyc
new file mode 100644
index 0000000..99d84d1
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetShortcutColumn.cpython-36.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetShortcutColumn.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetShortcutColumn.cpython-37.pyc
new file mode 100644
index 0000000..46cd536
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetShortcutColumn.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/DockWidgetSplitter.cpython-36.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetSplitter.cpython-36.pyc
new file mode 100644
index 0000000..6c8bb16
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetSplitter.cpython-36.pyc
diff --git a/DockWidgets/__pycache__/DockWidgetSplitter.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/DockWidgetSplitter.cpython-37.pyc
index 2f45777..d23e668 100644
--- a/DockWidgets/__pycache__/DockWidgetSplitter.cpython-37.pyc
+++ b/src/main/python/DockWidgets/__pycache__/DockWidgetSplitter.cpython-37.pyc
diff --git a/src/main/python/DockWidgets/__pycache__/__init__.cpython-37.pyc b/src/main/python/DockWidgets/__pycache__/__init__.cpython-37.pyc
new file mode 100644
index 0000000..9a9342e
--- /dev/null
+++ b/src/main/python/DockWidgets/__pycache__/__init__.cpython-37.pyc
diff --git a/OMChem/CompSep.py b/src/main/python/OMChem/CompSep.py
index 9579498..d538acb 100644
--- a/OMChem/CompSep.py
+++ b/src/main/python/OMChem/CompSep.py
@@ -6,7 +6,6 @@ class CompSep():
         self.SepFact = json.dumps(SepFact).replace('[','{').replace(']','}')
         self.SepStrm = str(SepStrm)
         self.SepFactValue = json.dumps(SepFactValue).replace('[','{').replace(']','}')
-        #self.name = name
         self.OM_data_eqn = ''
         self.OM_data_init = ''
         self.InputStms = []
diff --git a/OMChem/ConvReactor.py b/src/main/python/OMChem/ConvReactor.py
index ccdf524..5c83106 100644
--- a/OMChem/ConvReactor.py
+++ b/src/main/python/OMChem/ConvReactor.py
@@ -16,7 +16,7 @@ class ConvReactor():
         self.Tdef = str(Tdef)
       
         self.type = 'ConvReactor'
-        self.EngStms = EngStms(name="EngStm")
+        self.EngStms = EngStm(name="EngStm")
 
     def OM_Flowsheet_Init(self, addedcomp):
         self.OM_data_init = ''
diff --git a/OMChem/Cooler.py b/src/main/python/OMChem/Cooler.py
index 9a44033..9a44033 100644
--- a/OMChem/Cooler.py
+++ b/src/main/python/OMChem/Cooler.py
diff --git a/OMChem/DistCol.py b/src/main/python/OMChem/DistCol.py
index 1492bc2..c4a88c3 100644
--- a/OMChem/DistCol.py
+++ b/src/main/python/OMChem/DistCol.py
@@ -5,7 +5,6 @@ class DistCol():
         self.numStage = numStage
         self.numFeeds=numFeeds
         self.feedStages=feedStages
-        #self.name = name[0]
         self.name = name + str(DistCol.counter) 
         self.OM_data_eqn = ''
         self.OM_data_init = ''
@@ -13,7 +12,6 @@ class DistCol():
         self.OutputStms = None
         self.EngStm1 = EngStm(name='EngStm1'+self.name)
         self.EngStm2 = EngStm(name='EngStm2'+self.name)
-        #self.count = name[1]
         self.count = DistCol.counter
         self.thermoPackage='Raoults_Law'
         self.type = 'DistCol'
@@ -87,7 +85,6 @@ class DistCol():
 
     def OM_Flowsheet_Eqn(self, addedcomp):
         self.OM_data_eqn = ''
-        # self.OM_data_eqn = self.name + '.pressDrop = ' + str(self.PressDrop) + ';\n'
         self.OM_data_eqn = self.OM_data_eqn + ('connect('+self.name+'.'+'condensor_duty'+','+ self.EngStm1.name+'.inlet);\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect('+self.name+'.reboiler_duty'+', '+self.EngStm2.name+'.inlet);\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect('+self.name+'.distillate'+", "+self.OutputStms[0].name+'.inlet);\n')
diff --git a/OMChem/EngStm.py b/src/main/python/OMChem/EngStm.py
index cf938ad..c02a5d5 100644
--- a/OMChem/EngStm.py
+++ b/src/main/python/OMChem/EngStm.py
@@ -14,5 +14,5 @@ class EngStm():
         return self.OM_data_init
 
     def OM_Flowsheet_Eqn(self,addedcomp):
-    	self.OM_data_eqn = ''
-    	return self.OM_data_eqn
+        self.OM_data_eqn=''
+        return self.OM_data_eqn
diff --git a/OMChem/Flash.py b/src/main/python/OMChem/Flash.py
index a3bf5dc..165849a 100644
--- a/OMChem/Flash.py
+++ b/src/main/python/OMChem/Flash.py
@@ -1,13 +1,11 @@
 class Flash():
     counter = 1
     def __init__(self,name='Flash'):
-        #self.name = name[0]
         self.OM_data_eqn = ''
         self.OM_data_init = ''
         self.InputStms = None
         self.OutputStms = None
         self.type = 'flash'
-        #self.count = name[1]
         self.count = Flash.counter
         self.thermoPackage =None
 
diff --git a/OMChem/Flowsheet.py b/src/main/python/OMChem/Flowsheet.py
index f47c203..a83ac4e 100644
--- a/OMChem/Flowsheet.py
+++ b/src/main/python/OMChem/Flowsheet.py
@@ -1,11 +1,11 @@
 import os
 import csv
-from subprocess import Popen, PIPE
+from subprocess import Popen, PIPE,STARTUPINFO,STARTF_USESHOWWINDOW
 import pandas as pd
 
 class Flowsheet():
     def __init__(self):
-        self.sim_name = 'Simulator'
+        self.sim_name = '../Simulator'
         self.sim_method = ''
         self.unit_operations = []
         self.data = []
@@ -54,8 +54,9 @@ class Flowsheet():
         if self.sim_method == 'Eqn':
             simpath = self.eqn_mos_path
             os.chdir(self.sim_dir_path)
-            
-            self.process = Popen([self.omc_path, '-s',simpath], stdout=PIPE, stderr=PIPE)
+            startupinfo = STARTUPINFO
+            startupinfo.dwFlags |= STARTF_USESHOWWINDOW
+            self.process = Popen([self.omc_path, '-s',simpath], stdout=PIPE, stderr=PIPE, startupinfo=startupinfo)
             self.stdout, self.stderr = self.process.communicate()
            
             os.chdir(self.root_dir)
@@ -78,7 +79,7 @@ class Flowsheet():
         # print("############### StdOut ################")
         # print(stdout)
         self.result_data = []
-        print('Simulating '+unitop.name+'...')
+        #print('Simulating '+unitop.name+'...')
         csvpath = os.path.join(self.sim_dir_path,unitop.name+'_res.csv')
         with open(csvpath,'r') as resultFile:
             csvreader = csv.reader(resultFile,delimiter=',')
@@ -240,7 +241,7 @@ class Flowsheet():
                     mosFile.write("loadFile(\""+unitop.name.lower()+".mo\");\n")
                     mosFile.write("simulate("+unitop.name.lower()+", outputFormat=\"csv\", stopTime=1.0, numberOfIntervals=1);\n")
 
-                print("Initiating simulation in Sequential Modular Mode")
+                #print("Initiating simulation in Sequential Modular Mode")
                 self.omc_path = self.get_omc_path()
                 os.chdir(self.sim_dir_path)
                 sim = os.path.join(self.sim_dir_path,unitop.name.lower()+'.mos')
diff --git a/OMChem/Heater.py b/src/main/python/OMChem/Heater.py
index cf9b8f1..a24253d 100644
--- a/OMChem/Heater.py
+++ b/src/main/python/OMChem/Heater.py
@@ -4,12 +4,9 @@ class Heater():
     def __init__(self,name='Heater',PressureDrop = None, eff = None):
         self.PressureDrop = PressureDrop
         self.eff = eff
-        #self.name = name
         self.OM_data_eqn = ''
         self.OM_data_init = ''
         self.InputStms = None
-        #self.heatAdd=heatAdd
-        #self.outT = outT
         self.OutputStms = None
         self.EngStms = EngStm(name='EngStm'+name)
         self.type = 'Heater'
@@ -67,7 +64,6 @@ class Heater():
 
     def OM_Flowsheet_Eqn(self, addedcomp):
         self.OM_data_eqn = ''
-        # self.OM_data_eqn = self.name + '.pressDrop = ' + str(self.PressDrop) + ';\n'
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.InputStms[0].name + '.outlet,' +  self.name + '.inlet' + ');\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.name + '.outlet,' + self.OutputStms[0].name + '.inlet);\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.EngStms.name + '.outlet,' + self.name + '.energy);\n')
diff --git a/OMChem/Mixer.py b/src/main/python/OMChem/Mixer.py
index c726cdc..c726cdc 100644
--- a/OMChem/Mixer.py
+++ b/src/main/python/OMChem/Mixer.py
diff --git a/OMChem/Pump.py b/src/main/python/OMChem/Pump.py
index 3b6ed2c..e9b9149 100644
--- a/OMChem/Pump.py
+++ b/src/main/python/OMChem/Pump.py
@@ -3,12 +3,9 @@ class Pump():
     counter = 1
     def __init__(self,name='Pump',eff = None):
         self.eff = eff
-        #self.name = name
         self.OM_data_eqn = ''
         self.OM_data_init = ''
         self.InputStms = None
-        #self.heatAdd=heatAdd
-        #self.outT = outT
         self.OutputStms = None
         self.EngStms = EngStm(name='EngStm'+name)
         self.type = 'Pump'
@@ -54,7 +51,6 @@ class Pump():
 
     def OM_Flowsheet_Eqn(self, addedcomp):
         self.OM_data_eqn = ''
-        # self.OM_data_eqn = self.name + '.pressDrop = ' + str(self.PressDrop) + ';\n'
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.InputStms[0].name + '.outlet,' +  self.name + '.inlet' + ');\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.name + '.outlet,' + self.OutputStms[0].name + '.inlet);\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.EngStms.name + '.outlet,' + self.name + '.energy);\n')
diff --git a/OMChem/ShortcutColumn.py b/src/main/python/OMChem/ShortcutColumn.py
index a018873..60d9d1b 100644
--- a/OMChem/ShortcutColumn.py
+++ b/src/main/python/OMChem/ShortcutColumn.py
@@ -8,7 +8,6 @@ class ShortcutColumn():
         self.HKey = HKey
         self.LKeyMolFrac = None
         self.HKeyMolFrac = None
-        #self.name = name[0]
         self.name = name + str(ShortcutColumn.counter) 
         self.OM_data_eqn = ''
         self.OM_data_init = ''
@@ -17,7 +16,6 @@ class ShortcutColumn():
        
         self.EngStm1 = EngStm(name='EngStm1'+self.name)
         self.EngStm2 = EngStm(name='EngStm2'+self.name)
-        #self.count = name[1]
         self.count = ShortcutColumn.counter
         self.condType=''
         self.actR = None
diff --git a/OMChem/Splitter.py b/src/main/python/OMChem/Splitter.py
index f873146..98d41ab 100644
--- a/OMChem/Splitter.py
+++ b/src/main/python/OMChem/Splitter.py
@@ -51,7 +51,7 @@ class Splitter():
         self.OM_data_eqn = ''
         comp_count = len(addedcomp)
         strcount = 1
-        print("Output#########",self.OutputStms)
+        #print("Output#########",self.OutputStms)
         for strm in self.OutputStms:
             self.OM_data_eqn = self.OM_data_eqn + (
             'connect(' + strm.name + '.inlet,' + self.name + '.outlet[' + str(strcount) + ']);\n')
diff --git a/OMChem/Valve.py b/src/main/python/OMChem/Valve.py
index 9e8494b..05fa55f 100644
--- a/OMChem/Valve.py
+++ b/src/main/python/OMChem/Valve.py
@@ -1,10 +1,8 @@
 class Valve():
     counter = 1
     def __init__(self,name='Valve'):
-        #self.PressDrop = PressureDrop
         self.mode = None
         self.modeVal = None
-        #self.name = name
         self.OM_data_eqn = ''
         self.OM_data_init = ''
         self.InputStms = None
@@ -56,6 +54,5 @@ class Valve():
         
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.InputStms[0].name + '.outlet,' +  self.name + '.inlet' + ');\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.name + '.outlet,' + self.OutputStms[0].name + '.inlet);\n')
-        print("asdfvfdasdsqdfdedfdfv12345678987654321234567898765")
         self.OM_data_eqn = self.OM_data_eqn + (self.name+'.'+self.mode+'='+ self.modeVal + ';\n')
         return self.OM_data_eqn
\ No newline at end of file
diff --git a/venv/Lib/site-packages/astroid/interpreter/_import/__init__.py b/src/main/python/OMChem/__init__.py
index e69de29..e69de29 100644
--- a/venv/Lib/site-packages/astroid/interpreter/_import/__init__.py
+++ b/src/main/python/OMChem/__init__.py
diff --git a/src/main/python/OMChem/__pycache__/EngStm.cpython-36.pyc b/src/main/python/OMChem/__pycache__/EngStm.cpython-36.pyc
new file mode 100644
index 0000000..a5f5a78
--- /dev/null
+++ b/src/main/python/OMChem/__pycache__/EngStm.cpython-36.pyc
diff --git a/src/main/python/OMChem/__pycache__/EngStm.cpython-37.pyc b/src/main/python/OMChem/__pycache__/EngStm.cpython-37.pyc
new file mode 100644
index 0000000..d065cdb
--- /dev/null
+++ b/src/main/python/OMChem/__pycache__/EngStm.cpython-37.pyc
diff --git a/src/main/python/OMChem/__pycache__/Flowsheet.cpython-36.pyc b/src/main/python/OMChem/__pycache__/Flowsheet.cpython-36.pyc
new file mode 100644
index 0000000..4039084
--- /dev/null
+++ b/src/main/python/OMChem/__pycache__/Flowsheet.cpython-36.pyc
diff --git a/src/main/python/OMChem/__pycache__/Flowsheet.cpython-37.pyc b/src/main/python/OMChem/__pycache__/Flowsheet.cpython-37.pyc
new file mode 100644
index 0000000..1a76d03
--- /dev/null
+++ b/src/main/python/OMChem/__pycache__/Flowsheet.cpython-37.pyc
diff --git a/src/main/python/OMChem/__pycache__/__init__.cpython-37.pyc b/src/main/python/OMChem/__pycache__/__init__.cpython-37.pyc
new file mode 100644
index 0000000..ee871fe
--- /dev/null
+++ b/src/main/python/OMChem/__pycache__/__init__.cpython-37.pyc
diff --git a/OMChem/adiabatic_comp.py b/src/main/python/OMChem/adiabatic_comp.py
index d0a6b72..bda0476 100644
--- a/OMChem/adiabatic_comp.py
+++ b/src/main/python/OMChem/adiabatic_comp.py
@@ -3,7 +3,6 @@ class AdiabaticCompressor():
     counter = 1
     def __init__(self,name='AdiabaticCompressor', eff = None):
         self.eff = eff
-        #self.name = name[0]
         self.name = name + str(AdiabaticCompressor.counter) 
 
         self.OM_data_eqn = ''
@@ -11,7 +10,6 @@ class AdiabaticCompressor():
         self.InputStms = None
         self.OutputStms = None
         self.EngStms = EngStm(name='EngStm'+self.name)
-        #self.count = name[1]
         self.count = AdiabaticCompressor.counter
         self.type = 'AdiabaticCompressor'
         self.thermoPackage ="RaoultsLaw"
@@ -59,7 +57,6 @@ class AdiabaticCompressor():
 
     def OM_Flowsheet_Eqn(self, addedcomp):
         self.OM_data_eqn = ''
-        # self.OM_data_eqn = self.name + '.pressDrop = ' + str(self.PressDrop) + ';\n'
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.InputStms[0].name + '.outlet,' +  self.name + '.inlet' + ');\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.name + '.outlet,' + self.OutputStms[0].name + '.inlet);\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.EngStms.name + '.outlet,' + self.name + '.energy);\n')
diff --git a/OMChem/adiabatic_exp.py b/src/main/python/OMChem/adiabatic_exp.py
index 2754f0a..48381fa 100644
--- a/OMChem/adiabatic_exp.py
+++ b/src/main/python/OMChem/adiabatic_exp.py
@@ -3,14 +3,12 @@ class AdiabaticExpander():
     counter = 1
     def __init__(self,name='AdiabaticExpander', eff = None):
         self.eff = eff
-        #self.name = name[0]
         self.name = name + str(AdiabaticExpander.counter) 
         self.OM_data_eqn = ''
         self.OM_data_init = ''
         self.InputStms = None
         self.OutputStms = None
         self.EngStms = EngStm(name='EngStm'+self.name)
-        #self.count = name[1]
         self.count = AdiabaticExpander.counter
         self.type = 'AdiabaticExpander'
         self.thermoPackage ="RaoultsLaw"
@@ -59,7 +57,6 @@ class AdiabaticExpander():
 
     def OM_Flowsheet_Eqn(self, addedcomp):
         self.OM_data_eqn = ''
-        # self.OM_data_eqn = self.name + '.pressDrop = ' + str(self.PressDrop) + ';\n'
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.InputStms[0].name + '.outlet,' +  self.name + '.inlet' + ');\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.name + '.outlet,' + self.OutputStms[0].name + '.inlet);\n')
         self.OM_data_eqn = self.OM_data_eqn + ('connect(' + self.EngStms.name + '.outlet,' + self.name + '.energy);\n')
diff --git a/OMChem/setup.py b/src/main/python/OMChem/setup.py
index 037da1c..037da1c 100644
--- a/OMChem/setup.py
+++ b/src/main/python/OMChem/setup.py
diff --git a/mainApp.py b/src/main/python/mainApp.py
index d1fb2b7..bd6638c 100644
--- a/mainApp.py
+++ b/src/main/python/mainApp.py
@@ -5,6 +5,11 @@ import ctypes
 import sys
 import datetime
 from functools import partial
+import pyuac
+
+current = os.path.dirname(os.path.realpath(__file__))
+parentPath = os.path.dirname(current)
+sys.path.append(parentPath)
 
 from PyQt5.QtCore import *
 from PyQt5.QtWidgets import *
@@ -13,15 +18,15 @@ import PyQt5.QtGui as QtGui
 import PyQt5.QtCore as QtCore
 import PyQt5.QtWidgets as QtWidgets
 
-from OMChem.Flowsheet import Flowsheet
-from ComponentSelector import *
-from Bin_Phase_env import *
-from UnitOperations import *
-from Streams import *
-from Container import *
-from Graphics import *
+from python.OMChem.Flowsheet import Flowsheet
+from python.utils.ComponentSelector import *
+from python.utils.Bin_Phase_env import *
+from python.utils.UnitOperations import *
+from python.utils.Streams import *
+from python.utils.Container import *
+from python.utils.Graphics import *
 
-ui,_ = loadUiType('main.ui')
+ui,_ = loadUiType(parentPath+'/ui/utils/main.ui')
 
 '''
     MainApp class is responsible for all the main App Ui operations
@@ -82,10 +87,10 @@ class MainApp(QMainWindow,ui):
         self.actionSequentialMode.setShortcut('Ctrl+M') 
         self.actionEquationOriented.triggered.connect(partial(self.simulate,'EQN'))
         self.actionEquationOriented.setShortcut('Ctrl+E')
-        self.actionUndo.triggered.connect(self.undo)
-        self.actionUndo.setShortcut('Ctrl+Z')
-        self.actionRedo.triggered.connect(self.redo)
-        self.actionRedo.setShortcut('Ctrl+Y')
+        # self.actionUndo.triggered.connect(self.undo)
+        # self.actionUndo.setShortcut('Ctrl+Z')
+        # self.actionRedo.triggered.connect(self.redo)
+        # self.actionRedo.setShortcut('Ctrl+Y')
         self.actionSave.triggered.connect(self.save)
         self.actionSave.setShortcut('Ctrl+S')
         self.actionOpen.triggered.connect(self.open)
@@ -232,7 +237,7 @@ class MainApp(QMainWindow,ui):
     '''        
     def new(self):
         self.setWindowTitle('Untitled - Chemical Simulator GUI')
-        self.undo_redo_helper()
+        #self.undo_redo_helper()
         self.comp = ComponentSelector(self)
         self.textBrowser.append("<span>[" + str(self.current_time()) + "] <b>New</b> flowsheet is created ... </span>")
         dock_widget_lst.clear()
@@ -248,61 +253,61 @@ class MainApp(QMainWindow,ui):
         except Exception as e:
             print(e)
 
-    '''
-        It helps by clearing screen and loading the objects by undo redo methods
-    '''
-    def undo_redo_helper(self):
-        for i in self.container.unit_operations:
-            type(i).counter = 1
-        self.container = None
-        for i in dock_widget_lst:
-            i.hide()
-            del i
-        lst.clear()
-        self.container = Container(self.textBrowser, self.graphicsView)
-
-        compound_selected.clear()
-        self.scene = self.container.graphics.get_scene()
-        self.graphicsView.setScene(self.scene)
-        self.graphicsView.setMouseTracking(True)
-        self.graphicsView.keyPressEvent=self.delete_call
-
-    '''
-        Function for undo 
-    '''
-    def undo(self):
-        redo_data = pop('Undo')
-        if redo_data is not None:
-            push('Redo', redo_data)
-            undo_data = get_last_list('Undo')
-            messages = self.textBrowser.toPlainText()
-            try:
-                self.undo_redo_helper()
-                self.container.graphics.load_canvas(undo_data, self.container)
-                self.textBrowser.setText(messages)
-            except Exception as e:
-                print(e)
-                self.textBrowser.append(messages)
-        else:
-            messages = self.textBrowser.toPlainText()
-            self.textBrowser.setText(messages)
-            self.textBrowser.append("<span>[" + str(self.current_time()) + "] <b>No more undo can be done!</b>... </span>")
-
-    '''
-        Function for redo 
-    '''
-    def redo(self):
-        redo_data = pop('Redo')
-        if redo_data is not None:
-            push('Undo', redo_data)
-            messages = self.textBrowser.toPlainText()
-            self.undo_redo_helper()
-            self.container.graphics.load_canvas(redo_data, self.container)
-            self.textBrowser.setText(messages)
-        else:
-            messages = self.textBrowser.toPlainText()
-            self.textBrowser.setText(messages)
-            self.textBrowser.append("<span>[" + str(self.current_time()) + "] <b>No more redo can be done!</b>... </span>")
+    # '''
+    #     It helps by clearing screen and loading the objects by undo redo methods
+    # '''
+    # def undo_redo_helper(self):
+    #     for i in self.container.unit_operations:
+    #         type(i).counter = 1
+    #     self.container = None
+    #     for i in dock_widget_lst:
+    #         i.hide()
+    #         del i
+    #     lst.clear()
+    #     self.container = Container(self.textBrowser, self.graphicsView)
+
+    #     compound_selected.clear()
+    #     self.scene = self.container.graphics.get_scene()
+    #     self.graphicsView.setScene(self.scene)
+    #     self.graphicsView.setMouseTracking(True)
+    #     self.graphicsView.keyPressEvent=self.delete_call
+
+    # '''
+    #     Function for undo 
+    # '''
+    # def undo(self):
+    #     redo_data = pop('Undo')
+    #     if redo_data is not None:
+    #         push('Redo', redo_data)
+    #         undo_data = get_last_list('Undo')
+    #         messages = self.textBrowser.toPlainText()
+    #         try:
+    #             self.undo_redo_helper()
+    #             self.container.graphics.load_canvas(undo_data, self.container)
+    #             self.textBrowser.setText(messages)
+    #         except Exception as e:
+    #             print(e)
+    #             self.textBrowser.append(messages)
+    #     else:
+    #         messages = self.textBrowser.toPlainText()
+    #         self.textBrowser.setText(messages)
+    #         self.textBrowser.append("<span>[" + str(self.current_time()) + "] <b>No more undo can be done!</b>... </span>")
+
+    # '''
+    #     Function for redo 
+    # '''
+    # def redo(self):
+    #     redo_data = pop('Redo')
+    #     if redo_data is not None:
+    #         push('Undo', redo_data)
+    #         messages = self.textBrowser.toPlainText()
+    #         self.undo_redo_helper()
+    #         self.container.graphics.load_canvas(redo_data, self.container)
+    #         self.textBrowser.setText(messages)
+    #     else:
+    #         messages = self.textBrowser.toPlainText()
+    #         self.textBrowser.setText(messages)
+    #         self.textBrowser.append("<span>[" + str(self.current_time()) + "] <b>No more redo can be done!</b>... </span>")
 
     '''
         Function for saving the current canvas items and compound_selected
@@ -343,7 +348,7 @@ class MainApp(QMainWindow,ui):
                 fileName = file_name.split('/')[-1].split('.')[0]
                 self.setWindowTitle(fileName+' - Chemical Simulator GUI')
 
-                self.undo_redo_helper()
+                #self.undo_redo_helper()
 
                 with open(file_name, 'rb') as f:
                     obj = pickle.load(f)
@@ -362,7 +367,7 @@ class MainApp(QMainWindow,ui):
                 for i in dock_widget_lst:
                     #Submitting values 
                     i.param()
-
+                
                 #Disbaling input data tab for output stream
                 for i in self.container.graphics.scene.items():
                     if (isinstance(i, NodeItem) and i.type == 'MaterialStream'):
@@ -396,8 +401,8 @@ class MainApp(QMainWindow,ui):
     
 def main():
 
-    clean_file('Undo')
-    clean_file('Redo')
+    # clean_file('Undo')
+    # clean_file('Redo')
 
     app = QApplication(sys.argv)
     window = MainApp()
@@ -406,4 +411,7 @@ def main():
     
 
 if __name__ == '__main__':
-    main()
+    if not pyuac.isUserAdmin():
+        pyuac.runAsAdmin()
+    else:
+        main()
diff --git a/Bin_Phase_env.py b/src/main/python/utils/Bin_Phase_env.py
index 9a9d873..dd6f938 100644
--- a/Bin_Phase_env.py
+++ b/src/main/python/utils/Bin_Phase_env.py
@@ -17,7 +17,13 @@ from PyQt5.uic import loadUiType
 import pyqtgraph as pg
 import pyqtgraph.exporters
 
-ui_dialog,_ = loadUiType('Binary_Phase_Env.ui')
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
+ui_dialog,_ = loadUiType(parentPath+'/ui/utils/Binary_Phase_Env.ui')
+pg.CONFIG_OPTIONS['crashWarning'] = False
 
 class BinPhaseEnv(QWidget,ui_dialog):
     def __init__(self,comp):
@@ -36,7 +42,7 @@ class BinPhaseEnv(QWidget,ui_dialog):
 
         self.comboBox_2.addItem(str(self.compunds[0]))  
 
-        self.lines = [line.rstrip('\n') for line in open('thermopackage.txt')]
+        self.lines = [line.rstrip('\n') for line in open(parentPath+'/python/utils/thermopackage.txt')]
         for j in self.lines:
             self.comboBox_3.addItem(str(j))
 
@@ -92,7 +98,7 @@ class BinPhaseEnv(QWidget,ui_dialog):
                 self.omhome = '/usr'    
             return os.path.join(self.omhome, 'bin', 'omc')
         except BaseException:
-            print("The OpenModelica compiler is missing in the System path please install it" )
+            #print("The OpenModelica compiler is missing in the System path please install it" )
             raise
 
     def plot(self):        
@@ -106,7 +112,7 @@ class BinPhaseEnv(QWidget,ui_dialog):
             data_points = 0    
 
         self.curr_path = os.getcwd()
-        self.sim_dir_path = os.path.join(self.curr_path,'Simulator')
+        self.sim_dir_path = os.path.join(self.curr_path,'./../Simulator')
         self.Graphmo_path = os.path.join(self.sim_dir_path,'Graph.mo')
         self.plot_mos_path = os.path.join(self.sim_dir_path,'PlotGraph.mos')
 
diff --git a/ComponentSelector.py b/src/main/python/utils/ComponentSelector.py
index 56c6078..44a2696 100644
--- a/ComponentSelector.py
+++ b/src/main/python/utils/ComponentSelector.py
@@ -4,8 +4,13 @@ from PyQt5.QtGui import *
 from PyQt5.uic import loadUiType
 import os, sys
 import pandas as pd
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parent)
+
 from Simulator.Databases.Databases import ChemsepDatabase
-ui_dialog,_ = loadUiType('ComponentSelector.ui')
+ui_dialog,_ = loadUiType(parentPath+'/ui/utils/ComponentSelector.ui')
 
 
 #df = pd.read_csv("compoundsDatabase.csv")
@@ -19,7 +24,6 @@ class ComponentSelector(QDialog,ui_dialog):
         self.setupUi(self)
     
         self.dict1=dict()#empty dictionary which will store the obj and its compound
-        #self.DB1=#instance of Database class in Database.py module 
         self.instance=[ChemsepDatabase()]  #list of all the instances
         self.lines=[]
         
@@ -27,14 +31,7 @@ class ComponentSelector(QDialog,ui_dialog):
             x=i.get_comp_name_list()
             self.dict1[i]=x
             self.lines+=x
-        #print(self.lines)
-            
-            
-        #self.DB1_list=self.DB1.get_comp_name_list()
-		#storingchemsep
-        #database compound list in DB1_list
-        #self.dict1[self.DB1]=self.DB1_list #storing the list as a value and the db as key in dictionary
-        #self.lines=self.DB1_list #combined list of all the edited compounds        
+        #print(self.lines)   
        
         self.model = QStringListModel()
         self.model.setStringList(self.lines)
@@ -166,7 +163,7 @@ class ComponentSelector(QDialog,ui_dialog):
         return compound_selected
      
     def final_mo(self):
-        self.f_mo=open('Simulator/database.mo','w+')
+        self.f_mo=open(parentPath+'/Simulator/database.mo','w+')
         self.f_mo.write('package database\n')
         for line in self.prop_list:
             self.f_mo.write(line)
diff --git a/Container.py b/src/main/python/utils/Container.py
index fe5fae4..139346c 100644
--- a/Container.py
+++ b/src/main/python/utils/Container.py
@@ -1,11 +1,17 @@
 from collections import defaultdict
 import datetime
 import pickle 
-import os
+import os,sys
 
-from OMChem.Flowsheet import Flowsheet
-from ComponentSelector import *
-from Graphics import *
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
+from python.OMChem.Flowsheet import Flowsheet
+from python.utils.ComponentSelector import *
+from python.utils.Graphics import NodeItem, Graphics, dock_widget_lst
+from python.DockWidgets.DockWidget import DockWidget
 
 class Container():
     def __init__(self,msgbrowser, graphicsView):
@@ -44,7 +50,7 @@ class Container():
                 self.unit_operations.append(obj)
                 data = self.unit_operations[:]
                 data.append(compound_selected)
-                push('Undo', data)
+                #push('Undo', data)
                 self.msg.append("<span style=\"color:blue\">["+str(self.current_time())+"]<b> "+obj.name+" </b>is instantiated .""</span>")
 
     '''
@@ -86,10 +92,10 @@ class Container():
                 del item.obj
             del item
 
-            clean_file('Redo')
-            data = self.unit_operations[:]
-            data.append(compound_selected)
-            push('Undo', data)
+            # clean_file('Redo')
+            # data = self.unit_operations[:]
+            # data.append(compound_selected)
+            # push('Undo', data)
 
     def fetch_object(self,name):
         for i in self.unit_operations:
@@ -121,14 +127,26 @@ class Container():
     def simulate(self,mode):
 
         self.disableInterfaceforSimulation(True)
-        
+        toAppend = ''
         for i in self.graphics.scene.items():
-            if (isinstance(i, NodeItem)):
+            showConnectionWarning = False
+            if isinstance(i, NodeItem):
                 try:
                     i.dock_widget.clear_results()
                 except AttributeError:
                     pass
 
+                for ip in i.input:
+                    if len(ip.in_lines) == 0:
+                        showConnectionWarning = True
+                for op in i.output:
+                    if len(op.out_lines) == 0:
+                        showConnectionWarning = True
+                if showConnectionWarning:
+                    if toAppend != '':
+                        toAppend+='<br>'
+                    toAppend+="<span style=\"color:#999900\">Warning: "+i.name+" - Missing Socket Connection(s).</span>"
+
         #print("SIMULATE")
         #print(mode)
         self.compounds = compound_selected
@@ -141,12 +159,14 @@ class Container():
             
         if mode=='SM':
             self.msg.append("<span>["+str(self.current_time())+"] Simulating in <b>Sequential</b> mode ... </span>")
+            self.msg.append(toAppend)
             self.flowsheet.simulate_SM(self.ip,self.op)
             self.msg_browser()
             self.result=self.flowsheet.result_data
             
         elif mode=='EQN':
             self.msg.append("<span>["+str(self.current_time())+"] Simulating in <b>equation</b> mode ... </span>")
+            self.msg.append(toAppend)
             self.flowsheet.simulate_EQN(self.msg)
             self.result=self.flowsheet.result_data
 
diff --git a/Graphics.py b/src/main/python/utils/Graphics.py
index 1d9e7ef..eb9b3b9 100644
--- a/Graphics.py
+++ b/src/main/python/utils/Graphics.py
@@ -5,20 +5,26 @@ import PyQt5.QtGui as QtGui
 import PyQt5.QtCore as QtCore
 import PyQt5.QtWidgets as QtWidgets
 from PyQt5.QtWidgets import QLineEdit
-
-from DockWidgets.DockWidget import *
-from DockWidgets.DockWidgetMaterialStream import *
-from DockWidgets.DockWidgetDistillationColumn import *
-from DockWidgets.DockWidgetShortcutColumn import *
-from DockWidgets.DockWidgetMixer import *
-from DockWidgets.DockWidgetSplitter import *
-from DockWidgets.DockWidgetFlash import *
-from DockWidgets.DockWidgetCompoundSeparator import *
-from DockWidgets.DockWidgetCompressorExpander import *
-from Container import *
-from Streams import *
-from UnitOperations import *
-from ComponentSelector import *
+import os, sys
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
+from python.DockWidgets.DockWidget import *
+from python.DockWidgets.DockWidgetMaterialStream import *
+from python.DockWidgets.DockWidgetDistillationColumn import *
+from python.DockWidgets.DockWidgetShortcutColumn import *
+from python.DockWidgets.DockWidgetMixer import *
+from python.DockWidgets.DockWidgetSplitter import *
+from python.DockWidgets.DockWidgetFlash import *
+from python.DockWidgets.DockWidgetCompoundSeparator import *
+from python.DockWidgets.DockWidgetCompressorExpander import *
+from python.utils.Container import *
+from python.utils.Streams import *
+from python.utils.UnitOperations import *
+from python.utils.ComponentSelector import *
 
 class Graphics(QDialog, QtWidgets.QGraphicsItem):
 
@@ -295,7 +301,7 @@ class NodeSocket(QtWidgets.QGraphicsItem):
         cursor = QCursor( Qt.ArrowCursor )
         QApplication.instance().setOverrideCursor(cursor)
 
-        if self.type == 'op':
+        if self.type == 'op'and len(self.out_lines) == 0:
             rect = self.boundingRect()
             pointA = QtCore.QPointF(rect.x() + rect.width()/(2), rect.y() + rect.height()/(2))
             pointA = self.mapToScene(pointA)
@@ -303,7 +309,7 @@ class NodeSocket(QtWidgets.QGraphicsItem):
             self.new_line = NodeLine(pointA, pointB ,'op')
             self.out_lines.append(self.new_line)
             self.scene().addItem(self.new_line)    
-        elif self.type == 'in':
+        elif self.type == 'in' and len(self.in_lines) == 0:
             rect = self.boundingRect()
             pointA = self.mapToScene(event.pos())
             pointB = QtCore.QPointF(rect.x() + rect.width()/(2), rect.y() + rect.height()/(2))
@@ -342,7 +348,7 @@ class NodeSocket(QtWidgets.QGraphicsItem):
         item = self.scene().itemAt(event.scenePos().toPoint(),QtGui.QTransform())
         stm = ['MaterialStream','EngStm']
         item.other_line=self.new_line
-        if (self.type == 'op') and (item.type == 'in'):
+        if self.type == 'op' and item.type == 'in' and len(item.in_lines) == 0:
             self.new_line.source = self
             self.new_line.target = item
             item.in_lines.append(self.new_line)
@@ -364,7 +370,7 @@ class NodeSocket(QtWidgets.QGraphicsItem):
                 if(tg_no_input_lines > 0):
                     tg.obj.disableInputDataTab(tg.dock_widget)
 
-        elif (self.type =='in') and (item.type == 'op'):
+        elif self.type =='in' and item.type == 'op' and len(item.out_lines) == 0:
             self.new_line.source = item
             self.new_line.target = self
             item.out_lines.append(self.new_line)
@@ -470,35 +476,21 @@ class NodeItem(QtWidgets.QGraphicsItem):
                     default_tooltip = default_tooltip + f"   {i} : {j}\n"
             self.setToolTip(default_tooltip)
 
-        dlg = QMessageBox()
-        dlg.setWindowTitle("Error")
-        dlg.setIcon(QMessageBox.Critical)
-        dlg.setText('Enter valid input value!')
-
         if self.obj.type == 'Mixer' and not self.obj.saved:
-            text, self.ok = QInputDialog.getText(self.container.graphicsView, 'Mixer', 'Enter number of input(2-4):',
-                                            echo=QLineEdit.Normal, text=str(self.obj.no_of_inputs))
-            while self.ok and (int(text)< 2 or int(text) > 4):
-                dlg.exec_()
-                text, self.ok = QInputDialog.getText(self.container.graphicsView, 'Mixer', 'Enter number of input(2-4):',
-                                            echo=QLineEdit.Normal, text=str(self.obj.no_of_inputs))
+            combob_values = map(str,list(range(2,5)))
+            text, self.ok = QInputDialog.getItem(self.container.graphicsView, 'Mixer', 'Select number of inputs:',
+                                            combob_values, False)
+            
             if self.ok:
                 self.nin = int(text)
                 self.obj.no_of_inputs = self.nin
                 self.obj.variables['NI']['value'] = self.nin
-        # elif self.obj.type == 'Splitter' and not self.obj.saved:
-        #     text, ok = QInputDialog.getText(self.container.graphicsView, 'Splitter', 'Enter number of output:')
-        #     if ok and text:
-        #         self.nop = int(text)
-        #         self.obj.no_of_outputs = self.nop
-        #         self.obj.variables['No']['value'] = self.nop
+
         elif self.obj.type == 'DistillationColumn'and not self.obj.saved:
-            text, self.ok = QInputDialog.getText(self.container.graphicsView, 'DistillationColumn', 'Enter number of input(1-8):',
-                                            echo=QLineEdit.Normal, text=str(self.obj.no_of_inputs))
-            while self.ok and (int(text)< 1 or int(text) > 8):
-                dlg.exec_()
-                text, self.ok = QInputDialog.getText(self.container.graphicsView, 'DistillationColumn', 'Enter number of input(1-8):',
-                                        echo=QLineEdit.Normal, text=str(self.obj.no_of_inputs))
+            combob_values = map(str,list(range(1,9)))
+            text, self.ok = QInputDialog.getItem(self.container.graphicsView, 'DistillationColumn', 'Select number of input(s):',
+                                            combob_values, False)
+
             if self.ok:
                 self.nin = int(text)
                 self.obj.no_of_inputs = self.nin
@@ -527,7 +519,6 @@ class NodeItem(QtWidgets.QGraphicsItem):
         # updating input values
         if self.dock_widget.obj.type != 'MaterialStream':
             pass
-            #print(self.dock_widget.obj.type)
             try:
                 self.dock_widget.obj.param_setter(self.dock_widget.obj.param_getter(self.dock_widget.obj.mode))
             except Exception as e:
@@ -536,7 +527,7 @@ class NodeItem(QtWidgets.QGraphicsItem):
 
         self.dock_widget.hide()
         
-        self.pic=QtGui.QPixmap("Icons/"+self.type+".png")
+        self.pic=QtGui.QPixmap(parentPath+"/resources/base/Icons/"+self.type+".png")
         self.rect = QtCore.QRect(0,0,self.pic.width(),self.pic.height())
         self.text = QGraphicsTextItem(self)
         f = QFont()
diff --git a/Streams.py b/src/main/python/utils/Streams.py
index 1afa2bc..fa557e6 100644
--- a/Streams.py
+++ b/src/main/python/utils/Streams.py
@@ -1,7 +1,13 @@
 import json
-import sys
+import sys,os
+
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
 from PyQt5.QtCore import *
-from ComponentSelector import compound_selected
+from python.utils.ComponentSelector import compound_selected
 
 class MaterialStream():
     counter = 1
@@ -37,16 +43,16 @@ class MaterialStream():
             'T'     : {'name':'Temperature',      'value':300,       'unit':'K'},
             
             'xvap'   : {'name':'Vapour Mole Fraction',          'value':None,       'unit':''},
-            'H_p[1]'  : {'name':'Mixture Molar Entalpy',        'value':None,       'unit':'J/mol'},
+            'H_p[1]'  : {'name':'Mixture Molar Enthalpy',        'value':None,       'unit':'J/mol'},
             'S_p[1]'  : {'name':'Mixture Molar Entropy',        'value':None,       'unit':'J/mol.K'},
             'F_p[1]'  : {'name':'Mixture Molar Flow',           'value':100,       'unit':'mol/s'},
             'Fm_p[1]' : {'name':'Mixture Mass Flow',            'value':None,    'unit':'g/s'},
 
-            'H_p[2]'  : {'name':'Liquid Molar Entalpy',        'value':None,       'unit':'J/mol'},
+            'H_p[2]'  : {'name':'Liquid Molar Enthalpy',        'value':None,       'unit':'J/mol'},
             'S_p[2]'  : {'name':'Liquid Molar Entropy',        'value':None,       'unit':'J/mol.K'},
             'F_p[2]'  : {'name':'Liquid Molar Flow',            'value':None,       'unit':'mol/s'},
 
-            'H_p[3]'  : {'name':'Vapour Molar Entalpy',        'value':None,       'unit':'J/mol'},
+            'H_p[3]'  : {'name':'Vapour Molar Enthalpy',        'value':None,       'unit':'J/mol'},
             'S_p[3]'  : {'name':'Vapour Molar Entropy',        'value':None,       'unit':'J/mol.K'},
             'F_p[3]'  : {'name':'Vapour Molar Flow',            'value':None,       'unit':'mol/s'},
 
@@ -148,10 +154,14 @@ class MaterialStream():
         temp_val = self.variables['T']['value']
         temp_unit =  self.variables['T']['unit']
         mixMolEntal_name = self.variables['H_p[1]']['name']
-        mixMolEntal_val = round(float(self.variables['H_p[1]']['value']),2)
+        mixMolEntal_val = self.variables['H_p[1]']['value']
+        if mixMolEntal_val != None:
+            mixMolEntal_val = round(float(self.variables['H_p[1]']['value']),4)
         mixMolEntal_unit =  self.variables['H_p[1]']['unit']
         mixMolEntro_name = self.variables['S_p[1]']['name']
-        mixMolEntro_val = round(float(self.variables['S_p[1]']['value']),2)
+        mixMolEntro_val = self.variables['S_p[1]']['value']
+        if mixMolEntro_val != None:
+            mixMolEntro_val = round(float(self.variables['S_p[1]']['value']),4)
         mixMolEntro_unit =  self.variables['S_p[1]']['unit']
         vapMolFrac_name = self.variables['xvap']['name']
         vapMolFrac_val = self.variables['xvap']['value']
@@ -160,7 +170,9 @@ class MaterialStream():
         mixMolFlo_val = self.variables['F_p[1]']['value']
         mixMolFlo_unit =  self.variables['F_p[1]']['unit']
         mixMassFlo_name = self.variables['Fm_p[1]']['name']
-        mixMassFlo_val = round(float(self.variables['Fm_p[1]']['value']),2)
+        mixMassFlo_val = self.variables['Fm_p[1]']['value']
+        if mixMassFlo_val != None:
+            mixMassFlo_val = round(float(self.variables['Fm_p[1]']['value']),4)
         mixMassFlo_unit =  self.variables['Fm_p[1]']['unit']
         
         dict = {pressure_name:str(pressure_val)+' '+pressure_unit, 
@@ -183,38 +195,57 @@ class MaterialStream():
                 pass
         self.variables['x_pc']['value'] = temp
 
+        pressure_val = self.variables['P']['value']
+        temp_val = self.variables['T']['value']
+        mixMolFlo_val = self.variables['F_p[1]']['value']
+        mixMolEntal_val = self.variables['H_p[1]']['value']
+        vapMolFrac_val = self.variables['xvap']['value']
+        mixMolEntro_val = self.variables['S_p[1]']['value']
+
+        if pressure_val != None:
+            pressure_val = round(float(self.variables['P']['value']),4)
+        if temp_val != None:
+            temp_val = round(float(self.variables['T']['value']),4)
+        if mixMolFlo_val != None:
+            mixMolFlo_val = round(float(self.variables['F_p[1]']['value']),4)
+        if mixMolEntal_val != None:
+            mixMolEntal_val = round(float(self.variables['H_p[1]']['value']),4)
+        if vapMolFrac_val != None:
+            vapMolFrac_val = round(float(self.variables['xvap']['value']),4)
+        if mixMolEntro_val != None:
+            mixMolEntro_val = round(float(self.variables['S_p[1]']['value']),4)
         if(mode=="PT"):
             self.mode1 = 'P'
             self.mode2 = 'T'
-            
-            dict = {self.mode1:self.variables['P']['value'], self.mode2:self.variables['T']['value'],
-                    "MolFlow":self.variables['F_p[1]']['value'],"x_pc":self.variables['x_pc']['value'],
+
+            dict = {self.mode1:pressure_val, self.mode2:temp_val,
+                    "MolFlow":mixMolFlo_val,"x_pc":self.variables['x_pc']['value'],
                     "Thermo Package": self.thermo_package}
             #print('dictionary is :' + str(dict))
 
         elif(mode=="PH"):
             self.mode1 = 'P'
             self.mode2 = 'H_p[1]'
-            dict = {self.mode1:self.variables['P']['value'], self.mode2:self.variables['H_p[1]']['value'],
-                    "MolFlow":self.variables['F_p[1]']['value'], "x_pc":self.variables['x_pc']['value'],
+            dict = {self.mode1:pressure_val, self.mode2:mixMolEntal_val,
+                    "MolFlow":mixMolFlo_val, "x_pc":self.variables['x_pc']['value'],
                     "Thermo Package": self.thermo_package}
         elif(mode=="PVF"):
             self.mode1 = 'P'
             self.mode2 = 'xvap'
-            dict = {self.mode1:self.variables['P']['value'], self.mode2:self.variables['xvap']['value'],
-                    "MolFlow":self.variables['F_p[1]']['value'], "x_pc":self.variables['x_pc']['value'],
+            dict = {self.mode1:pressure_val, self.mode2:vapMolFrac_val,
+                    "MolFlow":mixMolFlo_val, "x_pc":self.variables['x_pc']['value'],
                     "Thermo Package": self.thermo_package}
         elif(mode=="TVF"):
             self.mode1 = 'T'
             self.mode2 = 'xvap'
-            dict = {self.mode1:self.variables['T']['value'], self.mode2:self.variables['xvap']['value'],
-                    "MolFlow":self.variables['F_p[1]']['value'], "x_pc":self.variables['x_pc']['value'],
+            dict = {self.mode1:temp_val, self.mode2:vapMolFrac_val,
+                    "MolFlow":mixMolFlo_val, "x_pc":self.variables['x_pc']['value'],
                     "Thermo Package": self.thermo_package}
         elif(mode=="PS"):
             self.mode1 = 'P'
             self.mode2 = 'S_p[1]'
-            dict = {self.mode1:self.variables['P']['value'], self.mode2: self.variables['S_p[1]']['value'],
-                    "MolFlow":self.variables['F_p[1]']['value'], "x_pc":self.variables['x_pc']['value'],
+            dict = {self.mode1:pressure_val, self.mode2: mixMolEntro_val,
+                    "MolFlow":mixMolFlo_val, "x_pc":self.variables['x_pc']['value'],
                     "Thermo Package": self.thermo_package}
         
         return dict
@@ -392,9 +423,9 @@ class MaterialStream():
 
         except Exception as e:
             exc_type, exc_obj, exc_tb = sys.exc_info()
-            print(exc_type,exc_tb.tb_lineno)
-            print(e)
-            print('error')
+            # print(exc_type,exc_tb.tb_lineno)
+            # print(e)
+            # print('error')
 
     def OM_Flowsheet_Initialize(self,addedcomp):
         self.OM_data_init = ''
@@ -431,15 +462,15 @@ class MaterialStream():
     def disableInputDataTab(self,dockwidget):
         #setting the value of input data tab in dock widget and disabling them
         dockwidget.comboBox.setDisabled(True)
-        dockwidget.input_dict['P'].setText(str(round(float(self.variables['P']['value']),2)))
+        dockwidget.input_dict['P'].setText(str(round(float(self.variables['P']['value']),4)))
         dockwidget.input_dict['P'].setDisabled(True)
-        dockwidget.input_dict['T'].setText(str(round(float(self.variables['T']['value']),2)))
+        dockwidget.input_dict['T'].setText(str(round(float(self.variables['T']['value']),4)))
         dockwidget.input_dict['T'].setDisabled(True)
-        dockwidget.input_dict['MolFlow'].setText(str(round(float(self.variables['F_p[1]']['value']),2)))
+        dockwidget.input_dict['MolFlow'].setText(str(round(float(self.variables['F_p[1]']['value']),4)))
         dockwidget.input_dict['MolFlow'].setDisabled(True)
         dockwidget.cbTP.setCurrentText(str(self.thermo_package))
         dockwidget.cbTP.setDisabled(True)
         dockwidget.pushButton_2.setDisabled(True)
         for index,k in enumerate(dockwidget.x_pclist):
-            k.setText(str(round(float(self.variables['x_pc[1,'+ str(index+1)+']']['value']),2)))
+            k.setText(str(round(float(self.variables['x_pc[1,'+ str(index+1)+']']['value']),4)))
             k.setDisabled(True)
diff --git a/UnitOperations.py b/src/main/python/utils/UnitOperations.py
index 064b2da..86a1ad7 100644
--- a/UnitOperations.py
+++ b/src/main/python/utils/UnitOperations.py
@@ -1,7 +1,14 @@
-from OMChem.Flowsheet import Flowsheet
-from OMChem.EngStm import EngStm
-from ComponentSelector import *
-from Container import *
+import os,sys
+import json
+current = os.path.dirname(os.path.realpath(__file__))
+parent = os.path.dirname(current)
+parentPath = os.path.dirname(parent)
+sys.path.append(parentPath)
+
+from python.OMChem.Flowsheet import Flowsheet
+from python.OMChem.EngStm import EngStm
+from python.utils.ComponentSelector import *
+from python.utils.Container import *
 from PyQt5.QtCore import *
 
 class UnitOperation():
@@ -57,7 +64,7 @@ class UnitOperation():
         return params
         
     def param_setter(self,params):
-        print("param_setter ", params)
+        #print("param_setter ", params)
         try:
             self.mode = list(params.keys())[0]
         except Exception as e:
@@ -160,7 +167,7 @@ class UnitOperation():
                 self.OM_data_eqn += ('connect(' + strm.name + '.Out,' + self.name + '.In[' + str(strcount) + ']);\n')
                 strcount += 1
         else:
-            print(self.input_stms)
+            #print(self.input_stms)
             self.OM_data_eqn += ('connect(' + self.name + '.In,' + self.input_stms[1].name + '.Out);\n')
 
         if len(self.output_stms)>1:
@@ -169,9 +176,11 @@ class UnitOperation():
                 self.OM_data_eqn += ('connect(' + strm.name + '.In,' + self.name + '.Out[' + str(strcount) + ']);\n')
                 strcount += 1
         else:
-            print("self.output_stms ", self.output_stms)
-            self.OM_data_eqn += ('connect(' + self.name + '.Out,' + self.output_stms[1].name + '.In);\n')
-        
+            #print("self.output_stms ", self.output_stms)
+            try:
+                self.OM_data_eqn += ('connect(' + self.name + '.Out,' + self.output_stms[1].name + '.In);\n')
+            except:
+                pass
         if self.mode:
             self.OM_data_eqn += (self.name + '.' + self.mode + '=' + str(self.mode_val) + ';\n')
 
@@ -224,7 +233,7 @@ class ShortcutColumn(UnitOperation):
         self.compounds = [c[:c.index('(')] for c in compound_selected]
 
     def param_setter(self,params):
-        print("param_setter ", params)
+        #print("param_setter ", params)
         self.variables['HKey']['value'] = self.compounds.index(params[0]) + 1
         self.variables['LKey']['value'] = self.compounds.index(params[1]) + 1
         self.variables['HKey_x_pc']['value'] = params[2]
@@ -261,10 +270,8 @@ class DistillationColumn(UnitOperation):
         self.EngStm2 = EngStm(name='EngStm2'+self.name)
         self.count = DistillationColumn.counter
         self.thermo_pack_req = True
-        # self.modes_list = ['RR', 'Nout', 'T']
         self.modes_list = []
         self.parameters = ['Nt', 'Ni', 'Ctype', 'Pcond', 'condmode', 'C_comp', 'C_Spec', 'Preb', 'rebmode', 'rebcomp', 'R_Spec']
-        #self.parameters = ['Nt', 'InT_s', 'In_s', 'thermo_package', 'Ctype', 'Pcond', 'Preb']
         self.result_parameters = ['Cduty.Q', 'Rduty.Q']
         self.Cspec_list = ['Reflux Ratio','Product Molar Flow   (mol/s)', 'Temperature  (K)', 'Compound Molar Fraction',    'Compound Molar Flow    (mol/s)']
         self.Rspec_list = ['Product Molar Flow   (mol/s)', 'Temperature  (K)', 'Compound Molar Fraction',    'Compound Molar Flow    (mol/s)']
@@ -293,7 +300,7 @@ class DistillationColumn(UnitOperation):
         self.compounds = [c[:c.index('(')] for c in compound_selected]
 
     def param_setter(self,params):
-        print("param_setter ", params)
+        #print("param_setter ", params)
         temp = 0
         self.variables['Nt']['value'] = params[0]
         for i in range(self.variables['Ni']['value']):
@@ -318,7 +325,7 @@ class DistillationColumn(UnitOperation):
             self.variables['R_Spec']['comp'] = params[temp+8]
         self.variables['R_Spec']['value'] = params[temp+9]
         self.variables['thermo_package']['value'] = params[temp+10]
-        print(self.variables)
+        #print(self.variables)
 
     def OM_Flowsheet_Initialize(self):
         self.OM_data_init = ''
@@ -353,17 +360,10 @@ class DistillationColumn(UnitOperation):
                     + str(self.variables['Ni']['value']) + ",InT_s=" + "{" +
                     str(self.variables['InT_s']['value']).strip('[').strip(']') + "}" + ',Ctype ="' +
                     self.variables['Ctype']['value'] + '");\n')
-        # self.OM_data_init = self.OM_data_init + 'Simulator.Streams.Energy_Stream '+self.EngStm1.name+';\n'
-        # self.OM_data_init = self.OM_data_init + 'Simulator.Streams.Energy_Stream '+self.EngStm2.name+';\n'
         return self.OM_data_init
 
     def OM_Flowsheet_Equation(self):
         self.OM_data_eqn = ''
-        # self.OM_data_eqn = self.name + '.pressDrop = ' + str(self.PressDrop) + ';\n'
-        # self.OM_data_eqn = self.OM_data_eqn + (
-        #             'connect(' + self.name + '.' + 'condensor_duty' + ',' + self.EngStm1.name + '.inlet);\n')
-           # self.OM_data_eqn = self.OM_data_eqn + (
-           #             'connect(' + self.name + '.reboiler_duty' + ', ' + self.EngStm2.name + '.inlet);\n')
         self.OM_data_eqn = self.OM_data_eqn + (
                 'connect(' + self.name + '.Dist' + ", " + self.output_stms[1].name + '.In);\n')
         self.OM_data_eqn = self.OM_data_eqn + (
@@ -458,7 +458,7 @@ class CompoundSeparator(UnitOperation):
         self.compounds = [c[:c.index('(')] for c in compound_selected]
 
     def param_setter(self,params):
-        print("param_setter CompSep ", params)
+        #print("param_setter CompSep ", params)
       
         if (params[0]):
             self.variables['SepStrm']['value'] = 1
@@ -469,11 +469,6 @@ class CompoundSeparator(UnitOperation):
                 self.variables['SepVal_c']['value'][index//2] = float(params[i])
             else:
                 self.variables['SepFact_c']['value'][index//2] = params[i]
-        
-        # self.variables['SepFact_c']['value'] = json.dumps(self.variables['SepFact_c']['value']).replace('[','{').replace(']','}')
-        # self.variables['SepStrm']['value'] = str(self.variables['SepStrm']['value'])
-        # self.variables['SepVal_c']['value'] = json.dumps(self.variables['SepVal_c']['value']).replace('[','{').replace(']','}')
-
 
     def OM_Flowsheet_Initialize(self):
         SepStrm = str(self.variables['SepStrm']['value'])
@@ -535,7 +530,7 @@ class Flash(UnitOperation):
         self.compounds = [c[:c.index('(')] for c in compound_selected]
 
     def param_setter(self,params):
-        print("param_setter ", params)
+        #print("param_setter ", params)
         self.variables['thermo_package']['value'] = params[0]
         self.variables['BTdef']['value'] = params[1]
         self.variables['Tdef']['value'] = params[2]
@@ -608,7 +603,7 @@ class Splitter(UnitOperation):
         self.compounds = [c[:c.index('(')] for c in compound_selected]
 
     def param_setter(self,params):
-        print("param_setter ", params)
+        #print("param_setter ", params)
         self.variables['No']['value'] = int(params[0])
         self.variables['CalcType']['value'] = params[1]
         self.variables['SpecVal_s']['value'] = [float(params[2]), float(params[3])]
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__init__.py b/src/main/python/utils/__init__.py
index e69de29..e69de29 100644
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__init__.py
+++ b/src/main/python/utils/__init__.py
diff --git a/src/main/python/utils/__pycache__/Bin_Phase_env.cpython-37.pyc b/src/main/python/utils/__pycache__/Bin_Phase_env.cpython-37.pyc
new file mode 100644
index 0000000..35c4753
--- /dev/null
+++ b/src/main/python/utils/__pycache__/Bin_Phase_env.cpython-37.pyc
diff --git a/src/main/python/utils/__pycache__/ComponentSelector.cpython-37.pyc b/src/main/python/utils/__pycache__/ComponentSelector.cpython-37.pyc
new file mode 100644
index 0000000..b6bceec
--- /dev/null
+++ b/src/main/python/utils/__pycache__/ComponentSelector.cpython-37.pyc
diff --git a/src/main/python/utils/__pycache__/Container.cpython-37.pyc b/src/main/python/utils/__pycache__/Container.cpython-37.pyc
new file mode 100644
index 0000000..98797d2
--- /dev/null
+++ b/src/main/python/utils/__pycache__/Container.cpython-37.pyc
diff --git a/src/main/python/utils/__pycache__/Graphics.cpython-37.pyc b/src/main/python/utils/__pycache__/Graphics.cpython-37.pyc
new file mode 100644
index 0000000..7426c2f
--- /dev/null
+++ b/src/main/python/utils/__pycache__/Graphics.cpython-37.pyc
diff --git a/src/main/python/utils/__pycache__/Streams.cpython-37.pyc b/src/main/python/utils/__pycache__/Streams.cpython-37.pyc
new file mode 100644
index 0000000..18287f2
--- /dev/null
+++ b/src/main/python/utils/__pycache__/Streams.cpython-37.pyc
diff --git a/src/main/python/utils/__pycache__/UnitOperations.cpython-37.pyc b/src/main/python/utils/__pycache__/UnitOperations.cpython-37.pyc
new file mode 100644
index 0000000..ac4d056
--- /dev/null
+++ b/src/main/python/utils/__pycache__/UnitOperations.cpython-37.pyc
diff --git a/src/main/python/utils/__pycache__/__init__.cpython-37.pyc b/src/main/python/utils/__pycache__/__init__.cpython-37.pyc
new file mode 100644
index 0000000..a687f51
--- /dev/null
+++ b/src/main/python/utils/__pycache__/__init__.cpython-37.pyc
diff --git a/thermopackage.txt b/src/main/python/utils/thermopackage.txt
index f9155f5..f9155f5 100644
--- a/thermopackage.txt
+++ b/src/main/python/utils/thermopackage.txt
diff --git a/icons/AdiabaticCompressor.png b/src/main/resources/base/icons/AdiabaticCompressor.png
index 1fd7bb0..1fd7bb0 100644
--- a/icons/AdiabaticCompressor.png
+++ b/src/main/resources/base/icons/AdiabaticCompressor.png
diff --git a/icons/AdiabaticExpander.png b/src/main/resources/base/icons/AdiabaticExpander.png
index 615a638..615a638 100644
--- a/icons/AdiabaticExpander.png
+++ b/src/main/resources/base/icons/AdiabaticExpander.png
diff --git a/icons/CentrifugalPump.png b/src/main/resources/base/icons/CentrifugalPump.png
index a2d3e8e..a2d3e8e 100644
--- a/icons/CentrifugalPump.png
+++ b/src/main/resources/base/icons/CentrifugalPump.png
diff --git a/icons/Column.png b/src/main/resources/base/icons/Column.png
index 84c0bcc..84c0bcc 100644
--- a/icons/Column.png
+++ b/src/main/resources/base/icons/Column.png
diff --git a/icons/CompoundSeparator.png b/src/main/resources/base/icons/CompoundSeparator.png
index 3435dcf..3435dcf 100644
--- a/icons/CompoundSeparator.png
+++ b/src/main/resources/base/icons/CompoundSeparator.png
diff --git a/icons/Cooler.png b/src/main/resources/base/icons/Cooler.png
index 4dcb802..4dcb802 100644
--- a/icons/Cooler.png
+++ b/src/main/resources/base/icons/Cooler.png
diff --git a/icons/DistillationColumn.png b/src/main/resources/base/icons/DistillationColumn.png
index f65150b..f65150b 100644
--- a/icons/DistillationColumn.png
+++ b/src/main/resources/base/icons/DistillationColumn.png
diff --git a/icons/Flash.png b/src/main/resources/base/icons/Flash.png
index 9a84def..9a84def 100644
--- a/icons/Flash.png
+++ b/src/main/resources/base/icons/Flash.png
diff --git a/icons/Heater.png b/src/main/resources/base/icons/Heater.png
index 52b8c00..52b8c00 100644
--- a/icons/Heater.png
+++ b/src/main/resources/base/icons/Heater.png
diff --git a/icons/MaterialStream.png b/src/main/resources/base/icons/MaterialStream.png
index b548d3f..b548d3f 100644
--- a/icons/MaterialStream.png
+++ b/src/main/resources/base/icons/MaterialStream.png
diff --git a/icons/Mixer.png b/src/main/resources/base/icons/Mixer.png
index 6656945..6656945 100644
--- a/icons/Mixer.png
+++ b/src/main/resources/base/icons/Mixer.png
diff --git a/icons/ShortcutColumn.png b/src/main/resources/base/icons/ShortcutColumn.png
index f65150b..f65150b 100644
--- a/icons/ShortcutColumn.png
+++ b/src/main/resources/base/icons/ShortcutColumn.png
diff --git a/icons/Splitter.png b/src/main/resources/base/icons/Splitter.png
index 778bcda..778bcda 100644
--- a/icons/Splitter.png
+++ b/src/main/resources/base/icons/Splitter.png
diff --git a/icons/Valve.png b/src/main/resources/base/icons/Valve.png
index 3cfd5c4..3cfd5c4 100644
--- a/icons/Valve.png
+++ b/src/main/resources/base/icons/Valve.png
diff --git a/icons/bpe.png b/src/main/resources/base/icons/bpe.png
index 000730a..000730a 100644
--- a/icons/bpe.png
+++ b/src/main/resources/base/icons/bpe.png
diff --git a/icons/compound.png b/src/main/resources/base/icons/compound.png
index a9c946d..a9c946d 100644
--- a/icons/compound.png
+++ b/src/main/resources/base/icons/compound.png
diff --git a/icons/eq.png b/src/main/resources/base/icons/eq.png
index cb0485a..cb0485a 100644
--- a/icons/eq.png
+++ b/src/main/resources/base/icons/eq.png
diff --git a/icons/help.png b/src/main/resources/base/icons/help.png
index 785ca95..785ca95 100644
--- a/icons/help.png
+++ b/src/main/resources/base/icons/help.png
diff --git a/icons/icon_1.svg b/src/main/resources/base/icons/icon_1.svg
index 7f6acd7..7f6acd7 100644
--- a/icons/icon_1.svg
+++ b/src/main/resources/base/icons/icon_1.svg
diff --git a/icons/images.png b/src/main/resources/base/icons/images.png
index 559fdbb..559fdbb 100644
--- a/icons/images.png
+++ b/src/main/resources/base/icons/images.png
diff --git a/src/main/resources/base/icons/logo.ico b/src/main/resources/base/icons/logo.ico
new file mode 100644
index 0000000..e1c2e78
--- /dev/null
+++ b/src/main/resources/base/icons/logo.ico
diff --git a/icons/logo.png b/src/main/resources/base/icons/logo.png
index 60d94d8..60d94d8 100644
--- a/icons/logo.png
+++ b/src/main/resources/base/icons/logo.png
diff --git a/icons/new.png b/src/main/resources/base/icons/new.png
index f4343a7..f4343a7 100644
--- a/icons/new.png
+++ b/src/main/resources/base/icons/new.png
diff --git a/icons/open.png b/src/main/resources/base/icons/open.png
index 305d09d..305d09d 100644
--- a/icons/open.png
+++ b/src/main/resources/base/icons/open.png
diff --git a/icons/redo.png b/src/main/resources/base/icons/redo.png
index 7881e86..7881e86 100644
--- a/icons/redo.png
+++ b/src/main/resources/base/icons/redo.png
diff --git a/icons/save.png b/src/main/resources/base/icons/save.png
index e09beb3..e09beb3 100644
--- a/icons/save.png
+++ b/src/main/resources/base/icons/save.png
diff --git a/icons/simulating.png b/src/main/resources/base/icons/simulating.png
index b8ff48f..b8ff48f 100644
--- a/icons/simulating.png
+++ b/src/main/resources/base/icons/simulating.png
diff --git a/icons/sq.png b/src/main/resources/base/icons/sq.png
index b963402..b963402 100644
--- a/icons/sq.png
+++ b/src/main/resources/base/icons/sq.png
diff --git a/icons/stop.png b/src/main/resources/base/icons/stop.png
index d365d34..d365d34 100644
--- a/icons/stop.png
+++ b/src/main/resources/base/icons/stop.png
diff --git a/icons/undo.png b/src/main/resources/base/icons/undo.png
index d6906b8..d6906b8 100644
--- a/icons/undo.png
+++ b/src/main/resources/base/icons/undo.png
diff --git a/icons/zoo.png b/src/main/resources/base/icons/zoo.png
index 1de4314..1de4314 100644
--- a/icons/zoo.png
+++ b/src/main/resources/base/icons/zoo.png
diff --git a/icons/zoom_in.png b/src/main/resources/base/icons/zoom_in.png
index cdf3e3f..cdf3e3f 100644
--- a/icons/zoom_in.png
+++ b/src/main/resources/base/icons/zoom_in.png
diff --git a/icons/zoom_out.png b/src/main/resources/base/icons/zoom_out.png
index b6dbcc9..b6dbcc9 100644
--- a/icons/zoom_out.png
+++ b/src/main/resources/base/icons/zoom_out.png
diff --git a/icons/zoom_reset.png b/src/main/resources/base/icons/zoom_reset.png
index ca9d36f..ca9d36f 100644
--- a/icons/zoom_reset.png
+++ b/src/main/resources/base/icons/zoom_reset.png
diff --git a/DockWidgets/DistillationColumnStagewiseResults.ui b/src/main/ui/DockWidgets/DistillationColumnStagewiseResults.ui
index fb0ef9c..fb0ef9c 100644
--- a/DockWidgets/DistillationColumnStagewiseResults.ui
+++ b/src/main/ui/DockWidgets/DistillationColumnStagewiseResults.ui
diff --git a/DockWidgets/DockWidget.ui b/src/main/ui/DockWidgets/DockWidget.ui
index ba6dc52..ba6dc52 100644
--- a/DockWidgets/DockWidget.ui
+++ b/src/main/ui/DockWidgets/DockWidget.ui
diff --git a/DockWidgets/DockWidgetCompoundSeparator.ui b/src/main/ui/DockWidgets/DockWidgetCompoundSeparator.ui
index ad9cda4..ad9cda4 100644
--- a/DockWidgets/DockWidgetCompoundSeparator.ui
+++ b/src/main/ui/DockWidgets/DockWidgetCompoundSeparator.ui
diff --git a/DockWidgets/DockWidgetCompressorExpander.ui b/src/main/ui/DockWidgets/DockWidgetCompressorExpander.ui
index 372fc0b..372fc0b 100644
--- a/DockWidgets/DockWidgetCompressorExpander.ui
+++ b/src/main/ui/DockWidgets/DockWidgetCompressorExpander.ui
diff --git a/DockWidgets/DockWidgetDistillationColumn.ui b/src/main/ui/DockWidgets/DockWidgetDistillationColumn.ui
index 920837b..83a6204 100644
--- a/DockWidgets/DockWidgetDistillationColumn.ui
+++ b/src/main/ui/DockWidgets/DockWidgetDistillationColumn.ui
@@ -31,9 +31,9 @@
   <widget class="QTabWidget" name="tabWidget">
    <property name="geometry">
     <rect>
-     <x>0</x>
+     <x>10</x>
      <y>30</y>
-     <width>381</width>
+     <width>351</width>
      <height>481</height>
     </rect>
    </property>
@@ -41,7 +41,7 @@
     <bool>true</bool>
    </property>
    <property name="currentIndex">
-    <number>0</number>
+    <number>1</number>
    </property>
    <widget class="QWidget" name="tab">
     <attribute name="title">
@@ -66,7 +66,7 @@
            </sizepolicy>
           </property>
           <property name="currentIndex">
-           <number>0</number>
+           <number>2</number>
           </property>
           <widget class="QWidget" name="tab1">
            <attribute name="title">
@@ -264,10 +264,16 @@
          <rect>
           <x>12</x>
           <y>15</y>
-          <width>341</width>
+          <width>301</width>
           <height>151</height>
          </rect>
         </property>
+        <property name="sizePolicy">
+         <sizepolicy hsizetype="Fixed" vsizetype="Expanding">
+          <horstretch>0</horstretch>
+          <verstretch>0</verstretch>
+         </sizepolicy>
+        </property>
         <property name="columnCount">
          <number>3</number>
         </property>
@@ -297,6 +303,12 @@
      </item>
      <item>
       <widget class="QPushButton" name="stageResultsButton">
+       <property name="sizePolicy">
+        <sizepolicy hsizetype="Minimum" vsizetype="Fixed">
+         <horstretch>0</horstretch>
+         <verstretch>0</verstretch>
+        </sizepolicy>
+       </property>
        <property name="text">
         <string>Stagewise Results</string>
        </property>
diff --git a/DockWidgets/DockWidgetFlash.ui b/src/main/ui/DockWidgets/DockWidgetFlash.ui
index c781aa6..c781aa6 100644
--- a/DockWidgets/DockWidgetFlash.ui
+++ b/src/main/ui/DockWidgets/DockWidgetFlash.ui
diff --git a/DockWidgets/DockWidgetMaterialStream.ui b/src/main/ui/DockWidgets/DockWidgetMaterialStream.ui
index 8b9df28..8b9df28 100644
--- a/DockWidgets/DockWidgetMaterialStream.ui
+++ b/src/main/ui/DockWidgets/DockWidgetMaterialStream.ui
diff --git a/DockWidgets/DockWidgetMixer.ui b/src/main/ui/DockWidgets/DockWidgetMixer.ui
index e039490..e039490 100644
--- a/DockWidgets/DockWidgetMixer.ui
+++ b/src/main/ui/DockWidgets/DockWidgetMixer.ui
diff --git a/DockWidgets/DockWidgetShortcutColumn.ui b/src/main/ui/DockWidgets/DockWidgetShortcutColumn.ui
index f79c27e..f79c27e 100644
--- a/DockWidgets/DockWidgetShortcutColumn.ui
+++ b/src/main/ui/DockWidgets/DockWidgetShortcutColumn.ui
diff --git a/DockWidgets/DockWidgetSplitter.ui b/src/main/ui/DockWidgets/DockWidgetSplitter.ui
index 02a865e..02a865e 100644
--- a/DockWidgets/DockWidgetSplitter.ui
+++ b/src/main/ui/DockWidgets/DockWidgetSplitter.ui
diff --git a/Binary_Phase_Env.ui b/src/main/ui/utils/Binary_Phase_Env.ui
index d9efde7..d9efde7 100644
--- a/Binary_Phase_Env.ui
+++ b/src/main/ui/utils/Binary_Phase_Env.ui
diff --git a/ComponentSelector.ui b/src/main/ui/utils/ComponentSelector.ui
index 7a43206..7a43206 100644
--- a/ComponentSelector.ui
+++ b/src/main/ui/utils/ComponentSelector.ui
diff --git a/main.ui b/src/main/ui/utils/main.ui
index abdb77d..129b8bf 100644
--- a/main.ui
+++ b/src/main/ui/utils/main.ui
@@ -15,7 +15,7 @@
   </property>
   <property name="windowIcon">
    <iconset>
-    <normaloff>icons/logo.png</normaloff>icons/logo.png</iconset>
+    <normaloff>./../../resources/base/icons/logo.png</normaloff>./../../resources/base/icons/logo.png</iconset>
   </property>
   <property name="iconSize">
    <size>
@@ -385,7 +385,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/MaterialStream.png</normaloff>icons/MaterialStream.png</iconset>
+             <normaloff>./../../resources/base/icons/MaterialStream.png</normaloff>./../../resources/base/icons/MaterialStream.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -888,7 +888,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/Mixer.png</normaloff>icons/Mixer.png</iconset>
+             <normaloff>./../../resources/base/icons/Mixer.png</normaloff>./../../resources/base/icons/Mixer.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -934,7 +934,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/Splitter.png</normaloff>icons/Splitter.png</iconset>
+             <normaloff>./../../resources/base/icons/Splitter.png</normaloff>./../../resources/base/icons/Splitter.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1437,7 +1437,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/Heater.png</normaloff>icons/Heater.png</iconset>
+             <normaloff>./../../resources/base/icons/Heater.png</normaloff>./../../resources/base/icons/Heater.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1492,7 +1492,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/Cooler.png</normaloff>icons/Cooler.png</iconset>
+             <normaloff>./../../resources/base/icons/Cooler.png</normaloff>./../../resources/base/icons/Cooler.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1583,7 +1583,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/Flash.png</normaloff>icons/Flash.png</iconset>
+             <normaloff>./../../resources/base/icons/Flash.png</normaloff>./../../resources/base/icons/Flash.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1629,7 +1629,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/CompoundSeparator.png</normaloff>icons/CompoundSeparator.png</iconset>
+             <normaloff>./../../resources/base/icons/CompoundSeparator.png</normaloff>./../../resources/base/icons/CompoundSeparator.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1714,7 +1714,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/Valve.png</normaloff>icons/Valve.png</iconset>
+             <normaloff>./../../resources/base/icons/Valve.png</normaloff>./../../resources/base/icons/Valve.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1760,7 +1760,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/CentrifugalPump.png</normaloff>icons/CentrifugalPump.png</iconset>
+             <normaloff>./../../resources/base/icons/CentrifugalPump.png</normaloff>./../../resources/base/icons/CentrifugalPump.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1806,7 +1806,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/AdiabaticCompressor.png</normaloff>icons/AdiabaticCompressor.png</iconset>
+             <normaloff>./../../resources/base/icons/AdiabaticCompressor.png</normaloff>./../../resources/base/icons/AdiabaticCompressor.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1855,7 +1855,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>icons/AdiabaticExpander.png</normaloff>icons/AdiabaticExpander.png</iconset>
+             <normaloff>./../../resources/base/icons/AdiabaticExpander.png</normaloff>./../../resources/base/icons/AdiabaticExpander.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1940,7 +1940,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>Icons/Column.png</normaloff>Icons/Column.png</iconset>
+             <normaloff>./../../resources/base/icons/Column.png</normaloff>./../../resources/base/icons/Column.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -1986,7 +1986,7 @@
            </property>
            <property name="icon">
             <iconset>
-             <normaloff>Icons/Column.png</normaloff>Icons/Column.png</iconset>
+             <normaloff>./../../resources/base/icons/Column.png</normaloff>./../../resources/base/icons/Column.png</iconset>
            </property>
            <property name="iconSize">
             <size>
@@ -2031,7 +2031,7 @@
   <action name="actionZoomIn">
    <property name="icon">
     <iconset>
-     <normaloff>Icons/zoom_in.png</normaloff>Icons/zoom_in.png</iconset>
+     <normaloff>./../../resources/base/icons/zoom_in.png</normaloff>./../../resources/base/icons/zoom_in.png</iconset>
    </property>
    <property name="text">
     <string>ZoomIn</string>
@@ -2040,7 +2040,7 @@
   <action name="actionZoomOut">
    <property name="icon">
     <iconset>
-     <normaloff>Icons/zoom_out.png</normaloff>Icons/zoom_out.png</iconset>
+     <normaloff>./../../resources/base/icons/zoom_out.png</normaloff>./../../resources/base/icons/zoom_out.png</iconset>
    </property>
    <property name="text">
     <string>ZoomOut</string>
@@ -2049,7 +2049,7 @@
   <action name="actionResetZoom">
    <property name="icon">
     <iconset>
-     <normaloff>Icons/zoom_reset.png</normaloff>Icons/zoom_reset.png</iconset>
+     <normaloff>./../../resources/base/icons/zoom_reset.png</normaloff>./../../resources/base/icons/zoom_reset.png</iconset>
    </property>
    <property name="text">
     <string>ResetZoom</string>
@@ -2058,7 +2058,7 @@
   <action name="actionEquationOriented">
    <property name="icon">
     <iconset>
-     <normaloff>Icons/eq.png</normaloff>Icons/eq.png</iconset>
+     <normaloff>./../../resources/base/icons/eq.png</normaloff>./../../resources/base/icons/eq.png</iconset>
    </property>
    <property name="text">
     <string>Equation oriented</string>
@@ -2070,7 +2070,7 @@
    </property>
    <property name="icon">
     <iconset>
-     <normaloff>Icons/sq.png</normaloff>Icons/sq.png</iconset>
+     <normaloff>./../../resources/base/icons/sq.png</normaloff>./../../resources/base/icons/sq.png</iconset>
    </property>
    <property name="text">
     <string>Sequential mode</string>
@@ -2082,7 +2082,7 @@
    </property>
    <property name="icon">
     <iconset>
-     <normaloff>Icons/stop.png</normaloff>Icons/stop.png</iconset>
+     <normaloff>./../../resources/base/icons/stop.png</normaloff>./../../resources/base/icons/stop.png</iconset>
    </property>
    <property name="text">
     <string>Stop Simulation</string>
@@ -2091,7 +2091,7 @@
   <action name="actionSelectCompounds">
    <property name="icon">
     <iconset>
-     <normaloff>Icons/compound.png</normaloff>Icons/compound.png</iconset>
+     <normaloff>./../../resources/base/icons/compound.png</normaloff>./../../resources/base/icons/compound.png</iconset>
    </property>
    <property name="text">
     <string>Select Compounds</string>
@@ -2100,7 +2100,7 @@
   <action name="actionNew">
    <property name="icon">
     <iconset>
-     <normaloff>Icons/new.png</normaloff>Icons/new.png</iconset>
+     <normaloff>./../../resources/base/icons/new.png</normaloff>./../../resources/base/icons/new.png</iconset>
    </property>
    <property name="text">
     <string>New</string>
@@ -2109,7 +2109,7 @@
   <action name="actionHelp">
     <property name="icon">
       <iconset>
-      <normaloff>Icons/help.png</normaloff>Icons/help.png</iconset>
+      <normaloff>./../../resources/base/icons/help.png</normaloff>./../../resources/base/icons/help.png</iconset>
     </property>
    <property name="text">
     <string>Help</string>
@@ -2118,7 +2118,7 @@
   <action name="actionSave">
     <property name="icon">
     <iconset>
-     <normaloff>Icons/save.png</normaloff>Icons/save.png</iconset>
+     <normaloff>./../../resources/base/icons/save.png</normaloff>./../../resources/base/icons/save.png</iconset>
    </property>
    <property name="text">
     <string>Save</string>
@@ -2127,7 +2127,7 @@
   <action name="actionOpen">
     <property name="icon">
       <iconset>
-      <normaloff>Icons/open.png</normaloff>Icons/open.png</iconset>
+      <normaloff>./../../resources/base/icons/open.png</normaloff>./../../resources/base/icons/open.png</iconset>
     </property>
    <property name="text">
     <string>Open</string>
@@ -2136,7 +2136,7 @@
   <action name="actionBinaryPhaseEnvelope">
     <property name="icon">
       <iconset>
-      <normaloff>Icons/bpe.png</normaloff>Icons/bpe.png</iconset>
+      <normaloff>./../../resources/base/icons/bpe.png</normaloff>./../../resources/base/icons/bpe.png</iconset>
     </property>
    <property name="text">
     <string>Binary Phase Envelope</string>
@@ -2153,7 +2153,7 @@
     </property>
     <property name="icon">
       <iconset>
-      <normaloff>Icons/undo.png</normaloff>Icons/undo.png</iconset>
+      <normaloff>./../../resources/base/icons/undo.png</normaloff>./../../resources/base/icons/undo.png</iconset>
     </property>
    <property name="text">
     <string>Undo</string>
@@ -2165,7 +2165,7 @@
     </property>
     <property name="icon">
       <iconset>
-      <normaloff>Icons/redo.png</normaloff>Icons/redo.png</iconset>
+      <normaloff>./../../resources/base/icons/redo.png</normaloff>./../../resources/base/icons/redo.png</iconset>
     </property>
    <property name="text">
     <string>Redo</string>
diff --git a/svg/CentrifugalPump.svg b/svg/CentrifugalPump.svg
deleted file mode 100644
index 5b60256..0000000
--- a/svg/CentrifugalPump.svg
+++ /dev/null
@@ -1,104 +0,0 @@
-<?xml version="1.0" encoding="UTF-8" standalone="no"?>
-<!-- Created with Inkscape (http://www.inkscape.org/) -->
-
-<svg
-   xmlns:dc="http://purl.org/dc/elements/1.1/"
-   xmlns:cc="http://creativecommons.org/ns#"
-   xmlns:rdf="http://www.w3.org/1999/02/22-rdf-syntax-ns#"
-   xmlns:svg="http://www.w3.org/2000/svg"
-   xmlns="http://www.w3.org/2000/svg"
-   xmlns:sodipodi="http://sodipodi.sourceforge.net/DTD/sodipodi-0.dtd"
-   xmlns:inkscape="http://www.inkscape.org/namespaces/inkscape"
-   width="5.8764515mm"
-   height="5.1060538mm"
-   viewBox="0 0 5.8764515 5.1060538"
-   version="1.1"
-   id="svg919"
-   inkscape:version="0.92.4 (5da689c313, 2019-01-14)"
-   sodipodi:docname="Centrifugal Pump.svg">
-  <defs
-     id="defs913" />
-  <sodipodi:namedview
-     id="base"
-     pagecolor="#ffffff"
-     bordercolor="#666666"
-     borderopacity="1.0"
-     inkscape:pageopacity="0.0"
-     inkscape:pageshadow="2"
-     inkscape:zoom="0.35"
-     inkscape:cx="11.105106"
-     inkscape:cy="9.6492281"
-     inkscape:document-units="mm"
-     inkscape:current-layer="layer1"
-     showgrid="false"
-     fit-margin-top="0"
-     fit-margin-left="0"
-     fit-margin-right="0"
-     fit-margin-bottom="0"
-     inkscape:window-width="1304"
-     inkscape:window-height="745"
-     inkscape:window-x="-8"
-     inkscape:window-y="-8"
-     inkscape:window-maximized="1" />
-  <metadata
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diff --git a/venv/Lib/site-packages/__pycache__/mccabe.cpython-37.pyc b/venv/Lib/site-packages/__pycache__/mccabe.cpython-37.pyc
deleted file mode 100644
index 44dca75..0000000
--- a/venv/Lib/site-packages/__pycache__/mccabe.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/__pycache__/six.cpython-37.pyc b/venv/Lib/site-packages/__pycache__/six.cpython-37.pyc
deleted file mode 100644
index 07b383b..0000000
--- a/venv/Lib/site-packages/__pycache__/six.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid-2.3.3.dist-info/COPYING b/venv/Lib/site-packages/astroid-2.3.3.dist-info/COPYING
deleted file mode 100644
index d511905..0000000
--- a/venv/Lib/site-packages/astroid-2.3.3.dist-info/COPYING
+++ /dev/null
@@ -1,339 +0,0 @@
-		    GNU GENERAL PUBLIC LICENSE
-		       Version 2, June 1991
-
- Copyright (C) 1989, 1991 Free Software Foundation, Inc.,
- 51 Franklin Street, Fifth Floor, Boston, MA 02110-1301 USA
- Everyone is permitted to copy and distribute verbatim copies
- of this license document, but changing it is not allowed.
-
-			    Preamble
-
-  The licenses for most software are designed to take away your
-freedom to share and change it.  By contrast, the GNU General Public
-License is intended to guarantee your freedom to share and change free
-software--to make sure the software is free for all its users.  This
-General Public License applies to most of the Free Software
-Foundation's software and to any other program whose authors commit to
-using it.  (Some other Free Software Foundation software is covered by
-the GNU Lesser General Public License instead.)  You can apply it to
-your programs, too.
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-  When we speak of free software, we are referring to freedom, not
-price.  Our General Public Licenses are designed to make sure that you
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-in new free programs; and that you know you can do these things.
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-anyone to deny you these rights or to ask you to surrender the rights.
-These restrictions translate to certain responsibilities for you if you
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-rights.
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-  We protect your rights with two steps: (1) copyright the software, and
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-  The precise terms and conditions for copying, distribution and
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-		    GNU GENERAL PUBLIC LICENSE
-   TERMS AND CONDITIONS FOR COPYING, DISTRIBUTION AND MODIFICATION
-
-  0. This License applies to any program or other work which contains
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diff --git a/venv/Lib/site-packages/astroid-2.3.3.dist-info/COPYING.LESSER b/venv/Lib/site-packages/astroid-2.3.3.dist-info/COPYING.LESSER
deleted file mode 100644
index 2d2d780..0000000
--- a/venv/Lib/site-packages/astroid-2.3.3.dist-info/COPYING.LESSER
+++ /dev/null
@@ -1,510 +0,0 @@
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diff --git a/venv/Lib/site-packages/astroid-2.3.3.dist-info/INSTALLER b/venv/Lib/site-packages/astroid-2.3.3.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/astroid-2.3.3.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/astroid-2.3.3.dist-info/METADATA b/venv/Lib/site-packages/astroid-2.3.3.dist-info/METADATA
deleted file mode 100644
index 2805693..0000000
--- a/venv/Lib/site-packages/astroid-2.3.3.dist-info/METADATA
+++ /dev/null
@@ -1,117 +0,0 @@
-Metadata-Version: 2.1
-Name: astroid
-Version: 2.3.3
-Summary: An abstract syntax tree for Python with inference support.
-Home-page: https://github.com/PyCQA/astroid
-Author: Python Code Quality Authority
-Author-email: code-quality@python.org
-License: LGPL
-Platform: UNKNOWN
-Classifier: Topic :: Software Development :: Libraries :: Python Modules
-Classifier: Topic :: Software Development :: Quality Assurance
-Classifier: Programming Language :: Python
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: Implementation :: CPython
-Classifier: Programming Language :: Python :: Implementation :: PyPy
-Requires-Python: >=3.5.*
-Requires-Dist: lazy-object-proxy (==1.4.*)
-Requires-Dist: six (~=1.12)
-Requires-Dist: wrapt (==1.11.*)
-Requires-Dist: typed-ast (<1.5,>=1.4.0) ; implementation_name == "cpython" and python_version < "3.8"
-
-Astroid
-=======
-
-.. image:: https://travis-ci.org/PyCQA/astroid.svg?branch=master
-    :target: https://travis-ci.org/PyCQA/astroid
-
-.. image:: https://ci.appveyor.com/api/projects/status/co3u42kunguhbh6l/branch/master?svg=true
-    :alt: AppVeyor Build Status
-    :target: https://ci.appveyor.com/project/PCManticore/astroid
-
-.. image:: https://coveralls.io/repos/github/PyCQA/astroid/badge.svg?branch=master
-    :target: https://coveralls.io/github/PyCQA/astroid?branch=master
-
-.. image:: https://readthedocs.org/projects/astroid/badge/?version=latest
-    :target: http://astroid.readthedocs.io/en/latest/?badge=latest
-    :alt: Documentation Status
-
-.. image:: https://img.shields.io/badge/code%20style-black-000000.svg
-    :target: https://github.com/ambv/black
-
-.. |tideliftlogo| image:: doc/media/Tidelift_Logos_RGB_Tidelift_Shorthand_On-White_small.png
-   :width: 75
-   :height: 60
-   :alt: Tidelift
-
-.. list-table::
-   :widths: 10 100
-
-   * - |tideliftlogo|
-     - Professional support for astroid is available as part of the `Tidelift
-       Subscription`_.  Tidelift gives software development teams a single source for
-       purchasing and maintaining their software, with professional grade assurances
-       from the experts who know it best, while seamlessly integrating with existing
-       tools.
-
-.. _Tidelift Subscription: https://tidelift.com/subscription/pkg/pypi-astroid?utm_source=pypi-astroid&utm_medium=referral&utm_campaign=readme
-
-
-
-What's this?
-------------
-
-The aim of this module is to provide a common base representation of
-python source code. It is currently the library powering pylint's capabilities.
-
-It provides a compatible representation which comes from the `_ast`
-module.  It rebuilds the tree generated by the builtin _ast module by
-recursively walking down the AST and building an extended ast. The new
-node classes have additional methods and attributes for different
-usages. They include some support for static inference and local name
-scopes. Furthermore, astroid can also build partial trees by inspecting living
-objects.
-
-
-Installation
-------------
-
-Extract the tarball, jump into the created directory and run::
-
-	pip install .
-
-
-If you want to do an editable installation, you can run::
-
-    pip install -e .
-
-
-If you have any questions, please mail the code-quality@python.org
-mailing list for support. See
-http://mail.python.org/mailman/listinfo/code-quality for subscription
-information and archives.
-
-Documentation
--------------
-http://astroid.readthedocs.io/en/latest/
-
-
-Python Versions
----------------
-
-astroid 2.0 is currently available for Python 3 only. If you want Python 2
-support, older versions of astroid will still supported until 2020.
-
-Test
-----
-
-Tests are in the 'test' subdirectory. To launch the whole tests suite, you can use
-either `tox` or `pytest`::
-
-  tox
-  pytest astroid
-
-
diff --git a/venv/Lib/site-packages/astroid-2.3.3.dist-info/RECORD b/venv/Lib/site-packages/astroid-2.3.3.dist-info/RECORD
deleted file mode 100644
index f5d983e..0000000
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@@ -1,145 +0,0 @@
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-astroid/context.py,sha256=VsyUDVB1J9fk1o8MQoE4ygfC7gdNjVYVUD4Bhgs9JM0,5164
-astroid/decorators.py,sha256=m0v63YRiQKc66-g8ckkYeJ0d5cji8AhkUxFPbTfLVDc,4229
-astroid/exceptions.py,sha256=_IJRdLfyNSPVjxYgEd11Uu9XpdqE7uBCVOEIxt3ua70,7047
-astroid/helpers.py,sha256=3HOFwK0ieIoLu7JhrbM1r0zxPyDtTl2oNSv-tXQ2iRw,9170
-astroid/inference.py,sha256=0diHXE-ZGiWU9y31flQa3YZhg6-v4dZgD4PPFAlHJGc,33023
-astroid/interpreter/__init__.py,sha256=47DEQpj8HBSa-_TImW-5JCeuQeRkm5NMpJWZG3hSuFU,0
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diff --git a/venv/Lib/site-packages/astroid-2.3.3.dist-info/WHEEL b/venv/Lib/site-packages/astroid-2.3.3.dist-info/WHEEL
deleted file mode 100644
index 3b5c403..0000000
--- a/venv/Lib/site-packages/astroid-2.3.3.dist-info/WHEEL
+++ /dev/null
@@ -1,5 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.33.6)
-Root-Is-Purelib: true
-Tag: py3-none-any
-
diff --git a/venv/Lib/site-packages/astroid-2.3.3.dist-info/top_level.txt b/venv/Lib/site-packages/astroid-2.3.3.dist-info/top_level.txt
deleted file mode 100644
index 450d4fe..0000000
--- a/venv/Lib/site-packages/astroid-2.3.3.dist-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-astroid
diff --git a/venv/Lib/site-packages/astroid/__init__.py b/venv/Lib/site-packages/astroid/__init__.py
deleted file mode 100644
index d36a5b4..0000000
--- a/venv/Lib/site-packages/astroid/__init__.py
+++ /dev/null
@@ -1,166 +0,0 @@
-# Copyright (c) 2006-2013, 2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Python Abstract Syntax Tree New Generation
-
-The aim of this module is to provide a common base representation of
-python source code for projects such as pychecker, pyreverse,
-pylint... Well, actually the development of this library is essentially
-governed by pylint's needs.
-
-It extends class defined in the python's _ast module with some
-additional methods and attributes. Instance attributes are added by a
-builder object, which can either generate extended ast (let's call
-them astroid ;) by visiting an existent ast tree or by inspecting living
-object. Methods are added by monkey patching ast classes.
-
-Main modules are:
-
-* nodes and scoped_nodes for more information about methods and
-  attributes added to different node classes
-
-* the manager contains a high level object to get astroid trees from
-  source files and living objects. It maintains a cache of previously
-  constructed tree for quick access
-
-* builder contains the class responsible to build astroid trees
-"""
-
-import enum
-import itertools
-import os
-import sys
-
-import wrapt
-
-
-_Context = enum.Enum("Context", "Load Store Del")
-Load = _Context.Load
-Store = _Context.Store
-Del = _Context.Del
-del _Context
-
-
-from .__pkginfo__ import version as __version__
-
-# WARNING: internal imports order matters !
-
-# pylint: disable=redefined-builtin
-
-# make all exception classes accessible from astroid package
-from astroid.exceptions import *
-
-# make all node classes accessible from astroid package
-from astroid.nodes import *
-
-# trigger extra monkey-patching
-from astroid import inference
-
-# more stuff available
-from astroid import raw_building
-from astroid.bases import BaseInstance, Instance, BoundMethod, UnboundMethod
-from astroid.node_classes import are_exclusive, unpack_infer
-from astroid.scoped_nodes import builtin_lookup
-from astroid.builder import parse, extract_node
-from astroid.util import Uninferable
-
-# make a manager instance (borg) accessible from astroid package
-from astroid.manager import AstroidManager
-
-MANAGER = AstroidManager()
-del AstroidManager
-
-# transform utilities (filters and decorator)
-
-
-# pylint: disable=dangerous-default-value
-@wrapt.decorator
-def _inference_tip_cached(func, instance, args, kwargs, _cache={}):
-    """Cache decorator used for inference tips"""
-    node = args[0]
-    try:
-        return iter(_cache[func, node])
-    except KeyError:
-        result = func(*args, **kwargs)
-        # Need to keep an iterator around
-        original, copy = itertools.tee(result)
-        _cache[func, node] = list(copy)
-        return original
-
-
-# pylint: enable=dangerous-default-value
-
-
-def inference_tip(infer_function, raise_on_overwrite=False):
-    """Given an instance specific inference function, return a function to be
-    given to MANAGER.register_transform to set this inference function.
-
-    :param bool raise_on_overwrite: Raise an `InferenceOverwriteError`
-        if the inference tip will overwrite another. Used for debugging
-
-    Typical usage
-
-    .. sourcecode:: python
-
-       MANAGER.register_transform(Call, inference_tip(infer_named_tuple),
-                                  predicate)
-
-    .. Note::
-
-        Using an inference tip will override
-        any previously set inference tip for the given
-        node. Use a predicate in the transform to prevent
-        excess overwrites.
-    """
-
-    def transform(node, infer_function=infer_function):
-        if (
-            raise_on_overwrite
-            and node._explicit_inference is not None
-            and node._explicit_inference is not infer_function
-        ):
-            raise InferenceOverwriteError(
-                "Inference already set to {existing_inference}. "
-                "Trying to overwrite with {new_inference} for {node}".format(
-                    existing_inference=infer_function,
-                    new_inference=node._explicit_inference,
-                    node=node,
-                )
-            )
-        # pylint: disable=no-value-for-parameter
-        node._explicit_inference = _inference_tip_cached(infer_function)
-        return node
-
-    return transform
-
-
-def register_module_extender(manager, module_name, get_extension_mod):
-    def transform(node):
-        extension_module = get_extension_mod()
-        for name, objs in extension_module.locals.items():
-            node.locals[name] = objs
-            for obj in objs:
-                if obj.parent is extension_module:
-                    obj.parent = node
-
-    manager.register_transform(Module, transform, lambda n: n.name == module_name)
-
-
-# load brain plugins
-BRAIN_MODULES_DIR = os.path.join(os.path.dirname(__file__), "brain")
-if BRAIN_MODULES_DIR not in sys.path:
-    # add it to the end of the list so user path take precedence
-    sys.path.append(BRAIN_MODULES_DIR)
-# load modules in this directory
-for module in os.listdir(BRAIN_MODULES_DIR):
-    if module.endswith(".py"):
-        __import__(module[:-3])
diff --git a/venv/Lib/site-packages/astroid/__pkginfo__.py b/venv/Lib/site-packages/astroid/__pkginfo__.py
deleted file mode 100644
index 4a17b5d..0000000
--- a/venv/Lib/site-packages/astroid/__pkginfo__.py
+++ /dev/null
@@ -1,51 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2015-2017 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Radosław Ganczarek <radoslaw@ganczarek.in>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2017 Hugo <hugovk@users.noreply.github.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 Calen Pennington <cale@edx.org>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""astroid packaging information"""
-
-version = "2.3.3"
-numversion = tuple(int(elem) for elem in version.split(".") if elem.isdigit())
-
-extras_require = {}
-install_requires = [
-    "lazy_object_proxy==1.4.*",
-    "six~=1.12",
-    "wrapt==1.11.*",
-    'typed-ast>=1.4.0,<1.5;implementation_name== "cpython" and python_version<"3.8"',
-]
-
-# pylint: disable=redefined-builtin; why license is a builtin anyway?
-license = "LGPL"
-
-author = "Python Code Quality Authority"
-author_email = "code-quality@python.org"
-mailinglist = "mailto://%s" % author_email
-web = "https://github.com/PyCQA/astroid"
-
-description = "An abstract syntax tree for Python with inference support."
-
-classifiers = [
-    "Topic :: Software Development :: Libraries :: Python Modules",
-    "Topic :: Software Development :: Quality Assurance",
-    "Programming Language :: Python",
-    "Programming Language :: Python :: 3",
-    "Programming Language :: Python :: 3.5",
-    "Programming Language :: Python :: 3.6",
-    "Programming Language :: Python :: 3.7",
-    "Programming Language :: Python :: Implementation :: CPython",
-    "Programming Language :: Python :: Implementation :: PyPy",
-]
diff --git a/venv/Lib/site-packages/astroid/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/astroid/__pycache__/__init__.cpython-37.pyc
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+++ /dev/null
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deleted file mode 100644
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--- a/venv/Lib/site-packages/astroid/__pycache__/transforms.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/__pycache__/util.cpython-37.pyc b/venv/Lib/site-packages/astroid/__pycache__/util.cpython-37.pyc
deleted file mode 100644
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+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/_ast.py b/venv/Lib/site-packages/astroid/_ast.py
deleted file mode 100644
index 2e44c1f..0000000
--- a/venv/Lib/site-packages/astroid/_ast.py
+++ /dev/null
@@ -1,49 +0,0 @@
-import ast
-from collections import namedtuple
-from functools import partial
-from typing import Optional
-import sys
-
-_ast_py2 = _ast_py3 = None
-try:
-    import typed_ast.ast3 as _ast_py3
-    import typed_ast.ast27 as _ast_py2
-except ImportError:
-    pass
-
-
-PY38 = sys.version_info[:2] >= (3, 8)
-if PY38:
-    # On Python 3.8, typed_ast was merged back into `ast`
-    _ast_py3 = ast
-
-
-FunctionType = namedtuple("FunctionType", ["argtypes", "returns"])
-
-
-def _get_parser_module(parse_python_two: bool = False):
-    if parse_python_two:
-        parser_module = _ast_py2
-    else:
-        parser_module = _ast_py3
-    return parser_module or ast
-
-
-def _parse(string: str, parse_python_two: bool = False):
-    parse_module = _get_parser_module(parse_python_two=parse_python_two)
-    parse_func = parse_module.parse
-    if _ast_py3:
-        if PY38:
-            parse_func = partial(parse_func, type_comments=True)
-        if not parse_python_two:
-            parse_func = partial(parse_func, feature_version=sys.version_info.minor)
-    return parse_func(string)
-
-
-def parse_function_type_comment(type_comment: str) -> Optional[FunctionType]:
-    """Given a correct type comment, obtain a FunctionType object"""
-    if _ast_py3 is None:
-        return None
-
-    func_type = _ast_py3.parse(type_comment, "<type_comment>", "func_type")
-    return FunctionType(argtypes=func_type.argtypes, returns=func_type.returns)
diff --git a/venv/Lib/site-packages/astroid/arguments.py b/venv/Lib/site-packages/astroid/arguments.py
deleted file mode 100644
index c4bdc6d..0000000
--- a/venv/Lib/site-packages/astroid/arguments.py
+++ /dev/null
@@ -1,285 +0,0 @@
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-from astroid import bases
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import nodes
-from astroid import util
-
-
-class CallSite:
-    """Class for understanding arguments passed into a call site
-
-    It needs a call context, which contains the arguments and the
-    keyword arguments that were passed into a given call site.
-    In order to infer what an argument represents, call
-    :meth:`infer_argument` with the corresponding function node
-    and the argument name.
-    """
-
-    def __init__(self, callcontext, argument_context_map=None):
-        if argument_context_map is None:
-            argument_context_map = {}
-        self.argument_context_map = argument_context_map
-        args = callcontext.args
-        keywords = callcontext.keywords
-        self.duplicated_keywords = set()
-        self._unpacked_args = self._unpack_args(args)
-        self._unpacked_kwargs = self._unpack_keywords(keywords)
-
-        self.positional_arguments = [
-            arg for arg in self._unpacked_args if arg is not util.Uninferable
-        ]
-        self.keyword_arguments = {
-            key: value
-            for key, value in self._unpacked_kwargs.items()
-            if value is not util.Uninferable
-        }
-
-    @classmethod
-    def from_call(cls, call_node):
-        """Get a CallSite object from the given Call node."""
-        callcontext = contextmod.CallContext(call_node.args, call_node.keywords)
-        return cls(callcontext)
-
-    def has_invalid_arguments(self):
-        """Check if in the current CallSite were passed *invalid* arguments
-
-        This can mean multiple things. For instance, if an unpacking
-        of an invalid object was passed, then this method will return True.
-        Other cases can be when the arguments can't be inferred by astroid,
-        for example, by passing objects which aren't known statically.
-        """
-        return len(self.positional_arguments) != len(self._unpacked_args)
-
-    def has_invalid_keywords(self):
-        """Check if in the current CallSite were passed *invalid* keyword arguments
-
-        For instance, unpacking a dictionary with integer keys is invalid
-        (**{1:2}), because the keys must be strings, which will make this
-        method to return True. Other cases where this might return True if
-        objects which can't be inferred were passed.
-        """
-        return len(self.keyword_arguments) != len(self._unpacked_kwargs)
-
-    def _unpack_keywords(self, keywords):
-        values = {}
-        context = contextmod.InferenceContext()
-        context.extra_context = self.argument_context_map
-        for name, value in keywords:
-            if name is None:
-                # Then it's an unpacking operation (**)
-                try:
-                    inferred = next(value.infer(context=context))
-                except exceptions.InferenceError:
-                    values[name] = util.Uninferable
-                    continue
-
-                if not isinstance(inferred, nodes.Dict):
-                    # Not something we can work with.
-                    values[name] = util.Uninferable
-                    continue
-
-                for dict_key, dict_value in inferred.items:
-                    try:
-                        dict_key = next(dict_key.infer(context=context))
-                    except exceptions.InferenceError:
-                        values[name] = util.Uninferable
-                        continue
-                    if not isinstance(dict_key, nodes.Const):
-                        values[name] = util.Uninferable
-                        continue
-                    if not isinstance(dict_key.value, str):
-                        values[name] = util.Uninferable
-                        continue
-                    if dict_key.value in values:
-                        # The name is already in the dictionary
-                        values[dict_key.value] = util.Uninferable
-                        self.duplicated_keywords.add(dict_key.value)
-                        continue
-                    values[dict_key.value] = dict_value
-            else:
-                values[name] = value
-        return values
-
-    def _unpack_args(self, args):
-        values = []
-        context = contextmod.InferenceContext()
-        context.extra_context = self.argument_context_map
-        for arg in args:
-            if isinstance(arg, nodes.Starred):
-                try:
-                    inferred = next(arg.value.infer(context=context))
-                except exceptions.InferenceError:
-                    values.append(util.Uninferable)
-                    continue
-
-                if inferred is util.Uninferable:
-                    values.append(util.Uninferable)
-                    continue
-                if not hasattr(inferred, "elts"):
-                    values.append(util.Uninferable)
-                    continue
-                values.extend(inferred.elts)
-            else:
-                values.append(arg)
-        return values
-
-    def infer_argument(self, funcnode, name, context):
-        """infer a function argument value according to the call context
-
-        Arguments:
-            funcnode: The function being called.
-            name: The name of the argument whose value is being inferred.
-            context: Inference context object
-        """
-        if name in self.duplicated_keywords:
-            raise exceptions.InferenceError(
-                "The arguments passed to {func!r} " " have duplicate keywords.",
-                call_site=self,
-                func=funcnode,
-                arg=name,
-                context=context,
-            )
-
-        # Look into the keywords first, maybe it's already there.
-        try:
-            return self.keyword_arguments[name].infer(context)
-        except KeyError:
-            pass
-
-        # Too many arguments given and no variable arguments.
-        if len(self.positional_arguments) > len(funcnode.args.args):
-            if not funcnode.args.vararg:
-                raise exceptions.InferenceError(
-                    "Too many positional arguments "
-                    "passed to {func!r} that does "
-                    "not have *args.",
-                    call_site=self,
-                    func=funcnode,
-                    arg=name,
-                    context=context,
-                )
-
-        positional = self.positional_arguments[: len(funcnode.args.args)]
-        vararg = self.positional_arguments[len(funcnode.args.args) :]
-        argindex = funcnode.args.find_argname(name)[0]
-        kwonlyargs = {arg.name for arg in funcnode.args.kwonlyargs}
-        kwargs = {
-            key: value
-            for key, value in self.keyword_arguments.items()
-            if key not in kwonlyargs
-        }
-        # If there are too few positionals compared to
-        # what the function expects to receive, check to see
-        # if the missing positional arguments were passed
-        # as keyword arguments and if so, place them into the
-        # positional args list.
-        if len(positional) < len(funcnode.args.args):
-            for func_arg in funcnode.args.args:
-                if func_arg.name in kwargs:
-                    arg = kwargs.pop(func_arg.name)
-                    positional.append(arg)
-
-        if argindex is not None:
-            # 2. first argument of instance/class method
-            if argindex == 0 and funcnode.type in ("method", "classmethod"):
-                if context.boundnode is not None:
-                    boundnode = context.boundnode
-                else:
-                    # XXX can do better ?
-                    boundnode = funcnode.parent.frame()
-
-                if isinstance(boundnode, nodes.ClassDef):
-                    # Verify that we're accessing a method
-                    # of the metaclass through a class, as in
-                    # `cls.metaclass_method`. In this case, the
-                    # first argument is always the class.
-                    method_scope = funcnode.parent.scope()
-                    if method_scope is boundnode.metaclass():
-                        return iter((boundnode,))
-
-                if funcnode.type == "method":
-                    if not isinstance(boundnode, bases.Instance):
-                        boundnode = bases.Instance(boundnode)
-                    return iter((boundnode,))
-                if funcnode.type == "classmethod":
-                    return iter((boundnode,))
-            # if we have a method, extract one position
-            # from the index, so we'll take in account
-            # the extra parameter represented by `self` or `cls`
-            if funcnode.type in ("method", "classmethod"):
-                argindex -= 1
-            # 2. search arg index
-            try:
-                return self.positional_arguments[argindex].infer(context)
-            except IndexError:
-                pass
-
-        if funcnode.args.kwarg == name:
-            # It wants all the keywords that were passed into
-            # the call site.
-            if self.has_invalid_keywords():
-                raise exceptions.InferenceError(
-                    "Inference failed to find values for all keyword arguments "
-                    "to {func!r}: {unpacked_kwargs!r} doesn't correspond to "
-                    "{keyword_arguments!r}.",
-                    keyword_arguments=self.keyword_arguments,
-                    unpacked_kwargs=self._unpacked_kwargs,
-                    call_site=self,
-                    func=funcnode,
-                    arg=name,
-                    context=context,
-                )
-            kwarg = nodes.Dict(
-                lineno=funcnode.args.lineno,
-                col_offset=funcnode.args.col_offset,
-                parent=funcnode.args,
-            )
-            kwarg.postinit(
-                [(nodes.const_factory(key), value) for key, value in kwargs.items()]
-            )
-            return iter((kwarg,))
-        if funcnode.args.vararg == name:
-            # It wants all the args that were passed into
-            # the call site.
-            if self.has_invalid_arguments():
-                raise exceptions.InferenceError(
-                    "Inference failed to find values for all positional "
-                    "arguments to {func!r}: {unpacked_args!r} doesn't "
-                    "correspond to {positional_arguments!r}.",
-                    positional_arguments=self.positional_arguments,
-                    unpacked_args=self._unpacked_args,
-                    call_site=self,
-                    func=funcnode,
-                    arg=name,
-                    context=context,
-                )
-            args = nodes.Tuple(
-                lineno=funcnode.args.lineno,
-                col_offset=funcnode.args.col_offset,
-                parent=funcnode.args,
-            )
-            args.postinit(vararg)
-            return iter((args,))
-
-        # Check if it's a default parameter.
-        try:
-            return funcnode.args.default_value(name).infer(context)
-        except exceptions.NoDefault:
-            pass
-        raise exceptions.InferenceError(
-            "No value found for argument {name} to " "{func!r}",
-            call_site=self,
-            func=funcnode,
-            arg=name,
-            context=context,
-        )
diff --git a/venv/Lib/site-packages/astroid/as_string.py b/venv/Lib/site-packages/astroid/as_string.py
deleted file mode 100644
index 3cd6e0d..0000000
--- a/venv/Lib/site-packages/astroid/as_string.py
+++ /dev/null
@@ -1,633 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2009-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2013-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016 Jared Garst <jgarst@users.noreply.github.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 rr- <rr-@sakuya.pl>
-# Copyright (c) 2018 brendanator <brendan.maginnis@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""This module renders Astroid nodes as string:
-
-* :func:`to_code` function return equivalent (hopefully valid) python string
-
-* :func:`dump` function return an internal representation of nodes found
-  in the tree, useful for debugging or understanding the tree structure
-"""
-
-# pylint: disable=unused-argument
-
-DOC_NEWLINE = "\0"
-
-
-class AsStringVisitor:
-    """Visitor to render an Astroid node as a valid python code string"""
-
-    def __init__(self, indent):
-        self.indent = indent
-
-    def __call__(self, node):
-        """Makes this visitor behave as a simple function"""
-        return node.accept(self).replace(DOC_NEWLINE, "\n")
-
-    def _docs_dedent(self, doc):
-        """Stop newlines in docs being indented by self._stmt_list"""
-        return '\n%s"""%s"""' % (self.indent, doc.replace("\n", DOC_NEWLINE))
-
-    def _stmt_list(self, stmts, indent=True):
-        """return a list of nodes to string"""
-        stmts = "\n".join(nstr for nstr in [n.accept(self) for n in stmts] if nstr)
-        if indent:
-            return self.indent + stmts.replace("\n", "\n" + self.indent)
-
-        return stmts
-
-    def _precedence_parens(self, node, child, is_left=True):
-        """Wrap child in parens only if required to keep same semantics"""
-        if self._should_wrap(node, child, is_left):
-            return "(%s)" % child.accept(self)
-
-        return child.accept(self)
-
-    def _should_wrap(self, node, child, is_left):
-        """Wrap child if:
-            - it has lower precedence
-            - same precedence with position opposite to associativity direction
-        """
-        node_precedence = node.op_precedence()
-        child_precedence = child.op_precedence()
-
-        if node_precedence > child_precedence:
-            # 3 * (4 + 5)
-            return True
-
-        if (
-            node_precedence == child_precedence
-            and is_left != node.op_left_associative()
-        ):
-            # 3 - (4 - 5)
-            # (2**3)**4
-            return True
-
-        return False
-
-    ## visit_<node> methods ###########################################
-
-    def visit_arguments(self, node):
-        """return an astroid.Function node as string"""
-        return node.format_args()
-
-    def visit_assignattr(self, node):
-        """return an astroid.AssAttr node as string"""
-        return self.visit_attribute(node)
-
-    def visit_assert(self, node):
-        """return an astroid.Assert node as string"""
-        if node.fail:
-            return "assert %s, %s" % (node.test.accept(self), node.fail.accept(self))
-        return "assert %s" % node.test.accept(self)
-
-    def visit_assignname(self, node):
-        """return an astroid.AssName node as string"""
-        return node.name
-
-    def visit_assign(self, node):
-        """return an astroid.Assign node as string"""
-        lhs = " = ".join(n.accept(self) for n in node.targets)
-        return "%s = %s" % (lhs, node.value.accept(self))
-
-    def visit_augassign(self, node):
-        """return an astroid.AugAssign node as string"""
-        return "%s %s %s" % (node.target.accept(self), node.op, node.value.accept(self))
-
-    def visit_annassign(self, node):
-        """Return an astroid.AugAssign node as string"""
-
-        target = node.target.accept(self)
-        annotation = node.annotation.accept(self)
-        if node.value is None:
-            return "%s: %s" % (target, annotation)
-        return "%s: %s = %s" % (target, annotation, node.value.accept(self))
-
-    def visit_repr(self, node):
-        """return an astroid.Repr node as string"""
-        return "`%s`" % node.value.accept(self)
-
-    def visit_binop(self, node):
-        """return an astroid.BinOp node as string"""
-        left = self._precedence_parens(node, node.left)
-        right = self._precedence_parens(node, node.right, is_left=False)
-        if node.op == "**":
-            return "%s%s%s" % (left, node.op, right)
-
-        return "%s %s %s" % (left, node.op, right)
-
-    def visit_boolop(self, node):
-        """return an astroid.BoolOp node as string"""
-        values = ["%s" % self._precedence_parens(node, n) for n in node.values]
-        return (" %s " % node.op).join(values)
-
-    def visit_break(self, node):
-        """return an astroid.Break node as string"""
-        return "break"
-
-    def visit_call(self, node):
-        """return an astroid.Call node as string"""
-        expr_str = self._precedence_parens(node, node.func)
-        args = [arg.accept(self) for arg in node.args]
-        if node.keywords:
-            keywords = [kwarg.accept(self) for kwarg in node.keywords]
-        else:
-            keywords = []
-
-        args.extend(keywords)
-        return "%s(%s)" % (expr_str, ", ".join(args))
-
-    def visit_classdef(self, node):
-        """return an astroid.ClassDef node as string"""
-        decorate = node.decorators.accept(self) if node.decorators else ""
-        bases = ", ".join(n.accept(self) for n in node.bases)
-        metaclass = node.metaclass()
-        if metaclass and not node.has_metaclass_hack():
-            if bases:
-                bases = "(%s, metaclass=%s)" % (bases, metaclass.name)
-            else:
-                bases = "(metaclass=%s)" % metaclass.name
-        else:
-            bases = "(%s)" % bases if bases else ""
-        docs = self._docs_dedent(node.doc) if node.doc else ""
-        return "\n\n%sclass %s%s:%s\n%s\n" % (
-            decorate,
-            node.name,
-            bases,
-            docs,
-            self._stmt_list(node.body),
-        )
-
-    def visit_compare(self, node):
-        """return an astroid.Compare node as string"""
-        rhs_str = " ".join(
-            [
-                "%s %s" % (op, self._precedence_parens(node, expr, is_left=False))
-                for op, expr in node.ops
-            ]
-        )
-        return "%s %s" % (self._precedence_parens(node, node.left), rhs_str)
-
-    def visit_comprehension(self, node):
-        """return an astroid.Comprehension node as string"""
-        ifs = "".join(" if %s" % n.accept(self) for n in node.ifs)
-        return "for %s in %s%s" % (
-            node.target.accept(self),
-            node.iter.accept(self),
-            ifs,
-        )
-
-    def visit_const(self, node):
-        """return an astroid.Const node as string"""
-        if node.value is Ellipsis:
-            return "..."
-        return repr(node.value)
-
-    def visit_continue(self, node):
-        """return an astroid.Continue node as string"""
-        return "continue"
-
-    def visit_delete(self, node):  # XXX check if correct
-        """return an astroid.Delete node as string"""
-        return "del %s" % ", ".join(child.accept(self) for child in node.targets)
-
-    def visit_delattr(self, node):
-        """return an astroid.DelAttr node as string"""
-        return self.visit_attribute(node)
-
-    def visit_delname(self, node):
-        """return an astroid.DelName node as string"""
-        return node.name
-
-    def visit_decorators(self, node):
-        """return an astroid.Decorators node as string"""
-        return "@%s\n" % "\n@".join(item.accept(self) for item in node.nodes)
-
-    def visit_dict(self, node):
-        """return an astroid.Dict node as string"""
-        return "{%s}" % ", ".join(self._visit_dict(node))
-
-    def _visit_dict(self, node):
-        for key, value in node.items:
-            key = key.accept(self)
-            value = value.accept(self)
-            if key == "**":
-                # It can only be a DictUnpack node.
-                yield key + value
-            else:
-                yield "%s: %s" % (key, value)
-
-    def visit_dictunpack(self, node):
-        return "**"
-
-    def visit_dictcomp(self, node):
-        """return an astroid.DictComp node as string"""
-        return "{%s: %s %s}" % (
-            node.key.accept(self),
-            node.value.accept(self),
-            " ".join(n.accept(self) for n in node.generators),
-        )
-
-    def visit_expr(self, node):
-        """return an astroid.Discard node as string"""
-        return node.value.accept(self)
-
-    def visit_emptynode(self, node):
-        """dummy method for visiting an Empty node"""
-        return ""
-
-    def visit_excepthandler(self, node):
-        if node.type:
-            if node.name:
-                excs = "except %s, %s" % (
-                    node.type.accept(self),
-                    node.name.accept(self),
-                )
-            else:
-                excs = "except %s" % node.type.accept(self)
-        else:
-            excs = "except"
-        return "%s:\n%s" % (excs, self._stmt_list(node.body))
-
-    def visit_ellipsis(self, node):
-        """return an astroid.Ellipsis node as string"""
-        return "..."
-
-    def visit_empty(self, node):
-        """return an Empty node as string"""
-        return ""
-
-    def visit_exec(self, node):
-        """return an astroid.Exec node as string"""
-        if node.locals:
-            return "exec %s in %s, %s" % (
-                node.expr.accept(self),
-                node.locals.accept(self),
-                node.globals.accept(self),
-            )
-        if node.globals:
-            return "exec %s in %s" % (node.expr.accept(self), node.globals.accept(self))
-        return "exec %s" % node.expr.accept(self)
-
-    def visit_extslice(self, node):
-        """return an astroid.ExtSlice node as string"""
-        return ", ".join(dim.accept(self) for dim in node.dims)
-
-    def visit_for(self, node):
-        """return an astroid.For node as string"""
-        fors = "for %s in %s:\n%s" % (
-            node.target.accept(self),
-            node.iter.accept(self),
-            self._stmt_list(node.body),
-        )
-        if node.orelse:
-            fors = "%s\nelse:\n%s" % (fors, self._stmt_list(node.orelse))
-        return fors
-
-    def visit_importfrom(self, node):
-        """return an astroid.ImportFrom node as string"""
-        return "from %s import %s" % (
-            "." * (node.level or 0) + node.modname,
-            _import_string(node.names),
-        )
-
-    def visit_functiondef(self, node):
-        """return an astroid.Function node as string"""
-        decorate = node.decorators.accept(self) if node.decorators else ""
-        docs = self._docs_dedent(node.doc) if node.doc else ""
-        trailer = ":"
-        if node.returns:
-            return_annotation = " -> " + node.returns.as_string()
-            trailer = return_annotation + ":"
-        def_format = "\n%sdef %s(%s)%s%s\n%s"
-        return def_format % (
-            decorate,
-            node.name,
-            node.args.accept(self),
-            trailer,
-            docs,
-            self._stmt_list(node.body),
-        )
-
-    def visit_generatorexp(self, node):
-        """return an astroid.GeneratorExp node as string"""
-        return "(%s %s)" % (
-            node.elt.accept(self),
-            " ".join(n.accept(self) for n in node.generators),
-        )
-
-    def visit_attribute(self, node):
-        """return an astroid.Getattr node as string"""
-        return "%s.%s" % (self._precedence_parens(node, node.expr), node.attrname)
-
-    def visit_global(self, node):
-        """return an astroid.Global node as string"""
-        return "global %s" % ", ".join(node.names)
-
-    def visit_if(self, node):
-        """return an astroid.If node as string"""
-        ifs = ["if %s:\n%s" % (node.test.accept(self), self._stmt_list(node.body))]
-        if node.has_elif_block():
-            ifs.append("el%s" % self._stmt_list(node.orelse, indent=False))
-        elif node.orelse:
-            ifs.append("else:\n%s" % self._stmt_list(node.orelse))
-        return "\n".join(ifs)
-
-    def visit_ifexp(self, node):
-        """return an astroid.IfExp node as string"""
-        return "%s if %s else %s" % (
-            self._precedence_parens(node, node.body, is_left=True),
-            self._precedence_parens(node, node.test, is_left=True),
-            self._precedence_parens(node, node.orelse, is_left=False),
-        )
-
-    def visit_import(self, node):
-        """return an astroid.Import node as string"""
-        return "import %s" % _import_string(node.names)
-
-    def visit_keyword(self, node):
-        """return an astroid.Keyword node as string"""
-        if node.arg is None:
-            return "**%s" % node.value.accept(self)
-        return "%s=%s" % (node.arg, node.value.accept(self))
-
-    def visit_lambda(self, node):
-        """return an astroid.Lambda node as string"""
-        args = node.args.accept(self)
-        body = node.body.accept(self)
-        if args:
-            return "lambda %s: %s" % (args, body)
-
-        return "lambda: %s" % body
-
-    def visit_list(self, node):
-        """return an astroid.List node as string"""
-        return "[%s]" % ", ".join(child.accept(self) for child in node.elts)
-
-    def visit_listcomp(self, node):
-        """return an astroid.ListComp node as string"""
-        return "[%s %s]" % (
-            node.elt.accept(self),
-            " ".join(n.accept(self) for n in node.generators),
-        )
-
-    def visit_module(self, node):
-        """return an astroid.Module node as string"""
-        docs = '"""%s"""\n\n' % node.doc if node.doc else ""
-        return docs + "\n".join(n.accept(self) for n in node.body) + "\n\n"
-
-    def visit_name(self, node):
-        """return an astroid.Name node as string"""
-        return node.name
-
-    def visit_pass(self, node):
-        """return an astroid.Pass node as string"""
-        return "pass"
-
-    def visit_print(self, node):
-        """return an astroid.Print node as string"""
-        nodes = ", ".join(n.accept(self) for n in node.values)
-        if not node.nl:
-            nodes = "%s," % nodes
-        if node.dest:
-            return "print >> %s, %s" % (node.dest.accept(self), nodes)
-        return "print %s" % nodes
-
-    def visit_raise(self, node):
-        """return an astroid.Raise node as string"""
-        if node.exc:
-            if node.inst:
-                if node.tback:
-                    return "raise %s, %s, %s" % (
-                        node.exc.accept(self),
-                        node.inst.accept(self),
-                        node.tback.accept(self),
-                    )
-                return "raise %s, %s" % (node.exc.accept(self), node.inst.accept(self))
-            return "raise %s" % node.exc.accept(self)
-        return "raise"
-
-    def visit_return(self, node):
-        """return an astroid.Return node as string"""
-        if node.is_tuple_return() and len(node.value.elts) > 1:
-            elts = [child.accept(self) for child in node.value.elts]
-            return "return %s" % ", ".join(elts)
-
-        if node.value:
-            return "return %s" % node.value.accept(self)
-
-        return "return"
-
-    def visit_index(self, node):
-        """return an astroid.Index node as string"""
-        return node.value.accept(self)
-
-    def visit_set(self, node):
-        """return an astroid.Set node as string"""
-        return "{%s}" % ", ".join(child.accept(self) for child in node.elts)
-
-    def visit_setcomp(self, node):
-        """return an astroid.SetComp node as string"""
-        return "{%s %s}" % (
-            node.elt.accept(self),
-            " ".join(n.accept(self) for n in node.generators),
-        )
-
-    def visit_slice(self, node):
-        """return an astroid.Slice node as string"""
-        lower = node.lower.accept(self) if node.lower else ""
-        upper = node.upper.accept(self) if node.upper else ""
-        step = node.step.accept(self) if node.step else ""
-        if step:
-            return "%s:%s:%s" % (lower, upper, step)
-        return "%s:%s" % (lower, upper)
-
-    def visit_subscript(self, node):
-        """return an astroid.Subscript node as string"""
-        idx = node.slice
-        if idx.__class__.__name__.lower() == "index":
-            idx = idx.value
-        idxstr = idx.accept(self)
-        if idx.__class__.__name__.lower() == "tuple" and idx.elts:
-            # Remove parenthesis in tuple and extended slice.
-            # a[(::1, 1:)] is not valid syntax.
-            idxstr = idxstr[1:-1]
-        return "%s[%s]" % (self._precedence_parens(node, node.value), idxstr)
-
-    def visit_tryexcept(self, node):
-        """return an astroid.TryExcept node as string"""
-        trys = ["try:\n%s" % self._stmt_list(node.body)]
-        for handler in node.handlers:
-            trys.append(handler.accept(self))
-        if node.orelse:
-            trys.append("else:\n%s" % self._stmt_list(node.orelse))
-        return "\n".join(trys)
-
-    def visit_tryfinally(self, node):
-        """return an astroid.TryFinally node as string"""
-        return "try:\n%s\nfinally:\n%s" % (
-            self._stmt_list(node.body),
-            self._stmt_list(node.finalbody),
-        )
-
-    def visit_tuple(self, node):
-        """return an astroid.Tuple node as string"""
-        if len(node.elts) == 1:
-            return "(%s, )" % node.elts[0].accept(self)
-        return "(%s)" % ", ".join(child.accept(self) for child in node.elts)
-
-    def visit_unaryop(self, node):
-        """return an astroid.UnaryOp node as string"""
-        if node.op == "not":
-            operator = "not "
-        else:
-            operator = node.op
-        return "%s%s" % (operator, self._precedence_parens(node, node.operand))
-
-    def visit_while(self, node):
-        """return an astroid.While node as string"""
-        whiles = "while %s:\n%s" % (node.test.accept(self), self._stmt_list(node.body))
-        if node.orelse:
-            whiles = "%s\nelse:\n%s" % (whiles, self._stmt_list(node.orelse))
-        return whiles
-
-    def visit_with(self, node):  # 'with' without 'as' is possible
-        """return an astroid.With node as string"""
-        items = ", ".join(
-            ("%s" % expr.accept(self)) + (vars and " as %s" % (vars.accept(self)) or "")
-            for expr, vars in node.items
-        )
-        return "with %s:\n%s" % (items, self._stmt_list(node.body))
-
-    def visit_yield(self, node):
-        """yield an ast.Yield node as string"""
-        yi_val = (" " + node.value.accept(self)) if node.value else ""
-        expr = "yield" + yi_val
-        if node.parent.is_statement:
-            return expr
-
-        return "(%s)" % (expr,)
-
-    def visit_starred(self, node):
-        """return Starred node as string"""
-        return "*" + node.value.accept(self)
-
-    # These aren't for real AST nodes, but for inference objects.
-
-    def visit_frozenset(self, node):
-        return node.parent.accept(self)
-
-    def visit_super(self, node):
-        return node.parent.accept(self)
-
-    def visit_uninferable(self, node):
-        return str(node)
-
-
-class AsStringVisitor3(AsStringVisitor):
-    """AsStringVisitor3 overwrites some AsStringVisitor methods"""
-
-    def visit_excepthandler(self, node):
-        if node.type:
-            if node.name:
-                excs = "except %s as %s" % (
-                    node.type.accept(self),
-                    node.name.accept(self),
-                )
-            else:
-                excs = "except %s" % node.type.accept(self)
-        else:
-            excs = "except"
-        return "%s:\n%s" % (excs, self._stmt_list(node.body))
-
-    def visit_nonlocal(self, node):
-        """return an astroid.Nonlocal node as string"""
-        return "nonlocal %s" % ", ".join(node.names)
-
-    def visit_raise(self, node):
-        """return an astroid.Raise node as string"""
-        if node.exc:
-            if node.cause:
-                return "raise %s from %s" % (
-                    node.exc.accept(self),
-                    node.cause.accept(self),
-                )
-            return "raise %s" % node.exc.accept(self)
-        return "raise"
-
-    def visit_yieldfrom(self, node):
-        """ Return an astroid.YieldFrom node as string. """
-        yi_val = (" " + node.value.accept(self)) if node.value else ""
-        expr = "yield from" + yi_val
-        if node.parent.is_statement:
-            return expr
-
-        return "(%s)" % (expr,)
-
-    def visit_asyncfunctiondef(self, node):
-        function = super(AsStringVisitor3, self).visit_functiondef(node)
-        return "async " + function.strip()
-
-    def visit_await(self, node):
-        return "await %s" % node.value.accept(self)
-
-    def visit_asyncwith(self, node):
-        return "async %s" % self.visit_with(node)
-
-    def visit_asyncfor(self, node):
-        return "async %s" % self.visit_for(node)
-
-    def visit_joinedstr(self, node):
-        # Special treatment for constants,
-        # as we want to join literals not reprs
-        string = "".join(
-            value.value if type(value).__name__ == "Const" else value.accept(self)
-            for value in node.values
-        )
-        return "f'%s'" % string
-
-    def visit_formattedvalue(self, node):
-        return "{%s}" % node.value.accept(self)
-
-    def visit_comprehension(self, node):
-        """return an astroid.Comprehension node as string"""
-        return "%s%s" % (
-            "async " if node.is_async else "",
-            super(AsStringVisitor3, self).visit_comprehension(node),
-        )
-
-    def visit_namedexpr(self, node):
-        """Return an assignment expression node as string"""
-        target = node.target.accept(self)
-        value = node.value.accept(self)
-        return "%s := %s" % (target, value)
-
-
-def _import_string(names):
-    """return a list of (name, asname) formatted as a string"""
-    _names = []
-    for name, asname in names:
-        if asname is not None:
-            _names.append("%s as %s" % (name, asname))
-        else:
-            _names.append(name)
-    return ", ".join(_names)
-
-
-AsStringVisitor = AsStringVisitor3
-
-# This sets the default indent to 4 spaces.
-to_code = AsStringVisitor("    ")
diff --git a/venv/Lib/site-packages/astroid/bases.py b/venv/Lib/site-packages/astroid/bases.py
deleted file mode 100644
index d5b042a..0000000
--- a/venv/Lib/site-packages/astroid/bases.py
+++ /dev/null
@@ -1,542 +0,0 @@
-# Copyright (c) 2009-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016-2017 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017 Calen Pennington <calen.pennington@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Daniel Colascione <dancol@dancol.org>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""This module contains base classes and functions for the nodes and some
-inference utils.
-"""
-
-import builtins
-import collections
-
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import util
-
-objectmodel = util.lazy_import("interpreter.objectmodel")
-helpers = util.lazy_import("helpers")
-BUILTINS = builtins.__name__
-manager = util.lazy_import("manager")
-MANAGER = manager.AstroidManager()
-
-# TODO: check if needs special treatment
-BUILTINS = "builtins"
-BOOL_SPECIAL_METHOD = "__bool__"
-
-PROPERTIES = {BUILTINS + ".property", "abc.abstractproperty"}
-# List of possible property names. We use this list in order
-# to see if a method is a property or not. This should be
-# pretty reliable and fast, the alternative being to check each
-# decorator to see if its a real property-like descriptor, which
-# can be too complicated.
-# Also, these aren't qualified, because each project can
-# define them, we shouldn't expect to know every possible
-# property-like decorator!
-POSSIBLE_PROPERTIES = {
-    "cached_property",
-    "cachedproperty",
-    "lazyproperty",
-    "lazy_property",
-    "reify",
-    "lazyattribute",
-    "lazy_attribute",
-    "LazyProperty",
-    "lazy",
-    "cache_readonly",
-}
-
-
-def _is_property(meth):
-    if PROPERTIES.intersection(meth.decoratornames()):
-        return True
-    stripped = {
-        name.split(".")[-1]
-        for name in meth.decoratornames()
-        if name is not util.Uninferable
-    }
-    if any(name in stripped for name in POSSIBLE_PROPERTIES):
-        return True
-
-    # Lookup for subclasses of *property*
-    if not meth.decorators:
-        return False
-    for decorator in meth.decorators.nodes or ():
-        inferred = helpers.safe_infer(decorator)
-        if inferred is None or inferred is util.Uninferable:
-            continue
-        if inferred.__class__.__name__ == "ClassDef":
-            for base_class in inferred.bases:
-                if base_class.__class__.__name__ != "Name":
-                    continue
-                module, _ = base_class.lookup(base_class.name)
-                if module.name == BUILTINS and base_class.name == "property":
-                    return True
-
-    return False
-
-
-class Proxy:
-    """a simple proxy object
-
-    Note:
-
-    Subclasses of this object will need a custom __getattr__
-    if new instance attributes are created. See the Const class
-    """
-
-    _proxied = None  # proxied object may be set by class or by instance
-
-    def __init__(self, proxied=None):
-        if proxied is not None:
-            self._proxied = proxied
-
-    def __getattr__(self, name):
-        if name == "_proxied":
-            return getattr(self.__class__, "_proxied")
-        if name in self.__dict__:
-            return self.__dict__[name]
-        return getattr(self._proxied, name)
-
-    def infer(self, context=None):
-        yield self
-
-
-def _infer_stmts(stmts, context, frame=None):
-    """Return an iterator on statements inferred by each statement in *stmts*."""
-    inferred = False
-    if context is not None:
-        name = context.lookupname
-        context = context.clone()
-    else:
-        name = None
-        context = contextmod.InferenceContext()
-
-    for stmt in stmts:
-        if stmt is util.Uninferable:
-            yield stmt
-            inferred = True
-            continue
-        context.lookupname = stmt._infer_name(frame, name)
-        try:
-            for inferred in stmt.infer(context=context):
-                yield inferred
-                inferred = True
-        except exceptions.NameInferenceError:
-            continue
-        except exceptions.InferenceError:
-            yield util.Uninferable
-            inferred = True
-    if not inferred:
-        raise exceptions.InferenceError(
-            "Inference failed for all members of {stmts!r}.",
-            stmts=stmts,
-            frame=frame,
-            context=context,
-        )
-
-
-def _infer_method_result_truth(instance, method_name, context):
-    # Get the method from the instance and try to infer
-    # its return's truth value.
-    meth = next(instance.igetattr(method_name, context=context), None)
-    if meth and hasattr(meth, "infer_call_result"):
-        if not meth.callable():
-            return util.Uninferable
-        try:
-            for value in meth.infer_call_result(instance, context=context):
-                if value is util.Uninferable:
-                    return value
-
-                inferred = next(value.infer(context=context))
-                return inferred.bool_value()
-        except exceptions.InferenceError:
-            pass
-    return util.Uninferable
-
-
-class BaseInstance(Proxy):
-    """An instance base class, which provides lookup methods for potential instances."""
-
-    special_attributes = None
-
-    def display_type(self):
-        return "Instance of"
-
-    def getattr(self, name, context=None, lookupclass=True):
-        try:
-            values = self._proxied.instance_attr(name, context)
-        except exceptions.AttributeInferenceError as exc:
-            if self.special_attributes and name in self.special_attributes:
-                return [self.special_attributes.lookup(name)]
-
-            if lookupclass:
-                # Class attributes not available through the instance
-                # unless they are explicitly defined.
-                return self._proxied.getattr(name, context, class_context=False)
-
-            raise exceptions.AttributeInferenceError(
-                target=self, attribute=name, context=context
-            ) from exc
-        # since we've no context information, return matching class members as
-        # well
-        if lookupclass:
-            try:
-                return values + self._proxied.getattr(
-                    name, context, class_context=False
-                )
-            except exceptions.AttributeInferenceError:
-                pass
-        return values
-
-    def igetattr(self, name, context=None):
-        """inferred getattr"""
-        if not context:
-            context = contextmod.InferenceContext()
-        try:
-            # avoid recursively inferring the same attr on the same class
-            if context.push((self._proxied, name)):
-                raise exceptions.InferenceError(
-                    message="Cannot infer the same attribute again",
-                    node=self,
-                    context=context,
-                )
-
-            # XXX frame should be self._proxied, or not ?
-            get_attr = self.getattr(name, context, lookupclass=False)
-            yield from _infer_stmts(
-                self._wrap_attr(get_attr, context), context, frame=self
-            )
-        except exceptions.AttributeInferenceError as error:
-            try:
-                # fallback to class.igetattr since it has some logic to handle
-                # descriptors
-                # But only if the _proxied is the Class.
-                if self._proxied.__class__.__name__ != "ClassDef":
-                    raise
-                attrs = self._proxied.igetattr(name, context, class_context=False)
-                yield from self._wrap_attr(attrs, context)
-            except exceptions.AttributeInferenceError as error:
-                raise exceptions.InferenceError(**vars(error)) from error
-
-    def _wrap_attr(self, attrs, context=None):
-        """wrap bound methods of attrs in a InstanceMethod proxies"""
-        for attr in attrs:
-            if isinstance(attr, UnboundMethod):
-                if _is_property(attr):
-                    yield from attr.infer_call_result(self, context)
-                else:
-                    yield BoundMethod(attr, self)
-            elif hasattr(attr, "name") and attr.name == "<lambda>":
-                if attr.args.args and attr.args.args[0].name == "self":
-                    yield BoundMethod(attr, self)
-                    continue
-                yield attr
-            else:
-                yield attr
-
-    def infer_call_result(self, caller, context=None):
-        """infer what a class instance is returning when called"""
-        context = contextmod.bind_context_to_node(context, self)
-        inferred = False
-        for node in self._proxied.igetattr("__call__", context):
-            if node is util.Uninferable or not node.callable():
-                continue
-            for res in node.infer_call_result(caller, context):
-                inferred = True
-                yield res
-        if not inferred:
-            raise exceptions.InferenceError(node=self, caller=caller, context=context)
-
-
-class Instance(BaseInstance):
-    """A special node representing a class instance."""
-
-    # pylint: disable=unnecessary-lambda
-    special_attributes = util.lazy_descriptor(lambda: objectmodel.InstanceModel())
-
-    def __repr__(self):
-        return "<Instance of %s.%s at 0x%s>" % (
-            self._proxied.root().name,
-            self._proxied.name,
-            id(self),
-        )
-
-    def __str__(self):
-        return "Instance of %s.%s" % (self._proxied.root().name, self._proxied.name)
-
-    def callable(self):
-        try:
-            self._proxied.getattr("__call__", class_context=False)
-            return True
-        except exceptions.AttributeInferenceError:
-            return False
-
-    def pytype(self):
-        return self._proxied.qname()
-
-    def display_type(self):
-        return "Instance of"
-
-    def bool_value(self):
-        """Infer the truth value for an Instance
-
-        The truth value of an instance is determined by these conditions:
-
-           * if it implements __bool__ on Python 3 or __nonzero__
-             on Python 2, then its bool value will be determined by
-             calling this special method and checking its result.
-           * when this method is not defined, __len__() is called, if it
-             is defined, and the object is considered true if its result is
-             nonzero. If a class defines neither __len__() nor __bool__(),
-             all its instances are considered true.
-        """
-        context = contextmod.InferenceContext()
-        context.callcontext = contextmod.CallContext(args=[])
-        context.boundnode = self
-
-        try:
-            result = _infer_method_result_truth(self, BOOL_SPECIAL_METHOD, context)
-        except (exceptions.InferenceError, exceptions.AttributeInferenceError):
-            # Fallback to __len__.
-            try:
-                result = _infer_method_result_truth(self, "__len__", context)
-            except (exceptions.AttributeInferenceError, exceptions.InferenceError):
-                return True
-        return result
-
-    # This is set in inference.py.
-    def getitem(self, index, context=None):
-        pass
-
-
-class UnboundMethod(Proxy):
-    """a special node representing a method not bound to an instance"""
-
-    # pylint: disable=unnecessary-lambda
-    special_attributes = util.lazy_descriptor(lambda: objectmodel.UnboundMethodModel())
-
-    def __repr__(self):
-        frame = self._proxied.parent.frame()
-        return "<%s %s of %s at 0x%s" % (
-            self.__class__.__name__,
-            self._proxied.name,
-            frame.qname(),
-            id(self),
-        )
-
-    def implicit_parameters(self):
-        return 0
-
-    def is_bound(self):
-        return False
-
-    def getattr(self, name, context=None):
-        if name in self.special_attributes:
-            return [self.special_attributes.lookup(name)]
-        return self._proxied.getattr(name, context)
-
-    def igetattr(self, name, context=None):
-        if name in self.special_attributes:
-            return iter((self.special_attributes.lookup(name),))
-        return self._proxied.igetattr(name, context)
-
-    def infer_call_result(self, caller, context):
-        """
-        The boundnode of the regular context with a function called
-        on ``object.__new__`` will be of type ``object``,
-        which is incorrect for the argument in general.
-        If no context is given the ``object.__new__`` call argument will
-        correctly inferred except when inside a call that requires
-        the additional context (such as a classmethod) of the boundnode
-        to determine which class the method was called from
-        """
-
-        # If we're unbound method __new__ of builtin object, the result is an
-        # instance of the class given as first argument.
-        if (
-            self._proxied.name == "__new__"
-            and self._proxied.parent.frame().qname() == "%s.object" % BUILTINS
-        ):
-            if caller.args:
-                node_context = context.extra_context.get(caller.args[0])
-                infer = caller.args[0].infer(context=node_context)
-            else:
-                infer = []
-            return (Instance(x) if x is not util.Uninferable else x for x in infer)
-        return self._proxied.infer_call_result(caller, context)
-
-    def bool_value(self):
-        return True
-
-
-class BoundMethod(UnboundMethod):
-    """a special node representing a method bound to an instance"""
-
-    # pylint: disable=unnecessary-lambda
-    special_attributes = util.lazy_descriptor(lambda: objectmodel.BoundMethodModel())
-
-    def __init__(self, proxy, bound):
-        UnboundMethod.__init__(self, proxy)
-        self.bound = bound
-
-    def implicit_parameters(self):
-        return 1
-
-    def is_bound(self):
-        return True
-
-    def _infer_type_new_call(self, caller, context):
-        """Try to infer what type.__new__(mcs, name, bases, attrs) returns.
-
-        In order for such call to be valid, the metaclass needs to be
-        a subtype of ``type``, the name needs to be a string, the bases
-        needs to be a tuple of classes
-        """
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import node_classes
-
-        # Verify the metaclass
-        mcs = next(caller.args[0].infer(context=context))
-        if mcs.__class__.__name__ != "ClassDef":
-            # Not a valid first argument.
-            return None
-        if not mcs.is_subtype_of("%s.type" % BUILTINS):
-            # Not a valid metaclass.
-            return None
-
-        # Verify the name
-        name = next(caller.args[1].infer(context=context))
-        if name.__class__.__name__ != "Const":
-            # Not a valid name, needs to be a const.
-            return None
-        if not isinstance(name.value, str):
-            # Needs to be a string.
-            return None
-
-        # Verify the bases
-        bases = next(caller.args[2].infer(context=context))
-        if bases.__class__.__name__ != "Tuple":
-            # Needs to be a tuple.
-            return None
-        inferred_bases = [next(elt.infer(context=context)) for elt in bases.elts]
-        if any(base.__class__.__name__ != "ClassDef" for base in inferred_bases):
-            # All the bases needs to be Classes
-            return None
-
-        # Verify the attributes.
-        attrs = next(caller.args[3].infer(context=context))
-        if attrs.__class__.__name__ != "Dict":
-            # Needs to be a dictionary.
-            return None
-        cls_locals = collections.defaultdict(list)
-        for key, value in attrs.items:
-            key = next(key.infer(context=context))
-            value = next(value.infer(context=context))
-            # Ignore non string keys
-            if key.__class__.__name__ == "Const" and isinstance(key.value, str):
-                cls_locals[key.value].append(value)
-
-        # Build the class from now.
-        cls = mcs.__class__(
-            name=name.value,
-            lineno=caller.lineno,
-            col_offset=caller.col_offset,
-            parent=caller,
-        )
-        empty = node_classes.Pass()
-        cls.postinit(
-            bases=bases.elts,
-            body=[empty],
-            decorators=[],
-            newstyle=True,
-            metaclass=mcs,
-            keywords=[],
-        )
-        cls.locals = cls_locals
-        return cls
-
-    def infer_call_result(self, caller, context=None):
-        context = contextmod.bind_context_to_node(context, self.bound)
-        if (
-            self.bound.__class__.__name__ == "ClassDef"
-            and self.bound.name == "type"
-            and self.name == "__new__"
-            and len(caller.args) == 4
-        ):
-            # Check if we have a ``type.__new__(mcs, name, bases, attrs)`` call.
-            new_cls = self._infer_type_new_call(caller, context)
-            if new_cls:
-                return iter((new_cls,))
-
-        return super(BoundMethod, self).infer_call_result(caller, context)
-
-    def bool_value(self):
-        return True
-
-
-class Generator(BaseInstance):
-    """a special node representing a generator.
-
-    Proxied class is set once for all in raw_building.
-    """
-
-    # pylint: disable=unnecessary-lambda
-    special_attributes = util.lazy_descriptor(lambda: objectmodel.GeneratorModel())
-
-    # pylint: disable=super-init-not-called
-    def __init__(self, parent=None):
-        self.parent = parent
-
-    def callable(self):
-        return False
-
-    def pytype(self):
-        return "%s.generator" % BUILTINS
-
-    def display_type(self):
-        return "Generator"
-
-    def bool_value(self):
-        return True
-
-    def __repr__(self):
-        return "<Generator(%s) l.%s at 0x%s>" % (
-            self._proxied.name,
-            self.lineno,
-            id(self),
-        )
-
-    def __str__(self):
-        return "Generator(%s)" % (self._proxied.name)
-
-
-class AsyncGenerator(Generator):
-    """Special node representing an async generator"""
-
-    def pytype(self):
-        return "%s.async_generator" % BUILTINS
-
-    def display_type(self):
-        return "AsyncGenerator"
-
-    def __repr__(self):
-        return "<AsyncGenerator(%s) l.%s at 0x%s>" % (
-            self._proxied.name,
-            self.lineno,
-            id(self),
-        )
-
-    def __str__(self):
-        return "AsyncGenerator(%s)" % (self._proxied.name)
diff --git a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_argparse.cpython-37.pyc b/venv/Lib/site-packages/astroid/brain/__pycache__/brain_argparse.cpython-37.pyc
deleted file mode 100644
index 02f8cf7..0000000
--- a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_argparse.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_attrs.cpython-37.pyc b/venv/Lib/site-packages/astroid/brain/__pycache__/brain_attrs.cpython-37.pyc
deleted file mode 100644
index 7cf4841..0000000
--- a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_attrs.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_curses.cpython-37.pyc b/venv/Lib/site-packages/astroid/brain/__pycache__/brain_curses.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_subprocess.cpython-37.pyc b/venv/Lib/site-packages/astroid/brain/__pycache__/brain_subprocess.cpython-37.pyc
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+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_threading.cpython-37.pyc b/venv/Lib/site-packages/astroid/brain/__pycache__/brain_threading.cpython-37.pyc
deleted file mode 100644
index a9214ba..0000000
--- a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_threading.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_typing.cpython-37.pyc b/venv/Lib/site-packages/astroid/brain/__pycache__/brain_typing.cpython-37.pyc
deleted file mode 100644
index 9cb0782..0000000
--- a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_typing.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_uuid.cpython-37.pyc b/venv/Lib/site-packages/astroid/brain/__pycache__/brain_uuid.cpython-37.pyc
deleted file mode 100644
index f6850ba..0000000
--- a/venv/Lib/site-packages/astroid/brain/__pycache__/brain_uuid.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/brain/brain_argparse.py b/venv/Lib/site-packages/astroid/brain/brain_argparse.py
deleted file mode 100644
index d489911..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_argparse.py
+++ /dev/null
@@ -1,33 +0,0 @@
-from astroid import MANAGER, arguments, nodes, inference_tip, UseInferenceDefault
-
-
-def infer_namespace(node, context=None):
-    callsite = arguments.CallSite.from_call(node)
-    if not callsite.keyword_arguments:
-        # Cannot make sense of it.
-        raise UseInferenceDefault()
-
-    class_node = nodes.ClassDef("Namespace", "docstring")
-    class_node.parent = node.parent
-    for attr in set(callsite.keyword_arguments):
-        fake_node = nodes.EmptyNode()
-        fake_node.parent = class_node
-        fake_node.attrname = attr
-        class_node.instance_attrs[attr] = [fake_node]
-    return iter((class_node.instantiate_class(),))
-
-
-def _looks_like_namespace(node):
-    func = node.func
-    if isinstance(func, nodes.Attribute):
-        return (
-            func.attrname == "Namespace"
-            and isinstance(func.expr, nodes.Name)
-            and func.expr.name == "argparse"
-        )
-    return False
-
-
-MANAGER.register_transform(
-    nodes.Call, inference_tip(infer_namespace), _looks_like_namespace
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_attrs.py b/venv/Lib/site-packages/astroid/brain/brain_attrs.py
deleted file mode 100644
index 670736f..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_attrs.py
+++ /dev/null
@@ -1,65 +0,0 @@
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-"""
-Astroid hook for the attrs library
-
-Without this hook pylint reports unsupported-assignment-operation
-for attrs classes
-"""
-
-import astroid
-from astroid import MANAGER
-
-
-ATTRIB_NAMES = frozenset(("attr.ib", "attrib", "attr.attrib"))
-ATTRS_NAMES = frozenset(("attr.s", "attrs", "attr.attrs", "attr.attributes"))
-
-
-def is_decorated_with_attrs(node, decorator_names=ATTRS_NAMES):
-    """Return True if a decorated node has
-    an attr decorator applied."""
-    if not node.decorators:
-        return False
-    for decorator_attribute in node.decorators.nodes:
-        if isinstance(decorator_attribute, astroid.Call):  # decorator with arguments
-            decorator_attribute = decorator_attribute.func
-        if decorator_attribute.as_string() in decorator_names:
-            return True
-    return False
-
-
-def attr_attributes_transform(node):
-    """Given that the ClassNode has an attr decorator,
-    rewrite class attributes as instance attributes
-    """
-    # Astroid can't infer this attribute properly
-    # Prevents https://github.com/PyCQA/pylint/issues/1884
-    node.locals["__attrs_attrs__"] = [astroid.Unknown(parent=node)]
-
-    for cdefbodynode in node.body:
-        if not isinstance(cdefbodynode, (astroid.Assign, astroid.AnnAssign)):
-            continue
-        if isinstance(cdefbodynode.value, astroid.Call):
-            if cdefbodynode.value.func.as_string() not in ATTRIB_NAMES:
-                continue
-        else:
-            continue
-        targets = (
-            cdefbodynode.targets
-            if hasattr(cdefbodynode, "targets")
-            else [cdefbodynode.target]
-        )
-        for target in targets:
-
-            rhs_node = astroid.Unknown(
-                lineno=cdefbodynode.lineno,
-                col_offset=cdefbodynode.col_offset,
-                parent=cdefbodynode,
-            )
-            node.locals[target.name] = [rhs_node]
-            node.instance_attrs[target.name] = [rhs_node]
-
-
-MANAGER.register_transform(
-    astroid.ClassDef, attr_attributes_transform, is_decorated_with_attrs
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_builtin_inference.py b/venv/Lib/site-packages/astroid/brain/brain_builtin_inference.py
deleted file mode 100644
index 2dd7cc5..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_builtin_inference.py
+++ /dev/null
@@ -1,829 +0,0 @@
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014-2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Rene Zhang <rz99@cornell.edu>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for various builtins."""
-
-from functools import partial
-from textwrap import dedent
-
-import six
-from astroid import (
-    MANAGER,
-    UseInferenceDefault,
-    AttributeInferenceError,
-    inference_tip,
-    InferenceError,
-    NameInferenceError,
-    AstroidTypeError,
-    MroError,
-)
-from astroid import arguments
-from astroid.builder import AstroidBuilder
-from astroid import helpers
-from astroid import nodes
-from astroid import objects
-from astroid import scoped_nodes
-from astroid import util
-
-
-OBJECT_DUNDER_NEW = "object.__new__"
-
-
-def _extend_str(class_node, rvalue):
-    """function to extend builtin str/unicode class"""
-    code = dedent(
-        """
-    class whatever(object):
-        def join(self, iterable):
-            return {rvalue}
-        def replace(self, old, new, count=None):
-            return {rvalue}
-        def format(self, *args, **kwargs):
-            return {rvalue}
-        def encode(self, encoding='ascii', errors=None):
-            return ''
-        def decode(self, encoding='ascii', errors=None):
-            return u''
-        def capitalize(self):
-            return {rvalue}
-        def title(self):
-            return {rvalue}
-        def lower(self):
-            return {rvalue}
-        def upper(self):
-            return {rvalue}
-        def swapcase(self):
-            return {rvalue}
-        def index(self, sub, start=None, end=None):
-            return 0
-        def find(self, sub, start=None, end=None):
-            return 0
-        def count(self, sub, start=None, end=None):
-            return 0
-        def strip(self, chars=None):
-            return {rvalue}
-        def lstrip(self, chars=None):
-            return {rvalue}
-        def rstrip(self, chars=None):
-            return {rvalue}
-        def rjust(self, width, fillchar=None):
-            return {rvalue}
-        def center(self, width, fillchar=None):
-            return {rvalue}
-        def ljust(self, width, fillchar=None):
-            return {rvalue}
-    """
-    )
-    code = code.format(rvalue=rvalue)
-    fake = AstroidBuilder(MANAGER).string_build(code)["whatever"]
-    for method in fake.mymethods():
-        method.parent = class_node
-        method.lineno = None
-        method.col_offset = None
-        if "__class__" in method.locals:
-            method.locals["__class__"] = [class_node]
-        class_node.locals[method.name] = [method]
-        method.parent = class_node
-
-
-def _extend_builtins(class_transforms):
-    builtin_ast = MANAGER.builtins_module
-    for class_name, transform in class_transforms.items():
-        transform(builtin_ast[class_name])
-
-
-_extend_builtins(
-    {
-        "bytes": partial(_extend_str, rvalue="b''"),
-        "str": partial(_extend_str, rvalue="''"),
-    }
-)
-
-
-def _builtin_filter_predicate(node, builtin_name):
-    if isinstance(node.func, nodes.Name) and node.func.name == builtin_name:
-        return True
-    if isinstance(node.func, nodes.Attribute):
-        return (
-            node.func.attrname == "fromkeys"
-            and isinstance(node.func.expr, nodes.Name)
-            and node.func.expr.name == "dict"
-        )
-    return False
-
-
-def register_builtin_transform(transform, builtin_name):
-    """Register a new transform function for the given *builtin_name*.
-
-    The transform function must accept two parameters, a node and
-    an optional context.
-    """
-
-    def _transform_wrapper(node, context=None):
-        result = transform(node, context=context)
-        if result:
-            if not result.parent:
-                # Let the transformation function determine
-                # the parent for its result. Otherwise,
-                # we set it to be the node we transformed from.
-                result.parent = node
-
-            if result.lineno is None:
-                result.lineno = node.lineno
-            if result.col_offset is None:
-                result.col_offset = node.col_offset
-        return iter([result])
-
-    MANAGER.register_transform(
-        nodes.Call,
-        inference_tip(_transform_wrapper),
-        partial(_builtin_filter_predicate, builtin_name=builtin_name),
-    )
-
-
-def _container_generic_inference(node, context, node_type, transform):
-    args = node.args
-    if not args:
-        return node_type()
-    if len(node.args) > 1:
-        raise UseInferenceDefault()
-
-    arg, = args
-    transformed = transform(arg)
-    if not transformed:
-        try:
-            inferred = next(arg.infer(context=context))
-        except (InferenceError, StopIteration):
-            raise UseInferenceDefault()
-        if inferred is util.Uninferable:
-            raise UseInferenceDefault()
-        transformed = transform(inferred)
-    if not transformed or transformed is util.Uninferable:
-        raise UseInferenceDefault()
-    return transformed
-
-
-def _container_generic_transform(arg, klass, iterables, build_elts):
-    if isinstance(arg, klass):
-        return arg
-    elif isinstance(arg, iterables):
-        if all(isinstance(elt, nodes.Const) for elt in arg.elts):
-            elts = [elt.value for elt in arg.elts]
-        else:
-            # TODO: Does not handle deduplication for sets.
-            elts = filter(None, map(helpers.safe_infer, arg.elts))
-    elif isinstance(arg, nodes.Dict):
-        # Dicts need to have consts as strings already.
-        if not all(isinstance(elt[0], nodes.Const) for elt in arg.items):
-            raise UseInferenceDefault()
-        elts = [item[0].value for item in arg.items]
-    elif isinstance(arg, nodes.Const) and isinstance(
-        arg.value, (six.string_types, six.binary_type)
-    ):
-        elts = arg.value
-    else:
-        return
-    return klass.from_elements(elts=build_elts(elts))
-
-
-def _infer_builtin_container(
-    node, context, klass=None, iterables=None, build_elts=None
-):
-    transform_func = partial(
-        _container_generic_transform,
-        klass=klass,
-        iterables=iterables,
-        build_elts=build_elts,
-    )
-
-    return _container_generic_inference(node, context, klass, transform_func)
-
-
-# pylint: disable=invalid-name
-infer_tuple = partial(
-    _infer_builtin_container,
-    klass=nodes.Tuple,
-    iterables=(
-        nodes.List,
-        nodes.Set,
-        objects.FrozenSet,
-        objects.DictItems,
-        objects.DictKeys,
-        objects.DictValues,
-    ),
-    build_elts=tuple,
-)
-
-infer_list = partial(
-    _infer_builtin_container,
-    klass=nodes.List,
-    iterables=(
-        nodes.Tuple,
-        nodes.Set,
-        objects.FrozenSet,
-        objects.DictItems,
-        objects.DictKeys,
-        objects.DictValues,
-    ),
-    build_elts=list,
-)
-
-infer_set = partial(
-    _infer_builtin_container,
-    klass=nodes.Set,
-    iterables=(nodes.List, nodes.Tuple, objects.FrozenSet, objects.DictKeys),
-    build_elts=set,
-)
-
-infer_frozenset = partial(
-    _infer_builtin_container,
-    klass=objects.FrozenSet,
-    iterables=(nodes.List, nodes.Tuple, nodes.Set, objects.FrozenSet, objects.DictKeys),
-    build_elts=frozenset,
-)
-
-
-def _get_elts(arg, context):
-    is_iterable = lambda n: isinstance(n, (nodes.List, nodes.Tuple, nodes.Set))
-    try:
-        inferred = next(arg.infer(context))
-    except (InferenceError, NameInferenceError):
-        raise UseInferenceDefault()
-    if isinstance(inferred, nodes.Dict):
-        items = inferred.items
-    elif is_iterable(inferred):
-        items = []
-        for elt in inferred.elts:
-            # If an item is not a pair of two items,
-            # then fallback to the default inference.
-            # Also, take in consideration only hashable items,
-            # tuples and consts. We are choosing Names as well.
-            if not is_iterable(elt):
-                raise UseInferenceDefault()
-            if len(elt.elts) != 2:
-                raise UseInferenceDefault()
-            if not isinstance(elt.elts[0], (nodes.Tuple, nodes.Const, nodes.Name)):
-                raise UseInferenceDefault()
-            items.append(tuple(elt.elts))
-    else:
-        raise UseInferenceDefault()
-    return items
-
-
-def infer_dict(node, context=None):
-    """Try to infer a dict call to a Dict node.
-
-    The function treats the following cases:
-
-        * dict()
-        * dict(mapping)
-        * dict(iterable)
-        * dict(iterable, **kwargs)
-        * dict(mapping, **kwargs)
-        * dict(**kwargs)
-
-    If a case can't be inferred, we'll fallback to default inference.
-    """
-    call = arguments.CallSite.from_call(node)
-    if call.has_invalid_arguments() or call.has_invalid_keywords():
-        raise UseInferenceDefault
-
-    args = call.positional_arguments
-    kwargs = list(call.keyword_arguments.items())
-
-    if not args and not kwargs:
-        # dict()
-        return nodes.Dict()
-    elif kwargs and not args:
-        # dict(a=1, b=2, c=4)
-        items = [(nodes.Const(key), value) for key, value in kwargs]
-    elif len(args) == 1 and kwargs:
-        # dict(some_iterable, b=2, c=4)
-        elts = _get_elts(args[0], context)
-        keys = [(nodes.Const(key), value) for key, value in kwargs]
-        items = elts + keys
-    elif len(args) == 1:
-        items = _get_elts(args[0], context)
-    else:
-        raise UseInferenceDefault()
-
-    value = nodes.Dict(
-        col_offset=node.col_offset, lineno=node.lineno, parent=node.parent
-    )
-    value.postinit(items)
-    return value
-
-
-def infer_super(node, context=None):
-    """Understand super calls.
-
-    There are some restrictions for what can be understood:
-
-        * unbounded super (one argument form) is not understood.
-
-        * if the super call is not inside a function (classmethod or method),
-          then the default inference will be used.
-
-        * if the super arguments can't be inferred, the default inference
-          will be used.
-    """
-    if len(node.args) == 1:
-        # Ignore unbounded super.
-        raise UseInferenceDefault
-
-    scope = node.scope()
-    if not isinstance(scope, nodes.FunctionDef):
-        # Ignore non-method uses of super.
-        raise UseInferenceDefault
-    if scope.type not in ("classmethod", "method"):
-        # Not interested in staticmethods.
-        raise UseInferenceDefault
-
-    cls = scoped_nodes.get_wrapping_class(scope)
-    if not len(node.args):
-        mro_pointer = cls
-        # In we are in a classmethod, the interpreter will fill
-        # automatically the class as the second argument, not an instance.
-        if scope.type == "classmethod":
-            mro_type = cls
-        else:
-            mro_type = cls.instantiate_class()
-    else:
-        try:
-            mro_pointer = next(node.args[0].infer(context=context))
-        except InferenceError:
-            raise UseInferenceDefault
-        try:
-            mro_type = next(node.args[1].infer(context=context))
-        except InferenceError:
-            raise UseInferenceDefault
-
-    if mro_pointer is util.Uninferable or mro_type is util.Uninferable:
-        # No way we could understand this.
-        raise UseInferenceDefault
-
-    super_obj = objects.Super(
-        mro_pointer=mro_pointer, mro_type=mro_type, self_class=cls, scope=scope
-    )
-    super_obj.parent = node
-    return super_obj
-
-
-def _infer_getattr_args(node, context):
-    if len(node.args) not in (2, 3):
-        # Not a valid getattr call.
-        raise UseInferenceDefault
-
-    try:
-        obj = next(node.args[0].infer(context=context))
-        attr = next(node.args[1].infer(context=context))
-    except InferenceError:
-        raise UseInferenceDefault
-
-    if obj is util.Uninferable or attr is util.Uninferable:
-        # If one of the arguments is something we can't infer,
-        # then also make the result of the getattr call something
-        # which is unknown.
-        return util.Uninferable, util.Uninferable
-
-    is_string = isinstance(attr, nodes.Const) and isinstance(
-        attr.value, six.string_types
-    )
-    if not is_string:
-        raise UseInferenceDefault
-
-    return obj, attr.value
-
-
-def infer_getattr(node, context=None):
-    """Understand getattr calls
-
-    If one of the arguments is an Uninferable object, then the
-    result will be an Uninferable object. Otherwise, the normal attribute
-    lookup will be done.
-    """
-    obj, attr = _infer_getattr_args(node, context)
-    if (
-        obj is util.Uninferable
-        or attr is util.Uninferable
-        or not hasattr(obj, "igetattr")
-    ):
-        return util.Uninferable
-
-    try:
-        return next(obj.igetattr(attr, context=context))
-    except (StopIteration, InferenceError, AttributeInferenceError):
-        if len(node.args) == 3:
-            # Try to infer the default and return it instead.
-            try:
-                return next(node.args[2].infer(context=context))
-            except InferenceError:
-                raise UseInferenceDefault
-
-    raise UseInferenceDefault
-
-
-def infer_hasattr(node, context=None):
-    """Understand hasattr calls
-
-    This always guarantees three possible outcomes for calling
-    hasattr: Const(False) when we are sure that the object
-    doesn't have the intended attribute, Const(True) when
-    we know that the object has the attribute and Uninferable
-    when we are unsure of the outcome of the function call.
-    """
-    try:
-        obj, attr = _infer_getattr_args(node, context)
-        if (
-            obj is util.Uninferable
-            or attr is util.Uninferable
-            or not hasattr(obj, "getattr")
-        ):
-            return util.Uninferable
-        obj.getattr(attr, context=context)
-    except UseInferenceDefault:
-        # Can't infer something from this function call.
-        return util.Uninferable
-    except AttributeInferenceError:
-        # Doesn't have it.
-        return nodes.Const(False)
-    return nodes.Const(True)
-
-
-def infer_callable(node, context=None):
-    """Understand callable calls
-
-    This follows Python's semantics, where an object
-    is callable if it provides an attribute __call__,
-    even though that attribute is something which can't be
-    called.
-    """
-    if len(node.args) != 1:
-        # Invalid callable call.
-        raise UseInferenceDefault
-
-    argument = node.args[0]
-    try:
-        inferred = next(argument.infer(context=context))
-    except InferenceError:
-        return util.Uninferable
-    if inferred is util.Uninferable:
-        return util.Uninferable
-    return nodes.Const(inferred.callable())
-
-
-def infer_bool(node, context=None):
-    """Understand bool calls."""
-    if len(node.args) > 1:
-        # Invalid bool call.
-        raise UseInferenceDefault
-
-    if not node.args:
-        return nodes.Const(False)
-
-    argument = node.args[0]
-    try:
-        inferred = next(argument.infer(context=context))
-    except InferenceError:
-        return util.Uninferable
-    if inferred is util.Uninferable:
-        return util.Uninferable
-
-    bool_value = inferred.bool_value()
-    if bool_value is util.Uninferable:
-        return util.Uninferable
-    return nodes.Const(bool_value)
-
-
-def infer_type(node, context=None):
-    """Understand the one-argument form of *type*."""
-    if len(node.args) != 1:
-        raise UseInferenceDefault
-
-    return helpers.object_type(node.args[0], context)
-
-
-def infer_slice(node, context=None):
-    """Understand `slice` calls."""
-    args = node.args
-    if not 0 < len(args) <= 3:
-        raise UseInferenceDefault
-
-    infer_func = partial(helpers.safe_infer, context=context)
-    args = [infer_func(arg) for arg in args]
-    for arg in args:
-        if not arg or arg is util.Uninferable:
-            raise UseInferenceDefault
-        if not isinstance(arg, nodes.Const):
-            raise UseInferenceDefault
-        if not isinstance(arg.value, (type(None), int)):
-            raise UseInferenceDefault
-
-    if len(args) < 3:
-        # Make sure we have 3 arguments.
-        args.extend([None] * (3 - len(args)))
-
-    slice_node = nodes.Slice(
-        lineno=node.lineno, col_offset=node.col_offset, parent=node.parent
-    )
-    slice_node.postinit(*args)
-    return slice_node
-
-
-def _infer_object__new__decorator(node, context=None):
-    # Instantiate class immediately
-    # since that's what @object.__new__ does
-    return iter((node.instantiate_class(),))
-
-
-def _infer_object__new__decorator_check(node):
-    """Predicate before inference_tip
-
-    Check if the given ClassDef has an @object.__new__ decorator
-    """
-    if not node.decorators:
-        return False
-
-    for decorator in node.decorators.nodes:
-        if isinstance(decorator, nodes.Attribute):
-            if decorator.as_string() == OBJECT_DUNDER_NEW:
-                return True
-    return False
-
-
-def infer_issubclass(callnode, context=None):
-    """Infer issubclass() calls
-
-    :param nodes.Call callnode: an `issubclass` call
-    :param InferenceContext: the context for the inference
-    :rtype nodes.Const: Boolean Const value of the `issubclass` call
-    :raises UseInferenceDefault: If the node cannot be inferred
-    """
-    call = arguments.CallSite.from_call(callnode)
-    if call.keyword_arguments:
-        # issubclass doesn't support keyword arguments
-        raise UseInferenceDefault("TypeError: issubclass() takes no keyword arguments")
-    if len(call.positional_arguments) != 2:
-        raise UseInferenceDefault(
-            "Expected two arguments, got {count}".format(
-                count=len(call.positional_arguments)
-            )
-        )
-    # The left hand argument is the obj to be checked
-    obj_node, class_or_tuple_node = call.positional_arguments
-
-    try:
-        obj_type = next(obj_node.infer(context=context))
-    except InferenceError as exc:
-        raise UseInferenceDefault from exc
-    if not isinstance(obj_type, nodes.ClassDef):
-        raise UseInferenceDefault("TypeError: arg 1 must be class")
-
-    # The right hand argument is the class(es) that the given
-    # object is to be checked against.
-    try:
-        class_container = _class_or_tuple_to_container(
-            class_or_tuple_node, context=context
-        )
-    except InferenceError as exc:
-        raise UseInferenceDefault from exc
-    try:
-        issubclass_bool = helpers.object_issubclass(obj_type, class_container, context)
-    except AstroidTypeError as exc:
-        raise UseInferenceDefault("TypeError: " + str(exc)) from exc
-    except MroError as exc:
-        raise UseInferenceDefault from exc
-    return nodes.Const(issubclass_bool)
-
-
-def infer_isinstance(callnode, context=None):
-    """Infer isinstance calls
-
-    :param nodes.Call callnode: an isinstance call
-    :param InferenceContext: context for call
-        (currently unused but is a common interface for inference)
-    :rtype nodes.Const: Boolean Const value of isinstance call
-
-    :raises UseInferenceDefault: If the node cannot be inferred
-    """
-    call = arguments.CallSite.from_call(callnode)
-    if call.keyword_arguments:
-        # isinstance doesn't support keyword arguments
-        raise UseInferenceDefault("TypeError: isinstance() takes no keyword arguments")
-    if len(call.positional_arguments) != 2:
-        raise UseInferenceDefault(
-            "Expected two arguments, got {count}".format(
-                count=len(call.positional_arguments)
-            )
-        )
-    # The left hand argument is the obj to be checked
-    obj_node, class_or_tuple_node = call.positional_arguments
-    # The right hand argument is the class(es) that the given
-    # obj is to be check is an instance of
-    try:
-        class_container = _class_or_tuple_to_container(
-            class_or_tuple_node, context=context
-        )
-    except InferenceError:
-        raise UseInferenceDefault
-    try:
-        isinstance_bool = helpers.object_isinstance(obj_node, class_container, context)
-    except AstroidTypeError as exc:
-        raise UseInferenceDefault("TypeError: " + str(exc))
-    except MroError as exc:
-        raise UseInferenceDefault from exc
-    if isinstance_bool is util.Uninferable:
-        raise UseInferenceDefault
-    return nodes.Const(isinstance_bool)
-
-
-def _class_or_tuple_to_container(node, context=None):
-    # Move inferences results into container
-    # to simplify later logic
-    # raises InferenceError if any of the inferences fall through
-    node_infer = next(node.infer(context=context))
-    # arg2 MUST be a type or a TUPLE of types
-    # for isinstance
-    if isinstance(node_infer, nodes.Tuple):
-        class_container = [
-            next(node.infer(context=context)) for node in node_infer.elts
-        ]
-        class_container = [
-            klass_node for klass_node in class_container if klass_node is not None
-        ]
-    else:
-        class_container = [node_infer]
-    return class_container
-
-
-def infer_len(node, context=None):
-    """Infer length calls
-
-    :param nodes.Call node: len call to infer
-    :param context.InferenceContext: node context
-    :rtype nodes.Const: a Const node with the inferred length, if possible
-    """
-    call = arguments.CallSite.from_call(node)
-    if call.keyword_arguments:
-        raise UseInferenceDefault("TypeError: len() must take no keyword arguments")
-    if len(call.positional_arguments) != 1:
-        raise UseInferenceDefault(
-            "TypeError: len() must take exactly one argument "
-            "({len}) given".format(len=len(call.positional_arguments))
-        )
-    [argument_node] = call.positional_arguments
-    try:
-        return nodes.Const(helpers.object_len(argument_node, context=context))
-    except (AstroidTypeError, InferenceError) as exc:
-        raise UseInferenceDefault(str(exc)) from exc
-
-
-def infer_str(node, context=None):
-    """Infer str() calls
-
-    :param nodes.Call node: str() call to infer
-    :param context.InferenceContext: node context
-    :rtype nodes.Const: a Const containing an empty string
-    """
-    call = arguments.CallSite.from_call(node)
-    if call.keyword_arguments:
-        raise UseInferenceDefault("TypeError: str() must take no keyword arguments")
-    try:
-        return nodes.Const("")
-    except (AstroidTypeError, InferenceError) as exc:
-        raise UseInferenceDefault(str(exc)) from exc
-
-
-def infer_int(node, context=None):
-    """Infer int() calls
-
-    :param nodes.Call node: int() call to infer
-    :param context.InferenceContext: node context
-    :rtype nodes.Const: a Const containing the integer value of the int() call
-    """
-    call = arguments.CallSite.from_call(node)
-    if call.keyword_arguments:
-        raise UseInferenceDefault("TypeError: int() must take no keyword arguments")
-
-    if call.positional_arguments:
-        try:
-            first_value = next(call.positional_arguments[0].infer(context=context))
-        except InferenceError as exc:
-            raise UseInferenceDefault(str(exc)) from exc
-
-        if first_value is util.Uninferable:
-            raise UseInferenceDefault
-
-        if isinstance(first_value, nodes.Const) and isinstance(
-            first_value.value, (int, str)
-        ):
-            try:
-                actual_value = int(first_value.value)
-            except ValueError:
-                return nodes.Const(0)
-            return nodes.Const(actual_value)
-
-    return nodes.Const(0)
-
-
-def infer_dict_fromkeys(node, context=None):
-    """Infer dict.fromkeys
-
-    :param nodes.Call node: dict.fromkeys() call to infer
-    :param context.InferenceContext: node context
-    :rtype nodes.Dict:
-        a Dictionary containing the values that astroid was able to infer.
-        In case the inference failed for any reason, an empty dictionary
-        will be inferred instead.
-    """
-
-    def _build_dict_with_elements(elements):
-        new_node = nodes.Dict(
-            col_offset=node.col_offset, lineno=node.lineno, parent=node.parent
-        )
-        new_node.postinit(elements)
-        return new_node
-
-    call = arguments.CallSite.from_call(node)
-    if call.keyword_arguments:
-        raise UseInferenceDefault("TypeError: int() must take no keyword arguments")
-    if len(call.positional_arguments) not in {1, 2}:
-        raise UseInferenceDefault(
-            "TypeError: Needs between 1 and 2 positional arguments"
-        )
-
-    default = nodes.Const(None)
-    values = call.positional_arguments[0]
-    try:
-        inferred_values = next(values.infer(context=context))
-    except InferenceError:
-        return _build_dict_with_elements([])
-    if inferred_values is util.Uninferable:
-        return _build_dict_with_elements([])
-
-    # Limit to a couple of potential values, as this can become pretty complicated
-    accepted_iterable_elements = (nodes.Const,)
-    if isinstance(inferred_values, (nodes.List, nodes.Set, nodes.Tuple)):
-        elements = inferred_values.elts
-        for element in elements:
-            if not isinstance(element, accepted_iterable_elements):
-                # Fallback to an empty dict
-                return _build_dict_with_elements([])
-
-        elements_with_value = [(element, default) for element in elements]
-        return _build_dict_with_elements(elements_with_value)
-
-    elif isinstance(inferred_values, nodes.Const) and isinstance(
-        inferred_values.value, (str, bytes)
-    ):
-        elements = [
-            (nodes.Const(element), default) for element in inferred_values.value
-        ]
-        return _build_dict_with_elements(elements)
-    elif isinstance(inferred_values, nodes.Dict):
-        keys = inferred_values.itered()
-        for key in keys:
-            if not isinstance(key, accepted_iterable_elements):
-                # Fallback to an empty dict
-                return _build_dict_with_elements([])
-
-        elements_with_value = [(element, default) for element in keys]
-        return _build_dict_with_elements(elements_with_value)
-
-    # Fallback to an empty dictionary
-    return _build_dict_with_elements([])
-
-
-# Builtins inference
-register_builtin_transform(infer_bool, "bool")
-register_builtin_transform(infer_super, "super")
-register_builtin_transform(infer_callable, "callable")
-register_builtin_transform(infer_getattr, "getattr")
-register_builtin_transform(infer_hasattr, "hasattr")
-register_builtin_transform(infer_tuple, "tuple")
-register_builtin_transform(infer_set, "set")
-register_builtin_transform(infer_list, "list")
-register_builtin_transform(infer_dict, "dict")
-register_builtin_transform(infer_frozenset, "frozenset")
-register_builtin_transform(infer_type, "type")
-register_builtin_transform(infer_slice, "slice")
-register_builtin_transform(infer_isinstance, "isinstance")
-register_builtin_transform(infer_issubclass, "issubclass")
-register_builtin_transform(infer_len, "len")
-register_builtin_transform(infer_str, "str")
-register_builtin_transform(infer_int, "int")
-register_builtin_transform(infer_dict_fromkeys, "dict.fromkeys")
-
-
-# Infer object.__new__ calls
-MANAGER.register_transform(
-    nodes.ClassDef,
-    inference_tip(_infer_object__new__decorator),
-    _infer_object__new__decorator_check,
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_collections.py b/venv/Lib/site-packages/astroid/brain/brain_collections.py
deleted file mode 100644
index e5b09ec..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_collections.py
+++ /dev/null
@@ -1,74 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016-2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2018 Ioana Tagirta <ioana.tagirta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import sys
-
-import astroid
-
-
-def _collections_transform():
-    return astroid.parse(
-        """
-    class defaultdict(dict):
-        default_factory = None
-        def __missing__(self, key): pass
-        def __getitem__(self, key): return default_factory
-
-    """
-        + _deque_mock()
-        + _ordered_dict_mock()
-    )
-
-
-def _deque_mock():
-    base_deque_class = """
-    class deque(object):
-        maxlen = 0
-        def __init__(self, iterable=None, maxlen=None):
-            self.iterable = iterable or []
-        def append(self, x): pass
-        def appendleft(self, x): pass
-        def clear(self): pass
-        def count(self, x): return 0
-        def extend(self, iterable): pass
-        def extendleft(self, iterable): pass
-        def pop(self): return self.iterable[0]
-        def popleft(self): return self.iterable[0]
-        def remove(self, value): pass
-        def reverse(self): return reversed(self.iterable)
-        def rotate(self, n=1): return self
-        def __iter__(self): return self
-        def __reversed__(self): return self.iterable[::-1]
-        def __getitem__(self, index): return self.iterable[index]
-        def __setitem__(self, index, value): pass
-        def __delitem__(self, index): pass
-        def __bool__(self): return bool(self.iterable)
-        def __nonzero__(self): return bool(self.iterable)
-        def __contains__(self, o): return o in self.iterable
-        def __len__(self): return len(self.iterable)
-        def __copy__(self): return deque(self.iterable)
-        def copy(self): return deque(self.iterable)
-        def index(self, x, start=0, end=0): return 0
-        def insert(self, x, i): pass
-        def __add__(self, other): pass
-        def __iadd__(self, other): pass
-        def __mul__(self, other): pass
-        def __imul__(self, other): pass
-        def __rmul__(self, other): pass"""
-    return base_deque_class
-
-
-def _ordered_dict_mock():
-    base_ordered_dict_class = """
-    class OrderedDict(dict):
-        def __reversed__(self): return self[::-1]
-        def move_to_end(self, key, last=False): pass"""
-    return base_ordered_dict_class
-
-
-astroid.register_module_extender(astroid.MANAGER, "collections", _collections_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_crypt.py b/venv/Lib/site-packages/astroid/brain/brain_crypt.py
deleted file mode 100644
index 491ee23..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_crypt.py
+++ /dev/null
@@ -1,26 +0,0 @@
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import sys
-import astroid
-
-PY37 = sys.version_info >= (3, 7)
-
-if PY37:
-    # Since Python 3.7 Hashing Methods are added
-    # dynamically to globals()
-
-    def _re_transform():
-        return astroid.parse(
-            """
-        from collections import namedtuple
-        _Method = namedtuple('_Method', 'name ident salt_chars total_size')
-
-        METHOD_SHA512 = _Method('SHA512', '6', 16, 106)
-        METHOD_SHA256 = _Method('SHA256', '5', 16, 63)
-        METHOD_BLOWFISH = _Method('BLOWFISH', 2, 'b', 22)
-        METHOD_MD5 = _Method('MD5', '1', 8, 34)
-        METHOD_CRYPT = _Method('CRYPT', None, 2, 13)
-        """
-        )
-
-    astroid.register_module_extender(astroid.MANAGER, "crypt", _re_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_curses.py b/venv/Lib/site-packages/astroid/brain/brain_curses.py
deleted file mode 100644
index 68e88b9..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_curses.py
+++ /dev/null
@@ -1,179 +0,0 @@
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import astroid
-
-
-def _curses_transform():
-    return astroid.parse(
-        """
-    A_ALTCHARSET = 1
-    A_BLINK = 1
-    A_BOLD = 1
-    A_DIM = 1
-    A_INVIS = 1
-    A_ITALIC = 1
-    A_NORMAL = 1
-    A_PROTECT = 1
-    A_REVERSE = 1
-    A_STANDOUT = 1
-    A_UNDERLINE = 1
-    A_HORIZONTAL = 1
-    A_LEFT = 1
-    A_LOW = 1
-    A_RIGHT = 1
-    A_TOP = 1
-    A_VERTICAL = 1
-    A_CHARTEXT = 1
-    A_ATTRIBUTES = 1
-    A_CHARTEXT = 1
-    A_COLOR = 1
-    KEY_MIN = 1
-    KEY_BREAK = 1
-    KEY_DOWN = 1
-    KEY_UP = 1
-    KEY_LEFT = 1
-    KEY_RIGHT = 1
-    KEY_HOME = 1
-    KEY_BACKSPACE = 1
-    KEY_F0 = 1
-    KEY_Fn = 1
-    KEY_DL = 1
-    KEY_IL = 1
-    KEY_DC = 1
-    KEY_IC = 1
-    KEY_EIC = 1
-    KEY_CLEAR = 1
-    KEY_EOS = 1
-    KEY_EOL = 1
-    KEY_SF = 1
-    KEY_SR = 1
-    KEY_NPAGE = 1
-    KEY_PPAGE = 1
-    KEY_STAB = 1
-    KEY_CTAB = 1
-    KEY_CATAB = 1
-    KEY_ENTER = 1
-    KEY_SRESET = 1
-    KEY_RESET = 1
-    KEY_PRINT = 1
-    KEY_LL = 1
-    KEY_A1 = 1
-    KEY_A3 = 1
-    KEY_B2 = 1
-    KEY_C1 = 1
-    KEY_C3 = 1
-    KEY_BTAB = 1
-    KEY_BEG = 1
-    KEY_CANCEL = 1
-    KEY_CLOSE = 1
-    KEY_COMMAND = 1
-    KEY_COPY = 1
-    KEY_CREATE = 1
-    KEY_END = 1
-    KEY_EXIT = 1
-    KEY_FIND = 1
-    KEY_HELP = 1
-    KEY_MARK = 1
-    KEY_MESSAGE = 1
-    KEY_MOVE = 1
-    KEY_NEXT = 1
-    KEY_OPEN = 1
-    KEY_OPTIONS = 1
-    KEY_PREVIOUS = 1
-    KEY_REDO = 1
-    KEY_REFERENCE = 1
-    KEY_REFRESH = 1
-    KEY_REPLACE = 1
-    KEY_RESTART = 1
-    KEY_RESUME = 1
-    KEY_SAVE = 1
-    KEY_SBEG = 1
-    KEY_SCANCEL = 1
-    KEY_SCOMMAND = 1
-    KEY_SCOPY = 1
-    KEY_SCREATE = 1
-    KEY_SDC = 1
-    KEY_SDL = 1
-    KEY_SELECT = 1
-    KEY_SEND = 1
-    KEY_SEOL = 1
-    KEY_SEXIT = 1
-    KEY_SFIND = 1
-    KEY_SHELP = 1
-    KEY_SHOME = 1
-    KEY_SIC = 1
-    KEY_SLEFT = 1
-    KEY_SMESSAGE = 1
-    KEY_SMOVE = 1
-    KEY_SNEXT = 1
-    KEY_SOPTIONS = 1
-    KEY_SPREVIOUS = 1
-    KEY_SPRINT = 1
-    KEY_SREDO = 1
-    KEY_SREPLACE = 1
-    KEY_SRIGHT = 1
-    KEY_SRSUME = 1
-    KEY_SSAVE = 1
-    KEY_SSUSPEND = 1
-    KEY_SUNDO = 1
-    KEY_SUSPEND = 1
-    KEY_UNDO = 1
-    KEY_MOUSE = 1
-    KEY_RESIZE = 1
-    KEY_MAX = 1
-    ACS_BBSS = 1
-    ACS_BLOCK = 1
-    ACS_BOARD = 1
-    ACS_BSBS = 1
-    ACS_BSSB = 1
-    ACS_BSSS = 1
-    ACS_BTEE = 1
-    ACS_BULLET = 1
-    ACS_CKBOARD = 1
-    ACS_DARROW = 1
-    ACS_DEGREE = 1
-    ACS_DIAMOND = 1
-    ACS_GEQUAL = 1
-    ACS_HLINE = 1
-    ACS_LANTERN = 1
-    ACS_LARROW = 1
-    ACS_LEQUAL = 1
-    ACS_LLCORNER = 1
-    ACS_LRCORNER = 1
-    ACS_LTEE = 1
-    ACS_NEQUAL = 1
-    ACS_PI = 1
-    ACS_PLMINUS = 1
-    ACS_PLUS = 1
-    ACS_RARROW = 1
-    ACS_RTEE = 1
-    ACS_S1 = 1
-    ACS_S3 = 1
-    ACS_S7 = 1
-    ACS_S9 = 1
-    ACS_SBBS = 1
-    ACS_SBSB = 1
-    ACS_SBSS = 1
-    ACS_SSBB = 1
-    ACS_SSBS = 1
-    ACS_SSSB = 1
-    ACS_SSSS = 1
-    ACS_STERLING = 1
-    ACS_TTEE = 1
-    ACS_UARROW = 1
-    ACS_ULCORNER = 1
-    ACS_URCORNER = 1
-    ACS_VLINE = 1
-    COLOR_BLACK = 1
-    COLOR_BLUE = 1
-    COLOR_CYAN = 1
-    COLOR_GREEN = 1
-    COLOR_MAGENTA = 1
-    COLOR_RED = 1
-    COLOR_WHITE = 1
-    COLOR_YELLOW = 1
-        """
-    )
-
-
-astroid.register_module_extender(astroid.MANAGER, "curses", _curses_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_dataclasses.py b/venv/Lib/site-packages/astroid/brain/brain_dataclasses.py
deleted file mode 100644
index 7a25e0c..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_dataclasses.py
+++ /dev/null
@@ -1,50 +0,0 @@
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-"""
-Astroid hook for the dataclasses library
-"""
-
-import astroid
-from astroid import MANAGER
-
-
-DATACLASSES_DECORATORS = frozenset(("dataclasses.dataclass", "dataclass"))
-
-
-def is_decorated_with_dataclass(node, decorator_names=DATACLASSES_DECORATORS):
-    """Return True if a decorated node has a `dataclass` decorator applied."""
-    if not node.decorators:
-        return False
-    for decorator_attribute in node.decorators.nodes:
-        if isinstance(decorator_attribute, astroid.Call):  # decorator with arguments
-            decorator_attribute = decorator_attribute.func
-        if decorator_attribute.as_string() in decorator_names:
-            return True
-    return False
-
-
-def dataclass_transform(node):
-    """Rewrite a dataclass to be easily understood by pylint"""
-
-    for assign_node in node.body:
-        if not isinstance(assign_node, (astroid.AnnAssign, astroid.Assign)):
-            continue
-
-        targets = (
-            assign_node.targets
-            if hasattr(assign_node, "targets")
-            else [assign_node.target]
-        )
-        for target in targets:
-            rhs_node = astroid.Unknown(
-                lineno=assign_node.lineno,
-                col_offset=assign_node.col_offset,
-                parent=assign_node,
-            )
-            node.instance_attrs[target.name] = [rhs_node]
-            node.locals[target.name] = [rhs_node]
-
-
-MANAGER.register_transform(
-    astroid.ClassDef, dataclass_transform, is_decorated_with_dataclass
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_dateutil.py b/venv/Lib/site-packages/astroid/brain/brain_dateutil.py
deleted file mode 100644
index a1c270f..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_dateutil.py
+++ /dev/null
@@ -1,28 +0,0 @@
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 raylu <lurayl@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for dateutil"""
-
-import textwrap
-
-from astroid import MANAGER, register_module_extender
-from astroid.builder import AstroidBuilder
-
-
-def dateutil_transform():
-    return AstroidBuilder(MANAGER).string_build(
-        textwrap.dedent(
-            """
-    import datetime
-    def parse(timestr, parserinfo=None, **kwargs):
-        return datetime.datetime()
-    """
-        )
-    )
-
-
-register_module_extender(MANAGER, "dateutil.parser", dateutil_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_fstrings.py b/venv/Lib/site-packages/astroid/brain/brain_fstrings.py
deleted file mode 100644
index 7d8c7b6..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_fstrings.py
+++ /dev/null
@@ -1,51 +0,0 @@
-# Copyright (c) 2017 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import collections
-import sys
-
-import astroid
-
-
-def _clone_node_with_lineno(node, parent, lineno):
-    cls = node.__class__
-    other_fields = node._other_fields
-    _astroid_fields = node._astroid_fields
-    init_params = {"lineno": lineno, "col_offset": node.col_offset, "parent": parent}
-    postinit_params = {param: getattr(node, param) for param in _astroid_fields}
-    if other_fields:
-        init_params.update({param: getattr(node, param) for param in other_fields})
-    new_node = cls(**init_params)
-    if hasattr(node, "postinit") and _astroid_fields:
-        for param, child in postinit_params.items():
-            if child and not isinstance(child, collections.Sequence):
-                cloned_child = _clone_node_with_lineno(
-                    node=child, lineno=new_node.lineno, parent=new_node
-                )
-                postinit_params[param] = cloned_child
-        new_node.postinit(**postinit_params)
-    return new_node
-
-
-def _transform_formatted_value(node):
-    if node.value and node.value.lineno == 1:
-        if node.lineno != node.value.lineno:
-            new_node = astroid.FormattedValue(
-                lineno=node.lineno, col_offset=node.col_offset, parent=node.parent
-            )
-            new_value = _clone_node_with_lineno(
-                node=node.value, lineno=node.lineno, parent=new_node
-            )
-            new_node.postinit(value=new_value, format_spec=node.format_spec)
-            return new_node
-
-
-if sys.version_info[:2] >= (3, 6):
-    # TODO: this fix tries to *patch* http://bugs.python.org/issue29051
-    # The problem is that FormattedValue.value, which is a Name node,
-    # has wrong line numbers, usually 1. This creates problems for pylint,
-    # which expects correct line numbers for things such as message control.
-    astroid.MANAGER.register_transform(
-        astroid.FormattedValue, _transform_formatted_value
-    )
diff --git a/venv/Lib/site-packages/astroid/brain/brain_functools.py b/venv/Lib/site-packages/astroid/brain/brain_functools.py
deleted file mode 100644
index 8b594ef..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_functools.py
+++ /dev/null
@@ -1,158 +0,0 @@
-# Copyright (c) 2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-"""Astroid hooks for understanding functools library module."""
-from functools import partial
-from itertools import chain
-
-import astroid
-from astroid import arguments
-from astroid import BoundMethod
-from astroid import extract_node
-from astroid import helpers
-from astroid.interpreter import objectmodel
-from astroid import MANAGER
-from astroid import objects
-
-
-LRU_CACHE = "functools.lru_cache"
-
-
-class LruWrappedModel(objectmodel.FunctionModel):
-    """Special attribute model for functions decorated with functools.lru_cache.
-
-    The said decorators patches at decoration time some functions onto
-    the decorated function.
-    """
-
-    @property
-    def attr___wrapped__(self):
-        return self._instance
-
-    @property
-    def attr_cache_info(self):
-        cache_info = extract_node(
-            """
-        from functools import _CacheInfo
-        _CacheInfo(0, 0, 0, 0)
-        """
-        )
-
-        class CacheInfoBoundMethod(BoundMethod):
-            def infer_call_result(self, caller, context=None):
-                yield helpers.safe_infer(cache_info)
-
-        return CacheInfoBoundMethod(proxy=self._instance, bound=self._instance)
-
-    @property
-    def attr_cache_clear(self):
-        node = extract_node("""def cache_clear(self): pass""")
-        return BoundMethod(proxy=node, bound=self._instance.parent.scope())
-
-
-def _transform_lru_cache(node, context=None):
-    # TODO: this is not ideal, since the node should be immutable,
-    # but due to https://github.com/PyCQA/astroid/issues/354,
-    # there's not much we can do now.
-    # Replacing the node would work partially, because,
-    # in pylint, the old node would still be available, leading
-    # to spurious false positives.
-    node.special_attributes = LruWrappedModel()(node)
-    return
-
-
-def _functools_partial_inference(node, context=None):
-    call = arguments.CallSite.from_call(node)
-    number_of_positional = len(call.positional_arguments)
-    if number_of_positional < 1:
-        raise astroid.UseInferenceDefault(
-            "functools.partial takes at least one argument"
-        )
-    if number_of_positional == 1 and not call.keyword_arguments:
-        raise astroid.UseInferenceDefault(
-            "functools.partial needs at least to have some filled arguments"
-        )
-
-    partial_function = call.positional_arguments[0]
-    try:
-        inferred_wrapped_function = next(partial_function.infer(context=context))
-    except astroid.InferenceError as exc:
-        raise astroid.UseInferenceDefault from exc
-    if inferred_wrapped_function is astroid.Uninferable:
-        raise astroid.UseInferenceDefault("Cannot infer the wrapped function")
-    if not isinstance(inferred_wrapped_function, astroid.FunctionDef):
-        raise astroid.UseInferenceDefault("The wrapped function is not a function")
-
-    # Determine if the passed keywords into the callsite are supported
-    # by the wrapped function.
-    function_parameters = chain(
-        inferred_wrapped_function.args.args or (),
-        inferred_wrapped_function.args.posonlyargs or (),
-        inferred_wrapped_function.args.kwonlyargs or (),
-    )
-    parameter_names = set(
-        param.name
-        for param in function_parameters
-        if isinstance(param, astroid.AssignName)
-    )
-    if set(call.keyword_arguments) - parameter_names:
-        raise astroid.UseInferenceDefault(
-            "wrapped function received unknown parameters"
-        )
-
-    partial_function = objects.PartialFunction(
-        call,
-        name=inferred_wrapped_function.name,
-        doc=inferred_wrapped_function.doc,
-        lineno=inferred_wrapped_function.lineno,
-        col_offset=inferred_wrapped_function.col_offset,
-        parent=inferred_wrapped_function.parent,
-    )
-    partial_function.postinit(
-        args=inferred_wrapped_function.args,
-        body=inferred_wrapped_function.body,
-        decorators=inferred_wrapped_function.decorators,
-        returns=inferred_wrapped_function.returns,
-        type_comment_returns=inferred_wrapped_function.type_comment_returns,
-        type_comment_args=inferred_wrapped_function.type_comment_args,
-    )
-    return iter((partial_function,))
-
-
-def _looks_like_lru_cache(node):
-    """Check if the given function node is decorated with lru_cache."""
-    if not node.decorators:
-        return False
-    for decorator in node.decorators.nodes:
-        if not isinstance(decorator, astroid.Call):
-            continue
-        if _looks_like_functools_member(decorator, "lru_cache"):
-            return True
-    return False
-
-
-def _looks_like_functools_member(node, member):
-    """Check if the given Call node is a functools.partial call"""
-    if isinstance(node.func, astroid.Name):
-        return node.func.name == member
-    elif isinstance(node.func, astroid.Attribute):
-        return (
-            node.func.attrname == member
-            and isinstance(node.func.expr, astroid.Name)
-            and node.func.expr.name == "functools"
-        )
-
-
-_looks_like_partial = partial(_looks_like_functools_member, member="partial")
-
-
-MANAGER.register_transform(
-    astroid.FunctionDef, _transform_lru_cache, _looks_like_lru_cache
-)
-
-
-MANAGER.register_transform(
-    astroid.Call,
-    astroid.inference_tip(_functools_partial_inference),
-    _looks_like_partial,
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_gi.py b/venv/Lib/site-packages/astroid/brain/brain_gi.py
deleted file mode 100644
index 0970610..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_gi.py
+++ /dev/null
@@ -1,220 +0,0 @@
-# Copyright (c) 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2014 Cole Robinson <crobinso@redhat.com>
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 David Shea <dshea@redhat.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016 Giuseppe Scrivano <gscrivan@redhat.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for the Python 2 GObject introspection bindings.
-
-Helps with understanding everything imported from 'gi.repository'
-"""
-
-import inspect
-import itertools
-import sys
-import re
-import warnings
-
-from astroid import MANAGER, AstroidBuildingError, nodes
-from astroid.builder import AstroidBuilder
-
-
-_inspected_modules = {}
-
-_identifier_re = r"^[A-Za-z_]\w*$"
-
-
-def _gi_build_stub(parent):
-    """
-    Inspect the passed module recursively and build stubs for functions,
-    classes, etc.
-    """
-    classes = {}
-    functions = {}
-    constants = {}
-    methods = {}
-    for name in dir(parent):
-        if name.startswith("__"):
-            continue
-
-        # Check if this is a valid name in python
-        if not re.match(_identifier_re, name):
-            continue
-
-        try:
-            obj = getattr(parent, name)
-        except:
-            continue
-
-        if inspect.isclass(obj):
-            classes[name] = obj
-        elif inspect.isfunction(obj) or inspect.isbuiltin(obj):
-            functions[name] = obj
-        elif inspect.ismethod(obj) or inspect.ismethoddescriptor(obj):
-            methods[name] = obj
-        elif (
-            str(obj).startswith("<flags")
-            or str(obj).startswith("<enum ")
-            or str(obj).startswith("<GType ")
-            or inspect.isdatadescriptor(obj)
-        ):
-            constants[name] = 0
-        elif isinstance(obj, (int, str)):
-            constants[name] = obj
-        elif callable(obj):
-            # Fall back to a function for anything callable
-            functions[name] = obj
-        else:
-            # Assume everything else is some manner of constant
-            constants[name] = 0
-
-    ret = ""
-
-    if constants:
-        ret += "# %s constants\n\n" % parent.__name__
-    for name in sorted(constants):
-        if name[0].isdigit():
-            # GDK has some busted constant names like
-            # Gdk.EventType.2BUTTON_PRESS
-            continue
-
-        val = constants[name]
-
-        strval = str(val)
-        if isinstance(val, str):
-            strval = '"%s"' % str(val).replace("\\", "\\\\")
-        ret += "%s = %s\n" % (name, strval)
-
-    if ret:
-        ret += "\n\n"
-    if functions:
-        ret += "# %s functions\n\n" % parent.__name__
-    for name in sorted(functions):
-        ret += "def %s(*args, **kwargs):\n" % name
-        ret += "    pass\n"
-
-    if ret:
-        ret += "\n\n"
-    if methods:
-        ret += "# %s methods\n\n" % parent.__name__
-    for name in sorted(methods):
-        ret += "def %s(self, *args, **kwargs):\n" % name
-        ret += "    pass\n"
-
-    if ret:
-        ret += "\n\n"
-    if classes:
-        ret += "# %s classes\n\n" % parent.__name__
-    for name, obj in sorted(classes.items()):
-        base = "object"
-        if issubclass(obj, Exception):
-            base = "Exception"
-        ret += "class %s(%s):\n" % (name, base)
-
-        classret = _gi_build_stub(obj)
-        if not classret:
-            classret = "pass\n"
-
-        for line in classret.splitlines():
-            ret += "    " + line + "\n"
-        ret += "\n"
-
-    return ret
-
-
-def _import_gi_module(modname):
-    # we only consider gi.repository submodules
-    if not modname.startswith("gi.repository."):
-        raise AstroidBuildingError(modname=modname)
-    # build astroid representation unless we already tried so
-    if modname not in _inspected_modules:
-        modnames = [modname]
-        optional_modnames = []
-
-        # GLib and GObject may have some special case handling
-        # in pygobject that we need to cope with. However at
-        # least as of pygobject3-3.13.91 the _glib module doesn't
-        # exist anymore, so if treat these modules as optional.
-        if modname == "gi.repository.GLib":
-            optional_modnames.append("gi._glib")
-        elif modname == "gi.repository.GObject":
-            optional_modnames.append("gi._gobject")
-
-        try:
-            modcode = ""
-            for m in itertools.chain(modnames, optional_modnames):
-                try:
-                    with warnings.catch_warnings():
-                        # Just inspecting the code can raise gi deprecation
-                        # warnings, so ignore them.
-                        try:
-                            from gi import PyGIDeprecationWarning, PyGIWarning
-
-                            warnings.simplefilter("ignore", PyGIDeprecationWarning)
-                            warnings.simplefilter("ignore", PyGIWarning)
-                        except Exception:
-                            pass
-
-                        __import__(m)
-                        modcode += _gi_build_stub(sys.modules[m])
-                except ImportError:
-                    if m not in optional_modnames:
-                        raise
-        except ImportError:
-            astng = _inspected_modules[modname] = None
-        else:
-            astng = AstroidBuilder(MANAGER).string_build(modcode, modname)
-            _inspected_modules[modname] = astng
-    else:
-        astng = _inspected_modules[modname]
-    if astng is None:
-        raise AstroidBuildingError(modname=modname)
-    return astng
-
-
-def _looks_like_require_version(node):
-    # Return whether this looks like a call to gi.require_version(<name>, <version>)
-    # Only accept function calls with two constant arguments
-    if len(node.args) != 2:
-        return False
-
-    if not all(isinstance(arg, nodes.Const) for arg in node.args):
-        return False
-
-    func = node.func
-    if isinstance(func, nodes.Attribute):
-        if func.attrname != "require_version":
-            return False
-        if isinstance(func.expr, nodes.Name) and func.expr.name == "gi":
-            return True
-
-        return False
-
-    if isinstance(func, nodes.Name):
-        return func.name == "require_version"
-
-    return False
-
-
-def _register_require_version(node):
-    # Load the gi.require_version locally
-    try:
-        import gi
-
-        gi.require_version(node.args[0].value, node.args[1].value)
-    except Exception:
-        pass
-
-    return node
-
-
-MANAGER.register_failed_import_hook(_import_gi_module)
-MANAGER.register_transform(
-    nodes.Call, _register_require_version, _looks_like_require_version
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_hashlib.py b/venv/Lib/site-packages/astroid/brain/brain_hashlib.py
deleted file mode 100644
index 98ae774..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_hashlib.py
+++ /dev/null
@@ -1,67 +0,0 @@
-# Copyright (c) 2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2018 Ioana Tagirta <ioana.tagirta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import sys
-
-import six
-
-import astroid
-
-PY36 = sys.version_info >= (3, 6)
-
-
-def _hashlib_transform():
-    signature = "value=''"
-    template = """
-    class %(name)s(object):
-      def __init__(self, %(signature)s): pass
-      def digest(self):
-        return %(digest)s
-      def copy(self):
-        return self
-      def update(self, value): pass
-      def hexdigest(self):
-        return ''
-      @property
-      def name(self):
-        return %(name)r
-      @property
-      def block_size(self):
-        return 1
-      @property
-      def digest_size(self):
-        return 1
-    """
-    algorithms_with_signature = dict.fromkeys(
-        ["md5", "sha1", "sha224", "sha256", "sha384", "sha512"], signature
-    )
-    if PY36:
-        blake2b_signature = "data=b'', *, digest_size=64, key=b'', salt=b'', \
-                person=b'', fanout=1, depth=1, leaf_size=0, node_offset=0, \
-                node_depth=0, inner_size=0, last_node=False"
-        blake2s_signature = "data=b'', *, digest_size=32, key=b'', salt=b'', \
-                person=b'', fanout=1, depth=1, leaf_size=0, node_offset=0, \
-                node_depth=0, inner_size=0, last_node=False"
-        new_algorithms = dict.fromkeys(
-            ["sha3_224", "sha3_256", "sha3_384", "sha3_512", "shake_128", "shake_256"],
-            signature,
-        )
-        algorithms_with_signature.update(new_algorithms)
-        algorithms_with_signature.update(
-            {"blake2b": blake2b_signature, "blake2s": blake2s_signature}
-        )
-    classes = "".join(
-        template
-        % {
-            "name": hashfunc,
-            "digest": 'b""' if six.PY3 else '""',
-            "signature": signature,
-        }
-        for hashfunc, signature in algorithms_with_signature.items()
-    )
-    return astroid.parse(classes)
-
-
-astroid.register_module_extender(astroid.MANAGER, "hashlib", _hashlib_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_http.py b/venv/Lib/site-packages/astroid/brain/brain_http.py
deleted file mode 100644
index a3aa814..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_http.py
+++ /dev/null
@@ -1,201 +0,0 @@
-# Copyright (c) 2018 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid brain hints for some of the `http` module."""
-import textwrap
-
-import astroid
-from astroid.builder import AstroidBuilder
-
-
-def _http_transform():
-    code = textwrap.dedent(
-        """
-    from collections import namedtuple
-    _HTTPStatus = namedtuple('_HTTPStatus', 'value phrase description')
-
-    class HTTPStatus:
-
-        # informational
-        CONTINUE = _HTTPStatus(100, 'Continue', 'Request received, please continue')
-        SWITCHING_PROTOCOLS = _HTTPStatus(101, 'Switching Protocols',
-                'Switching to new protocol; obey Upgrade header')
-        PROCESSING = _HTTPStatus(102, 'Processing', '')
-        OK = _HTTPStatus(200, 'OK', 'Request fulfilled, document follows')
-        CREATED = _HTTPStatus(201, 'Created', 'Document created, URL follows')
-        ACCEPTED = _HTTPStatus(202, 'Accepted',
-            'Request accepted, processing continues off-line')
-        NON_AUTHORITATIVE_INFORMATION = _HTTPStatus(203,
-            'Non-Authoritative Information', 'Request fulfilled from cache')
-        NO_CONTENT = _HTTPStatus(204, 'No Content', 'Request fulfilled, nothing follows')
-        RESET_CONTENT =_HTTPStatus(205, 'Reset Content', 'Clear input form for further input')
-        PARTIAL_CONTENT = _HTTPStatus(206, 'Partial Content', 'Partial content follows')
-        MULTI_STATUS = _HTTPStatus(207, 'Multi-Status', '')
-        ALREADY_REPORTED = _HTTPStatus(208, 'Already Reported', '')
-        IM_USED = _HTTPStatus(226, 'IM Used', '')
-        MULTIPLE_CHOICES = _HTTPStatus(300, 'Multiple Choices',
-            'Object has several resources -- see URI list')
-        MOVED_PERMANENTLY = _HTTPStatus(301, 'Moved Permanently',
-            'Object moved permanently -- see URI list')
-        FOUND = _HTTPStatus(302, 'Found', 'Object moved temporarily -- see URI list')
-        SEE_OTHER = _HTTPStatus(303, 'See Other', 'Object moved -- see Method and URL list')
-        NOT_MODIFIED = _HTTPStatus(304, 'Not Modified',
-            'Document has not changed since given time')
-        USE_PROXY = _HTTPStatus(305, 'Use Proxy',
-            'You must use proxy specified in Location to access this resource')
-        TEMPORARY_REDIRECT = _HTTPStatus(307, 'Temporary Redirect',
-            'Object moved temporarily -- see URI list')
-        PERMANENT_REDIRECT = _HTTPStatus(308, 'Permanent Redirect',
-            'Object moved permanently -- see URI list')
-        BAD_REQUEST = _HTTPStatus(400, 'Bad Request',
-            'Bad request syntax or unsupported method')
-        UNAUTHORIZED = _HTTPStatus(401, 'Unauthorized',
-            'No permission -- see authorization schemes')
-        PAYMENT_REQUIRED = _HTTPStatus(402, 'Payment Required',
-            'No payment -- see charging schemes')
-        FORBIDDEN = _HTTPStatus(403, 'Forbidden',
-            'Request forbidden -- authorization will not help')
-        NOT_FOUND = _HTTPStatus(404, 'Not Found',
-            'Nothing matches the given URI')
-        METHOD_NOT_ALLOWED = _HTTPStatus(405, 'Method Not Allowed',
-            'Specified method is invalid for this resource')
-        NOT_ACCEPTABLE = _HTTPStatus(406, 'Not Acceptable',
-            'URI not available in preferred format')
-        PROXY_AUTHENTICATION_REQUIRED = _HTTPStatus(407,
-            'Proxy Authentication Required',
-            'You must authenticate with this proxy before proceeding')
-        REQUEST_TIMEOUT = _HTTPStatus(408, 'Request Timeout',
-            'Request timed out; try again later')
-        CONFLICT = _HTTPStatus(409, 'Conflict', 'Request conflict')
-        GONE = _HTTPStatus(410, 'Gone',
-            'URI no longer exists and has been permanently removed')
-        LENGTH_REQUIRED = _HTTPStatus(411, 'Length Required',
-            'Client must specify Content-Length')
-        PRECONDITION_FAILED = _HTTPStatus(412, 'Precondition Failed',
-            'Precondition in headers is false')
-        REQUEST_ENTITY_TOO_LARGE = _HTTPStatus(413, 'Request Entity Too Large',
-            'Entity is too large')
-        REQUEST_URI_TOO_LONG = _HTTPStatus(414, 'Request-URI Too Long',
-            'URI is too long')
-        UNSUPPORTED_MEDIA_TYPE = _HTTPStatus(415, 'Unsupported Media Type',
-            'Entity body in unsupported format')
-        REQUESTED_RANGE_NOT_SATISFIABLE = _HTTPStatus(416,
-            'Requested Range Not Satisfiable',
-            'Cannot satisfy request range')
-        EXPECTATION_FAILED = _HTTPStatus(417, 'Expectation Failed',
-            'Expect condition could not be satisfied')
-        MISDIRECTED_REQUEST = _HTTPStatus(421, 'Misdirected Request',
-            'Server is not able to produce a response')
-        UNPROCESSABLE_ENTITY = _HTTPStatus(422, 'Unprocessable Entity')
-        LOCKED = _HTTPStatus(423, 'Locked')
-        FAILED_DEPENDENCY = _HTTPStatus(424, 'Failed Dependency')
-        UPGRADE_REQUIRED = _HTTPStatus(426, 'Upgrade Required')
-        PRECONDITION_REQUIRED = _HTTPStatus(428, 'Precondition Required',
-            'The origin server requires the request to be conditional')
-        TOO_MANY_REQUESTS = _HTTPStatus(429, 'Too Many Requests',
-            'The user has sent too many requests in '
-            'a given amount of time ("rate limiting")')
-        REQUEST_HEADER_FIELDS_TOO_LARGE = _HTTPStatus(431,
-            'Request Header Fields Too Large',
-            'The server is unwilling to process the request because its header '
-            'fields are too large')
-        UNAVAILABLE_FOR_LEGAL_REASONS = _HTTPStatus(451,
-            'Unavailable For Legal Reasons',
-            'The server is denying access to the '
-            'resource as a consequence of a legal demand')
-        INTERNAL_SERVER_ERROR = _HTTPStatus(500, 'Internal Server Error',
-            'Server got itself in trouble')
-        NOT_IMPLEMENTED = _HTTPStatus(501, 'Not Implemented',
-            'Server does not support this operation')
-        BAD_GATEWAY = _HTTPStatus(502, 'Bad Gateway',
-            'Invalid responses from another server/proxy')
-        SERVICE_UNAVAILABLE = _HTTPStatus(503, 'Service Unavailable',
-            'The server cannot process the request due to a high load')
-        GATEWAY_TIMEOUT = _HTTPStatus(504, 'Gateway Timeout',
-            'The gateway server did not receive a timely response')
-        HTTP_VERSION_NOT_SUPPORTED = _HTTPStatus(505, 'HTTP Version Not Supported',
-            'Cannot fulfill request')
-        VARIANT_ALSO_NEGOTIATES = _HTTPStatus(506, 'Variant Also Negotiates')
-        INSUFFICIENT_STORAGE = _HTTPStatus(507, 'Insufficient Storage')
-        LOOP_DETECTED = _HTTPStatus(508, 'Loop Detected')
-        NOT_EXTENDED = _HTTPStatus(510, 'Not Extended')
-        NETWORK_AUTHENTICATION_REQUIRED = _HTTPStatus(511,
-            'Network Authentication Required',
-            'The client needs to authenticate to gain network access')
-    """
-    )
-    return AstroidBuilder(astroid.MANAGER).string_build(code)
-
-
-def _http_client_transform():
-    return AstroidBuilder(astroid.MANAGER).string_build(
-        textwrap.dedent(
-            """
-    from http import HTTPStatus
-
-    CONTINUE = HTTPStatus.CONTINUE
-    SWITCHING_PROTOCOLS = HTTPStatus.SWITCHING_PROTOCOLS
-    PROCESSING = HTTPStatus.PROCESSING
-    OK = HTTPStatus.OK
-    CREATED = HTTPStatus.CREATED
-    ACCEPTED = HTTPStatus.ACCEPTED
-    NON_AUTHORITATIVE_INFORMATION = HTTPStatus.NON_AUTHORITATIVE_INFORMATION
-    NO_CONTENT = HTTPStatus.NO_CONTENT
-    RESET_CONTENT = HTTPStatus.RESET_CONTENT
-    PARTIAL_CONTENT = HTTPStatus.PARTIAL_CONTENT
-    MULTI_STATUS = HTTPStatus.MULTI_STATUS
-    ALREADY_REPORTED = HTTPStatus.ALREADY_REPORTED
-    IM_USED = HTTPStatus.IM_USED
-    MULTIPLE_CHOICES = HTTPStatus.MULTIPLE_CHOICES
-    MOVED_PERMANENTLY = HTTPStatus.MOVED_PERMANENTLY
-    FOUND = HTTPStatus.FOUND
-    SEE_OTHER = HTTPStatus.SEE_OTHER
-    NOT_MODIFIED = HTTPStatus.NOT_MODIFIED
-    USE_PROXY = HTTPStatus.USE_PROXY
-    TEMPORARY_REDIRECT = HTTPStatus.TEMPORARY_REDIRECT
-    PERMANENT_REDIRECT = HTTPStatus.PERMANENT_REDIRECT
-    BAD_REQUEST = HTTPStatus.BAD_REQUEST
-    UNAUTHORIZED = HTTPStatus.UNAUTHORIZED
-    PAYMENT_REQUIRED = HTTPStatus.PAYMENT_REQUIRED
-    FORBIDDEN = HTTPStatus.FORBIDDEN
-    NOT_FOUND = HTTPStatus.NOT_FOUND
-    METHOD_NOT_ALLOWED = HTTPStatus.METHOD_NOT_ALLOWED
-    NOT_ACCEPTABLE = HTTPStatus.NOT_ACCEPTABLE
-    PROXY_AUTHENTICATION_REQUIRED = HTTPStatus.PROXY_AUTHENTICATION_REQUIRED
-    REQUEST_TIMEOUT = HTTPStatus.REQUEST_TIMEOUT
-    CONFLICT = HTTPStatus.CONFLICT
-    GONE = HTTPStatus.GONE
-    LENGTH_REQUIRED = HTTPStatus.LENGTH_REQUIRED
-    PRECONDITION_FAILED = HTTPStatus.PRECONDITION_FAILED
-    REQUEST_ENTITY_TOO_LARGE = HTTPStatus.REQUEST_ENTITY_TOO_LARGE
-    REQUEST_URI_TOO_LONG = HTTPStatus.REQUEST_URI_TOO_LONG
-    UNSUPPORTED_MEDIA_TYPE = HTTPStatus.UNSUPPORTED_MEDIA_TYPE
-    REQUESTED_RANGE_NOT_SATISFIABLE = HTTPStatus.REQUESTED_RANGE_NOT_SATISFIABLE
-    EXPECTATION_FAILED = HTTPStatus.EXPECTATION_FAILED
-    UNPROCESSABLE_ENTITY = HTTPStatus.UNPROCESSABLE_ENTITY
-    LOCKED = HTTPStatus.LOCKED
-    FAILED_DEPENDENCY = HTTPStatus.FAILED_DEPENDENCY
-    UPGRADE_REQUIRED = HTTPStatus.UPGRADE_REQUIRED
-    PRECONDITION_REQUIRED = HTTPStatus.PRECONDITION_REQUIRED
-    TOO_MANY_REQUESTS = HTTPStatus.TOO_MANY_REQUESTS
-    REQUEST_HEADER_FIELDS_TOO_LARGE = HTTPStatus.REQUEST_HEADER_FIELDS_TOO_LARGE
-    INTERNAL_SERVER_ERROR = HTTPStatus.INTERNAL_SERVER_ERROR
-    NOT_IMPLEMENTED = HTTPStatus.NOT_IMPLEMENTED
-    BAD_GATEWAY = HTTPStatus.BAD_GATEWAY
-    SERVICE_UNAVAILABLE = HTTPStatus.SERVICE_UNAVAILABLE
-    GATEWAY_TIMEOUT = HTTPStatus.GATEWAY_TIMEOUT
-    HTTP_VERSION_NOT_SUPPORTED = HTTPStatus.HTTP_VERSION_NOT_SUPPORTED
-    VARIANT_ALSO_NEGOTIATES = HTTPStatus.VARIANT_ALSO_NEGOTIATES
-    INSUFFICIENT_STORAGE = HTTPStatus.INSUFFICIENT_STORAGE
-    LOOP_DETECTED = HTTPStatus.LOOP_DETECTED
-    NOT_EXTENDED = HTTPStatus.NOT_EXTENDED
-    NETWORK_AUTHENTICATION_REQUIRED = HTTPStatus.NETWORK_AUTHENTICATION_REQUIRED
-    """
-        )
-    )
-
-
-astroid.register_module_extender(astroid.MANAGER, "http", _http_transform)
-astroid.register_module_extender(astroid.MANAGER, "http.client", _http_client_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_io.py b/venv/Lib/site-packages/astroid/brain/brain_io.py
deleted file mode 100644
index 4c68922..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_io.py
+++ /dev/null
@@ -1,45 +0,0 @@
-# Copyright (c) 2016 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid brain hints for some of the _io C objects."""
-
-import astroid
-
-
-BUFFERED = {"BufferedWriter", "BufferedReader"}
-TextIOWrapper = "TextIOWrapper"
-FileIO = "FileIO"
-BufferedWriter = "BufferedWriter"
-
-
-def _generic_io_transform(node, name, cls):
-    """Transform the given name, by adding the given *class* as a member of the node."""
-
-    io_module = astroid.MANAGER.ast_from_module_name("_io")
-    attribute_object = io_module[cls]
-    instance = attribute_object.instantiate_class()
-    node.locals[name] = [instance]
-
-
-def _transform_text_io_wrapper(node):
-    # This is not always correct, since it can vary with the type of the descriptor,
-    # being stdout, stderr or stdin. But we cannot get access to the name of the
-    # stream, which is why we are using the BufferedWriter class as a default
-    # value
-    return _generic_io_transform(node, name="buffer", cls=BufferedWriter)
-
-
-def _transform_buffered(node):
-    return _generic_io_transform(node, name="raw", cls=FileIO)
-
-
-astroid.MANAGER.register_transform(
-    astroid.ClassDef, _transform_buffered, lambda node: node.name in BUFFERED
-)
-astroid.MANAGER.register_transform(
-    astroid.ClassDef,
-    _transform_text_io_wrapper,
-    lambda node: node.name == TextIOWrapper,
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_mechanize.py b/venv/Lib/site-packages/astroid/brain/brain_mechanize.py
deleted file mode 100644
index 93f282e..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_mechanize.py
+++ /dev/null
@@ -1,29 +0,0 @@
-# Copyright (c) 2012-2013 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-from astroid import MANAGER, register_module_extender
-from astroid.builder import AstroidBuilder
-
-
-def mechanize_transform():
-    return AstroidBuilder(MANAGER).string_build(
-        """
-
-class Browser(object):
-    def open(self, url, data=None, timeout=None):
-        return None
-    def open_novisit(self, url, data=None, timeout=None):
-        return None
-    def open_local_file(self, filename):
-        return None
-
-"""
-    )
-
-
-register_module_extender(MANAGER, "mechanize", mechanize_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_multiprocessing.py b/venv/Lib/site-packages/astroid/brain/brain_multiprocessing.py
deleted file mode 100644
index 71256ee..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_multiprocessing.py
+++ /dev/null
@@ -1,106 +0,0 @@
-# Copyright (c) 2016 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-import sys
-
-import astroid
-from astroid import exceptions
-
-
-def _multiprocessing_transform():
-    module = astroid.parse(
-        """
-    from multiprocessing.managers import SyncManager
-    def Manager():
-        return SyncManager()
-    """
-    )
-    # Multiprocessing uses a getattr lookup inside contexts,
-    # in order to get the attributes they need. Since it's extremely
-    # dynamic, we use this approach to fake it.
-    node = astroid.parse(
-        """
-    from multiprocessing.context import DefaultContext, BaseContext
-    default = DefaultContext()
-    base = BaseContext()
-    """
-    )
-    try:
-        context = next(node["default"].infer())
-        base = next(node["base"].infer())
-    except exceptions.InferenceError:
-        return module
-
-    for node in (context, base):
-        for key, value in node.locals.items():
-            if key.startswith("_"):
-                continue
-
-            value = value[0]
-            if isinstance(value, astroid.FunctionDef):
-                # We need to rebound this, since otherwise
-                # it will have an extra argument (self).
-                value = astroid.BoundMethod(value, node)
-            module[key] = value
-    return module
-
-
-def _multiprocessing_managers_transform():
-    return astroid.parse(
-        """
-    import array
-    import threading
-    import multiprocessing.pool as pool
-
-    import six
-
-    class Namespace(object):
-        pass
-
-    class Value(object):
-        def __init__(self, typecode, value, lock=True):
-            self._typecode = typecode
-            self._value = value
-        def get(self):
-            return self._value
-        def set(self, value):
-            self._value = value
-        def __repr__(self):
-            return '%s(%r, %r)'%(type(self).__name__, self._typecode, self._value)
-        value = property(get, set)
-
-    def Array(typecode, sequence, lock=True):
-        return array.array(typecode, sequence)
-
-    class SyncManager(object):
-        Queue = JoinableQueue = six.moves.queue.Queue
-        Event = threading.Event
-        RLock = threading.RLock
-        BoundedSemaphore = threading.BoundedSemaphore
-        Condition = threading.Condition
-        Barrier = threading.Barrier
-        Pool = pool.Pool
-        list = list
-        dict = dict
-        Value = Value
-        Array = Array
-        Namespace = Namespace
-        __enter__ = lambda self: self
-        __exit__ = lambda *args: args
-
-        def start(self, initializer=None, initargs=None):
-            pass
-        def shutdown(self):
-            pass
-    """
-    )
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "multiprocessing.managers", _multiprocessing_managers_transform
-)
-astroid.register_module_extender(
-    astroid.MANAGER, "multiprocessing", _multiprocessing_transform
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_namedtuple_enum.py b/venv/Lib/site-packages/astroid/brain/brain_namedtuple_enum.py
deleted file mode 100644
index de24067..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_namedtuple_enum.py
+++ /dev/null
@@ -1,449 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2012-2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2015 David Shea <dshea@redhat.com>
-# Copyright (c) 2015 Philip Lorenz <philip@bithub.de>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016 Mateusz Bysiek <mb@mbdev.pl>
-# Copyright (c) 2017 Hugo <hugovk@users.noreply.github.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for the Python standard library."""
-
-import functools
-import keyword
-from textwrap import dedent
-
-from astroid import MANAGER, UseInferenceDefault, inference_tip, InferenceError
-from astroid import arguments
-from astroid import exceptions
-from astroid import nodes
-from astroid.builder import AstroidBuilder, extract_node
-from astroid import util
-
-
-TYPING_NAMEDTUPLE_BASENAMES = {"NamedTuple", "typing.NamedTuple"}
-ENUM_BASE_NAMES = {
-    "Enum",
-    "IntEnum",
-    "enum.Enum",
-    "enum.IntEnum",
-    "IntFlag",
-    "enum.IntFlag",
-}
-
-
-def _infer_first(node, context):
-    if node is util.Uninferable:
-        raise UseInferenceDefault
-    try:
-        value = next(node.infer(context=context))
-        if value is util.Uninferable:
-            raise UseInferenceDefault()
-        else:
-            return value
-    except StopIteration:
-        raise InferenceError()
-
-
-def _find_func_form_arguments(node, context):
-    def _extract_namedtuple_arg_or_keyword(position, key_name=None):
-
-        if len(args) > position:
-            return _infer_first(args[position], context)
-        if key_name and key_name in found_keywords:
-            return _infer_first(found_keywords[key_name], context)
-
-    args = node.args
-    keywords = node.keywords
-    found_keywords = (
-        {keyword.arg: keyword.value for keyword in keywords} if keywords else {}
-    )
-
-    name = _extract_namedtuple_arg_or_keyword(position=0, key_name="typename")
-    names = _extract_namedtuple_arg_or_keyword(position=1, key_name="field_names")
-    if name and names:
-        return name.value, names
-
-    raise UseInferenceDefault()
-
-
-def infer_func_form(node, base_type, context=None, enum=False):
-    """Specific inference function for namedtuple or Python 3 enum. """
-    # node is a Call node, class name as first argument and generated class
-    # attributes as second argument
-
-    # namedtuple or enums list of attributes can be a list of strings or a
-    # whitespace-separate string
-    try:
-        name, names = _find_func_form_arguments(node, context)
-        try:
-            attributes = names.value.replace(",", " ").split()
-        except AttributeError:
-            if not enum:
-                attributes = [
-                    _infer_first(const, context).value for const in names.elts
-                ]
-            else:
-                # Enums supports either iterator of (name, value) pairs
-                # or mappings.
-                if hasattr(names, "items") and isinstance(names.items, list):
-                    attributes = [
-                        _infer_first(const[0], context).value
-                        for const in names.items
-                        if isinstance(const[0], nodes.Const)
-                    ]
-                elif hasattr(names, "elts"):
-                    # Enums can support either ["a", "b", "c"]
-                    # or [("a", 1), ("b", 2), ...], but they can't
-                    # be mixed.
-                    if all(isinstance(const, nodes.Tuple) for const in names.elts):
-                        attributes = [
-                            _infer_first(const.elts[0], context).value
-                            for const in names.elts
-                            if isinstance(const, nodes.Tuple)
-                        ]
-                    else:
-                        attributes = [
-                            _infer_first(const, context).value for const in names.elts
-                        ]
-                else:
-                    raise AttributeError
-                if not attributes:
-                    raise AttributeError
-    except (AttributeError, exceptions.InferenceError):
-        raise UseInferenceDefault()
-
-    # If we can't infer the name of the class, don't crash, up to this point
-    # we know it is a namedtuple anyway.
-    name = name or "Uninferable"
-    # we want to return a Class node instance with proper attributes set
-    class_node = nodes.ClassDef(name, "docstring")
-    class_node.parent = node.parent
-    # set base class=tuple
-    class_node.bases.append(base_type)
-    # XXX add __init__(*attributes) method
-    for attr in attributes:
-        fake_node = nodes.EmptyNode()
-        fake_node.parent = class_node
-        fake_node.attrname = attr
-        class_node.instance_attrs[attr] = [fake_node]
-    return class_node, name, attributes
-
-
-def _has_namedtuple_base(node):
-    """Predicate for class inference tip
-
-    :type node: ClassDef
-    :rtype: bool
-    """
-    return set(node.basenames) & TYPING_NAMEDTUPLE_BASENAMES
-
-
-def _looks_like(node, name):
-    func = node.func
-    if isinstance(func, nodes.Attribute):
-        return func.attrname == name
-    if isinstance(func, nodes.Name):
-        return func.name == name
-    return False
-
-
-_looks_like_namedtuple = functools.partial(_looks_like, name="namedtuple")
-_looks_like_enum = functools.partial(_looks_like, name="Enum")
-_looks_like_typing_namedtuple = functools.partial(_looks_like, name="NamedTuple")
-
-
-def infer_named_tuple(node, context=None):
-    """Specific inference function for namedtuple Call node"""
-    tuple_base_name = nodes.Name(name="tuple", parent=node.root())
-    class_node, name, attributes = infer_func_form(
-        node, tuple_base_name, context=context
-    )
-    call_site = arguments.CallSite.from_call(node)
-    func = next(extract_node("import collections; collections.namedtuple").infer())
-    try:
-        rename = next(call_site.infer_argument(func, "rename", context)).bool_value()
-    except InferenceError:
-        rename = False
-
-    if rename:
-        attributes = _get_renamed_namedtuple_attributes(attributes)
-
-    replace_args = ", ".join("{arg}=None".format(arg=arg) for arg in attributes)
-    field_def = (
-        "    {name} = property(lambda self: self[{index:d}], "
-        "doc='Alias for field number {index:d}')"
-    )
-    field_defs = "\n".join(
-        field_def.format(name=name, index=index)
-        for index, name in enumerate(attributes)
-    )
-    fake = AstroidBuilder(MANAGER).string_build(
-        """
-class %(name)s(tuple):
-    __slots__ = ()
-    _fields = %(fields)r
-    def _asdict(self):
-        return self.__dict__
-    @classmethod
-    def _make(cls, iterable, new=tuple.__new__, len=len):
-        return new(cls, iterable)
-    def _replace(self, %(replace_args)s):
-        return self
-    def __getnewargs__(self):
-        return tuple(self)
-%(field_defs)s
-    """
-        % {
-            "name": name,
-            "fields": attributes,
-            "field_defs": field_defs,
-            "replace_args": replace_args,
-        }
-    )
-    class_node.locals["_asdict"] = fake.body[0].locals["_asdict"]
-    class_node.locals["_make"] = fake.body[0].locals["_make"]
-    class_node.locals["_replace"] = fake.body[0].locals["_replace"]
-    class_node.locals["_fields"] = fake.body[0].locals["_fields"]
-    for attr in attributes:
-        class_node.locals[attr] = fake.body[0].locals[attr]
-    # we use UseInferenceDefault, we can't be a generator so return an iterator
-    return iter([class_node])
-
-
-def _get_renamed_namedtuple_attributes(field_names):
-    names = list(field_names)
-    seen = set()
-    for i, name in enumerate(field_names):
-        if (
-            not all(c.isalnum() or c == "_" for c in name)
-            or keyword.iskeyword(name)
-            or not name
-            or name[0].isdigit()
-            or name.startswith("_")
-            or name in seen
-        ):
-            names[i] = "_%d" % i
-        seen.add(name)
-    return tuple(names)
-
-
-def infer_enum(node, context=None):
-    """ Specific inference function for enum Call node. """
-    enum_meta = extract_node(
-        """
-    class EnumMeta(object):
-        'docstring'
-        def __call__(self, node):
-            class EnumAttribute(object):
-                name = ''
-                value = 0
-            return EnumAttribute()
-        def __iter__(self):
-            class EnumAttribute(object):
-                name = ''
-                value = 0
-            return [EnumAttribute()]
-        def __reversed__(self):
-            class EnumAttribute(object):
-                name = ''
-                value = 0
-            return (EnumAttribute, )
-        def __next__(self):
-            return next(iter(self))
-        def __getitem__(self, attr):
-            class Value(object):
-                @property
-                def name(self):
-                    return ''
-                @property
-                def value(self):
-                    return attr
-
-            return Value()
-        __members__ = ['']
-    """
-    )
-    class_node = infer_func_form(node, enum_meta, context=context, enum=True)[0]
-    return iter([class_node.instantiate_class()])
-
-
-INT_FLAG_ADDITION_METHODS = """
-    def __or__(self, other):
-        return {name}(self.value | other.value)
-    def __and__(self, other):
-        return {name}(self.value & other.value)
-    def __xor__(self, other):
-        return {name}(self.value ^ other.value)
-    def __add__(self, other):
-        return {name}(self.value + other.value)
-    def __div__(self, other):
-        return {name}(self.value / other.value)
-    def __invert__(self):
-        return {name}(~self.value)
-    def __mul__(self, other):
-        return {name}(self.value * other.value)
-"""
-
-
-def infer_enum_class(node):
-    """ Specific inference for enums. """
-    for basename in node.basenames:
-        # TODO: doesn't handle subclasses yet. This implementation
-        # is a hack to support enums.
-        if basename not in ENUM_BASE_NAMES:
-            continue
-        if node.root().name == "enum":
-            # Skip if the class is directly from enum module.
-            break
-        for local, values in node.locals.items():
-            if any(not isinstance(value, nodes.AssignName) for value in values):
-                continue
-
-            targets = []
-            stmt = values[0].statement()
-            if isinstance(stmt, nodes.Assign):
-                if isinstance(stmt.targets[0], nodes.Tuple):
-                    targets = stmt.targets[0].itered()
-                else:
-                    targets = stmt.targets
-            elif isinstance(stmt, nodes.AnnAssign):
-                targets = [stmt.target]
-
-            inferred_return_value = None
-            if isinstance(stmt, nodes.Assign):
-                if isinstance(stmt.value, nodes.Const):
-                    if isinstance(stmt.value.value, str):
-                        inferred_return_value = repr(stmt.value.value)
-                    else:
-                        inferred_return_value = stmt.value.value
-                else:
-                    inferred_return_value = stmt.value.as_string()
-
-            new_targets = []
-            for target in targets:
-                # Replace all the assignments with our mocked class.
-                classdef = dedent(
-                    """
-                class {name}({types}):
-                    @property
-                    def value(self):
-                        return {return_value}
-                    @property
-                    def name(self):
-                        return "{name}"
-                """.format(
-                        name=target.name,
-                        types=", ".join(node.basenames),
-                        return_value=inferred_return_value,
-                    )
-                )
-                if "IntFlag" in basename:
-                    # Alright, we need to add some additional methods.
-                    # Unfortunately we still can't infer the resulting objects as
-                    # Enum members, but once we'll be able to do that, the following
-                    # should result in some nice symbolic execution
-                    classdef += INT_FLAG_ADDITION_METHODS.format(name=target.name)
-
-                fake = AstroidBuilder(MANAGER).string_build(classdef)[target.name]
-                fake.parent = target.parent
-                for method in node.mymethods():
-                    fake.locals[method.name] = [method]
-                new_targets.append(fake.instantiate_class())
-            node.locals[local] = new_targets
-        break
-    return node
-
-
-def infer_typing_namedtuple_class(class_node, context=None):
-    """Infer a subclass of typing.NamedTuple"""
-    # Check if it has the corresponding bases
-    annassigns_fields = [
-        annassign.target.name
-        for annassign in class_node.body
-        if isinstance(annassign, nodes.AnnAssign)
-    ]
-    code = dedent(
-        """
-    from collections import namedtuple
-    namedtuple({typename!r}, {fields!r})
-    """
-    ).format(typename=class_node.name, fields=",".join(annassigns_fields))
-    node = extract_node(code)
-    generated_class_node = next(infer_named_tuple(node, context))
-    for method in class_node.mymethods():
-        generated_class_node.locals[method.name] = [method]
-
-    for assign in class_node.body:
-        if not isinstance(assign, nodes.Assign):
-            continue
-
-        for target in assign.targets:
-            attr = target.name
-            generated_class_node.locals[attr] = class_node.locals[attr]
-
-    return iter((generated_class_node,))
-
-
-def infer_typing_namedtuple(node, context=None):
-    """Infer a typing.NamedTuple(...) call."""
-    # This is essentially a namedtuple with different arguments
-    # so we extract the args and infer a named tuple.
-    try:
-        func = next(node.func.infer())
-    except InferenceError:
-        raise UseInferenceDefault
-
-    if func.qname() != "typing.NamedTuple":
-        raise UseInferenceDefault
-
-    if len(node.args) != 2:
-        raise UseInferenceDefault
-
-    if not isinstance(node.args[1], (nodes.List, nodes.Tuple)):
-        raise UseInferenceDefault
-
-    names = []
-    for elt in node.args[1].elts:
-        if not isinstance(elt, (nodes.List, nodes.Tuple)):
-            raise UseInferenceDefault
-        if len(elt.elts) != 2:
-            raise UseInferenceDefault
-        names.append(elt.elts[0].as_string())
-
-    typename = node.args[0].as_string()
-    if names:
-        field_names = "({},)".format(",".join(names))
-    else:
-        field_names = "''"
-    node = extract_node(
-        "namedtuple({typename}, {fields})".format(typename=typename, fields=field_names)
-    )
-    return infer_named_tuple(node, context)
-
-
-MANAGER.register_transform(
-    nodes.Call, inference_tip(infer_named_tuple), _looks_like_namedtuple
-)
-MANAGER.register_transform(nodes.Call, inference_tip(infer_enum), _looks_like_enum)
-MANAGER.register_transform(
-    nodes.ClassDef,
-    infer_enum_class,
-    predicate=lambda cls: any(
-        basename for basename in cls.basenames if basename in ENUM_BASE_NAMES
-    ),
-)
-MANAGER.register_transform(
-    nodes.ClassDef, inference_tip(infer_typing_namedtuple_class), _has_namedtuple_base
-)
-MANAGER.register_transform(
-    nodes.Call, inference_tip(infer_typing_namedtuple), _looks_like_typing_namedtuple
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_nose.py b/venv/Lib/site-packages/astroid/brain/brain_nose.py
deleted file mode 100644
index 7b12d76..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_nose.py
+++ /dev/null
@@ -1,77 +0,0 @@
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Hooks for nose library."""
-
-import re
-import textwrap
-
-import astroid
-import astroid.builder
-
-_BUILDER = astroid.builder.AstroidBuilder(astroid.MANAGER)
-
-
-def _pep8(name, caps=re.compile("([A-Z])")):
-    return caps.sub(lambda m: "_" + m.groups()[0].lower(), name)
-
-
-def _nose_tools_functions():
-    """Get an iterator of names and bound methods."""
-    module = _BUILDER.string_build(
-        textwrap.dedent(
-            """
-    import unittest
-
-    class Test(unittest.TestCase):
-        pass
-    a = Test()
-    """
-        )
-    )
-    try:
-        case = next(module["a"].infer())
-    except astroid.InferenceError:
-        return
-    for method in case.methods():
-        if method.name.startswith("assert") and "_" not in method.name:
-            pep8_name = _pep8(method.name)
-            yield pep8_name, astroid.BoundMethod(method, case)
-        if method.name == "assertEqual":
-            # nose also exports assert_equals.
-            yield "assert_equals", astroid.BoundMethod(method, case)
-
-
-def _nose_tools_transform(node):
-    for method_name, method in _nose_tools_functions():
-        node.locals[method_name] = [method]
-
-
-def _nose_tools_trivial_transform():
-    """Custom transform for the nose.tools module."""
-    stub = _BUILDER.string_build("""__all__ = []""")
-    all_entries = ["ok_", "eq_"]
-
-    for pep8_name, method in _nose_tools_functions():
-        all_entries.append(pep8_name)
-        stub[pep8_name] = method
-
-    # Update the __all__ variable, since nose.tools
-    # does this manually with .append.
-    all_assign = stub["__all__"].parent
-    all_object = astroid.List(all_entries)
-    all_object.parent = all_assign
-    all_assign.value = all_object
-    return stub
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "nose.tools.trivial", _nose_tools_trivial_transform
-)
-astroid.MANAGER.register_transform(
-    astroid.Module, _nose_tools_transform, lambda n: n.name == "nose.tools"
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_fromnumeric.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_core_fromnumeric.py
deleted file mode 100644
index 43b30e4..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_fromnumeric.py
+++ /dev/null
@@ -1,23 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Astroid hooks for numpy.core.fromnumeric module."""
-
-import astroid
-
-
-def numpy_core_fromnumeric_transform():
-    return astroid.parse(
-        """
-    def sum(a, axis=None, dtype=None, out=None, keepdims=None, initial=None):
-        return numpy.ndarray([0, 0])
-    """
-    )
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "numpy.core.fromnumeric", numpy_core_fromnumeric_transform
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_function_base.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_core_function_base.py
deleted file mode 100644
index 05a73d9..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_function_base.py
+++ /dev/null
@@ -1,29 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Astroid hooks for numpy.core.function_base module."""
-
-import functools
-import astroid
-from brain_numpy_utils import looks_like_numpy_member, infer_numpy_member
-
-
-METHODS_TO_BE_INFERRED = {
-    "linspace": """def linspace(start, stop, num=50, endpoint=True, retstep=False, dtype=None, axis=0):
-            return numpy.ndarray([0, 0])""",
-    "logspace": """def logspace(start, stop, num=50, endpoint=True, base=10.0, dtype=None, axis=0):
-            return numpy.ndarray([0, 0])""",
-    "geomspace": """def geomspace(start, stop, num=50, endpoint=True, dtype=None, axis=0):
-            return numpy.ndarray([0, 0])""",
-}
-
-for func_name, func_src in METHODS_TO_BE_INFERRED.items():
-    inference_function = functools.partial(infer_numpy_member, func_src)
-    astroid.MANAGER.register_transform(
-        astroid.Attribute,
-        astroid.inference_tip(inference_function),
-        functools.partial(looks_like_numpy_member, func_name),
-    )
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_multiarray.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_core_multiarray.py
deleted file mode 100644
index 3032acc..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_multiarray.py
+++ /dev/null
@@ -1,55 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Astroid hooks for numpy.core.multiarray module."""
-
-import functools
-import astroid
-from brain_numpy_utils import looks_like_numpy_member, infer_numpy_member
-
-
-def numpy_core_multiarray_transform():
-    return astroid.parse(
-        """
-    # different functions defined in multiarray.py
-    def inner(a, b):
-        return numpy.ndarray([0, 0])
-
-    def vdot(a, b):
-        return numpy.ndarray([0, 0])
-        """
-    )
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "numpy.core.multiarray", numpy_core_multiarray_transform
-)
-
-
-METHODS_TO_BE_INFERRED = {
-    "array": """def array(object, dtype=None, copy=True, order='K', subok=False, ndmin=0):
-            return numpy.ndarray([0, 0])""",
-    "dot": """def dot(a, b, out=None):
-            return numpy.ndarray([0, 0])""",
-    "empty_like": """def empty_like(a, dtype=None, order='K', subok=True):
-            return numpy.ndarray((0, 0))""",
-    "concatenate": """def concatenate(arrays, axis=None, out=None):
-            return numpy.ndarray((0, 0))""",
-    "where": """def where(condition, x=None, y=None):
-            return numpy.ndarray([0, 0])""",
-    "empty": """def empty(shape, dtype=float, order='C'):
-            return numpy.ndarray([0, 0])""",
-    "zeros": """def zeros(shape, dtype=float, order='C'):
-            return numpy.ndarray([0, 0])""",
-}
-
-for method_name, function_src in METHODS_TO_BE_INFERRED.items():
-    inference_function = functools.partial(infer_numpy_member, function_src)
-    astroid.MANAGER.register_transform(
-        astroid.Attribute,
-        astroid.inference_tip(inference_function),
-        functools.partial(looks_like_numpy_member, method_name),
-    )
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_numeric.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_core_numeric.py
deleted file mode 100644
index ba43c94..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_numeric.py
+++ /dev/null
@@ -1,43 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Astroid hooks for numpy.core.numeric module."""
-
-import functools
-import astroid
-from brain_numpy_utils import looks_like_numpy_member, infer_numpy_member
-
-
-def numpy_core_numeric_transform():
-    return astroid.parse(
-        """
-    # different functions defined in numeric.py
-    import numpy
-    def zeros_like(a, dtype=None, order='K', subok=True): return numpy.ndarray((0, 0))
-    def ones_like(a, dtype=None, order='K', subok=True): return numpy.ndarray((0, 0))
-    def full_like(a, fill_value, dtype=None, order='K', subok=True): return numpy.ndarray((0, 0))
-        """
-    )
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "numpy.core.numeric", numpy_core_numeric_transform
-)
-
-
-METHODS_TO_BE_INFERRED = {
-    "ones": """def ones(shape, dtype=None, order='C'):
-            return numpy.ndarray([0, 0])"""
-}
-
-
-for method_name, function_src in METHODS_TO_BE_INFERRED.items():
-    inference_function = functools.partial(infer_numpy_member, function_src)
-    astroid.MANAGER.register_transform(
-        astroid.Attribute,
-        astroid.inference_tip(inference_function),
-        functools.partial(looks_like_numpy_member, method_name),
-    )
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_numerictypes.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_core_numerictypes.py
deleted file mode 100644
index 42021fa..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_numerictypes.py
+++ /dev/null
@@ -1,250 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-# TODO(hippo91) : correct the methods signature.
-
-"""Astroid hooks for numpy.core.numerictypes module."""
-
-import astroid
-
-
-def numpy_core_numerictypes_transform():
-    return astroid.parse(
-        """
-    # different types defined in numerictypes.py
-    class generic(object):
-        def __init__(self, value):
-            self.T = None
-            self.base = None
-            self.data = None
-            self.dtype = None
-            self.flags = None
-            self.flat = None
-            self.imag = None
-            self.itemsize = None
-            self.nbytes = None
-            self.ndim = None
-            self.real = None
-            self.size = None
-            self.strides = None
-
-        def all(self): return uninferable
-        def any(self): return uninferable
-        def argmax(self): return uninferable
-        def argmin(self): return uninferable
-        def argsort(self): return uninferable
-        def astype(self): return uninferable
-        def base(self): return uninferable
-        def byteswap(self): return uninferable
-        def choose(self): return uninferable
-        def clip(self): return uninferable
-        def compress(self): return uninferable
-        def conj(self): return uninferable
-        def conjugate(self): return uninferable
-        def copy(self): return uninferable
-        def cumprod(self): return uninferable
-        def cumsum(self): return uninferable
-        def data(self): return uninferable
-        def diagonal(self): return uninferable
-        def dtype(self): return uninferable
-        def dump(self): return uninferable
-        def dumps(self): return uninferable
-        def fill(self): return uninferable
-        def flags(self): return uninferable
-        def flat(self): return uninferable
-        def flatten(self): return uninferable
-        def getfield(self): return uninferable
-        def imag(self): return uninferable
-        def item(self): return uninferable
-        def itemset(self): return uninferable
-        def itemsize(self): return uninferable
-        def max(self): return uninferable
-        def mean(self): return uninferable
-        def min(self): return uninferable
-        def nbytes(self): return uninferable
-        def ndim(self): return uninferable
-        def newbyteorder(self): return uninferable
-        def nonzero(self): return uninferable
-        def prod(self): return uninferable
-        def ptp(self): return uninferable
-        def put(self): return uninferable
-        def ravel(self): return uninferable
-        def real(self): return uninferable
-        def repeat(self): return uninferable
-        def reshape(self): return uninferable
-        def resize(self): return uninferable
-        def round(self): return uninferable
-        def searchsorted(self): return uninferable
-        def setfield(self): return uninferable
-        def setflags(self): return uninferable
-        def shape(self): return uninferable
-        def size(self): return uninferable
-        def sort(self): return uninferable
-        def squeeze(self): return uninferable
-        def std(self): return uninferable
-        def strides(self): return uninferable
-        def sum(self): return uninferable
-        def swapaxes(self): return uninferable
-        def take(self): return uninferable
-        def tobytes(self): return uninferable
-        def tofile(self): return uninferable
-        def tolist(self): return uninferable
-        def tostring(self): return uninferable
-        def trace(self): return uninferable
-        def transpose(self): return uninferable
-        def var(self): return uninferable
-        def view(self): return uninferable
-
-
-    class dtype(object):
-        def __init__(self, obj, align=False, copy=False):
-            self.alignment = None
-            self.base = None
-            self.byteorder = None
-            self.char = None
-            self.descr = None
-            self.fields = None
-            self.flags = None
-            self.hasobject = None
-            self.isalignedstruct = None
-            self.isbuiltin = None
-            self.isnative = None
-            self.itemsize = None
-            self.kind = None
-            self.metadata = None
-            self.name = None
-            self.names = None
-            self.num = None
-            self.shape = None
-            self.str = None
-            self.subdtype = None
-            self.type = None
-
-        def newbyteorder(self, new_order='S'): return uninferable
-        def __neg__(self): return uninferable
-
-    class busdaycalendar(object):
-        def __init__(self, weekmask='1111100', holidays=None):
-            self.holidays = None
-            self.weekmask = None
-
-    class flexible(generic): pass
-    class bool_(generic): pass
-    class number(generic):
-        def __neg__(self): return uninferable
-    class datetime64(generic):
-        def __init__(self, nb, unit=None): pass
-
-
-    class void(flexible):
-        def __init__(self, *args, **kwargs):
-            self.base = None
-            self.dtype = None
-            self.flags = None
-        def getfield(self): return uninferable
-        def setfield(self): return uninferable
-
-
-    class character(flexible): pass
-
-
-    class integer(number):
-        def __init__(self, value):
-           self.denominator = None
-           self.numerator = None
-
-
-    class inexact(number): pass
-
-
-    class str_(str, character):
-        def maketrans(self, x, y=None, z=None): return uninferable
-
-
-    class bytes_(bytes, character):
-        def fromhex(self, string): return uninferable
-        def maketrans(self, frm, to): return uninferable
-
-
-    class signedinteger(integer): pass
-
-
-    class unsignedinteger(integer): pass
-
-
-    class complexfloating(inexact): pass
-
-
-    class floating(inexact): pass
-
-
-    class float64(floating, float):
-        def fromhex(self, string): return uninferable
-
-
-    class uint64(unsignedinteger): pass
-    class complex64(complexfloating): pass
-    class int16(signedinteger): pass
-    class float96(floating): pass
-    class int8(signedinteger): pass
-    class uint32(unsignedinteger): pass
-    class uint8(unsignedinteger): pass
-    class _typedict(dict): pass
-    class complex192(complexfloating): pass
-    class timedelta64(signedinteger):
-        def __init__(self, nb, unit=None): pass
-    class int32(signedinteger): pass
-    class uint16(unsignedinteger): pass
-    class float32(floating): pass
-    class complex128(complexfloating, complex): pass
-    class float16(floating): pass
-    class int64(signedinteger): pass
-
-    buffer_type = memoryview
-    bool8 = bool_
-    byte = int8
-    bytes0 = bytes_
-    cdouble = complex128
-    cfloat = complex128
-    clongdouble = complex192
-    clongfloat = complex192
-    complex_ = complex128
-    csingle = complex64
-    double = float64
-    float_ = float64
-    half = float16
-    int0 = int32
-    int_ = int32
-    intc = int32
-    intp = int32
-    long = int32
-    longcomplex = complex192
-    longdouble = float96
-    longfloat = float96
-    longlong = int64
-    object0 = object_
-    object_ = object_
-    short = int16
-    single = float32
-    singlecomplex = complex64
-    str0 = str_
-    string_ = bytes_
-    ubyte = uint8
-    uint = uint32
-    uint0 = uint32
-    uintc = uint32
-    uintp = uint32
-    ulonglong = uint64
-    unicode = str_
-    unicode_ = str_
-    ushort = uint16
-    void0 = void
-    """
-    )
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "numpy.core.numerictypes", numpy_core_numerictypes_transform
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_umath.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_core_umath.py
deleted file mode 100644
index 459d38c..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_core_umath.py
+++ /dev/null
@@ -1,105 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Astroid hooks for numpy.core.umath module."""
-
-import astroid
-
-
-def numpy_core_umath_transform():
-    ufunc_optional_keyword_arguments = (
-        """out=None, where=True, casting='same_kind', order='K', """
-        """dtype=None, subok=True"""
-    )
-    return astroid.parse(
-        """
-    # Constants
-    e = 2.718281828459045
-    euler_gamma = 0.5772156649015329
-
-    # No arg functions
-    def geterrobj(): return []
-
-    # One arg functions
-    def seterrobj(errobj): return None
-
-    # One arg functions with optional kwargs
-    def arccos(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def arccosh(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def arcsin(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def arcsinh(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def arctan(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def arctanh(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def cbrt(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def conj(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def conjugate(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def cosh(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def deg2rad(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def degrees(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def exp2(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def expm1(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def fabs(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def frexp(x, {opt_args:s}): return (numpy.ndarray((0, 0)), numpy.ndarray((0, 0)))
-    def isfinite(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def isinf(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def log(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def log1p(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def log2(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def logical_not(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def modf(x, {opt_args:s}): return (numpy.ndarray((0, 0)), numpy.ndarray((0, 0)))
-    def negative(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def rad2deg(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def radians(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def reciprocal(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def rint(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def sign(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def signbit(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def sinh(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def spacing(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def square(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def tan(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def tanh(x, {opt_args:s}): return numpy.ndarray((0, 0))
-    def trunc(x, {opt_args:s}): return numpy.ndarray((0, 0))
-
-    # Two args functions with optional kwargs
-    def bitwise_and(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def bitwise_or(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def bitwise_xor(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def copysign(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def divide(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def equal(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def floor_divide(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def fmax(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def fmin(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def fmod(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def greater(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def hypot(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def ldexp(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def left_shift(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def less(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def logaddexp(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def logaddexp2(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def logical_and(x1, x2, {opt_args:s}): return numpy.ndarray([0, 0])
-    def logical_or(x1, x2, {opt_args:s}): return numpy.ndarray([0, 0])
-    def logical_xor(x1, x2, {opt_args:s}): return numpy.ndarray([0, 0])
-    def maximum(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def minimum(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def nextafter(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def not_equal(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def power(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def remainder(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def right_shift(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def subtract(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    def true_divide(x1, x2, {opt_args:s}): return numpy.ndarray((0, 0))
-    """.format(
-            opt_args=ufunc_optional_keyword_arguments
-        )
-    )
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "numpy.core.umath", numpy_core_umath_transform
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_ndarray.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_ndarray.py
deleted file mode 100644
index 8c231a3..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_ndarray.py
+++ /dev/null
@@ -1,153 +0,0 @@
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Astroid hooks for numpy ndarray class."""
-
-import functools
-import astroid
-
-
-def infer_numpy_ndarray(node, context=None):
-    ndarray = """
-    class ndarray(object):
-        def __init__(self, shape, dtype=float, buffer=None, offset=0,
-                     strides=None, order=None):
-            self.T = None
-            self.base = None
-            self.ctypes = None
-            self.data = None
-            self.dtype = None
-            self.flags = None
-            self.flat = None
-            self.imag = None
-            self.itemsize = None
-            self.nbytes = None
-            self.ndim = None
-            self.real = None
-            self.shape = None
-            self.size = None
-            self.strides = None
-
-        def __abs__(self): return numpy.ndarray([0, 0])
-        def __add__(self, value): return numpy.ndarray([0, 0]) 
-        def __and__(self, value): return numpy.ndarray([0, 0]) 
-        def __array__(self, dtype=None): return numpy.ndarray([0, 0]) 
-        def __array_wrap__(self, obj): return numpy.ndarray([0, 0]) 
-        def __contains__(self, key): return True
-        def __copy__(self): return numpy.ndarray([0, 0])
-        def __deepcopy__(self, memo): return numpy.ndarray([0, 0])
-        def __divmod__(self, value): return (numpy.ndarray([0, 0]), numpy.ndarray([0, 0]))
-        def __eq__(self, value): return numpy.ndarray([0, 0])
-        def __float__(self): return 0.
-        def __floordiv__(self): return numpy.ndarray([0, 0])
-        def __ge__(self, value): return numpy.ndarray([0, 0])
-        def __getitem__(self, key): return uninferable
-        def __gt__(self, value): return numpy.ndarray([0, 0])
-        def __iadd__(self, value): return numpy.ndarray([0, 0])
-        def __iand__(self, value): return numpy.ndarray([0, 0])
-        def __ifloordiv__(self, value): return numpy.ndarray([0, 0])
-        def __ilshift__(self, value): return numpy.ndarray([0, 0])
-        def __imod__(self, value): return numpy.ndarray([0, 0])
-        def __imul__(self, value): return numpy.ndarray([0, 0])
-        def __int__(self): return 0
-        def __invert__(self): return numpy.ndarray([0, 0])
-        def __ior__(self, value): return numpy.ndarray([0, 0])
-        def __ipow__(self, value): return numpy.ndarray([0, 0])
-        def __irshift__(self, value): return numpy.ndarray([0, 0])
-        def __isub__(self, value): return numpy.ndarray([0, 0])
-        def __itruediv__(self, value): return numpy.ndarray([0, 0])
-        def __ixor__(self, value): return numpy.ndarray([0, 0])
-        def __le__(self, value): return numpy.ndarray([0, 0])
-        def __len__(self): return 1
-        def __lshift__(self, value): return numpy.ndarray([0, 0])
-        def __lt__(self, value): return numpy.ndarray([0, 0])
-        def __matmul__(self, value): return numpy.ndarray([0, 0])
-        def __mod__(self, value): return numpy.ndarray([0, 0])
-        def __mul__(self, value): return numpy.ndarray([0, 0])
-        def __ne__(self, value): return numpy.ndarray([0, 0])
-        def __neg__(self): return numpy.ndarray([0, 0])
-        def __or__(self): return numpy.ndarray([0, 0])
-        def __pos__(self): return numpy.ndarray([0, 0])
-        def __pow__(self): return numpy.ndarray([0, 0])
-        def __repr__(self): return str()
-        def __rshift__(self): return numpy.ndarray([0, 0])
-        def __setitem__(self, key, value): return uninferable
-        def __str__(self): return str()
-        def __sub__(self, value): return numpy.ndarray([0, 0])
-        def __truediv__(self, value): return numpy.ndarray([0, 0])
-        def __xor__(self, value): return numpy.ndarray([0, 0])
-        def all(self, axis=None, out=None, keepdims=False): return np.ndarray([0, 0])
-        def any(self, axis=None, out=None, keepdims=False): return np.ndarray([0, 0])
-        def argmax(self, axis=None, out=None): return np.ndarray([0, 0])
-        def argmin(self, axis=None, out=None): return np.ndarray([0, 0])
-        def argpartition(self, kth, axis=-1, kind='introselect', order=None): return np.ndarray([0, 0])
-        def argsort(self, axis=-1, kind='quicksort', order=None): return np.ndarray([0, 0])
-        def astype(self, dtype, order='K', casting='unsafe', subok=True, copy=True): return np.ndarray([0, 0])
-        def byteswap(self, inplace=False): return np.ndarray([0, 0])
-        def choose(self, choices, out=None, mode='raise'): return np.ndarray([0, 0])
-        def clip(self, min=None, max=None, out=None): return np.ndarray([0, 0])
-        def compress(self, condition, axis=None, out=None): return np.ndarray([0, 0])
-        def conj(self): return np.ndarray([0, 0])
-        def conjugate(self): return np.ndarray([0, 0])
-        def copy(self, order='C'): return np.ndarray([0, 0])
-        def cumprod(self, axis=None, dtype=None, out=None): return np.ndarray([0, 0])
-        def cumsum(self, axis=None, dtype=None, out=None): return np.ndarray([0, 0])
-        def diagonal(self, offset=0, axis1=0, axis2=1): return np.ndarray([0, 0])
-        def dot(self, b, out=None): return np.ndarray([0, 0])
-        def dump(self, file): return None
-        def dumps(self): return str()
-        def fill(self, value): return None
-        def flatten(self, order='C'): return np.ndarray([0, 0])
-        def getfield(self, dtype, offset=0): return np.ndarray([0, 0])
-        def item(self, *args): return uninferable
-        def itemset(self, *args): return None
-        def max(self, axis=None, out=None): return np.ndarray([0, 0])
-        def mean(self, axis=None, dtype=None, out=None, keepdims=False): return np.ndarray([0, 0])
-        def min(self, axis=None, out=None, keepdims=False): return np.ndarray([0, 0])
-        def newbyteorder(self, new_order='S'): return np.ndarray([0, 0])
-        def nonzero(self): return (1,)
-        def partition(self, kth, axis=-1, kind='introselect', order=None): return None
-        def prod(self, axis=None, dtype=None, out=None, keepdims=False): return np.ndarray([0, 0])
-        def ptp(self, axis=None, out=None): return np.ndarray([0, 0])
-        def put(self, indices, values, mode='raise'): return None
-        def ravel(self, order='C'): return np.ndarray([0, 0])
-        def repeat(self, repeats, axis=None): return np.ndarray([0, 0])
-        def reshape(self, shape, order='C'): return np.ndarray([0, 0])
-        def resize(self, new_shape, refcheck=True): return None
-        def round(self, decimals=0, out=None): return np.ndarray([0, 0])
-        def searchsorted(self, v, side='left', sorter=None): return np.ndarray([0, 0])
-        def setfield(self, val, dtype, offset=0): return None
-        def setflags(self, write=None, align=None, uic=None): return None
-        def sort(self, axis=-1, kind='quicksort', order=None): return None
-        def squeeze(self, axis=None): return np.ndarray([0, 0])
-        def std(self, axis=None, dtype=None, out=None, ddof=0, keepdims=False): return np.ndarray([0, 0])
-        def sum(self, axis=None, dtype=None, out=None, keepdims=False): return np.ndarray([0, 0])
-        def swapaxes(self, axis1, axis2): return np.ndarray([0, 0])
-        def take(self, indices, axis=None, out=None, mode='raise'): return np.ndarray([0, 0])
-        def tobytes(self, order='C'): return b''
-        def tofile(self, fid, sep="", format="%s"): return None
-        def tolist(self, ): return []
-        def tostring(self, order='C'): return b''
-        def trace(self, offset=0, axis1=0, axis2=1, dtype=None, out=None): return np.ndarray([0, 0])
-        def transpose(self, *axes): return np.ndarray([0, 0])
-        def var(self, axis=None, dtype=None, out=None, ddof=0, keepdims=False): return np.ndarray([0, 0])
-        def view(self, dtype=None, type=None): return np.ndarray([0, 0])
-    """
-    node = astroid.extract_node(ndarray)
-    return node.infer(context=context)
-
-
-def _looks_like_numpy_ndarray(node):
-    return isinstance(node, astroid.Attribute) and node.attrname == "ndarray"
-
-
-astroid.MANAGER.register_transform(
-    astroid.Attribute,
-    astroid.inference_tip(infer_numpy_ndarray),
-    _looks_like_numpy_ndarray,
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_random_mtrand.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_random_mtrand.py
deleted file mode 100644
index 772bfc4..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_random_mtrand.py
+++ /dev/null
@@ -1,70 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-# TODO(hippo91) : correct the functions return types
-"""Astroid hooks for numpy.random.mtrand module."""
-
-import astroid
-
-
-def numpy_random_mtrand_transform():
-    return astroid.parse(
-        """
-    def beta(a, b, size=None): return uninferable
-    def binomial(n, p, size=None): return uninferable
-    def bytes(length): return uninferable
-    def chisquare(df, size=None): return uninferable
-    def choice(a, size=None, replace=True, p=None): return uninferable
-    def dirichlet(alpha, size=None): return uninferable
-    def exponential(scale=1.0, size=None): return uninferable
-    def f(dfnum, dfden, size=None): return uninferable
-    def gamma(shape, scale=1.0, size=None): return uninferable
-    def geometric(p, size=None): return uninferable
-    def get_state(): return uninferable
-    def gumbel(loc=0.0, scale=1.0, size=None): return uninferable
-    def hypergeometric(ngood, nbad, nsample, size=None): return uninferable
-    def laplace(loc=0.0, scale=1.0, size=None): return uninferable
-    def logistic(loc=0.0, scale=1.0, size=None): return uninferable
-    def lognormal(mean=0.0, sigma=1.0, size=None): return uninferable
-    def logseries(p, size=None): return uninferable
-    def multinomial(n, pvals, size=None): return uninferable
-    def multivariate_normal(mean, cov, size=None): return uninferable
-    def negative_binomial(n, p, size=None): return uninferable
-    def noncentral_chisquare(df, nonc, size=None): return uninferable
-    def noncentral_f(dfnum, dfden, nonc, size=None): return uninferable
-    def normal(loc=0.0, scale=1.0, size=None): return uninferable
-    def pareto(a, size=None): return uninferable
-    def permutation(x): return uninferable
-    def poisson(lam=1.0, size=None): return uninferable
-    def power(a, size=None): return uninferable
-    def rand(*args): return uninferable
-    def randint(low, high=None, size=None, dtype='l'): 
-        import numpy
-        return numpy.ndarray((1,1))
-    def randn(*args): return uninferable
-    def random_integers(low, high=None, size=None): return uninferable
-    def random_sample(size=None): return uninferable
-    def rayleigh(scale=1.0, size=None): return uninferable
-    def seed(seed=None): return uninferable
-    def set_state(state): return uninferable
-    def shuffle(x): return uninferable
-    def standard_cauchy(size=None): return uninferable
-    def standard_exponential(size=None): return uninferable
-    def standard_gamma(shape, size=None): return uninferable
-    def standard_normal(size=None): return uninferable
-    def standard_t(df, size=None): return uninferable
-    def triangular(left, mode, right, size=None): return uninferable
-    def uniform(low=0.0, high=1.0, size=None): return uninferable
-    def vonmises(mu, kappa, size=None): return uninferable
-    def wald(mean, scale, size=None): return uninferable
-    def weibull(a, size=None): return uninferable
-    def zipf(a, size=None): return uninferable
-    """
-    )
-
-
-astroid.register_module_extender(
-    astroid.MANAGER, "numpy.random.mtrand", numpy_random_mtrand_transform
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_numpy_utils.py b/venv/Lib/site-packages/astroid/brain/brain_numpy_utils.py
deleted file mode 100644
index 2bad01e..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_numpy_utils.py
+++ /dev/null
@@ -1,56 +0,0 @@
-# Copyright (c) 2018-2019 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Different utilities for the numpy brains"""
-
-
-import astroid
-
-
-def infer_numpy_member(src, node, context=None):
-    node = astroid.extract_node(src)
-    return node.infer(context=context)
-
-
-def _is_a_numpy_module(node: astroid.node_classes.Name) -> bool:
-    """
-    Returns True if the node is a representation of a numpy module.
-
-    For example in :
-        import numpy as np
-        x = np.linspace(1, 2)
-    The node <Name.np> is a representation of the numpy module.
-
-    :param node: node to test
-    :return: True if the node is a representation of the numpy module.
-    """
-    module_nickname = node.name
-    potential_import_target = [
-        x for x in node.lookup(module_nickname)[1] if isinstance(x, astroid.Import)
-    ]
-    for target in potential_import_target:
-        if ("numpy", module_nickname) in target.names:
-            return True
-    return False
-
-
-def looks_like_numpy_member(
-    member_name: str, node: astroid.node_classes.NodeNG
-) -> bool:
-    """
-    Returns True if the node is a member of numpy whose
-    name is member_name.
-
-    :param member_name: name of the member
-    :param node: node to test
-    :return: True if the node is a member of numpy
-    """
-    return (
-        isinstance(node, astroid.Attribute)
-        and node.attrname == member_name
-        and isinstance(node.expr, astroid.Name)
-        and _is_a_numpy_module(node.expr)
-    )
diff --git a/venv/Lib/site-packages/astroid/brain/brain_pkg_resources.py b/venv/Lib/site-packages/astroid/brain/brain_pkg_resources.py
deleted file mode 100644
index 25e7649..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_pkg_resources.py
+++ /dev/null
@@ -1,75 +0,0 @@
-# Copyright (c) 2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-import astroid
-from astroid import parse
-from astroid import inference_tip
-from astroid import register_module_extender
-from astroid import MANAGER
-
-
-def pkg_resources_transform():
-    return parse(
-        """
-def require(*requirements):
-    return pkg_resources.working_set.require(*requirements)
-
-def run_script(requires, script_name):
-    return pkg_resources.working_set.run_script(requires, script_name)
-
-def iter_entry_points(group, name=None):
-    return pkg_resources.working_set.iter_entry_points(group, name)
-
-def resource_exists(package_or_requirement, resource_name):
-    return get_provider(package_or_requirement).has_resource(resource_name)
-
-def resource_isdir(package_or_requirement, resource_name):
-    return get_provider(package_or_requirement).resource_isdir(
-        resource_name)
-
-def resource_filename(package_or_requirement, resource_name):
-    return get_provider(package_or_requirement).get_resource_filename(
-        self, resource_name)
-
-def resource_stream(package_or_requirement, resource_name):
-    return get_provider(package_or_requirement).get_resource_stream(
-        self, resource_name)
-
-def resource_string(package_or_requirement, resource_name):
-    return get_provider(package_or_requirement).get_resource_string(
-        self, resource_name)
-
-def resource_listdir(package_or_requirement, resource_name):
-    return get_provider(package_or_requirement).resource_listdir(
-        resource_name)
-
-def extraction_error():
-    pass
-
-def get_cache_path(archive_name, names=()):
-    extract_path = self.extraction_path or get_default_cache()
-    target_path = os.path.join(extract_path, archive_name+'-tmp', *names)
-    return target_path
-
-def postprocess(tempname, filename):
-    pass
-
-def set_extraction_path(path):
-    pass
-
-def cleanup_resources(force=False):
-    pass
-
-def get_distribution(dist):
-    return Distribution(dist)
-
-_namespace_packages = {}
-"""
-    )
-
-
-register_module_extender(MANAGER, "pkg_resources", pkg_resources_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_pytest.py b/venv/Lib/site-packages/astroid/brain/brain_pytest.py
deleted file mode 100644
index d7e3ac8..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_pytest.py
+++ /dev/null
@@ -1,88 +0,0 @@
-# Copyright (c) 2014-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Jeff Quast <contact@jeffquast.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2016 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for pytest."""
-from __future__ import absolute_import
-from astroid import MANAGER, register_module_extender
-from astroid.builder import AstroidBuilder
-
-
-def pytest_transform():
-    return AstroidBuilder(MANAGER).string_build(
-        """
-
-try:
-    import _pytest.mark
-    import _pytest.recwarn
-    import _pytest.runner
-    import _pytest.python
-    import _pytest.skipping
-    import _pytest.assertion
-except ImportError:
-    pass
-else:
-    deprecated_call = _pytest.recwarn.deprecated_call
-    warns = _pytest.recwarn.warns
-
-    exit = _pytest.runner.exit
-    fail = _pytest.runner.fail
-    skip = _pytest.runner.skip
-    importorskip = _pytest.runner.importorskip
-
-    xfail = _pytest.skipping.xfail
-    mark = _pytest.mark.MarkGenerator()
-    raises = _pytest.python.raises
-
-    # New in pytest 3.0
-    try:
-        approx = _pytest.python.approx
-        register_assert_rewrite = _pytest.assertion.register_assert_rewrite
-    except AttributeError:
-        pass
-
-
-# Moved in pytest 3.0
-
-try:
-    import _pytest.freeze_support
-    freeze_includes = _pytest.freeze_support.freeze_includes
-except ImportError:
-    try:
-        import _pytest.genscript
-        freeze_includes = _pytest.genscript.freeze_includes
-    except ImportError:
-        pass
-
-try:
-    import _pytest.debugging
-    set_trace = _pytest.debugging.pytestPDB().set_trace
-except ImportError:
-    try:
-        import _pytest.pdb
-        set_trace = _pytest.pdb.pytestPDB().set_trace
-    except ImportError:
-        pass
-
-try:
-    import _pytest.fixtures
-    fixture = _pytest.fixtures.fixture
-    yield_fixture = _pytest.fixtures.yield_fixture
-except ImportError:
-    try:
-        import _pytest.python
-        fixture = _pytest.python.fixture
-        yield_fixture = _pytest.python.yield_fixture
-    except ImportError:
-        pass
-"""
-    )
-
-
-register_module_extender(MANAGER, "pytest", pytest_transform)
-register_module_extender(MANAGER, "py.test", pytest_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_qt.py b/venv/Lib/site-packages/astroid/brain/brain_qt.py
deleted file mode 100644
index 8679d14..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_qt.py
+++ /dev/null
@@ -1,82 +0,0 @@
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2017 Roy Wright <roy@wright.org>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for the PyQT library."""
-
-from astroid import MANAGER, register_module_extender
-from astroid.builder import AstroidBuilder
-from astroid import nodes
-from astroid import parse
-
-
-def _looks_like_signal(node, signal_name="pyqtSignal"):
-    if "__class__" in node.instance_attrs:
-        try:
-            cls = node.instance_attrs["__class__"][0]
-            return cls.name == signal_name
-        except AttributeError:
-            # return False if the cls does not have a name attribute
-            pass
-    return False
-
-
-def transform_pyqt_signal(node):
-    module = parse(
-        """
-    class pyqtSignal(object):
-        def connect(self, slot, type=None, no_receiver_check=False):
-            pass
-        def disconnect(self, slot):
-            pass
-        def emit(self, *args):
-            pass
-    """
-    )
-    signal_cls = module["pyqtSignal"]
-    node.instance_attrs["emit"] = signal_cls["emit"]
-    node.instance_attrs["disconnect"] = signal_cls["disconnect"]
-    node.instance_attrs["connect"] = signal_cls["connect"]
-
-
-def transform_pyside_signal(node):
-    module = parse(
-        """
-    class NotPySideSignal(object):
-        def connect(self, receiver, type=None):
-            pass
-        def disconnect(self, receiver):
-            pass
-        def emit(self, *args):
-            pass
-    """
-    )
-    signal_cls = module["NotPySideSignal"]
-    node.instance_attrs["connect"] = signal_cls["connect"]
-    node.instance_attrs["disconnect"] = signal_cls["disconnect"]
-    node.instance_attrs["emit"] = signal_cls["emit"]
-
-
-def pyqt4_qtcore_transform():
-    return AstroidBuilder(MANAGER).string_build(
-        """
-
-def SIGNAL(signal_name): pass
-
-class QObject(object):
-    def emit(self, signal): pass
-"""
-    )
-
-
-register_module_extender(MANAGER, "PyQt4.QtCore", pyqt4_qtcore_transform)
-MANAGER.register_transform(nodes.FunctionDef, transform_pyqt_signal, _looks_like_signal)
-MANAGER.register_transform(
-    nodes.ClassDef,
-    transform_pyside_signal,
-    lambda node: node.qname() in ("PySide.QtCore.Signal", "PySide2.QtCore.Signal"),
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_random.py b/venv/Lib/site-packages/astroid/brain/brain_random.py
deleted file mode 100644
index 5ec858a..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_random.py
+++ /dev/null
@@ -1,75 +0,0 @@
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import random
-
-import astroid
-from astroid import helpers
-from astroid import MANAGER
-
-
-ACCEPTED_ITERABLES_FOR_SAMPLE = (astroid.List, astroid.Set, astroid.Tuple)
-
-
-def _clone_node_with_lineno(node, parent, lineno):
-    cls = node.__class__
-    other_fields = node._other_fields
-    _astroid_fields = node._astroid_fields
-    init_params = {"lineno": lineno, "col_offset": node.col_offset, "parent": parent}
-    postinit_params = {param: getattr(node, param) for param in _astroid_fields}
-    if other_fields:
-        init_params.update({param: getattr(node, param) for param in other_fields})
-    new_node = cls(**init_params)
-    if hasattr(node, "postinit") and _astroid_fields:
-        new_node.postinit(**postinit_params)
-    return new_node
-
-
-def infer_random_sample(node, context=None):
-    if len(node.args) != 2:
-        raise astroid.UseInferenceDefault
-
-    length = node.args[1]
-    if not isinstance(length, astroid.Const):
-        raise astroid.UseInferenceDefault
-    if not isinstance(length.value, int):
-        raise astroid.UseInferenceDefault
-
-    inferred_sequence = helpers.safe_infer(node.args[0], context=context)
-    if not inferred_sequence:
-        raise astroid.UseInferenceDefault
-
-    if not isinstance(inferred_sequence, ACCEPTED_ITERABLES_FOR_SAMPLE):
-        raise astroid.UseInferenceDefault
-
-    if length.value > len(inferred_sequence.elts):
-        # In this case, this will raise a ValueError
-        raise astroid.UseInferenceDefault
-
-    try:
-        elts = random.sample(inferred_sequence.elts, length.value)
-    except ValueError:
-        raise astroid.UseInferenceDefault
-
-    new_node = astroid.List(
-        lineno=node.lineno, col_offset=node.col_offset, parent=node.scope()
-    )
-    new_elts = [
-        _clone_node_with_lineno(elt, parent=new_node, lineno=new_node.lineno)
-        for elt in elts
-    ]
-    new_node.postinit(new_elts)
-    return iter((new_node,))
-
-
-def _looks_like_random_sample(node):
-    func = node.func
-    if isinstance(func, astroid.Attribute):
-        return func.attrname == "sample"
-    if isinstance(func, astroid.Name):
-        return func.name == "sample"
-    return False
-
-
-MANAGER.register_transform(
-    astroid.Call, astroid.inference_tip(infer_random_sample), _looks_like_random_sample
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_re.py b/venv/Lib/site-packages/astroid/brain/brain_re.py
deleted file mode 100644
index c7ee51a..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_re.py
+++ /dev/null
@@ -1,36 +0,0 @@
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import sys
-import astroid
-
-PY36 = sys.version_info >= (3, 6)
-
-if PY36:
-    # Since Python 3.6 there is the RegexFlag enum
-    # where every entry will be exposed via updating globals()
-
-    def _re_transform():
-        return astroid.parse(
-            """
-        import sre_compile
-        ASCII = sre_compile.SRE_FLAG_ASCII
-        IGNORECASE = sre_compile.SRE_FLAG_IGNORECASE
-        LOCALE = sre_compile.SRE_FLAG_LOCALE
-        UNICODE = sre_compile.SRE_FLAG_UNICODE
-        MULTILINE = sre_compile.SRE_FLAG_MULTILINE
-        DOTALL = sre_compile.SRE_FLAG_DOTALL
-        VERBOSE = sre_compile.SRE_FLAG_VERBOSE
-        A = ASCII
-        I = IGNORECASE
-        L = LOCALE
-        U = UNICODE
-        M = MULTILINE
-        S = DOTALL
-        X = VERBOSE
-        TEMPLATE = sre_compile.SRE_FLAG_TEMPLATE
-        T = TEMPLATE
-        DEBUG = sre_compile.SRE_FLAG_DEBUG
-        """
-        )
-
-    astroid.register_module_extender(astroid.MANAGER, "re", _re_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_six.py b/venv/Lib/site-packages/astroid/brain/brain_six.py
deleted file mode 100644
index b342fbf..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_six.py
+++ /dev/null
@@ -1,200 +0,0 @@
-# Copyright (c) 2014-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""Astroid hooks for six module."""
-
-from textwrap import dedent
-
-from astroid import MANAGER, register_module_extender
-from astroid.builder import AstroidBuilder
-from astroid.exceptions import (
-    AstroidBuildingError,
-    InferenceError,
-    AttributeInferenceError,
-)
-from astroid import nodes
-
-
-SIX_ADD_METACLASS = "six.add_metaclass"
-
-
-def _indent(text, prefix, predicate=None):
-    """Adds 'prefix' to the beginning of selected lines in 'text'.
-
-    If 'predicate' is provided, 'prefix' will only be added to the lines
-    where 'predicate(line)' is True. If 'predicate' is not provided,
-    it will default to adding 'prefix' to all non-empty lines that do not
-    consist solely of whitespace characters.
-    """
-    if predicate is None:
-        predicate = lambda line: line.strip()
-
-    def prefixed_lines():
-        for line in text.splitlines(True):
-            yield prefix + line if predicate(line) else line
-
-    return "".join(prefixed_lines())
-
-
-_IMPORTS = """
-import _io
-cStringIO = _io.StringIO
-filter = filter
-from itertools import filterfalse
-input = input
-from sys import intern
-map = map
-range = range
-from imp import reload as reload_module
-from functools import reduce
-from shlex import quote as shlex_quote
-from io import StringIO
-from collections import UserDict, UserList, UserString
-xrange = range
-zip = zip
-from itertools import zip_longest
-import builtins
-import configparser
-import copyreg
-import _dummy_thread
-import http.cookiejar as http_cookiejar
-import http.cookies as http_cookies
-import html.entities as html_entities
-import html.parser as html_parser
-import http.client as http_client
-import http.server as http_server
-BaseHTTPServer = CGIHTTPServer = SimpleHTTPServer = http.server
-import pickle as cPickle
-import queue
-import reprlib
-import socketserver
-import _thread
-import winreg
-import xmlrpc.server as xmlrpc_server
-import xmlrpc.client as xmlrpc_client
-import urllib.robotparser as urllib_robotparser
-import email.mime.multipart as email_mime_multipart
-import email.mime.nonmultipart as email_mime_nonmultipart
-import email.mime.text as email_mime_text
-import email.mime.base as email_mime_base
-import urllib.parse as urllib_parse
-import urllib.error as urllib_error
-import tkinter
-import tkinter.dialog as tkinter_dialog
-import tkinter.filedialog as tkinter_filedialog
-import tkinter.scrolledtext as tkinter_scrolledtext
-import tkinter.simpledialog as tkinder_simpledialog
-import tkinter.tix as tkinter_tix
-import tkinter.ttk as tkinter_ttk
-import tkinter.constants as tkinter_constants
-import tkinter.dnd as tkinter_dnd
-import tkinter.colorchooser as tkinter_colorchooser
-import tkinter.commondialog as tkinter_commondialog
-import tkinter.filedialog as tkinter_tkfiledialog
-import tkinter.font as tkinter_font
-import tkinter.messagebox as tkinter_messagebox
-import urllib
-import urllib.request as urllib_request
-import urllib.robotparser as urllib_robotparser
-import urllib.parse as urllib_parse
-import urllib.error as urllib_error
-"""
-
-
-def six_moves_transform():
-    code = dedent(
-        """
-    class Moves(object):
-    {}
-    moves = Moves()
-    """
-    ).format(_indent(_IMPORTS, "    "))
-    module = AstroidBuilder(MANAGER).string_build(code)
-    module.name = "six.moves"
-    return module
-
-
-def _six_fail_hook(modname):
-    """Fix six.moves imports due to the dynamic nature of this
-    class.
-
-    Construct a pseudo-module which contains all the necessary imports
-    for six
-
-    :param modname: Name of failed module
-    :type modname: str
-
-    :return: An astroid module
-    :rtype: nodes.Module
-    """
-
-    attribute_of = modname != "six.moves" and modname.startswith("six.moves")
-    if modname != "six.moves" and not attribute_of:
-        raise AstroidBuildingError(modname=modname)
-    module = AstroidBuilder(MANAGER).string_build(_IMPORTS)
-    module.name = "six.moves"
-    if attribute_of:
-        # Facilitate import of submodules in Moves
-        start_index = len(module.name)
-        attribute = modname[start_index:].lstrip(".").replace(".", "_")
-        try:
-            import_attr = module.getattr(attribute)[0]
-        except AttributeInferenceError:
-            raise AstroidBuildingError(modname=modname)
-        if isinstance(import_attr, nodes.Import):
-            submodule = MANAGER.ast_from_module_name(import_attr.names[0][0])
-            return submodule
-    # Let dummy submodule imports pass through
-    # This will cause an Uninferable result, which is okay
-    return module
-
-
-def _looks_like_decorated_with_six_add_metaclass(node):
-    if not node.decorators:
-        return False
-
-    for decorator in node.decorators.nodes:
-        if not isinstance(decorator, nodes.Call):
-            continue
-        if decorator.func.as_string() == SIX_ADD_METACLASS:
-            return True
-    return False
-
-
-def transform_six_add_metaclass(node):
-    """Check if the given class node is decorated with *six.add_metaclass*
-
-    If so, inject its argument as the metaclass of the underlying class.
-    """
-    if not node.decorators:
-        return
-
-    for decorator in node.decorators.nodes:
-        if not isinstance(decorator, nodes.Call):
-            continue
-
-        try:
-            func = next(decorator.func.infer())
-        except InferenceError:
-            continue
-        if func.qname() == SIX_ADD_METACLASS and decorator.args:
-            metaclass = decorator.args[0]
-            node._metaclass = metaclass
-            return node
-
-
-register_module_extender(MANAGER, "six", six_moves_transform)
-register_module_extender(
-    MANAGER, "requests.packages.urllib3.packages.six", six_moves_transform
-)
-MANAGER.register_failed_import_hook(_six_fail_hook)
-MANAGER.register_transform(
-    nodes.ClassDef,
-    transform_six_add_metaclass,
-    _looks_like_decorated_with_six_add_metaclass,
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_ssl.py b/venv/Lib/site-packages/astroid/brain/brain_ssl.py
deleted file mode 100644
index 893d8a2..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_ssl.py
+++ /dev/null
@@ -1,74 +0,0 @@
-# Copyright (c) 2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for the ssl library."""
-
-from astroid import MANAGER, register_module_extender
-from astroid.builder import AstroidBuilder
-from astroid import nodes
-from astroid import parse
-
-
-def ssl_transform():
-    return parse(
-        """
-    from _ssl import OPENSSL_VERSION_NUMBER, OPENSSL_VERSION_INFO, OPENSSL_VERSION
-    from _ssl import _SSLContext, MemoryBIO
-    from _ssl import (
-        SSLError, SSLZeroReturnError, SSLWantReadError, SSLWantWriteError,
-        SSLSyscallError, SSLEOFError,
-        )
-    from _ssl import CERT_NONE, CERT_OPTIONAL, CERT_REQUIRED
-    from _ssl import txt2obj as _txt2obj, nid2obj as _nid2obj
-    from _ssl import RAND_status, RAND_add, RAND_bytes, RAND_pseudo_bytes
-    try:
-        from _ssl import RAND_egd
-    except ImportError:
-        # LibreSSL does not provide RAND_egd
-        pass
-    from _ssl import (OP_ALL, OP_CIPHER_SERVER_PREFERENCE,
-                      OP_NO_COMPRESSION, OP_NO_SSLv2, OP_NO_SSLv3,
-                      OP_NO_TLSv1, OP_NO_TLSv1_1, OP_NO_TLSv1_2,
-                      OP_SINGLE_DH_USE, OP_SINGLE_ECDH_USE)
-
-    from _ssl import (ALERT_DESCRIPTION_ACCESS_DENIED, ALERT_DESCRIPTION_BAD_CERTIFICATE,
-                      ALERT_DESCRIPTION_BAD_CERTIFICATE_HASH_VALUE,
-                      ALERT_DESCRIPTION_BAD_CERTIFICATE_STATUS_RESPONSE,
-                      ALERT_DESCRIPTION_BAD_RECORD_MAC,
-                      ALERT_DESCRIPTION_CERTIFICATE_EXPIRED,
-                      ALERT_DESCRIPTION_CERTIFICATE_REVOKED,
-                      ALERT_DESCRIPTION_CERTIFICATE_UNKNOWN,
-                      ALERT_DESCRIPTION_CERTIFICATE_UNOBTAINABLE,
-                      ALERT_DESCRIPTION_CLOSE_NOTIFY, ALERT_DESCRIPTION_DECODE_ERROR,
-                      ALERT_DESCRIPTION_DECOMPRESSION_FAILURE,
-                      ALERT_DESCRIPTION_DECRYPT_ERROR,
-                      ALERT_DESCRIPTION_HANDSHAKE_FAILURE,
-                      ALERT_DESCRIPTION_ILLEGAL_PARAMETER,
-                      ALERT_DESCRIPTION_INSUFFICIENT_SECURITY,
-                      ALERT_DESCRIPTION_INTERNAL_ERROR,
-                      ALERT_DESCRIPTION_NO_RENEGOTIATION,
-                      ALERT_DESCRIPTION_PROTOCOL_VERSION,
-                      ALERT_DESCRIPTION_RECORD_OVERFLOW,
-                      ALERT_DESCRIPTION_UNEXPECTED_MESSAGE,
-                      ALERT_DESCRIPTION_UNKNOWN_CA,
-                      ALERT_DESCRIPTION_UNKNOWN_PSK_IDENTITY,
-                      ALERT_DESCRIPTION_UNRECOGNIZED_NAME,
-                      ALERT_DESCRIPTION_UNSUPPORTED_CERTIFICATE,
-                      ALERT_DESCRIPTION_UNSUPPORTED_EXTENSION,
-                      ALERT_DESCRIPTION_USER_CANCELLED)
-    from _ssl import (SSL_ERROR_EOF, SSL_ERROR_INVALID_ERROR_CODE, SSL_ERROR_SSL,
-                      SSL_ERROR_SYSCALL, SSL_ERROR_WANT_CONNECT, SSL_ERROR_WANT_READ,
-                      SSL_ERROR_WANT_WRITE, SSL_ERROR_WANT_X509_LOOKUP, SSL_ERROR_ZERO_RETURN)
-    from _ssl import VERIFY_CRL_CHECK_CHAIN, VERIFY_CRL_CHECK_LEAF, VERIFY_DEFAULT, VERIFY_X509_STRICT
-    from _ssl import HAS_SNI, HAS_ECDH, HAS_NPN, HAS_ALPN
-    from _ssl import _OPENSSL_API_VERSION
-    from _ssl import PROTOCOL_SSLv23, PROTOCOL_TLSv1, PROTOCOL_TLSv1_1, PROTOCOL_TLSv1_2
-    from _ssl import PROTOCOL_TLS, PROTOCOL_TLS_CLIENT, PROTOCOL_TLS_SERVER
-    """
-    )
-
-
-register_module_extender(MANAGER, "ssl", ssl_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_subprocess.py b/venv/Lib/site-packages/astroid/brain/brain_subprocess.py
deleted file mode 100644
index c14dc55..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_subprocess.py
+++ /dev/null
@@ -1,111 +0,0 @@
-# Copyright (c) 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2017 Hugo <hugovk@users.noreply.github.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-import sys
-import textwrap
-
-import astroid
-
-
-PY37 = sys.version_info >= (3, 7)
-PY36 = sys.version_info >= (3, 6)
-
-
-def _subprocess_transform():
-    communicate = (bytes("string", "ascii"), bytes("string", "ascii"))
-    communicate_signature = "def communicate(self, input=None, timeout=None)"
-    if PY37:
-        init = """
-        def __init__(self, args, bufsize=0, executable=None,
-                     stdin=None, stdout=None, stderr=None,
-                     preexec_fn=None, close_fds=False, shell=False,
-                     cwd=None, env=None, universal_newlines=False,
-                     startupinfo=None, creationflags=0, restore_signals=True,
-                     start_new_session=False, pass_fds=(), *,
-                     encoding=None, errors=None, text=None):
-            pass
-        """
-    elif PY36:
-        init = """
-        def __init__(self, args, bufsize=0, executable=None,
-                     stdin=None, stdout=None, stderr=None,
-                     preexec_fn=None, close_fds=False, shell=False,
-                     cwd=None, env=None, universal_newlines=False,
-                     startupinfo=None, creationflags=0, restore_signals=True,
-                     start_new_session=False, pass_fds=(), *,
-                     encoding=None, errors=None):
-            pass
-        """
-    else:
-        init = """
-        def __init__(self, args, bufsize=0, executable=None,
-                     stdin=None, stdout=None, stderr=None,
-                     preexec_fn=None, close_fds=False, shell=False,
-                     cwd=None, env=None, universal_newlines=False,
-                     startupinfo=None, creationflags=0, restore_signals=True,
-                     start_new_session=False, pass_fds=()):
-            pass
-        """
-    wait_signature = "def wait(self, timeout=None)"
-    ctx_manager = """
-        def __enter__(self): return self
-        def __exit__(self, *args): pass
-    """
-    py3_args = "args = []"
-    code = textwrap.dedent(
-        """
-    def check_output(
-        args, *,
-        stdin=None,
-        stderr=None,
-        shell=False,
-        cwd=None,
-        encoding=None,
-        errors=None,
-        universal_newlines=False,
-        timeout=None,
-        env=None
-    ):
-
-        if universal_newlines:
-            return ""
-        return b""
-    class Popen(object):
-        returncode = pid = 0
-        stdin = stdout = stderr = file()
-        %(py3_args)s
-
-        %(communicate_signature)s:
-            return %(communicate)r
-        %(wait_signature)s:
-            return self.returncode
-        def poll(self):
-            return self.returncode
-        def send_signal(self, signal):
-            pass
-        def terminate(self):
-            pass
-        def kill(self):
-            pass
-        %(ctx_manager)s
-       """
-        % {
-            "communicate": communicate,
-            "communicate_signature": communicate_signature,
-            "wait_signature": wait_signature,
-            "ctx_manager": ctx_manager,
-            "py3_args": py3_args,
-        }
-    )
-
-    init_lines = textwrap.dedent(init).splitlines()
-    indented_init = "\n".join(" " * 4 + line for line in init_lines)
-    code += indented_init
-    return astroid.parse(code)
-
-
-astroid.register_module_extender(astroid.MANAGER, "subprocess", _subprocess_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_threading.py b/venv/Lib/site-packages/astroid/brain/brain_threading.py
deleted file mode 100644
index dffa55a..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_threading.py
+++ /dev/null
@@ -1,31 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-import astroid
-
-
-def _thread_transform():
-    return astroid.parse(
-        """
-    class lock(object):
-        def acquire(self, blocking=True, timeout=-1):
-            pass
-        def release(self):
-            pass
-        def __enter__(self):
-            return True
-        def __exit__(self, *args):
-            pass
-        def locked(self):
-            return False
-
-    def Lock():
-        return lock()
-    """
-    )
-
-
-astroid.register_module_extender(astroid.MANAGER, "threading", _thread_transform)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_typing.py b/venv/Lib/site-packages/astroid/brain/brain_typing.py
deleted file mode 100644
index 9ff7227..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_typing.py
+++ /dev/null
@@ -1,96 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2017-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 David Euresti <github@euresti.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-"""Astroid hooks for typing.py support."""
-import typing
-
-from astroid import (
-    MANAGER,
-    UseInferenceDefault,
-    extract_node,
-    inference_tip,
-    nodes,
-    InferenceError,
-)
-
-
-TYPING_NAMEDTUPLE_BASENAMES = {"NamedTuple", "typing.NamedTuple"}
-TYPING_TYPEVARS = {"TypeVar", "NewType"}
-TYPING_TYPEVARS_QUALIFIED = {"typing.TypeVar", "typing.NewType"}
-TYPING_TYPE_TEMPLATE = """
-class Meta(type):
-    def __getitem__(self, item):
-        return self
-
-    @property
-    def __args__(self):
-        return ()
-
-class {0}(metaclass=Meta):
-    pass
-"""
-TYPING_MEMBERS = set(typing.__all__)
-
-
-def looks_like_typing_typevar_or_newtype(node):
-    func = node.func
-    if isinstance(func, nodes.Attribute):
-        return func.attrname in TYPING_TYPEVARS
-    if isinstance(func, nodes.Name):
-        return func.name in TYPING_TYPEVARS
-    return False
-
-
-def infer_typing_typevar_or_newtype(node, context=None):
-    """Infer a typing.TypeVar(...) or typing.NewType(...) call"""
-    try:
-        func = next(node.func.infer(context=context))
-    except InferenceError as exc:
-        raise UseInferenceDefault from exc
-
-    if func.qname() not in TYPING_TYPEVARS_QUALIFIED:
-        raise UseInferenceDefault
-    if not node.args:
-        raise UseInferenceDefault
-
-    typename = node.args[0].as_string().strip("'")
-    node = extract_node(TYPING_TYPE_TEMPLATE.format(typename))
-    return node.infer(context=context)
-
-
-def _looks_like_typing_subscript(node):
-    """Try to figure out if a Subscript node *might* be a typing-related subscript"""
-    if isinstance(node, nodes.Name):
-        return node.name in TYPING_MEMBERS
-    elif isinstance(node, nodes.Attribute):
-        return node.attrname in TYPING_MEMBERS
-    elif isinstance(node, nodes.Subscript):
-        return _looks_like_typing_subscript(node.value)
-    return False
-
-
-def infer_typing_attr(node, context=None):
-    """Infer a typing.X[...] subscript"""
-    try:
-        value = next(node.value.infer())
-    except InferenceError as exc:
-        raise UseInferenceDefault from exc
-
-    if not value.qname().startswith("typing."):
-        raise UseInferenceDefault
-
-    node = extract_node(TYPING_TYPE_TEMPLATE.format(value.qname().split(".")[-1]))
-    return node.infer(context=context)
-
-
-MANAGER.register_transform(
-    nodes.Call,
-    inference_tip(infer_typing_typevar_or_newtype),
-    looks_like_typing_typevar_or_newtype,
-)
-MANAGER.register_transform(
-    nodes.Subscript, inference_tip(infer_typing_attr), _looks_like_typing_subscript
-)
diff --git a/venv/Lib/site-packages/astroid/brain/brain_uuid.py b/venv/Lib/site-packages/astroid/brain/brain_uuid.py
deleted file mode 100644
index 8bda631..0000000
--- a/venv/Lib/site-packages/astroid/brain/brain_uuid.py
+++ /dev/null
@@ -1,20 +0,0 @@
-# Copyright (c) 2017 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Astroid hooks for the UUID module."""
-
-
-from astroid import MANAGER
-from astroid import nodes
-
-
-def _patch_uuid_class(node):
-    # The .int member is patched using __dict__
-    node.locals["int"] = [nodes.Const(0, parent=node)]
-
-
-MANAGER.register_transform(
-    nodes.ClassDef, _patch_uuid_class, lambda node: node.qname() == "uuid.UUID"
-)
diff --git a/venv/Lib/site-packages/astroid/builder.py b/venv/Lib/site-packages/astroid/builder.py
deleted file mode 100644
index ac71093..0000000
--- a/venv/Lib/site-packages/astroid/builder.py
+++ /dev/null
@@ -1,435 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013 Phil Schaf <flying-sheep@web.de>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014-2015 Google, Inc.
-# Copyright (c) 2014 Alexander Presnyakov <flagist0@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""The AstroidBuilder makes astroid from living object and / or from _ast
-
-The builder is not thread safe and can't be used to parse different sources
-at the same time.
-"""
-
-import os
-import textwrap
-from tokenize import detect_encoding
-
-from astroid._ast import _parse
-from astroid import bases
-from astroid import exceptions
-from astroid import manager
-from astroid import modutils
-from astroid import raw_building
-from astroid import rebuilder
-from astroid import nodes
-from astroid import util
-
-# The name of the transient function that is used to
-# wrap expressions to be extracted when calling
-# extract_node.
-_TRANSIENT_FUNCTION = "__"
-
-# The comment used to select a statement to be extracted
-# when calling extract_node.
-_STATEMENT_SELECTOR = "#@"
-
-MANAGER = manager.AstroidManager()
-
-
-def open_source_file(filename):
-    with open(filename, "rb") as byte_stream:
-        encoding = detect_encoding(byte_stream.readline)[0]
-    stream = open(filename, "r", newline=None, encoding=encoding)
-    data = stream.read()
-    return stream, encoding, data
-
-
-def _can_assign_attr(node, attrname):
-    try:
-        slots = node.slots()
-    except NotImplementedError:
-        pass
-    else:
-        if slots and attrname not in {slot.value for slot in slots}:
-            return False
-    return True
-
-
-class AstroidBuilder(raw_building.InspectBuilder):
-    """Class for building an astroid tree from source code or from a live module.
-
-    The param *manager* specifies the manager class which should be used.
-    If no manager is given, then the default one will be used. The
-    param *apply_transforms* determines if the transforms should be
-    applied after the tree was built from source or from a live object,
-    by default being True.
-    """
-
-    # pylint: disable=redefined-outer-name
-    def __init__(self, manager=None, apply_transforms=True):
-        super(AstroidBuilder, self).__init__()
-        self._manager = manager or MANAGER
-        self._apply_transforms = apply_transforms
-
-    def module_build(self, module, modname=None):
-        """Build an astroid from a living module instance."""
-        node = None
-        path = getattr(module, "__file__", None)
-        if path is not None:
-            path_, ext = os.path.splitext(modutils._path_from_filename(path))
-            if ext in (".py", ".pyc", ".pyo") and os.path.exists(path_ + ".py"):
-                node = self.file_build(path_ + ".py", modname)
-        if node is None:
-            # this is a built-in module
-            # get a partial representation by introspection
-            node = self.inspect_build(module, modname=modname, path=path)
-            if self._apply_transforms:
-                # We have to handle transformation by ourselves since the
-                # rebuilder isn't called for builtin nodes
-                node = self._manager.visit_transforms(node)
-        return node
-
-    def file_build(self, path, modname=None):
-        """Build astroid from a source code file (i.e. from an ast)
-
-        *path* is expected to be a python source file
-        """
-        try:
-            stream, encoding, data = open_source_file(path)
-        except IOError as exc:
-            raise exceptions.AstroidBuildingError(
-                "Unable to load file {path}:\n{error}",
-                modname=modname,
-                path=path,
-                error=exc,
-            ) from exc
-        except (SyntaxError, LookupError) as exc:
-            raise exceptions.AstroidSyntaxError(
-                "Python 3 encoding specification error or unknown encoding:\n"
-                "{error}",
-                modname=modname,
-                path=path,
-                error=exc,
-            ) from exc
-        except UnicodeError as exc:  # wrong encoding
-            # detect_encoding returns utf-8 if no encoding specified
-            raise exceptions.AstroidBuildingError(
-                "Wrong or no encoding specified for {filename}.", filename=path
-            ) from exc
-        with stream:
-            # get module name if necessary
-            if modname is None:
-                try:
-                    modname = ".".join(modutils.modpath_from_file(path))
-                except ImportError:
-                    modname = os.path.splitext(os.path.basename(path))[0]
-            # build astroid representation
-            module = self._data_build(data, modname, path)
-            return self._post_build(module, encoding)
-
-    def string_build(self, data, modname="", path=None):
-        """Build astroid from source code string."""
-        module = self._data_build(data, modname, path)
-        module.file_bytes = data.encode("utf-8")
-        return self._post_build(module, "utf-8")
-
-    def _post_build(self, module, encoding):
-        """Handles encoding and delayed nodes after a module has been built"""
-        module.file_encoding = encoding
-        self._manager.cache_module(module)
-        # post tree building steps after we stored the module in the cache:
-        for from_node in module._import_from_nodes:
-            if from_node.modname == "__future__":
-                for symbol, _ in from_node.names:
-                    module.future_imports.add(symbol)
-            self.add_from_names_to_locals(from_node)
-        # handle delayed assattr nodes
-        for delayed in module._delayed_assattr:
-            self.delayed_assattr(delayed)
-
-        # Visit the transforms
-        if self._apply_transforms:
-            module = self._manager.visit_transforms(module)
-        return module
-
-    def _data_build(self, data, modname, path):
-        """Build tree node from data and add some informations"""
-        try:
-            node = _parse(data + "\n")
-        except (TypeError, ValueError, SyntaxError) as exc:
-            raise exceptions.AstroidSyntaxError(
-                "Parsing Python code failed:\n{error}",
-                source=data,
-                modname=modname,
-                path=path,
-                error=exc,
-            ) from exc
-        if path is not None:
-            node_file = os.path.abspath(path)
-        else:
-            node_file = "<?>"
-        if modname.endswith(".__init__"):
-            modname = modname[:-9]
-            package = True
-        else:
-            package = (
-                path is not None
-                and os.path.splitext(os.path.basename(path))[0] == "__init__"
-            )
-        builder = rebuilder.TreeRebuilder(self._manager)
-        module = builder.visit_module(node, modname, node_file, package)
-        module._import_from_nodes = builder._import_from_nodes
-        module._delayed_assattr = builder._delayed_assattr
-        return module
-
-    def add_from_names_to_locals(self, node):
-        """Store imported names to the locals
-
-        Resort the locals if coming from a delayed node
-        """
-        _key_func = lambda node: node.fromlineno
-
-        def sort_locals(my_list):
-            my_list.sort(key=_key_func)
-
-        for (name, asname) in node.names:
-            if name == "*":
-                try:
-                    imported = node.do_import_module()
-                except exceptions.AstroidBuildingError:
-                    continue
-                for name in imported.public_names():
-                    node.parent.set_local(name, node)
-                    sort_locals(node.parent.scope().locals[name])
-            else:
-                node.parent.set_local(asname or name, node)
-                sort_locals(node.parent.scope().locals[asname or name])
-
-    def delayed_assattr(self, node):
-        """Visit a AssAttr node
-
-        This adds name to locals and handle members definition.
-        """
-        try:
-            frame = node.frame()
-            for inferred in node.expr.infer():
-                if inferred is util.Uninferable:
-                    continue
-                try:
-                    if inferred.__class__ is bases.Instance:
-                        inferred = inferred._proxied
-                        iattrs = inferred.instance_attrs
-                        if not _can_assign_attr(inferred, node.attrname):
-                            continue
-                    elif isinstance(inferred, bases.Instance):
-                        # Const, Tuple, ... we may be wrong, may be not, but
-                        # anyway we don't want to pollute builtin's namespace
-                        continue
-                    elif inferred.is_function:
-                        iattrs = inferred.instance_attrs
-                    else:
-                        iattrs = inferred.locals
-                except AttributeError:
-                    # XXX log error
-                    continue
-                values = iattrs.setdefault(node.attrname, [])
-                if node in values:
-                    continue
-                # get assign in __init__ first XXX useful ?
-                if (
-                    frame.name == "__init__"
-                    and values
-                    and values[0].frame().name != "__init__"
-                ):
-                    values.insert(0, node)
-                else:
-                    values.append(node)
-        except exceptions.InferenceError:
-            pass
-
-
-def build_namespace_package_module(name, path):
-    return nodes.Module(name, doc="", path=path, package=True)
-
-
-def parse(code, module_name="", path=None, apply_transforms=True):
-    """Parses a source string in order to obtain an astroid AST from it
-
-    :param str code: The code for the module.
-    :param str module_name: The name for the module, if any
-    :param str path: The path for the module
-    :param bool apply_transforms:
-        Apply the transforms for the give code. Use it if you
-        don't want the default transforms to be applied.
-    """
-    code = textwrap.dedent(code)
-    builder = AstroidBuilder(manager=MANAGER, apply_transforms=apply_transforms)
-    return builder.string_build(code, modname=module_name, path=path)
-
-
-def _extract_expressions(node):
-    """Find expressions in a call to _TRANSIENT_FUNCTION and extract them.
-
-    The function walks the AST recursively to search for expressions that
-    are wrapped into a call to _TRANSIENT_FUNCTION. If it finds such an
-    expression, it completely removes the function call node from the tree,
-    replacing it by the wrapped expression inside the parent.
-
-    :param node: An astroid node.
-    :type node:  astroid.bases.NodeNG
-    :yields: The sequence of wrapped expressions on the modified tree
-    expression can be found.
-    """
-    if (
-        isinstance(node, nodes.Call)
-        and isinstance(node.func, nodes.Name)
-        and node.func.name == _TRANSIENT_FUNCTION
-    ):
-        real_expr = node.args[0]
-        real_expr.parent = node.parent
-        # Search for node in all _astng_fields (the fields checked when
-        # get_children is called) of its parent. Some of those fields may
-        # be lists or tuples, in which case the elements need to be checked.
-        # When we find it, replace it by real_expr, so that the AST looks
-        # like no call to _TRANSIENT_FUNCTION ever took place.
-        for name in node.parent._astroid_fields:
-            child = getattr(node.parent, name)
-            if isinstance(child, (list, tuple)):
-                for idx, compound_child in enumerate(child):
-                    if compound_child is node:
-                        child[idx] = real_expr
-            elif child is node:
-                setattr(node.parent, name, real_expr)
-        yield real_expr
-    else:
-        for child in node.get_children():
-            yield from _extract_expressions(child)
-
-
-def _find_statement_by_line(node, line):
-    """Extracts the statement on a specific line from an AST.
-
-    If the line number of node matches line, it will be returned;
-    otherwise its children are iterated and the function is called
-    recursively.
-
-    :param node: An astroid node.
-    :type node: astroid.bases.NodeNG
-    :param line: The line number of the statement to extract.
-    :type line: int
-    :returns: The statement on the line, or None if no statement for the line
-      can be found.
-    :rtype:  astroid.bases.NodeNG or None
-    """
-    if isinstance(node, (nodes.ClassDef, nodes.FunctionDef)):
-        # This is an inaccuracy in the AST: the nodes that can be
-        # decorated do not carry explicit information on which line
-        # the actual definition (class/def), but .fromline seems to
-        # be close enough.
-        node_line = node.fromlineno
-    else:
-        node_line = node.lineno
-
-    if node_line == line:
-        return node
-
-    for child in node.get_children():
-        result = _find_statement_by_line(child, line)
-        if result:
-            return result
-
-    return None
-
-
-def extract_node(code, module_name=""):
-    """Parses some Python code as a module and extracts a designated AST node.
-
-    Statements:
-     To extract one or more statement nodes, append #@ to the end of the line
-
-     Examples:
-       >>> def x():
-       >>>   def y():
-       >>>     return 1 #@
-
-       The return statement will be extracted.
-
-       >>> class X(object):
-       >>>   def meth(self): #@
-       >>>     pass
-
-      The function object 'meth' will be extracted.
-
-    Expressions:
-     To extract arbitrary expressions, surround them with the fake
-     function call __(...). After parsing, the surrounded expression
-     will be returned and the whole AST (accessible via the returned
-     node's parent attribute) will look like the function call was
-     never there in the first place.
-
-     Examples:
-       >>> a = __(1)
-
-       The const node will be extracted.
-
-       >>> def x(d=__(foo.bar)): pass
-
-       The node containing the default argument will be extracted.
-
-       >>> def foo(a, b):
-       >>>   return 0 < __(len(a)) < b
-
-       The node containing the function call 'len' will be extracted.
-
-    If no statements or expressions are selected, the last toplevel
-    statement will be returned.
-
-    If the selected statement is a discard statement, (i.e. an expression
-    turned into a statement), the wrapped expression is returned instead.
-
-    For convenience, singleton lists are unpacked.
-
-    :param str code: A piece of Python code that is parsed as
-    a module. Will be passed through textwrap.dedent first.
-    :param str module_name: The name of the module.
-    :returns: The designated node from the parse tree, or a list of nodes.
-    :rtype: astroid.bases.NodeNG, or a list of nodes.
-    """
-
-    def _extract(node):
-        if isinstance(node, nodes.Expr):
-            return node.value
-
-        return node
-
-    requested_lines = []
-    for idx, line in enumerate(code.splitlines()):
-        if line.strip().endswith(_STATEMENT_SELECTOR):
-            requested_lines.append(idx + 1)
-
-    tree = parse(code, module_name=module_name)
-    if not tree.body:
-        raise ValueError("Empty tree, cannot extract from it")
-
-    extracted = []
-    if requested_lines:
-        extracted = [_find_statement_by_line(tree, line) for line in requested_lines]
-
-    # Modifies the tree.
-    extracted.extend(_extract_expressions(tree))
-
-    if not extracted:
-        extracted.append(tree.body[-1])
-
-    extracted = [_extract(node) for node in extracted]
-    if len(extracted) == 1:
-        return extracted[0]
-    return extracted
diff --git a/venv/Lib/site-packages/astroid/context.py b/venv/Lib/site-packages/astroid/context.py
deleted file mode 100644
index 70a9208..0000000
--- a/venv/Lib/site-packages/astroid/context.py
+++ /dev/null
@@ -1,179 +0,0 @@
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Various context related utilities, including inference and call contexts."""
-import contextlib
-import pprint
-from typing import Optional
-
-
-class InferenceContext:
-    """Provide context for inference
-
-    Store already inferred nodes to save time
-    Account for already visited nodes to infinite stop infinite recursion
-    """
-
-    __slots__ = (
-        "path",
-        "lookupname",
-        "callcontext",
-        "boundnode",
-        "inferred",
-        "extra_context",
-    )
-
-    def __init__(self, path=None, inferred=None):
-        self.path = path or set()
-        """
-        :type: set(tuple(NodeNG, optional(str)))
-
-        Path of visited nodes and their lookupname
-
-        Currently this key is ``(node, context.lookupname)``
-        """
-        self.lookupname = None
-        """
-        :type: optional[str]
-
-        The original name of the node
-
-        e.g.
-        foo = 1
-        The inference of 'foo' is nodes.Const(1) but the lookup name is 'foo'
-        """
-        self.callcontext = None
-        """
-        :type: optional[CallContext]
-
-        The call arguments and keywords for the given context
-        """
-        self.boundnode = None
-        """
-        :type: optional[NodeNG]
-
-        The bound node of the given context
-
-        e.g. the bound node of object.__new__(cls) is the object node
-        """
-        self.inferred = inferred or {}
-        """
-        :type: dict(seq, seq)
-
-        Inferred node contexts to their mapped results
-        Currently the key is ``(node, lookupname, callcontext, boundnode)``
-        and the value is tuple of the inferred results
-        """
-        self.extra_context = {}
-        """
-        :type: dict(NodeNG, Context)
-
-        Context that needs to be passed down through call stacks
-        for call arguments
-        """
-
-    def push(self, node):
-        """Push node into inference path
-
-        :return: True if node is already in context path else False
-        :rtype: bool
-
-        Allows one to see if the given node has already
-        been looked at for this inference context"""
-        name = self.lookupname
-        if (node, name) in self.path:
-            return True
-
-        self.path.add((node, name))
-        return False
-
-    def clone(self):
-        """Clone inference path
-
-        For example, each side of a binary operation (BinOp)
-        starts with the same context but diverge as each side is inferred
-        so the InferenceContext will need be cloned"""
-        # XXX copy lookupname/callcontext ?
-        clone = InferenceContext(self.path, inferred=self.inferred)
-        clone.callcontext = self.callcontext
-        clone.boundnode = self.boundnode
-        clone.extra_context = self.extra_context
-        return clone
-
-    def cache_generator(self, key, generator):
-        """Cache result of generator into dictionary
-
-        Used to cache inference results"""
-        results = []
-        for result in generator:
-            results.append(result)
-            yield result
-
-        self.inferred[key] = tuple(results)
-
-    @contextlib.contextmanager
-    def restore_path(self):
-        path = set(self.path)
-        yield
-        self.path = path
-
-    def __str__(self):
-        state = (
-            "%s=%s"
-            % (field, pprint.pformat(getattr(self, field), width=80 - len(field)))
-            for field in self.__slots__
-        )
-        return "%s(%s)" % (type(self).__name__, ",\n    ".join(state))
-
-
-class CallContext:
-    """Holds information for a call site."""
-
-    __slots__ = ("args", "keywords")
-
-    def __init__(self, args, keywords=None):
-        """
-        :param List[NodeNG] args: Call positional arguments
-        :param Union[List[nodes.Keyword], None] keywords: Call keywords
-        """
-        self.args = args
-        if keywords:
-            keywords = [(arg.arg, arg.value) for arg in keywords]
-        else:
-            keywords = []
-        self.keywords = keywords
-
-
-def copy_context(context: Optional[InferenceContext]) -> InferenceContext:
-    """Clone a context if given, or return a fresh contexxt"""
-    if context is not None:
-        return context.clone()
-
-    return InferenceContext()
-
-
-def bind_context_to_node(context, node):
-    """Give a context a boundnode
-    to retrieve the correct function name or attribute value
-    with from further inference.
-
-    Do not use an existing context since the boundnode could then
-    be incorrectly propagated higher up in the call stack.
-
-    :param context: Context to use
-    :type context: Optional(context)
-
-    :param node: Node to do name lookups from
-    :type node NodeNG:
-
-    :returns: A new context
-    :rtype: InferenceContext
-    """
-    context = copy_context(context)
-    context.boundnode = node
-    return context
diff --git a/venv/Lib/site-packages/astroid/decorators.py b/venv/Lib/site-packages/astroid/decorators.py
deleted file mode 100644
index 1448757..0000000
--- a/venv/Lib/site-packages/astroid/decorators.py
+++ /dev/null
@@ -1,141 +0,0 @@
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2018 HoverHell <hoverhell@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-""" A few useful function/method decorators."""
-
-import functools
-
-import wrapt
-
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import util
-
-
-@wrapt.decorator
-def cached(func, instance, args, kwargs):
-    """Simple decorator to cache result of method calls without args."""
-    cache = getattr(instance, "__cache", None)
-    if cache is None:
-        instance.__cache = cache = {}
-    try:
-        return cache[func]
-    except KeyError:
-        cache[func] = result = func(*args, **kwargs)
-        return result
-
-
-class cachedproperty:
-    """ Provides a cached property equivalent to the stacking of
-    @cached and @property, but more efficient.
-
-    After first usage, the <property_name> becomes part of the object's
-    __dict__. Doing:
-
-      del obj.<property_name> empties the cache.
-
-    Idea taken from the pyramid_ framework and the mercurial_ project.
-
-    .. _pyramid: http://pypi.python.org/pypi/pyramid
-    .. _mercurial: http://pypi.python.org/pypi/Mercurial
-    """
-
-    __slots__ = ("wrapped",)
-
-    def __init__(self, wrapped):
-        try:
-            wrapped.__name__
-        except AttributeError as exc:
-            raise TypeError("%s must have a __name__ attribute" % wrapped) from exc
-        self.wrapped = wrapped
-
-    @property
-    def __doc__(self):
-        doc = getattr(self.wrapped, "__doc__", None)
-        return "<wrapped by the cachedproperty decorator>%s" % (
-            "\n%s" % doc if doc else ""
-        )
-
-    def __get__(self, inst, objtype=None):
-        if inst is None:
-            return self
-        val = self.wrapped(inst)
-        setattr(inst, self.wrapped.__name__, val)
-        return val
-
-
-def path_wrapper(func):
-    """return the given infer function wrapped to handle the path
-
-    Used to stop inference if the node has already been looked
-    at for a given `InferenceContext` to prevent infinite recursion
-    """
-
-    @functools.wraps(func)
-    def wrapped(node, context=None, _func=func, **kwargs):
-        """wrapper function handling context"""
-        if context is None:
-            context = contextmod.InferenceContext()
-        if context.push(node):
-            return None
-
-        yielded = set()
-        generator = _func(node, context, **kwargs)
-        try:
-            while True:
-                res = next(generator)
-                # unproxy only true instance, not const, tuple, dict...
-                if res.__class__.__name__ == "Instance":
-                    ares = res._proxied
-                else:
-                    ares = res
-                if ares not in yielded:
-                    yield res
-                    yielded.add(ares)
-        except StopIteration as error:
-            if error.args:
-                return error.args[0]
-            return None
-
-    return wrapped
-
-
-@wrapt.decorator
-def yes_if_nothing_inferred(func, instance, args, kwargs):
-    generator = func(*args, **kwargs)
-
-    try:
-        yield next(generator)
-    except StopIteration:
-        # generator is empty
-        yield util.Uninferable
-        return
-
-    yield from generator
-
-
-@wrapt.decorator
-def raise_if_nothing_inferred(func, instance, args, kwargs):
-    generator = func(*args, **kwargs)
-
-    try:
-        yield next(generator)
-    except StopIteration as error:
-        # generator is empty
-        if error.args:
-            # pylint: disable=not-a-mapping
-            raise exceptions.InferenceError(**error.args[0])
-        raise exceptions.InferenceError(
-            "StopIteration raised without any error information."
-        )
-
-    yield from generator
diff --git a/venv/Lib/site-packages/astroid/exceptions.py b/venv/Lib/site-packages/astroid/exceptions.py
deleted file mode 100644
index 7e9d655..0000000
--- a/venv/Lib/site-packages/astroid/exceptions.py
+++ /dev/null
@@ -1,230 +0,0 @@
-# Copyright (c) 2007, 2009-2010, 2013 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""this module contains exceptions used in the astroid library
-"""
-from astroid import util
-
-
-class AstroidError(Exception):
-    """base exception class for all astroid related exceptions
-
-    AstroidError and its subclasses are structured, intended to hold
-    objects representing state when the exception is thrown.  Field
-    values are passed to the constructor as keyword-only arguments.
-    Each subclass has its own set of standard fields, but use your
-    best judgment to decide whether a specific exception instance
-    needs more or fewer fields for debugging.  Field values may be
-    used to lazily generate the error message: self.message.format()
-    will be called with the field names and values supplied as keyword
-    arguments.
-    """
-
-    def __init__(self, message="", **kws):
-        super(AstroidError, self).__init__(message)
-        self.message = message
-        for key, value in kws.items():
-            setattr(self, key, value)
-
-    def __str__(self):
-        return self.message.format(**vars(self))
-
-
-class AstroidBuildingError(AstroidError):
-    """exception class when we are unable to build an astroid representation
-
-    Standard attributes:
-        modname: Name of the module that AST construction failed for.
-        error: Exception raised during construction.
-    """
-
-    def __init__(self, message="Failed to import module {modname}.", **kws):
-        super(AstroidBuildingError, self).__init__(message, **kws)
-
-
-class AstroidImportError(AstroidBuildingError):
-    """Exception class used when a module can't be imported by astroid."""
-
-
-class TooManyLevelsError(AstroidImportError):
-    """Exception class which is raised when a relative import was beyond the top-level.
-
-    Standard attributes:
-        level: The level which was attempted.
-        name: the name of the module on which the relative import was attempted.
-    """
-
-    level = None
-    name = None
-
-    def __init__(
-        self,
-        message="Relative import with too many levels " "({level}) for module {name!r}",
-        **kws
-    ):
-        super(TooManyLevelsError, self).__init__(message, **kws)
-
-
-class AstroidSyntaxError(AstroidBuildingError):
-    """Exception class used when a module can't be parsed."""
-
-
-class NoDefault(AstroidError):
-    """raised by function's `default_value` method when an argument has
-    no default value
-
-    Standard attributes:
-        func: Function node.
-        name: Name of argument without a default.
-    """
-
-    func = None
-    name = None
-
-    def __init__(self, message="{func!r} has no default for {name!r}.", **kws):
-        super(NoDefault, self).__init__(message, **kws)
-
-
-class ResolveError(AstroidError):
-    """Base class of astroid resolution/inference error.
-
-    ResolveError is not intended to be raised.
-
-    Standard attributes:
-        context: InferenceContext object.
-    """
-
-    context = None
-
-
-class MroError(ResolveError):
-    """Error raised when there is a problem with method resolution of a class.
-
-    Standard attributes:
-        mros: A sequence of sequences containing ClassDef nodes.
-        cls: ClassDef node whose MRO resolution failed.
-        context: InferenceContext object.
-    """
-
-    mros = ()
-    cls = None
-
-    def __str__(self):
-        mro_names = ", ".join(
-            "({})".format(", ".join(b.name for b in m)) for m in self.mros
-        )
-        return self.message.format(mros=mro_names, cls=self.cls)
-
-
-class DuplicateBasesError(MroError):
-    """Error raised when there are duplicate bases in the same class bases."""
-
-
-class InconsistentMroError(MroError):
-    """Error raised when a class's MRO is inconsistent."""
-
-
-class SuperError(ResolveError):
-    """Error raised when there is a problem with a *super* call.
-
-    Standard attributes:
-        *super_*: The Super instance that raised the exception.
-        context: InferenceContext object.
-    """
-
-    super_ = None
-
-    def __str__(self):
-        return self.message.format(**vars(self.super_))
-
-
-class InferenceError(ResolveError):
-    """raised when we are unable to infer a node
-
-    Standard attributes:
-        node: The node inference was called on.
-        context: InferenceContext object.
-    """
-
-    node = None
-    context = None
-
-    def __init__(self, message="Inference failed for {node!r}.", **kws):
-        super(InferenceError, self).__init__(message, **kws)
-
-
-# Why does this inherit from InferenceError rather than ResolveError?
-# Changing it causes some inference tests to fail.
-class NameInferenceError(InferenceError):
-    """Raised when a name lookup fails, corresponds to NameError.
-
-    Standard attributes:
-        name: The name for which lookup failed, as a string.
-        scope: The node representing the scope in which the lookup occurred.
-        context: InferenceContext object.
-    """
-
-    name = None
-    scope = None
-
-    def __init__(self, message="{name!r} not found in {scope!r}.", **kws):
-        super(NameInferenceError, self).__init__(message, **kws)
-
-
-class AttributeInferenceError(ResolveError):
-    """Raised when an attribute lookup fails, corresponds to AttributeError.
-
-    Standard attributes:
-        target: The node for which lookup failed.
-        attribute: The attribute for which lookup failed, as a string.
-        context: InferenceContext object.
-    """
-
-    target = None
-    attribute = None
-
-    def __init__(self, message="{attribute!r} not found on {target!r}.", **kws):
-        super(AttributeInferenceError, self).__init__(message, **kws)
-
-
-class UseInferenceDefault(Exception):
-    """exception to be raised in custom inference function to indicate that it
-    should go back to the default behaviour
-    """
-
-
-class _NonDeducibleTypeHierarchy(Exception):
-    """Raised when is_subtype / is_supertype can't deduce the relation between two types."""
-
-
-class AstroidIndexError(AstroidError):
-    """Raised when an Indexable / Mapping does not have an index / key."""
-
-
-class AstroidTypeError(AstroidError):
-    """Raised when a TypeError would be expected in Python code."""
-
-
-class InferenceOverwriteError(AstroidError):
-    """Raised when an inference tip is overwritten
-
-    Currently only used for debugging.
-    """
-
-
-# Backwards-compatibility aliases
-OperationError = util.BadOperationMessage
-UnaryOperationError = util.BadUnaryOperationMessage
-BinaryOperationError = util.BadBinaryOperationMessage
-
-SuperArgumentTypeError = SuperError
-UnresolvableName = NameInferenceError
-NotFoundError = AttributeInferenceError
-AstroidBuildingException = AstroidBuildingError
diff --git a/venv/Lib/site-packages/astroid/helpers.py b/venv/Lib/site-packages/astroid/helpers.py
deleted file mode 100644
index be133b3..0000000
--- a/venv/Lib/site-packages/astroid/helpers.py
+++ /dev/null
@@ -1,273 +0,0 @@
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""
-Various helper utilities.
-"""
-
-import builtins as builtins_mod
-
-from astroid import bases
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import manager
-from astroid import nodes
-from astroid import raw_building
-from astroid import scoped_nodes
-from astroid import util
-
-
-BUILTINS = builtins_mod.__name__
-
-
-def _build_proxy_class(cls_name, builtins):
-    proxy = raw_building.build_class(cls_name)
-    proxy.parent = builtins
-    return proxy
-
-
-def _function_type(function, builtins):
-    if isinstance(function, scoped_nodes.Lambda):
-        if function.root().name == BUILTINS:
-            cls_name = "builtin_function_or_method"
-        else:
-            cls_name = "function"
-    elif isinstance(function, bases.BoundMethod):
-        cls_name = "method"
-    elif isinstance(function, bases.UnboundMethod):
-        cls_name = "function"
-    return _build_proxy_class(cls_name, builtins)
-
-
-def _object_type(node, context=None):
-    astroid_manager = manager.AstroidManager()
-    builtins = astroid_manager.builtins_module
-    context = context or contextmod.InferenceContext()
-
-    for inferred in node.infer(context=context):
-        if isinstance(inferred, scoped_nodes.ClassDef):
-            if inferred.newstyle:
-                metaclass = inferred.metaclass(context=context)
-                if metaclass:
-                    yield metaclass
-                    continue
-            yield builtins.getattr("type")[0]
-        elif isinstance(inferred, (scoped_nodes.Lambda, bases.UnboundMethod)):
-            yield _function_type(inferred, builtins)
-        elif isinstance(inferred, scoped_nodes.Module):
-            yield _build_proxy_class("module", builtins)
-        else:
-            yield inferred._proxied
-
-
-def object_type(node, context=None):
-    """Obtain the type of the given node
-
-    This is used to implement the ``type`` builtin, which means that it's
-    used for inferring type calls, as well as used in a couple of other places
-    in the inference.
-    The node will be inferred first, so this function can support all
-    sorts of objects, as long as they support inference.
-    """
-
-    try:
-        types = set(_object_type(node, context))
-    except exceptions.InferenceError:
-        return util.Uninferable
-    if len(types) > 1 or not types:
-        return util.Uninferable
-    return list(types)[0]
-
-
-def _object_type_is_subclass(obj_type, class_or_seq, context=None):
-    if not isinstance(class_or_seq, (tuple, list)):
-        class_seq = (class_or_seq,)
-    else:
-        class_seq = class_or_seq
-
-    if obj_type is util.Uninferable:
-        return util.Uninferable
-
-    # Instances are not types
-    class_seq = [
-        item if not isinstance(item, bases.Instance) else util.Uninferable
-        for item in class_seq
-    ]
-    # strict compatibility with issubclass
-    # issubclass(type, (object, 1)) evaluates to true
-    # issubclass(object, (1, type)) raises TypeError
-    for klass in class_seq:
-        if klass is util.Uninferable:
-            raise exceptions.AstroidTypeError("arg 2 must be a type or tuple of types")
-
-        for obj_subclass in obj_type.mro():
-            if obj_subclass == klass:
-                return True
-    return False
-
-
-def object_isinstance(node, class_or_seq, context=None):
-    """Check if a node 'isinstance' any node in class_or_seq
-
-    :param node: A given node
-    :param class_or_seq: Union[nodes.NodeNG, Sequence[nodes.NodeNG]]
-    :rtype: bool
-
-    :raises AstroidTypeError: if the given ``classes_or_seq`` are not types
-    """
-    obj_type = object_type(node, context)
-    if obj_type is util.Uninferable:
-        return util.Uninferable
-    return _object_type_is_subclass(obj_type, class_or_seq, context=context)
-
-
-def object_issubclass(node, class_or_seq, context=None):
-    """Check if a type is a subclass of any node in class_or_seq
-
-    :param node: A given node
-    :param class_or_seq: Union[Nodes.NodeNG, Sequence[nodes.NodeNG]]
-    :rtype: bool
-
-    :raises AstroidTypeError: if the given ``classes_or_seq`` are not types
-    :raises AstroidError: if the type of the given node cannot be inferred
-        or its type's mro doesn't work
-    """
-    if not isinstance(node, nodes.ClassDef):
-        raise TypeError("{node} needs to be a ClassDef node".format(node=node))
-    return _object_type_is_subclass(node, class_or_seq, context=context)
-
-
-def safe_infer(node, context=None):
-    """Return the inferred value for the given node.
-
-    Return None if inference failed or if there is some ambiguity (more than
-    one node has been inferred).
-    """
-    try:
-        inferit = node.infer(context=context)
-        value = next(inferit)
-    except exceptions.InferenceError:
-        return None
-    try:
-        next(inferit)
-        return None  # None if there is ambiguity on the inferred node
-    except exceptions.InferenceError:
-        return None  # there is some kind of ambiguity
-    except StopIteration:
-        return value
-
-
-def has_known_bases(klass, context=None):
-    """Return true if all base classes of a class could be inferred."""
-    try:
-        return klass._all_bases_known
-    except AttributeError:
-        pass
-    for base in klass.bases:
-        result = safe_infer(base, context=context)
-        # TODO: check for A->B->A->B pattern in class structure too?
-        if (
-            not isinstance(result, scoped_nodes.ClassDef)
-            or result is klass
-            or not has_known_bases(result, context=context)
-        ):
-            klass._all_bases_known = False
-            return False
-    klass._all_bases_known = True
-    return True
-
-
-def _type_check(type1, type2):
-    if not all(map(has_known_bases, (type1, type2))):
-        raise exceptions._NonDeducibleTypeHierarchy
-
-    if not all([type1.newstyle, type2.newstyle]):
-        return False
-    try:
-        return type1 in type2.mro()[:-1]
-    except exceptions.MroError:
-        # The MRO is invalid.
-        raise exceptions._NonDeducibleTypeHierarchy
-
-
-def is_subtype(type1, type2):
-    """Check if *type1* is a subtype of *type2*."""
-    return _type_check(type1=type2, type2=type1)
-
-
-def is_supertype(type1, type2):
-    """Check if *type2* is a supertype of *type1*."""
-    return _type_check(type1, type2)
-
-
-def class_instance_as_index(node):
-    """Get the value as an index for the given instance.
-
-    If an instance provides an __index__ method, then it can
-    be used in some scenarios where an integer is expected,
-    for instance when multiplying or subscripting a list.
-    """
-    context = contextmod.InferenceContext()
-    context.callcontext = contextmod.CallContext(args=[node])
-
-    try:
-        for inferred in node.igetattr("__index__", context=context):
-            if not isinstance(inferred, bases.BoundMethod):
-                continue
-
-            for result in inferred.infer_call_result(node, context=context):
-                if isinstance(result, nodes.Const) and isinstance(result.value, int):
-                    return result
-    except exceptions.InferenceError:
-        pass
-    return None
-
-
-def object_len(node, context=None):
-    """Infer length of given node object
-
-    :param Union[nodes.ClassDef, nodes.Instance] node:
-    :param node: Node to infer length of
-
-    :raises AstroidTypeError: If an invalid node is returned
-        from __len__ method or no __len__ method exists
-    :raises InferenceError: If the given node cannot be inferred
-        or if multiple nodes are inferred
-    :rtype int: Integer length of node
-    """
-    # pylint: disable=import-outside-toplevel; circular import
-    from astroid.objects import FrozenSet
-
-    inferred_node = safe_infer(node, context=context)
-    if inferred_node is None or inferred_node is util.Uninferable:
-        raise exceptions.InferenceError(node=node)
-    if isinstance(inferred_node, nodes.Const) and isinstance(
-        inferred_node.value, (bytes, str)
-    ):
-        return len(inferred_node.value)
-    if isinstance(inferred_node, (nodes.List, nodes.Set, nodes.Tuple, FrozenSet)):
-        return len(inferred_node.elts)
-    if isinstance(inferred_node, nodes.Dict):
-        return len(inferred_node.items)
-    try:
-        node_type = object_type(inferred_node, context=context)
-        len_call = next(node_type.igetattr("__len__", context=context))
-    except exceptions.AttributeInferenceError:
-        raise exceptions.AstroidTypeError(
-            "object of type '{}' has no len()".format(len_call.pytype())
-        )
-
-    result_of_len = next(len_call.infer_call_result(node, context))
-    if (
-        isinstance(result_of_len, nodes.Const)
-        and result_of_len.pytype() == "builtins.int"
-    ):
-        return result_of_len.value
-    raise exceptions.AstroidTypeError(
-        "'{}' object cannot be interpreted as an integer".format(result_of_len)
-    )
diff --git a/venv/Lib/site-packages/astroid/inference.py b/venv/Lib/site-packages/astroid/inference.py
deleted file mode 100644
index 77c6b1d..0000000
--- a/venv/Lib/site-packages/astroid/inference.py
+++ /dev/null
@@ -1,943 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2017 Michał Masłowski <m.maslowski@clearcode.cc>
-# Copyright (c) 2017 Calen Pennington <cale@edx.org>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2018 HoverHell <hoverhell@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""this module contains a set of functions to handle inference on astroid trees
-"""
-
-import functools
-import itertools
-import operator
-
-from astroid import bases
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import decorators
-from astroid import helpers
-from astroid import manager
-from astroid import nodes
-from astroid.interpreter import dunder_lookup
-from astroid import protocols
-from astroid import util
-
-
-MANAGER = manager.AstroidManager()
-
-
-# .infer method ###############################################################
-
-
-def infer_end(self, context=None):
-    """inference's end for node such as Module, ClassDef, FunctionDef,
-    Const...
-
-    """
-    yield self
-
-
-nodes.Module._infer = infer_end
-nodes.ClassDef._infer = infer_end
-nodes.FunctionDef._infer = infer_end
-nodes.Lambda._infer = infer_end
-nodes.Const._infer = infer_end
-nodes.Slice._infer = infer_end
-
-
-def _infer_sequence_helper(node, context=None):
-    """Infer all values based on _BaseContainer.elts"""
-    values = []
-
-    for elt in node.elts:
-        if isinstance(elt, nodes.Starred):
-            starred = helpers.safe_infer(elt.value, context)
-            if not starred:
-                raise exceptions.InferenceError(node=node, context=context)
-            if not hasattr(starred, "elts"):
-                raise exceptions.InferenceError(node=node, context=context)
-            values.extend(_infer_sequence_helper(starred))
-        elif isinstance(elt, nodes.NamedExpr):
-            value = helpers.safe_infer(elt.value, context)
-            if not value:
-                raise exceptions.InferenceError(node=node, context=context)
-            values.append(value)
-        else:
-            values.append(elt)
-    return values
-
-
-@decorators.raise_if_nothing_inferred
-def infer_sequence(self, context=None):
-    has_starred_named_expr = any(
-        isinstance(e, (nodes.Starred, nodes.NamedExpr)) for e in self.elts
-    )
-    if has_starred_named_expr:
-        values = _infer_sequence_helper(self, context)
-        new_seq = type(self)(
-            lineno=self.lineno, col_offset=self.col_offset, parent=self.parent
-        )
-        new_seq.postinit(values)
-
-        yield new_seq
-    else:
-        yield self
-
-
-nodes.List._infer = infer_sequence
-nodes.Tuple._infer = infer_sequence
-nodes.Set._infer = infer_sequence
-
-
-def infer_map(self, context=None):
-    if not any(isinstance(k, nodes.DictUnpack) for k, _ in self.items):
-        yield self
-    else:
-        items = _infer_map(self, context)
-        new_seq = type(self)(self.lineno, self.col_offset, self.parent)
-        new_seq.postinit(list(items.items()))
-        yield new_seq
-
-
-def _update_with_replacement(lhs_dict, rhs_dict):
-    """Delete nodes that equate to duplicate keys
-
-    Since an astroid node doesn't 'equal' another node with the same value,
-    this function uses the as_string method to make sure duplicate keys
-    don't get through
-
-    Note that both the key and the value are astroid nodes
-
-    Fixes issue with DictUnpack causing duplicte keys
-    in inferred Dict items
-
-    :param dict(nodes.NodeNG, nodes.NodeNG) lhs_dict: Dictionary to 'merge' nodes into
-    :param dict(nodes.NodeNG, nodes.NodeNG) rhs_dict: Dictionary with nodes to pull from
-    :return dict(nodes.NodeNG, nodes.NodeNG): merged dictionary of nodes
-    """
-    combined_dict = itertools.chain(lhs_dict.items(), rhs_dict.items())
-    # Overwrite keys which have the same string values
-    string_map = {key.as_string(): (key, value) for key, value in combined_dict}
-    # Return to dictionary
-    return dict(string_map.values())
-
-
-def _infer_map(node, context):
-    """Infer all values based on Dict.items"""
-    values = {}
-    for name, value in node.items:
-        if isinstance(name, nodes.DictUnpack):
-            double_starred = helpers.safe_infer(value, context)
-            if not double_starred:
-                raise exceptions.InferenceError
-            if not isinstance(double_starred, nodes.Dict):
-                raise exceptions.InferenceError(node=node, context=context)
-            unpack_items = _infer_map(double_starred, context)
-            values = _update_with_replacement(values, unpack_items)
-        else:
-            key = helpers.safe_infer(name, context=context)
-            value = helpers.safe_infer(value, context=context)
-            if any(not elem for elem in (key, value)):
-                raise exceptions.InferenceError(node=node, context=context)
-            values = _update_with_replacement(values, {key: value})
-    return values
-
-
-nodes.Dict._infer = infer_map
-
-
-def _higher_function_scope(node):
-    """ Search for the first function which encloses the given
-    scope. This can be used for looking up in that function's
-    scope, in case looking up in a lower scope for a particular
-    name fails.
-
-    :param node: A scope node.
-    :returns:
-        ``None``, if no parent function scope was found,
-        otherwise an instance of :class:`astroid.scoped_nodes.Function`,
-        which encloses the given node.
-    """
-    current = node
-    while current.parent and not isinstance(current.parent, nodes.FunctionDef):
-        current = current.parent
-    if current and current.parent:
-        return current.parent
-    return None
-
-
-def infer_name(self, context=None):
-    """infer a Name: use name lookup rules"""
-    frame, stmts = self.lookup(self.name)
-    if not stmts:
-        # Try to see if the name is enclosed in a nested function
-        # and use the higher (first function) scope for searching.
-        parent_function = _higher_function_scope(self.scope())
-        if parent_function:
-            _, stmts = parent_function.lookup(self.name)
-
-        if not stmts:
-            raise exceptions.NameInferenceError(
-                name=self.name, scope=self.scope(), context=context
-            )
-    context = contextmod.copy_context(context)
-    context.lookupname = self.name
-    return bases._infer_stmts(stmts, context, frame)
-
-
-# pylint: disable=no-value-for-parameter
-nodes.Name._infer = decorators.raise_if_nothing_inferred(
-    decorators.path_wrapper(infer_name)
-)
-nodes.AssignName.infer_lhs = infer_name  # won't work with a path wrapper
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_call(self, context=None):
-    """infer a Call node by trying to guess what the function returns"""
-    callcontext = contextmod.copy_context(context)
-    callcontext.callcontext = contextmod.CallContext(
-        args=self.args, keywords=self.keywords
-    )
-    callcontext.boundnode = None
-    if context is not None:
-        callcontext.extra_context = _populate_context_lookup(self, context.clone())
-
-    for callee in self.func.infer(context):
-        if callee is util.Uninferable:
-            yield callee
-            continue
-        try:
-            if hasattr(callee, "infer_call_result"):
-                yield from callee.infer_call_result(caller=self, context=callcontext)
-        except exceptions.InferenceError:
-            continue
-    return dict(node=self, context=context)
-
-
-nodes.Call._infer = infer_call
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_import(self, context=None, asname=True):
-    """infer an Import node: return the imported module/object"""
-    name = context.lookupname
-    if name is None:
-        raise exceptions.InferenceError(node=self, context=context)
-
-    try:
-        if asname:
-            yield self.do_import_module(self.real_name(name))
-        else:
-            yield self.do_import_module(name)
-    except exceptions.AstroidBuildingError as exc:
-        raise exceptions.InferenceError(node=self, context=context) from exc
-
-
-nodes.Import._infer = infer_import
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_import_from(self, context=None, asname=True):
-    """infer a ImportFrom node: return the imported module/object"""
-    name = context.lookupname
-    if name is None:
-        raise exceptions.InferenceError(node=self, context=context)
-    if asname:
-        name = self.real_name(name)
-
-    try:
-        module = self.do_import_module()
-    except exceptions.AstroidBuildingError as exc:
-        raise exceptions.InferenceError(node=self, context=context) from exc
-
-    try:
-        context = contextmod.copy_context(context)
-        context.lookupname = name
-        stmts = module.getattr(name, ignore_locals=module is self.root())
-        return bases._infer_stmts(stmts, context)
-    except exceptions.AttributeInferenceError as error:
-        raise exceptions.InferenceError(
-            error.message, target=self, attribute=name, context=context
-        ) from error
-
-
-nodes.ImportFrom._infer = infer_import_from
-
-
-def infer_attribute(self, context=None):
-    """infer an Attribute node by using getattr on the associated object"""
-    for owner in self.expr.infer(context):
-        if owner is util.Uninferable:
-            yield owner
-            continue
-
-        if context and context.boundnode:
-            # This handles the situation where the attribute is accessed through a subclass
-            # of a base class and the attribute is defined at the base class's level,
-            # by taking in consideration a redefinition in the subclass.
-            if isinstance(owner, bases.Instance) and isinstance(
-                context.boundnode, bases.Instance
-            ):
-                try:
-                    if helpers.is_subtype(
-                        helpers.object_type(context.boundnode),
-                        helpers.object_type(owner),
-                    ):
-                        owner = context.boundnode
-                except exceptions._NonDeducibleTypeHierarchy:
-                    # Can't determine anything useful.
-                    pass
-
-        try:
-            context.boundnode = owner
-            yield from owner.igetattr(self.attrname, context)
-            context.boundnode = None
-        except (exceptions.AttributeInferenceError, exceptions.InferenceError):
-            context.boundnode = None
-        except AttributeError:
-            # XXX method / function
-            context.boundnode = None
-    return dict(node=self, context=context)
-
-
-nodes.Attribute._infer = decorators.raise_if_nothing_inferred(
-    decorators.path_wrapper(infer_attribute)
-)
-# won't work with a path wrapper
-nodes.AssignAttr.infer_lhs = decorators.raise_if_nothing_inferred(infer_attribute)
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_global(self, context=None):
-    if context.lookupname is None:
-        raise exceptions.InferenceError(node=self, context=context)
-    try:
-        return bases._infer_stmts(self.root().getattr(context.lookupname), context)
-    except exceptions.AttributeInferenceError as error:
-        raise exceptions.InferenceError(
-            error.message, target=self, attribute=context.lookupname, context=context
-        ) from error
-
-
-nodes.Global._infer = infer_global
-
-
-_SUBSCRIPT_SENTINEL = object()
-
-
-@decorators.raise_if_nothing_inferred
-def infer_subscript(self, context=None):
-    """Inference for subscripts
-
-    We're understanding if the index is a Const
-    or a slice, passing the result of inference
-    to the value's `getitem` method, which should
-    handle each supported index type accordingly.
-    """
-
-    found_one = False
-    for value in self.value.infer(context):
-        if value is util.Uninferable:
-            yield util.Uninferable
-            return None
-        for index in self.slice.infer(context):
-            if index is util.Uninferable:
-                yield util.Uninferable
-                return None
-
-            # Try to deduce the index value.
-            index_value = _SUBSCRIPT_SENTINEL
-            if value.__class__ == bases.Instance:
-                index_value = index
-            else:
-                if index.__class__ == bases.Instance:
-                    instance_as_index = helpers.class_instance_as_index(index)
-                    if instance_as_index:
-                        index_value = instance_as_index
-                else:
-                    index_value = index
-            if index_value is _SUBSCRIPT_SENTINEL:
-                raise exceptions.InferenceError(node=self, context=context)
-
-            try:
-                assigned = value.getitem(index_value, context)
-            except (
-                exceptions.AstroidTypeError,
-                exceptions.AstroidIndexError,
-                exceptions.AttributeInferenceError,
-                AttributeError,
-            ) as exc:
-                raise exceptions.InferenceError(node=self, context=context) from exc
-
-            # Prevent inferring if the inferred subscript
-            # is the same as the original subscripted object.
-            if self is assigned or assigned is util.Uninferable:
-                yield util.Uninferable
-                return None
-            yield from assigned.infer(context)
-            found_one = True
-
-    if found_one:
-        return dict(node=self, context=context)
-    return None
-
-
-nodes.Subscript._infer = decorators.path_wrapper(infer_subscript)
-nodes.Subscript.infer_lhs = infer_subscript
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def _infer_boolop(self, context=None):
-    """Infer a boolean operation (and / or / not).
-
-    The function will calculate the boolean operation
-    for all pairs generated through inference for each component
-    node.
-    """
-    values = self.values
-    if self.op == "or":
-        predicate = operator.truth
-    else:
-        predicate = operator.not_
-
-    try:
-        values = [value.infer(context=context) for value in values]
-    except exceptions.InferenceError:
-        yield util.Uninferable
-        return None
-
-    for pair in itertools.product(*values):
-        if any(item is util.Uninferable for item in pair):
-            # Can't infer the final result, just yield Uninferable.
-            yield util.Uninferable
-            continue
-
-        bool_values = [item.bool_value() for item in pair]
-        if any(item is util.Uninferable for item in bool_values):
-            # Can't infer the final result, just yield Uninferable.
-            yield util.Uninferable
-            continue
-
-        # Since the boolean operations are short circuited operations,
-        # this code yields the first value for which the predicate is True
-        # and if no value respected the predicate, then the last value will
-        # be returned (or Uninferable if there was no last value).
-        # This is conforming to the semantics of `and` and `or`:
-        #   1 and 0 -> 1
-        #   0 and 1 -> 0
-        #   1 or 0 -> 1
-        #   0 or 1 -> 1
-        value = util.Uninferable
-        for value, bool_value in zip(pair, bool_values):
-            if predicate(bool_value):
-                yield value
-                break
-        else:
-            yield value
-
-    return dict(node=self, context=context)
-
-
-nodes.BoolOp._infer = _infer_boolop
-
-
-# UnaryOp, BinOp and AugAssign inferences
-
-
-def _filter_operation_errors(self, infer_callable, context, error):
-    for result in infer_callable(self, context):
-        if isinstance(result, error):
-            # For the sake of .infer(), we don't care about operation
-            # errors, which is the job of pylint. So return something
-            # which shows that we can't infer the result.
-            yield util.Uninferable
-        else:
-            yield result
-
-
-def _infer_unaryop(self, context=None):
-    """Infer what an UnaryOp should return when evaluated."""
-    for operand in self.operand.infer(context):
-        try:
-            yield operand.infer_unary_op(self.op)
-        except TypeError as exc:
-            # The operand doesn't support this operation.
-            yield util.BadUnaryOperationMessage(operand, self.op, exc)
-        except AttributeError as exc:
-            meth = protocols.UNARY_OP_METHOD[self.op]
-            if meth is None:
-                # `not node`. Determine node's boolean
-                # value and negate its result, unless it is
-                # Uninferable, which will be returned as is.
-                bool_value = operand.bool_value()
-                if bool_value is not util.Uninferable:
-                    yield nodes.const_factory(not bool_value)
-                else:
-                    yield util.Uninferable
-            else:
-                if not isinstance(operand, (bases.Instance, nodes.ClassDef)):
-                    # The operation was used on something which
-                    # doesn't support it.
-                    yield util.BadUnaryOperationMessage(operand, self.op, exc)
-                    continue
-
-                try:
-                    try:
-                        methods = dunder_lookup.lookup(operand, meth)
-                    except exceptions.AttributeInferenceError:
-                        yield util.BadUnaryOperationMessage(operand, self.op, exc)
-                        continue
-
-                    meth = methods[0]
-                    inferred = next(meth.infer(context=context))
-                    if inferred is util.Uninferable or not inferred.callable():
-                        continue
-
-                    context = contextmod.copy_context(context)
-                    context.callcontext = contextmod.CallContext(args=[operand])
-                    call_results = inferred.infer_call_result(self, context=context)
-                    result = next(call_results, None)
-                    if result is None:
-                        # Failed to infer, return the same type.
-                        yield operand
-                    else:
-                        yield result
-                except exceptions.AttributeInferenceError as exc:
-                    # The unary operation special method was not found.
-                    yield util.BadUnaryOperationMessage(operand, self.op, exc)
-                except exceptions.InferenceError:
-                    yield util.Uninferable
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_unaryop(self, context=None):
-    """Infer what an UnaryOp should return when evaluated."""
-    yield from _filter_operation_errors(
-        self, _infer_unaryop, context, util.BadUnaryOperationMessage
-    )
-    return dict(node=self, context=context)
-
-
-nodes.UnaryOp._infer_unaryop = _infer_unaryop
-nodes.UnaryOp._infer = infer_unaryop
-
-
-def _is_not_implemented(const):
-    """Check if the given const node is NotImplemented."""
-    return isinstance(const, nodes.Const) and const.value is NotImplemented
-
-
-def _invoke_binop_inference(instance, opnode, op, other, context, method_name):
-    """Invoke binary operation inference on the given instance."""
-    methods = dunder_lookup.lookup(instance, method_name)
-    context = contextmod.bind_context_to_node(context, instance)
-    method = methods[0]
-    inferred = next(method.infer(context=context))
-    if inferred is util.Uninferable:
-        raise exceptions.InferenceError
-    return instance.infer_binary_op(opnode, op, other, context, inferred)
-
-
-def _aug_op(instance, opnode, op, other, context, reverse=False):
-    """Get an inference callable for an augmented binary operation."""
-    method_name = protocols.AUGMENTED_OP_METHOD[op]
-    return functools.partial(
-        _invoke_binop_inference,
-        instance=instance,
-        op=op,
-        opnode=opnode,
-        other=other,
-        context=context,
-        method_name=method_name,
-    )
-
-
-def _bin_op(instance, opnode, op, other, context, reverse=False):
-    """Get an inference callable for a normal binary operation.
-
-    If *reverse* is True, then the reflected method will be used instead.
-    """
-    if reverse:
-        method_name = protocols.REFLECTED_BIN_OP_METHOD[op]
-    else:
-        method_name = protocols.BIN_OP_METHOD[op]
-    return functools.partial(
-        _invoke_binop_inference,
-        instance=instance,
-        op=op,
-        opnode=opnode,
-        other=other,
-        context=context,
-        method_name=method_name,
-    )
-
-
-def _get_binop_contexts(context, left, right):
-    """Get contexts for binary operations.
-
-    This will return two inference contexts, the first one
-    for x.__op__(y), the other one for y.__rop__(x), where
-    only the arguments are inversed.
-    """
-    # The order is important, since the first one should be
-    # left.__op__(right).
-    for arg in (right, left):
-        new_context = context.clone()
-        new_context.callcontext = contextmod.CallContext(args=[arg])
-        new_context.boundnode = None
-        yield new_context
-
-
-def _same_type(type1, type2):
-    """Check if type1 is the same as type2."""
-    return type1.qname() == type2.qname()
-
-
-def _get_binop_flow(
-    left, left_type, binary_opnode, right, right_type, context, reverse_context
-):
-    """Get the flow for binary operations.
-
-    The rules are a bit messy:
-
-        * if left and right have the same type, then only one
-          method will be called, left.__op__(right)
-        * if left and right are unrelated typewise, then first
-          left.__op__(right) is tried and if this does not exist
-          or returns NotImplemented, then right.__rop__(left) is tried.
-        * if left is a subtype of right, then only left.__op__(right)
-          is tried.
-        * if left is a supertype of right, then right.__rop__(left)
-          is first tried and then left.__op__(right)
-    """
-    op = binary_opnode.op
-    if _same_type(left_type, right_type):
-        methods = [_bin_op(left, binary_opnode, op, right, context)]
-    elif helpers.is_subtype(left_type, right_type):
-        methods = [_bin_op(left, binary_opnode, op, right, context)]
-    elif helpers.is_supertype(left_type, right_type):
-        methods = [
-            _bin_op(right, binary_opnode, op, left, reverse_context, reverse=True),
-            _bin_op(left, binary_opnode, op, right, context),
-        ]
-    else:
-        methods = [
-            _bin_op(left, binary_opnode, op, right, context),
-            _bin_op(right, binary_opnode, op, left, reverse_context, reverse=True),
-        ]
-    return methods
-
-
-def _get_aug_flow(
-    left, left_type, aug_opnode, right, right_type, context, reverse_context
-):
-    """Get the flow for augmented binary operations.
-
-    The rules are a bit messy:
-
-        * if left and right have the same type, then left.__augop__(right)
-          is first tried and then left.__op__(right).
-        * if left and right are unrelated typewise, then
-          left.__augop__(right) is tried, then left.__op__(right)
-          is tried and then right.__rop__(left) is tried.
-        * if left is a subtype of right, then left.__augop__(right)
-          is tried and then left.__op__(right).
-        * if left is a supertype of right, then left.__augop__(right)
-          is tried, then right.__rop__(left) and then
-          left.__op__(right)
-    """
-    bin_op = aug_opnode.op.strip("=")
-    aug_op = aug_opnode.op
-    if _same_type(left_type, right_type):
-        methods = [
-            _aug_op(left, aug_opnode, aug_op, right, context),
-            _bin_op(left, aug_opnode, bin_op, right, context),
-        ]
-    elif helpers.is_subtype(left_type, right_type):
-        methods = [
-            _aug_op(left, aug_opnode, aug_op, right, context),
-            _bin_op(left, aug_opnode, bin_op, right, context),
-        ]
-    elif helpers.is_supertype(left_type, right_type):
-        methods = [
-            _aug_op(left, aug_opnode, aug_op, right, context),
-            _bin_op(right, aug_opnode, bin_op, left, reverse_context, reverse=True),
-            _bin_op(left, aug_opnode, bin_op, right, context),
-        ]
-    else:
-        methods = [
-            _aug_op(left, aug_opnode, aug_op, right, context),
-            _bin_op(left, aug_opnode, bin_op, right, context),
-            _bin_op(right, aug_opnode, bin_op, left, reverse_context, reverse=True),
-        ]
-    return methods
-
-
-def _infer_binary_operation(left, right, binary_opnode, context, flow_factory):
-    """Infer a binary operation between a left operand and a right operand
-
-    This is used by both normal binary operations and augmented binary
-    operations, the only difference is the flow factory used.
-    """
-
-    context, reverse_context = _get_binop_contexts(context, left, right)
-    left_type = helpers.object_type(left)
-    right_type = helpers.object_type(right)
-    methods = flow_factory(
-        left, left_type, binary_opnode, right, right_type, context, reverse_context
-    )
-    for method in methods:
-        try:
-            results = list(method())
-        except AttributeError:
-            continue
-        except exceptions.AttributeInferenceError:
-            continue
-        except exceptions.InferenceError:
-            yield util.Uninferable
-            return
-        else:
-            if any(result is util.Uninferable for result in results):
-                yield util.Uninferable
-                return
-
-            if all(map(_is_not_implemented, results)):
-                continue
-            not_implemented = sum(
-                1 for result in results if _is_not_implemented(result)
-            )
-            if not_implemented and not_implemented != len(results):
-                # Can't infer yet what this is.
-                yield util.Uninferable
-                return
-
-            yield from results
-            return
-    # The operation doesn't seem to be supported so let the caller know about it
-    yield util.BadBinaryOperationMessage(left_type, binary_opnode.op, right_type)
-
-
-def _infer_binop(self, context):
-    """Binary operation inference logic."""
-    left = self.left
-    right = self.right
-
-    # we use two separate contexts for evaluating lhs and rhs because
-    # 1. evaluating lhs may leave some undesired entries in context.path
-    #    which may not let us infer right value of rhs
-    context = context or contextmod.InferenceContext()
-    lhs_context = contextmod.copy_context(context)
-    rhs_context = contextmod.copy_context(context)
-    lhs_iter = left.infer(context=lhs_context)
-    rhs_iter = right.infer(context=rhs_context)
-    for lhs, rhs in itertools.product(lhs_iter, rhs_iter):
-        if any(value is util.Uninferable for value in (rhs, lhs)):
-            # Don't know how to process this.
-            yield util.Uninferable
-            return
-
-        try:
-            yield from _infer_binary_operation(lhs, rhs, self, context, _get_binop_flow)
-        except exceptions._NonDeducibleTypeHierarchy:
-            yield util.Uninferable
-
-
-@decorators.yes_if_nothing_inferred
-@decorators.path_wrapper
-def infer_binop(self, context=None):
-    return _filter_operation_errors(
-        self, _infer_binop, context, util.BadBinaryOperationMessage
-    )
-
-
-nodes.BinOp._infer_binop = _infer_binop
-nodes.BinOp._infer = infer_binop
-
-
-def _infer_augassign(self, context=None):
-    """Inference logic for augmented binary operations."""
-    if context is None:
-        context = contextmod.InferenceContext()
-
-    rhs_context = context.clone()
-
-    lhs_iter = self.target.infer_lhs(context=context)
-    rhs_iter = self.value.infer(context=rhs_context)
-    for lhs, rhs in itertools.product(lhs_iter, rhs_iter):
-        if any(value is util.Uninferable for value in (rhs, lhs)):
-            # Don't know how to process this.
-            yield util.Uninferable
-            return
-
-        try:
-            yield from _infer_binary_operation(
-                left=lhs,
-                right=rhs,
-                binary_opnode=self,
-                context=context,
-                flow_factory=_get_aug_flow,
-            )
-        except exceptions._NonDeducibleTypeHierarchy:
-            yield util.Uninferable
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_augassign(self, context=None):
-    return _filter_operation_errors(
-        self, _infer_augassign, context, util.BadBinaryOperationMessage
-    )
-
-
-nodes.AugAssign._infer_augassign = _infer_augassign
-nodes.AugAssign._infer = infer_augassign
-
-# End of binary operation inference.
-
-
-@decorators.raise_if_nothing_inferred
-def infer_arguments(self, context=None):
-    name = context.lookupname
-    if name is None:
-        raise exceptions.InferenceError(node=self, context=context)
-    return protocols._arguments_infer_argname(self, name, context)
-
-
-nodes.Arguments._infer = infer_arguments
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_assign(self, context=None):
-    """infer a AssignName/AssignAttr: need to inspect the RHS part of the
-    assign node
-    """
-    stmt = self.statement()
-    if isinstance(stmt, nodes.AugAssign):
-        return stmt.infer(context)
-
-    stmts = list(self.assigned_stmts(context=context))
-    return bases._infer_stmts(stmts, context)
-
-
-nodes.AssignName._infer = infer_assign
-nodes.AssignAttr._infer = infer_assign
-
-
-@decorators.raise_if_nothing_inferred
-@decorators.path_wrapper
-def infer_empty_node(self, context=None):
-    if not self.has_underlying_object():
-        yield util.Uninferable
-    else:
-        try:
-            yield from MANAGER.infer_ast_from_something(self.object, context=context)
-        except exceptions.AstroidError:
-            yield util.Uninferable
-
-
-nodes.EmptyNode._infer = infer_empty_node
-
-
-@decorators.raise_if_nothing_inferred
-def infer_index(self, context=None):
-    return self.value.infer(context)
-
-
-nodes.Index._infer = infer_index
-
-# TODO: move directly into bases.Instance when the dependency hell
-# will be solved.
-def instance_getitem(self, index, context=None):
-    # Rewrap index to Const for this case
-    new_context = contextmod.bind_context_to_node(context, self)
-    if not context:
-        context = new_context
-
-    # Create a new callcontext for providing index as an argument.
-    new_context.callcontext = contextmod.CallContext(args=[index])
-
-    method = next(self.igetattr("__getitem__", context=context), None)
-    if not isinstance(method, bases.BoundMethod):
-        raise exceptions.InferenceError(
-            "Could not find __getitem__ for {node!r}.", node=self, context=context
-        )
-
-    return next(method.infer_call_result(self, new_context))
-
-
-bases.Instance.getitem = instance_getitem
-
-
-def _populate_context_lookup(call, context):
-    # Allows context to be saved for later
-    # for inference inside a function
-    context_lookup = {}
-    if context is None:
-        return context_lookup
-    for arg in call.args:
-        if isinstance(arg, nodes.Starred):
-            context_lookup[arg.value] = context
-        else:
-            context_lookup[arg] = context
-    keywords = call.keywords if call.keywords is not None else []
-    for keyword in keywords:
-        context_lookup[keyword.value] = context
-    return context_lookup
-
-
-@decorators.raise_if_nothing_inferred
-def infer_ifexp(self, context=None):
-    """Support IfExp inference
-
-    If we can't infer the truthiness of the condition, we default
-    to inferring both branches. Otherwise, we infer either branch
-    depending on the condition.
-    """
-    both_branches = False
-    # We use two separate contexts for evaluating lhs and rhs because
-    # evaluating lhs may leave some undesired entries in context.path
-    # which may not let us infer right value of rhs.
-
-    context = context or contextmod.InferenceContext()
-    lhs_context = contextmod.copy_context(context)
-    rhs_context = contextmod.copy_context(context)
-    try:
-        test = next(self.test.infer(context=context.clone()))
-    except exceptions.InferenceError:
-        both_branches = True
-    else:
-        if test is not util.Uninferable:
-            if test.bool_value():
-                yield from self.body.infer(context=lhs_context)
-            else:
-                yield from self.orelse.infer(context=rhs_context)
-        else:
-            both_branches = True
-    if both_branches:
-        yield from self.body.infer(context=lhs_context)
-        yield from self.orelse.infer(context=rhs_context)
-
-
-nodes.IfExp._infer = infer_ifexp
diff --git a/venv/Lib/site-packages/astroid/interpreter/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/astroid/interpreter/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 1bd9d33..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/interpreter/__pycache__/dunder_lookup.cpython-37.pyc b/venv/Lib/site-packages/astroid/interpreter/__pycache__/dunder_lookup.cpython-37.pyc
deleted file mode 100644
index 4001903..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/__pycache__/dunder_lookup.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/interpreter/__pycache__/objectmodel.cpython-37.pyc b/venv/Lib/site-packages/astroid/interpreter/__pycache__/objectmodel.cpython-37.pyc
deleted file mode 100644
index dc15f91..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/__pycache__/objectmodel.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 6cdce33..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/spec.cpython-37.pyc b/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/spec.cpython-37.pyc
deleted file mode 100644
index 1f091df..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/spec.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/util.cpython-37.pyc b/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/util.cpython-37.pyc
deleted file mode 100644
index 2a7fdbb..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/_import/__pycache__/util.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/astroid/interpreter/_import/spec.py b/venv/Lib/site-packages/astroid/interpreter/_import/spec.py
deleted file mode 100644
index 84e093b..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/_import/spec.py
+++ /dev/null
@@ -1,344 +0,0 @@
-# Copyright (c) 2016-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017 Chris Philip <chrisp533@gmail.com>
-# Copyright (c) 2017 Hugo <hugovk@users.noreply.github.com>
-# Copyright (c) 2017 ioanatia <ioanatia@users.noreply.github.com>
-# Copyright (c) 2017 Calen Pennington <cale@edx.org>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-import abc
-import collections
-import distutils
-import enum
-import imp
-import os
-import sys
-import zipimport
-
-try:
-    import importlib.machinery
-
-    _HAS_MACHINERY = True
-except ImportError:
-    _HAS_MACHINERY = False
-
-try:
-    from functools import lru_cache
-except ImportError:
-    from backports.functools_lru_cache import lru_cache
-
-from . import util
-
-ModuleType = enum.Enum(
-    "ModuleType",
-    "C_BUILTIN C_EXTENSION PKG_DIRECTORY "
-    "PY_CODERESOURCE PY_COMPILED PY_FROZEN PY_RESOURCE "
-    "PY_SOURCE PY_ZIPMODULE PY_NAMESPACE",
-)
-_ImpTypes = {
-    imp.C_BUILTIN: ModuleType.C_BUILTIN,
-    imp.C_EXTENSION: ModuleType.C_EXTENSION,
-    imp.PKG_DIRECTORY: ModuleType.PKG_DIRECTORY,
-    imp.PY_COMPILED: ModuleType.PY_COMPILED,
-    imp.PY_FROZEN: ModuleType.PY_FROZEN,
-    imp.PY_SOURCE: ModuleType.PY_SOURCE,
-}
-if hasattr(imp, "PY_RESOURCE"):
-    _ImpTypes[imp.PY_RESOURCE] = ModuleType.PY_RESOURCE
-if hasattr(imp, "PY_CODERESOURCE"):
-    _ImpTypes[imp.PY_CODERESOURCE] = ModuleType.PY_CODERESOURCE
-
-
-def _imp_type_to_module_type(imp_type):
-    return _ImpTypes[imp_type]
-
-
-_ModuleSpec = collections.namedtuple(
-    "_ModuleSpec", "name type location " "origin submodule_search_locations"
-)
-
-
-class ModuleSpec(_ModuleSpec):
-    """Defines a class similar to PEP 420's ModuleSpec
-
-    A module spec defines a name of a module, its type, location
-    and where submodules can be found, if the module is a package.
-    """
-
-    def __new__(
-        cls,
-        name,
-        module_type,
-        location=None,
-        origin=None,
-        submodule_search_locations=None,
-    ):
-        return _ModuleSpec.__new__(
-            cls,
-            name=name,
-            type=module_type,
-            location=location,
-            origin=origin,
-            submodule_search_locations=submodule_search_locations,
-        )
-
-
-class Finder:
-    """A finder is a class which knows how to find a particular module."""
-
-    def __init__(self, path=None):
-        self._path = path or sys.path
-
-    @abc.abstractmethod
-    def find_module(self, modname, module_parts, processed, submodule_path):
-        """Find the given module
-
-        Each finder is responsible for each protocol of finding, as long as
-        they all return a ModuleSpec.
-
-        :param str modname: The module which needs to be searched.
-        :param list module_parts: It should be a list of strings,
-                                  where each part contributes to the module's
-                                  namespace.
-        :param list processed: What parts from the module parts were processed
-                               so far.
-        :param list submodule_path: A list of paths where the module
-                                    can be looked into.
-        :returns: A ModuleSpec, describing how and where the module was found,
-                  None, otherwise.
-        """
-
-    def contribute_to_path(self, spec, processed):
-        """Get a list of extra paths where this finder can search."""
-
-
-class ImpFinder(Finder):
-    """A finder based on the imp module."""
-
-    def find_module(self, modname, module_parts, processed, submodule_path):
-        if submodule_path is not None:
-            submodule_path = list(submodule_path)
-        try:
-            stream, mp_filename, mp_desc = imp.find_module(modname, submodule_path)
-        except ImportError:
-            return None
-
-        # Close resources.
-        if stream:
-            stream.close()
-
-        return ModuleSpec(
-            name=modname,
-            location=mp_filename,
-            module_type=_imp_type_to_module_type(mp_desc[2]),
-        )
-
-    def contribute_to_path(self, spec, processed):
-        if spec.location is None:
-            # Builtin.
-            return None
-
-        if _is_setuptools_namespace(spec.location):
-            # extend_path is called, search sys.path for module/packages
-            # of this name see pkgutil.extend_path documentation
-            path = [
-                os.path.join(p, *processed)
-                for p in sys.path
-                if os.path.isdir(os.path.join(p, *processed))
-            ]
-        # We already import distutils elsewhere in astroid,
-        # so if it is the same module, we can use it directly.
-        elif spec.name == "distutils" and spec.location in distutils.__path__:
-            # distutils is patched inside virtualenvs to pick up submodules
-            # from the original Python, not from the virtualenv itself.
-            path = list(distutils.__path__)
-        else:
-            path = [spec.location]
-        return path
-
-
-class ExplicitNamespacePackageFinder(ImpFinder):
-    """A finder for the explicit namespace packages, generated through pkg_resources."""
-
-    def find_module(self, modname, module_parts, processed, submodule_path):
-        if processed:
-            modname = ".".join(processed + [modname])
-        if util.is_namespace(modname) and modname in sys.modules:
-            submodule_path = sys.modules[modname].__path__
-            return ModuleSpec(
-                name=modname,
-                location="",
-                origin="namespace",
-                module_type=ModuleType.PY_NAMESPACE,
-                submodule_search_locations=submodule_path,
-            )
-        return None
-
-    def contribute_to_path(self, spec, processed):
-        return spec.submodule_search_locations
-
-
-class ZipFinder(Finder):
-    """Finder that knows how to find a module inside zip files."""
-
-    def __init__(self, path):
-        super(ZipFinder, self).__init__(path)
-        self._zipimporters = _precache_zipimporters(path)
-
-    def find_module(self, modname, module_parts, processed, submodule_path):
-        try:
-            file_type, filename, path = _search_zip(module_parts, self._zipimporters)
-        except ImportError:
-            return None
-
-        return ModuleSpec(
-            name=modname,
-            location=filename,
-            origin="egg",
-            module_type=file_type,
-            submodule_search_locations=path,
-        )
-
-
-class PathSpecFinder(Finder):
-    """Finder based on importlib.machinery.PathFinder."""
-
-    def find_module(self, modname, module_parts, processed, submodule_path):
-        spec = importlib.machinery.PathFinder.find_spec(modname, path=submodule_path)
-        if spec:
-            # origin can be either a string on older Python versions
-            # or None in case it is a namespace package:
-            # https://github.com/python/cpython/pull/5481
-            is_namespace_pkg = spec.origin in ("namespace", None)
-            location = spec.origin if not is_namespace_pkg else None
-            module_type = ModuleType.PY_NAMESPACE if is_namespace_pkg else None
-            spec = ModuleSpec(
-                name=spec.name,
-                location=location,
-                origin=spec.origin,
-                module_type=module_type,
-                submodule_search_locations=list(spec.submodule_search_locations or []),
-            )
-        return spec
-
-    def contribute_to_path(self, spec, processed):
-        if spec.type == ModuleType.PY_NAMESPACE:
-            return spec.submodule_search_locations
-        return None
-
-
-_SPEC_FINDERS = (ImpFinder, ZipFinder)
-if _HAS_MACHINERY:
-    _SPEC_FINDERS += (PathSpecFinder,)
-_SPEC_FINDERS += (ExplicitNamespacePackageFinder,)
-
-
-def _is_setuptools_namespace(location):
-    try:
-        with open(os.path.join(location, "__init__.py"), "rb") as stream:
-            data = stream.read(4096)
-    except IOError:
-        pass
-    else:
-        extend_path = b"pkgutil" in data and b"extend_path" in data
-        declare_namespace = (
-            b"pkg_resources" in data and b"declare_namespace(__name__)" in data
-        )
-        return extend_path or declare_namespace
-
-
-@lru_cache()
-def _cached_set_diff(left, right):
-    result = set(left)
-    result.difference_update(right)
-    return result
-
-
-def _precache_zipimporters(path=None):
-    pic = sys.path_importer_cache
-
-    # When measured, despite having the same complexity (O(n)),
-    # converting to tuples and then caching the conversion to sets
-    # and the set difference is faster than converting to sets
-    # and then only caching the set difference.
-
-    req_paths = tuple(path or sys.path)
-    cached_paths = tuple(pic)
-    new_paths = _cached_set_diff(req_paths, cached_paths)
-    for entry_path in new_paths:
-        try:
-            pic[entry_path] = zipimport.zipimporter(entry_path)
-        except zipimport.ZipImportError:
-            continue
-    return pic
-
-
-def _search_zip(modpath, pic):
-    for filepath, importer in list(pic.items()):
-        if importer is not None:
-            found = importer.find_module(modpath[0])
-            if found:
-                if not importer.find_module(os.path.sep.join(modpath)):
-                    raise ImportError(
-                        "No module named %s in %s/%s"
-                        % (".".join(modpath[1:]), filepath, modpath)
-                    )
-                # import code; code.interact(local=locals())
-                return (
-                    ModuleType.PY_ZIPMODULE,
-                    os.path.abspath(filepath) + os.path.sep + os.path.sep.join(modpath),
-                    filepath,
-                )
-    raise ImportError("No module named %s" % ".".join(modpath))
-
-
-def _find_spec_with_path(search_path, modname, module_parts, processed, submodule_path):
-    finders = [finder(search_path) for finder in _SPEC_FINDERS]
-    for finder in finders:
-        spec = finder.find_module(modname, module_parts, processed, submodule_path)
-        if spec is None:
-            continue
-        return finder, spec
-
-    raise ImportError("No module named %s" % ".".join(module_parts))
-
-
-def find_spec(modpath, path=None):
-    """Find a spec for the given module.
-
-    :type modpath: list or tuple
-    :param modpath:
-      split module's name (i.e name of a module or package split
-      on '.'), with leading empty strings for explicit relative import
-
-    :type path: list or None
-    :param path:
-      optional list of path where the module or package should be
-      searched (use sys.path if nothing or None is given)
-
-    :rtype: ModuleSpec
-    :return: A module spec, which describes how the module was
-             found and where.
-    """
-    _path = path or sys.path
-
-    # Need a copy for not mutating the argument.
-    modpath = modpath[:]
-
-    submodule_path = None
-    module_parts = modpath[:]
-    processed = []
-
-    while modpath:
-        modname = modpath.pop(0)
-        finder, spec = _find_spec_with_path(
-            _path, modname, module_parts, processed, submodule_path or path
-        )
-        processed.append(modname)
-        if modpath:
-            submodule_path = finder.contribute_to_path(spec, processed)
-
-        if spec.type == ModuleType.PKG_DIRECTORY:
-            spec = spec._replace(submodule_search_locations=submodule_path)
-
-    return spec
diff --git a/venv/Lib/site-packages/astroid/interpreter/_import/util.py b/venv/Lib/site-packages/astroid/interpreter/_import/util.py
deleted file mode 100644
index a917bd3..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/_import/util.py
+++ /dev/null
@@ -1,10 +0,0 @@
-# Copyright (c) 2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-
-try:
-    import pkg_resources
-except ImportError:
-    pkg_resources = None
-
-
-def is_namespace(modname):
-    return pkg_resources is not None and modname in pkg_resources._namespace_packages
diff --git a/venv/Lib/site-packages/astroid/interpreter/dunder_lookup.py b/venv/Lib/site-packages/astroid/interpreter/dunder_lookup.py
deleted file mode 100644
index 0ae9bc9..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/dunder_lookup.py
+++ /dev/null
@@ -1,66 +0,0 @@
-# Copyright (c) 2016-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Contains logic for retrieving special methods.
-
-This implementation does not rely on the dot attribute access
-logic, found in ``.getattr()``. The difference between these two
-is that the dunder methods are looked with the type slots
-(you can find more about these here
-http://lucumr.pocoo.org/2014/8/16/the-python-i-would-like-to-see/)
-As such, the lookup for the special methods is actually simpler than
-the dot attribute access.
-"""
-import itertools
-
-import astroid
-from astroid import exceptions
-
-
-def _lookup_in_mro(node, name):
-    attrs = node.locals.get(name, [])
-
-    nodes = itertools.chain.from_iterable(
-        ancestor.locals.get(name, []) for ancestor in node.ancestors(recurs=True)
-    )
-    values = list(itertools.chain(attrs, nodes))
-    if not values:
-        raise exceptions.AttributeInferenceError(attribute=name, target=node)
-
-    return values
-
-
-def lookup(node, name):
-    """Lookup the given special method name in the given *node*
-
-    If the special method was found, then a list of attributes
-    will be returned. Otherwise, `astroid.AttributeInferenceError`
-    is going to be raised.
-    """
-    if isinstance(
-        node, (astroid.List, astroid.Tuple, astroid.Const, astroid.Dict, astroid.Set)
-    ):
-        return _builtin_lookup(node, name)
-    if isinstance(node, astroid.Instance):
-        return _lookup_in_mro(node, name)
-    if isinstance(node, astroid.ClassDef):
-        return _class_lookup(node, name)
-
-    raise exceptions.AttributeInferenceError(attribute=name, target=node)
-
-
-def _class_lookup(node, name):
-    metaclass = node.metaclass()
-    if metaclass is None:
-        raise exceptions.AttributeInferenceError(attribute=name, target=node)
-
-    return _lookup_in_mro(metaclass, name)
-
-
-def _builtin_lookup(node, name):
-    values = node.locals.get(name, [])
-    if not values:
-        raise exceptions.AttributeInferenceError(attribute=name, target=node)
-
-    return values
diff --git a/venv/Lib/site-packages/astroid/interpreter/objectmodel.py b/venv/Lib/site-packages/astroid/interpreter/objectmodel.py
deleted file mode 100644
index 5e488d9..0000000
--- a/venv/Lib/site-packages/astroid/interpreter/objectmodel.py
+++ /dev/null
@@ -1,738 +0,0 @@
-# Copyright (c) 2016-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017-2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2017 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2017 Calen Pennington <cale@edx.org>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-"""
-Data object model, as per https://docs.python.org/3/reference/datamodel.html.
-
-This module describes, at least partially, a data object model for some
-of astroid's nodes. The model contains special attributes that nodes such
-as functions, classes, modules etc have, such as __doc__, __class__,
-__module__ etc, being used when doing attribute lookups over nodes.
-
-For instance, inferring `obj.__class__` will first trigger an inference
-of the `obj` variable. If it was successfully inferred, then an attribute
-`__class__ will be looked for in the inferred object. This is the part
-where the data model occurs. The model is attached to those nodes
-and the lookup mechanism will try to see if attributes such as
-`__class__` are defined by the model or not. If they are defined,
-the model will be requested to return the corresponding value of that
-attribute. Thus the model can be viewed as a special part of the lookup
-mechanism.
-"""
-
-import itertools
-import pprint
-import os
-import types
-from functools import lru_cache
-
-import astroid
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import node_classes
-
-
-IMPL_PREFIX = "attr_"
-
-
-def _dunder_dict(instance, attributes):
-    obj = node_classes.Dict(parent=instance)
-
-    # Convert the keys to node strings
-    keys = [
-        node_classes.Const(value=value, parent=obj) for value in list(attributes.keys())
-    ]
-
-    # The original attribute has a list of elements for each key,
-    # but that is not useful for retrieving the special attribute's value.
-    # In this case, we're picking the last value from each list.
-    values = [elem[-1] for elem in attributes.values()]
-
-    obj.postinit(list(zip(keys, values)))
-    return obj
-
-
-class ObjectModel:
-    def __init__(self):
-        self._instance = None
-
-    def __repr__(self):
-        result = []
-        cname = type(self).__name__
-        string = "%(cname)s(%(fields)s)"
-        alignment = len(cname) + 1
-        for field in sorted(self.attributes()):
-            width = 80 - len(field) - alignment
-            lines = pprint.pformat(field, indent=2, width=width).splitlines(True)
-
-            inner = [lines[0]]
-            for line in lines[1:]:
-                inner.append(" " * alignment + line)
-            result.append(field)
-
-        return string % {
-            "cname": cname,
-            "fields": (",\n" + " " * alignment).join(result),
-        }
-
-    def __call__(self, instance):
-        self._instance = instance
-        return self
-
-    def __get__(self, instance, cls=None):
-        # ObjectModel needs to be a descriptor so that just doing
-        # `special_attributes = SomeObjectModel` should be enough in the body of a node.
-        # But at the same time, node.special_attributes should return an object
-        # which can be used for manipulating the special attributes. That's the reason
-        # we pass the instance through which it got accessed to ObjectModel.__call__,
-        # returning itself afterwards, so we can still have access to the
-        # underlying data model and to the instance for which it got accessed.
-        return self(instance)
-
-    def __contains__(self, name):
-        return name in self.attributes()
-
-    @lru_cache(maxsize=None)
-    def attributes(self):
-        """Get the attributes which are exported by this object model."""
-        return [
-            obj[len(IMPL_PREFIX) :] for obj in dir(self) if obj.startswith(IMPL_PREFIX)
-        ]
-
-    def lookup(self, name):
-        """Look up the given *name* in the current model
-
-        It should return an AST or an interpreter object,
-        but if the name is not found, then an AttributeInferenceError will be raised.
-        """
-
-        if name in self.attributes():
-            return getattr(self, IMPL_PREFIX + name)
-        raise exceptions.AttributeInferenceError(target=self._instance, attribute=name)
-
-
-class ModuleModel(ObjectModel):
-    def _builtins(self):
-        builtins_ast_module = astroid.MANAGER.builtins_module
-        return builtins_ast_module.special_attributes.lookup("__dict__")
-
-    @property
-    def attr_builtins(self):
-        return self._builtins()
-
-    @property
-    def attr___path__(self):
-        if not self._instance.package:
-            raise exceptions.AttributeInferenceError(
-                target=self._instance, attribute="__path__"
-            )
-
-        path_objs = [
-            node_classes.Const(
-                value=path
-                if not path.endswith("__init__.py")
-                else os.path.dirname(path),
-                parent=self._instance,
-            )
-            for path in self._instance.path
-        ]
-
-        container = node_classes.List(parent=self._instance)
-        container.postinit(path_objs)
-
-        return container
-
-    @property
-    def attr___name__(self):
-        return node_classes.Const(value=self._instance.name, parent=self._instance)
-
-    @property
-    def attr___doc__(self):
-        return node_classes.Const(value=self._instance.doc, parent=self._instance)
-
-    @property
-    def attr___file__(self):
-        return node_classes.Const(value=self._instance.file, parent=self._instance)
-
-    @property
-    def attr___dict__(self):
-        return _dunder_dict(self._instance, self._instance.globals)
-
-    @property
-    def attr___package__(self):
-        if not self._instance.package:
-            value = ""
-        else:
-            value = self._instance.name
-
-        return node_classes.Const(value=value, parent=self._instance)
-
-    # These are related to the Python 3 implementation of the
-    # import system,
-    # https://docs.python.org/3/reference/import.html#import-related-module-attributes
-
-    @property
-    def attr___spec__(self):
-        # No handling for now.
-        return node_classes.Unknown()
-
-    @property
-    def attr___loader__(self):
-        # No handling for now.
-        return node_classes.Unknown()
-
-    @property
-    def attr___cached__(self):
-        # No handling for now.
-        return node_classes.Unknown()
-
-
-class FunctionModel(ObjectModel):
-    @property
-    def attr___name__(self):
-        return node_classes.Const(value=self._instance.name, parent=self._instance)
-
-    @property
-    def attr___doc__(self):
-        return node_classes.Const(value=self._instance.doc, parent=self._instance)
-
-    @property
-    def attr___qualname__(self):
-        return node_classes.Const(value=self._instance.qname(), parent=self._instance)
-
-    @property
-    def attr___defaults__(self):
-        func = self._instance
-        if not func.args.defaults:
-            return node_classes.Const(value=None, parent=func)
-
-        defaults_obj = node_classes.Tuple(parent=func)
-        defaults_obj.postinit(func.args.defaults)
-        return defaults_obj
-
-    @property
-    def attr___annotations__(self):
-        obj = node_classes.Dict(parent=self._instance)
-
-        if not self._instance.returns:
-            returns = None
-        else:
-            returns = self._instance.returns
-
-        args = self._instance.args
-        pair_annotations = itertools.chain(
-            zip(args.args or [], args.annotations),
-            zip(args.kwonlyargs, args.kwonlyargs_annotations),
-            zip(args.posonlyargs or [], args.posonlyargs_annotations),
-        )
-
-        annotations = {
-            arg.name: annotation for (arg, annotation) in pair_annotations if annotation
-        }
-        if args.varargannotation:
-            annotations[args.vararg] = args.varargannotation
-        if args.kwargannotation:
-            annotations[args.kwarg] = args.kwargannotation
-        if returns:
-            annotations["return"] = returns
-
-        items = [
-            (node_classes.Const(key, parent=obj), value)
-            for (key, value) in annotations.items()
-        ]
-
-        obj.postinit(items)
-        return obj
-
-    @property
-    def attr___dict__(self):
-        return node_classes.Dict(parent=self._instance)
-
-    attr___globals__ = attr___dict__
-
-    @property
-    def attr___kwdefaults__(self):
-        def _default_args(args, parent):
-            for arg in args.kwonlyargs:
-                try:
-                    default = args.default_value(arg.name)
-                except exceptions.NoDefault:
-                    continue
-
-                name = node_classes.Const(arg.name, parent=parent)
-                yield name, default
-
-        args = self._instance.args
-        obj = node_classes.Dict(parent=self._instance)
-        defaults = dict(_default_args(args, obj))
-
-        obj.postinit(list(defaults.items()))
-        return obj
-
-    @property
-    def attr___module__(self):
-        return node_classes.Const(self._instance.root().qname())
-
-    @property
-    def attr___get__(self):
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import bases
-
-        func = self._instance
-
-        class DescriptorBoundMethod(bases.BoundMethod):
-            """Bound method which knows how to understand calling descriptor binding."""
-
-            def implicit_parameters(self):
-                # Different than BoundMethod since the signature
-                # is different.
-                return 0
-
-            def infer_call_result(self, caller, context=None):
-                if len(caller.args) > 2 or len(caller.args) < 1:
-                    raise exceptions.InferenceError(
-                        "Invalid arguments for descriptor binding",
-                        target=self,
-                        context=context,
-                    )
-
-                context = contextmod.copy_context(context)
-                cls = next(caller.args[0].infer(context=context))
-
-                if cls is astroid.Uninferable:
-                    raise exceptions.InferenceError(
-                        "Invalid class inferred", target=self, context=context
-                    )
-
-                # For some reason func is a Node that the below
-                # code is not expecting
-                if isinstance(func, bases.BoundMethod):
-                    yield func
-                    return
-
-                # Rebuild the original value, but with the parent set as the
-                # class where it will be bound.
-                new_func = func.__class__(
-                    name=func.name,
-                    doc=func.doc,
-                    lineno=func.lineno,
-                    col_offset=func.col_offset,
-                    parent=cls,
-                )
-                # pylint: disable=no-member
-                new_func.postinit(func.args, func.body, func.decorators, func.returns)
-
-                # Build a proper bound method that points to our newly built function.
-                proxy = bases.UnboundMethod(new_func)
-                yield bases.BoundMethod(proxy=proxy, bound=cls)
-
-            @property
-            def args(self):
-                """Overwrite the underlying args to match those of the underlying func
-
-                Usually the underlying *func* is a function/method, as in:
-
-                    def test(self):
-                        pass
-
-                This has only the *self* parameter but when we access test.__get__
-                we get a new object which has two parameters, *self* and *type*.
-                """
-                nonlocal func
-                positional_or_keyword_params = func.args.args.copy()
-                positional_or_keyword_params.append(astroid.AssignName(name="type"))
-
-                positional_only_params = func.args.posonlyargs.copy()
-
-                arguments = astroid.Arguments(parent=func.args.parent)
-                arguments.postinit(
-                    args=positional_or_keyword_params,
-                    posonlyargs=positional_only_params,
-                    defaults=[],
-                    kwonlyargs=[],
-                    kw_defaults=[],
-                    annotations=[],
-                )
-                return arguments
-
-        return DescriptorBoundMethod(proxy=self._instance, bound=self._instance)
-
-    # These are here just for completion.
-    @property
-    def attr___ne__(self):
-        return node_classes.Unknown()
-
-    attr___subclasshook__ = attr___ne__
-    attr___str__ = attr___ne__
-    attr___sizeof__ = attr___ne__
-    attr___setattr___ = attr___ne__
-    attr___repr__ = attr___ne__
-    attr___reduce__ = attr___ne__
-    attr___reduce_ex__ = attr___ne__
-    attr___new__ = attr___ne__
-    attr___lt__ = attr___ne__
-    attr___eq__ = attr___ne__
-    attr___gt__ = attr___ne__
-    attr___format__ = attr___ne__
-    attr___delattr___ = attr___ne__
-    attr___getattribute__ = attr___ne__
-    attr___hash__ = attr___ne__
-    attr___init__ = attr___ne__
-    attr___dir__ = attr___ne__
-    attr___call__ = attr___ne__
-    attr___class__ = attr___ne__
-    attr___closure__ = attr___ne__
-    attr___code__ = attr___ne__
-
-
-class ClassModel(ObjectModel):
-    @property
-    def attr___module__(self):
-        return node_classes.Const(self._instance.root().qname())
-
-    @property
-    def attr___name__(self):
-        return node_classes.Const(self._instance.name)
-
-    @property
-    def attr___qualname__(self):
-        return node_classes.Const(self._instance.qname())
-
-    @property
-    def attr___doc__(self):
-        return node_classes.Const(self._instance.doc)
-
-    @property
-    def attr___mro__(self):
-        if not self._instance.newstyle:
-            raise exceptions.AttributeInferenceError(
-                target=self._instance, attribute="__mro__"
-            )
-
-        mro = self._instance.mro()
-        obj = node_classes.Tuple(parent=self._instance)
-        obj.postinit(mro)
-        return obj
-
-    @property
-    def attr_mro(self):
-        if not self._instance.newstyle:
-            raise exceptions.AttributeInferenceError(
-                target=self._instance, attribute="mro"
-            )
-
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import bases
-
-        other_self = self
-
-        # Cls.mro is a method and we need to return one in order to have a proper inference.
-        # The method we're returning is capable of inferring the underlying MRO though.
-        class MroBoundMethod(bases.BoundMethod):
-            def infer_call_result(self, caller, context=None):
-                yield other_self.attr___mro__
-
-        implicit_metaclass = self._instance.implicit_metaclass()
-        mro_method = implicit_metaclass.locals["mro"][0]
-        return MroBoundMethod(proxy=mro_method, bound=implicit_metaclass)
-
-    @property
-    def attr___bases__(self):
-        obj = node_classes.Tuple()
-        context = contextmod.InferenceContext()
-        elts = list(self._instance._inferred_bases(context))
-        obj.postinit(elts=elts)
-        return obj
-
-    @property
-    def attr___class__(self):
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import helpers
-
-        return helpers.object_type(self._instance)
-
-    @property
-    def attr___subclasses__(self):
-        """Get the subclasses of the underlying class
-
-        This looks only in the current module for retrieving the subclasses,
-        thus it might miss a couple of them.
-        """
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import bases
-        from astroid import scoped_nodes
-
-        if not self._instance.newstyle:
-            raise exceptions.AttributeInferenceError(
-                target=self._instance, attribute="__subclasses__"
-            )
-
-        qname = self._instance.qname()
-        root = self._instance.root()
-        classes = [
-            cls
-            for cls in root.nodes_of_class(scoped_nodes.ClassDef)
-            if cls != self._instance and cls.is_subtype_of(qname)
-        ]
-
-        obj = node_classes.List(parent=self._instance)
-        obj.postinit(classes)
-
-        class SubclassesBoundMethod(bases.BoundMethod):
-            def infer_call_result(self, caller, context=None):
-                yield obj
-
-        implicit_metaclass = self._instance.implicit_metaclass()
-        subclasses_method = implicit_metaclass.locals["__subclasses__"][0]
-        return SubclassesBoundMethod(proxy=subclasses_method, bound=implicit_metaclass)
-
-    @property
-    def attr___dict__(self):
-        return node_classes.Dict(parent=self._instance)
-
-
-class SuperModel(ObjectModel):
-    @property
-    def attr___thisclass__(self):
-        return self._instance.mro_pointer
-
-    @property
-    def attr___self_class__(self):
-        return self._instance._self_class
-
-    @property
-    def attr___self__(self):
-        return self._instance.type
-
-    @property
-    def attr___class__(self):
-        return self._instance._proxied
-
-
-class UnboundMethodModel(ObjectModel):
-    @property
-    def attr___class__(self):
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import helpers
-
-        return helpers.object_type(self._instance)
-
-    @property
-    def attr___func__(self):
-        return self._instance._proxied
-
-    @property
-    def attr___self__(self):
-        return node_classes.Const(value=None, parent=self._instance)
-
-    attr_im_func = attr___func__
-    attr_im_class = attr___class__
-    attr_im_self = attr___self__
-
-
-class BoundMethodModel(FunctionModel):
-    @property
-    def attr___func__(self):
-        return self._instance._proxied._proxied
-
-    @property
-    def attr___self__(self):
-        return self._instance.bound
-
-
-class GeneratorModel(FunctionModel):
-    def __new__(cls, *args, **kwargs):
-        # Append the values from the GeneratorType unto this object.
-        ret = super(GeneratorModel, cls).__new__(cls, *args, **kwargs)
-        generator = astroid.MANAGER.builtins_module["generator"]
-        for name, values in generator.locals.items():
-            method = values[0]
-            patched = lambda cls, meth=method: meth
-
-            setattr(type(ret), IMPL_PREFIX + name, property(patched))
-
-        return ret
-
-    @property
-    def attr___name__(self):
-        return node_classes.Const(
-            value=self._instance.parent.name, parent=self._instance
-        )
-
-    @property
-    def attr___doc__(self):
-        return node_classes.Const(
-            value=self._instance.parent.doc, parent=self._instance
-        )
-
-
-class AsyncGeneratorModel(GeneratorModel):
-    def __new__(cls, *args, **kwargs):
-        # Append the values from the AGeneratorType unto this object.
-        ret = super().__new__(cls, *args, **kwargs)
-        astroid_builtins = astroid.MANAGER.builtins_module
-        generator = astroid_builtins.get("async_generator")
-        if generator is None:
-            # Make it backward compatible.
-            generator = astroid_builtins.get("generator")
-
-        for name, values in generator.locals.items():
-            method = values[0]
-            patched = lambda cls, meth=method: meth
-
-            setattr(type(ret), IMPL_PREFIX + name, property(patched))
-
-        return ret
-
-
-class InstanceModel(ObjectModel):
-    @property
-    def attr___class__(self):
-        return self._instance._proxied
-
-    @property
-    def attr___module__(self):
-        return node_classes.Const(self._instance.root().qname())
-
-    @property
-    def attr___doc__(self):
-        return node_classes.Const(self._instance.doc)
-
-    @property
-    def attr___dict__(self):
-        return _dunder_dict(self._instance, self._instance.instance_attrs)
-
-
-# Exception instances
-
-
-class ExceptionInstanceModel(InstanceModel):
-    @property
-    def attr_args(self):
-        message = node_classes.Const("")
-        args = node_classes.Tuple(parent=self._instance)
-        args.postinit((message,))
-        return args
-
-    @property
-    def attr___traceback__(self):
-        builtins_ast_module = astroid.MANAGER.builtins_module
-        traceback_type = builtins_ast_module[types.TracebackType.__name__]
-        return traceback_type.instantiate_class()
-
-
-class SyntaxErrorInstanceModel(ExceptionInstanceModel):
-    @property
-    def attr_text(self):
-        return node_classes.Const("")
-
-
-class OSErrorInstanceModel(ExceptionInstanceModel):
-    @property
-    def attr_filename(self):
-        return node_classes.Const("")
-
-    @property
-    def attr_errno(self):
-        return node_classes.Const(0)
-
-    @property
-    def attr_strerror(self):
-        return node_classes.Const("")
-
-    attr_filename2 = attr_filename
-
-
-class ImportErrorInstanceModel(ExceptionInstanceModel):
-    @property
-    def attr_name(self):
-        return node_classes.Const("")
-
-    @property
-    def attr_path(self):
-        return node_classes.Const("")
-
-
-BUILTIN_EXCEPTIONS = {
-    "builtins.SyntaxError": SyntaxErrorInstanceModel,
-    "builtins.ImportError": ImportErrorInstanceModel,
-    # These are all similar to OSError in terms of attributes
-    "builtins.OSError": OSErrorInstanceModel,
-    "builtins.BlockingIOError": OSErrorInstanceModel,
-    "builtins.BrokenPipeError": OSErrorInstanceModel,
-    "builtins.ChildProcessError": OSErrorInstanceModel,
-    "builtins.ConnectionAbortedError": OSErrorInstanceModel,
-    "builtins.ConnectionError": OSErrorInstanceModel,
-    "builtins.ConnectionRefusedError": OSErrorInstanceModel,
-    "builtins.ConnectionResetError": OSErrorInstanceModel,
-    "builtins.FileExistsError": OSErrorInstanceModel,
-    "builtins.FileNotFoundError": OSErrorInstanceModel,
-    "builtins.InterruptedError": OSErrorInstanceModel,
-    "builtins.IsADirectoryError": OSErrorInstanceModel,
-    "builtins.NotADirectoryError": OSErrorInstanceModel,
-    "builtins.PermissionError": OSErrorInstanceModel,
-    "builtins.ProcessLookupError": OSErrorInstanceModel,
-    "builtins.TimeoutError": OSErrorInstanceModel,
-}
-
-
-class DictModel(ObjectModel):
-    @property
-    def attr___class__(self):
-        return self._instance._proxied
-
-    def _generic_dict_attribute(self, obj, name):
-        """Generate a bound method that can infer the given *obj*."""
-
-        class DictMethodBoundMethod(astroid.BoundMethod):
-            def infer_call_result(self, caller, context=None):
-                yield obj
-
-        meth = next(self._instance._proxied.igetattr(name))
-        return DictMethodBoundMethod(proxy=meth, bound=self._instance)
-
-    @property
-    def attr_items(self):
-        elems = []
-        obj = node_classes.List(parent=self._instance)
-        for key, value in self._instance.items:
-            elem = node_classes.Tuple(parent=obj)
-            elem.postinit((key, value))
-            elems.append(elem)
-        obj.postinit(elts=elems)
-
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import objects
-
-        obj = objects.DictItems(obj)
-        return self._generic_dict_attribute(obj, "items")
-
-    @property
-    def attr_keys(self):
-        keys = [key for (key, _) in self._instance.items]
-        obj = node_classes.List(parent=self._instance)
-        obj.postinit(elts=keys)
-
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import objects
-
-        obj = objects.DictKeys(obj)
-        return self._generic_dict_attribute(obj, "keys")
-
-    @property
-    def attr_values(self):
-
-        values = [value for (_, value) in self._instance.items]
-        obj = node_classes.List(parent=self._instance)
-        obj.postinit(values)
-
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid import objects
-
-        obj = objects.DictValues(obj)
-        return self._generic_dict_attribute(obj, "values")
diff --git a/venv/Lib/site-packages/astroid/manager.py b/venv/Lib/site-packages/astroid/manager.py
deleted file mode 100644
index e5fd0d6..0000000
--- a/venv/Lib/site-packages/astroid/manager.py
+++ /dev/null
@@ -1,337 +0,0 @@
-# Copyright (c) 2006-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 BioGeek <jeroen.vangoey@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017 Iva Miholic <ivamiho@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""astroid manager: avoid multiple astroid build of a same module when
-possible by providing a class responsible to get astroid representation
-from various source and using a cache of built modules)
-"""
-
-import os
-import zipimport
-
-from astroid import exceptions
-from astroid.interpreter._import import spec
-from astroid import modutils
-from astroid import transforms
-
-
-ZIP_IMPORT_EXTS = (".zip", ".egg", ".whl")
-
-
-def safe_repr(obj):
-    try:
-        return repr(obj)
-    except Exception:  # pylint: disable=broad-except
-        return "???"
-
-
-class AstroidManager:
-    """the astroid manager, responsible to build astroid from files
-     or modules.
-
-    Use the Borg pattern.
-    """
-
-    name = "astroid loader"
-    brain = {}
-
-    def __init__(self):
-        self.__dict__ = AstroidManager.brain
-        if not self.__dict__:
-            # NOTE: cache entries are added by the [re]builder
-            self.astroid_cache = {}
-            self._mod_file_cache = {}
-            self._failed_import_hooks = []
-            self.always_load_extensions = False
-            self.optimize_ast = False
-            self.extension_package_whitelist = set()
-            self._transform = transforms.TransformVisitor()
-
-            # Export these APIs for convenience
-            self.register_transform = self._transform.register_transform
-            self.unregister_transform = self._transform.unregister_transform
-            self.max_inferable_values = 100
-
-    @property
-    def builtins_module(self):
-        return self.astroid_cache["builtins"]
-
-    def visit_transforms(self, node):
-        """Visit the transforms and apply them to the given *node*."""
-        return self._transform.visit(node)
-
-    def ast_from_file(self, filepath, modname=None, fallback=True, source=False):
-        """given a module name, return the astroid object"""
-        try:
-            filepath = modutils.get_source_file(filepath, include_no_ext=True)
-            source = True
-        except modutils.NoSourceFile:
-            pass
-        if modname is None:
-            try:
-                modname = ".".join(modutils.modpath_from_file(filepath))
-            except ImportError:
-                modname = filepath
-        if (
-            modname in self.astroid_cache
-            and self.astroid_cache[modname].file == filepath
-        ):
-            return self.astroid_cache[modname]
-        if source:
-            # pylint: disable=import-outside-toplevel; circular import
-            from astroid.builder import AstroidBuilder
-
-            return AstroidBuilder(self).file_build(filepath, modname)
-        if fallback and modname:
-            return self.ast_from_module_name(modname)
-        raise exceptions.AstroidBuildingError(
-            "Unable to build an AST for {path}.", path=filepath
-        )
-
-    def _build_stub_module(self, modname):
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid.builder import AstroidBuilder
-
-        return AstroidBuilder(self).string_build("", modname)
-
-    def _build_namespace_module(self, modname, path):
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid.builder import build_namespace_package_module
-
-        return build_namespace_package_module(modname, path)
-
-    def _can_load_extension(self, modname):
-        if self.always_load_extensions:
-            return True
-        if modutils.is_standard_module(modname):
-            return True
-        parts = modname.split(".")
-        return any(
-            ".".join(parts[:x]) in self.extension_package_whitelist
-            for x in range(1, len(parts) + 1)
-        )
-
-    def ast_from_module_name(self, modname, context_file=None):
-        """given a module name, return the astroid object"""
-        if modname in self.astroid_cache:
-            return self.astroid_cache[modname]
-        if modname == "__main__":
-            return self._build_stub_module(modname)
-        old_cwd = os.getcwd()
-        if context_file:
-            os.chdir(os.path.dirname(context_file))
-        try:
-            found_spec = self.file_from_module_name(modname, context_file)
-            if found_spec.type == spec.ModuleType.PY_ZIPMODULE:
-                module = self.zip_import_data(found_spec.location)
-                if module is not None:
-                    return module
-
-            elif found_spec.type in (
-                spec.ModuleType.C_BUILTIN,
-                spec.ModuleType.C_EXTENSION,
-            ):
-                if (
-                    found_spec.type == spec.ModuleType.C_EXTENSION
-                    and not self._can_load_extension(modname)
-                ):
-                    return self._build_stub_module(modname)
-                try:
-                    module = modutils.load_module_from_name(modname)
-                except Exception as ex:
-                    raise exceptions.AstroidImportError(
-                        "Loading {modname} failed with:\n{error}",
-                        modname=modname,
-                        path=found_spec.location,
-                    ) from ex
-                return self.ast_from_module(module, modname)
-
-            elif found_spec.type == spec.ModuleType.PY_COMPILED:
-                raise exceptions.AstroidImportError(
-                    "Unable to load compiled module {modname}.",
-                    modname=modname,
-                    path=found_spec.location,
-                )
-
-            elif found_spec.type == spec.ModuleType.PY_NAMESPACE:
-                return self._build_namespace_module(
-                    modname, found_spec.submodule_search_locations
-                )
-
-            if found_spec.location is None:
-                raise exceptions.AstroidImportError(
-                    "Can't find a file for module {modname}.", modname=modname
-                )
-
-            return self.ast_from_file(found_spec.location, modname, fallback=False)
-        except exceptions.AstroidBuildingError as e:
-            for hook in self._failed_import_hooks:
-                try:
-                    return hook(modname)
-                except exceptions.AstroidBuildingError:
-                    pass
-            raise e
-        finally:
-            os.chdir(old_cwd)
-
-    def zip_import_data(self, filepath):
-        if zipimport is None:
-            return None
-
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid.builder import AstroidBuilder
-
-        builder = AstroidBuilder(self)
-        for ext in ZIP_IMPORT_EXTS:
-            try:
-                eggpath, resource = filepath.rsplit(ext + os.path.sep, 1)
-            except ValueError:
-                continue
-            try:
-                importer = zipimport.zipimporter(eggpath + ext)
-                zmodname = resource.replace(os.path.sep, ".")
-                if importer.is_package(resource):
-                    zmodname = zmodname + ".__init__"
-                module = builder.string_build(
-                    importer.get_source(resource), zmodname, filepath
-                )
-                return module
-            except Exception:  # pylint: disable=broad-except
-                continue
-        return None
-
-    def file_from_module_name(self, modname, contextfile):
-        try:
-            value = self._mod_file_cache[(modname, contextfile)]
-        except KeyError:
-            try:
-                value = modutils.file_info_from_modpath(
-                    modname.split("."), context_file=contextfile
-                )
-            except ImportError as ex:
-                value = exceptions.AstroidImportError(
-                    "Failed to import module {modname} with error:\n{error}.",
-                    modname=modname,
-                    error=ex,
-                )
-            self._mod_file_cache[(modname, contextfile)] = value
-        if isinstance(value, exceptions.AstroidBuildingError):
-            raise value
-        return value
-
-    def ast_from_module(self, module, modname=None):
-        """given an imported module, return the astroid object"""
-        modname = modname or module.__name__
-        if modname in self.astroid_cache:
-            return self.astroid_cache[modname]
-        try:
-            # some builtin modules don't have __file__ attribute
-            filepath = module.__file__
-            if modutils.is_python_source(filepath):
-                return self.ast_from_file(filepath, modname)
-        except AttributeError:
-            pass
-
-        # pylint: disable=import-outside-toplevel; circular import
-        from astroid.builder import AstroidBuilder
-
-        return AstroidBuilder(self).module_build(module, modname)
-
-    def ast_from_class(self, klass, modname=None):
-        """get astroid for the given class"""
-        if modname is None:
-            try:
-                modname = klass.__module__
-            except AttributeError as exc:
-                raise exceptions.AstroidBuildingError(
-                    "Unable to get module for class {class_name}.",
-                    cls=klass,
-                    class_repr=safe_repr(klass),
-                    modname=modname,
-                ) from exc
-        modastroid = self.ast_from_module_name(modname)
-        return modastroid.getattr(klass.__name__)[0]  # XXX
-
-    def infer_ast_from_something(self, obj, context=None):
-        """infer astroid for the given class"""
-        if hasattr(obj, "__class__") and not isinstance(obj, type):
-            klass = obj.__class__
-        else:
-            klass = obj
-        try:
-            modname = klass.__module__
-        except AttributeError as exc:
-            raise exceptions.AstroidBuildingError(
-                "Unable to get module for {class_repr}.",
-                cls=klass,
-                class_repr=safe_repr(klass),
-            ) from exc
-        except Exception as exc:
-            raise exceptions.AstroidImportError(
-                "Unexpected error while retrieving module for {class_repr}:\n"
-                "{error}",
-                cls=klass,
-                class_repr=safe_repr(klass),
-            ) from exc
-        try:
-            name = klass.__name__
-        except AttributeError as exc:
-            raise exceptions.AstroidBuildingError(
-                "Unable to get name for {class_repr}:\n",
-                cls=klass,
-                class_repr=safe_repr(klass),
-            ) from exc
-        except Exception as exc:
-            raise exceptions.AstroidImportError(
-                "Unexpected error while retrieving name for {class_repr}:\n" "{error}",
-                cls=klass,
-                class_repr=safe_repr(klass),
-            ) from exc
-        # take care, on living object __module__ is regularly wrong :(
-        modastroid = self.ast_from_module_name(modname)
-        if klass is obj:
-            for inferred in modastroid.igetattr(name, context):
-                yield inferred
-        else:
-            for inferred in modastroid.igetattr(name, context):
-                yield inferred.instantiate_class()
-
-    def register_failed_import_hook(self, hook):
-        """Registers a hook to resolve imports that cannot be found otherwise.
-
-        `hook` must be a function that accepts a single argument `modname` which
-        contains the name of the module or package that could not be imported.
-        If `hook` can resolve the import, must return a node of type `astroid.Module`,
-        otherwise, it must raise `AstroidBuildingError`.
-        """
-        self._failed_import_hooks.append(hook)
-
-    def cache_module(self, module):
-        """Cache a module if no module with the same name is known yet."""
-        self.astroid_cache.setdefault(module.name, module)
-
-    def bootstrap(self):
-        """Bootstrap the required AST modules needed for the manager to work
-
-        The bootstrap usually involves building the AST for the builtins
-        module, which is required by the rest of astroid to work correctly.
-        """
-        from astroid import raw_building  # pylint: disable=import-outside-toplevel
-
-        raw_building._astroid_bootstrapping()
-
-    def clear_cache(self):
-        """Clear the underlying cache. Also bootstraps the builtins module."""
-        self.astroid_cache.clear()
-        self.bootstrap()
diff --git a/venv/Lib/site-packages/astroid/mixins.py b/venv/Lib/site-packages/astroid/mixins.py
deleted file mode 100644
index 497a840..0000000
--- a/venv/Lib/site-packages/astroid/mixins.py
+++ /dev/null
@@ -1,160 +0,0 @@
-# Copyright (c) 2010-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""This module contains some mixins for the different nodes.
-"""
-import itertools
-
-from astroid import decorators
-from astroid import exceptions
-
-
-class BlockRangeMixIn:
-    """override block range """
-
-    @decorators.cachedproperty
-    def blockstart_tolineno(self):
-        return self.lineno
-
-    def _elsed_block_range(self, lineno, orelse, last=None):
-        """handle block line numbers range for try/finally, for, if and while
-        statements
-        """
-        if lineno == self.fromlineno:
-            return lineno, lineno
-        if orelse:
-            if lineno >= orelse[0].fromlineno:
-                return lineno, orelse[-1].tolineno
-            return lineno, orelse[0].fromlineno - 1
-        return lineno, last or self.tolineno
-
-
-class FilterStmtsMixin:
-    """Mixin for statement filtering and assignment type"""
-
-    def _get_filtered_stmts(self, _, node, _stmts, mystmt):
-        """method used in _filter_stmts to get statements and trigger break"""
-        if self.statement() is mystmt:
-            # original node's statement is the assignment, only keep
-            # current node (gen exp, list comp)
-            return [node], True
-        return _stmts, False
-
-    def assign_type(self):
-        return self
-
-
-class AssignTypeMixin:
-    def assign_type(self):
-        return self
-
-    def _get_filtered_stmts(self, lookup_node, node, _stmts, mystmt):
-        """method used in filter_stmts"""
-        if self is mystmt:
-            return _stmts, True
-        if self.statement() is mystmt:
-            # original node's statement is the assignment, only keep
-            # current node (gen exp, list comp)
-            return [node], True
-        return _stmts, False
-
-
-class ParentAssignTypeMixin(AssignTypeMixin):
-    def assign_type(self):
-        return self.parent.assign_type()
-
-
-class ImportFromMixin(FilterStmtsMixin):
-    """MixIn for From and Import Nodes"""
-
-    def _infer_name(self, frame, name):
-        return name
-
-    def do_import_module(self, modname=None):
-        """return the ast for a module whose name is <modname> imported by <self>
-        """
-        # handle special case where we are on a package node importing a module
-        # using the same name as the package, which may end in an infinite loop
-        # on relative imports
-        # XXX: no more needed ?
-        mymodule = self.root()
-        level = getattr(self, "level", None)  # Import as no level
-        if modname is None:
-            modname = self.modname
-        # XXX we should investigate deeper if we really want to check
-        # importing itself: modname and mymodule.name be relative or absolute
-        if mymodule.relative_to_absolute_name(modname, level) == mymodule.name:
-            # FIXME: we used to raise InferenceError here, but why ?
-            return mymodule
-
-        return mymodule.import_module(
-            modname, level=level, relative_only=level and level >= 1
-        )
-
-    def real_name(self, asname):
-        """get name from 'as' name"""
-        for name, _asname in self.names:
-            if name == "*":
-                return asname
-            if not _asname:
-                name = name.split(".", 1)[0]
-                _asname = name
-            if asname == _asname:
-                return name
-        raise exceptions.AttributeInferenceError(
-            "Could not find original name for {attribute} in {target!r}",
-            target=self,
-            attribute=asname,
-        )
-
-
-class MultiLineBlockMixin:
-    """Mixin for nodes with multi-line blocks, e.g. For and FunctionDef.
-    Note that this does not apply to every node with a `body` field.
-    For instance, an If node has a multi-line body, but the body of an
-    IfExpr is not multi-line, and hence cannot contain Return nodes,
-    Assign nodes, etc.
-    """
-
-    @decorators.cachedproperty
-    def _multi_line_blocks(self):
-        return tuple(getattr(self, field) for field in self._multi_line_block_fields)
-
-    def _get_return_nodes_skip_functions(self):
-        for block in self._multi_line_blocks:
-            for child_node in block:
-                if child_node.is_function:
-                    continue
-                yield from child_node._get_return_nodes_skip_functions()
-
-    def _get_yield_nodes_skip_lambdas(self):
-        for block in self._multi_line_blocks:
-            for child_node in block:
-                if child_node.is_lambda:
-                    continue
-                yield from child_node._get_yield_nodes_skip_lambdas()
-
-    @decorators.cached
-    def _get_assign_nodes(self):
-        children_assign_nodes = (
-            child_node._get_assign_nodes()
-            for block in self._multi_line_blocks
-            for child_node in block
-        )
-        return list(itertools.chain.from_iterable(children_assign_nodes))
-
-
-class NoChildrenMixin:
-    """Mixin for nodes with no children, e.g. Pass."""
-
-    def get_children(self):
-        yield from ()
diff --git a/venv/Lib/site-packages/astroid/modutils.py b/venv/Lib/site-packages/astroid/modutils.py
deleted file mode 100644
index 0c009b1..0000000
--- a/venv/Lib/site-packages/astroid/modutils.py
+++ /dev/null
@@ -1,698 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2014 Denis Laxalde <denis.laxalde@logilab.fr>
-# Copyright (c) 2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Radosław Ganczarek <radoslaw@ganczarek.in>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2018 Mario Corchero <mcorcherojim@bloomberg.net>
-# Copyright (c) 2018 Mario Corchero <mariocj89@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Python modules manipulation utility functions.
-
-:type PY_SOURCE_EXTS: tuple(str)
-:var PY_SOURCE_EXTS: list of possible python source file extension
-
-:type STD_LIB_DIRS: set of str
-:var STD_LIB_DIRS: directories where standard modules are located
-
-:type BUILTIN_MODULES: dict
-:var BUILTIN_MODULES: dictionary with builtin module names has key
-"""
-import imp
-import os
-import platform
-import sys
-import itertools
-from distutils.sysconfig import get_python_lib  # pylint: disable=import-error
-
-# pylint: disable=import-error, no-name-in-module
-from distutils.errors import DistutilsPlatformError
-
-# distutils is replaced by virtualenv with a module that does
-# weird path manipulations in order to get to the
-# real distutils module.
-
-from .interpreter._import import spec
-from .interpreter._import import util
-
-if sys.platform.startswith("win"):
-    PY_SOURCE_EXTS = ("py", "pyw")
-    PY_COMPILED_EXTS = ("dll", "pyd")
-else:
-    PY_SOURCE_EXTS = ("py",)
-    PY_COMPILED_EXTS = ("so",)
-
-
-try:
-    # The explicit sys.prefix is to work around a patch in virtualenv that
-    # replaces the 'real' sys.prefix (i.e. the location of the binary)
-    # with the prefix from which the virtualenv was created. This throws
-    # off the detection logic for standard library modules, thus the
-    # workaround.
-    STD_LIB_DIRS = {
-        get_python_lib(standard_lib=True, prefix=sys.prefix),
-        # Take care of installations where exec_prefix != prefix.
-        get_python_lib(standard_lib=True, prefix=sys.exec_prefix),
-        get_python_lib(standard_lib=True),
-    }
-# get_python_lib(standard_lib=1) is not available on pypy, set STD_LIB_DIR to
-# non-valid path, see https://bugs.pypy.org/issue1164
-except DistutilsPlatformError:
-    STD_LIB_DIRS = set()
-
-if os.name == "nt":
-    STD_LIB_DIRS.add(os.path.join(sys.prefix, "dlls"))
-    try:
-        # real_prefix is defined when running inside virtual environments,
-        # created with the **virtualenv** library.
-        STD_LIB_DIRS.add(os.path.join(sys.real_prefix, "dlls"))
-    except AttributeError:
-        # sys.base_exec_prefix is always defined, but in a virtual environment
-        # created with the stdlib **venv** module, it points to the original
-        # installation, if the virtual env is activated.
-        try:
-            STD_LIB_DIRS.add(os.path.join(sys.base_exec_prefix, "dlls"))
-        except AttributeError:
-            pass
-
-if platform.python_implementation() == "PyPy":
-    _root = os.path.join(sys.prefix, "lib_pypy")
-    STD_LIB_DIRS.add(_root)
-    try:
-        # real_prefix is defined when running inside virtualenv.
-        STD_LIB_DIRS.add(os.path.join(sys.real_prefix, "lib_pypy"))
-    except AttributeError:
-        pass
-    del _root
-if os.name == "posix":
-    # Need the real prefix is we're under a virtualenv, otherwise
-    # the usual one will do.
-    try:
-        prefix = sys.real_prefix
-    except AttributeError:
-        prefix = sys.prefix
-
-    def _posix_path(path):
-        base_python = "python%d.%d" % sys.version_info[:2]
-        return os.path.join(prefix, path, base_python)
-
-    STD_LIB_DIRS.add(_posix_path("lib"))
-    if sys.maxsize > 2 ** 32:
-        # This tries to fix a problem with /usr/lib64 builds,
-        # where systems are running both 32-bit and 64-bit code
-        # on the same machine, which reflects into the places where
-        # standard library could be found. More details can be found
-        # here http://bugs.python.org/issue1294959.
-        # An easy reproducing case would be
-        # https://github.com/PyCQA/pylint/issues/712#issuecomment-163178753
-        STD_LIB_DIRS.add(_posix_path("lib64"))
-
-EXT_LIB_DIRS = {get_python_lib(), get_python_lib(True)}
-IS_JYTHON = platform.python_implementation() == "Jython"
-BUILTIN_MODULES = dict.fromkeys(sys.builtin_module_names, True)
-
-
-class NoSourceFile(Exception):
-    """exception raised when we are not able to get a python
-    source file for a precompiled file
-    """
-
-
-def _normalize_path(path):
-    return os.path.normcase(os.path.abspath(path))
-
-
-def _canonicalize_path(path):
-    return os.path.realpath(os.path.expanduser(path))
-
-
-def _path_from_filename(filename, is_jython=IS_JYTHON):
-    if not is_jython:
-        return filename
-    head, has_pyclass, _ = filename.partition("$py.class")
-    if has_pyclass:
-        return head + ".py"
-    return filename
-
-
-def _handle_blacklist(blacklist, dirnames, filenames):
-    """remove files/directories in the black list
-
-    dirnames/filenames are usually from os.walk
-    """
-    for norecurs in blacklist:
-        if norecurs in dirnames:
-            dirnames.remove(norecurs)
-        elif norecurs in filenames:
-            filenames.remove(norecurs)
-
-
-_NORM_PATH_CACHE = {}
-
-
-def _cache_normalize_path(path):
-    """abspath with caching"""
-    # _module_file calls abspath on every path in sys.path every time it's
-    # called; on a larger codebase this easily adds up to half a second just
-    # assembling path components. This cache alleviates that.
-    try:
-        return _NORM_PATH_CACHE[path]
-    except KeyError:
-        if not path:  # don't cache result for ''
-            return _normalize_path(path)
-        result = _NORM_PATH_CACHE[path] = _normalize_path(path)
-        return result
-
-
-def load_module_from_name(dotted_name, path=None, use_sys=True):
-    """Load a Python module from its name.
-
-    :type dotted_name: str
-    :param dotted_name: python name of a module or package
-
-    :type path: list or None
-    :param path:
-      optional list of path where the module or package should be
-      searched (use sys.path if nothing or None is given)
-
-    :type use_sys: bool
-    :param use_sys:
-      boolean indicating whether the sys.modules dictionary should be
-      used or not
-
-
-    :raise ImportError: if the module or package is not found
-
-    :rtype: module
-    :return: the loaded module
-    """
-    return load_module_from_modpath(dotted_name.split("."), path, use_sys)
-
-
-def load_module_from_modpath(parts, path=None, use_sys=1):
-    """Load a python module from its split name.
-
-    :type parts: list(str) or tuple(str)
-    :param parts:
-      python name of a module or package split on '.'
-
-    :type path: list or None
-    :param path:
-      optional list of path where the module or package should be
-      searched (use sys.path if nothing or None is given)
-
-    :type use_sys: bool
-    :param use_sys:
-      boolean indicating whether the sys.modules dictionary should be used or not
-
-    :raise ImportError: if the module or package is not found
-
-    :rtype: module
-    :return: the loaded module
-    """
-    if use_sys:
-        try:
-            return sys.modules[".".join(parts)]
-        except KeyError:
-            pass
-    modpath = []
-    prevmodule = None
-    for part in parts:
-        modpath.append(part)
-        curname = ".".join(modpath)
-        module = None
-        if len(modpath) != len(parts):
-            # even with use_sys=False, should try to get outer packages from sys.modules
-            module = sys.modules.get(curname)
-        elif use_sys:
-            # because it may have been indirectly loaded through a parent
-            module = sys.modules.get(curname)
-        if module is None:
-            mp_file, mp_filename, mp_desc = imp.find_module(part, path)
-            module = imp.load_module(curname, mp_file, mp_filename, mp_desc)
-            # mp_file still needs to be closed.
-            if mp_file:
-                mp_file.close()
-        if prevmodule:
-            setattr(prevmodule, part, module)
-        _file = getattr(module, "__file__", "")
-        prevmodule = module
-        if not _file and util.is_namespace(curname):
-            continue
-        if not _file and len(modpath) != len(parts):
-            raise ImportError("no module in %s" % ".".join(parts[len(modpath) :]))
-        path = [os.path.dirname(_file)]
-    return module
-
-
-def load_module_from_file(filepath, path=None, use_sys=True, extrapath=None):
-    """Load a Python module from it's path.
-
-    :type filepath: str
-    :param filepath: path to the python module or package
-
-    :type path: list or None
-    :param path:
-      optional list of path where the module or package should be
-      searched (use sys.path if nothing or None is given)
-
-    :type use_sys: bool
-    :param use_sys:
-      boolean indicating whether the sys.modules dictionary should be
-      used or not
-
-
-    :raise ImportError: if the module or package is not found
-
-    :rtype: module
-    :return: the loaded module
-    """
-    modpath = modpath_from_file(filepath, extrapath)
-    return load_module_from_modpath(modpath, path, use_sys)
-
-
-def check_modpath_has_init(path, mod_path):
-    """check there are some __init__.py all along the way"""
-    modpath = []
-    for part in mod_path:
-        modpath.append(part)
-        path = os.path.join(path, part)
-        if not _has_init(path):
-            old_namespace = util.is_namespace(".".join(modpath))
-            if not old_namespace:
-                return False
-    return True
-
-
-def _get_relative_base_path(filename, path_to_check):
-    """Extracts the relative mod path of the file to import from
-
-    Check if a file is within the passed in path and if so, returns the
-    relative mod path from the one passed in.
-
-    If the filename is no in path_to_check, returns None
-
-    Note this function will look for both abs and realpath of the file,
-    this allows to find the relative base path even if the file is a
-    symlink of a file in the passed in path
-
-    Examples:
-        _get_relative_base_path("/a/b/c/d.py", "/a/b") ->  ["c","d"]
-        _get_relative_base_path("/a/b/c/d.py", "/dev") ->  None
-    """
-    importable_path = None
-    path_to_check = os.path.normcase(path_to_check)
-    abs_filename = os.path.abspath(filename)
-    if os.path.normcase(abs_filename).startswith(path_to_check):
-        importable_path = abs_filename
-
-    real_filename = os.path.realpath(filename)
-    if os.path.normcase(real_filename).startswith(path_to_check):
-        importable_path = real_filename
-
-    if importable_path:
-        base_path = os.path.splitext(importable_path)[0]
-        relative_base_path = base_path[len(path_to_check) :]
-        return [pkg for pkg in relative_base_path.split(os.sep) if pkg]
-
-    return None
-
-
-def modpath_from_file_with_callback(filename, extrapath=None, is_package_cb=None):
-    filename = os.path.expanduser(_path_from_filename(filename))
-
-    if extrapath is not None:
-        for path_ in itertools.chain(map(_canonicalize_path, extrapath), extrapath):
-            path = os.path.abspath(path_)
-            if not path:
-                continue
-            submodpath = _get_relative_base_path(filename, path)
-            if not submodpath:
-                continue
-            if is_package_cb(path, submodpath[:-1]):
-                return extrapath[path_].split(".") + submodpath
-
-    for path in itertools.chain(map(_canonicalize_path, sys.path), sys.path):
-        path = _cache_normalize_path(path)
-        if not path:
-            continue
-        modpath = _get_relative_base_path(filename, path)
-        if not modpath:
-            continue
-        if is_package_cb(path, modpath[:-1]):
-            return modpath
-
-    raise ImportError(
-        "Unable to find module for %s in %s" % (filename, ", \n".join(sys.path))
-    )
-
-
-def modpath_from_file(filename, extrapath=None):
-    """given a file path return the corresponding split module's name
-    (i.e name of a module or package split on '.')
-
-    :type filename: str
-    :param filename: file's path for which we want the module's name
-
-    :type extrapath: dict
-    :param extrapath:
-      optional extra search path, with path as key and package name for the path
-      as value. This is usually useful to handle package split in multiple
-      directories using __path__ trick.
-
-
-    :raise ImportError:
-      if the corresponding module's name has not been found
-
-    :rtype: list(str)
-    :return: the corresponding split module's name
-    """
-    return modpath_from_file_with_callback(filename, extrapath, check_modpath_has_init)
-
-
-def file_from_modpath(modpath, path=None, context_file=None):
-    return file_info_from_modpath(modpath, path, context_file).location
-
-
-def file_info_from_modpath(modpath, path=None, context_file=None):
-    """given a mod path (i.e. split module / package name), return the
-    corresponding file, giving priority to source file over precompiled
-    file if it exists
-
-    :type modpath: list or tuple
-    :param modpath:
-      split module's name (i.e name of a module or package split
-      on '.')
-      (this means explicit relative imports that start with dots have
-      empty strings in this list!)
-
-    :type path: list or None
-    :param path:
-      optional list of path where the module or package should be
-      searched (use sys.path if nothing or None is given)
-
-    :type context_file: str or None
-    :param context_file:
-      context file to consider, necessary if the identifier has been
-      introduced using a relative import unresolvable in the actual
-      context (i.e. modutils)
-
-    :raise ImportError: if there is no such module in the directory
-
-    :rtype: (str or None, import type)
-    :return:
-      the path to the module's file or None if it's an integrated
-      builtin module such as 'sys'
-    """
-    if context_file is not None:
-        context = os.path.dirname(context_file)
-    else:
-        context = context_file
-    if modpath[0] == "xml":
-        # handle _xmlplus
-        try:
-            return _spec_from_modpath(["_xmlplus"] + modpath[1:], path, context)
-        except ImportError:
-            return _spec_from_modpath(modpath, path, context)
-    elif modpath == ["os", "path"]:
-        # FIXME: currently ignoring search_path...
-        return spec.ModuleSpec(
-            name="os.path", location=os.path.__file__, module_type=imp.PY_SOURCE
-        )
-    return _spec_from_modpath(modpath, path, context)
-
-
-def get_module_part(dotted_name, context_file=None):
-    """given a dotted name return the module part of the name :
-
-    >>> get_module_part('astroid.as_string.dump')
-    'astroid.as_string'
-
-    :type dotted_name: str
-    :param dotted_name: full name of the identifier we are interested in
-
-    :type context_file: str or None
-    :param context_file:
-      context file to consider, necessary if the identifier has been
-      introduced using a relative import unresolvable in the actual
-      context (i.e. modutils)
-
-
-    :raise ImportError: if there is no such module in the directory
-
-    :rtype: str or None
-    :return:
-      the module part of the name or None if we have not been able at
-      all to import the given name
-
-    XXX: deprecated, since it doesn't handle package precedence over module
-    (see #10066)
-    """
-    # os.path trick
-    if dotted_name.startswith("os.path"):
-        return "os.path"
-    parts = dotted_name.split(".")
-    if context_file is not None:
-        # first check for builtin module which won't be considered latter
-        # in that case (path != None)
-        if parts[0] in BUILTIN_MODULES:
-            if len(parts) > 2:
-                raise ImportError(dotted_name)
-            return parts[0]
-        # don't use += or insert, we want a new list to be created !
-    path = None
-    starti = 0
-    if parts[0] == "":
-        assert (
-            context_file is not None
-        ), "explicit relative import, but no context_file?"
-        path = []  # prevent resolving the import non-relatively
-        starti = 1
-    while parts[starti] == "":  # for all further dots: change context
-        starti += 1
-        context_file = os.path.dirname(context_file)
-    for i in range(starti, len(parts)):
-        try:
-            file_from_modpath(
-                parts[starti : i + 1], path=path, context_file=context_file
-            )
-        except ImportError:
-            if i < max(1, len(parts) - 2):
-                raise
-            return ".".join(parts[:i])
-    return dotted_name
-
-
-def get_module_files(src_directory, blacklist, list_all=False):
-    """given a package directory return a list of all available python
-    module's files in the package and its subpackages
-
-    :type src_directory: str
-    :param src_directory:
-      path of the directory corresponding to the package
-
-    :type blacklist: list or tuple
-    :param blacklist: iterable
-      list of files or directories to ignore.
-
-    :type list_all: bool
-    :param list_all:
-        get files from all paths, including ones without __init__.py
-
-    :rtype: list
-    :return:
-      the list of all available python module's files in the package and
-      its subpackages
-    """
-    files = []
-    for directory, dirnames, filenames in os.walk(src_directory):
-        if directory in blacklist:
-            continue
-        _handle_blacklist(blacklist, dirnames, filenames)
-        # check for __init__.py
-        if not list_all and "__init__.py" not in filenames:
-            dirnames[:] = ()
-            continue
-        for filename in filenames:
-            if _is_python_file(filename):
-                src = os.path.join(directory, filename)
-                files.append(src)
-    return files
-
-
-def get_source_file(filename, include_no_ext=False):
-    """given a python module's file name return the matching source file
-    name (the filename will be returned identically if it's already an
-    absolute path to a python source file...)
-
-    :type filename: str
-    :param filename: python module's file name
-
-
-    :raise NoSourceFile: if no source file exists on the file system
-
-    :rtype: str
-    :return: the absolute path of the source file if it exists
-    """
-    filename = os.path.abspath(_path_from_filename(filename))
-    base, orig_ext = os.path.splitext(filename)
-    for ext in PY_SOURCE_EXTS:
-        source_path = "%s.%s" % (base, ext)
-        if os.path.exists(source_path):
-            return source_path
-    if include_no_ext and not orig_ext and os.path.exists(base):
-        return base
-    raise NoSourceFile(filename)
-
-
-def is_python_source(filename):
-    """
-    rtype: bool
-    return: True if the filename is a python source file
-    """
-    return os.path.splitext(filename)[1][1:] in PY_SOURCE_EXTS
-
-
-def is_standard_module(modname, std_path=None):
-    """try to guess if a module is a standard python module (by default,
-    see `std_path` parameter's description)
-
-    :type modname: str
-    :param modname: name of the module we are interested in
-
-    :type std_path: list(str) or tuple(str)
-    :param std_path: list of path considered has standard
-
-
-    :rtype: bool
-    :return:
-      true if the module:
-      - is located on the path listed in one of the directory in `std_path`
-      - is a built-in module
-    """
-    modname = modname.split(".")[0]
-    try:
-        filename = file_from_modpath([modname])
-    except ImportError:
-        # import failed, i'm probably not so wrong by supposing it's
-        # not standard...
-        return False
-    # modules which are not living in a file are considered standard
-    # (sys and __builtin__ for instance)
-    if filename is None:
-        # we assume there are no namespaces in stdlib
-        return not util.is_namespace(modname)
-    filename = _normalize_path(filename)
-    for path in EXT_LIB_DIRS:
-        if filename.startswith(_cache_normalize_path(path)):
-            return False
-    if std_path is None:
-        std_path = STD_LIB_DIRS
-    for path in std_path:
-        if filename.startswith(_cache_normalize_path(path)):
-            return True
-    return False
-
-
-def is_relative(modname, from_file):
-    """return true if the given module name is relative to the given
-    file name
-
-    :type modname: str
-    :param modname: name of the module we are interested in
-
-    :type from_file: str
-    :param from_file:
-      path of the module from which modname has been imported
-
-    :rtype: bool
-    :return:
-      true if the module has been imported relatively to `from_file`
-    """
-    if not os.path.isdir(from_file):
-        from_file = os.path.dirname(from_file)
-    if from_file in sys.path:
-        return False
-    try:
-        stream, _, _ = imp.find_module(modname.split(".")[0], [from_file])
-
-        # Close the stream to avoid ResourceWarnings.
-        if stream:
-            stream.close()
-        return True
-    except ImportError:
-        return False
-
-
-# internal only functions #####################################################
-
-
-def _spec_from_modpath(modpath, path=None, context=None):
-    """given a mod path (i.e. split module / package name), return the
-    corresponding spec
-
-    this function is used internally, see `file_from_modpath`'s
-    documentation for more information
-    """
-    assert modpath
-    location = None
-    if context is not None:
-        try:
-            found_spec = spec.find_spec(modpath, [context])
-            location = found_spec.location
-        except ImportError:
-            found_spec = spec.find_spec(modpath, path)
-            location = found_spec.location
-    else:
-        found_spec = spec.find_spec(modpath, path)
-    if found_spec.type == spec.ModuleType.PY_COMPILED:
-        try:
-            location = get_source_file(found_spec.location)
-            return found_spec._replace(
-                location=location, type=spec.ModuleType.PY_SOURCE
-            )
-        except NoSourceFile:
-            return found_spec._replace(location=location)
-    elif found_spec.type == spec.ModuleType.C_BUILTIN:
-        # integrated builtin module
-        return found_spec._replace(location=None)
-    elif found_spec.type == spec.ModuleType.PKG_DIRECTORY:
-        location = _has_init(found_spec.location)
-        return found_spec._replace(location=location, type=spec.ModuleType.PY_SOURCE)
-    return found_spec
-
-
-def _is_python_file(filename):
-    """return true if the given filename should be considered as a python file
-
-    .pyc and .pyo are ignored
-    """
-    return filename.endswith((".py", ".so", ".pyd", ".pyw"))
-
-
-def _has_init(directory):
-    """if the given directory has a valid __init__ file, return its path,
-    else return None
-    """
-    mod_or_pack = os.path.join(directory, "__init__")
-    for ext in PY_SOURCE_EXTS + ("pyc", "pyo"):
-        if os.path.exists(mod_or_pack + "." + ext):
-            return mod_or_pack + "." + ext
-    return None
-
-
-def is_namespace(specobj):
-    return specobj.type == spec.ModuleType.PY_NAMESPACE
-
-
-def is_directory(specobj):
-    return specobj.type == spec.ModuleType.PKG_DIRECTORY
diff --git a/venv/Lib/site-packages/astroid/node_classes.py b/venv/Lib/site-packages/astroid/node_classes.py
deleted file mode 100644
index 994c96b..0000000
--- a/venv/Lib/site-packages/astroid/node_classes.py
+++ /dev/null
@@ -1,4775 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2009-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016-2017 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2016 Jared Garst <jgarst@users.noreply.github.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016 Dave Baum <dbaum@google.com>
-# Copyright (c) 2017-2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 rr- <rr-@sakuya.pl>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 brendanator <brendan.maginnis@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 HoverHell <hoverhell@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-# pylint: disable=too-many-lines; https://github.com/PyCQA/astroid/issues/465
-
-"""Module for some node classes. More nodes in scoped_nodes.py
-"""
-
-import abc
-import builtins as builtins_mod
-import itertools
-import pprint
-import sys
-from functools import lru_cache, singledispatch as _singledispatch
-
-from astroid import as_string
-from astroid import bases
-from astroid import context as contextmod
-from astroid import decorators
-from astroid import exceptions
-from astroid import manager
-from astroid import mixins
-from astroid import util
-
-
-BUILTINS = builtins_mod.__name__
-MANAGER = manager.AstroidManager()
-PY38 = sys.version_info[:2] >= (3, 8)
-
-
-def _is_const(value):
-    return isinstance(value, tuple(CONST_CLS))
-
-
-@decorators.raise_if_nothing_inferred
-def unpack_infer(stmt, context=None):
-    """recursively generate nodes inferred by the given statement.
-    If the inferred value is a list or a tuple, recurse on the elements
-    """
-    if isinstance(stmt, (List, Tuple)):
-        for elt in stmt.elts:
-            if elt is util.Uninferable:
-                yield elt
-                continue
-            yield from unpack_infer(elt, context)
-        return dict(node=stmt, context=context)
-    # if inferred is a final node, return it and stop
-    inferred = next(stmt.infer(context))
-    if inferred is stmt:
-        yield inferred
-        return dict(node=stmt, context=context)
-    # else, infer recursively, except Uninferable object that should be returned as is
-    for inferred in stmt.infer(context):
-        if inferred is util.Uninferable:
-            yield inferred
-        else:
-            yield from unpack_infer(inferred, context)
-
-    return dict(node=stmt, context=context)
-
-
-def are_exclusive(
-    stmt1, stmt2, exceptions=None
-):  # pylint: disable=redefined-outer-name
-    """return true if the two given statements are mutually exclusive
-
-    `exceptions` may be a list of exception names. If specified, discard If
-    branches and check one of the statement is in an exception handler catching
-    one of the given exceptions.
-
-    algorithm :
-     1) index stmt1's parents
-     2) climb among stmt2's parents until we find a common parent
-     3) if the common parent is a If or TryExcept statement, look if nodes are
-        in exclusive branches
-    """
-    # index stmt1's parents
-    stmt1_parents = {}
-    children = {}
-    node = stmt1.parent
-    previous = stmt1
-    while node:
-        stmt1_parents[node] = 1
-        children[node] = previous
-        previous = node
-        node = node.parent
-    # climb among stmt2's parents until we find a common parent
-    node = stmt2.parent
-    previous = stmt2
-    while node:
-        if node in stmt1_parents:
-            # if the common parent is a If or TryExcept statement, look if
-            # nodes are in exclusive branches
-            if isinstance(node, If) and exceptions is None:
-                if (
-                    node.locate_child(previous)[1]
-                    is not node.locate_child(children[node])[1]
-                ):
-                    return True
-            elif isinstance(node, TryExcept):
-                c2attr, c2node = node.locate_child(previous)
-                c1attr, c1node = node.locate_child(children[node])
-                if c1node is not c2node:
-                    first_in_body_caught_by_handlers = (
-                        c2attr == "handlers"
-                        and c1attr == "body"
-                        and previous.catch(exceptions)
-                    )
-                    second_in_body_caught_by_handlers = (
-                        c2attr == "body"
-                        and c1attr == "handlers"
-                        and children[node].catch(exceptions)
-                    )
-                    first_in_else_other_in_handlers = (
-                        c2attr == "handlers" and c1attr == "orelse"
-                    )
-                    second_in_else_other_in_handlers = (
-                        c2attr == "orelse" and c1attr == "handlers"
-                    )
-                    if any(
-                        (
-                            first_in_body_caught_by_handlers,
-                            second_in_body_caught_by_handlers,
-                            first_in_else_other_in_handlers,
-                            second_in_else_other_in_handlers,
-                        )
-                    ):
-                        return True
-                elif c2attr == "handlers" and c1attr == "handlers":
-                    return previous is not children[node]
-            return False
-        previous = node
-        node = node.parent
-    return False
-
-
-# getitem() helpers.
-
-_SLICE_SENTINEL = object()
-
-
-def _slice_value(index, context=None):
-    """Get the value of the given slice index."""
-
-    if isinstance(index, Const):
-        if isinstance(index.value, (int, type(None))):
-            return index.value
-    elif index is None:
-        return None
-    else:
-        # Try to infer what the index actually is.
-        # Since we can't return all the possible values,
-        # we'll stop at the first possible value.
-        try:
-            inferred = next(index.infer(context=context))
-        except exceptions.InferenceError:
-            pass
-        else:
-            if isinstance(inferred, Const):
-                if isinstance(inferred.value, (int, type(None))):
-                    return inferred.value
-
-    # Use a sentinel, because None can be a valid
-    # value that this function can return,
-    # as it is the case for unspecified bounds.
-    return _SLICE_SENTINEL
-
-
-def _infer_slice(node, context=None):
-    lower = _slice_value(node.lower, context)
-    upper = _slice_value(node.upper, context)
-    step = _slice_value(node.step, context)
-    if all(elem is not _SLICE_SENTINEL for elem in (lower, upper, step)):
-        return slice(lower, upper, step)
-
-    raise exceptions.AstroidTypeError(
-        message="Could not infer slice used in subscript",
-        node=node,
-        index=node.parent,
-        context=context,
-    )
-
-
-def _container_getitem(instance, elts, index, context=None):
-    """Get a slice or an item, using the given *index*, for the given sequence."""
-    try:
-        if isinstance(index, Slice):
-            index_slice = _infer_slice(index, context=context)
-            new_cls = instance.__class__()
-            new_cls.elts = elts[index_slice]
-            new_cls.parent = instance.parent
-            return new_cls
-        if isinstance(index, Const):
-            return elts[index.value]
-    except IndexError as exc:
-        raise exceptions.AstroidIndexError(
-            message="Index {index!s} out of range",
-            node=instance,
-            index=index,
-            context=context,
-        ) from exc
-    except TypeError as exc:
-        raise exceptions.AstroidTypeError(
-            message="Type error {error!r}", node=instance, index=index, context=context
-        ) from exc
-
-    raise exceptions.AstroidTypeError("Could not use %s as subscript index" % index)
-
-
-OP_PRECEDENCE = {
-    op: precedence
-    for precedence, ops in enumerate(
-        [
-            ["Lambda"],  # lambda x: x + 1
-            ["IfExp"],  # 1 if True else 2
-            ["or"],
-            ["and"],
-            ["not"],
-            ["Compare"],  # in, not in, is, is not, <, <=, >, >=, !=, ==
-            ["|"],
-            ["^"],
-            ["&"],
-            ["<<", ">>"],
-            ["+", "-"],
-            ["*", "@", "/", "//", "%"],
-            ["UnaryOp"],  # +, -, ~
-            ["**"],
-            ["Await"],
-        ]
-    )
-    for op in ops
-}
-
-
-class NodeNG:
-    """ A node of the new Abstract Syntax Tree (AST).
-
-    This is the base class for all Astroid node classes.
-    """
-
-    is_statement = False
-    """Whether this node indicates a statement.
-
-    :type: bool
-    """
-    optional_assign = False  # True for For (and for Comprehension if py <3.0)
-    """Whether this node optionally assigns a variable.
-
-    This is for loop assignments because loop won't necessarily perform an
-    assignment if the loop has no iterations.
-    This is also the case from comprehensions in Python 2.
-
-    :type: bool
-    """
-    is_function = False  # True for FunctionDef nodes
-    """Whether this node indicates a function.
-
-    :type: bool
-    """
-    is_lambda = False
-    # Attributes below are set by the builder module or by raw factories
-    lineno = None
-    """The line that this node appears on in the source code.
-
-    :type: int or None
-    """
-    col_offset = None
-    """The column that this node appears on in the source code.
-
-    :type: int or None
-    """
-    parent = None
-    """The parent node in the syntax tree.
-
-    :type: NodeNG or None
-    """
-    _astroid_fields = ()
-    """Node attributes that contain child nodes.
-
-    This is redefined in most concrete classes.
-
-    :type: tuple(str)
-    """
-    _other_fields = ()
-    """Node attributes that do not contain child nodes.
-
-    :type: tuple(str)
-    """
-    _other_other_fields = ()
-    """Attributes that contain AST-dependent fields.
-
-    :type: tuple(str)
-    """
-    # instance specific inference function infer(node, context)
-    _explicit_inference = None
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        """
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.lineno = lineno
-        self.col_offset = col_offset
-        self.parent = parent
-
-    def infer(self, context=None, **kwargs):
-        """Get a generator of the inferred values.
-
-        This is the main entry point to the inference system.
-
-        .. seealso:: :ref:`inference`
-
-        If the instance has some explicit inference function set, it will be
-        called instead of the default interface.
-
-        :returns: The inferred values.
-        :rtype: iterable
-        """
-        if context is not None:
-            context = context.extra_context.get(self, context)
-        if self._explicit_inference is not None:
-            # explicit_inference is not bound, give it self explicitly
-            try:
-                # pylint: disable=not-callable
-                return self._explicit_inference(self, context, **kwargs)
-            except exceptions.UseInferenceDefault:
-                pass
-
-        if not context:
-            return self._infer(context, **kwargs)
-
-        key = (self, context.lookupname, context.callcontext, context.boundnode)
-        if key in context.inferred:
-            return iter(context.inferred[key])
-
-        gen = context.cache_generator(key, self._infer(context, **kwargs))
-        return util.limit_inference(gen, MANAGER.max_inferable_values)
-
-    def _repr_name(self):
-        """Get a name for nice representation.
-
-        This is either :attr:`name`, :attr:`attrname`, or the empty string.
-
-        :returns: The nice name.
-        :rtype: str
-        """
-        names = {"name", "attrname"}
-        if all(name not in self._astroid_fields for name in names):
-            return getattr(self, "name", getattr(self, "attrname", ""))
-        return ""
-
-    def __str__(self):
-        rname = self._repr_name()
-        cname = type(self).__name__
-        if rname:
-            string = "%(cname)s.%(rname)s(%(fields)s)"
-            alignment = len(cname) + len(rname) + 2
-        else:
-            string = "%(cname)s(%(fields)s)"
-            alignment = len(cname) + 1
-        result = []
-        for field in self._other_fields + self._astroid_fields:
-            value = getattr(self, field)
-            width = 80 - len(field) - alignment
-            lines = pprint.pformat(value, indent=2, width=width).splitlines(True)
-
-            inner = [lines[0]]
-            for line in lines[1:]:
-                inner.append(" " * alignment + line)
-            result.append("%s=%s" % (field, "".join(inner)))
-
-        return string % {
-            "cname": cname,
-            "rname": rname,
-            "fields": (",\n" + " " * alignment).join(result),
-        }
-
-    def __repr__(self):
-        rname = self._repr_name()
-        if rname:
-            string = "<%(cname)s.%(rname)s l.%(lineno)s at 0x%(id)x>"
-        else:
-            string = "<%(cname)s l.%(lineno)s at 0x%(id)x>"
-        return string % {
-            "cname": type(self).__name__,
-            "rname": rname,
-            "lineno": self.fromlineno,
-            "id": id(self),
-        }
-
-    def accept(self, visitor):
-        """Visit this node using the given visitor."""
-        func = getattr(visitor, "visit_" + self.__class__.__name__.lower())
-        return func(self)
-
-    def get_children(self):
-        """Get the child nodes below this node.
-
-        :returns: The children.
-        :rtype: iterable(NodeNG)
-        """
-        for field in self._astroid_fields:
-            attr = getattr(self, field)
-            if attr is None:
-                continue
-            if isinstance(attr, (list, tuple)):
-                yield from attr
-            else:
-                yield attr
-
-    def last_child(self):
-        """An optimized version of list(get_children())[-1]
-
-        :returns: The last child, or None if no children exist.
-        :rtype: NodeNG or None
-        """
-        for field in self._astroid_fields[::-1]:
-            attr = getattr(self, field)
-            if not attr:  # None or empty listy / tuple
-                continue
-            if isinstance(attr, (list, tuple)):
-                return attr[-1]
-
-            return attr
-        return None
-
-    def parent_of(self, node):
-        """Check if this node is the parent of the given node.
-
-        :param node: The node to check if it is the child.
-        :type node: NodeNG
-
-        :returns: True if this node is the parent of the given node,
-            False otherwise.
-        :rtype: bool
-        """
-        parent = node.parent
-        while parent is not None:
-            if self is parent:
-                return True
-            parent = parent.parent
-        return False
-
-    def statement(self):
-        """The first parent node, including self, marked as statement node.
-
-        :returns: The first parent statement.
-        :rtype: NodeNG
-        """
-        if self.is_statement:
-            return self
-        return self.parent.statement()
-
-    def frame(self):
-        """The first parent frame node.
-
-        A frame node is a :class:`Module`, :class:`FunctionDef`,
-        or :class:`ClassDef`.
-
-        :returns: The first parent frame node.
-        :rtype: Module or FunctionDef or ClassDef
-        """
-        return self.parent.frame()
-
-    def scope(self):
-        """The first parent node defining a new scope.
-
-        :returns: The first parent scope node.
-        :rtype: Module or FunctionDef or ClassDef or Lambda or GenExpr
-        """
-        if self.parent:
-            return self.parent.scope()
-        return None
-
-    def root(self):
-        """Return the root node of the syntax tree.
-
-        :returns: The root node.
-        :rtype: Module
-        """
-        if self.parent:
-            return self.parent.root()
-        return self
-
-    def child_sequence(self, child):
-        """Search for the sequence that contains this child.
-
-        :param child: The child node to search sequences for.
-        :type child: NodeNG
-
-        :returns: The sequence containing the given child node.
-        :rtype: iterable(NodeNG)
-
-        :raises AstroidError: If no sequence could be found that contains
-            the given child.
-        """
-        for field in self._astroid_fields:
-            node_or_sequence = getattr(self, field)
-            if node_or_sequence is child:
-                return [node_or_sequence]
-            # /!\ compiler.ast Nodes have an __iter__ walking over child nodes
-            if (
-                isinstance(node_or_sequence, (tuple, list))
-                and child in node_or_sequence
-            ):
-                return node_or_sequence
-
-        msg = "Could not find %s in %s's children"
-        raise exceptions.AstroidError(msg % (repr(child), repr(self)))
-
-    def locate_child(self, child):
-        """Find the field of this node that contains the given child.
-
-        :param child: The child node to search fields for.
-        :type child: NodeNG
-
-        :returns: A tuple of the name of the field that contains the child,
-            and the sequence or node that contains the child node.
-        :rtype: tuple(str, iterable(NodeNG) or NodeNG)
-
-        :raises AstroidError: If no field could be found that contains
-            the given child.
-        """
-        for field in self._astroid_fields:
-            node_or_sequence = getattr(self, field)
-            # /!\ compiler.ast Nodes have an __iter__ walking over child nodes
-            if child is node_or_sequence:
-                return field, child
-            if (
-                isinstance(node_or_sequence, (tuple, list))
-                and child in node_or_sequence
-            ):
-                return field, node_or_sequence
-        msg = "Could not find %s in %s's children"
-        raise exceptions.AstroidError(msg % (repr(child), repr(self)))
-
-    # FIXME : should we merge child_sequence and locate_child ? locate_child
-    # is only used in are_exclusive, child_sequence one time in pylint.
-
-    def next_sibling(self):
-        """The next sibling statement node.
-
-        :returns: The next sibling statement node.
-        :rtype: NodeNG or None
-        """
-        return self.parent.next_sibling()
-
-    def previous_sibling(self):
-        """The previous sibling statement.
-
-        :returns: The previous sibling statement node.
-        :rtype: NodeNG or None
-        """
-        return self.parent.previous_sibling()
-
-    # these are lazy because they're relatively expensive to compute for every
-    # single node, and they rarely get looked at
-
-    @decorators.cachedproperty
-    def fromlineno(self):
-        """The first line that this node appears on in the source code.
-
-        :type: int or None
-        """
-        if self.lineno is None:
-            return self._fixed_source_line()
-
-        return self.lineno
-
-    @decorators.cachedproperty
-    def tolineno(self):
-        """The last line that this node appears on in the source code.
-
-        :type: int or None
-        """
-        if not self._astroid_fields:
-            # can't have children
-            lastchild = None
-        else:
-            lastchild = self.last_child()
-        if lastchild is None:
-            return self.fromlineno
-
-        return lastchild.tolineno
-
-    def _fixed_source_line(self):
-        """Attempt to find the line that this node appears on.
-
-        We need this method since not all nodes have :attr:`lineno` set.
-
-        :returns: The line number of this node,
-            or None if this could not be determined.
-        :rtype: int or None
-        """
-        line = self.lineno
-        _node = self
-        try:
-            while line is None:
-                _node = next(_node.get_children())
-                line = _node.lineno
-        except StopIteration:
-            _node = self.parent
-            while _node and line is None:
-                line = _node.lineno
-                _node = _node.parent
-        return line
-
-    def block_range(self, lineno):
-        """Get a range from the given line number to where this node ends.
-
-        :param lineno: The line number to start the range at.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to,
-            starting at the given line number.
-        :rtype: tuple(int, int or None)
-        """
-        return lineno, self.tolineno
-
-    def set_local(self, name, stmt):
-        """Define that the given name is declared in the given statement node.
-
-        This definition is stored on the parent scope node.
-
-        .. seealso:: :meth:`scope`
-
-        :param name: The name that is being defined.
-        :type name: str
-
-        :param stmt: The statement that defines the given name.
-        :type stmt: NodeNG
-        """
-        self.parent.set_local(name, stmt)
-
-    def nodes_of_class(self, klass, skip_klass=None):
-        """Get the nodes (including this one or below) of the given types.
-
-        :param klass: The types of node to search for.
-        :type klass: builtins.type or tuple(builtins.type)
-
-        :param skip_klass: The types of node to ignore. This is useful to ignore
-            subclasses of :attr:`klass`.
-        :type skip_klass: builtins.type or tuple(builtins.type)
-
-        :returns: The node of the given types.
-        :rtype: iterable(NodeNG)
-        """
-        if isinstance(self, klass):
-            yield self
-
-        if skip_klass is None:
-            for child_node in self.get_children():
-                yield from child_node.nodes_of_class(klass, skip_klass)
-
-            return
-
-        for child_node in self.get_children():
-            if isinstance(child_node, skip_klass):
-                continue
-            yield from child_node.nodes_of_class(klass, skip_klass)
-
-    @decorators.cached
-    def _get_assign_nodes(self):
-        return []
-
-    def _get_name_nodes(self):
-        for child_node in self.get_children():
-            yield from child_node._get_name_nodes()
-
-    def _get_return_nodes_skip_functions(self):
-        yield from ()
-
-    def _get_yield_nodes_skip_lambdas(self):
-        yield from ()
-
-    def _infer_name(self, frame, name):
-        # overridden for ImportFrom, Import, Global, TryExcept and Arguments
-        pass
-
-    def _infer(self, context=None):
-        """we don't know how to resolve a statement by default"""
-        # this method is overridden by most concrete classes
-        raise exceptions.InferenceError(
-            "No inference function for {node!r}.", node=self, context=context
-        )
-
-    def inferred(self):
-        """Get a list of the inferred values.
-
-        .. seealso:: :ref:`inference`
-
-        :returns: The inferred values.
-        :rtype: list
-        """
-        return list(self.infer())
-
-    def instantiate_class(self):
-        """Instantiate an instance of the defined class.
-
-        .. note::
-
-            On anything other than a :class:`ClassDef` this will return self.
-
-        :returns: An instance of the defined class.
-        :rtype: object
-        """
-        return self
-
-    def has_base(self, node):
-        """Check if this node inherits from the given type.
-
-        :param node: The node defining the base to look for.
-            Usually this is a :class:`Name` node.
-        :type node: NodeNG
-        """
-        return False
-
-    def callable(self):
-        """Whether this node defines something that is callable.
-
-        :returns: True if this defines something that is callable,
-            False otherwise.
-        :rtype: bool
-        """
-        return False
-
-    def eq(self, value):
-        return False
-
-    def as_string(self):
-        """Get the source code that this node represents.
-
-        :returns: The source code.
-        :rtype: str
-        """
-        return as_string.to_code(self)
-
-    def repr_tree(
-        self,
-        ids=False,
-        include_linenos=False,
-        ast_state=False,
-        indent="   ",
-        max_depth=0,
-        max_width=80,
-    ):
-        """Get a string representation of the AST from this node.
-
-        :param ids: If true, includes the ids with the node type names.
-        :type ids: bool
-
-        :param include_linenos: If true, includes the line numbers and
-            column offsets.
-        :type include_linenos: bool
-
-        :param ast_state: If true, includes information derived from
-            the whole AST like local and global variables.
-        :type ast_state: bool
-
-        :param indent: A string to use to indent the output string.
-        :type indent: str
-
-        :param max_depth: If set to a positive integer, won't return
-            nodes deeper than max_depth in the string.
-        :type max_depth: int
-
-        :param max_width: Attempt to format the output string to stay
-            within this number of characters, but can exceed it under some
-            circumstances. Only positive integer values are valid, the default is 80.
-        :type max_width: int
-
-        :returns: The string representation of the AST.
-        :rtype: str
-        """
-        # pylint: disable=too-many-statements
-        @_singledispatch
-        def _repr_tree(node, result, done, cur_indent="", depth=1):
-            """Outputs a representation of a non-tuple/list, non-node that's
-            contained within an AST, including strings.
-            """
-            lines = pprint.pformat(
-                node, width=max(max_width - len(cur_indent), 1)
-            ).splitlines(True)
-            result.append(lines[0])
-            result.extend([cur_indent + line for line in lines[1:]])
-            return len(lines) != 1
-
-        # pylint: disable=unused-variable; doesn't understand singledispatch
-        @_repr_tree.register(tuple)
-        @_repr_tree.register(list)
-        def _repr_seq(node, result, done, cur_indent="", depth=1):
-            """Outputs a representation of a sequence that's contained within an AST."""
-            cur_indent += indent
-            result.append("[")
-            if not node:
-                broken = False
-            elif len(node) == 1:
-                broken = _repr_tree(node[0], result, done, cur_indent, depth)
-            elif len(node) == 2:
-                broken = _repr_tree(node[0], result, done, cur_indent, depth)
-                if not broken:
-                    result.append(", ")
-                else:
-                    result.append(",\n")
-                    result.append(cur_indent)
-                broken = _repr_tree(node[1], result, done, cur_indent, depth) or broken
-            else:
-                result.append("\n")
-                result.append(cur_indent)
-                for child in node[:-1]:
-                    _repr_tree(child, result, done, cur_indent, depth)
-                    result.append(",\n")
-                    result.append(cur_indent)
-                _repr_tree(node[-1], result, done, cur_indent, depth)
-                broken = True
-            result.append("]")
-            return broken
-
-        # pylint: disable=unused-variable; doesn't understand singledispatch
-        @_repr_tree.register(NodeNG)
-        def _repr_node(node, result, done, cur_indent="", depth=1):
-            """Outputs a strings representation of an astroid node."""
-            if node in done:
-                result.append(
-                    indent
-                    + "<Recursion on %s with id=%s" % (type(node).__name__, id(node))
-                )
-                return False
-            done.add(node)
-
-            if max_depth and depth > max_depth:
-                result.append("...")
-                return False
-            depth += 1
-            cur_indent += indent
-            if ids:
-                result.append("%s<0x%x>(\n" % (type(node).__name__, id(node)))
-            else:
-                result.append("%s(" % type(node).__name__)
-            fields = []
-            if include_linenos:
-                fields.extend(("lineno", "col_offset"))
-            fields.extend(node._other_fields)
-            fields.extend(node._astroid_fields)
-            if ast_state:
-                fields.extend(node._other_other_fields)
-            if not fields:
-                broken = False
-            elif len(fields) == 1:
-                result.append("%s=" % fields[0])
-                broken = _repr_tree(
-                    getattr(node, fields[0]), result, done, cur_indent, depth
-                )
-            else:
-                result.append("\n")
-                result.append(cur_indent)
-                for field in fields[:-1]:
-                    result.append("%s=" % field)
-                    _repr_tree(getattr(node, field), result, done, cur_indent, depth)
-                    result.append(",\n")
-                    result.append(cur_indent)
-                result.append("%s=" % fields[-1])
-                _repr_tree(getattr(node, fields[-1]), result, done, cur_indent, depth)
-                broken = True
-            result.append(")")
-            return broken
-
-        result = []
-        _repr_tree(self, result, set())
-        return "".join(result)
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        The boolean value of a node can have three
-        possible values:
-
-            * False: For instance, empty data structures,
-              False, empty strings, instances which return
-              explicitly False from the __nonzero__ / __bool__
-              method.
-            * True: Most of constructs are True by default:
-              classes, functions, modules etc
-            * Uninferable: The inference engine is uncertain of the
-              node's value.
-
-        :returns: The boolean value of this node.
-        :rtype: bool or Uninferable
-        """
-        return util.Uninferable
-
-    def op_precedence(self):
-        # Look up by class name or default to highest precedence
-        return OP_PRECEDENCE.get(self.__class__.__name__, len(OP_PRECEDENCE))
-
-    def op_left_associative(self):
-        # Everything is left associative except `**` and IfExp
-        return True
-
-
-class Statement(NodeNG):
-    """Statement node adding a few attributes"""
-
-    is_statement = True
-    """Whether this node indicates a statement.
-
-    :type: bool
-    """
-
-    def next_sibling(self):
-        """The next sibling statement node.
-
-        :returns: The next sibling statement node.
-        :rtype: NodeNG or None
-        """
-        stmts = self.parent.child_sequence(self)
-        index = stmts.index(self)
-        try:
-            return stmts[index + 1]
-        except IndexError:
-            pass
-
-    def previous_sibling(self):
-        """The previous sibling statement.
-
-        :returns: The previous sibling statement node.
-        :rtype: NodeNG or None
-        """
-        stmts = self.parent.child_sequence(self)
-        index = stmts.index(self)
-        if index >= 1:
-            return stmts[index - 1]
-        return None
-
-
-class _BaseContainer(
-    mixins.ParentAssignTypeMixin, NodeNG, bases.Instance, metaclass=abc.ABCMeta
-):
-    """Base class for Set, FrozenSet, Tuple and List."""
-
-    _astroid_fields = ("elts",)
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        """
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.elts = []
-        """The elements in the node.
-
-        :type: list(NodeNG)
-        """
-
-        super(_BaseContainer, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, elts):
-        """Do some setup after initialisation.
-
-        :param elts: The list of elements the that node contains.
-        :type elts: list(NodeNG)
-        """
-        self.elts = elts
-
-    @classmethod
-    def from_elements(cls, elts=None):
-        """Create a node of this type from the given list of elements.
-
-        :param elts: The list of elements that the node should contain.
-        :type elts: list(NodeNG)
-
-        :returns: A new node containing the given elements.
-        :rtype: NodeNG
-        """
-        node = cls()
-        if elts is None:
-            node.elts = []
-        else:
-            node.elts = [const_factory(e) if _is_const(e) else e for e in elts]
-        return node
-
-    def itered(self):
-        """An iterator over the elements this node contains.
-
-        :returns: The contents of this node.
-        :rtype: iterable(NodeNG)
-        """
-        return self.elts
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-        :rtype: bool or Uninferable
-        """
-        return bool(self.elts)
-
-    @abc.abstractmethod
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-
-    def get_children(self):
-        yield from self.elts
-
-
-class LookupMixIn:
-    """Mixin to look up a name in the right scope."""
-
-    @lru_cache(maxsize=None)
-    def lookup(self, name):
-        """Lookup where the given variable is assigned.
-
-        The lookup starts from self's scope. If self is not a frame itself
-        and the name is found in the inner frame locals, statements will be
-        filtered to remove ignorable statements according to self's location.
-
-        :param name: The name of the variable to find assignments for.
-        :type name: str
-
-        :returns: The scope node and the list of assignments associated to the
-            given name according to the scope where it has been found (locals,
-            globals or builtin).
-        :rtype: tuple(str, list(NodeNG))
-        """
-        return self.scope().scope_lookup(self, name)
-
-    def ilookup(self, name):
-        """Lookup the inferred values of the given variable.
-
-        :param name: The variable name to find values for.
-        :type name: str
-
-        :returns: The inferred values of the statements returned from
-            :meth:`lookup`.
-        :rtype: iterable
-        """
-        frame, stmts = self.lookup(name)
-        context = contextmod.InferenceContext()
-        return bases._infer_stmts(stmts, context, frame)
-
-    def _get_filtered_node_statements(self, nodes):
-        statements = [(node, node.statement()) for node in nodes]
-        # Next we check if we have ExceptHandlers that are parent
-        # of the underlying variable, in which case the last one survives
-        if len(statements) > 1 and all(
-            isinstance(stmt, ExceptHandler) for _, stmt in statements
-        ):
-            statements = [
-                (node, stmt) for node, stmt in statements if stmt.parent_of(self)
-            ]
-        return statements
-
-    def _filter_stmts(self, stmts, frame, offset):
-        """Filter the given list of statements to remove ignorable statements.
-
-        If self is not a frame itself and the name is found in the inner
-        frame locals, statements will be filtered to remove ignorable
-        statements according to self's location.
-
-        :param stmts: The statements to filter.
-        :type stmts: list(NodeNG)
-
-        :param frame: The frame that all of the given statements belong to.
-        :type frame: NodeNG
-
-        :param offset: The line offset to filter statements up to.
-        :type offset: int
-
-        :returns: The filtered statements.
-        :rtype: list(NodeNG)
-        """
-        # if offset == -1, my actual frame is not the inner frame but its parent
-        #
-        # class A(B): pass
-        #
-        # we need this to resolve B correctly
-        if offset == -1:
-            myframe = self.frame().parent.frame()
-        else:
-            myframe = self.frame()
-            # If the frame of this node is the same as the statement
-            # of this node, then the node is part of a class or
-            # a function definition and the frame of this node should be the
-            # the upper frame, not the frame of the definition.
-            # For more information why this is important,
-            # see Pylint issue #295.
-            # For example, for 'b', the statement is the same
-            # as the frame / scope:
-            #
-            # def test(b=1):
-            #     ...
-
-            if self.statement() is myframe and myframe.parent:
-                myframe = myframe.parent.frame()
-        mystmt = self.statement()
-        # line filtering if we are in the same frame
-        #
-        # take care node may be missing lineno information (this is the case for
-        # nodes inserted for living objects)
-        if myframe is frame and mystmt.fromlineno is not None:
-            assert mystmt.fromlineno is not None, mystmt
-            mylineno = mystmt.fromlineno + offset
-        else:
-            # disabling lineno filtering
-            mylineno = 0
-
-        _stmts = []
-        _stmt_parents = []
-        statements = self._get_filtered_node_statements(stmts)
-
-        for node, stmt in statements:
-            # line filtering is on and we have reached our location, break
-            if stmt.fromlineno > mylineno > 0:
-                break
-            # Ignore decorators with the same name as the
-            # decorated function
-            # Fixes issue #375
-            if mystmt is stmt and is_from_decorator(self):
-                continue
-            assert hasattr(node, "assign_type"), (
-                node,
-                node.scope(),
-                node.scope().locals,
-            )
-            assign_type = node.assign_type()
-            if node.has_base(self):
-                break
-
-            _stmts, done = assign_type._get_filtered_stmts(self, node, _stmts, mystmt)
-            if done:
-                break
-
-            optional_assign = assign_type.optional_assign
-            if optional_assign and assign_type.parent_of(self):
-                # we are inside a loop, loop var assignment is hiding previous
-                # assignment
-                _stmts = [node]
-                _stmt_parents = [stmt.parent]
-                continue
-
-            if isinstance(assign_type, NamedExpr):
-                _stmts = [node]
-                continue
-
-            # XXX comment various branches below!!!
-            try:
-                pindex = _stmt_parents.index(stmt.parent)
-            except ValueError:
-                pass
-            else:
-                # we got a parent index, this means the currently visited node
-                # is at the same block level as a previously visited node
-                if _stmts[pindex].assign_type().parent_of(assign_type):
-                    # both statements are not at the same block level
-                    continue
-                # if currently visited node is following previously considered
-                # assignment and both are not exclusive, we can drop the
-                # previous one. For instance in the following code ::
-                #
-                #   if a:
-                #     x = 1
-                #   else:
-                #     x = 2
-                #   print x
-                #
-                # we can't remove neither x = 1 nor x = 2 when looking for 'x'
-                # of 'print x'; while in the following ::
-                #
-                #   x = 1
-                #   x = 2
-                #   print x
-                #
-                # we can remove x = 1 when we see x = 2
-                #
-                # moreover, on loop assignment types, assignment won't
-                # necessarily be done if the loop has no iteration, so we don't
-                # want to clear previous assignments if any (hence the test on
-                # optional_assign)
-                if not (optional_assign or are_exclusive(_stmts[pindex], node)):
-                    if (
-                        # In case of partial function node, if the statement is different
-                        # from the origin function then it can be deleted otherwise it should
-                        # remain to be able to correctly infer the call to origin function.
-                        not node.is_function
-                        or node.qname() != "PartialFunction"
-                        or node.name != _stmts[pindex].name
-                    ):
-                        del _stmt_parents[pindex]
-                        del _stmts[pindex]
-            if isinstance(node, AssignName):
-                if not optional_assign and stmt.parent is mystmt.parent:
-                    _stmts = []
-                    _stmt_parents = []
-            elif isinstance(node, DelName):
-                _stmts = []
-                _stmt_parents = []
-                continue
-            if not are_exclusive(self, node):
-                _stmts.append(node)
-                _stmt_parents.append(stmt.parent)
-        return _stmts
-
-
-# Name classes
-
-
-class AssignName(
-    mixins.NoChildrenMixin, LookupMixIn, mixins.ParentAssignTypeMixin, NodeNG
-):
-    """Variation of :class:`ast.Assign` representing assignment to a name.
-
-    An :class:`AssignName` is the name of something that is assigned to.
-    This includes variables defined in a function signature or in a loop.
-
-    >>> node = astroid.extract_node('variable = range(10)')
-    >>> node
-    <Assign l.1 at 0x7effe1db8550>
-    >>> list(node.get_children())
-    [<AssignName.variable l.1 at 0x7effe1db8748>, <Call l.1 at 0x7effe1db8630>]
-    >>> list(node.get_children())[0].as_string()
-    'variable'
-    """
-
-    _other_fields = ("name",)
-
-    def __init__(self, name=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param name: The name that is assigned to.
-        :type name: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.name = name
-        """The name that is assigned to.
-
-        :type: str or None
-        """
-
-        super(AssignName, self).__init__(lineno, col_offset, parent)
-
-
-class DelName(
-    mixins.NoChildrenMixin, LookupMixIn, mixins.ParentAssignTypeMixin, NodeNG
-):
-    """Variation of :class:`ast.Delete` representing deletion of a name.
-
-    A :class:`DelName` is the name of something that is deleted.
-
-    >>> node = astroid.extract_node("del variable #@")
-    >>> list(node.get_children())
-    [<DelName.variable l.1 at 0x7effe1da4d30>]
-    >>> list(node.get_children())[0].as_string()
-    'variable'
-    """
-
-    _other_fields = ("name",)
-
-    def __init__(self, name=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param name: The name that is being deleted.
-        :type name: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.name = name
-        """The name that is being deleted.
-
-        :type: str or None
-        """
-
-        super(DelName, self).__init__(lineno, col_offset, parent)
-
-
-class Name(mixins.NoChildrenMixin, LookupMixIn, NodeNG):
-    """Class representing an :class:`ast.Name` node.
-
-    A :class:`Name` node is something that is named, but not covered by
-    :class:`AssignName` or :class:`DelName`.
-
-    >>> node = astroid.extract_node('range(10)')
-    >>> node
-    <Call l.1 at 0x7effe1db8710>
-    >>> list(node.get_children())
-    [<Name.range l.1 at 0x7effe1db86a0>, <Const.int l.1 at 0x7effe1db8518>]
-    >>> list(node.get_children())[0].as_string()
-    'range'
-    """
-
-    _other_fields = ("name",)
-
-    def __init__(self, name=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param name: The name that this node refers to.
-        :type name: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.name = name
-        """The name that this node refers to.
-
-        :type: str or None
-        """
-
-        super(Name, self).__init__(lineno, col_offset, parent)
-
-    def _get_name_nodes(self):
-        yield self
-
-        for child_node in self.get_children():
-            yield from child_node._get_name_nodes()
-
-
-class Arguments(mixins.AssignTypeMixin, NodeNG):
-    """Class representing an :class:`ast.arguments` node.
-
-    An :class:`Arguments` node represents that arguments in a
-    function definition.
-
-    >>> node = astroid.extract_node('def foo(bar): pass')
-    >>> node
-    <FunctionDef.foo l.1 at 0x7effe1db8198>
-    >>> node.args
-    <Arguments l.1 at 0x7effe1db82e8>
-    """
-
-    # Python 3.4+ uses a different approach regarding annotations,
-    # each argument is a new class, _ast.arg, which exposes an
-    # 'annotation' attribute. In astroid though, arguments are exposed
-    # as is in the Arguments node and the only way to expose annotations
-    # is by using something similar with Python 3.3:
-    #  - we expose 'varargannotation' and 'kwargannotation' of annotations
-    #    of varargs and kwargs.
-    #  - we expose 'annotation', a list with annotations for
-    #    for each normal argument. If an argument doesn't have an
-    #    annotation, its value will be None.
-
-    _astroid_fields = (
-        "args",
-        "defaults",
-        "kwonlyargs",
-        "posonlyargs",
-        "kw_defaults",
-        "annotations",
-        "varargannotation",
-        "kwargannotation",
-        "kwonlyargs_annotations",
-        "type_comment_args",
-    )
-    varargannotation = None
-    """The type annotation for the variable length arguments.
-
-    :type: NodeNG
-    """
-    kwargannotation = None
-    """The type annotation for the variable length keyword arguments.
-
-    :type: NodeNG
-    """
-
-    _other_fields = ("vararg", "kwarg")
-
-    def __init__(self, vararg=None, kwarg=None, parent=None):
-        """
-        :param vararg: The name of the variable length arguments.
-        :type vararg: str or None
-
-        :param kwarg: The name of the variable length keyword arguments.
-        :type kwarg: str or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        super(Arguments, self).__init__(parent=parent)
-        self.vararg = vararg
-        """The name of the variable length arguments.
-
-        :type: str or None
-        """
-
-        self.kwarg = kwarg
-        """The name of the variable length keyword arguments.
-
-        :type: str or None
-        """
-
-        self.args = []
-        """The names of the required arguments.
-
-        :type: list(AssignName)
-        """
-
-        self.defaults = []
-        """The default values for arguments that can be passed positionally.
-
-        :type: list(NodeNG)
-        """
-
-        self.kwonlyargs = []
-        """The keyword arguments that cannot be passed positionally.
-
-        :type: list(AssignName)
-        """
-
-        self.posonlyargs = []
-        """The arguments that can only be passed positionally.
-
-        :type: list(AssignName)
-        """
-
-        self.kw_defaults = []
-        """The default values for keyword arguments that cannot be passed positionally.
-
-        :type: list(NodeNG)
-        """
-
-        self.annotations = []
-        """The type annotations of arguments that can be passed positionally.
-
-        :type: list(NodeNG)
-        """
-
-        self.posonlyargs_annotations = []
-        """The type annotations of arguments that can only be passed positionally.
-
-        :type: list(NodeNG)
-        """
-
-        self.kwonlyargs_annotations = []
-        """The type annotations of arguments that cannot be passed positionally.
-
-        :type: list(NodeNG)
-        """
-
-        self.type_comment_args = []
-        """The type annotation, passed by a type comment, of each argument.
-
-        If an argument does not have a type comment,
-        the value for that argument will be None.
-
-        :type: list(NodeNG or None)
-        """
-
-    # pylint: disable=too-many-arguments
-    def postinit(
-        self,
-        args,
-        defaults,
-        kwonlyargs,
-        kw_defaults,
-        annotations,
-        posonlyargs=None,
-        kwonlyargs_annotations=None,
-        posonlyargs_annotations=None,
-        varargannotation=None,
-        kwargannotation=None,
-        type_comment_args=None,
-    ):
-        """Do some setup after initialisation.
-
-        :param args: The names of the required arguments.
-        :type args: list(AssignName)
-
-        :param defaults: The default values for arguments that can be passed
-            positionally.
-        :type defaults: list(NodeNG)
-
-        :param kwonlyargs: The keyword arguments that cannot be passed
-            positionally.
-        :type kwonlyargs: list(AssignName)
-
-        :param posonlyargs: The arguments that can only be passed
-            positionally.
-        :type kwonlyargs: list(AssignName)
-
-        :param kw_defaults: The default values for keyword arguments that
-            cannot be passed positionally.
-        :type kw_defaults: list(NodeNG)
-
-        :param annotations: The type annotations of arguments that can be
-            passed positionally.
-        :type annotations: list(NodeNG)
-
-        :param kwonlyargs_annotations: The type annotations of arguments that
-            cannot be passed positionally. This should always be passed in
-            Python 3.
-        :type kwonlyargs_annotations: list(NodeNG)
-
-        :param posonlyargs_annotations: The type annotations of arguments that
-            can only be passed positionally. This should always be passed in
-            Python 3.
-        :type posonlyargs_annotations: list(NodeNG)
-
-        :param varargannotation: The type annotation for the variable length
-            arguments.
-        :type varargannotation: NodeNG
-
-        :param kwargannotation: The type annotation for the variable length
-            keyword arguments.
-        :type kwargannotation: NodeNG
-
-        :param type_comment_args: The type annotation,
-            passed by a type comment, of each argument.
-        :type type_comment_args: list(NodeNG or None)
-        """
-        self.args = args
-        self.defaults = defaults
-        self.kwonlyargs = kwonlyargs
-        self.posonlyargs = posonlyargs
-        self.kw_defaults = kw_defaults
-        self.annotations = annotations
-        self.kwonlyargs_annotations = kwonlyargs_annotations
-        self.posonlyargs_annotations = posonlyargs_annotations
-        self.varargannotation = varargannotation
-        self.kwargannotation = kwargannotation
-        self.type_comment_args = type_comment_args
-
-    # pylint: disable=too-many-arguments
-
-    def _infer_name(self, frame, name):
-        if self.parent is frame:
-            return name
-        return None
-
-    @decorators.cachedproperty
-    def fromlineno(self):
-        """The first line that this node appears on in the source code.
-
-        :type: int or None
-        """
-        lineno = super(Arguments, self).fromlineno
-        return max(lineno, self.parent.fromlineno or 0)
-
-    def format_args(self):
-        """Get the arguments formatted as string.
-
-        :returns: The formatted arguments.
-        :rtype: str
-        """
-        result = []
-        positional_only_defaults = []
-        positional_or_keyword_defaults = self.defaults
-        if self.defaults:
-            args = self.args or []
-            positional_or_keyword_defaults = self.defaults[-len(args) :]
-            positional_only_defaults = self.defaults[: len(self.defaults) - len(args)]
-
-        if self.posonlyargs:
-            result.append(_format_args(self.posonlyargs, positional_only_defaults))
-            result.append("/")
-        if self.args:
-            result.append(
-                _format_args(
-                    self.args,
-                    positional_or_keyword_defaults,
-                    getattr(self, "annotations", None),
-                )
-            )
-        if self.vararg:
-            result.append("*%s" % self.vararg)
-        if self.kwonlyargs:
-            if not self.vararg:
-                result.append("*")
-            result.append(
-                _format_args(
-                    self.kwonlyargs, self.kw_defaults, self.kwonlyargs_annotations
-                )
-            )
-        if self.kwarg:
-            result.append("**%s" % self.kwarg)
-        return ", ".join(result)
-
-    def default_value(self, argname):
-        """Get the default value for an argument.
-
-        :param argname: The name of the argument to get the default value for.
-        :type argname: str
-
-        :raises NoDefault: If there is no default value defined for the
-            given argument.
-        """
-        args = list(itertools.chain((self.posonlyargs or ()), self.args or ()))
-        index = _find_arg(argname, args)[0]
-        if index is not None:
-            idx = index - (len(args) - len(self.defaults))
-            if idx >= 0:
-                return self.defaults[idx]
-        index = _find_arg(argname, self.kwonlyargs)[0]
-        if index is not None and self.kw_defaults[index] is not None:
-            return self.kw_defaults[index]
-        raise exceptions.NoDefault(func=self.parent, name=argname)
-
-    def is_argument(self, name):
-        """Check if the given name is defined in the arguments.
-
-        :param name: The name to check for.
-        :type name: str
-
-        :returns: True if the given name is defined in the arguments,
-            False otherwise.
-        :rtype: bool
-        """
-        if name == self.vararg:
-            return True
-        if name == self.kwarg:
-            return True
-        return (
-            self.find_argname(name, rec=True)[1] is not None
-            or self.kwonlyargs
-            and _find_arg(name, self.kwonlyargs, rec=True)[1] is not None
-        )
-
-    def find_argname(self, argname, rec=False):
-        """Get the index and :class:`AssignName` node for given name.
-
-        :param argname: The name of the argument to search for.
-        :type argname: str
-
-        :param rec: Whether or not to include arguments in unpacked tuples
-            in the search.
-        :type rec: bool
-
-        :returns: The index and node for the argument.
-        :rtype: tuple(str or None, AssignName or None)
-        """
-        if (
-            self.args or self.posonlyargs
-        ):  # self.args may be None in some cases (builtin function)
-            arguments = itertools.chain(self.posonlyargs or (), self.args or ())
-            return _find_arg(argname, arguments, rec)
-        return None, None
-
-    def get_children(self):
-        yield from self.posonlyargs or ()
-        yield from self.args or ()
-
-        yield from self.defaults
-        yield from self.kwonlyargs
-
-        for elt in self.kw_defaults:
-            if elt is not None:
-                yield elt
-
-        for elt in self.annotations:
-            if elt is not None:
-                yield elt
-
-        if self.varargannotation is not None:
-            yield self.varargannotation
-
-        if self.kwargannotation is not None:
-            yield self.kwargannotation
-
-        for elt in self.kwonlyargs_annotations:
-            if elt is not None:
-                yield elt
-
-
-def _find_arg(argname, args, rec=False):
-    for i, arg in enumerate(args):
-        if isinstance(arg, Tuple):
-            if rec:
-                found = _find_arg(argname, arg.elts)
-                if found[0] is not None:
-                    return found
-        elif arg.name == argname:
-            return i, arg
-    return None, None
-
-
-def _format_args(args, defaults=None, annotations=None):
-    values = []
-    if args is None:
-        return ""
-    if annotations is None:
-        annotations = []
-    if defaults is not None:
-        default_offset = len(args) - len(defaults)
-    packed = itertools.zip_longest(args, annotations)
-    for i, (arg, annotation) in enumerate(packed):
-        if isinstance(arg, Tuple):
-            values.append("(%s)" % _format_args(arg.elts))
-        else:
-            argname = arg.name
-            default_sep = "="
-            if annotation is not None:
-                argname += ": " + annotation.as_string()
-                default_sep = " = "
-            values.append(argname)
-
-            if defaults is not None and i >= default_offset:
-                if defaults[i - default_offset] is not None:
-                    values[-1] += default_sep + defaults[i - default_offset].as_string()
-    return ", ".join(values)
-
-
-class AssignAttr(mixins.ParentAssignTypeMixin, NodeNG):
-    """Variation of :class:`ast.Assign` representing assignment to an attribute.
-
-    >>> node = astroid.extract_node('self.attribute = range(10)')
-    >>> node
-    <Assign l.1 at 0x7effe1d521d0>
-    >>> list(node.get_children())
-    [<AssignAttr.attribute l.1 at 0x7effe1d52320>, <Call l.1 at 0x7effe1d522e8>]
-    >>> list(node.get_children())[0].as_string()
-    'self.attribute'
-    """
-
-    _astroid_fields = ("expr",)
-    _other_fields = ("attrname",)
-    expr = None
-    """What has the attribute that is being assigned to.
-
-    :type: NodeNG or None
-    """
-
-    def __init__(self, attrname=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param attrname: The name of the attribute being assigned to.
-        :type attrname: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.attrname = attrname
-        """The name of the attribute being assigned to.
-
-        :type: str or None
-        """
-
-        super(AssignAttr, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, expr=None):
-        """Do some setup after initialisation.
-
-        :param expr: What has the attribute that is being assigned to.
-        :type expr: NodeNG or None
-        """
-        self.expr = expr
-
-    def get_children(self):
-        yield self.expr
-
-
-class Assert(Statement):
-    """Class representing an :class:`ast.Assert` node.
-
-    An :class:`Assert` node represents an assert statement.
-
-    >>> node = astroid.extract_node('assert len(things) == 10, "Not enough things"')
-    >>> node
-    <Assert l.1 at 0x7effe1d527b8>
-    """
-
-    _astroid_fields = ("test", "fail")
-    test = None
-    """The test that passes or fails the assertion.
-
-    :type: NodeNG or None
-    """
-    fail = None
-    """The message shown when the assertion fails.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, test=None, fail=None):
-        """Do some setup after initialisation.
-
-        :param test: The test that passes or fails the assertion.
-        :type test: NodeNG or None
-
-        :param fail: The message shown when the assertion fails.
-        :type fail: NodeNG or None
-        """
-        self.fail = fail
-        self.test = test
-
-    def get_children(self):
-        yield self.test
-
-        if self.fail is not None:
-            yield self.fail
-
-
-class Assign(mixins.AssignTypeMixin, Statement):
-    """Class representing an :class:`ast.Assign` node.
-
-    An :class:`Assign` is a statement where something is explicitly
-    asssigned to.
-
-    >>> node = astroid.extract_node('variable = range(10)')
-    >>> node
-    <Assign l.1 at 0x7effe1db8550>
-    """
-
-    _astroid_fields = ("targets", "value")
-    _other_other_fields = ("type_annotation",)
-    targets = None
-    """What is being assigned to.
-
-    :type: list(NodeNG) or None
-    """
-    value = None
-    """The value being assigned to the variables.
-
-    :type: NodeNG or None
-    """
-    type_annotation = None
-    """If present, this will contain the type annotation passed by a type comment
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, targets=None, value=None, type_annotation=None):
-        """Do some setup after initialisation.
-
-        :param targets: What is being assigned to.
-        :type targets: list(NodeNG) or None
-
-        :param value: The value being assigned to the variables.
-        :type: NodeNG or None
-        """
-        self.targets = targets
-        self.value = value
-        self.type_annotation = type_annotation
-
-    def get_children(self):
-        yield from self.targets
-
-        yield self.value
-
-    @decorators.cached
-    def _get_assign_nodes(self):
-        return [self] + list(self.value._get_assign_nodes())
-
-    def _get_yield_nodes_skip_lambdas(self):
-        yield from self.value._get_yield_nodes_skip_lambdas()
-
-
-class AnnAssign(mixins.AssignTypeMixin, Statement):
-    """Class representing an :class:`ast.AnnAssign` node.
-
-    An :class:`AnnAssign` is an assignment with a type annotation.
-
-    >>> node = astroid.extract_node('variable: List[int] = range(10)')
-    >>> node
-    <AnnAssign l.1 at 0x7effe1d4c630>
-    """
-
-    _astroid_fields = ("target", "annotation", "value")
-    _other_fields = ("simple",)
-    target = None
-    """What is being assigned to.
-
-    :type: NodeNG or None
-    """
-    annotation = None
-    """The type annotation of what is being assigned to.
-
-    :type: NodeNG
-    """
-    value = None
-    """The value being assigned to the variables.
-
-    :type: NodeNG or None
-    """
-    simple = None
-    """Whether :attr:`target` is a pure name or a complex statement.
-
-    :type: int
-    """
-
-    def postinit(self, target, annotation, simple, value=None):
-        """Do some setup after initialisation.
-
-        :param target: What is being assigned to.
-        :type target: NodeNG
-
-        :param annotation: The type annotation of what is being assigned to.
-        :type: NodeNG
-
-        :param simple: Whether :attr:`target` is a pure name
-            or a complex statement.
-        :type simple: int
-
-        :param value: The value being assigned to the variables.
-        :type: NodeNG or None
-        """
-        self.target = target
-        self.annotation = annotation
-        self.value = value
-        self.simple = simple
-
-    def get_children(self):
-        yield self.target
-        yield self.annotation
-
-        if self.value is not None:
-            yield self.value
-
-
-class AugAssign(mixins.AssignTypeMixin, Statement):
-    """Class representing an :class:`ast.AugAssign` node.
-
-    An :class:`AugAssign` is an assignment paired with an operator.
-
-    >>> node = astroid.extract_node('variable += 1')
-    >>> node
-    <AugAssign l.1 at 0x7effe1db4d68>
-    """
-
-    _astroid_fields = ("target", "value")
-    _other_fields = ("op",)
-    target = None
-    """What is being assigned to.
-
-    :type: NodeNG or None
-    """
-    value = None
-    """The value being assigned to the variable.
-
-    :type: NodeNG or None
-    """
-
-    def __init__(self, op=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param op: The operator that is being combined with the assignment.
-            This includes the equals sign.
-        :type op: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.op = op
-        """The operator that is being combined with the assignment.
-
-        This includes the equals sign.
-
-        :type: str or None
-        """
-
-        super(AugAssign, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, target=None, value=None):
-        """Do some setup after initialisation.
-
-        :param target: What is being assigned to.
-        :type target: NodeNG or None
-
-        :param value: The value being assigned to the variable.
-        :type: NodeNG or None
-        """
-        self.target = target
-        self.value = value
-
-    # This is set by inference.py
-    def _infer_augassign(self, context=None):
-        raise NotImplementedError
-
-    def type_errors(self, context=None):
-        """Get a list of type errors which can occur during inference.
-
-        Each TypeError is represented by a :class:`BadBinaryOperationMessage` ,
-        which holds the original exception.
-
-        :returns: The list of possible type errors.
-        :rtype: list(BadBinaryOperationMessage)
-        """
-        try:
-            results = self._infer_augassign(context=context)
-            return [
-                result
-                for result in results
-                if isinstance(result, util.BadBinaryOperationMessage)
-            ]
-        except exceptions.InferenceError:
-            return []
-
-    def get_children(self):
-        yield self.target
-        yield self.value
-
-
-class Repr(NodeNG):
-    """Class representing an :class:`ast.Repr` node.
-
-    A :class:`Repr` node represents the backtick syntax,
-    which is a deprecated alias for :func:`repr` removed in Python 3.
-
-    >>> node = astroid.extract_node('`variable`')
-    >>> node
-    <Repr l.1 at 0x7fa0951d75d0>
-    """
-
-    _astroid_fields = ("value",)
-    value = None
-    """What is having :func:`repr` called on it.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: What is having :func:`repr` called on it.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-
-class BinOp(NodeNG):
-    """Class representing an :class:`ast.BinOp` node.
-
-    A :class:`BinOp` node is an application of a binary operator.
-
-    >>> node = astroid.extract_node('a + b')
-    >>> node
-    <BinOp l.1 at 0x7f23b2e8cfd0>
-    """
-
-    _astroid_fields = ("left", "right")
-    _other_fields = ("op",)
-    left = None
-    """What is being applied to the operator on the left side.
-
-    :type: NodeNG or None
-    """
-    right = None
-    """What is being applied to the operator on the right side.
-
-    :type: NodeNG or None
-    """
-
-    def __init__(self, op=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param op: The operator.
-        :type: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.op = op
-        """The operator.
-
-        :type: str or None
-        """
-
-        super(BinOp, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, left=None, right=None):
-        """Do some setup after initialisation.
-
-        :param left: What is being applied to the operator on the left side.
-        :type left: NodeNG or None
-
-        :param right: What is being applied to the operator on the right side.
-        :type right: NodeNG or None
-        """
-        self.left = left
-        self.right = right
-
-    # This is set by inference.py
-    def _infer_binop(self, context=None):
-        raise NotImplementedError
-
-    def type_errors(self, context=None):
-        """Get a list of type errors which can occur during inference.
-
-        Each TypeError is represented by a :class:`BadBinaryOperationMessage`,
-        which holds the original exception.
-
-        :returns: The list of possible type errors.
-        :rtype: list(BadBinaryOperationMessage)
-        """
-        try:
-            results = self._infer_binop(context=context)
-            return [
-                result
-                for result in results
-                if isinstance(result, util.BadBinaryOperationMessage)
-            ]
-        except exceptions.InferenceError:
-            return []
-
-    def get_children(self):
-        yield self.left
-        yield self.right
-
-    def op_precedence(self):
-        return OP_PRECEDENCE[self.op]
-
-    def op_left_associative(self):
-        # 2**3**4 == 2**(3**4)
-        return self.op != "**"
-
-
-class BoolOp(NodeNG):
-    """Class representing an :class:`ast.BoolOp` node.
-
-    A :class:`BoolOp` is an application of a boolean operator.
-
-    >>> node = astroid.extract_node('a and b')
-    >>> node
-    <BinOp l.1 at 0x7f23b2e71c50>
-    """
-
-    _astroid_fields = ("values",)
-    _other_fields = ("op",)
-    values = None
-    """The values being applied to the operator.
-
-    :type: list(NodeNG) or None
-    """
-
-    def __init__(self, op=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param op: The operator.
-        :type: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.op = op
-        """The operator.
-
-        :type: str or None
-        """
-
-        super(BoolOp, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, values=None):
-        """Do some setup after initialisation.
-
-        :param values: The values being applied to the operator.
-        :type values: list(NodeNG) or None
-        """
-        self.values = values
-
-    def get_children(self):
-        yield from self.values
-
-    def op_precedence(self):
-        return OP_PRECEDENCE[self.op]
-
-
-class Break(mixins.NoChildrenMixin, Statement):
-    """Class representing an :class:`ast.Break` node.
-
-    >>> node = astroid.extract_node('break')
-    >>> node
-    <Break l.1 at 0x7f23b2e9e5c0>
-    """
-
-
-class Call(NodeNG):
-    """Class representing an :class:`ast.Call` node.
-
-    A :class:`Call` node is a call to a function, method, etc.
-
-    >>> node = astroid.extract_node('function()')
-    >>> node
-    <Call l.1 at 0x7f23b2e71eb8>
-    """
-
-    _astroid_fields = ("func", "args", "keywords")
-    func = None
-    """What is being called.
-
-    :type: NodeNG or None
-    """
-    args = None
-    """The positional arguments being given to the call.
-
-    :type: list(NodeNG) or None
-    """
-    keywords = None
-    """The keyword arguments being given to the call.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, func=None, args=None, keywords=None):
-        """Do some setup after initialisation.
-
-        :param func: What is being called.
-        :type func: NodeNG or None
-
-        :param args: The positional arguments being given to the call.
-        :type args: list(NodeNG) or None
-
-        :param keywords: The keyword arguments being given to the call.
-        :type keywords: list(NodeNG) or None
-        """
-        self.func = func
-        self.args = args
-        self.keywords = keywords
-
-    @property
-    def starargs(self):
-        """The positional arguments that unpack something.
-
-        :type: list(Starred)
-        """
-        args = self.args or []
-        return [arg for arg in args if isinstance(arg, Starred)]
-
-    @property
-    def kwargs(self):
-        """The keyword arguments that unpack something.
-
-        :type: list(Keyword)
-        """
-        keywords = self.keywords or []
-        return [keyword for keyword in keywords if keyword.arg is None]
-
-    def get_children(self):
-        yield self.func
-
-        yield from self.args
-
-        yield from self.keywords or ()
-
-
-class Compare(NodeNG):
-    """Class representing an :class:`ast.Compare` node.
-
-    A :class:`Compare` node indicates a comparison.
-
-    >>> node = astroid.extract_node('a <= b <= c')
-    >>> node
-    <Compare l.1 at 0x7f23b2e9e6d8>
-    >>> node.ops
-    [('<=', <Name.b l.1 at 0x7f23b2e9e2b0>), ('<=', <Name.c l.1 at 0x7f23b2e9e390>)]
-    """
-
-    _astroid_fields = ("left", "ops")
-    left = None
-    """The value at the left being applied to a comparison operator.
-
-    :type: NodeNG or None
-    """
-    ops = None
-    """The remainder of the operators and their relevant right hand value.
-
-    :type: list(tuple(str, NodeNG)) or None
-    """
-
-    def postinit(self, left=None, ops=None):
-        """Do some setup after initialisation.
-
-        :param left: The value at the left being applied to a comparison
-            operator.
-        :type left: NodeNG or None
-
-        :param ops: The remainder of the operators
-            and their relevant right hand value.
-        :type ops: list(tuple(str, NodeNG)) or None
-        """
-        self.left = left
-        self.ops = ops
-
-    def get_children(self):
-        """Get the child nodes below this node.
-
-        Overridden to handle the tuple fields and skip returning the operator
-        strings.
-
-        :returns: The children.
-        :rtype: iterable(NodeNG)
-        """
-        yield self.left
-        for _, comparator in self.ops:
-            yield comparator  # we don't want the 'op'
-
-    def last_child(self):
-        """An optimized version of list(get_children())[-1]
-
-        :returns: The last child.
-        :rtype: NodeNG
-        """
-        # XXX maybe if self.ops:
-        return self.ops[-1][1]
-        # return self.left
-
-
-class Comprehension(NodeNG):
-    """Class representing an :class:`ast.comprehension` node.
-
-    A :class:`Comprehension` indicates the loop inside any type of
-    comprehension including generator expressions.
-
-    >>> node = astroid.extract_node('[x for x in some_values]')
-    >>> list(node.get_children())
-    [<Name.x l.1 at 0x7f23b2e352b0>, <Comprehension l.1 at 0x7f23b2e35320>]
-    >>> list(node.get_children())[1].as_string()
-    'for x in some_values'
-    """
-
-    _astroid_fields = ("target", "iter", "ifs")
-    _other_fields = ("is_async",)
-    target = None
-    """What is assigned to by the comprehension.
-
-    :type: NodeNG or None
-    """
-    iter = None
-    """What is iterated over by the comprehension.
-
-    :type: NodeNG or None
-    """
-    ifs = None
-    """The contents of any if statements that filter the comprehension.
-
-    :type: list(NodeNG) or None
-    """
-    is_async = None
-    """Whether this is an asynchronous comprehension or not.
-
-    :type: bool or None
-    """
-
-    def __init__(self, parent=None):
-        """
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        super(Comprehension, self).__init__()
-        self.parent = parent
-
-    # pylint: disable=redefined-builtin; same name as builtin ast module.
-    def postinit(self, target=None, iter=None, ifs=None, is_async=None):
-        """Do some setup after initialisation.
-
-        :param target: What is assigned to by the comprehension.
-        :type target: NodeNG or None
-
-        :param iter: What is iterated over by the comprehension.
-        :type iter: NodeNG or None
-
-        :param ifs: The contents of any if statements that filter
-            the comprehension.
-        :type ifs: list(NodeNG) or None
-
-        :param is_async: Whether this is an asynchronous comprehension or not.
-        :type: bool or None
-        """
-        self.target = target
-        self.iter = iter
-        self.ifs = ifs
-        self.is_async = is_async
-
-    optional_assign = True
-    """Whether this node optionally assigns a variable.
-
-    :type: bool
-    """
-
-    def assign_type(self):
-        """The type of assignment that this node performs.
-
-        :returns: The assignment type.
-        :rtype: NodeNG
-        """
-        return self
-
-    def _get_filtered_stmts(self, lookup_node, node, stmts, mystmt):
-        """method used in filter_stmts"""
-        if self is mystmt:
-            if isinstance(lookup_node, (Const, Name)):
-                return [lookup_node], True
-
-        elif self.statement() is mystmt:
-            # original node's statement is the assignment, only keeps
-            # current node (gen exp, list comp)
-
-            return [node], True
-
-        return stmts, False
-
-    def get_children(self):
-        yield self.target
-        yield self.iter
-
-        yield from self.ifs
-
-
-class Const(mixins.NoChildrenMixin, NodeNG, bases.Instance):
-    """Class representing any constant including num, str, bool, None, bytes.
-
-    >>> node = astroid.extract_node('(5, "This is a string.", True, None, b"bytes")')
-    >>> node
-    <Tuple.tuple l.1 at 0x7f23b2e358d0>
-    >>> list(node.get_children())
-    [<Const.int l.1 at 0x7f23b2e35940>,
-    <Const.str l.1 at 0x7f23b2e35978>,
-    <Const.bool l.1 at 0x7f23b2e359b0>,
-    <Const.NoneType l.1 at 0x7f23b2e359e8>,
-    <Const.bytes l.1 at 0x7f23b2e35a20>]
-    """
-
-    _other_fields = ("value",)
-
-    def __init__(self, value, lineno=None, col_offset=None, parent=None):
-        """
-        :param value: The value that the constant represents.
-        :type value: object
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.value = value
-        """The value that the constant represents.
-
-        :type: object
-        """
-
-        super(Const, self).__init__(lineno, col_offset, parent)
-
-    def __getattr__(self, name):
-        # This is needed because of Proxy's __getattr__ method.
-        # Calling object.__new__ on this class without calling
-        # __init__ would result in an infinite loop otherwise
-        # since __getattr__ is called when an attribute doesn't
-        # exist and self._proxied indirectly calls self.value
-        # and Proxy __getattr__ calls self.value
-        if name == "value":
-            raise AttributeError
-        return super().__getattr__(name)
-
-    def getitem(self, index, context=None):
-        """Get an item from this node if subscriptable.
-
-        :param index: The node to use as a subscript index.
-        :type index: Const or Slice
-
-        :raises AstroidTypeError: When the given index cannot be used as a
-            subscript index, or if this node is not subscriptable.
-        """
-        if isinstance(index, Const):
-            index_value = index.value
-        elif isinstance(index, Slice):
-            index_value = _infer_slice(index, context=context)
-
-        else:
-            raise exceptions.AstroidTypeError(
-                "Could not use type {} as subscript index".format(type(index))
-            )
-
-        try:
-            if isinstance(self.value, (str, bytes)):
-                return Const(self.value[index_value])
-        except IndexError as exc:
-            raise exceptions.AstroidIndexError(
-                message="Index {index!r} out of range",
-                node=self,
-                index=index,
-                context=context,
-            ) from exc
-        except TypeError as exc:
-            raise exceptions.AstroidTypeError(
-                message="Type error {error!r}", node=self, index=index, context=context
-            ) from exc
-
-        raise exceptions.AstroidTypeError("%r (value=%s)" % (self, self.value))
-
-    def has_dynamic_getattr(self):
-        """Check if the node has a custom __getattr__ or __getattribute__.
-
-        :returns: True if the class has a custom
-            __getattr__ or __getattribute__, False otherwise.
-            For a :class:`Const` this is always ``False``.
-        :rtype: bool
-        """
-        return False
-
-    def itered(self):
-        """An iterator over the elements this node contains.
-
-        :returns: The contents of this node.
-        :rtype: iterable(str)
-
-        :raises TypeError: If this node does not represent something that is iterable.
-        """
-        if isinstance(self.value, str):
-            return self.value
-        raise TypeError()
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        return self._proxied.qname()
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-        :rtype: bool
-        """
-        return bool(self.value)
-
-
-class Continue(mixins.NoChildrenMixin, Statement):
-    """Class representing an :class:`ast.Continue` node.
-
-    >>> node = astroid.extract_node('continue')
-    >>> node
-    <Continue l.1 at 0x7f23b2e35588>
-    """
-
-
-class Decorators(NodeNG):
-    """A node representing a list of decorators.
-
-    A :class:`Decorators` is the decorators that are applied to
-    a method or function.
-
-    >>> node = astroid.extract_node('''
-    @property
-    def my_property(self):
-        return 3
-    ''')
-    >>> node
-    <FunctionDef.my_property l.2 at 0x7f23b2e35d30>
-    >>> list(node.get_children())[0]
-    <Decorators l.1 at 0x7f23b2e35d68>
-    """
-
-    _astroid_fields = ("nodes",)
-    nodes = None
-    """The decorators that this node contains.
-
-    :type: list(Name or Call) or None
-    """
-
-    def postinit(self, nodes):
-        """Do some setup after initialisation.
-
-        :param nodes: The decorators that this node contains.
-        :type nodes: list(Name or Call)
-        """
-        self.nodes = nodes
-
-    def scope(self):
-        """The first parent node defining a new scope.
-
-        :returns: The first parent scope node.
-        :rtype: Module or FunctionDef or ClassDef or Lambda or GenExpr
-        """
-        # skip the function node to go directly to the upper level scope
-        return self.parent.parent.scope()
-
-    def get_children(self):
-        yield from self.nodes
-
-
-class DelAttr(mixins.ParentAssignTypeMixin, NodeNG):
-    """Variation of :class:`ast.Delete` representing deletion of an attribute.
-
-    >>> node = astroid.extract_node('del self.attr')
-    >>> node
-    <Delete l.1 at 0x7f23b2e35f60>
-    >>> list(node.get_children())[0]
-    <DelAttr.attr l.1 at 0x7f23b2e411d0>
-    """
-
-    _astroid_fields = ("expr",)
-    _other_fields = ("attrname",)
-    expr = None
-    """The name that this node represents.
-
-    :type: Name or None
-    """
-
-    def __init__(self, attrname=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param attrname: The name of the attribute that is being deleted.
-        :type attrname: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.attrname = attrname
-        """The name of the attribute that is being deleted.
-
-        :type: str or None
-        """
-
-        super(DelAttr, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, expr=None):
-        """Do some setup after initialisation.
-
-        :param expr: The name that this node represents.
-        :type expr: Name or None
-        """
-        self.expr = expr
-
-    def get_children(self):
-        yield self.expr
-
-
-class Delete(mixins.AssignTypeMixin, Statement):
-    """Class representing an :class:`ast.Delete` node.
-
-    A :class:`Delete` is a ``del`` statement this is deleting something.
-
-    >>> node = astroid.extract_node('del self.attr')
-    >>> node
-    <Delete l.1 at 0x7f23b2e35f60>
-    """
-
-    _astroid_fields = ("targets",)
-    targets = None
-    """What is being deleted.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, targets=None):
-        """Do some setup after initialisation.
-
-        :param targets: What is being deleted.
-        :type targets: list(NodeNG) or None
-        """
-        self.targets = targets
-
-    def get_children(self):
-        yield from self.targets
-
-
-class Dict(NodeNG, bases.Instance):
-    """Class representing an :class:`ast.Dict` node.
-
-    A :class:`Dict` is a dictionary that is created with ``{}`` syntax.
-
-    >>> node = astroid.extract_node('{1: "1"}')
-    >>> node
-    <Dict.dict l.1 at 0x7f23b2e35cc0>
-    """
-
-    _astroid_fields = ("items",)
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        """
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.items = []
-        """The key-value pairs contained in the dictionary.
-
-        :type: list(tuple(NodeNG, NodeNG))
-        """
-
-        super(Dict, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, items):
-        """Do some setup after initialisation.
-
-        :param items: The key-value pairs contained in the dictionary.
-        :type items: list(tuple(NodeNG, NodeNG))
-        """
-        self.items = items
-
-    @classmethod
-    def from_elements(cls, items=None):
-        """Create a :class:`Dict` of constants from a live dictionary.
-
-        :param items: The items to store in the node.
-        :type items: dict
-
-        :returns: The created dictionary node.
-        :rtype: Dict
-        """
-        node = cls()
-        if items is None:
-            node.items = []
-        else:
-            node.items = [
-                (const_factory(k), const_factory(v) if _is_const(v) else v)
-                for k, v in items.items()
-                # The keys need to be constants
-                if _is_const(k)
-            ]
-        return node
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        return "%s.dict" % BUILTINS
-
-    def get_children(self):
-        """Get the key and value nodes below this node.
-
-        Children are returned in the order that they are defined in the source
-        code, key first then the value.
-
-        :returns: The children.
-        :rtype: iterable(NodeNG)
-        """
-        for key, value in self.items:
-            yield key
-            yield value
-
-    def last_child(self):
-        """An optimized version of list(get_children())[-1]
-
-        :returns: The last child, or None if no children exist.
-        :rtype: NodeNG or None
-        """
-        if self.items:
-            return self.items[-1][1]
-        return None
-
-    def itered(self):
-        """An iterator over the keys this node contains.
-
-        :returns: The keys of this node.
-        :rtype: iterable(NodeNG)
-        """
-        return [key for (key, _) in self.items]
-
-    def getitem(self, index, context=None):
-        """Get an item from this node.
-
-        :param index: The node to use as a subscript index.
-        :type index: Const or Slice
-
-        :raises AstroidTypeError: When the given index cannot be used as a
-            subscript index, or if this node is not subscriptable.
-        :raises AstroidIndexError: If the given index does not exist in the
-            dictionary.
-        """
-        for key, value in self.items:
-            # TODO(cpopa): no support for overriding yet, {1:2, **{1: 3}}.
-            if isinstance(key, DictUnpack):
-                try:
-                    return value.getitem(index, context)
-                except (exceptions.AstroidTypeError, exceptions.AstroidIndexError):
-                    continue
-            for inferredkey in key.infer(context):
-                if inferredkey is util.Uninferable:
-                    continue
-                if isinstance(inferredkey, Const) and isinstance(index, Const):
-                    if inferredkey.value == index.value:
-                        return value
-
-        raise exceptions.AstroidIndexError(index)
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-        :rtype: bool
-        """
-        return bool(self.items)
-
-
-class Expr(Statement):
-    """Class representing an :class:`ast.Expr` node.
-
-    An :class:`Expr` is any expression that does not have its value used or
-    stored.
-
-    >>> node = astroid.extract_node('method()')
-    >>> node
-    <Call l.1 at 0x7f23b2e352b0>
-    >>> node.parent
-    <Expr l.1 at 0x7f23b2e35278>
-    """
-
-    _astroid_fields = ("value",)
-    value = None
-    """What the expression does.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: What the expression does.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-    def get_children(self):
-        yield self.value
-
-    def _get_yield_nodes_skip_lambdas(self):
-        if not self.value.is_lambda:
-            yield from self.value._get_yield_nodes_skip_lambdas()
-
-
-class Ellipsis(mixins.NoChildrenMixin, NodeNG):  # pylint: disable=redefined-builtin
-    """Class representing an :class:`ast.Ellipsis` node.
-
-    An :class:`Ellipsis` is the ``...`` syntax.
-
-    >>> node = astroid.extract_node('...')
-    >>> node
-    <Ellipsis l.1 at 0x7f23b2e35160>
-    """
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For an :class:`Ellipsis` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-
-class EmptyNode(mixins.NoChildrenMixin, NodeNG):
-    """Holds an arbitrary object in the :attr:`LocalsDictNodeNG.locals`."""
-
-    object = None
-
-
-class ExceptHandler(mixins.MultiLineBlockMixin, mixins.AssignTypeMixin, Statement):
-    """Class representing an :class:`ast.ExceptHandler`. node.
-
-    An :class:`ExceptHandler` is an ``except`` block on a try-except.
-
-    >>> node = astroid.extract_node('''
-        try:
-            do_something()
-        except Exception as error:
-            print("Error!")
-        ''')
-    >>> node
-    <TryExcept l.2 at 0x7f23b2e9d908>
-    >>> >>> node.handlers
-    [<ExceptHandler l.4 at 0x7f23b2e9e860>]
-    """
-
-    _astroid_fields = ("type", "name", "body")
-    _multi_line_block_fields = ("body",)
-    type = None
-    """The types that the block handles.
-
-    :type: Tuple or NodeNG or None
-    """
-    name = None
-    """The name that the caught exception is assigned to.
-
-    :type: AssignName or None
-    """
-    body = None
-    """The contents of the block.
-
-    :type: list(NodeNG) or None
-    """
-
-    def get_children(self):
-        if self.type is not None:
-            yield self.type
-
-        if self.name is not None:
-            yield self.name
-
-        yield from self.body
-
-    # pylint: disable=redefined-builtin; had to use the same name as builtin ast module.
-    def postinit(self, type=None, name=None, body=None):
-        """Do some setup after initialisation.
-
-        :param type: The types that the block handles.
-        :type type: Tuple or NodeNG or None
-
-        :param name: The name that the caught exception is assigned to.
-        :type name: AssignName or None
-
-        :param body:The contents of the block.
-        :type body: list(NodeNG) or None
-        """
-        self.type = type
-        self.name = name
-        self.body = body
-
-    @decorators.cachedproperty
-    def blockstart_tolineno(self):
-        """The line on which the beginning of this block ends.
-
-        :type: int
-        """
-        if self.name:
-            return self.name.tolineno
-        if self.type:
-            return self.type.tolineno
-        return self.lineno
-
-    def catch(self, exceptions):  # pylint: disable=redefined-outer-name
-        """Check if this node handles any of the given exceptions.
-
-        If ``exceptions`` is empty, this will default to ``True``.
-
-        :param exceptions: The name of the exceptions to check for.
-        :type exceptions: list(str)
-        """
-        if self.type is None or exceptions is None:
-            return True
-        for node in self.type._get_name_nodes():
-            if node.name in exceptions:
-                return True
-        return False
-
-
-class Exec(Statement):
-    """Class representing the ``exec`` statement.
-
-    >>> node = astroid.extract_node('exec "True"')
-    >>> node
-    <Exec l.1 at 0x7f0e8106c6d0>
-    """
-
-    _astroid_fields = ("expr", "globals", "locals")
-    expr = None
-    """The expression to be executed.
-
-    :type: NodeNG or None
-    """
-    globals = None
-    """The globals dictionary to execute with.
-
-    :type: NodeNG or None
-    """
-    locals = None
-    """The locals dictionary to execute with.
-
-    :type: NodeNG or None
-    """
-
-    # pylint: disable=redefined-builtin; had to use the same name as builtin ast module.
-    def postinit(self, expr=None, globals=None, locals=None):
-        """Do some setup after initialisation.
-
-        :param expr: The expression to be executed.
-        :type expr: NodeNG or None
-
-        :param globals:The globals dictionary to execute with.
-        :type globals: NodeNG or None
-
-        :param locals: The locals dictionary to execute with.
-        :type locals: NodeNG or None
-        """
-        self.expr = expr
-        self.globals = globals
-        self.locals = locals
-
-
-class ExtSlice(NodeNG):
-    """Class representing an :class:`ast.ExtSlice` node.
-
-    An :class:`ExtSlice` is a complex slice expression.
-
-    >>> node = astroid.extract_node('l[1:3, 5]')
-    >>> node
-    <Subscript l.1 at 0x7f23b2e9e550>
-    >>> node.slice
-    <ExtSlice l.1 at 0x7f23b7b05ef0>
-    """
-
-    _astroid_fields = ("dims",)
-    dims = None
-    """The simple dimensions that form the complete slice.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, dims=None):
-        """Do some setup after initialisation.
-
-        :param dims: The simple dimensions that form the complete slice.
-        :type dims: list(NodeNG) or None
-        """
-        self.dims = dims
-
-
-class For(
-    mixins.MultiLineBlockMixin,
-    mixins.BlockRangeMixIn,
-    mixins.AssignTypeMixin,
-    Statement,
-):
-    """Class representing an :class:`ast.For` node.
-
-    >>> node = astroid.extract_node('for thing in things: print(thing)')
-    >>> node
-    <For l.1 at 0x7f23b2e8cf28>
-    """
-
-    _astroid_fields = ("target", "iter", "body", "orelse")
-    _other_other_fields = ("type_annotation",)
-    _multi_line_block_fields = ("body", "orelse")
-    target = None
-    """What the loop assigns to.
-
-    :type: NodeNG or None
-    """
-    iter = None
-    """What the loop iterates over.
-
-    :type: NodeNG or None
-    """
-    body = None
-    """The contents of the body of the loop.
-
-    :type: list(NodeNG) or None
-    """
-    orelse = None
-    """The contents of the ``else`` block of the loop.
-
-    :type: list(NodeNG) or None
-    """
-    type_annotation = None
-    """If present, this will contain the type annotation passed by a type comment
-
-    :type: NodeNG or None
-    """
-
-    # pylint: disable=redefined-builtin; had to use the same name as builtin ast module.
-    def postinit(
-        self, target=None, iter=None, body=None, orelse=None, type_annotation=None
-    ):
-        """Do some setup after initialisation.
-
-        :param target: What the loop assigns to.
-        :type target: NodeNG or None
-
-        :param iter: What the loop iterates over.
-        :type iter: NodeNG or None
-
-        :param body: The contents of the body of the loop.
-        :type body: list(NodeNG) or None
-
-        :param orelse: The contents of the ``else`` block of the loop.
-        :type orelse: list(NodeNG) or None
-        """
-        self.target = target
-        self.iter = iter
-        self.body = body
-        self.orelse = orelse
-        self.type_annotation = type_annotation
-
-    optional_assign = True
-    """Whether this node optionally assigns a variable.
-
-    This is always ``True`` for :class:`For` nodes.
-
-    :type: bool
-    """
-
-    @decorators.cachedproperty
-    def blockstart_tolineno(self):
-        """The line on which the beginning of this block ends.
-
-        :type: int
-        """
-        return self.iter.tolineno
-
-    def get_children(self):
-        yield self.target
-        yield self.iter
-
-        yield from self.body
-        yield from self.orelse
-
-
-class AsyncFor(For):
-    """Class representing an :class:`ast.AsyncFor` node.
-
-    An :class:`AsyncFor` is an asynchronous :class:`For` built with
-    the ``async`` keyword.
-
-    >>> node = astroid.extract_node('''
-    async def func(things):
-        async for thing in things:
-            print(thing)
-    ''')
-    >>> node
-    <AsyncFunctionDef.func l.2 at 0x7f23b2e416d8>
-    >>> node.body[0]
-    <AsyncFor l.3 at 0x7f23b2e417b8>
-    """
-
-
-class Await(NodeNG):
-    """Class representing an :class:`ast.Await` node.
-
-    An :class:`Await` is the ``await`` keyword.
-
-    >>> node = astroid.extract_node('''
-    async def func(things):
-        await other_func()
-    ''')
-    >>> node
-    <AsyncFunctionDef.func l.2 at 0x7f23b2e41748>
-    >>> node.body[0]
-    <Expr l.3 at 0x7f23b2e419e8>
-    >>> list(node.body[0].get_children())[0]
-    <Await l.3 at 0x7f23b2e41a20>
-    """
-
-    _astroid_fields = ("value",)
-    value = None
-    """What to wait for.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: What to wait for.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-    def get_children(self):
-        yield self.value
-
-
-class ImportFrom(mixins.NoChildrenMixin, mixins.ImportFromMixin, Statement):
-    """Class representing an :class:`ast.ImportFrom` node.
-
-    >>> node = astroid.extract_node('from my_package import my_module')
-    >>> node
-    <ImportFrom l.1 at 0x7f23b2e415c0>
-    """
-
-    _other_fields = ("modname", "names", "level")
-
-    def __init__(
-        self, fromname, names, level=0, lineno=None, col_offset=None, parent=None
-    ):
-        """
-        :param fromname: The module that is being imported from.
-        :type fromname: str or None
-
-        :param names: What is being imported from the module.
-        :type names: list(tuple(str, str or None))
-
-        :param level: The level of relative import.
-        :type level: int
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.modname = fromname
-        """The module that is being imported from.
-
-        This is ``None`` for relative imports.
-
-        :type: str or None
-        """
-
-        self.names = names
-        """What is being imported from the module.
-
-        Each entry is a :class:`tuple` of the name being imported,
-        and the alias that the name is assigned to (if any).
-
-        :type: list(tuple(str, str or None))
-        """
-
-        self.level = level
-        """The level of relative import.
-
-        Essentially this is the number of dots in the import.
-        This is always 0 for absolute imports.
-
-        :type: int
-        """
-
-        super(ImportFrom, self).__init__(lineno, col_offset, parent)
-
-
-class Attribute(NodeNG):
-    """Class representing an :class:`ast.Attribute` node."""
-
-    _astroid_fields = ("expr",)
-    _other_fields = ("attrname",)
-    expr = None
-    """The name that this node represents.
-
-    :type: Name or None
-    """
-
-    def __init__(self, attrname=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param attrname: The name of the attribute.
-        :type attrname: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.attrname = attrname
-        """The name of the attribute.
-
-        :type: str or None
-        """
-
-        super(Attribute, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, expr=None):
-        """Do some setup after initialisation.
-
-        :param expr: The name that this node represents.
-        :type expr: Name or None
-        """
-        self.expr = expr
-
-    def get_children(self):
-        yield self.expr
-
-
-class Global(mixins.NoChildrenMixin, Statement):
-    """Class representing an :class:`ast.Global` node.
-
-    >>> node = astroid.extract_node('global a_global')
-    >>> node
-    <Global l.1 at 0x7f23b2e9de10>
-    """
-
-    _other_fields = ("names",)
-
-    def __init__(self, names, lineno=None, col_offset=None, parent=None):
-        """
-        :param names: The names being declared as global.
-        :type names: list(str)
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.names = names
-        """The names being declared as global.
-
-        :type: list(str)
-        """
-
-        super(Global, self).__init__(lineno, col_offset, parent)
-
-    def _infer_name(self, frame, name):
-        return name
-
-
-class If(mixins.MultiLineBlockMixin, mixins.BlockRangeMixIn, Statement):
-    """Class representing an :class:`ast.If` node.
-
-    >>> node = astroid.extract_node('if condition: print(True)')
-    >>> node
-    <If l.1 at 0x7f23b2e9dd30>
-    """
-
-    _astroid_fields = ("test", "body", "orelse")
-    _multi_line_block_fields = ("body", "orelse")
-    test = None
-    """The condition that the statement tests.
-
-    :type: NodeNG or None
-    """
-    body = None
-    """The contents of the block.
-
-    :type: list(NodeNG) or None
-    """
-    orelse = None
-    """The contents of the ``else`` block.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, test=None, body=None, orelse=None):
-        """Do some setup after initialisation.
-
-        :param test: The condition that the statement tests.
-        :type test: NodeNG or None
-
-        :param body: The contents of the block.
-        :type body: list(NodeNG) or None
-
-        :param orelse: The contents of the ``else`` block.
-        :type orelse: list(NodeNG) or None
-        """
-        self.test = test
-        self.body = body
-        self.orelse = orelse
-
-    @decorators.cachedproperty
-    def blockstart_tolineno(self):
-        """The line on which the beginning of this block ends.
-
-        :type: int
-        """
-        return self.test.tolineno
-
-    def block_range(self, lineno):
-        """Get a range from the given line number to where this node ends.
-
-        :param lineno: The line number to start the range at.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to,
-            starting at the given line number.
-        :rtype: tuple(int, int)
-        """
-        if lineno == self.body[0].fromlineno:
-            return lineno, lineno
-        if lineno <= self.body[-1].tolineno:
-            return lineno, self.body[-1].tolineno
-        return self._elsed_block_range(lineno, self.orelse, self.body[0].fromlineno - 1)
-
-    def get_children(self):
-        yield self.test
-
-        yield from self.body
-        yield from self.orelse
-
-    def has_elif_block(self):
-        return len(self.orelse) == 1 and isinstance(self.orelse[0], If)
-
-
-class IfExp(NodeNG):
-    """Class representing an :class:`ast.IfExp` node.
-
-    >>> node = astroid.extract_node('value if condition else other')
-    >>> node
-    <IfExp l.1 at 0x7f23b2e9dbe0>
-    """
-
-    _astroid_fields = ("test", "body", "orelse")
-    test = None
-    """The condition that the statement tests.
-
-    :type: NodeNG or None
-    """
-    body = None
-    """The contents of the block.
-
-    :type: list(NodeNG) or None
-    """
-    orelse = None
-    """The contents of the ``else`` block.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, test=None, body=None, orelse=None):
-        """Do some setup after initialisation.
-
-        :param test: The condition that the statement tests.
-        :type test: NodeNG or None
-
-        :param body: The contents of the block.
-        :type body: list(NodeNG) or None
-
-        :param orelse: The contents of the ``else`` block.
-        :type orelse: list(NodeNG) or None
-        """
-        self.test = test
-        self.body = body
-        self.orelse = orelse
-
-    def get_children(self):
-        yield self.test
-        yield self.body
-        yield self.orelse
-
-    def op_left_associative(self):
-        # `1 if True else 2 if False else 3` is parsed as
-        # `1 if True else (2 if False else 3)`
-        return False
-
-
-class Import(mixins.NoChildrenMixin, mixins.ImportFromMixin, Statement):
-    """Class representing an :class:`ast.Import` node.
-
-    >>> node = astroid.extract_node('import astroid')
-    >>> node
-    <Import l.1 at 0x7f23b2e4e5c0>
-    """
-
-    _other_fields = ("names",)
-
-    def __init__(self, names=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param names: The names being imported.
-        :type names: list(tuple(str, str or None)) or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.names = names
-        """The names being imported.
-
-        Each entry is a :class:`tuple` of the name being imported,
-        and the alias that the name is assigned to (if any).
-
-        :type: list(tuple(str, str or None)) or None
-        """
-
-        super(Import, self).__init__(lineno, col_offset, parent)
-
-
-class Index(NodeNG):
-    """Class representing an :class:`ast.Index` node.
-
-    An :class:`Index` is a simple subscript.
-
-    >>> node = astroid.extract_node('things[1]')
-    >>> node
-    <Subscript l.1 at 0x7f23b2e9e2b0>
-    >>> node.slice
-    <Index l.1 at 0x7f23b2e9e6a0>
-    """
-
-    _astroid_fields = ("value",)
-    value = None
-    """The value to subscript with.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: The value to subscript with.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-    def get_children(self):
-        yield self.value
-
-
-class Keyword(NodeNG):
-    """Class representing an :class:`ast.keyword` node.
-
-    >>> node = astroid.extract_node('function(a_kwarg=True)')
-    >>> node
-    <Call l.1 at 0x7f23b2e9e320>
-    >>> node.keywords
-    [<Keyword l.1 at 0x7f23b2e9e9b0>]
-    """
-
-    _astroid_fields = ("value",)
-    _other_fields = ("arg",)
-    value = None
-    """The value being assigned to the keyword argument.
-
-    :type: NodeNG or None
-    """
-
-    def __init__(self, arg=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param arg: The argument being assigned to.
-        :type arg: Name or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.arg = arg
-        """The argument being assigned to.
-
-        :type: Name or None
-        """
-
-        super(Keyword, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: The value being assigned to the ketword argument.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-    def get_children(self):
-        yield self.value
-
-
-class List(_BaseContainer):
-    """Class representing an :class:`ast.List` node.
-
-    >>> node = astroid.extract_node('[1, 2, 3]')
-    >>> node
-    <List.list l.1 at 0x7f23b2e9e128>
-    """
-
-    _other_fields = ("ctx",)
-
-    def __init__(self, ctx=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param ctx: Whether the list is assigned to or loaded from.
-        :type ctx: Context or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.ctx = ctx
-        """Whether the list is assigned to or loaded from.
-
-        :type: Context or None
-        """
-
-        super(List, self).__init__(lineno, col_offset, parent)
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        return "%s.list" % BUILTINS
-
-    def getitem(self, index, context=None):
-        """Get an item from this node.
-
-        :param index: The node to use as a subscript index.
-        :type index: Const or Slice
-        """
-        return _container_getitem(self, self.elts, index, context=context)
-
-
-class Nonlocal(mixins.NoChildrenMixin, Statement):
-    """Class representing an :class:`ast.Nonlocal` node.
-
-    >>> node = astroid.extract_node('''
-    def function():
-        nonlocal var
-    ''')
-    >>> node
-    <FunctionDef.function l.2 at 0x7f23b2e9e208>
-    >>> node.body[0]
-    <Nonlocal l.3 at 0x7f23b2e9e908>
-    """
-
-    _other_fields = ("names",)
-
-    def __init__(self, names, lineno=None, col_offset=None, parent=None):
-        """
-        :param names: The names being declared as not local.
-        :type names: list(str)
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.names = names
-        """The names being declared as not local.
-
-        :type: list(str)
-        """
-
-        super(Nonlocal, self).__init__(lineno, col_offset, parent)
-
-    def _infer_name(self, frame, name):
-        return name
-
-
-class Pass(mixins.NoChildrenMixin, Statement):
-    """Class representing an :class:`ast.Pass` node.
-
-    >>> node = astroid.extract_node('pass')
-    >>> node
-    <Pass l.1 at 0x7f23b2e9e748>
-    """
-
-
-class Print(Statement):
-    """Class representing an :class:`ast.Print` node.
-
-    >>> node = astroid.extract_node('print "A message"')
-    >>> node
-    <Print l.1 at 0x7f0e8101d290>
-    """
-
-    _astroid_fields = ("dest", "values")
-    dest = None
-    """Where to print to.
-
-    :type: NodeNG or None
-    """
-    values = None
-    """What to print.
-
-    :type: list(NodeNG) or None
-    """
-
-    def __init__(self, nl=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param nl: Whether to print a new line.
-        :type nl: bool or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.nl = nl
-        """Whether to print a new line.
-
-        :type: bool or None
-        """
-
-        super(Print, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, dest=None, values=None):
-        """Do some setup after initialisation.
-
-        :param dest: Where to print to.
-        :type dest: NodeNG or None
-
-        :param values: What to print.
-        :type values: list(NodeNG) or None
-        """
-        self.dest = dest
-        self.values = values
-
-
-class Raise(Statement):
-    """Class representing an :class:`ast.Raise` node.
-
-    >>> node = astroid.extract_node('raise RuntimeError("Something bad happened!")')
-    >>> node
-    <Raise l.1 at 0x7f23b2e9e828>
-    """
-
-    exc = None
-    """What is being raised.
-
-    :type: NodeNG or None
-    """
-    _astroid_fields = ("exc", "cause")
-    cause = None
-    """The exception being used to raise this one.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, exc=None, cause=None):
-        """Do some setup after initialisation.
-
-        :param exc: What is being raised.
-        :type exc: NodeNG or None
-
-        :param cause: The exception being used to raise this one.
-        :type cause: NodeNG or None
-        """
-        self.exc = exc
-        self.cause = cause
-
-    def raises_not_implemented(self):
-        """Check if this node raises a :class:`NotImplementedError`.
-
-        :returns: True if this node raises a :class:`NotImplementedError`,
-            False otherwise.
-        :rtype: bool
-        """
-        if not self.exc:
-            return False
-        for name in self.exc._get_name_nodes():
-            if name.name == "NotImplementedError":
-                return True
-        return False
-
-    def get_children(self):
-        if self.exc is not None:
-            yield self.exc
-
-        if self.cause is not None:
-            yield self.cause
-
-
-class Return(Statement):
-    """Class representing an :class:`ast.Return` node.
-
-    >>> node = astroid.extract_node('return True')
-    >>> node
-    <Return l.1 at 0x7f23b8211908>
-    """
-
-    _astroid_fields = ("value",)
-    value = None
-    """The value being returned.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: The value being returned.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-    def get_children(self):
-        if self.value is not None:
-            yield self.value
-
-    def is_tuple_return(self):
-        return isinstance(self.value, Tuple)
-
-    def _get_return_nodes_skip_functions(self):
-        yield self
-
-
-class Set(_BaseContainer):
-    """Class representing an :class:`ast.Set` node.
-
-    >>> node = astroid.extract_node('{1, 2, 3}')
-    >>> node
-    <Set.set l.1 at 0x7f23b2e71d68>
-    """
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        return "%s.set" % BUILTINS
-
-
-class Slice(NodeNG):
-    """Class representing an :class:`ast.Slice` node.
-
-    >>> node = astroid.extract_node('things[1:3]')
-    >>> node
-    <Subscript l.1 at 0x7f23b2e71f60>
-    >>> node.slice
-    <Slice l.1 at 0x7f23b2e71e80>
-    """
-
-    _astroid_fields = ("lower", "upper", "step")
-    lower = None
-    """The lower index in the slice.
-
-    :type: NodeNG or None
-    """
-    upper = None
-    """The upper index in the slice.
-
-    :type: NodeNG or None
-    """
-    step = None
-    """The step to take between indexes.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, lower=None, upper=None, step=None):
-        """Do some setup after initialisation.
-
-        :param lower: The lower index in the slice.
-        :value lower: NodeNG or None
-
-        :param upper: The upper index in the slice.
-        :value upper: NodeNG or None
-
-        :param step: The step to take between index.
-        :param step: NodeNG or None
-        """
-        self.lower = lower
-        self.upper = upper
-        self.step = step
-
-    def _wrap_attribute(self, attr):
-        """Wrap the empty attributes of the Slice in a Const node."""
-        if not attr:
-            const = const_factory(attr)
-            const.parent = self
-            return const
-        return attr
-
-    @decorators.cachedproperty
-    def _proxied(self):
-        builtins = MANAGER.builtins_module
-        return builtins.getattr("slice")[0]
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        return "%s.slice" % BUILTINS
-
-    def igetattr(self, attrname, context=None):
-        """Infer the possible values of the given attribute on the slice.
-
-        :param attrname: The name of the attribute to infer.
-        :type attrname: str
-
-        :returns: The inferred possible values.
-        :rtype: iterable(NodeNG)
-        """
-        if attrname == "start":
-            yield self._wrap_attribute(self.lower)
-        elif attrname == "stop":
-            yield self._wrap_attribute(self.upper)
-        elif attrname == "step":
-            yield self._wrap_attribute(self.step)
-        else:
-            yield from self.getattr(attrname, context=context)
-
-    def getattr(self, attrname, context=None):
-        return self._proxied.getattr(attrname, context)
-
-    def get_children(self):
-        if self.lower is not None:
-            yield self.lower
-
-        if self.upper is not None:
-            yield self.upper
-
-        if self.step is not None:
-            yield self.step
-
-
-class Starred(mixins.ParentAssignTypeMixin, NodeNG):
-    """Class representing an :class:`ast.Starred` node.
-
-    >>> node = astroid.extract_node('*args')
-    >>> node
-    <Starred l.1 at 0x7f23b2e41978>
-    """
-
-    _astroid_fields = ("value",)
-    _other_fields = ("ctx",)
-    value = None
-    """What is being unpacked.
-
-    :type: NodeNG or None
-    """
-
-    def __init__(self, ctx=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param ctx: Whether the list is assigned to or loaded from.
-        :type ctx: Context or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.ctx = ctx
-        """Whether the starred item is assigned to or loaded from.
-
-        :type: Context or None
-        """
-
-        super(Starred, self).__init__(
-            lineno=lineno, col_offset=col_offset, parent=parent
-        )
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: What is being unpacked.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-    def get_children(self):
-        yield self.value
-
-
-class Subscript(NodeNG):
-    """Class representing an :class:`ast.Subscript` node.
-
-    >>> node = astroid.extract_node('things[1:3]')
-    >>> node
-    <Subscript l.1 at 0x7f23b2e71f60>
-    """
-
-    _astroid_fields = ("value", "slice")
-    _other_fields = ("ctx",)
-    value = None
-    """What is being indexed.
-
-    :type: NodeNG or None
-    """
-    slice = None
-    """The slice being used to lookup.
-
-    :type: NodeNG or None
-    """
-
-    def __init__(self, ctx=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param ctx: Whether the subscripted item is assigned to or loaded from.
-        :type ctx: Context or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.ctx = ctx
-        """Whether the subscripted item is assigned to or loaded from.
-
-        :type: Context or None
-        """
-
-        super(Subscript, self).__init__(
-            lineno=lineno, col_offset=col_offset, parent=parent
-        )
-
-    # pylint: disable=redefined-builtin; had to use the same name as builtin ast module.
-    def postinit(self, value=None, slice=None):
-        """Do some setup after initialisation.
-
-        :param value: What is being indexed.
-        :type value: NodeNG or None
-
-        :param slice: The slice being used to lookup.
-        :type slice: NodeNG or None
-        """
-        self.value = value
-        self.slice = slice
-
-    def get_children(self):
-        yield self.value
-        yield self.slice
-
-
-class TryExcept(mixins.MultiLineBlockMixin, mixins.BlockRangeMixIn, Statement):
-    """Class representing an :class:`ast.TryExcept` node.
-
-    >>> node = astroid.extract_node('''
-        try:
-            do_something()
-        except Exception as error:
-            print("Error!")
-        ''')
-    >>> node
-    <TryExcept l.2 at 0x7f23b2e9d908>
-    """
-
-    _astroid_fields = ("body", "handlers", "orelse")
-    _multi_line_block_fields = ("body", "handlers", "orelse")
-    body = None
-    """The contents of the block to catch exceptions from.
-
-    :type: list(NodeNG) or None
-    """
-    handlers = None
-    """The exception handlers.
-
-    :type: list(ExceptHandler) or None
-    """
-    orelse = None
-    """The contents of the ``else`` block.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, body=None, handlers=None, orelse=None):
-        """Do some setup after initialisation.
-
-        :param body: The contents of the block to catch exceptions from.
-        :type body: list(NodeNG) or None
-
-        :param handlers: The exception handlers.
-        :type handlers: list(ExceptHandler) or None
-
-        :param orelse: The contents of the ``else`` block.
-        :type orelse: list(NodeNG) or None
-        """
-        self.body = body
-        self.handlers = handlers
-        self.orelse = orelse
-
-    def _infer_name(self, frame, name):
-        return name
-
-    def block_range(self, lineno):
-        """Get a range from the given line number to where this node ends.
-
-        :param lineno: The line number to start the range at.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to,
-            starting at the given line number.
-        :rtype: tuple(int, int)
-        """
-        last = None
-        for exhandler in self.handlers:
-            if exhandler.type and lineno == exhandler.type.fromlineno:
-                return lineno, lineno
-            if exhandler.body[0].fromlineno <= lineno <= exhandler.body[-1].tolineno:
-                return lineno, exhandler.body[-1].tolineno
-            if last is None:
-                last = exhandler.body[0].fromlineno - 1
-        return self._elsed_block_range(lineno, self.orelse, last)
-
-    def get_children(self):
-        yield from self.body
-
-        yield from self.handlers or ()
-        yield from self.orelse or ()
-
-
-class TryFinally(mixins.MultiLineBlockMixin, mixins.BlockRangeMixIn, Statement):
-    """Class representing an :class:`ast.TryFinally` node.
-
-    >>> node = astroid.extract_node('''
-    try:
-        do_something()
-    except Exception as error:
-        print("Error!")
-    finally:
-        print("Cleanup!")
-    ''')
-    >>> node
-    <TryFinally l.2 at 0x7f23b2e41d68>
-    """
-
-    _astroid_fields = ("body", "finalbody")
-    _multi_line_block_fields = ("body", "finalbody")
-    body = None
-    """The try-except that the finally is attached to.
-
-    :type: list(TryExcept) or None
-    """
-    finalbody = None
-    """The contents of the ``finally`` block.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, body=None, finalbody=None):
-        """Do some setup after initialisation.
-
-        :param body: The try-except that the finally is attached to.
-        :type body: list(TryExcept) or None
-
-        :param finalbody: The contents of the ``finally`` block.
-        :type finalbody: list(NodeNG) or None
-        """
-        self.body = body
-        self.finalbody = finalbody
-
-    def block_range(self, lineno):
-        """Get a range from the given line number to where this node ends.
-
-        :param lineno: The line number to start the range at.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to,
-            starting at the given line number.
-        :rtype: tuple(int, int)
-        """
-        child = self.body[0]
-        # py2.5 try: except: finally:
-        if (
-            isinstance(child, TryExcept)
-            and child.fromlineno == self.fromlineno
-            and child.tolineno >= lineno > self.fromlineno
-        ):
-            return child.block_range(lineno)
-        return self._elsed_block_range(lineno, self.finalbody)
-
-    def get_children(self):
-        yield from self.body
-        yield from self.finalbody
-
-
-class Tuple(_BaseContainer):
-    """Class representing an :class:`ast.Tuple` node.
-
-    >>> node = astroid.extract_node('(1, 2, 3)')
-    >>> node
-    <Tuple.tuple l.1 at 0x7f23b2e41780>
-    """
-
-    _other_fields = ("ctx",)
-
-    def __init__(self, ctx=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param ctx: Whether the tuple is assigned to or loaded from.
-        :type ctx: Context or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.ctx = ctx
-        """Whether the tuple is assigned to or loaded from.
-
-        :type: Context or None
-        """
-
-        super(Tuple, self).__init__(lineno, col_offset, parent)
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        return "%s.tuple" % BUILTINS
-
-    def getitem(self, index, context=None):
-        """Get an item from this node.
-
-        :param index: The node to use as a subscript index.
-        :type index: Const or Slice
-        """
-        return _container_getitem(self, self.elts, index, context=context)
-
-
-class UnaryOp(NodeNG):
-    """Class representing an :class:`ast.UnaryOp` node.
-
-    >>> node = astroid.extract_node('-5')
-    >>> node
-    <UnaryOp l.1 at 0x7f23b2e4e198>
-    """
-
-    _astroid_fields = ("operand",)
-    _other_fields = ("op",)
-    operand = None
-    """What the unary operator is applied to.
-
-    :type: NodeNG or None
-    """
-
-    def __init__(self, op=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param op: The operator.
-        :type: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.op = op
-        """The operator.
-
-        :type: str or None
-        """
-
-        super(UnaryOp, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, operand=None):
-        """Do some setup after initialisation.
-
-        :param operand: What the unary operator is applied to.
-        :type operand: NodeNG or None
-        """
-        self.operand = operand
-
-    # This is set by inference.py
-    def _infer_unaryop(self, context=None):
-        raise NotImplementedError
-
-    def type_errors(self, context=None):
-        """Get a list of type errors which can occur during inference.
-
-        Each TypeError is represented by a :class:`BadBinaryOperationMessage`,
-        which holds the original exception.
-
-        :returns: The list of possible type errors.
-        :rtype: list(BadBinaryOperationMessage)
-        """
-        try:
-            results = self._infer_unaryop(context=context)
-            return [
-                result
-                for result in results
-                if isinstance(result, util.BadUnaryOperationMessage)
-            ]
-        except exceptions.InferenceError:
-            return []
-
-    def get_children(self):
-        yield self.operand
-
-    def op_precedence(self):
-        if self.op == "not":
-            return OP_PRECEDENCE[self.op]
-
-        return super().op_precedence()
-
-
-class While(mixins.MultiLineBlockMixin, mixins.BlockRangeMixIn, Statement):
-    """Class representing an :class:`ast.While` node.
-
-    >>> node = astroid.extract_node('''
-    while condition():
-        print("True")
-    ''')
-    >>> node
-    <While l.2 at 0x7f23b2e4e390>
-    """
-
-    _astroid_fields = ("test", "body", "orelse")
-    _multi_line_block_fields = ("body", "orelse")
-    test = None
-    """The condition that the loop tests.
-
-    :type: NodeNG or None
-    """
-    body = None
-    """The contents of the loop.
-
-    :type: list(NodeNG) or None
-    """
-    orelse = None
-    """The contents of the ``else`` block.
-
-    :type: list(NodeNG) or None
-    """
-
-    def postinit(self, test=None, body=None, orelse=None):
-        """Do some setup after initialisation.
-
-        :param test: The condition that the loop tests.
-        :type test: NodeNG or None
-
-        :param body: The contents of the loop.
-        :type body: list(NodeNG) or None
-
-        :param orelse: The contents of the ``else`` block.
-        :type orelse: list(NodeNG) or None
-        """
-        self.test = test
-        self.body = body
-        self.orelse = orelse
-
-    @decorators.cachedproperty
-    def blockstart_tolineno(self):
-        """The line on which the beginning of this block ends.
-
-        :type: int
-        """
-        return self.test.tolineno
-
-    def block_range(self, lineno):
-        """Get a range from the given line number to where this node ends.
-
-        :param lineno: The line number to start the range at.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to,
-            starting at the given line number.
-        :rtype: tuple(int, int)
-        """
-        return self._elsed_block_range(lineno, self.orelse)
-
-    def get_children(self):
-        yield self.test
-
-        yield from self.body
-        yield from self.orelse
-
-
-class With(
-    mixins.MultiLineBlockMixin,
-    mixins.BlockRangeMixIn,
-    mixins.AssignTypeMixin,
-    Statement,
-):
-    """Class representing an :class:`ast.With` node.
-
-    >>> node = astroid.extract_node('''
-    with open(file_path) as file_:
-        print(file_.read())
-    ''')
-    >>> node
-    <With l.2 at 0x7f23b2e4e710>
-    """
-
-    _astroid_fields = ("items", "body")
-    _other_other_fields = ("type_annotation",)
-    _multi_line_block_fields = ("body",)
-    items = None
-    """The pairs of context managers and the names they are assigned to.
-
-    :type: list(tuple(NodeNG, AssignName or None)) or None
-    """
-    body = None
-    """The contents of the ``with`` block.
-
-    :type: list(NodeNG) or None
-    """
-    type_annotation = None
-    """If present, this will contain the type annotation passed by a type comment
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, items=None, body=None, type_annotation=None):
-        """Do some setup after initialisation.
-
-        :param items: The pairs of context managers and the names
-            they are assigned to.
-        :type items: list(tuple(NodeNG, AssignName or None)) or None
-
-        :param body: The contents of the ``with`` block.
-        :type body: list(NodeNG) or None
-        """
-        self.items = items
-        self.body = body
-        self.type_annotation = type_annotation
-
-    @decorators.cachedproperty
-    def blockstart_tolineno(self):
-        """The line on which the beginning of this block ends.
-
-        :type: int
-        """
-        return self.items[-1][0].tolineno
-
-    def get_children(self):
-        """Get the child nodes below this node.
-
-        :returns: The children.
-        :rtype: iterable(NodeNG)
-        """
-        for expr, var in self.items:
-            yield expr
-            if var:
-                yield var
-        yield from self.body
-
-
-class AsyncWith(With):
-    """Asynchronous ``with`` built with the ``async`` keyword."""
-
-
-class Yield(NodeNG):
-    """Class representing an :class:`ast.Yield` node.
-
-    >>> node = astroid.extract_node('yield True')
-    >>> node
-    <Yield l.1 at 0x7f23b2e4e5f8>
-    """
-
-    _astroid_fields = ("value",)
-    value = None
-    """The value to yield.
-
-    :type: NodeNG or None
-    """
-
-    def postinit(self, value=None):
-        """Do some setup after initialisation.
-
-        :param value: The value to yield.
-        :type value: NodeNG or None
-        """
-        self.value = value
-
-    def get_children(self):
-        if self.value is not None:
-            yield self.value
-
-    def _get_yield_nodes_skip_lambdas(self):
-        yield self
-
-
-class YieldFrom(Yield):
-    """Class representing an :class:`ast.YieldFrom` node."""
-
-
-class DictUnpack(mixins.NoChildrenMixin, NodeNG):
-    """Represents the unpacking of dicts into dicts using :pep:`448`."""
-
-
-class FormattedValue(NodeNG):
-    """Class representing an :class:`ast.FormattedValue` node.
-
-    Represents a :pep:`498` format string.
-
-    >>> node = astroid.extract_node('f"Format {type_}"')
-    >>> node
-    <JoinedStr l.1 at 0x7f23b2e4ed30>
-    >>> node.values
-    [<Const.str l.1 at 0x7f23b2e4eda0>, <FormattedValue l.1 at 0x7f23b2e4edd8>]
-    """
-
-    _astroid_fields = ("value", "format_spec")
-    value = None
-    """The value to be formatted into the string.
-
-    :type: NodeNG or None
-    """
-    conversion = None
-    """The type of formatting to be applied to the value.
-
-    .. seealso::
-        :class:`ast.FormattedValue`
-
-    :type: int or None
-    """
-    format_spec = None
-    """The formatting to be applied to the value.
-
-    .. seealso::
-        :class:`ast.FormattedValue`
-
-    :type: JoinedStr or None
-    """
-
-    def postinit(self, value, conversion=None, format_spec=None):
-        """Do some setup after initialisation.
-
-        :param value: The value to be formatted into the string.
-        :type value: NodeNG
-
-        :param conversion: The type of formatting to be applied to the value.
-        :type conversion: int or None
-
-        :param format_spec: The formatting to be applied to the value.
-        :type format_spec: JoinedStr or None
-        """
-        self.value = value
-        self.conversion = conversion
-        self.format_spec = format_spec
-
-    def get_children(self):
-        yield self.value
-
-        if self.format_spec is not None:
-            yield self.format_spec
-
-
-class JoinedStr(NodeNG):
-    """Represents a list of string expressions to be joined.
-
-    >>> node = astroid.extract_node('f"Format {type_}"')
-    >>> node
-    <JoinedStr l.1 at 0x7f23b2e4ed30>
-    """
-
-    _astroid_fields = ("values",)
-    values = None
-    """The string expressions to be joined.
-
-    :type: list(FormattedValue or Const) or None
-    """
-
-    def postinit(self, values=None):
-        """Do some setup after initialisation.
-
-        :param value: The string expressions to be joined.
-
-        :type: list(FormattedValue or Const) or None
-        """
-        self.values = values
-
-    def get_children(self):
-        yield from self.values
-
-
-class NamedExpr(mixins.AssignTypeMixin, NodeNG):
-    """Represents the assignment from the assignment expression
-
-    >>> module = astroid.parse('if a := 1: pass')
-    >>> module.body[0].test
-    <NamedExpr l.1 at 0x7f23b2e4ed30>
-    """
-
-    _astroid_fields = ("target", "value")
-    target = None
-    """The assignment target
-
-    :type: Name
-    """
-    value = None
-    """The value that gets assigned in the expression
-
-    :type: NodeNG
-    """
-
-    def postinit(self, target, value):
-        self.target = target
-        self.value = value
-
-
-class Unknown(mixins.AssignTypeMixin, NodeNG):
-    """This node represents a node in a constructed AST where
-    introspection is not possible.  At the moment, it's only used in
-    the args attribute of FunctionDef nodes where function signature
-    introspection failed.
-    """
-
-    name = "Unknown"
-
-    def qname(self):
-        return "Unknown"
-
-    def infer(self, context=None, **kwargs):
-        """Inference on an Unknown node immediately terminates."""
-        yield util.Uninferable
-
-
-# constants ##############################################################
-
-CONST_CLS = {
-    list: List,
-    tuple: Tuple,
-    dict: Dict,
-    set: Set,
-    type(None): Const,
-    type(NotImplemented): Const,
-}
-if PY38:
-    CONST_CLS[type(...)] = Const
-
-
-def _update_const_classes():
-    """update constant classes, so the keys of CONST_CLS can be reused"""
-    klasses = (bool, int, float, complex, str, bytes)
-    for kls in klasses:
-        CONST_CLS[kls] = Const
-
-
-_update_const_classes()
-
-
-def _two_step_initialization(cls, value):
-    instance = cls()
-    instance.postinit(value)
-    return instance
-
-
-def _dict_initialization(cls, value):
-    if isinstance(value, dict):
-        value = tuple(value.items())
-    return _two_step_initialization(cls, value)
-
-
-_CONST_CLS_CONSTRUCTORS = {
-    List: _two_step_initialization,
-    Tuple: _two_step_initialization,
-    Dict: _dict_initialization,
-    Set: _two_step_initialization,
-    Const: lambda cls, value: cls(value),
-}
-
-
-def const_factory(value):
-    """return an astroid node for a python value"""
-    # XXX we should probably be stricter here and only consider stuff in
-    # CONST_CLS or do better treatment: in case where value is not in CONST_CLS,
-    # we should rather recall the builder on this value than returning an empty
-    # node (another option being that const_factory shouldn't be called with something
-    # not in CONST_CLS)
-    assert not isinstance(value, NodeNG)
-
-    # Hack for ignoring elements of a sequence
-    # or a mapping, in order to avoid transforming
-    # each element to an AST. This is fixed in 2.0
-    # and this approach is a temporary hack.
-    if isinstance(value, (list, set, tuple, dict)):
-        elts = []
-    else:
-        elts = value
-
-    try:
-        initializer_cls = CONST_CLS[value.__class__]
-        initializer = _CONST_CLS_CONSTRUCTORS[initializer_cls]
-        return initializer(initializer_cls, elts)
-    except (KeyError, AttributeError):
-        node = EmptyNode()
-        node.object = value
-        return node
-
-
-def is_from_decorator(node):
-    """Return True if the given node is the child of a decorator"""
-    parent = node.parent
-    while parent is not None:
-        if isinstance(parent, Decorators):
-            return True
-        parent = parent.parent
-    return False
diff --git a/venv/Lib/site-packages/astroid/nodes.py b/venv/Lib/site-packages/astroid/nodes.py
deleted file mode 100644
index bf6911a..0000000
--- a/venv/Lib/site-packages/astroid/nodes.py
+++ /dev/null
@@ -1,175 +0,0 @@
-# Copyright (c) 2006-2011, 2013 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016 Jared Garst <jgarst@users.noreply.github.com>
-# Copyright (c) 2017 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017 rr- <rr-@sakuya.pl>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Every available node class.
-
-.. seealso::
-    :doc:`ast documentation <green_tree_snakes:nodes>`
-
-All nodes inherit from :class:`~astroid.node_classes.NodeNG`.
-"""
-# pylint: disable=unused-import,redefined-builtin
-
-from astroid.node_classes import (
-    Arguments,
-    AssignAttr,
-    Assert,
-    Assign,
-    AnnAssign,
-    AssignName,
-    AugAssign,
-    Repr,
-    BinOp,
-    BoolOp,
-    Break,
-    Call,
-    Compare,
-    Comprehension,
-    Const,
-    Continue,
-    Decorators,
-    DelAttr,
-    DelName,
-    Delete,
-    Dict,
-    Expr,
-    Ellipsis,
-    EmptyNode,
-    ExceptHandler,
-    Exec,
-    ExtSlice,
-    For,
-    ImportFrom,
-    Attribute,
-    Global,
-    If,
-    IfExp,
-    Import,
-    Index,
-    Keyword,
-    List,
-    Name,
-    NamedExpr,
-    Nonlocal,
-    Pass,
-    Print,
-    Raise,
-    Return,
-    Set,
-    Slice,
-    Starred,
-    Subscript,
-    TryExcept,
-    TryFinally,
-    Tuple,
-    UnaryOp,
-    While,
-    With,
-    Yield,
-    YieldFrom,
-    const_factory,
-    AsyncFor,
-    Await,
-    AsyncWith,
-    FormattedValue,
-    JoinedStr,
-    # Node not present in the builtin ast module.
-    DictUnpack,
-    Unknown,
-)
-from astroid.scoped_nodes import (
-    Module,
-    GeneratorExp,
-    Lambda,
-    DictComp,
-    ListComp,
-    SetComp,
-    FunctionDef,
-    ClassDef,
-    AsyncFunctionDef,
-)
-
-
-ALL_NODE_CLASSES = (
-    AsyncFunctionDef,
-    AsyncFor,
-    AsyncWith,
-    Await,
-    Arguments,
-    AssignAttr,
-    Assert,
-    Assign,
-    AnnAssign,
-    AssignName,
-    AugAssign,
-    Repr,
-    BinOp,
-    BoolOp,
-    Break,
-    Call,
-    ClassDef,
-    Compare,
-    Comprehension,
-    Const,
-    Continue,
-    Decorators,
-    DelAttr,
-    DelName,
-    Delete,
-    Dict,
-    DictComp,
-    DictUnpack,
-    Expr,
-    Ellipsis,
-    EmptyNode,
-    ExceptHandler,
-    Exec,
-    ExtSlice,
-    For,
-    ImportFrom,
-    FunctionDef,
-    Attribute,
-    GeneratorExp,
-    Global,
-    If,
-    IfExp,
-    Import,
-    Index,
-    Keyword,
-    Lambda,
-    List,
-    ListComp,
-    Name,
-    NamedExpr,
-    Nonlocal,
-    Module,
-    Pass,
-    Print,
-    Raise,
-    Return,
-    Set,
-    SetComp,
-    Slice,
-    Starred,
-    Subscript,
-    TryExcept,
-    TryFinally,
-    Tuple,
-    UnaryOp,
-    While,
-    With,
-    Yield,
-    YieldFrom,
-    FormattedValue,
-    JoinedStr,
-)
diff --git a/venv/Lib/site-packages/astroid/objects.py b/venv/Lib/site-packages/astroid/objects.py
deleted file mode 100644
index 888ca36..0000000
--- a/venv/Lib/site-packages/astroid/objects.py
+++ /dev/null
@@ -1,282 +0,0 @@
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""
-Inference objects are a way to represent composite AST nodes,
-which are used only as inference results, so they can't be found in the
-original AST tree. For instance, inferring the following frozenset use,
-leads to an inferred FrozenSet:
-
-    Call(func=Name('frozenset'), args=Tuple(...))
-"""
-
-import builtins
-
-from astroid import bases
-from astroid import decorators
-from astroid import exceptions
-from astroid import MANAGER
-from astroid import node_classes
-from astroid import scoped_nodes
-from astroid import util
-
-
-BUILTINS = builtins.__name__
-objectmodel = util.lazy_import("interpreter.objectmodel")
-
-
-class FrozenSet(node_classes._BaseContainer):
-    """class representing a FrozenSet composite node"""
-
-    def pytype(self):
-        return "%s.frozenset" % BUILTINS
-
-    def _infer(self, context=None):
-        yield self
-
-    @decorators.cachedproperty
-    def _proxied(self):  # pylint: disable=method-hidden
-        ast_builtins = MANAGER.builtins_module
-        return ast_builtins.getattr("frozenset")[0]
-
-
-class Super(node_classes.NodeNG):
-    """Proxy class over a super call.
-
-    This class offers almost the same behaviour as Python's super,
-    which is MRO lookups for retrieving attributes from the parents.
-
-    The *mro_pointer* is the place in the MRO from where we should
-    start looking, not counting it. *mro_type* is the object which
-    provides the MRO, it can be both a type or an instance.
-    *self_class* is the class where the super call is, while
-    *scope* is the function where the super call is.
-    """
-
-    # pylint: disable=unnecessary-lambda
-    special_attributes = util.lazy_descriptor(lambda: objectmodel.SuperModel())
-
-    # pylint: disable=super-init-not-called
-    def __init__(self, mro_pointer, mro_type, self_class, scope):
-        self.type = mro_type
-        self.mro_pointer = mro_pointer
-        self._class_based = False
-        self._self_class = self_class
-        self._scope = scope
-
-    def _infer(self, context=None):
-        yield self
-
-    def super_mro(self):
-        """Get the MRO which will be used to lookup attributes in this super."""
-        if not isinstance(self.mro_pointer, scoped_nodes.ClassDef):
-            raise exceptions.SuperError(
-                "The first argument to super must be a subtype of "
-                "type, not {mro_pointer}.",
-                super_=self,
-            )
-
-        if isinstance(self.type, scoped_nodes.ClassDef):
-            # `super(type, type)`, most likely in a class method.
-            self._class_based = True
-            mro_type = self.type
-        else:
-            mro_type = getattr(self.type, "_proxied", None)
-            if not isinstance(mro_type, (bases.Instance, scoped_nodes.ClassDef)):
-                raise exceptions.SuperError(
-                    "The second argument to super must be an "
-                    "instance or subtype of type, not {type}.",
-                    super_=self,
-                )
-
-        if not mro_type.newstyle:
-            raise exceptions.SuperError(
-                "Unable to call super on old-style classes.", super_=self
-            )
-
-        mro = mro_type.mro()
-        if self.mro_pointer not in mro:
-            raise exceptions.SuperError(
-                "The second argument to super must be an "
-                "instance or subtype of type, not {type}.",
-                super_=self,
-            )
-
-        index = mro.index(self.mro_pointer)
-        return mro[index + 1 :]
-
-    @decorators.cachedproperty
-    def _proxied(self):
-        ast_builtins = MANAGER.builtins_module
-        return ast_builtins.getattr("super")[0]
-
-    def pytype(self):
-        return "%s.super" % BUILTINS
-
-    def display_type(self):
-        return "Super of"
-
-    @property
-    def name(self):
-        """Get the name of the MRO pointer."""
-        return self.mro_pointer.name
-
-    def qname(self):
-        return "super"
-
-    def igetattr(self, name, context=None):
-        """Retrieve the inferred values of the given attribute name."""
-
-        if name in self.special_attributes:
-            yield self.special_attributes.lookup(name)
-            return
-
-        try:
-            mro = self.super_mro()
-        # Don't let invalid MROs or invalid super calls
-        # leak out as is from this function.
-        except exceptions.SuperError as exc:
-            raise exceptions.AttributeInferenceError(
-                (
-                    "Lookup for {name} on {target!r} because super call {super!r} "
-                    "is invalid."
-                ),
-                target=self,
-                attribute=name,
-                context=context,
-                super_=exc.super_,
-            ) from exc
-        except exceptions.MroError as exc:
-            raise exceptions.AttributeInferenceError(
-                (
-                    "Lookup for {name} on {target!r} failed because {cls!r} has an "
-                    "invalid MRO."
-                ),
-                target=self,
-                attribute=name,
-                context=context,
-                mros=exc.mros,
-                cls=exc.cls,
-            ) from exc
-        found = False
-        for cls in mro:
-            if name not in cls.locals:
-                continue
-
-            found = True
-            for inferred in bases._infer_stmts([cls[name]], context, frame=self):
-                if not isinstance(inferred, scoped_nodes.FunctionDef):
-                    yield inferred
-                    continue
-
-                # We can obtain different descriptors from a super depending
-                # on what we are accessing and where the super call is.
-                if inferred.type == "classmethod":
-                    yield bases.BoundMethod(inferred, cls)
-                elif self._scope.type == "classmethod" and inferred.type == "method":
-                    yield inferred
-                elif self._class_based or inferred.type == "staticmethod":
-                    yield inferred
-                elif bases._is_property(inferred):
-                    # TODO: support other descriptors as well.
-                    try:
-                        yield from inferred.infer_call_result(self, context)
-                    except exceptions.InferenceError:
-                        yield util.Uninferable
-                else:
-                    yield bases.BoundMethod(inferred, cls)
-
-        if not found:
-            raise exceptions.AttributeInferenceError(
-                target=self, attribute=name, context=context
-            )
-
-    def getattr(self, name, context=None):
-        return list(self.igetattr(name, context=context))
-
-
-class ExceptionInstance(bases.Instance):
-    """Class for instances of exceptions
-
-    It has special treatment for some of the exceptions's attributes,
-    which are transformed at runtime into certain concrete objects, such as
-    the case of .args.
-    """
-
-    @decorators.cachedproperty
-    def special_attributes(self):
-        qname = self.qname()
-        instance = objectmodel.BUILTIN_EXCEPTIONS.get(
-            qname, objectmodel.ExceptionInstanceModel
-        )
-        return instance()(self)
-
-
-class DictInstance(bases.Instance):
-    """Special kind of instances for dictionaries
-
-    This instance knows the underlying object model of the dictionaries, which means
-    that methods such as .values or .items can be properly inferred.
-    """
-
-    # pylint: disable=unnecessary-lambda
-    special_attributes = util.lazy_descriptor(lambda: objectmodel.DictModel())
-
-
-# Custom objects tailored for dictionaries, which are used to
-# disambiguate between the types of Python 2 dict's method returns
-# and Python 3 (where they return set like objects).
-class DictItems(bases.Proxy):
-    __str__ = node_classes.NodeNG.__str__
-    __repr__ = node_classes.NodeNG.__repr__
-
-
-class DictKeys(bases.Proxy):
-    __str__ = node_classes.NodeNG.__str__
-    __repr__ = node_classes.NodeNG.__repr__
-
-
-class DictValues(bases.Proxy):
-    __str__ = node_classes.NodeNG.__str__
-    __repr__ = node_classes.NodeNG.__repr__
-
-
-class PartialFunction(scoped_nodes.FunctionDef):
-    """A class representing partial function obtained via functools.partial"""
-
-    def __init__(
-        self, call, name=None, doc=None, lineno=None, col_offset=None, parent=None
-    ):
-        super().__init__(name, doc, lineno, col_offset, parent)
-        self.filled_positionals = len(call.positional_arguments[1:])
-        self.filled_args = call.positional_arguments[1:]
-        self.filled_keywords = call.keyword_arguments
-
-    def infer_call_result(self, caller=None, context=None):
-        if context:
-            current_passed_keywords = {
-                keyword for (keyword, _) in context.callcontext.keywords
-            }
-            for keyword, value in self.filled_keywords.items():
-                if keyword not in current_passed_keywords:
-                    context.callcontext.keywords.append((keyword, value))
-
-            call_context_args = context.callcontext.args or []
-            context.callcontext.args = self.filled_args + call_context_args
-
-        return super().infer_call_result(caller=caller, context=context)
-
-    def qname(self):
-        return self.__class__.__name__
-
-
-# TODO: Hack to solve the circular import problem between node_classes and objects
-# This is not needed in 2.0, which has a cleaner design overall
-node_classes.Dict.__bases__ = (node_classes.NodeNG, DictInstance)
diff --git a/venv/Lib/site-packages/astroid/protocols.py b/venv/Lib/site-packages/astroid/protocols.py
deleted file mode 100644
index c1825f1..0000000
--- a/venv/Lib/site-packages/astroid/protocols.py
+++ /dev/null
@@ -1,766 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2009-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017-2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 rr- <rr-@sakuya.pl>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 HoverHell <hoverhell@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""this module contains a set of functions to handle python protocols for nodes
-where it makes sense.
-"""
-
-import collections
-import operator as operator_mod
-
-import itertools
-
-from astroid import Store
-from astroid import arguments
-from astroid import bases
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import decorators
-from astroid import node_classes
-from astroid import helpers
-from astroid import nodes
-from astroid import util
-
-raw_building = util.lazy_import("raw_building")
-objects = util.lazy_import("objects")
-
-
-def _reflected_name(name):
-    return "__r" + name[2:]
-
-
-def _augmented_name(name):
-    return "__i" + name[2:]
-
-
-_CONTEXTLIB_MGR = "contextlib.contextmanager"
-BIN_OP_METHOD = {
-    "+": "__add__",
-    "-": "__sub__",
-    "/": "__truediv__",
-    "//": "__floordiv__",
-    "*": "__mul__",
-    "**": "__pow__",
-    "%": "__mod__",
-    "&": "__and__",
-    "|": "__or__",
-    "^": "__xor__",
-    "<<": "__lshift__",
-    ">>": "__rshift__",
-    "@": "__matmul__",
-}
-
-REFLECTED_BIN_OP_METHOD = {
-    key: _reflected_name(value) for (key, value) in BIN_OP_METHOD.items()
-}
-AUGMENTED_OP_METHOD = {
-    key + "=": _augmented_name(value) for (key, value) in BIN_OP_METHOD.items()
-}
-
-UNARY_OP_METHOD = {
-    "+": "__pos__",
-    "-": "__neg__",
-    "~": "__invert__",
-    "not": None,  # XXX not '__nonzero__'
-}
-_UNARY_OPERATORS = {
-    "+": operator_mod.pos,
-    "-": operator_mod.neg,
-    "~": operator_mod.invert,
-    "not": operator_mod.not_,
-}
-
-
-def _infer_unary_op(obj, op):
-    func = _UNARY_OPERATORS[op]
-    value = func(obj)
-    return nodes.const_factory(value)
-
-
-nodes.Tuple.infer_unary_op = lambda self, op: _infer_unary_op(tuple(self.elts), op)
-nodes.List.infer_unary_op = lambda self, op: _infer_unary_op(self.elts, op)
-nodes.Set.infer_unary_op = lambda self, op: _infer_unary_op(set(self.elts), op)
-nodes.Const.infer_unary_op = lambda self, op: _infer_unary_op(self.value, op)
-nodes.Dict.infer_unary_op = lambda self, op: _infer_unary_op(dict(self.items), op)
-
-# Binary operations
-
-BIN_OP_IMPL = {
-    "+": lambda a, b: a + b,
-    "-": lambda a, b: a - b,
-    "/": lambda a, b: a / b,
-    "//": lambda a, b: a // b,
-    "*": lambda a, b: a * b,
-    "**": lambda a, b: a ** b,
-    "%": lambda a, b: a % b,
-    "&": lambda a, b: a & b,
-    "|": lambda a, b: a | b,
-    "^": lambda a, b: a ^ b,
-    "<<": lambda a, b: a << b,
-    ">>": lambda a, b: a >> b,
-    "@": operator_mod.matmul,
-}
-for _KEY, _IMPL in list(BIN_OP_IMPL.items()):
-    BIN_OP_IMPL[_KEY + "="] = _IMPL
-
-
-@decorators.yes_if_nothing_inferred
-def const_infer_binary_op(self, opnode, operator, other, context, _):
-    not_implemented = nodes.Const(NotImplemented)
-    if isinstance(other, nodes.Const):
-        try:
-            impl = BIN_OP_IMPL[operator]
-            try:
-                yield nodes.const_factory(impl(self.value, other.value))
-            except TypeError:
-                # ArithmeticError is not enough: float >> float is a TypeError
-                yield not_implemented
-            except Exception:  # pylint: disable=broad-except
-                yield util.Uninferable
-        except TypeError:
-            yield not_implemented
-    elif isinstance(self.value, str) and operator == "%":
-        # TODO(cpopa): implement string interpolation later on.
-        yield util.Uninferable
-    else:
-        yield not_implemented
-
-
-nodes.Const.infer_binary_op = const_infer_binary_op
-
-
-def _multiply_seq_by_int(self, opnode, other, context):
-    node = self.__class__(parent=opnode)
-    filtered_elts = (
-        helpers.safe_infer(elt, context) or util.Uninferable
-        for elt in self.elts
-        if elt is not util.Uninferable
-    )
-    node.elts = list(filtered_elts) * other.value
-    return node
-
-
-def _filter_uninferable_nodes(elts, context):
-    for elt in elts:
-        if elt is util.Uninferable:
-            yield nodes.Unknown()
-        else:
-            for inferred in elt.infer(context):
-                if inferred is not util.Uninferable:
-                    yield inferred
-                else:
-                    yield nodes.Unknown()
-
-
-@decorators.yes_if_nothing_inferred
-def tl_infer_binary_op(self, opnode, operator, other, context, method):
-    not_implemented = nodes.Const(NotImplemented)
-    if isinstance(other, self.__class__) and operator == "+":
-        node = self.__class__(parent=opnode)
-        node.elts = list(
-            itertools.chain(
-                _filter_uninferable_nodes(self.elts, context),
-                _filter_uninferable_nodes(other.elts, context),
-            )
-        )
-        yield node
-    elif isinstance(other, nodes.Const) and operator == "*":
-        if not isinstance(other.value, int):
-            yield not_implemented
-            return
-        yield _multiply_seq_by_int(self, opnode, other, context)
-    elif isinstance(other, bases.Instance) and operator == "*":
-        # Verify if the instance supports __index__.
-        as_index = helpers.class_instance_as_index(other)
-        if not as_index:
-            yield util.Uninferable
-        else:
-            yield _multiply_seq_by_int(self, opnode, as_index, context)
-    else:
-        yield not_implemented
-
-
-nodes.Tuple.infer_binary_op = tl_infer_binary_op
-nodes.List.infer_binary_op = tl_infer_binary_op
-
-
-@decorators.yes_if_nothing_inferred
-def instance_class_infer_binary_op(self, opnode, operator, other, context, method):
-    return method.infer_call_result(self, context)
-
-
-bases.Instance.infer_binary_op = instance_class_infer_binary_op
-nodes.ClassDef.infer_binary_op = instance_class_infer_binary_op
-
-
-# assignment ##################################################################
-
-"""the assigned_stmts method is responsible to return the assigned statement
-(e.g. not inferred) according to the assignment type.
-
-The `assign_path` argument is used to record the lhs path of the original node.
-For instance if we want assigned statements for 'c' in 'a, (b,c)', assign_path
-will be [1, 1] once arrived to the Assign node.
-
-The `context` argument is the current inference context which should be given
-to any intermediary inference necessary.
-"""
-
-
-def _resolve_looppart(parts, assign_path, context):
-    """recursive function to resolve multiple assignments on loops"""
-    assign_path = assign_path[:]
-    index = assign_path.pop(0)
-    for part in parts:
-        if part is util.Uninferable:
-            continue
-        if not hasattr(part, "itered"):
-            continue
-        try:
-            itered = part.itered()
-        except TypeError:
-            continue
-        for stmt in itered:
-            index_node = nodes.Const(index)
-            try:
-                assigned = stmt.getitem(index_node, context)
-            except (
-                AttributeError,
-                exceptions.AstroidTypeError,
-                exceptions.AstroidIndexError,
-            ):
-                continue
-            if not assign_path:
-                # we achieved to resolved the assignment path,
-                # don't infer the last part
-                yield assigned
-            elif assigned is util.Uninferable:
-                break
-            else:
-                # we are not yet on the last part of the path
-                # search on each possibly inferred value
-                try:
-                    yield from _resolve_looppart(
-                        assigned.infer(context), assign_path, context
-                    )
-                except exceptions.InferenceError:
-                    break
-
-
-@decorators.raise_if_nothing_inferred
-def for_assigned_stmts(self, node=None, context=None, assign_path=None):
-    if isinstance(self, nodes.AsyncFor) or getattr(self, "is_async", False):
-        # Skip inferring of async code for now
-        return dict(node=self, unknown=node, assign_path=assign_path, context=context)
-    if assign_path is None:
-        for lst in self.iter.infer(context):
-            if isinstance(lst, (nodes.Tuple, nodes.List)):
-                yield from lst.elts
-    else:
-        yield from _resolve_looppart(self.iter.infer(context), assign_path, context)
-    return dict(node=self, unknown=node, assign_path=assign_path, context=context)
-
-
-nodes.For.assigned_stmts = for_assigned_stmts
-nodes.Comprehension.assigned_stmts = for_assigned_stmts
-
-
-def sequence_assigned_stmts(self, node=None, context=None, assign_path=None):
-    if assign_path is None:
-        assign_path = []
-    try:
-        index = self.elts.index(node)
-    except ValueError as exc:
-        raise exceptions.InferenceError(
-            "Tried to retrieve a node {node!r} which does not exist",
-            node=self,
-            assign_path=assign_path,
-            context=context,
-        ) from exc
-
-    assign_path.insert(0, index)
-    return self.parent.assigned_stmts(
-        node=self, context=context, assign_path=assign_path
-    )
-
-
-nodes.Tuple.assigned_stmts = sequence_assigned_stmts
-nodes.List.assigned_stmts = sequence_assigned_stmts
-
-
-def assend_assigned_stmts(self, node=None, context=None, assign_path=None):
-    return self.parent.assigned_stmts(node=self, context=context)
-
-
-nodes.AssignName.assigned_stmts = assend_assigned_stmts
-nodes.AssignAttr.assigned_stmts = assend_assigned_stmts
-
-
-def _arguments_infer_argname(self, name, context):
-    # arguments information may be missing, in which case we can't do anything
-    # more
-    if not (self.args or self.vararg or self.kwarg):
-        yield util.Uninferable
-        return
-    # first argument of instance/class method
-    if self.args and getattr(self.args[0], "name", None) == name:
-        functype = self.parent.type
-        cls = self.parent.parent.scope()
-        is_metaclass = isinstance(cls, nodes.ClassDef) and cls.type == "metaclass"
-        # If this is a metaclass, then the first argument will always
-        # be the class, not an instance.
-        if is_metaclass or functype == "classmethod":
-            yield cls
-            return
-        if functype == "method":
-            yield bases.Instance(cls)
-            return
-
-    if context and context.callcontext:
-        call_site = arguments.CallSite(context.callcontext, context.extra_context)
-        yield from call_site.infer_argument(self.parent, name, context)
-        return
-
-    if name == self.vararg:
-        vararg = nodes.const_factory(())
-        vararg.parent = self
-        yield vararg
-        return
-    if name == self.kwarg:
-        kwarg = nodes.const_factory({})
-        kwarg.parent = self
-        yield kwarg
-        return
-    # if there is a default value, yield it. And then yield Uninferable to reflect
-    # we can't guess given argument value
-    try:
-        context = contextmod.copy_context(context)
-        yield from self.default_value(name).infer(context)
-        yield util.Uninferable
-    except exceptions.NoDefault:
-        yield util.Uninferable
-
-
-def arguments_assigned_stmts(self, node=None, context=None, assign_path=None):
-    if context.callcontext:
-        # reset call context/name
-        callcontext = context.callcontext
-        context = contextmod.copy_context(context)
-        context.callcontext = None
-        args = arguments.CallSite(callcontext)
-        return args.infer_argument(self.parent, node.name, context)
-    return _arguments_infer_argname(self, node.name, context)
-
-
-nodes.Arguments.assigned_stmts = arguments_assigned_stmts
-
-
-@decorators.raise_if_nothing_inferred
-def assign_assigned_stmts(self, node=None, context=None, assign_path=None):
-    if not assign_path:
-        yield self.value
-        return None
-    yield from _resolve_assignment_parts(
-        self.value.infer(context), assign_path, context
-    )
-
-    return dict(node=self, unknown=node, assign_path=assign_path, context=context)
-
-
-def assign_annassigned_stmts(self, node=None, context=None, assign_path=None):
-    for inferred in assign_assigned_stmts(self, node, context, assign_path):
-        if inferred is None:
-            yield util.Uninferable
-        else:
-            yield inferred
-
-
-nodes.Assign.assigned_stmts = assign_assigned_stmts
-nodes.AnnAssign.assigned_stmts = assign_annassigned_stmts
-nodes.AugAssign.assigned_stmts = assign_assigned_stmts
-
-
-def _resolve_assignment_parts(parts, assign_path, context):
-    """recursive function to resolve multiple assignments"""
-    assign_path = assign_path[:]
-    index = assign_path.pop(0)
-    for part in parts:
-        assigned = None
-        if isinstance(part, nodes.Dict):
-            # A dictionary in an iterating context
-            try:
-                assigned, _ = part.items[index]
-            except IndexError:
-                return
-
-        elif hasattr(part, "getitem"):
-            index_node = nodes.Const(index)
-            try:
-                assigned = part.getitem(index_node, context)
-            except (exceptions.AstroidTypeError, exceptions.AstroidIndexError):
-                return
-
-        if not assigned:
-            return
-
-        if not assign_path:
-            # we achieved to resolved the assignment path, don't infer the
-            # last part
-            yield assigned
-        elif assigned is util.Uninferable:
-            return
-        else:
-            # we are not yet on the last part of the path search on each
-            # possibly inferred value
-            try:
-                yield from _resolve_assignment_parts(
-                    assigned.infer(context), assign_path, context
-                )
-            except exceptions.InferenceError:
-                return
-
-
-@decorators.raise_if_nothing_inferred
-def excepthandler_assigned_stmts(self, node=None, context=None, assign_path=None):
-    for assigned in node_classes.unpack_infer(self.type):
-        if isinstance(assigned, nodes.ClassDef):
-            assigned = objects.ExceptionInstance(assigned)
-
-        yield assigned
-    return dict(node=self, unknown=node, assign_path=assign_path, context=context)
-
-
-nodes.ExceptHandler.assigned_stmts = excepthandler_assigned_stmts
-
-
-def _infer_context_manager(self, mgr, context):
-    inferred = next(mgr.infer(context=context))
-    if isinstance(inferred, bases.Generator):
-        # Check if it is decorated with contextlib.contextmanager.
-        func = inferred.parent
-        if not func.decorators:
-            raise exceptions.InferenceError(
-                "No decorators found on inferred generator %s", node=func
-            )
-
-        for decorator_node in func.decorators.nodes:
-            decorator = next(decorator_node.infer(context))
-            if isinstance(decorator, nodes.FunctionDef):
-                if decorator.qname() == _CONTEXTLIB_MGR:
-                    break
-        else:
-            # It doesn't interest us.
-            raise exceptions.InferenceError(node=func)
-
-        # Get the first yield point. If it has multiple yields,
-        # then a RuntimeError will be raised.
-
-        possible_yield_points = func.nodes_of_class(nodes.Yield)
-        # Ignore yields in nested functions
-        yield_point = next(
-            (node for node in possible_yield_points if node.scope() == func), None
-        )
-        if yield_point:
-            if not yield_point.value:
-                const = nodes.Const(None)
-                const.parent = yield_point
-                const.lineno = yield_point.lineno
-                yield const
-            else:
-                yield from yield_point.value.infer(context=context)
-    elif isinstance(inferred, bases.Instance):
-        try:
-            enter = next(inferred.igetattr("__enter__", context=context))
-        except (exceptions.InferenceError, exceptions.AttributeInferenceError):
-            raise exceptions.InferenceError(node=inferred)
-        if not isinstance(enter, bases.BoundMethod):
-            raise exceptions.InferenceError(node=enter)
-        yield from enter.infer_call_result(self, context)
-    else:
-        raise exceptions.InferenceError(node=mgr)
-
-
-@decorators.raise_if_nothing_inferred
-def with_assigned_stmts(self, node=None, context=None, assign_path=None):
-    """Infer names and other nodes from a *with* statement.
-
-    This enables only inference for name binding in a *with* statement.
-    For instance, in the following code, inferring `func` will return
-    the `ContextManager` class, not whatever ``__enter__`` returns.
-    We are doing this intentionally, because we consider that the context
-    manager result is whatever __enter__ returns and what it is binded
-    using the ``as`` keyword.
-
-        class ContextManager(object):
-            def __enter__(self):
-                return 42
-        with ContextManager() as f:
-            pass
-
-        # ContextManager().infer() will return ContextManager
-        # f.infer() will return 42.
-
-    Arguments:
-        self: nodes.With
-        node: The target of the assignment, `as (a, b)` in `with foo as (a, b)`.
-        context: Inference context used for caching already inferred objects
-        assign_path:
-            A list of indices, where each index specifies what item to fetch from
-            the inference results.
-    """
-    try:
-        mgr = next(mgr for (mgr, vars) in self.items if vars == node)
-    except StopIteration:
-        return None
-    if assign_path is None:
-        yield from _infer_context_manager(self, mgr, context)
-    else:
-        for result in _infer_context_manager(self, mgr, context):
-            # Walk the assign_path and get the item at the final index.
-            obj = result
-            for index in assign_path:
-                if not hasattr(obj, "elts"):
-                    raise exceptions.InferenceError(
-                        "Wrong type ({targets!r}) for {node!r} assignment",
-                        node=self,
-                        targets=node,
-                        assign_path=assign_path,
-                        context=context,
-                    )
-                try:
-                    obj = obj.elts[index]
-                except IndexError as exc:
-                    raise exceptions.InferenceError(
-                        "Tried to infer a nonexistent target with index {index} "
-                        "in {node!r}.",
-                        node=self,
-                        targets=node,
-                        assign_path=assign_path,
-                        context=context,
-                    ) from exc
-                except TypeError as exc:
-                    raise exceptions.InferenceError(
-                        "Tried to unpack a non-iterable value " "in {node!r}.",
-                        node=self,
-                        targets=node,
-                        assign_path=assign_path,
-                        context=context,
-                    ) from exc
-            yield obj
-    return dict(node=self, unknown=node, assign_path=assign_path, context=context)
-
-
-nodes.With.assigned_stmts = with_assigned_stmts
-
-
-@decorators.raise_if_nothing_inferred
-def named_expr_assigned_stmts(self, node, context=None, assign_path=None):
-    """Infer names and other nodes from an assignment expression"""
-    if self.target == node:
-        yield from self.value.infer(context=context)
-    else:
-        raise exceptions.InferenceError(
-            "Cannot infer NamedExpr node {node!r}",
-            node=self,
-            assign_path=assign_path,
-            context=context,
-        )
-
-
-nodes.NamedExpr.assigned_stmts = named_expr_assigned_stmts
-
-
-@decorators.yes_if_nothing_inferred
-def starred_assigned_stmts(self, node=None, context=None, assign_path=None):
-    """
-    Arguments:
-        self: nodes.Starred
-        node: a node related to the current underlying Node.
-        context: Inference context used for caching already inferred objects
-        assign_path:
-            A list of indices, where each index specifies what item to fetch from
-            the inference results.
-    """
-    # pylint: disable=too-many-locals,too-many-branches,too-many-statements
-    def _determine_starred_iteration_lookups(starred, target, lookups):
-        # Determine the lookups for the rhs of the iteration
-        itered = target.itered()
-        for index, element in enumerate(itered):
-            if (
-                isinstance(element, nodes.Starred)
-                and element.value.name == starred.value.name
-            ):
-                lookups.append((index, len(itered)))
-                break
-            if isinstance(element, nodes.Tuple):
-                lookups.append((index, len(element.itered())))
-                _determine_starred_iteration_lookups(starred, element, lookups)
-
-    stmt = self.statement()
-    if not isinstance(stmt, (nodes.Assign, nodes.For)):
-        raise exceptions.InferenceError(
-            "Statement {stmt!r} enclosing {node!r} " "must be an Assign or For node.",
-            node=self,
-            stmt=stmt,
-            unknown=node,
-            context=context,
-        )
-
-    if context is None:
-        context = contextmod.InferenceContext()
-
-    if isinstance(stmt, nodes.Assign):
-        value = stmt.value
-        lhs = stmt.targets[0]
-
-        if sum(1 for _ in lhs.nodes_of_class(nodes.Starred)) > 1:
-            raise exceptions.InferenceError(
-                "Too many starred arguments in the " " assignment targets {lhs!r}.",
-                node=self,
-                targets=lhs,
-                unknown=node,
-                context=context,
-            )
-
-        try:
-            rhs = next(value.infer(context))
-        except exceptions.InferenceError:
-            yield util.Uninferable
-            return
-        if rhs is util.Uninferable or not hasattr(rhs, "itered"):
-            yield util.Uninferable
-            return
-
-        try:
-            elts = collections.deque(rhs.itered())
-        except TypeError:
-            yield util.Uninferable
-            return
-
-        # Unpack iteratively the values from the rhs of the assignment,
-        # until the find the starred node. What will remain will
-        # be the list of values which the Starred node will represent
-        # This is done in two steps, from left to right to remove
-        # anything before the starred node and from right to left
-        # to remove anything after the starred node.
-
-        for index, left_node in enumerate(lhs.elts):
-            if not isinstance(left_node, nodes.Starred):
-                if not elts:
-                    break
-                elts.popleft()
-                continue
-            lhs_elts = collections.deque(reversed(lhs.elts[index:]))
-            for right_node in lhs_elts:
-                if not isinstance(right_node, nodes.Starred):
-                    if not elts:
-                        break
-                    elts.pop()
-                    continue
-                # We're done
-                packed = nodes.List(
-                    ctx=Store, parent=self, lineno=lhs.lineno, col_offset=lhs.col_offset
-                )
-                packed.postinit(elts=elts)
-                yield packed
-                break
-
-    if isinstance(stmt, nodes.For):
-        try:
-            inferred_iterable = next(stmt.iter.infer(context=context))
-        except exceptions.InferenceError:
-            yield util.Uninferable
-            return
-        if inferred_iterable is util.Uninferable or not hasattr(
-            inferred_iterable, "itered"
-        ):
-            yield util.Uninferable
-            return
-        try:
-            itered = inferred_iterable.itered()
-        except TypeError:
-            yield util.Uninferable
-            return
-
-        target = stmt.target
-
-        if not isinstance(target, nodes.Tuple):
-            raise exceptions.InferenceError(
-                "Could not make sense of this, the target must be a tuple",
-                context=context,
-            )
-
-        lookups = []
-        _determine_starred_iteration_lookups(self, target, lookups)
-        if not lookups:
-            raise exceptions.InferenceError(
-                "Could not make sense of this, needs at least a lookup", context=context
-            )
-
-        # Make the last lookup a slice, since that what we want for a Starred node
-        last_element_index, last_element_length = lookups[-1]
-        is_starred_last = last_element_index == (last_element_length - 1)
-
-        lookup_slice = slice(
-            last_element_index,
-            None if is_starred_last else (last_element_length - last_element_index),
-        )
-        lookups[-1] = lookup_slice
-
-        for element in itered:
-
-            # We probably want to infer the potential values *for each* element in an
-            # iterable, but we can't infer a list of all values, when only a list of
-            # step values are expected:
-            #
-            # for a, *b in [...]:
-            #   b
-            #
-            # *b* should now point to just the elements at that particular iteration step,
-            # which astroid can't know about.
-
-            found_element = None
-            for lookup in lookups:
-                if not hasattr(element, "itered"):
-                    break
-                if not isinstance(lookup, slice):
-                    # Grab just the index, not the whole length
-                    lookup = lookup[0]
-                try:
-                    itered_inner_element = element.itered()
-                    element = itered_inner_element[lookup]
-                except IndexError:
-                    break
-                except TypeError:
-                    # Most likely the itered() call failed, cannot make sense of this
-                    yield util.Uninferable
-                    return
-                else:
-                    found_element = element
-
-            unpacked = nodes.List(
-                ctx=Store, parent=self, lineno=self.lineno, col_offset=self.col_offset
-            )
-            unpacked.postinit(elts=found_element or [])
-            yield unpacked
-            return
-
-        yield util.Uninferable
-
-
-nodes.Starred.assigned_stmts = starred_assigned_stmts
diff --git a/venv/Lib/site-packages/astroid/raw_building.py b/venv/Lib/site-packages/astroid/raw_building.py
deleted file mode 100644
index d94f924..0000000
--- a/venv/Lib/site-packages/astroid/raw_building.py
+++ /dev/null
@@ -1,468 +0,0 @@
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Google, Inc.
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Ovidiu Sabou <ovidiu@sabou.org>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""this module contains a set of functions to create astroid trees from scratch
-(build_* functions) or from living object (object_build_* functions)
-"""
-
-import builtins
-import inspect
-import os
-import sys
-import types
-
-from astroid import bases
-from astroid import manager
-from astroid import node_classes
-from astroid import nodes
-
-
-MANAGER = manager.AstroidManager()
-# the keys of CONST_CLS eg python builtin types
-
-_CONSTANTS = tuple(node_classes.CONST_CLS)
-_BUILTINS = vars(builtins)
-TYPE_NONE = type(None)
-TYPE_NOTIMPLEMENTED = type(NotImplemented)
-TYPE_ELLIPSIS = type(...)
-
-
-def _io_discrepancy(member):
-    # _io module names itself `io`: http://bugs.python.org/issue18602
-    member_self = getattr(member, "__self__", None)
-    return (
-        member_self
-        and inspect.ismodule(member_self)
-        and member_self.__name__ == "_io"
-        and member.__module__ == "io"
-    )
-
-
-def _attach_local_node(parent, node, name):
-    node.name = name  # needed by add_local_node
-    parent.add_local_node(node)
-
-
-def _add_dunder_class(func, member):
-    """Add a __class__ member to the given func node, if we can determine it."""
-    python_cls = member.__class__
-    cls_name = getattr(python_cls, "__name__", None)
-    if not cls_name:
-        return
-    cls_bases = [ancestor.__name__ for ancestor in python_cls.__bases__]
-    ast_klass = build_class(cls_name, cls_bases, python_cls.__doc__)
-    func.instance_attrs["__class__"] = [ast_klass]
-
-
-_marker = object()
-
-
-def attach_dummy_node(node, name, runtime_object=_marker):
-    """create a dummy node and register it in the locals of the given
-    node with the specified name
-    """
-    enode = nodes.EmptyNode()
-    enode.object = runtime_object
-    _attach_local_node(node, enode, name)
-
-
-def _has_underlying_object(self):
-    return self.object is not None and self.object is not _marker
-
-
-nodes.EmptyNode.has_underlying_object = _has_underlying_object
-
-
-def attach_const_node(node, name, value):
-    """create a Const node and register it in the locals of the given
-    node with the specified name
-    """
-    if name not in node.special_attributes:
-        _attach_local_node(node, nodes.const_factory(value), name)
-
-
-def attach_import_node(node, modname, membername):
-    """create a ImportFrom node and register it in the locals of the given
-    node with the specified name
-    """
-    from_node = nodes.ImportFrom(modname, [(membername, None)])
-    _attach_local_node(node, from_node, membername)
-
-
-def build_module(name, doc=None):
-    """create and initialize an astroid Module node"""
-    node = nodes.Module(name, doc, pure_python=False)
-    node.package = False
-    node.parent = None
-    return node
-
-
-def build_class(name, basenames=(), doc=None):
-    """create and initialize an astroid ClassDef node"""
-    node = nodes.ClassDef(name, doc)
-    for base in basenames:
-        basenode = nodes.Name()
-        basenode.name = base
-        node.bases.append(basenode)
-        basenode.parent = node
-    return node
-
-
-def build_function(name, args=None, posonlyargs=None, defaults=None, doc=None):
-    """create and initialize an astroid FunctionDef node"""
-    args, defaults, posonlyargs = args or [], defaults or [], posonlyargs or []
-    # first argument is now a list of decorators
-    func = nodes.FunctionDef(name, doc)
-    func.args = argsnode = nodes.Arguments()
-    argsnode.args = []
-    argsnode.posonlyargs = []
-    for arg in args:
-        argsnode.args.append(nodes.Name())
-        argsnode.args[-1].name = arg
-        argsnode.args[-1].parent = argsnode
-    for arg in posonlyargs:
-        argsnode.posonlyargs.append(nodes.Name())
-        argsnode.posonlyargs[-1].name = arg
-        argsnode.posonlyargs[-1].parent = argsnode
-    argsnode.defaults = []
-    for default in defaults:
-        argsnode.defaults.append(nodes.const_factory(default))
-        argsnode.defaults[-1].parent = argsnode
-    argsnode.kwarg = None
-    argsnode.vararg = None
-    argsnode.parent = func
-    if args:
-        register_arguments(func)
-    return func
-
-
-def build_from_import(fromname, names):
-    """create and initialize an astroid ImportFrom import statement"""
-    return nodes.ImportFrom(fromname, [(name, None) for name in names])
-
-
-def register_arguments(func, args=None):
-    """add given arguments to local
-
-    args is a list that may contains nested lists
-    (i.e. def func(a, (b, c, d)): ...)
-    """
-    if args is None:
-        args = func.args.args
-        if func.args.vararg:
-            func.set_local(func.args.vararg, func.args)
-        if func.args.kwarg:
-            func.set_local(func.args.kwarg, func.args)
-    for arg in args:
-        if isinstance(arg, nodes.Name):
-            func.set_local(arg.name, arg)
-        else:
-            register_arguments(func, arg.elts)
-
-
-def object_build_class(node, member, localname):
-    """create astroid for a living class object"""
-    basenames = [base.__name__ for base in member.__bases__]
-    return _base_class_object_build(node, member, basenames, localname=localname)
-
-
-def object_build_function(node, member, localname):
-    """create astroid for a living function object"""
-    signature = inspect.signature(member)
-    args = []
-    defaults = []
-    posonlyargs = []
-    for param_name, param in signature.parameters.items():
-        if param.kind == inspect.Parameter.POSITIONAL_ONLY:
-            posonlyargs.append(param_name)
-        elif param.kind == inspect.Parameter.POSITIONAL_OR_KEYWORD:
-            args.append(param_name)
-        elif param.kind == inspect.Parameter.VAR_POSITIONAL:
-            args.append(param_name)
-        elif param.kind == inspect.Parameter.VAR_KEYWORD:
-            args.append(param_name)
-        if param.default is not inspect._empty:
-            defaults.append(param.default)
-    func = build_function(
-        getattr(member, "__name__", None) or localname,
-        args,
-        posonlyargs,
-        defaults,
-        member.__doc__,
-    )
-    node.add_local_node(func, localname)
-
-
-def object_build_datadescriptor(node, member, name):
-    """create astroid for a living data descriptor object"""
-    return _base_class_object_build(node, member, [], name)
-
-
-def object_build_methoddescriptor(node, member, localname):
-    """create astroid for a living method descriptor object"""
-    # FIXME get arguments ?
-    func = build_function(
-        getattr(member, "__name__", None) or localname, doc=member.__doc__
-    )
-    # set node's arguments to None to notice that we have no information, not
-    # and empty argument list
-    func.args.args = None
-    node.add_local_node(func, localname)
-    _add_dunder_class(func, member)
-
-
-def _base_class_object_build(node, member, basenames, name=None, localname=None):
-    """create astroid for a living class object, with a given set of base names
-    (e.g. ancestors)
-    """
-    klass = build_class(
-        name or getattr(member, "__name__", None) or localname,
-        basenames,
-        member.__doc__,
-    )
-    klass._newstyle = isinstance(member, type)
-    node.add_local_node(klass, localname)
-    try:
-        # limit the instantiation trick since it's too dangerous
-        # (such as infinite test execution...)
-        # this at least resolves common case such as Exception.args,
-        # OSError.errno
-        if issubclass(member, Exception):
-            instdict = member().__dict__
-        else:
-            raise TypeError
-    except TypeError:
-        pass
-    else:
-        for item_name, obj in instdict.items():
-            valnode = nodes.EmptyNode()
-            valnode.object = obj
-            valnode.parent = klass
-            valnode.lineno = 1
-            klass.instance_attrs[item_name] = [valnode]
-    return klass
-
-
-def _build_from_function(node, name, member, module):
-    # verify this is not an imported function
-    try:
-        code = member.__code__
-    except AttributeError:
-        # Some implementations don't provide the code object,
-        # such as Jython.
-        code = None
-    filename = getattr(code, "co_filename", None)
-    if filename is None:
-        assert isinstance(member, object)
-        object_build_methoddescriptor(node, member, name)
-    elif filename != getattr(module, "__file__", None):
-        attach_dummy_node(node, name, member)
-    else:
-        object_build_function(node, member, name)
-
-
-class InspectBuilder:
-    """class for building nodes from living object
-
-    this is actually a really minimal representation, including only Module,
-    FunctionDef and ClassDef nodes and some others as guessed.
-    """
-
-    def __init__(self):
-        self._done = {}
-        self._module = None
-
-    def inspect_build(self, module, modname=None, path=None):
-        """build astroid from a living module (i.e. using inspect)
-        this is used when there is no python source code available (either
-        because it's a built-in module or because the .py is not available)
-        """
-        self._module = module
-        if modname is None:
-            modname = module.__name__
-        try:
-            node = build_module(modname, module.__doc__)
-        except AttributeError:
-            # in jython, java modules have no __doc__ (see #109562)
-            node = build_module(modname)
-        node.file = node.path = os.path.abspath(path) if path else path
-        node.name = modname
-        MANAGER.cache_module(node)
-        node.package = hasattr(module, "__path__")
-        self._done = {}
-        self.object_build(node, module)
-        return node
-
-    def object_build(self, node, obj):
-        """recursive method which create a partial ast from real objects
-         (only function, class, and method are handled)
-        """
-        if obj in self._done:
-            return self._done[obj]
-        self._done[obj] = node
-        for name in dir(obj):
-            try:
-                member = getattr(obj, name)
-            except AttributeError:
-                # damned ExtensionClass.Base, I know you're there !
-                attach_dummy_node(node, name)
-                continue
-            if inspect.ismethod(member):
-                member = member.__func__
-            if inspect.isfunction(member):
-                _build_from_function(node, name, member, self._module)
-            elif inspect.isbuiltin(member):
-                if not _io_discrepancy(member) and self.imported_member(
-                    node, member, name
-                ):
-                    continue
-                object_build_methoddescriptor(node, member, name)
-            elif inspect.isclass(member):
-                if self.imported_member(node, member, name):
-                    continue
-                if member in self._done:
-                    class_node = self._done[member]
-                    if class_node not in node.locals.get(name, ()):
-                        node.add_local_node(class_node, name)
-                else:
-                    class_node = object_build_class(node, member, name)
-                    # recursion
-                    self.object_build(class_node, member)
-                if name == "__class__" and class_node.parent is None:
-                    class_node.parent = self._done[self._module]
-            elif inspect.ismethoddescriptor(member):
-                assert isinstance(member, object)
-                object_build_methoddescriptor(node, member, name)
-            elif inspect.isdatadescriptor(member):
-                assert isinstance(member, object)
-                object_build_datadescriptor(node, member, name)
-            elif isinstance(member, _CONSTANTS):
-                attach_const_node(node, name, member)
-            elif inspect.isroutine(member):
-                # This should be called for Jython, where some builtin
-                # methods aren't caught by isbuiltin branch.
-                _build_from_function(node, name, member, self._module)
-            else:
-                # create an empty node so that the name is actually defined
-                attach_dummy_node(node, name, member)
-        return None
-
-    def imported_member(self, node, member, name):
-        """verify this is not an imported class or handle it"""
-        # /!\ some classes like ExtensionClass doesn't have a __module__
-        # attribute ! Also, this may trigger an exception on badly built module
-        # (see http://www.logilab.org/ticket/57299 for instance)
-        try:
-            modname = getattr(member, "__module__", None)
-        except TypeError:
-            modname = None
-        if modname is None:
-            if name in ("__new__", "__subclasshook__"):
-                # Python 2.5.1 (r251:54863, Sep  1 2010, 22:03:14)
-                # >>> print object.__new__.__module__
-                # None
-                modname = builtins.__name__
-            else:
-                attach_dummy_node(node, name, member)
-                return True
-
-        real_name = {"gtk": "gtk_gtk", "_io": "io"}.get(modname, modname)
-
-        if real_name != self._module.__name__:
-            # check if it sounds valid and then add an import node, else use a
-            # dummy node
-            try:
-                getattr(sys.modules[modname], name)
-            except (KeyError, AttributeError):
-                attach_dummy_node(node, name, member)
-            else:
-                attach_import_node(node, modname, name)
-            return True
-        return False
-
-
-### astroid bootstrapping ######################################################
-
-_CONST_PROXY = {}
-
-# TODO : find a nicer way to handle this situation;
-def _set_proxied(const):
-    return _CONST_PROXY[const.value.__class__]
-
-
-def _astroid_bootstrapping():
-    """astroid bootstrapping the builtins module"""
-    # this boot strapping is necessary since we need the Const nodes to
-    # inspect_build builtins, and then we can proxy Const
-    builder = InspectBuilder()
-    astroid_builtin = builder.inspect_build(builtins)
-
-    # pylint: disable=redefined-outer-name
-    for cls, node_cls in node_classes.CONST_CLS.items():
-        if cls is TYPE_NONE:
-            proxy = build_class("NoneType")
-            proxy.parent = astroid_builtin
-        elif cls is TYPE_NOTIMPLEMENTED:
-            proxy = build_class("NotImplementedType")
-            proxy.parent = astroid_builtin
-        elif cls is TYPE_ELLIPSIS:
-            proxy = build_class("Ellipsis")
-            proxy.parent = astroid_builtin
-        else:
-            proxy = astroid_builtin.getattr(cls.__name__)[0]
-        if cls in (dict, list, set, tuple):
-            node_cls._proxied = proxy
-        else:
-            _CONST_PROXY[cls] = proxy
-
-    # Set the builtin module as parent for some builtins.
-    nodes.Const._proxied = property(_set_proxied)
-
-    _GeneratorType = nodes.ClassDef(
-        types.GeneratorType.__name__, types.GeneratorType.__doc__
-    )
-    _GeneratorType.parent = astroid_builtin
-    bases.Generator._proxied = _GeneratorType
-    builder.object_build(bases.Generator._proxied, types.GeneratorType)
-
-    if hasattr(types, "AsyncGeneratorType"):
-        # pylint: disable=no-member; AsyncGeneratorType
-        _AsyncGeneratorType = nodes.ClassDef(
-            types.AsyncGeneratorType.__name__, types.AsyncGeneratorType.__doc__
-        )
-        _AsyncGeneratorType.parent = astroid_builtin
-        bases.AsyncGenerator._proxied = _AsyncGeneratorType
-        builder.object_build(bases.AsyncGenerator._proxied, types.AsyncGeneratorType)
-    builtin_types = (
-        types.GetSetDescriptorType,
-        types.GeneratorType,
-        types.MemberDescriptorType,
-        TYPE_NONE,
-        TYPE_NOTIMPLEMENTED,
-        types.FunctionType,
-        types.MethodType,
-        types.BuiltinFunctionType,
-        types.ModuleType,
-        types.TracebackType,
-    )
-    for _type in builtin_types:
-        if _type.__name__ not in astroid_builtin:
-            cls = nodes.ClassDef(_type.__name__, _type.__doc__)
-            cls.parent = astroid_builtin
-            builder.object_build(cls, _type)
-            astroid_builtin[_type.__name__] = cls
-
-
-_astroid_bootstrapping()
diff --git a/venv/Lib/site-packages/astroid/rebuilder.py b/venv/Lib/site-packages/astroid/rebuilder.py
deleted file mode 100644
index fb78f7b..0000000
--- a/venv/Lib/site-packages/astroid/rebuilder.py
+++ /dev/null
@@ -1,1090 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2009-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014 Alexander Presnyakov <flagist0@gmail.com>
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016-2017 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2016 Jared Garst <jgarst@users.noreply.github.com>
-# Copyright (c) 2017 Hugo <hugovk@users.noreply.github.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 rr- <rr-@sakuya.pl>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""this module contains utilities for rebuilding a _ast tree in
-order to get a single Astroid representation
-"""
-
-import sys
-
-import astroid
-from astroid._ast import _parse, _get_parser_module, parse_function_type_comment
-from astroid import nodes
-
-
-CONST_NAME_TRANSFORMS = {"None": None, "True": True, "False": False}
-
-REDIRECT = {
-    "arguments": "Arguments",
-    "comprehension": "Comprehension",
-    "ListCompFor": "Comprehension",
-    "GenExprFor": "Comprehension",
-    "excepthandler": "ExceptHandler",
-    "keyword": "Keyword",
-}
-PY37 = sys.version_info >= (3, 7)
-PY38 = sys.version_info >= (3, 8)
-
-
-def _binary_operators_from_module(module):
-    binary_operators = {
-        module.Add: "+",
-        module.BitAnd: "&",
-        module.BitOr: "|",
-        module.BitXor: "^",
-        module.Div: "/",
-        module.FloorDiv: "//",
-        module.MatMult: "@",
-        module.Mod: "%",
-        module.Mult: "*",
-        module.Pow: "**",
-        module.Sub: "-",
-        module.LShift: "<<",
-        module.RShift: ">>",
-    }
-    return binary_operators
-
-
-def _bool_operators_from_module(module):
-    return {module.And: "and", module.Or: "or"}
-
-
-def _unary_operators_from_module(module):
-    return {module.UAdd: "+", module.USub: "-", module.Not: "not", module.Invert: "~"}
-
-
-def _compare_operators_from_module(module):
-    return {
-        module.Eq: "==",
-        module.Gt: ">",
-        module.GtE: ">=",
-        module.In: "in",
-        module.Is: "is",
-        module.IsNot: "is not",
-        module.Lt: "<",
-        module.LtE: "<=",
-        module.NotEq: "!=",
-        module.NotIn: "not in",
-    }
-
-
-def _contexts_from_module(module):
-    return {
-        module.Load: astroid.Load,
-        module.Store: astroid.Store,
-        module.Del: astroid.Del,
-        module.Param: astroid.Store,
-    }
-
-
-def _visit_or_none(node, attr, visitor, parent, visit="visit", **kws):
-    """If the given node has an attribute, visits the attribute, and
-    otherwise returns None.
-
-    """
-    value = getattr(node, attr, None)
-    if value:
-        return getattr(visitor, visit)(value, parent, **kws)
-
-    return None
-
-
-class TreeRebuilder:
-    """Rebuilds the _ast tree to become an Astroid tree"""
-
-    def __init__(self, manager, parse_python_two: bool = False):
-        self._manager = manager
-        self._global_names = []
-        self._import_from_nodes = []
-        self._delayed_assattr = []
-        self._visit_meths = {}
-
-        # Configure the right classes for the right module
-        self._parser_module = _get_parser_module(parse_python_two=parse_python_two)
-        self._unary_op_classes = _unary_operators_from_module(self._parser_module)
-        self._cmp_op_classes = _compare_operators_from_module(self._parser_module)
-        self._bool_op_classes = _bool_operators_from_module(self._parser_module)
-        self._bin_op_classes = _binary_operators_from_module(self._parser_module)
-        self._context_classes = _contexts_from_module(self._parser_module)
-
-    def _get_doc(self, node):
-        try:
-            if PY37 and hasattr(node, "docstring"):
-                doc = node.docstring
-                return node, doc
-            if node.body and isinstance(node.body[0], self._parser_module.Expr):
-
-                first_value = node.body[0].value
-                if isinstance(first_value, self._parser_module.Str) or (
-                    PY38
-                    and isinstance(first_value, self._parser_module.Constant)
-                    and isinstance(first_value.value, str)
-                ):
-                    doc = first_value.value if PY38 else first_value.s
-                    node.body = node.body[1:]
-                    return node, doc
-        except IndexError:
-            pass  # ast built from scratch
-        return node, None
-
-    def _get_context(self, node):
-        return self._context_classes.get(type(node.ctx), astroid.Load)
-
-    def visit_module(self, node, modname, modpath, package):
-        """visit a Module node by returning a fresh instance of it"""
-        node, doc = self._get_doc(node)
-        newnode = nodes.Module(
-            name=modname,
-            doc=doc,
-            file=modpath,
-            path=[modpath],
-            package=package,
-            parent=None,
-        )
-        newnode.postinit([self.visit(child, newnode) for child in node.body])
-        return newnode
-
-    def visit(self, node, parent):
-        cls = node.__class__
-        if cls in self._visit_meths:
-            visit_method = self._visit_meths[cls]
-        else:
-            cls_name = cls.__name__
-            visit_name = "visit_" + REDIRECT.get(cls_name, cls_name).lower()
-            visit_method = getattr(self, visit_name)
-            self._visit_meths[cls] = visit_method
-        return visit_method(node, parent)
-
-    def _save_assignment(self, node, name=None):
-        """save assignement situation since node.parent is not available yet"""
-        if self._global_names and node.name in self._global_names[-1]:
-            node.root().set_local(node.name, node)
-        else:
-            node.parent.set_local(node.name, node)
-
-    def visit_arguments(self, node, parent):
-        """visit an Arguments node by returning a fresh instance of it"""
-        vararg, kwarg = node.vararg, node.kwarg
-        newnode = nodes.Arguments(
-            vararg.arg if vararg else None, kwarg.arg if kwarg else None, parent
-        )
-        args = [self.visit(child, newnode) for child in node.args]
-        defaults = [self.visit(child, newnode) for child in node.defaults]
-        varargannotation = None
-        kwargannotation = None
-        posonlyargs = []
-        # change added in 82732 (7c5c678e4164), vararg and kwarg
-        # are instances of `_ast.arg`, not strings
-        if vararg:
-            if node.vararg.annotation:
-                varargannotation = self.visit(node.vararg.annotation, newnode)
-            vararg = vararg.arg
-        if kwarg:
-            if node.kwarg.annotation:
-                kwargannotation = self.visit(node.kwarg.annotation, newnode)
-            kwarg = kwarg.arg
-        kwonlyargs = [self.visit(child, newnode) for child in node.kwonlyargs]
-        kw_defaults = [
-            self.visit(child, newnode) if child else None for child in node.kw_defaults
-        ]
-        annotations = [
-            self.visit(arg.annotation, newnode) if arg.annotation else None
-            for arg in node.args
-        ]
-        kwonlyargs_annotations = [
-            self.visit(arg.annotation, newnode) if arg.annotation else None
-            for arg in node.kwonlyargs
-        ]
-
-        posonlyargs_annotations = []
-        if PY38:
-            posonlyargs = [self.visit(child, newnode) for child in node.posonlyargs]
-            posonlyargs_annotations = [
-                self.visit(arg.annotation, newnode) if arg.annotation else None
-                for arg in node.posonlyargs
-            ]
-        type_comment_args = [
-            self.check_type_comment(child, parent=newnode) for child in node.args
-        ]
-
-        newnode.postinit(
-            args=args,
-            defaults=defaults,
-            kwonlyargs=kwonlyargs,
-            posonlyargs=posonlyargs,
-            kw_defaults=kw_defaults,
-            annotations=annotations,
-            kwonlyargs_annotations=kwonlyargs_annotations,
-            posonlyargs_annotations=posonlyargs_annotations,
-            varargannotation=varargannotation,
-            kwargannotation=kwargannotation,
-            type_comment_args=type_comment_args,
-        )
-        # save argument names in locals:
-        if vararg:
-            newnode.parent.set_local(vararg, newnode)
-        if kwarg:
-            newnode.parent.set_local(kwarg, newnode)
-        return newnode
-
-    def visit_assert(self, node, parent):
-        """visit a Assert node by returning a fresh instance of it"""
-        newnode = nodes.Assert(node.lineno, node.col_offset, parent)
-        if node.msg:
-            msg = self.visit(node.msg, newnode)
-        else:
-            msg = None
-        newnode.postinit(self.visit(node.test, newnode), msg)
-        return newnode
-
-    def check_type_comment(self, node, parent):
-        type_comment = getattr(node, "type_comment", None)
-        if not type_comment:
-            return None
-
-        try:
-            type_comment_ast = _parse(type_comment)
-        except SyntaxError:
-            # Invalid type comment, just skip it.
-            return None
-
-        type_object = self.visit(type_comment_ast.body[0], parent=parent)
-        if not isinstance(type_object, nodes.Expr):
-            return None
-
-        return type_object.value
-
-    def check_function_type_comment(self, node):
-        type_comment = getattr(node, "type_comment", None)
-        if not type_comment:
-            return None
-
-        try:
-            type_comment_ast = parse_function_type_comment(type_comment)
-        except SyntaxError:
-            # Invalid type comment, just skip it.
-            return None
-
-        returns = None
-        argtypes = [
-            self.visit(elem, node) for elem in (type_comment_ast.argtypes or [])
-        ]
-        if type_comment_ast.returns:
-            returns = self.visit(type_comment_ast.returns, node)
-
-        return returns, argtypes
-
-    def visit_assign(self, node, parent):
-        """visit a Assign node by returning a fresh instance of it"""
-        newnode = nodes.Assign(node.lineno, node.col_offset, parent)
-        type_annotation = self.check_type_comment(node, parent=newnode)
-        newnode.postinit(
-            targets=[self.visit(child, newnode) for child in node.targets],
-            value=self.visit(node.value, newnode),
-            type_annotation=type_annotation,
-        )
-        return newnode
-
-    def visit_assignname(self, node, parent, node_name=None):
-        """visit a node and return a AssignName node"""
-        newnode = nodes.AssignName(
-            node_name,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-        self._save_assignment(newnode)
-        return newnode
-
-    def visit_augassign(self, node, parent):
-        """visit a AugAssign node by returning a fresh instance of it"""
-        newnode = nodes.AugAssign(
-            self._bin_op_classes[type(node.op)] + "=",
-            node.lineno,
-            node.col_offset,
-            parent,
-        )
-        newnode.postinit(
-            self.visit(node.target, newnode), self.visit(node.value, newnode)
-        )
-        return newnode
-
-    def visit_repr(self, node, parent):
-        """visit a Backquote node by returning a fresh instance of it"""
-        newnode = nodes.Repr(node.lineno, node.col_offset, parent)
-        newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    def visit_binop(self, node, parent):
-        """visit a BinOp node by returning a fresh instance of it"""
-        newnode = nodes.BinOp(
-            self._bin_op_classes[type(node.op)], node.lineno, node.col_offset, parent
-        )
-        newnode.postinit(
-            self.visit(node.left, newnode), self.visit(node.right, newnode)
-        )
-        return newnode
-
-    def visit_boolop(self, node, parent):
-        """visit a BoolOp node by returning a fresh instance of it"""
-        newnode = nodes.BoolOp(
-            self._bool_op_classes[type(node.op)], node.lineno, node.col_offset, parent
-        )
-        newnode.postinit([self.visit(child, newnode) for child in node.values])
-        return newnode
-
-    def visit_break(self, node, parent):
-        """visit a Break node by returning a fresh instance of it"""
-        return nodes.Break(
-            getattr(node, "lineno", None), getattr(node, "col_offset", None), parent
-        )
-
-    def visit_call(self, node, parent):
-        """visit a CallFunc node by returning a fresh instance of it"""
-        newnode = nodes.Call(node.lineno, node.col_offset, parent)
-        starargs = _visit_or_none(node, "starargs", self, newnode)
-        kwargs = _visit_or_none(node, "kwargs", self, newnode)
-        args = [self.visit(child, newnode) for child in node.args]
-
-        if node.keywords:
-            keywords = [self.visit(child, newnode) for child in node.keywords]
-        else:
-            keywords = None
-        if starargs:
-            new_starargs = nodes.Starred(
-                col_offset=starargs.col_offset,
-                lineno=starargs.lineno,
-                parent=starargs.parent,
-            )
-            new_starargs.postinit(value=starargs)
-            args.append(new_starargs)
-        if kwargs:
-            new_kwargs = nodes.Keyword(
-                arg=None,
-                col_offset=kwargs.col_offset,
-                lineno=kwargs.lineno,
-                parent=kwargs.parent,
-            )
-            new_kwargs.postinit(value=kwargs)
-            if keywords:
-                keywords.append(new_kwargs)
-            else:
-                keywords = [new_kwargs]
-
-        newnode.postinit(self.visit(node.func, newnode), args, keywords)
-        return newnode
-
-    def visit_classdef(self, node, parent, newstyle=None):
-        """visit a ClassDef node to become astroid"""
-        node, doc = self._get_doc(node)
-        newnode = nodes.ClassDef(node.name, doc, node.lineno, node.col_offset, parent)
-        metaclass = None
-        for keyword in node.keywords:
-            if keyword.arg == "metaclass":
-                metaclass = self.visit(keyword, newnode).value
-                break
-        if node.decorator_list:
-            decorators = self.visit_decorators(node, newnode)
-        else:
-            decorators = None
-        newnode.postinit(
-            [self.visit(child, newnode) for child in node.bases],
-            [self.visit(child, newnode) for child in node.body],
-            decorators,
-            newstyle,
-            metaclass,
-            [
-                self.visit(kwd, newnode)
-                for kwd in node.keywords
-                if kwd.arg != "metaclass"
-            ],
-        )
-        return newnode
-
-    def visit_const(self, node, parent):
-        """visit a Const node by returning a fresh instance of it"""
-        return nodes.Const(
-            node.value,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-
-    def visit_continue(self, node, parent):
-        """visit a Continue node by returning a fresh instance of it"""
-        return nodes.Continue(
-            getattr(node, "lineno", None), getattr(node, "col_offset", None), parent
-        )
-
-    def visit_compare(self, node, parent):
-        """visit a Compare node by returning a fresh instance of it"""
-        newnode = nodes.Compare(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.left, newnode),
-            [
-                (self._cmp_op_classes[op.__class__], self.visit(expr, newnode))
-                for (op, expr) in zip(node.ops, node.comparators)
-            ],
-        )
-        return newnode
-
-    def visit_comprehension(self, node, parent):
-        """visit a Comprehension node by returning a fresh instance of it"""
-        newnode = nodes.Comprehension(parent)
-        newnode.postinit(
-            self.visit(node.target, newnode),
-            self.visit(node.iter, newnode),
-            [self.visit(child, newnode) for child in node.ifs],
-            getattr(node, "is_async", None),
-        )
-        return newnode
-
-    def visit_decorators(self, node, parent):
-        """visit a Decorators node by returning a fresh instance of it"""
-        # /!\ node is actually a _ast.FunctionDef node while
-        # parent is an astroid.nodes.FunctionDef node
-        if PY38:
-            # Set the line number of the first decorator for Python 3.8+.
-            lineno = node.decorator_list[0].lineno
-        else:
-            lineno = node.lineno
-        newnode = nodes.Decorators(lineno, node.col_offset, parent)
-        newnode.postinit([self.visit(child, newnode) for child in node.decorator_list])
-        return newnode
-
-    def visit_delete(self, node, parent):
-        """visit a Delete node by returning a fresh instance of it"""
-        newnode = nodes.Delete(node.lineno, node.col_offset, parent)
-        newnode.postinit([self.visit(child, newnode) for child in node.targets])
-        return newnode
-
-    def _visit_dict_items(self, node, parent, newnode):
-        for key, value in zip(node.keys, node.values):
-            rebuilt_value = self.visit(value, newnode)
-            if not key:
-                # Python 3.5 and extended unpacking
-                rebuilt_key = nodes.DictUnpack(
-                    rebuilt_value.lineno, rebuilt_value.col_offset, parent
-                )
-            else:
-                rebuilt_key = self.visit(key, newnode)
-            yield rebuilt_key, rebuilt_value
-
-    def visit_dict(self, node, parent):
-        """visit a Dict node by returning a fresh instance of it"""
-        newnode = nodes.Dict(node.lineno, node.col_offset, parent)
-        items = list(self._visit_dict_items(node, parent, newnode))
-        newnode.postinit(items)
-        return newnode
-
-    def visit_dictcomp(self, node, parent):
-        """visit a DictComp node by returning a fresh instance of it"""
-        newnode = nodes.DictComp(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.key, newnode),
-            self.visit(node.value, newnode),
-            [self.visit(child, newnode) for child in node.generators],
-        )
-        return newnode
-
-    def visit_expr(self, node, parent):
-        """visit a Expr node by returning a fresh instance of it"""
-        newnode = nodes.Expr(node.lineno, node.col_offset, parent)
-        newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    # Not used in Python 3.8+.
-    def visit_ellipsis(self, node, parent):
-        """visit an Ellipsis node by returning a fresh instance of it"""
-        return nodes.Ellipsis(
-            getattr(node, "lineno", None), getattr(node, "col_offset", None), parent
-        )
-
-    def visit_emptynode(self, node, parent):
-        """visit an EmptyNode node by returning a fresh instance of it"""
-        return nodes.EmptyNode(
-            getattr(node, "lineno", None), getattr(node, "col_offset", None), parent
-        )
-
-    def visit_excepthandler(self, node, parent):
-        """visit an ExceptHandler node by returning a fresh instance of it"""
-        newnode = nodes.ExceptHandler(node.lineno, node.col_offset, parent)
-        # /!\ node.name can be a tuple
-        newnode.postinit(
-            _visit_or_none(node, "type", self, newnode),
-            _visit_or_none(node, "name", self, newnode),
-            [self.visit(child, newnode) for child in node.body],
-        )
-        return newnode
-
-    def visit_exec(self, node, parent):
-        """visit an Exec node by returning a fresh instance of it"""
-        newnode = nodes.Exec(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.body, newnode),
-            _visit_or_none(node, "globals", self, newnode),
-            _visit_or_none(node, "locals", self, newnode),
-        )
-        return newnode
-
-    # Not used in Python 3.8+.
-    def visit_extslice(self, node, parent):
-        """visit an ExtSlice node by returning a fresh instance of it"""
-        newnode = nodes.ExtSlice(parent=parent)
-        newnode.postinit([self.visit(dim, newnode) for dim in node.dims])
-        return newnode
-
-    def _visit_for(self, cls, node, parent):
-        """visit a For node by returning a fresh instance of it"""
-        newnode = cls(node.lineno, node.col_offset, parent)
-        type_annotation = self.check_type_comment(node, parent=newnode)
-        newnode.postinit(
-            target=self.visit(node.target, newnode),
-            iter=self.visit(node.iter, newnode),
-            body=[self.visit(child, newnode) for child in node.body],
-            orelse=[self.visit(child, newnode) for child in node.orelse],
-            type_annotation=type_annotation,
-        )
-        return newnode
-
-    def visit_for(self, node, parent):
-        return self._visit_for(nodes.For, node, parent)
-
-    def visit_importfrom(self, node, parent):
-        """visit an ImportFrom node by returning a fresh instance of it"""
-        names = [(alias.name, alias.asname) for alias in node.names]
-        newnode = nodes.ImportFrom(
-            node.module or "",
-            names,
-            node.level or None,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-        # store From names to add them to locals after building
-        self._import_from_nodes.append(newnode)
-        return newnode
-
-    def _visit_functiondef(self, cls, node, parent):
-        """visit an FunctionDef node to become astroid"""
-        self._global_names.append({})
-        node, doc = self._get_doc(node)
-
-        lineno = node.lineno
-        if PY38 and node.decorator_list:
-            # Python 3.8 sets the line number of a decorated function
-            # to be the actual line number of the function, but the
-            # previous versions expected the decorator's line number instead.
-            # We reset the function's line number to that of the
-            # first decorator to maintain backward compatibility.
-            # It's not ideal but this discrepancy was baked into
-            # the framework for *years*.
-            lineno = node.decorator_list[0].lineno
-
-        newnode = cls(node.name, doc, lineno, node.col_offset, parent)
-        if node.decorator_list:
-            decorators = self.visit_decorators(node, newnode)
-        else:
-            decorators = None
-        if node.returns:
-            returns = self.visit(node.returns, newnode)
-        else:
-            returns = None
-
-        type_comment_args = type_comment_returns = None
-        type_comment_annotation = self.check_function_type_comment(node)
-        if type_comment_annotation:
-            type_comment_returns, type_comment_args = type_comment_annotation
-        newnode.postinit(
-            args=self.visit(node.args, newnode),
-            body=[self.visit(child, newnode) for child in node.body],
-            decorators=decorators,
-            returns=returns,
-            type_comment_returns=type_comment_returns,
-            type_comment_args=type_comment_args,
-        )
-        self._global_names.pop()
-        return newnode
-
-    def visit_functiondef(self, node, parent):
-        return self._visit_functiondef(nodes.FunctionDef, node, parent)
-
-    def visit_generatorexp(self, node, parent):
-        """visit a GeneratorExp node by returning a fresh instance of it"""
-        newnode = nodes.GeneratorExp(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.elt, newnode),
-            [self.visit(child, newnode) for child in node.generators],
-        )
-        return newnode
-
-    def visit_attribute(self, node, parent):
-        """visit an Attribute node by returning a fresh instance of it"""
-        context = self._get_context(node)
-        if context == astroid.Del:
-            # FIXME : maybe we should reintroduce and visit_delattr ?
-            # for instance, deactivating assign_ctx
-            newnode = nodes.DelAttr(node.attr, node.lineno, node.col_offset, parent)
-        elif context == astroid.Store:
-            newnode = nodes.AssignAttr(node.attr, node.lineno, node.col_offset, parent)
-            # Prohibit a local save if we are in an ExceptHandler.
-            if not isinstance(parent, astroid.ExceptHandler):
-                self._delayed_assattr.append(newnode)
-        else:
-            newnode = nodes.Attribute(node.attr, node.lineno, node.col_offset, parent)
-        newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    def visit_global(self, node, parent):
-        """visit a Global node to become astroid"""
-        newnode = nodes.Global(
-            node.names,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-        if self._global_names:  # global at the module level, no effect
-            for name in node.names:
-                self._global_names[-1].setdefault(name, []).append(newnode)
-        return newnode
-
-    def visit_if(self, node, parent):
-        """visit an If node by returning a fresh instance of it"""
-        newnode = nodes.If(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.test, newnode),
-            [self.visit(child, newnode) for child in node.body],
-            [self.visit(child, newnode) for child in node.orelse],
-        )
-        return newnode
-
-    def visit_ifexp(self, node, parent):
-        """visit a IfExp node by returning a fresh instance of it"""
-        newnode = nodes.IfExp(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.test, newnode),
-            self.visit(node.body, newnode),
-            self.visit(node.orelse, newnode),
-        )
-        return newnode
-
-    def visit_import(self, node, parent):
-        """visit a Import node by returning a fresh instance of it"""
-        names = [(alias.name, alias.asname) for alias in node.names]
-        newnode = nodes.Import(
-            names,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-        # save import names in parent's locals:
-        for (name, asname) in newnode.names:
-            name = asname or name
-            parent.set_local(name.split(".")[0], newnode)
-        return newnode
-
-    # Not used in Python 3.8+.
-    def visit_index(self, node, parent):
-        """visit a Index node by returning a fresh instance of it"""
-        newnode = nodes.Index(parent=parent)
-        newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    def visit_keyword(self, node, parent):
-        """visit a Keyword node by returning a fresh instance of it"""
-        newnode = nodes.Keyword(node.arg, parent=parent)
-        newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    def visit_lambda(self, node, parent):
-        """visit a Lambda node by returning a fresh instance of it"""
-        newnode = nodes.Lambda(node.lineno, node.col_offset, parent)
-        newnode.postinit(self.visit(node.args, newnode), self.visit(node.body, newnode))
-        return newnode
-
-    def visit_list(self, node, parent):
-        """visit a List node by returning a fresh instance of it"""
-        context = self._get_context(node)
-        newnode = nodes.List(
-            ctx=context, lineno=node.lineno, col_offset=node.col_offset, parent=parent
-        )
-        newnode.postinit([self.visit(child, newnode) for child in node.elts])
-        return newnode
-
-    def visit_listcomp(self, node, parent):
-        """visit a ListComp node by returning a fresh instance of it"""
-        newnode = nodes.ListComp(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.elt, newnode),
-            [self.visit(child, newnode) for child in node.generators],
-        )
-        return newnode
-
-    def visit_name(self, node, parent):
-        """visit a Name node by returning a fresh instance of it"""
-        context = self._get_context(node)
-        # True and False can be assigned to something in py2x, so we have to
-        # check first the context.
-        if context == astroid.Del:
-            newnode = nodes.DelName(node.id, node.lineno, node.col_offset, parent)
-        elif context == astroid.Store:
-            newnode = nodes.AssignName(node.id, node.lineno, node.col_offset, parent)
-        elif node.id in CONST_NAME_TRANSFORMS:
-            newnode = nodes.Const(
-                CONST_NAME_TRANSFORMS[node.id],
-                getattr(node, "lineno", None),
-                getattr(node, "col_offset", None),
-                parent,
-            )
-            return newnode
-        else:
-            newnode = nodes.Name(node.id, node.lineno, node.col_offset, parent)
-        # XXX REMOVE me :
-        if context in (astroid.Del, astroid.Store):  # 'Aug' ??
-            self._save_assignment(newnode)
-        return newnode
-
-    def visit_constant(self, node, parent):
-        """visit a Constant node by returning a fresh instance of Const"""
-        return nodes.Const(
-            node.value,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-
-    # Not used in Python 3.8+.
-    def visit_str(self, node, parent):
-        """visit a String/Bytes node by returning a fresh instance of Const"""
-        return nodes.Const(
-            node.s,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-
-    visit_bytes = visit_str
-
-    # Not used in Python 3.8+.
-    def visit_num(self, node, parent):
-        """visit a Num node by returning a fresh instance of Const"""
-        return nodes.Const(
-            node.n,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-
-    def visit_pass(self, node, parent):
-        """visit a Pass node by returning a fresh instance of it"""
-        return nodes.Pass(node.lineno, node.col_offset, parent)
-
-    def visit_print(self, node, parent):
-        """visit a Print node by returning a fresh instance of it"""
-        newnode = nodes.Print(node.nl, node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            _visit_or_none(node, "dest", self, newnode),
-            [self.visit(child, newnode) for child in node.values],
-        )
-        return newnode
-
-    def visit_raise(self, node, parent):
-        """visit a Raise node by returning a fresh instance of it"""
-        newnode = nodes.Raise(node.lineno, node.col_offset, parent)
-        # pylint: disable=too-many-function-args
-        newnode.postinit(
-            _visit_or_none(node, "type", self, newnode),
-            _visit_or_none(node, "inst", self, newnode),
-            _visit_or_none(node, "tback", self, newnode),
-        )
-        return newnode
-
-    def visit_return(self, node, parent):
-        """visit a Return node by returning a fresh instance of it"""
-        newnode = nodes.Return(node.lineno, node.col_offset, parent)
-        if node.value is not None:
-            newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    def visit_set(self, node, parent):
-        """visit a Set node by returning a fresh instance of it"""
-        newnode = nodes.Set(node.lineno, node.col_offset, parent)
-        newnode.postinit([self.visit(child, newnode) for child in node.elts])
-        return newnode
-
-    def visit_setcomp(self, node, parent):
-        """visit a SetComp node by returning a fresh instance of it"""
-        newnode = nodes.SetComp(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.elt, newnode),
-            [self.visit(child, newnode) for child in node.generators],
-        )
-        return newnode
-
-    def visit_slice(self, node, parent):
-        """visit a Slice node by returning a fresh instance of it"""
-        newnode = nodes.Slice(parent=parent)
-        newnode.postinit(
-            _visit_or_none(node, "lower", self, newnode),
-            _visit_or_none(node, "upper", self, newnode),
-            _visit_or_none(node, "step", self, newnode),
-        )
-        return newnode
-
-    def visit_subscript(self, node, parent):
-        """visit a Subscript node by returning a fresh instance of it"""
-        context = self._get_context(node)
-        newnode = nodes.Subscript(
-            ctx=context, lineno=node.lineno, col_offset=node.col_offset, parent=parent
-        )
-        newnode.postinit(
-            self.visit(node.value, newnode), self.visit(node.slice, newnode)
-        )
-        return newnode
-
-    def visit_tryexcept(self, node, parent):
-        """visit a TryExcept node by returning a fresh instance of it"""
-        newnode = nodes.TryExcept(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            [self.visit(child, newnode) for child in node.body],
-            [self.visit(child, newnode) for child in node.handlers],
-            [self.visit(child, newnode) for child in node.orelse],
-        )
-        return newnode
-
-    def visit_tryfinally(self, node, parent):
-        """visit a TryFinally node by returning a fresh instance of it"""
-        newnode = nodes.TryFinally(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            [self.visit(child, newnode) for child in node.body],
-            [self.visit(n, newnode) for n in node.finalbody],
-        )
-        return newnode
-
-    def visit_tuple(self, node, parent):
-        """visit a Tuple node by returning a fresh instance of it"""
-        context = self._get_context(node)
-        newnode = nodes.Tuple(
-            ctx=context, lineno=node.lineno, col_offset=node.col_offset, parent=parent
-        )
-        newnode.postinit([self.visit(child, newnode) for child in node.elts])
-        return newnode
-
-    def visit_unaryop(self, node, parent):
-        """visit a UnaryOp node by returning a fresh instance of it"""
-        newnode = nodes.UnaryOp(
-            self._unary_op_classes[node.op.__class__],
-            node.lineno,
-            node.col_offset,
-            parent,
-        )
-        newnode.postinit(self.visit(node.operand, newnode))
-        return newnode
-
-    def visit_while(self, node, parent):
-        """visit a While node by returning a fresh instance of it"""
-        newnode = nodes.While(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.test, newnode),
-            [self.visit(child, newnode) for child in node.body],
-            [self.visit(child, newnode) for child in node.orelse],
-        )
-        return newnode
-
-    def visit_with(self, node, parent):
-        newnode = nodes.With(node.lineno, node.col_offset, parent)
-        expr = self.visit(node.context_expr, newnode)
-        if node.optional_vars is not None:
-            optional_vars = self.visit(node.optional_vars, newnode)
-        else:
-            optional_vars = None
-
-        type_annotation = self.check_type_comment(node, parent=newnode)
-        newnode.postinit(
-            items=[(expr, optional_vars)],
-            body=[self.visit(child, newnode) for child in node.body],
-            type_annotation=type_annotation,
-        )
-        return newnode
-
-    def visit_yield(self, node, parent):
-        """visit a Yield node by returning a fresh instance of it"""
-        newnode = nodes.Yield(node.lineno, node.col_offset, parent)
-        if node.value is not None:
-            newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-
-class TreeRebuilder3(TreeRebuilder):
-    """extend and overwrite TreeRebuilder for python3k"""
-
-    def visit_arg(self, node, parent):
-        """visit an arg node by returning a fresh AssName instance"""
-        return self.visit_assignname(node, parent, node.arg)
-
-    # Not used in Python 3.8+.
-    def visit_nameconstant(self, node, parent):
-        # in Python 3.4 we have NameConstant for True / False / None
-        return nodes.Const(
-            node.value,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-
-    def visit_excepthandler(self, node, parent):
-        """visit an ExceptHandler node by returning a fresh instance of it"""
-        newnode = nodes.ExceptHandler(node.lineno, node.col_offset, parent)
-        if node.name:
-            name = self.visit_assignname(node, newnode, node.name)
-        else:
-            name = None
-        newnode.postinit(
-            _visit_or_none(node, "type", self, newnode),
-            name,
-            [self.visit(child, newnode) for child in node.body],
-        )
-        return newnode
-
-    def visit_nonlocal(self, node, parent):
-        """visit a Nonlocal node and return a new instance of it"""
-        return nodes.Nonlocal(
-            node.names,
-            getattr(node, "lineno", None),
-            getattr(node, "col_offset", None),
-            parent,
-        )
-
-    def visit_raise(self, node, parent):
-        """visit a Raise node by returning a fresh instance of it"""
-        newnode = nodes.Raise(node.lineno, node.col_offset, parent)
-        # no traceback; anyway it is not used in Pylint
-        newnode.postinit(
-            _visit_or_none(node, "exc", self, newnode),
-            _visit_or_none(node, "cause", self, newnode),
-        )
-        return newnode
-
-    def visit_starred(self, node, parent):
-        """visit a Starred node and return a new instance of it"""
-        context = self._get_context(node)
-        newnode = nodes.Starred(
-            ctx=context, lineno=node.lineno, col_offset=node.col_offset, parent=parent
-        )
-        newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    def visit_try(self, node, parent):
-        # python 3.3 introduce a new Try node replacing
-        # TryFinally/TryExcept nodes
-        if node.finalbody:
-            newnode = nodes.TryFinally(node.lineno, node.col_offset, parent)
-            if node.handlers:
-                body = [self.visit_tryexcept(node, newnode)]
-            else:
-                body = [self.visit(child, newnode) for child in node.body]
-            newnode.postinit(body, [self.visit(n, newnode) for n in node.finalbody])
-            return newnode
-        if node.handlers:
-            return self.visit_tryexcept(node, parent)
-        return None
-
-    def visit_annassign(self, node, parent):
-        """visit an AnnAssign node by returning a fresh instance of it"""
-        newnode = nodes.AnnAssign(node.lineno, node.col_offset, parent)
-        annotation = _visit_or_none(node, "annotation", self, newnode)
-        newnode.postinit(
-            target=self.visit(node.target, newnode),
-            annotation=annotation,
-            simple=node.simple,
-            value=_visit_or_none(node, "value", self, newnode),
-        )
-        return newnode
-
-    def _visit_with(self, cls, node, parent):
-        if "items" not in node._fields:
-            # python < 3.3
-            return super(TreeRebuilder3, self).visit_with(node, parent)
-
-        newnode = cls(node.lineno, node.col_offset, parent)
-
-        def visit_child(child):
-            expr = self.visit(child.context_expr, newnode)
-            var = _visit_or_none(child, "optional_vars", self, newnode)
-            return expr, var
-
-        type_annotation = self.check_type_comment(node, parent=newnode)
-        newnode.postinit(
-            items=[visit_child(child) for child in node.items],
-            body=[self.visit(child, newnode) for child in node.body],
-            type_annotation=type_annotation,
-        )
-        return newnode
-
-    def visit_with(self, node, parent):
-        return self._visit_with(nodes.With, node, parent)
-
-    def visit_yieldfrom(self, node, parent):
-        newnode = nodes.YieldFrom(node.lineno, node.col_offset, parent)
-        if node.value is not None:
-            newnode.postinit(self.visit(node.value, newnode))
-        return newnode
-
-    def visit_classdef(self, node, parent, newstyle=True):
-        return super(TreeRebuilder3, self).visit_classdef(
-            node, parent, newstyle=newstyle
-        )
-
-    # Async structs added in Python 3.5
-    def visit_asyncfunctiondef(self, node, parent):
-        return self._visit_functiondef(nodes.AsyncFunctionDef, node, parent)
-
-    def visit_asyncfor(self, node, parent):
-        return self._visit_for(nodes.AsyncFor, node, parent)
-
-    def visit_await(self, node, parent):
-        newnode = nodes.Await(node.lineno, node.col_offset, parent)
-        newnode.postinit(value=self.visit(node.value, newnode))
-        return newnode
-
-    def visit_asyncwith(self, node, parent):
-        return self._visit_with(nodes.AsyncWith, node, parent)
-
-    def visit_joinedstr(self, node, parent):
-        newnode = nodes.JoinedStr(node.lineno, node.col_offset, parent)
-        newnode.postinit([self.visit(child, newnode) for child in node.values])
-        return newnode
-
-    def visit_formattedvalue(self, node, parent):
-        newnode = nodes.FormattedValue(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.value, newnode),
-            node.conversion,
-            _visit_or_none(node, "format_spec", self, newnode),
-        )
-        return newnode
-
-    def visit_namedexpr(self, node, parent):
-        newnode = nodes.NamedExpr(node.lineno, node.col_offset, parent)
-        newnode.postinit(
-            self.visit(node.target, newnode), self.visit(node.value, newnode)
-        )
-        return newnode
-
-
-TreeRebuilder = TreeRebuilder3
diff --git a/venv/Lib/site-packages/astroid/scoped_nodes.py b/venv/Lib/site-packages/astroid/scoped_nodes.py
deleted file mode 100644
index d02b653..0000000
--- a/venv/Lib/site-packages/astroid/scoped_nodes.py
+++ /dev/null
@@ -1,2836 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2011, 2013-2015 Google, Inc.
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2013 Phil Schaf <flying-sheep@web.de>
-# Copyright (c) 2014 Eevee (Alex Munroe) <amunroe@yelp.com>
-# Copyright (c) 2015-2016 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2015 Rene Zhang <rz99@cornell.edu>
-# Copyright (c) 2015 Philip Lorenz <philip@bithub.de>
-# Copyright (c) 2016-2017 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017-2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2017-2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 David Euresti <david@dropbox.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 HoverHell <hoverhell@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-"""
-This module contains the classes for "scoped" node, i.e. which are opening a
-new local scope in the language definition : Module, ClassDef, FunctionDef (and
-Lambda, GeneratorExp, DictComp and SetComp to some extent).
-"""
-
-import builtins
-import sys
-import io
-import itertools
-from typing import Optional, List
-
-from astroid import bases
-from astroid import context as contextmod
-from astroid import exceptions
-from astroid import decorators as decorators_mod
-from astroid.interpreter import objectmodel
-from astroid.interpreter import dunder_lookup
-from astroid import manager
-from astroid import mixins
-from astroid import node_classes
-from astroid import util
-
-
-BUILTINS = builtins.__name__
-ITER_METHODS = ("__iter__", "__getitem__")
-EXCEPTION_BASE_CLASSES = frozenset({"Exception", "BaseException"})
-objects = util.lazy_import("objects")
-
-
-def _c3_merge(sequences, cls, context):
-    """Merges MROs in *sequences* to a single MRO using the C3 algorithm.
-
-    Adapted from http://www.python.org/download/releases/2.3/mro/.
-
-    """
-    result = []
-    while True:
-        sequences = [s for s in sequences if s]  # purge empty sequences
-        if not sequences:
-            return result
-        for s1 in sequences:  # find merge candidates among seq heads
-            candidate = s1[0]
-            for s2 in sequences:
-                if candidate in s2[1:]:
-                    candidate = None
-                    break  # reject the current head, it appears later
-            else:
-                break
-        if not candidate:
-            # Show all the remaining bases, which were considered as
-            # candidates for the next mro sequence.
-            raise exceptions.InconsistentMroError(
-                message="Cannot create a consistent method resolution order "
-                "for MROs {mros} of class {cls!r}.",
-                mros=sequences,
-                cls=cls,
-                context=context,
-            )
-
-        result.append(candidate)
-        # remove the chosen candidate
-        for seq in sequences:
-            if seq[0] == candidate:
-                del seq[0]
-    return None
-
-
-def clean_duplicates_mro(sequences, cls, context):
-    for sequence in sequences:
-        names = [
-            (node.lineno, node.qname()) if node.name else None for node in sequence
-        ]
-        last_index = dict(map(reversed, enumerate(names)))
-        if names and names[0] is not None and last_index[names[0]] != 0:
-            raise exceptions.DuplicateBasesError(
-                message="Duplicates found in MROs {mros} for {cls!r}.",
-                mros=sequences,
-                cls=cls,
-                context=context,
-            )
-        yield [
-            node
-            for i, (node, name) in enumerate(zip(sequence, names))
-            if name is None or last_index[name] == i
-        ]
-
-
-def function_to_method(n, klass):
-    if isinstance(n, FunctionDef):
-        if n.type == "classmethod":
-            return bases.BoundMethod(n, klass)
-        if n.type != "staticmethod":
-            return bases.UnboundMethod(n)
-    return n
-
-
-MANAGER = manager.AstroidManager()
-
-
-def builtin_lookup(name):
-    """lookup a name into the builtin module
-    return the list of matching statements and the astroid for the builtin
-    module
-    """
-    builtin_astroid = MANAGER.ast_from_module(builtins)
-    if name == "__dict__":
-        return builtin_astroid, ()
-    try:
-        stmts = builtin_astroid.locals[name]
-    except KeyError:
-        stmts = ()
-    return builtin_astroid, stmts
-
-
-# TODO move this Mixin to mixins.py; problem: 'FunctionDef' in _scope_lookup
-class LocalsDictNodeNG(node_classes.LookupMixIn, node_classes.NodeNG):
-    """ this class provides locals handling common to Module, FunctionDef
-    and ClassDef nodes, including a dict like interface for direct access
-    to locals information
-    """
-
-    # attributes below are set by the builder module or by raw factories
-
-    locals = {}
-    """A map of the name of a local variable to the node defining the local.
-
-    :type: dict(str, NodeNG)
-    """
-
-    def qname(self):
-        """Get the 'qualified' name of the node.
-
-        For example: module.name, module.class.name ...
-
-        :returns: The qualified name.
-        :rtype: str
-        """
-        # pylint: disable=no-member; github.com/pycqa/astroid/issues/278
-        if self.parent is None:
-            return self.name
-        return "%s.%s" % (self.parent.frame().qname(), self.name)
-
-    def frame(self):
-        """The first parent frame node.
-
-        A frame node is a :class:`Module`, :class:`FunctionDef`,
-        or :class:`ClassDef`.
-
-        :returns: The first parent frame node.
-        :rtype: Module or FunctionDef or ClassDef
-        """
-        return self
-
-    def scope(self):
-        """The first parent node defining a new scope.
-
-        :returns: The first parent scope node.
-        :rtype: Module or FunctionDef or ClassDef or Lambda or GenExpr
-        """
-        return self
-
-    def _scope_lookup(self, node, name, offset=0):
-        """XXX method for interfacing the scope lookup"""
-        try:
-            stmts = node._filter_stmts(self.locals[name], self, offset)
-        except KeyError:
-            stmts = ()
-        if stmts:
-            return self, stmts
-        if self.parent:  # i.e. not Module
-            # nested scope: if parent scope is a function, that's fine
-            # else jump to the module
-            pscope = self.parent.scope()
-            if not pscope.is_function:
-                pscope = pscope.root()
-            return pscope.scope_lookup(node, name)
-        return builtin_lookup(name)  # Module
-
-    def set_local(self, name, stmt):
-        """Define that the given name is declared in the given statement node.
-
-        .. seealso:: :meth:`scope`
-
-        :param name: The name that is being defined.
-        :type name: str
-
-        :param stmt: The statement that defines the given name.
-        :type stmt: NodeNG
-        """
-        # assert not stmt in self.locals.get(name, ()), (self, stmt)
-        self.locals.setdefault(name, []).append(stmt)
-
-    __setitem__ = set_local
-
-    def _append_node(self, child):
-        """append a child, linking it in the tree"""
-        # pylint: disable=no-member; depending by the class
-        # which uses the current class as a mixin or base class.
-        # It's rewritten in 2.0, so it makes no sense for now
-        # to spend development time on it.
-        self.body.append(child)
-        child.parent = self
-
-    def add_local_node(self, child_node, name=None):
-        """Append a child that should alter the locals of this scope node.
-
-        :param child_node: The child node that will alter locals.
-        :type child_node: NodeNG
-
-        :param name: The name of the local that will be altered by
-            the given child node.
-        :type name: str or None
-        """
-        if name != "__class__":
-            # add __class__ node as a child will cause infinite recursion later!
-            self._append_node(child_node)
-        self.set_local(name or child_node.name, child_node)
-
-    def __getitem__(self, item):
-        """The first node the defines the given local.
-
-        :param item: The name of the locally defined object.
-        :type item: str
-
-        :raises KeyError: If the name is not defined.
-        """
-        return self.locals[item][0]
-
-    def __iter__(self):
-        """Iterate over the names of locals defined in this scoped node.
-
-        :returns: The names of the defined locals.
-        :rtype: iterable(str)
-        """
-        return iter(self.keys())
-
-    def keys(self):
-        """The names of locals defined in this scoped node.
-
-        :returns: The names of the defined locals.
-        :rtype: list(str)
-        """
-        return list(self.locals.keys())
-
-    def values(self):
-        """The nodes that define the locals in this scoped node.
-
-        :returns: The nodes that define locals.
-        :rtype: list(NodeNG)
-        """
-        return [self[key] for key in self.keys()]
-
-    def items(self):
-        """Get the names of the locals and the node that defines the local.
-
-        :returns: The names of locals and their associated node.
-        :rtype: list(tuple(str, NodeNG))
-        """
-        return list(zip(self.keys(), self.values()))
-
-    def __contains__(self, name):
-        """Check if a local is defined in this scope.
-
-        :param name: The name of the local to check for.
-        :type name: str
-
-        :returns: True if this node has a local of the given name,
-            False otherwise.
-        :rtype: bool
-        """
-        return name in self.locals
-
-
-class Module(LocalsDictNodeNG):
-    """Class representing an :class:`ast.Module` node.
-
-    >>> node = astroid.extract_node('import astroid')
-    >>> node
-    <Import l.1 at 0x7f23b2e4e5c0>
-    >>> node.parent
-    <Module l.0 at 0x7f23b2e4eda0>
-    """
-
-    _astroid_fields = ("body",)
-
-    fromlineno = 0
-    """The first line that this node appears on in the source code.
-
-    :type: int or None
-    """
-    lineno = 0
-    """The line that this node appears on in the source code.
-
-    :type: int or None
-    """
-
-    # attributes below are set by the builder module or by raw factories
-
-    file = None
-    """The path to the file that this ast has been extracted from.
-
-    This will be ``None`` when the representation has been built from a
-    built-in module.
-
-    :type: str or None
-    """
-    file_bytes = None
-    """The string/bytes that this ast was built from.
-
-    :type: str or bytes or None
-    """
-    file_encoding = None
-    """The encoding of the source file.
-
-    This is used to get unicode out of a source file.
-    Python 2 only.
-
-    :type: str or None
-    """
-    name = None
-    """The name of the module.
-
-    :type: str or None
-    """
-    pure_python = None
-    """Whether the ast was built from source.
-
-    :type: bool or None
-    """
-    package = None
-    """Whether the node represents a package or a module.
-
-    :type: bool or None
-    """
-    globals = None
-    """A map of the name of a global variable to the node defining the global.
-
-    :type: dict(str, NodeNG)
-    """
-
-    # Future imports
-    future_imports = None
-    """The imports from ``__future__``.
-
-    :type: set(str) or None
-    """
-    special_attributes = objectmodel.ModuleModel()
-    """The names of special attributes that this module has.
-
-    :type: objectmodel.ModuleModel
-    """
-
-    # names of module attributes available through the global scope
-    scope_attrs = {"__name__", "__doc__", "__file__", "__path__", "__package__"}
-    """The names of module attributes available through the global scope.
-
-    :type: str(str)
-    """
-
-    _other_fields = (
-        "name",
-        "doc",
-        "file",
-        "path",
-        "package",
-        "pure_python",
-        "future_imports",
-    )
-    _other_other_fields = ("locals", "globals")
-
-    def __init__(
-        self,
-        name,
-        doc,
-        file=None,
-        path: Optional[List[str]] = None,
-        package=None,
-        parent=None,
-        pure_python=True,
-    ):
-        """
-        :param name: The name of the module.
-        :type name: str
-
-        :param doc: The module docstring.
-        :type doc: str
-
-        :param file: The path to the file that this ast has been extracted from.
-        :type file: str or None
-
-        :param path:
-        :type path: Optional[List[str]]
-
-        :param package: Whether the node represents a package or a module.
-        :type package: bool or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-
-        :param pure_python: Whether the ast was built from source.
-        :type pure_python: bool or None
-        """
-        self.name = name
-        self.doc = doc
-        self.file = file
-        self.path = path
-        self.package = package
-        self.parent = parent
-        self.pure_python = pure_python
-        self.locals = self.globals = {}
-        """A map of the name of a local variable to the node defining the local.
-
-        :type: dict(str, NodeNG)
-        """
-        self.body = []
-        """The contents of the module.
-
-        :type: list(NodeNG) or None
-        """
-        self.future_imports = set()
-
-    # pylint: enable=redefined-builtin
-
-    def postinit(self, body=None):
-        """Do some setup after initialisation.
-
-        :param body: The contents of the module.
-        :type body: list(NodeNG) or None
-        """
-        self.body = body
-
-    def _get_stream(self):
-        if self.file_bytes is not None:
-            return io.BytesIO(self.file_bytes)
-        if self.file is not None:
-            stream = open(self.file, "rb")
-            return stream
-        return None
-
-    def stream(self):
-        """Get a stream to the underlying file or bytes.
-
-        :type: file or io.BytesIO or None
-        """
-        return self._get_stream()
-
-    def block_range(self, lineno):
-        """Get a range from where this node starts to where this node ends.
-
-        :param lineno: Unused.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to.
-        :rtype: tuple(int, int)
-        """
-        return self.fromlineno, self.tolineno
-
-    def scope_lookup(self, node, name, offset=0):
-        """Lookup where the given variable is assigned.
-
-        :param node: The node to look for assignments up to.
-            Any assignments after the given node are ignored.
-        :type node: NodeNG
-
-        :param name: The name of the variable to find assignments for.
-        :type name: str
-
-        :param offset: The line offset to filter statements up to.
-        :type offset: int
-
-        :returns: This scope node and the list of assignments associated to the
-            given name according to the scope where it has been found (locals,
-            globals or builtin).
-        :rtype: tuple(str, list(NodeNG))
-        """
-        if name in self.scope_attrs and name not in self.locals:
-            try:
-                return self, self.getattr(name)
-            except exceptions.AttributeInferenceError:
-                return self, ()
-        return self._scope_lookup(node, name, offset)
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        return "%s.module" % BUILTINS
-
-    def display_type(self):
-        """A human readable type of this node.
-
-        :returns: The type of this node.
-        :rtype: str
-        """
-        return "Module"
-
-    def getattr(self, name, context=None, ignore_locals=False):
-        result = []
-        name_in_locals = name in self.locals
-
-        if name in self.special_attributes and not ignore_locals and not name_in_locals:
-            result = [self.special_attributes.lookup(name)]
-        elif not ignore_locals and name_in_locals:
-            result = self.locals[name]
-        elif self.package:
-            try:
-                result = [self.import_module(name, relative_only=True)]
-            except (exceptions.AstroidBuildingError, SyntaxError) as exc:
-                raise exceptions.AttributeInferenceError(
-                    target=self, attribute=name, context=context
-                ) from exc
-        result = [n for n in result if not isinstance(n, node_classes.DelName)]
-        if result:
-            return result
-        raise exceptions.AttributeInferenceError(
-            target=self, attribute=name, context=context
-        )
-
-    def igetattr(self, name, context=None):
-        """Infer the possible values of the given variable.
-
-        :param name: The name of the variable to infer.
-        :type name: str
-
-        :returns: The inferred possible values.
-        :rtype: iterable(NodeNG) or None
-        """
-        # set lookup name since this is necessary to infer on import nodes for
-        # instance
-        context = contextmod.copy_context(context)
-        context.lookupname = name
-        try:
-            return bases._infer_stmts(self.getattr(name, context), context, frame=self)
-        except exceptions.AttributeInferenceError as error:
-            raise exceptions.InferenceError(
-                error.message, target=self, attribute=name, context=context
-            ) from error
-
-    def fully_defined(self):
-        """Check if this module has been build from a .py file.
-
-        If so, the module contains a complete representation,
-        including the code.
-
-        :returns: True if the module has been built from a .py file.
-        :rtype: bool
-        """
-        return self.file is not None and self.file.endswith(".py")
-
-    def statement(self):
-        """The first parent node, including self, marked as statement node.
-
-        :returns: The first parent statement.
-        :rtype: NodeNG
-        """
-        return self
-
-    def previous_sibling(self):
-        """The previous sibling statement.
-
-        :returns: The previous sibling statement node.
-        :rtype: NodeNG or None
-        """
-
-    def next_sibling(self):
-        """The next sibling statement node.
-
-        :returns: The next sibling statement node.
-        :rtype: NodeNG or None
-        """
-
-    _absolute_import_activated = True
-
-    def absolute_import_activated(self):
-        """Whether :pep:`328` absolute import behaviour has been enabled.
-
-        :returns: True if :pep:`328` has been enabled, False otherwise.
-        :rtype: bool
-        """
-        return self._absolute_import_activated
-
-    def import_module(self, modname, relative_only=False, level=None):
-        """Get the ast for a given module as if imported from this module.
-
-        :param modname: The name of the module to "import".
-        :type modname: str
-
-        :param relative_only: Whether to only consider relative imports.
-        :type relative_only: bool
-
-        :param level: The level of relative import.
-        :type level: int or None
-
-        :returns: The imported module ast.
-        :rtype: NodeNG
-        """
-        if relative_only and level is None:
-            level = 0
-        absmodname = self.relative_to_absolute_name(modname, level)
-
-        try:
-            return MANAGER.ast_from_module_name(absmodname)
-        except exceptions.AstroidBuildingError:
-            # we only want to import a sub module or package of this module,
-            # skip here
-            if relative_only:
-                raise
-        return MANAGER.ast_from_module_name(modname)
-
-    def relative_to_absolute_name(self, modname, level):
-        """Get the absolute module name for a relative import.
-
-        The relative import can be implicit or explicit.
-
-        :param modname: The module name to convert.
-        :type modname: str
-
-        :param level: The level of relative import.
-        :type level: int
-
-        :returns: The absolute module name.
-        :rtype: str
-
-        :raises TooManyLevelsError: When the relative import refers to a
-            module too far above this one.
-        """
-        # XXX this returns non sens when called on an absolute import
-        # like 'pylint.checkers.astroid.utils'
-        # XXX doesn't return absolute name if self.name isn't absolute name
-        if self.absolute_import_activated() and level is None:
-            return modname
-        if level:
-            if self.package:
-                level = level - 1
-            if level and self.name.count(".") < level:
-                raise exceptions.TooManyLevelsError(level=level, name=self.name)
-
-            package_name = self.name.rsplit(".", level)[0]
-        elif self.package:
-            package_name = self.name
-        else:
-            package_name = self.name.rsplit(".", 1)[0]
-
-        if package_name:
-            if not modname:
-                return package_name
-            return "%s.%s" % (package_name, modname)
-        return modname
-
-    def wildcard_import_names(self):
-        """The list of imported names when this module is 'wildcard imported'.
-
-        It doesn't include the '__builtins__' name which is added by the
-        current CPython implementation of wildcard imports.
-
-        :returns: The list of imported names.
-        :rtype: list(str)
-        """
-        # We separate the different steps of lookup in try/excepts
-        # to avoid catching too many Exceptions
-        default = [name for name in self.keys() if not name.startswith("_")]
-        try:
-            all_values = self["__all__"]
-        except KeyError:
-            return default
-
-        try:
-            explicit = next(all_values.assigned_stmts())
-        except exceptions.InferenceError:
-            return default
-        except AttributeError:
-            # not an assignment node
-            # XXX infer?
-            return default
-
-        # Try our best to detect the exported name.
-        inferred = []
-        try:
-            explicit = next(explicit.infer())
-        except exceptions.InferenceError:
-            return default
-        if not isinstance(explicit, (node_classes.Tuple, node_classes.List)):
-            return default
-
-        str_const = lambda node: (
-            isinstance(node, node_classes.Const) and isinstance(node.value, str)
-        )
-        for node in explicit.elts:
-            if str_const(node):
-                inferred.append(node.value)
-            else:
-                try:
-                    inferred_node = next(node.infer())
-                except exceptions.InferenceError:
-                    continue
-                if str_const(inferred_node):
-                    inferred.append(inferred_node.value)
-        return inferred
-
-    def public_names(self):
-        """The list of the names that are publicly available in this module.
-
-        :returns: The list of publc names.
-        :rtype: list(str)
-        """
-        return [name for name in self.keys() if not name.startswith("_")]
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`Module` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-    def get_children(self):
-        yield from self.body
-
-
-class ComprehensionScope(LocalsDictNodeNG):
-    """Scoping for different types of comprehensions."""
-
-    def frame(self):
-        """The first parent frame node.
-
-        A frame node is a :class:`Module`, :class:`FunctionDef`,
-        or :class:`ClassDef`.
-
-        :returns: The first parent frame node.
-        :rtype: Module or FunctionDef or ClassDef
-        """
-        return self.parent.frame()
-
-    scope_lookup = LocalsDictNodeNG._scope_lookup
-
-
-class GeneratorExp(ComprehensionScope):
-    """Class representing an :class:`ast.GeneratorExp` node.
-
-    >>> node = astroid.extract_node('(thing for thing in things if thing)')
-    >>> node
-    <GeneratorExp l.1 at 0x7f23b2e4e400>
-    """
-
-    _astroid_fields = ("elt", "generators")
-    _other_other_fields = ("locals",)
-    elt = None
-    """The element that forms the output of the expression.
-
-    :type: NodeNG or None
-    """
-    generators = None
-    """The generators that are looped through.
-
-    :type: list(Comprehension) or None
-    """
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        """
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.locals = {}
-        """A map of the name of a local variable to the node defining the local.
-
-        :type: dict(str, NodeNG)
-        """
-
-        super(GeneratorExp, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, elt=None, generators=None):
-        """Do some setup after initialisation.
-
-        :param elt: The element that forms the output of the expression.
-        :type elt: NodeNG or None
-
-        :param generators: The generators that are looped through.
-        :type generators: list(Comprehension) or None
-        """
-        self.elt = elt
-        if generators is None:
-            self.generators = []
-        else:
-            self.generators = generators
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`GeneratorExp` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-    def get_children(self):
-        yield self.elt
-
-        yield from self.generators
-
-
-class DictComp(ComprehensionScope):
-    """Class representing an :class:`ast.DictComp` node.
-
-    >>> node = astroid.extract_node('{k:v for k, v in things if k > v}')
-    >>> node
-    <DictComp l.1 at 0x7f23b2e41d68>
-    """
-
-    _astroid_fields = ("key", "value", "generators")
-    _other_other_fields = ("locals",)
-    key = None
-    """What produces the keys.
-
-    :type: NodeNG or None
-    """
-    value = None
-    """What produces the values.
-
-    :type: NodeNG or None
-    """
-    generators = None
-    """The generators that are looped through.
-
-    :type: list(Comprehension) or None
-    """
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        """
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.locals = {}
-        """A map of the name of a local variable to the node defining the local.
-
-        :type: dict(str, NodeNG)
-        """
-
-        super(DictComp, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, key=None, value=None, generators=None):
-        """Do some setup after initialisation.
-
-        :param key: What produces the keys.
-        :type key: NodeNG or None
-
-        :param value: What produces the values.
-        :type value: NodeNG or None
-
-        :param generators: The generators that are looped through.
-        :type generators: list(Comprehension) or None
-        """
-        self.key = key
-        self.value = value
-        if generators is None:
-            self.generators = []
-        else:
-            self.generators = generators
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`DictComp` this is always :class:`Uninferable`.
-        :rtype: Uninferable
-        """
-        return util.Uninferable
-
-    def get_children(self):
-        yield self.key
-        yield self.value
-
-        yield from self.generators
-
-
-class SetComp(ComprehensionScope):
-    """Class representing an :class:`ast.SetComp` node.
-
-    >>> node = astroid.extract_node('{thing for thing in things if thing}')
-    >>> node
-    <SetComp l.1 at 0x7f23b2e41898>
-    """
-
-    _astroid_fields = ("elt", "generators")
-    _other_other_fields = ("locals",)
-    elt = None
-    """The element that forms the output of the expression.
-
-    :type: NodeNG or None
-    """
-    generators = None
-    """The generators that are looped through.
-
-    :type: list(Comprehension) or None
-    """
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        """
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.locals = {}
-        """A map of the name of a local variable to the node defining the local.
-
-        :type: dict(str, NodeNG)
-        """
-
-        super(SetComp, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, elt=None, generators=None):
-        """Do some setup after initialisation.
-
-        :param elt: The element that forms the output of the expression.
-        :type elt: NodeNG or None
-
-        :param generators: The generators that are looped through.
-        :type generators: list(Comprehension) or None
-        """
-        self.elt = elt
-        if generators is None:
-            self.generators = []
-        else:
-            self.generators = generators
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`SetComp` this is always :class:`Uninferable`.
-        :rtype: Uninferable
-        """
-        return util.Uninferable
-
-    def get_children(self):
-        yield self.elt
-
-        yield from self.generators
-
-
-class _ListComp(node_classes.NodeNG):
-    """Class representing an :class:`ast.ListComp` node.
-
-    >>> node = astroid.extract_node('[thing for thing in things if thing]')
-    >>> node
-    <ListComp l.1 at 0x7f23b2e418d0>
-    """
-
-    _astroid_fields = ("elt", "generators")
-    elt = None
-    """The element that forms the output of the expression.
-
-    :type: NodeNG or None
-    """
-    generators = None
-    """The generators that are looped through.
-
-    :type: list(Comprehension) or None
-    """
-
-    def postinit(self, elt=None, generators=None):
-        """Do some setup after initialisation.
-
-        :param elt: The element that forms the output of the expression.
-        :type elt: NodeNG or None
-
-        :param generators: The generators that are looped through.
-        :type generators: list(Comprehension) or None
-        """
-        self.elt = elt
-        self.generators = generators
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`ListComp` this is always :class:`Uninferable`.
-        :rtype: Uninferable
-        """
-        return util.Uninferable
-
-    def get_children(self):
-        yield self.elt
-
-        yield from self.generators
-
-
-class ListComp(_ListComp, ComprehensionScope):
-    """Class representing an :class:`ast.ListComp` node.
-
-    >>> node = astroid.extract_node('[thing for thing in things if thing]')
-    >>> node
-    <ListComp l.1 at 0x7f23b2e418d0>
-    """
-
-    _other_other_fields = ("locals",)
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        self.locals = {}
-        """A map of the name of a local variable to the node defining it.
-
-        :type: dict(str, NodeNG)
-        """
-
-        super(ListComp, self).__init__(lineno, col_offset, parent)
-
-
-def _infer_decorator_callchain(node):
-    """Detect decorator call chaining and see if the end result is a
-    static or a classmethod.
-    """
-    if not isinstance(node, FunctionDef):
-        return None
-    if not node.parent:
-        return None
-    try:
-        result = next(node.infer_call_result(node.parent))
-    except exceptions.InferenceError:
-        return None
-    if isinstance(result, bases.Instance):
-        result = result._proxied
-    if isinstance(result, ClassDef):
-        if result.is_subtype_of("%s.classmethod" % BUILTINS):
-            return "classmethod"
-        if result.is_subtype_of("%s.staticmethod" % BUILTINS):
-            return "staticmethod"
-    return None
-
-
-class Lambda(mixins.FilterStmtsMixin, LocalsDictNodeNG):
-    """Class representing an :class:`ast.Lambda` node.
-
-    >>> node = astroid.extract_node('lambda arg: arg + 1')
-    >>> node
-    <Lambda.<lambda> l.1 at 0x7f23b2e41518>
-    """
-
-    _astroid_fields = ("args", "body")
-    _other_other_fields = ("locals",)
-    name = "<lambda>"
-    is_lambda = True
-
-    def implicit_parameters(self):
-        return 0
-
-    # function's type, 'function' | 'method' | 'staticmethod' | 'classmethod'
-    @property
-    def type(self):
-        """Whether this is a method or function.
-
-        :returns: 'method' if this is a method, 'function' otherwise.
-        :rtype: str
-        """
-        # pylint: disable=no-member
-        if self.args.args and self.args.args[0].name == "self":
-            if isinstance(self.parent.scope(), ClassDef):
-                return "method"
-        return "function"
-
-    def __init__(self, lineno=None, col_offset=None, parent=None):
-        """
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.locals = {}
-        """A map of the name of a local variable to the node defining it.
-
-        :type: dict(str, NodeNG)
-        """
-
-        self.args = []
-        """The arguments that the function takes.
-
-        :type: Arguments or list
-        """
-
-        self.body = []
-        """The contents of the function body.
-
-        :type: list(NodeNG)
-        """
-
-        super(Lambda, self).__init__(lineno, col_offset, parent)
-
-    def postinit(self, args, body):
-        """Do some setup after initialisation.
-
-        :param args: The arguments that the function takes.
-        :type args: Arguments
-
-        :param body: The contents of the function body.
-        :type body: list(NodeNG)
-        """
-        self.args = args
-        self.body = body
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        if "method" in self.type:
-            return "%s.instancemethod" % BUILTINS
-        return "%s.function" % BUILTINS
-
-    def display_type(self):
-        """A human readable type of this node.
-
-        :returns: The type of this node.
-        :rtype: str
-        """
-        if "method" in self.type:
-            return "Method"
-        return "Function"
-
-    def callable(self):
-        """Whether this node defines something that is callable.
-
-        :returns: True if this defines something that is callable,
-            False otherwise.
-            For a :class:`Lambda` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-    def argnames(self):
-        """Get the names of each of the arguments.
-
-        :returns: The names of the arguments.
-        :rtype: list(str)
-        """
-        # pylint: disable=no-member; github.com/pycqa/astroid/issues/291
-        # args is in fact redefined later on by postinit. Can't be changed
-        # to None due to a strong interaction between Lambda and FunctionDef.
-
-        if self.args.args:  # maybe None with builtin functions
-            names = _rec_get_names(self.args.args)
-        else:
-            names = []
-        if self.args.vararg:
-            names.append(self.args.vararg)
-        if self.args.kwarg:
-            names.append(self.args.kwarg)
-        return names
-
-    def infer_call_result(self, caller, context=None):
-        """Infer what the function returns when called.
-
-        :param caller: Unused
-        :type caller: object
-        """
-        # pylint: disable=no-member; github.com/pycqa/astroid/issues/291
-        # args is in fact redefined later on by postinit. Can't be changed
-        # to None due to a strong interaction between Lambda and FunctionDef.
-        return self.body.infer(context)
-
-    def scope_lookup(self, node, name, offset=0):
-        """Lookup where the given names is assigned.
-
-        :param node: The node to look for assignments up to.
-            Any assignments after the given node are ignored.
-        :type node: NodeNG
-
-        :param name: The name to find assignments for.
-        :type name: str
-
-        :param offset: The line offset to filter statements up to.
-        :type offset: int
-
-        :returns: This scope node and the list of assignments associated to the
-            given name according to the scope where it has been found (locals,
-            globals or builtin).
-        :rtype: tuple(str, list(NodeNG))
-        """
-        # pylint: disable=no-member; github.com/pycqa/astroid/issues/291
-        # args is in fact redefined later on by postinit. Can't be changed
-        # to None due to a strong interaction between Lambda and FunctionDef.
-
-        if node in self.args.defaults or node in self.args.kw_defaults:
-            frame = self.parent.frame()
-            # line offset to avoid that def func(f=func) resolve the default
-            # value to the defined function
-            offset = -1
-        else:
-            # check this is not used in function decorators
-            frame = self
-        return frame._scope_lookup(node, name, offset)
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`Lambda` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-    def get_children(self):
-        yield self.args
-        yield self.body
-
-
-class FunctionDef(mixins.MultiLineBlockMixin, node_classes.Statement, Lambda):
-    """Class representing an :class:`ast.FunctionDef`.
-
-    >>> node = astroid.extract_node('''
-    ... def my_func(arg):
-    ...     return arg + 1
-    ... ''')
-    >>> node
-    <FunctionDef.my_func l.2 at 0x7f23b2e71e10>
-    """
-
-    _astroid_fields = ("decorators", "args", "returns", "body")
-    _multi_line_block_fields = ("body",)
-    returns = None
-    decorators = None
-    """The decorators that are applied to this method or function.
-
-    :type: Decorators or None
-    """
-    special_attributes = objectmodel.FunctionModel()
-    """The names of special attributes that this function has.
-
-    :type: objectmodel.FunctionModel
-    """
-    is_function = True
-    """Whether this node indicates a function.
-
-    For a :class:`FunctionDef` this is always ``True``.
-
-    :type: bool
-    """
-    type_annotation = None
-    """If present, this will contain the type annotation passed by a type comment
-
-    :type: NodeNG or None
-    """
-    type_comment_args = None
-    """
-    If present, this will contain the type annotation for arguments
-    passed by a type comment
-    """
-    type_comment_returns = None
-    """If present, this will contain the return type annotation, passed by a type comment"""
-    # attributes below are set by the builder module or by raw factories
-    _other_fields = ("name", "doc")
-    _other_other_fields = (
-        "locals",
-        "_type",
-        "type_comment_returns",
-        "type_comment_args",
-    )
-    _type = None
-
-    def __init__(self, name=None, doc=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param name: The name of the function.
-        :type name: str or None
-
-        :param doc: The function's docstring.
-        :type doc: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.name = name
-        """The name of the function.
-
-        :type name: str or None
-        """
-
-        self.doc = doc
-        """The function's docstring.
-
-        :type doc: str or None
-        """
-
-        self.instance_attrs = {}
-        super(FunctionDef, self).__init__(lineno, col_offset, parent)
-        if parent:
-            frame = parent.frame()
-            frame.set_local(name, self)
-
-    # pylint: disable=arguments-differ; different than Lambdas
-    def postinit(
-        self,
-        args,
-        body,
-        decorators=None,
-        returns=None,
-        type_comment_returns=None,
-        type_comment_args=None,
-    ):
-        """Do some setup after initialisation.
-
-        :param args: The arguments that the function takes.
-        :type args: Arguments or list
-
-        :param body: The contents of the function body.
-        :type body: list(NodeNG)
-
-        :param decorators: The decorators that are applied to this
-            method or function.
-        :type decorators: Decorators or None
-        :params type_comment_returns:
-            The return type annotation passed via a type comment.
-        :params type_comment_args:
-            The args type annotation passed via a type comment.
-        """
-        self.args = args
-        self.body = body
-        self.decorators = decorators
-        self.returns = returns
-        self.type_comment_returns = type_comment_returns
-        self.type_comment_args = type_comment_args
-
-    @decorators_mod.cachedproperty
-    def extra_decorators(self):
-        """The extra decorators that this function can have.
-
-        Additional decorators are considered when they are used as
-        assignments, as in ``method = staticmethod(method)``.
-        The property will return all the callables that are used for
-        decoration.
-
-        :type: list(NodeNG)
-        """
-        frame = self.parent.frame()
-        if not isinstance(frame, ClassDef):
-            return []
-
-        decorators = []
-        for assign in frame._get_assign_nodes():
-            if isinstance(assign.value, node_classes.Call) and isinstance(
-                assign.value.func, node_classes.Name
-            ):
-                for assign_node in assign.targets:
-                    if not isinstance(assign_node, node_classes.AssignName):
-                        # Support only `name = callable(name)`
-                        continue
-
-                    if assign_node.name != self.name:
-                        # Interested only in the assignment nodes that
-                        # decorates the current method.
-                        continue
-                    try:
-                        meth = frame[self.name]
-                    except KeyError:
-                        continue
-                    else:
-                        # Must be a function and in the same frame as the
-                        # original method.
-                        if (
-                            isinstance(meth, FunctionDef)
-                            and assign_node.frame() == frame
-                        ):
-                            decorators.append(assign.value)
-        return decorators
-
-    @decorators_mod.cachedproperty
-    def type(self):  # pylint: disable=invalid-overridden-method
-        """The function type for this node.
-
-        Possible values are: method, function, staticmethod, classmethod.
-
-        :type: str
-        """
-        builtin_descriptors = {"classmethod", "staticmethod"}
-
-        for decorator in self.extra_decorators:
-            if decorator.func.name in builtin_descriptors:
-                return decorator.func.name
-
-        frame = self.parent.frame()
-        type_name = "function"
-        if isinstance(frame, ClassDef):
-            if self.name == "__new__":
-                return "classmethod"
-            if sys.version_info >= (3, 6) and self.name == "__init_subclass__":
-                return "classmethod"
-
-            type_name = "method"
-
-        if not self.decorators:
-            return type_name
-
-        for node in self.decorators.nodes:
-            if isinstance(node, node_classes.Name):
-                if node.name in builtin_descriptors:
-                    return node.name
-
-            if isinstance(node, node_classes.Call):
-                # Handle the following case:
-                # @some_decorator(arg1, arg2)
-                # def func(...)
-                #
-                try:
-                    current = next(node.func.infer())
-                except exceptions.InferenceError:
-                    continue
-                _type = _infer_decorator_callchain(current)
-                if _type is not None:
-                    return _type
-
-            try:
-                for inferred in node.infer():
-                    # Check to see if this returns a static or a class method.
-                    _type = _infer_decorator_callchain(inferred)
-                    if _type is not None:
-                        return _type
-
-                    if not isinstance(inferred, ClassDef):
-                        continue
-                    for ancestor in inferred.ancestors():
-                        if not isinstance(ancestor, ClassDef):
-                            continue
-                        if ancestor.is_subtype_of("%s.classmethod" % BUILTINS):
-                            return "classmethod"
-                        if ancestor.is_subtype_of("%s.staticmethod" % BUILTINS):
-                            return "staticmethod"
-            except exceptions.InferenceError:
-                pass
-        return type_name
-
-    @decorators_mod.cachedproperty
-    def fromlineno(self):
-        """The first line that this node appears on in the source code.
-
-        :type: int or None
-        """
-        # lineno is the line number of the first decorator, we want the def
-        # statement lineno
-        lineno = self.lineno
-        if self.decorators is not None:
-            lineno += sum(
-                node.tolineno - node.lineno + 1 for node in self.decorators.nodes
-            )
-
-        return lineno
-
-    @decorators_mod.cachedproperty
-    def blockstart_tolineno(self):
-        """The line on which the beginning of this block ends.
-
-        :type: int
-        """
-        return self.args.tolineno
-
-    def block_range(self, lineno):
-        """Get a range from the given line number to where this node ends.
-
-        :param lineno: Unused.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to,
-        :rtype: tuple(int, int)
-        """
-        return self.fromlineno, self.tolineno
-
-    def getattr(self, name, context=None):
-        """this method doesn't look in the instance_attrs dictionary since it's
-        done by an Instance proxy at inference time.
-        """
-        if name in self.instance_attrs:
-            return self.instance_attrs[name]
-        if name in self.special_attributes:
-            return [self.special_attributes.lookup(name)]
-        raise exceptions.AttributeInferenceError(target=self, attribute=name)
-
-    def igetattr(self, name, context=None):
-        """Inferred getattr, which returns an iterator of inferred statements."""
-        try:
-            return bases._infer_stmts(self.getattr(name, context), context, frame=self)
-        except exceptions.AttributeInferenceError as error:
-            raise exceptions.InferenceError(
-                error.message, target=self, attribute=name, context=context
-            ) from error
-
-    def is_method(self):
-        """Check if this function node represents a method.
-
-        :returns: True if this is a method, False otherwise.
-        :rtype: bool
-        """
-        # check we are defined in a ClassDef, because this is usually expected
-        # (e.g. pylint...) when is_method() return True
-        return self.type != "function" and isinstance(self.parent.frame(), ClassDef)
-
-    @decorators_mod.cached
-    def decoratornames(self):
-        """Get the qualified names of each of the decorators on this function.
-
-        :returns: The names of the decorators.
-        :rtype: set(str)
-        """
-        result = set()
-        decoratornodes = []
-        if self.decorators is not None:
-            decoratornodes += self.decorators.nodes
-        decoratornodes += self.extra_decorators
-        for decnode in decoratornodes:
-            try:
-                for infnode in decnode.infer():
-                    result.add(infnode.qname())
-            except exceptions.InferenceError:
-                continue
-        return result
-
-    def is_bound(self):
-        """Check if the function is bound to an instance or class.
-
-        :returns: True if the function is bound to an instance or class,
-            False otherwise.
-        :rtype: bool
-        """
-        return self.type == "classmethod"
-
-    def is_abstract(self, pass_is_abstract=True):
-        """Check if the method is abstract.
-
-        A method is considered abstract if any of the following is true:
-        * The only statement is 'raise NotImplementedError'
-        * The only statement is 'pass' and pass_is_abstract is True
-        * The method is annotated with abc.astractproperty/abc.abstractmethod
-
-        :returns: True if the method is abstract, False otherwise.
-        :rtype: bool
-        """
-        if self.decorators:
-            for node in self.decorators.nodes:
-                try:
-                    inferred = next(node.infer())
-                except exceptions.InferenceError:
-                    continue
-                if inferred and inferred.qname() in (
-                    "abc.abstractproperty",
-                    "abc.abstractmethod",
-                ):
-                    return True
-
-        for child_node in self.body:
-            if isinstance(child_node, node_classes.Raise):
-                if child_node.raises_not_implemented():
-                    return True
-            return pass_is_abstract and isinstance(child_node, node_classes.Pass)
-        # empty function is the same as function with a single "pass" statement
-        if pass_is_abstract:
-            return True
-
-    def is_generator(self):
-        """Check if this is a generator function.
-
-        :returns: True is this is a generator function, False otherwise.
-        :rtype: bool
-        """
-        return next(self._get_yield_nodes_skip_lambdas(), False)
-
-    def infer_call_result(self, caller=None, context=None):
-        """Infer what the function returns when called.
-
-        :returns: What the function returns.
-        :rtype: iterable(NodeNG or Uninferable) or None
-        """
-        if self.is_generator():
-            if isinstance(self, AsyncFunctionDef):
-                generator_cls = bases.AsyncGenerator
-            else:
-                generator_cls = bases.Generator
-            result = generator_cls(self)
-            yield result
-            return
-        # This is really a gigantic hack to work around metaclass generators
-        # that return transient class-generating functions. Pylint's AST structure
-        # cannot handle a base class object that is only used for calling __new__,
-        # but does not contribute to the inheritance structure itself. We inject
-        # a fake class into the hierarchy here for several well-known metaclass
-        # generators, and filter it out later.
-        if (
-            self.name == "with_metaclass"
-            and len(self.args.args) == 1
-            and self.args.vararg is not None
-        ):
-            metaclass = next(caller.args[0].infer(context))
-            if isinstance(metaclass, ClassDef):
-                class_bases = [next(arg.infer(context)) for arg in caller.args[1:]]
-                new_class = ClassDef(name="temporary_class")
-                new_class.hide = True
-                new_class.parent = self
-                new_class.postinit(
-                    bases=[base for base in class_bases if base != util.Uninferable],
-                    body=[],
-                    decorators=[],
-                    metaclass=metaclass,
-                )
-                yield new_class
-                return
-        returns = self._get_return_nodes_skip_functions()
-
-        first_return = next(returns, None)
-        if not first_return:
-            if self.body and isinstance(self.body[-1], node_classes.Assert):
-                yield node_classes.Const(None)
-                return
-
-            raise exceptions.InferenceError(
-                "The function does not have any return statements"
-            )
-
-        for returnnode in itertools.chain((first_return,), returns):
-            if returnnode.value is None:
-                yield node_classes.Const(None)
-            else:
-                try:
-                    yield from returnnode.value.infer(context)
-                except exceptions.InferenceError:
-                    yield util.Uninferable
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`FunctionDef` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-    def get_children(self):
-        if self.decorators is not None:
-            yield self.decorators
-
-        yield self.args
-
-        if self.returns is not None:
-            yield self.returns
-
-        yield from self.body
-
-    def scope_lookup(self, node, name, offset=0):
-        """Lookup where the given name is assigned."""
-        if name == "__class__":
-            # __class__ is an implicit closure reference created by the compiler
-            # if any methods in a class body refer to either __class__ or super.
-            # In our case, we want to be able to look it up in the current scope
-            # when `__class__` is being used.
-            frame = self.parent.frame()
-            if isinstance(frame, ClassDef):
-                return self, [frame]
-        return super().scope_lookup(node, name, offset)
-
-
-class AsyncFunctionDef(FunctionDef):
-    """Class representing an :class:`ast.FunctionDef` node.
-
-    A :class:`AsyncFunctionDef` is an asynchronous function
-    created with the `async` keyword.
-
-    >>> node = astroid.extract_node('''
-    async def func(things):
-        async for thing in things:
-            print(thing)
-    ''')
-    >>> node
-    <AsyncFunctionDef.func l.2 at 0x7f23b2e416d8>
-    >>> node.body[0]
-    <AsyncFor l.3 at 0x7f23b2e417b8>
-    """
-
-
-def _rec_get_names(args, names=None):
-    """return a list of all argument names"""
-    if names is None:
-        names = []
-    for arg in args:
-        if isinstance(arg, node_classes.Tuple):
-            _rec_get_names(arg.elts, names)
-        else:
-            names.append(arg.name)
-    return names
-
-
-def _is_metaclass(klass, seen=None):
-    """ Return if the given class can be
-    used as a metaclass.
-    """
-    if klass.name == "type":
-        return True
-    if seen is None:
-        seen = set()
-    for base in klass.bases:
-        try:
-            for baseobj in base.infer():
-                baseobj_name = baseobj.qname()
-                if baseobj_name in seen:
-                    continue
-
-                seen.add(baseobj_name)
-                if isinstance(baseobj, bases.Instance):
-                    # not abstract
-                    return False
-                if baseobj is util.Uninferable:
-                    continue
-                if baseobj is klass:
-                    continue
-                if not isinstance(baseobj, ClassDef):
-                    continue
-                if baseobj._type == "metaclass":
-                    return True
-                if _is_metaclass(baseobj, seen):
-                    return True
-        except exceptions.InferenceError:
-            continue
-    return False
-
-
-def _class_type(klass, ancestors=None):
-    """return a ClassDef node type to differ metaclass and exception
-    from 'regular' classes
-    """
-    # XXX we have to store ancestors in case we have an ancestor loop
-    if klass._type is not None:
-        return klass._type
-    if _is_metaclass(klass):
-        klass._type = "metaclass"
-    elif klass.name.endswith("Exception"):
-        klass._type = "exception"
-    else:
-        if ancestors is None:
-            ancestors = set()
-        klass_name = klass.qname()
-        if klass_name in ancestors:
-            # XXX we are in loop ancestors, and have found no type
-            klass._type = "class"
-            return "class"
-        ancestors.add(klass_name)
-        for base in klass.ancestors(recurs=False):
-            name = _class_type(base, ancestors)
-            if name != "class":
-                if name == "metaclass" and not _is_metaclass(klass):
-                    # don't propagate it if the current class
-                    # can't be a metaclass
-                    continue
-                klass._type = base.type
-                break
-    if klass._type is None:
-        klass._type = "class"
-    return klass._type
-
-
-def get_wrapping_class(node):
-    """Get the class that wraps the given node.
-
-    We consider that a class wraps a node if the class
-    is a parent for the said node.
-
-    :returns: The class that wraps the given node
-    :rtype: ClassDef or None
-    """
-
-    klass = node.frame()
-    while klass is not None and not isinstance(klass, ClassDef):
-        if klass.parent is None:
-            klass = None
-        else:
-            klass = klass.parent.frame()
-    return klass
-
-
-class ClassDef(mixins.FilterStmtsMixin, LocalsDictNodeNG, node_classes.Statement):
-    """Class representing an :class:`ast.ClassDef` node.
-
-    >>> node = astroid.extract_node('''
-    class Thing:
-        def my_meth(self, arg):
-            return arg + self.offset
-    ''')
-    >>> node
-    <ClassDef.Thing l.2 at 0x7f23b2e9e748>
-    """
-
-    # some of the attributes below are set by the builder module or
-    # by a raw factories
-
-    # a dictionary of class instances attributes
-    _astroid_fields = ("decorators", "bases", "body")  # name
-
-    decorators = None
-    """The decorators that are applied to this class.
-
-    :type: Decorators or None
-    """
-    special_attributes = objectmodel.ClassModel()
-    """The names of special attributes that this class has.
-
-    :type: objectmodel.ClassModel
-    """
-
-    _type = None
-    _metaclass_hack = False
-    hide = False
-    type = property(
-        _class_type,
-        doc=(
-            "The class type for this node.\n\n"
-            "Possible values are: class, metaclass, exception.\n\n"
-            ":type: str"
-        ),
-    )
-    _other_fields = ("name", "doc")
-    _other_other_fields = ("locals", "_newstyle")
-    _newstyle = None
-
-    def __init__(self, name=None, doc=None, lineno=None, col_offset=None, parent=None):
-        """
-        :param name: The name of the class.
-        :type name: str or None
-
-        :param doc: The function's docstring.
-        :type doc: str or None
-
-        :param lineno: The line that this node appears on in the source code.
-        :type lineno: int or None
-
-        :param col_offset: The column that this node appears on in the
-            source code.
-        :type col_offset: int or None
-
-        :param parent: The parent node in the syntax tree.
-        :type parent: NodeNG or None
-        """
-        self.instance_attrs = {}
-        self.locals = {}
-        """A map of the name of a local variable to the node defining it.
-
-        :type: dict(str, NodeNG)
-        """
-
-        self.keywords = []
-        """The keywords given to the class definition.
-
-        This is usually for :pep:`3115` style metaclass declaration.
-
-        :type: list(Keyword) or None
-        """
-
-        self.bases = []
-        """What the class inherits from.
-
-        :type: list(NodeNG)
-        """
-
-        self.body = []
-        """The contents of the class body.
-
-        :type: list(NodeNG)
-        """
-
-        self.name = name
-        """The name of the class.
-
-        :type name: str or None
-        """
-
-        self.doc = doc
-        """The class' docstring.
-
-        :type doc: str or None
-        """
-
-        super(ClassDef, self).__init__(lineno, col_offset, parent)
-        if parent is not None:
-            parent.frame().set_local(name, self)
-
-        for local_name, node in self.implicit_locals():
-            self.add_local_node(node, local_name)
-
-    def implicit_parameters(self):
-        return 1
-
-    def implicit_locals(self):
-        """Get implicitly defined class definition locals.
-
-        :returns: the the name and Const pair for each local
-        :rtype: tuple(tuple(str, node_classes.Const), ...)
-        """
-        locals_ = (("__module__", self.special_attributes.attr___module__),)
-        # __qualname__ is defined in PEP3155
-        locals_ += (("__qualname__", self.special_attributes.attr___qualname__),)
-        return locals_
-
-    # pylint: disable=redefined-outer-name
-    def postinit(
-        self, bases, body, decorators, newstyle=None, metaclass=None, keywords=None
-    ):
-        """Do some setup after initialisation.
-
-        :param bases: What the class inherits from.
-        :type bases: list(NodeNG)
-
-        :param body: The contents of the class body.
-        :type body: list(NodeNG)
-
-        :param decorators: The decorators that are applied to this class.
-        :type decorators: Decorators or None
-
-        :param newstyle: Whether this is a new style class or not.
-        :type newstyle: bool or None
-
-        :param metaclass: The metaclass of this class.
-        :type metaclass: NodeNG or None
-
-        :param keywords: The keywords given to the class definition.
-        :type keywords: list(Keyword) or None
-        """
-        self.keywords = keywords
-        self.bases = bases
-        self.body = body
-        self.decorators = decorators
-        if newstyle is not None:
-            self._newstyle = newstyle
-        if metaclass is not None:
-            self._metaclass = metaclass
-
-    def _newstyle_impl(self, context=None):
-        if context is None:
-            context = contextmod.InferenceContext()
-        if self._newstyle is not None:
-            return self._newstyle
-        for base in self.ancestors(recurs=False, context=context):
-            if base._newstyle_impl(context):
-                self._newstyle = True
-                break
-        klass = self.declared_metaclass()
-        # could be any callable, we'd need to infer the result of klass(name,
-        # bases, dict).  punt if it's not a class node.
-        if klass is not None and isinstance(klass, ClassDef):
-            self._newstyle = klass._newstyle_impl(context)
-        if self._newstyle is None:
-            self._newstyle = False
-        return self._newstyle
-
-    _newstyle = None
-    newstyle = property(
-        _newstyle_impl,
-        doc=("Whether this is a new style class or not\n\n" ":type: bool or None"),
-    )
-
-    @decorators_mod.cachedproperty
-    def blockstart_tolineno(self):
-        """The line on which the beginning of this block ends.
-
-        :type: int
-        """
-        if self.bases:
-            return self.bases[-1].tolineno
-
-        return self.fromlineno
-
-    def block_range(self, lineno):
-        """Get a range from the given line number to where this node ends.
-
-        :param lineno: Unused.
-        :type lineno: int
-
-        :returns: The range of line numbers that this node belongs to,
-        :rtype: tuple(int, int)
-        """
-        return self.fromlineno, self.tolineno
-
-    def pytype(self):
-        """Get the name of the type that this node represents.
-
-        :returns: The name of the type.
-        :rtype: str
-        """
-        if self.newstyle:
-            return "%s.type" % BUILTINS
-        return "%s.classobj" % BUILTINS
-
-    def display_type(self):
-        """A human readable type of this node.
-
-        :returns: The type of this node.
-        :rtype: str
-        """
-        return "Class"
-
-    def callable(self):
-        """Whether this node defines something that is callable.
-
-        :returns: True if this defines something that is callable,
-            False otherwise.
-            For a :class:`ClassDef` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-    def is_subtype_of(self, type_name, context=None):
-        """Whether this class is a subtype of the given type.
-
-        :param type_name: The name of the type of check against.
-        :type type_name: str
-
-        :returns: True if this class is a subtype of the given type,
-            False otherwise.
-        :rtype: bool
-        """
-        if self.qname() == type_name:
-            return True
-        for anc in self.ancestors(context=context):
-            if anc.qname() == type_name:
-                return True
-        return False
-
-    def _infer_type_call(self, caller, context):
-        name_node = next(caller.args[0].infer(context))
-        if isinstance(name_node, node_classes.Const) and isinstance(
-            name_node.value, str
-        ):
-            name = name_node.value
-        else:
-            return util.Uninferable
-
-        result = ClassDef(name, None)
-
-        # Get the bases of the class.
-        class_bases = next(caller.args[1].infer(context))
-        if isinstance(class_bases, (node_classes.Tuple, node_classes.List)):
-            result.bases = class_bases.itered()
-        else:
-            # There is currently no AST node that can represent an 'unknown'
-            # node (Uninferable is not an AST node), therefore we simply return Uninferable here
-            # although we know at least the name of the class.
-            return util.Uninferable
-
-        # Get the members of the class
-        try:
-            members = next(caller.args[2].infer(context))
-        except exceptions.InferenceError:
-            members = None
-
-        if members and isinstance(members, node_classes.Dict):
-            for attr, value in members.items:
-                if isinstance(attr, node_classes.Const) and isinstance(attr.value, str):
-                    result.locals[attr.value] = [value]
-
-        result.parent = caller.parent
-        return result
-
-    def infer_call_result(self, caller, context=None):
-        """infer what a class is returning when called"""
-        if (
-            self.is_subtype_of("%s.type" % (BUILTINS,), context)
-            and len(caller.args) == 3
-        ):
-            result = self._infer_type_call(caller, context)
-            yield result
-            return
-
-        dunder_call = None
-        try:
-            metaclass = self.metaclass(context=context)
-            if metaclass is not None:
-                dunder_call = next(metaclass.igetattr("__call__", context))
-        except exceptions.AttributeInferenceError:
-            pass
-
-        if dunder_call and dunder_call.qname() != "builtins.type.__call__":
-            # Call type.__call__ if not set metaclass
-            # (since type is the default metaclass)
-            context = contextmod.bind_context_to_node(context, self)
-            yield from dunder_call.infer_call_result(caller, context)
-        else:
-            if any(cls.name in EXCEPTION_BASE_CLASSES for cls in self.mro()):
-                # Subclasses of exceptions can be exception instances
-                yield objects.ExceptionInstance(self)
-            else:
-                yield bases.Instance(self)
-
-    def scope_lookup(self, node, name, offset=0):
-        """Lookup where the given name is assigned.
-
-        :param node: The node to look for assignments up to.
-            Any assignments after the given node are ignored.
-        :type node: NodeNG
-
-        :param name: The name to find assignments for.
-        :type name: str
-
-        :param offset: The line offset to filter statements up to.
-        :type offset: int
-
-        :returns: This scope node and the list of assignments associated to the
-            given name according to the scope where it has been found (locals,
-            globals or builtin).
-        :rtype: tuple(str, list(NodeNG))
-        """
-        # If the name looks like a builtin name, just try to look
-        # into the upper scope of this class. We might have a
-        # decorator that it's poorly named after a builtin object
-        # inside this class.
-        lookup_upper_frame = (
-            isinstance(node.parent, node_classes.Decorators)
-            and name in MANAGER.builtins_module
-        )
-        if (
-            any(node == base or base.parent_of(node) for base in self.bases)
-            or lookup_upper_frame
-        ):
-            # Handle the case where we have either a name
-            # in the bases of a class, which exists before
-            # the actual definition or the case where we have
-            # a Getattr node, with that name.
-            #
-            # name = ...
-            # class A(name):
-            #     def name(self): ...
-            #
-            # import name
-            # class A(name.Name):
-            #     def name(self): ...
-
-            frame = self.parent.frame()
-            # line offset to avoid that class A(A) resolve the ancestor to
-            # the defined class
-            offset = -1
-        else:
-            frame = self
-        return frame._scope_lookup(node, name, offset)
-
-    @property
-    def basenames(self):
-        """The names of the parent classes
-
-        Names are given in the order they appear in the class definition.
-
-        :type: list(str)
-        """
-        return [bnode.as_string() for bnode in self.bases]
-
-    def ancestors(self, recurs=True, context=None):
-        """Iterate over the base classes in prefixed depth first order.
-
-        :param recurs: Whether to recurse or return direct ancestors only.
-        :type recurs: bool
-
-        :returns: The base classes
-        :rtype: iterable(NodeNG)
-        """
-        # FIXME: should be possible to choose the resolution order
-        # FIXME: inference make infinite loops possible here
-        yielded = {self}
-        if context is None:
-            context = contextmod.InferenceContext()
-        if not self.bases and self.qname() != "builtins.object":
-            yield builtin_lookup("object")[1][0]
-            return
-
-        for stmt in self.bases:
-            with context.restore_path():
-                try:
-                    for baseobj in stmt.infer(context):
-                        if not isinstance(baseobj, ClassDef):
-                            if isinstance(baseobj, bases.Instance):
-                                baseobj = baseobj._proxied
-                            else:
-                                continue
-                        if not baseobj.hide:
-                            if baseobj in yielded:
-                                continue
-                            yielded.add(baseobj)
-                            yield baseobj
-                        if not recurs:
-                            continue
-                        for grandpa in baseobj.ancestors(recurs=True, context=context):
-                            if grandpa is self:
-                                # This class is the ancestor of itself.
-                                break
-                            if grandpa in yielded:
-                                continue
-                            yielded.add(grandpa)
-                            yield grandpa
-                except exceptions.InferenceError:
-                    continue
-
-    def local_attr_ancestors(self, name, context=None):
-        """Iterate over the parents that define the given name.
-
-        :param name: The name to find definitions for.
-        :type name: str
-
-        :returns: The parents that define the given name.
-        :rtype: iterable(NodeNG)
-        """
-        # Look up in the mro if we can. This will result in the
-        # attribute being looked up just as Python does it.
-        try:
-            ancestors = self.mro(context)[1:]
-        except exceptions.MroError:
-            # Fallback to use ancestors, we can't determine
-            # a sane MRO.
-            ancestors = self.ancestors(context=context)
-        for astroid in ancestors:
-            if name in astroid:
-                yield astroid
-
-    def instance_attr_ancestors(self, name, context=None):
-        """Iterate over the parents that define the given name as an attribute.
-
-        :param name: The name to find definitions for.
-        :type name: str
-
-        :returns: The parents that define the given name as
-            an instance attribute.
-        :rtype: iterable(NodeNG)
-        """
-        for astroid in self.ancestors(context=context):
-            if name in astroid.instance_attrs:
-                yield astroid
-
-    def has_base(self, node):
-        """Whether this class directly inherits from the given node.
-
-        :param node: The node to check for.
-        :type node: NodeNG
-
-        :returns: True if this class directly inherits from the given node.
-        :rtype: bool
-        """
-        return node in self.bases
-
-    def local_attr(self, name, context=None):
-        """Get the list of assign nodes associated to the given name.
-
-        Assignments are looked for in both this class and in parents.
-
-        :returns: The list of assignments to the given name.
-        :rtype: list(NodeNG)
-
-        :raises AttributeInferenceError: If no attribute with this name
-            can be found in this class or parent classes.
-        """
-        result = []
-        if name in self.locals:
-            result = self.locals[name]
-        else:
-            class_node = next(self.local_attr_ancestors(name, context), None)
-            if class_node:
-                result = class_node.locals[name]
-        result = [n for n in result if not isinstance(n, node_classes.DelAttr)]
-        if result:
-            return result
-        raise exceptions.AttributeInferenceError(
-            target=self, attribute=name, context=context
-        )
-
-    def instance_attr(self, name, context=None):
-        """Get the list of nodes associated to the given attribute name.
-
-        Assignments are looked for in both this class and in parents.
-
-        :returns: The list of assignments to the given name.
-        :rtype: list(NodeNG)
-
-        :raises AttributeInferenceError: If no attribute with this name
-            can be found in this class or parent classes.
-        """
-        # Return a copy, so we don't modify self.instance_attrs,
-        # which could lead to infinite loop.
-        values = list(self.instance_attrs.get(name, []))
-        # get all values from parents
-        for class_node in self.instance_attr_ancestors(name, context):
-            values += class_node.instance_attrs[name]
-        values = [n for n in values if not isinstance(n, node_classes.DelAttr)]
-        if values:
-            return values
-        raise exceptions.AttributeInferenceError(
-            target=self, attribute=name, context=context
-        )
-
-    def instantiate_class(self):
-        """Get an :class:`Instance` of the :class:`ClassDef` node.
-
-        :returns: An :class:`Instance` of the :class:`ClassDef` node,
-            or self if this is not possible.
-        :rtype: Instance or ClassDef
-        """
-        return bases.Instance(self)
-
-    def getattr(self, name, context=None, class_context=True):
-        """Get an attribute from this class, using Python's attribute semantic.
-
-        This method doesn't look in the :attr:`instance_attrs` dictionary
-        since it is done by an :class:`Instance` proxy at inference time.
-        It may return an :class:`Uninferable` object if
-        the attribute has not been
-        found, but a ``__getattr__`` or ``__getattribute__`` method is defined.
-        If ``class_context`` is given, then it is considered that the
-        attribute is accessed from a class context,
-        e.g. ClassDef.attribute, otherwise it might have been accessed
-        from an instance as well. If ``class_context`` is used in that
-        case, then a lookup in the implicit metaclass and the explicit
-        metaclass will be done.
-
-        :param name: The attribute to look for.
-        :type name: str
-
-        :param class_context: Whether the attribute can be accessed statically.
-        :type class_context: bool
-
-        :returns: The attribute.
-        :rtype: list(NodeNG)
-
-        :raises AttributeInferenceError: If the attribute cannot be inferred.
-        """
-        values = self.locals.get(name, [])
-        if name in self.special_attributes and class_context and not values:
-            result = [self.special_attributes.lookup(name)]
-            if name == "__bases__":
-                # Need special treatment, since they are mutable
-                # and we need to return all the values.
-                result += values
-            return result
-
-        # don't modify the list in self.locals!
-        values = list(values)
-        for classnode in self.ancestors(recurs=True, context=context):
-            values += classnode.locals.get(name, [])
-
-        if class_context:
-            values += self._metaclass_lookup_attribute(name, context)
-
-        if not values:
-            raise exceptions.AttributeInferenceError(
-                target=self, attribute=name, context=context
-            )
-
-        # Look for AnnAssigns, which are not attributes in the purest sense.
-        for value in values:
-            if isinstance(value, node_classes.AssignName):
-                stmt = value.statement()
-                if isinstance(stmt, node_classes.AnnAssign) and stmt.value is None:
-                    raise exceptions.AttributeInferenceError(
-                        target=self, attribute=name, context=context
-                    )
-        return values
-
-    def _metaclass_lookup_attribute(self, name, context):
-        """Search the given name in the implicit and the explicit metaclass."""
-        attrs = set()
-        implicit_meta = self.implicit_metaclass()
-        metaclass = self.metaclass()
-        for cls in {implicit_meta, metaclass}:
-            if cls and cls != self and isinstance(cls, ClassDef):
-                cls_attributes = self._get_attribute_from_metaclass(cls, name, context)
-                attrs.update(set(cls_attributes))
-        return attrs
-
-    def _get_attribute_from_metaclass(self, cls, name, context):
-        try:
-            attrs = cls.getattr(name, context=context, class_context=True)
-        except exceptions.AttributeInferenceError:
-            return
-
-        for attr in bases._infer_stmts(attrs, context, frame=cls):
-            if not isinstance(attr, FunctionDef):
-                yield attr
-                continue
-
-            if bases._is_property(attr):
-                yield from attr.infer_call_result(self, context)
-                continue
-            if attr.type == "classmethod":
-                # If the method is a classmethod, then it will
-                # be bound to the metaclass, not to the class
-                # from where the attribute is retrieved.
-                # get_wrapping_class could return None, so just
-                # default to the current class.
-                frame = get_wrapping_class(attr) or self
-                yield bases.BoundMethod(attr, frame)
-            elif attr.type == "staticmethod":
-                yield attr
-            else:
-                yield bases.BoundMethod(attr, self)
-
-    def igetattr(self, name, context=None, class_context=True):
-        """Infer the possible values of the given variable.
-
-        :param name: The name of the variable to infer.
-        :type name: str
-
-        :returns: The inferred possible values.
-        :rtype: iterable(NodeNG or Uninferable)
-        """
-        # set lookup name since this is necessary to infer on import nodes for
-        # instance
-        context = contextmod.copy_context(context)
-        context.lookupname = name
-        try:
-            attr = self.getattr(name, context, class_context=class_context)[0]
-            for inferred in bases._infer_stmts([attr], context, frame=self):
-                # yield Uninferable object instead of descriptors when necessary
-                if not isinstance(inferred, node_classes.Const) and isinstance(
-                    inferred, bases.Instance
-                ):
-                    try:
-                        inferred._proxied.getattr("__get__", context)
-                    except exceptions.AttributeInferenceError:
-                        yield inferred
-                    else:
-                        yield util.Uninferable
-                else:
-                    yield function_to_method(inferred, self)
-        except exceptions.AttributeInferenceError as error:
-            if not name.startswith("__") and self.has_dynamic_getattr(context):
-                # class handle some dynamic attributes, return a Uninferable object
-                yield util.Uninferable
-            else:
-                raise exceptions.InferenceError(
-                    error.message, target=self, attribute=name, context=context
-                )
-
-    def has_dynamic_getattr(self, context=None):
-        """Check if the class has a custom __getattr__ or __getattribute__.
-
-        If any such method is found and it is not from
-        builtins, nor from an extension module, then the function
-        will return True.
-
-        :returns: True if the class has a custom
-            __getattr__ or __getattribute__, False otherwise.
-        :rtype: bool
-        """
-
-        def _valid_getattr(node):
-            root = node.root()
-            return root.name != BUILTINS and getattr(root, "pure_python", None)
-
-        try:
-            return _valid_getattr(self.getattr("__getattr__", context)[0])
-        except exceptions.AttributeInferenceError:
-            # if self.newstyle: XXX cause an infinite recursion error
-            try:
-                getattribute = self.getattr("__getattribute__", context)[0]
-                return _valid_getattr(getattribute)
-            except exceptions.AttributeInferenceError:
-                pass
-        return False
-
-    def getitem(self, index, context=None):
-        """Return the inference of a subscript.
-
-        This is basically looking up the method in the metaclass and calling it.
-
-        :returns: The inferred value of a subscript to this class.
-        :rtype: NodeNG
-
-        :raises AstroidTypeError: If this class does not define a
-            ``__getitem__`` method.
-        """
-        try:
-            methods = dunder_lookup.lookup(self, "__getitem__")
-        except exceptions.AttributeInferenceError as exc:
-            raise exceptions.AstroidTypeError(node=self, context=context) from exc
-
-        method = methods[0]
-
-        # Create a new callcontext for providing index as an argument.
-        new_context = contextmod.bind_context_to_node(context, self)
-        new_context.callcontext = contextmod.CallContext(args=[index])
-
-        try:
-            return next(method.infer_call_result(self, new_context))
-        except exceptions.InferenceError:
-            return util.Uninferable
-
-    def methods(self):
-        """Iterate over all of the method defined in this class and its parents.
-
-        :returns: The methods defined on the class.
-        :rtype: iterable(FunctionDef)
-        """
-        done = {}
-        for astroid in itertools.chain(iter((self,)), self.ancestors()):
-            for meth in astroid.mymethods():
-                if meth.name in done:
-                    continue
-                done[meth.name] = None
-                yield meth
-
-    def mymethods(self):
-        """Iterate over all of the method defined in this class only.
-
-        :returns: The methods defined on the class.
-        :rtype: iterable(FunctionDef)
-        """
-        for member in self.values():
-            if isinstance(member, FunctionDef):
-                yield member
-
-    def implicit_metaclass(self):
-        """Get the implicit metaclass of the current class.
-
-        For newstyle classes, this will return an instance of builtins.type.
-        For oldstyle classes, it will simply return None, since there's
-        no implicit metaclass there.
-
-        :returns: The metaclass.
-        :rtype: builtins.type or None
-        """
-        if self.newstyle:
-            return builtin_lookup("type")[1][0]
-        return None
-
-    _metaclass = None
-
-    def declared_metaclass(self, context=None):
-        """Return the explicit declared metaclass for the current class.
-
-        An explicit declared metaclass is defined
-        either by passing the ``metaclass`` keyword argument
-        in the class definition line (Python 3) or (Python 2) by
-        having a ``__metaclass__`` class attribute, or if there are
-        no explicit bases but there is a global ``__metaclass__`` variable.
-
-        :returns: The metaclass of this class,
-            or None if one could not be found.
-        :rtype: NodeNG or None
-        """
-        for base in self.bases:
-            try:
-                for baseobj in base.infer(context=context):
-                    if isinstance(baseobj, ClassDef) and baseobj.hide:
-                        self._metaclass = baseobj._metaclass
-                        self._metaclass_hack = True
-                        break
-            except exceptions.InferenceError:
-                pass
-
-        if self._metaclass:
-            # Expects this from Py3k TreeRebuilder
-            try:
-                return next(
-                    node
-                    for node in self._metaclass.infer(context=context)
-                    if node is not util.Uninferable
-                )
-            except (exceptions.InferenceError, StopIteration):
-                return None
-
-        return None
-
-    def _find_metaclass(self, seen=None, context=None):
-        if seen is None:
-            seen = set()
-        seen.add(self)
-
-        klass = self.declared_metaclass(context=context)
-        if klass is None:
-            for parent in self.ancestors(context=context):
-                if parent not in seen:
-                    klass = parent._find_metaclass(seen)
-                    if klass is not None:
-                        break
-        return klass
-
-    def metaclass(self, context=None):
-        """Get the metaclass of this class.
-
-        If this class does not define explicitly a metaclass,
-        then the first defined metaclass in ancestors will be used
-        instead.
-
-        :returns: The metaclass of this class.
-        :rtype: NodeNG or None
-        """
-        return self._find_metaclass(context=context)
-
-    def has_metaclass_hack(self):
-        return self._metaclass_hack
-
-    def _islots(self):
-        """ Return an iterator with the inferred slots. """
-        if "__slots__" not in self.locals:
-            return None
-        for slots in self.igetattr("__slots__"):
-            # check if __slots__ is a valid type
-            for meth in ITER_METHODS:
-                try:
-                    slots.getattr(meth)
-                    break
-                except exceptions.AttributeInferenceError:
-                    continue
-            else:
-                continue
-
-            if isinstance(slots, node_classes.Const):
-                # a string. Ignore the following checks,
-                # but yield the node, only if it has a value
-                if slots.value:
-                    yield slots
-                continue
-            if not hasattr(slots, "itered"):
-                # we can't obtain the values, maybe a .deque?
-                continue
-
-            if isinstance(slots, node_classes.Dict):
-                values = [item[0] for item in slots.items]
-            else:
-                values = slots.itered()
-            if values is util.Uninferable:
-                continue
-            if not values:
-                # Stop the iteration, because the class
-                # has an empty list of slots.
-                return values
-
-            for elt in values:
-                try:
-                    for inferred in elt.infer():
-                        if inferred is util.Uninferable:
-                            continue
-                        if not isinstance(
-                            inferred, node_classes.Const
-                        ) or not isinstance(inferred.value, str):
-                            continue
-                        if not inferred.value:
-                            continue
-                        yield inferred
-                except exceptions.InferenceError:
-                    continue
-
-        return None
-
-    def _slots(self):
-        if not self.newstyle:
-            raise NotImplementedError(
-                "The concept of slots is undefined for old-style classes."
-            )
-
-        slots = self._islots()
-        try:
-            first = next(slots)
-        except StopIteration as exc:
-            # The class doesn't have a __slots__ definition or empty slots.
-            if exc.args and exc.args[0] not in ("", None):
-                return exc.args[0]
-            return None
-        return [first] + list(slots)
-
-    # Cached, because inferring them all the time is expensive
-    @decorators_mod.cached
-    def slots(self):
-        """Get all the slots for this node.
-
-        :returns: The names of slots for this class.
-            If the class doesn't define any slot, through the ``__slots__``
-            variable, then this function will return a None.
-            Also, it will return None in the case the slots were not inferred.
-        :rtype: list(str) or None
-        """
-
-        def grouped_slots():
-            # Not interested in object, since it can't have slots.
-            for cls in self.mro()[:-1]:
-                try:
-                    cls_slots = cls._slots()
-                except NotImplementedError:
-                    continue
-                if cls_slots is not None:
-                    yield from cls_slots
-                else:
-                    yield None
-
-        if not self.newstyle:
-            raise NotImplementedError(
-                "The concept of slots is undefined for old-style classes."
-            )
-
-        slots = list(grouped_slots())
-        if not all(slot is not None for slot in slots):
-            return None
-
-        return sorted(slots, key=lambda item: item.value)
-
-    def _inferred_bases(self, context=None):
-        # Similar with .ancestors, but the difference is when one base is inferred,
-        # only the first object is wanted. That's because
-        # we aren't interested in superclasses, as in the following
-        # example:
-        #
-        # class SomeSuperClass(object): pass
-        # class SomeClass(SomeSuperClass): pass
-        # class Test(SomeClass): pass
-        #
-        # Inferring SomeClass from the Test's bases will give
-        # us both SomeClass and SomeSuperClass, but we are interested
-        # only in SomeClass.
-
-        if context is None:
-            context = contextmod.InferenceContext()
-        if not self.bases and self.qname() != "builtins.object":
-            yield builtin_lookup("object")[1][0]
-            return
-
-        for stmt in self.bases:
-            try:
-                baseobj = next(stmt.infer(context=context))
-            except exceptions.InferenceError:
-                continue
-            if isinstance(baseobj, bases.Instance):
-                baseobj = baseobj._proxied
-            if not isinstance(baseobj, ClassDef):
-                continue
-            if not baseobj.hide:
-                yield baseobj
-            else:
-                yield from baseobj.bases
-
-    def _compute_mro(self, context=None):
-        inferred_bases = list(self._inferred_bases(context=context))
-        bases_mro = []
-        for base in inferred_bases:
-            if base is self:
-                continue
-
-            try:
-                mro = base._compute_mro(context=context)
-                bases_mro.append(mro)
-            except NotImplementedError:
-                # Some classes have in their ancestors both newstyle and
-                # old style classes. For these we can't retrieve the .mro,
-                # although in Python it's possible, since the class we are
-                # currently working is in fact new style.
-                # So, we fallback to ancestors here.
-                ancestors = list(base.ancestors(context=context))
-                bases_mro.append(ancestors)
-
-        unmerged_mro = [[self]] + bases_mro + [inferred_bases]
-        unmerged_mro = list(clean_duplicates_mro(unmerged_mro, self, context))
-        return _c3_merge(unmerged_mro, self, context)
-
-    def mro(self, context=None) -> List["ClassDef"]:
-        """Get the method resolution order, using C3 linearization.
-
-        :returns: The list of ancestors, sorted by the mro.
-        :rtype: list(NodeNG)
-        :raises DuplicateBasesError: Duplicate bases in the same class base
-        :raises InconsistentMroError: A class' MRO is inconsistent
-        """
-        return self._compute_mro(context=context)
-
-    def bool_value(self):
-        """Determine the boolean value of this node.
-
-        :returns: The boolean value of this node.
-            For a :class:`ClassDef` this is always ``True``.
-        :rtype: bool
-        """
-        return True
-
-    def get_children(self):
-        if self.decorators is not None:
-            yield self.decorators
-
-        yield from self.bases
-        yield from self.body
-
-    @decorators_mod.cached
-    def _get_assign_nodes(self):
-        children_assign_nodes = (
-            child_node._get_assign_nodes() for child_node in self.body
-        )
-        return list(itertools.chain.from_iterable(children_assign_nodes))
diff --git a/venv/Lib/site-packages/astroid/test_utils.py b/venv/Lib/site-packages/astroid/test_utils.py
deleted file mode 100644
index 6c965ef..0000000
--- a/venv/Lib/site-packages/astroid/test_utils.py
+++ /dev/null
@@ -1,73 +0,0 @@
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-"""Utility functions for test code that uses astroid ASTs as input."""
-import contextlib
-import functools
-import sys
-import warnings
-
-import pytest
-
-from astroid import nodes
-
-
-def require_version(minver=None, maxver=None):
-    """ Compare version of python interpreter to the given one. Skip the test
-    if older.
-    """
-
-    def parse(string, default=None):
-        string = string or default
-        try:
-            return tuple(int(v) for v in string.split("."))
-        except ValueError as exc:
-            raise ValueError(
-                "{string} is not a correct version : should be X.Y[.Z].".format(
-                    string=string
-                )
-            ) from exc
-
-    def check_require_version(f):
-        current = sys.version_info[:3]
-        if parse(minver, "0") < current <= parse(maxver, "4"):
-            return f
-
-        str_version = ".".join(str(v) for v in sys.version_info)
-
-        @functools.wraps(f)
-        def new_f(*args, **kwargs):
-            if minver is not None:
-                pytest.skip(
-                    "Needs Python > %s. Current version is %s." % (minver, str_version)
-                )
-            elif maxver is not None:
-                pytest.skip(
-                    "Needs Python <= %s. Current version is %s." % (maxver, str_version)
-                )
-
-        return new_f
-
-    return check_require_version
-
-
-def get_name_node(start_from, name, index=0):
-    return [n for n in start_from.nodes_of_class(nodes.Name) if n.name == name][index]
-
-
-@contextlib.contextmanager
-def enable_warning(warning):
-    warnings.simplefilter("always", warning)
-    try:
-        yield
-    finally:
-        # Reset it to default value, so it will take
-        # into account the values from the -W flag.
-        warnings.simplefilter("default", warning)
diff --git a/venv/Lib/site-packages/astroid/transforms.py b/venv/Lib/site-packages/astroid/transforms.py
deleted file mode 100644
index e5506cc..0000000
--- a/venv/Lib/site-packages/astroid/transforms.py
+++ /dev/null
@@ -1,90 +0,0 @@
-# Copyright (c) 2015-2016, 2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-
-import collections
-from functools import lru_cache
-
-
-class TransformVisitor:
-    """A visitor for handling transforms.
-
-    The standard approach of using it is to call
-    :meth:`~visit` with an *astroid* module and the class
-    will take care of the rest, walking the tree and running the
-    transforms for each encountered node.
-    """
-
-    TRANSFORM_MAX_CACHE_SIZE = 10000
-
-    def __init__(self):
-        self.transforms = collections.defaultdict(list)
-
-    @lru_cache(maxsize=TRANSFORM_MAX_CACHE_SIZE)
-    def _transform(self, node):
-        """Call matching transforms for the given node if any and return the
-        transformed node.
-        """
-        cls = node.__class__
-        if cls not in self.transforms:
-            # no transform registered for this class of node
-            return node
-
-        transforms = self.transforms[cls]
-        for transform_func, predicate in transforms:
-            if predicate is None or predicate(node):
-                ret = transform_func(node)
-                # if the transformation function returns something, it's
-                # expected to be a replacement for the node
-                if ret is not None:
-                    node = ret
-                if ret.__class__ != cls:
-                    # Can no longer apply the rest of the transforms.
-                    break
-        return node
-
-    def _visit(self, node):
-        if hasattr(node, "_astroid_fields"):
-            for name in node._astroid_fields:
-                value = getattr(node, name)
-                visited = self._visit_generic(value)
-                if visited != value:
-                    setattr(node, name, visited)
-        return self._transform(node)
-
-    def _visit_generic(self, node):
-        if isinstance(node, list):
-            return [self._visit_generic(child) for child in node]
-        if isinstance(node, tuple):
-            return tuple(self._visit_generic(child) for child in node)
-        if not node or isinstance(node, str):
-            return node
-
-        return self._visit(node)
-
-    def register_transform(self, node_class, transform, predicate=None):
-        """Register `transform(node)` function to be applied on the given
-        astroid's `node_class` if `predicate` is None or returns true
-        when called with the node as argument.
-
-        The transform function may return a value which is then used to
-        substitute the original node in the tree.
-        """
-        self.transforms[node_class].append((transform, predicate))
-
-    def unregister_transform(self, node_class, transform, predicate=None):
-        """Unregister the given transform."""
-        self.transforms[node_class].remove((transform, predicate))
-
-    def visit(self, module):
-        """Walk the given astroid *tree* and transform each encountered node
-
-        Only the nodes which have transforms registered will actually
-        be replaced or changed.
-        """
-        module.body = [self._visit(child) for child in module.body]
-        return self._transform(module)
diff --git a/venv/Lib/site-packages/astroid/util.py b/venv/Lib/site-packages/astroid/util.py
deleted file mode 100644
index 3ab7561..0000000
--- a/venv/Lib/site-packages/astroid/util.py
+++ /dev/null
@@ -1,164 +0,0 @@
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015-2016 Ceridwen <ceridwenv@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the LGPL: https://www.gnu.org/licenses/old-licenses/lgpl-2.1.en.html
-# For details: https://github.com/PyCQA/astroid/blob/master/COPYING.LESSER
-
-import warnings
-from itertools import islice
-
-import importlib
-import lazy_object_proxy
-
-
-def lazy_descriptor(obj):
-    class DescriptorProxy(lazy_object_proxy.Proxy):
-        def __get__(self, instance, owner=None):
-            return self.__class__.__get__(self, instance)
-
-    return DescriptorProxy(obj)
-
-
-def lazy_import(module_name):
-    return lazy_object_proxy.Proxy(
-        lambda: importlib.import_module("." + module_name, "astroid")
-    )
-
-
-@object.__new__
-class Uninferable:
-    """Special inference object, which is returned when inference fails."""
-
-    def __repr__(self):
-        return "Uninferable"
-
-    __str__ = __repr__
-
-    def __getattribute__(self, name):
-        if name == "next":
-            raise AttributeError("next method should not be called")
-        if name.startswith("__") and name.endswith("__"):
-            return object.__getattribute__(self, name)
-        if name == "accept":
-            return object.__getattribute__(self, name)
-        return self
-
-    def __call__(self, *args, **kwargs):
-        return self
-
-    def __bool__(self):
-        return False
-
-    __nonzero__ = __bool__
-
-    def accept(self, visitor):
-        func = getattr(visitor, "visit_uninferable")
-        return func(self)
-
-
-class BadOperationMessage:
-    """Object which describes a TypeError occurred somewhere in the inference chain
-
-    This is not an exception, but a container object which holds the types and
-    the error which occurred.
-    """
-
-
-class BadUnaryOperationMessage(BadOperationMessage):
-    """Object which describes operational failures on UnaryOps."""
-
-    def __init__(self, operand, op, error):
-        self.operand = operand
-        self.op = op
-        self.error = error
-
-    @property
-    def _object_type_helper(self):
-        helpers = lazy_import("helpers")
-        return helpers.object_type
-
-    def _object_type(self, obj):
-        # pylint: disable=not-callable; can't infer lazy_import
-        objtype = self._object_type_helper(obj)
-        if objtype is Uninferable:
-            return None
-
-        return objtype
-
-    def __str__(self):
-        if hasattr(self.operand, "name"):
-            operand_type = self.operand.name
-        else:
-            object_type = self._object_type(self.operand)
-            if hasattr(object_type, "name"):
-                operand_type = object_type.name
-            else:
-                # Just fallback to as_string
-                operand_type = object_type.as_string()
-
-        msg = "bad operand type for unary {}: {}"
-        return msg.format(self.op, operand_type)
-
-
-class BadBinaryOperationMessage(BadOperationMessage):
-    """Object which describes type errors for BinOps."""
-
-    def __init__(self, left_type, op, right_type):
-        self.left_type = left_type
-        self.right_type = right_type
-        self.op = op
-
-    def __str__(self):
-        msg = "unsupported operand type(s) for {}: {!r} and {!r}"
-        return msg.format(self.op, self.left_type.name, self.right_type.name)
-
-
-def _instancecheck(cls, other):
-    wrapped = cls.__wrapped__
-    other_cls = other.__class__
-    is_instance_of = wrapped is other_cls or issubclass(other_cls, wrapped)
-    warnings.warn(
-        "%r is deprecated and slated for removal in astroid "
-        "2.0, use %r instead" % (cls.__class__.__name__, wrapped.__name__),
-        PendingDeprecationWarning,
-        stacklevel=2,
-    )
-    return is_instance_of
-
-
-def proxy_alias(alias_name, node_type):
-    """Get a Proxy from the given name to the given node type."""
-    proxy = type(
-        alias_name,
-        (lazy_object_proxy.Proxy,),
-        {
-            "__class__": object.__dict__["__class__"],
-            "__instancecheck__": _instancecheck,
-        },
-    )
-    return proxy(lambda: node_type)
-
-
-def limit_inference(iterator, size):
-    """Limit inference amount.
-
-    Limit inference amount to help with performance issues with
-    exponentially exploding possible results.
-
-    :param iterator: Inference generator to limit
-    :type iterator: Iterator(NodeNG)
-
-    :param size: Maximum mount of nodes yielded plus an
-        Uninferable at the end if limit reached
-    :type size: int
-
-    :yields: A possibly modified generator
-    :rtype param: Iterable
-    """
-    yield from islice(iterator, size)
-    has_more = next(iterator, False)
-    if has_more is not False:
-        yield Uninferable
-        return
diff --git a/venv/Lib/site-packages/colorama-0.4.3.dist-info/INSTALLER b/venv/Lib/site-packages/colorama-0.4.3.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/colorama-0.4.3.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/colorama-0.4.3.dist-info/LICENSE.txt b/venv/Lib/site-packages/colorama-0.4.3.dist-info/LICENSE.txt
deleted file mode 100644
index 3105888..0000000
--- a/venv/Lib/site-packages/colorama-0.4.3.dist-info/LICENSE.txt
+++ /dev/null
@@ -1,27 +0,0 @@
-Copyright (c) 2010 Jonathan Hartley
-All rights reserved.
-
-Redistribution and use in source and binary forms, with or without
-modification, are permitted provided that the following conditions are met:
-
-* Redistributions of source code must retain the above copyright notice, this
-  list of conditions and the following disclaimer.
-
-* Redistributions in binary form must reproduce the above copyright notice,
-  this list of conditions and the following disclaimer in the documentation
-  and/or other materials provided with the distribution.
-
-* Neither the name of the copyright holders, nor those of its contributors
-  may be used to endorse or promote products derived from this software without
-  specific prior written permission.
-
-THIS SOFTWARE IS PROVIDED BY THE COPYRIGHT HOLDERS AND CONTRIBUTORS "AS IS" AND
-ANY EXPRESS OR IMPLIED WARRANTIES, INCLUDING, BUT NOT LIMITED TO, THE IMPLIED
-WARRANTIES OF MERCHANTABILITY AND FITNESS FOR A PARTICULAR PURPOSE ARE
-DISCLAIMED. IN NO EVENT SHALL THE COPYRIGHT HOLDER OR CONTRIBUTORS BE LIABLE
-FOR ANY DIRECT, INDIRECT, INCIDENTAL, SPECIAL, EXEMPLARY, OR CONSEQUENTIAL
-DAMAGES (INCLUDING, BUT NOT LIMITED TO, PROCUREMENT OF SUBSTITUTE GOODS OR
-SERVICES; LOSS OF USE, DATA, OR PROFITS; OR BUSINESS INTERRUPTION) HOWEVER
-CAUSED AND ON ANY THEORY OF LIABILITY, WHETHER IN CONTRACT, STRICT LIABILITY,
-OR TORT (INCLUDING NEGLIGENCE OR OTHERWISE) ARISING IN ANY WAY OUT OF THE USE
-OF THIS SOFTWARE, EVEN IF ADVISED OF THE POSSIBILITY OF SUCH DAMAGE.
diff --git a/venv/Lib/site-packages/colorama-0.4.3.dist-info/METADATA b/venv/Lib/site-packages/colorama-0.4.3.dist-info/METADATA
deleted file mode 100644
index c455cb5..0000000
--- a/venv/Lib/site-packages/colorama-0.4.3.dist-info/METADATA
+++ /dev/null
@@ -1,411 +0,0 @@
-Metadata-Version: 2.1
-Name: colorama
-Version: 0.4.3
-Summary: Cross-platform colored terminal text.
-Home-page: https://github.com/tartley/colorama
-Author: Jonathan Hartley
-Author-email: tartley@tartley.com
-Maintainer: Arnon Yaari
-License: BSD
-Keywords: color colour terminal text ansi windows crossplatform xplatform
-Platform: UNKNOWN
-Classifier: Development Status :: 5 - Production/Stable
-Classifier: Environment :: Console
-Classifier: Intended Audience :: Developers
-Classifier: License :: OSI Approved :: BSD License
-Classifier: Operating System :: OS Independent
-Classifier: Programming Language :: Python
-Classifier: Programming Language :: Python :: 2
-Classifier: Programming Language :: Python :: 2.7
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: 3.8
-Classifier: Programming Language :: Python :: Implementation :: CPython
-Classifier: Programming Language :: Python :: Implementation :: PyPy
-Classifier: Topic :: Terminals
-Requires-Python: >=2.7, !=3.0.*, !=3.1.*, !=3.2.*, !=3.3.*, !=3.4.*
-
-.. image:: https://img.shields.io/pypi/v/colorama.svg
-    :target: https://pypi.org/project/colorama/
-    :alt: Latest Version
-
-.. image:: https://img.shields.io/pypi/pyversions/colorama.svg
-    :target: https://pypi.org/project/colorama/
-    :alt: Supported Python versions
-
-.. image:: https://travis-ci.org/tartley/colorama.svg?branch=master
-    :target: https://travis-ci.org/tartley/colorama
-    :alt: Build Status
-
-Download and docs:
-    https://pypi.org/project/colorama/
-Source code & Development:
-    https://github.com/tartley/colorama
-Colorama for Enterprise:
-    https://github.com/tartley/colorama/blob/master/ENTERPRISE.md
-
-Description
-===========
-
-Makes ANSI escape character sequences (for producing colored terminal text and
-cursor positioning) work under MS Windows.
-
-ANSI escape character sequences have long been used to produce colored terminal
-text and cursor positioning on Unix and Macs. Colorama makes this work on
-Windows, too, by wrapping ``stdout``, stripping ANSI sequences it finds (which
-would appear as gobbledygook in the output), and converting them into the
-appropriate win32 calls to modify the state of the terminal. On other platforms,
-Colorama does nothing.
-
-Colorama also provides some shortcuts to help generate ANSI sequences
-but works fine in conjunction with any other ANSI sequence generation library,
-such as the venerable Termcolor (https://pypi.org/project/termcolor/)
-or the fabulous Blessings (https://pypi.org/project/blessings/).
-
-This has the upshot of providing a simple cross-platform API for printing
-colored terminal text from Python, and has the happy side-effect that existing
-applications or libraries which use ANSI sequences to produce colored output on
-Linux or Macs can now also work on Windows, simply by calling
-``colorama.init()``.
-
-An alternative approach is to install ``ansi.sys`` on Windows machines, which
-provides the same behaviour for all applications running in terminals. Colorama
-is intended for situations where that isn't easy (e.g., maybe your app doesn't
-have an installer.)
-
-Demo scripts in the source code repository print some colored text using
-ANSI sequences. Compare their output under Gnome-terminal's built in ANSI
-handling, versus on Windows Command-Prompt using Colorama:
-
-.. image:: https://github.com/tartley/colorama/raw/master/screenshots/ubuntu-demo.png
-    :width: 661
-    :height: 357
-    :alt: ANSI sequences on Ubuntu under gnome-terminal.
-
-.. image:: https://github.com/tartley/colorama/raw/master/screenshots/windows-demo.png
-    :width: 668
-    :height: 325
-    :alt: Same ANSI sequences on Windows, using Colorama.
-
-These screengrabs show that, on Windows, Colorama does not support ANSI 'dim
-text'; it looks the same as 'normal text'.
-
-
-License
-=======
-
-Copyright Jonathan Hartley & Arnon Yaari, 2013. BSD 3-Clause license; see LICENSE file.
-
-
-Dependencies
-============
-
-None, other than Python. Tested on Python 2.7, 3.5, 3.6, 3.7 and 3.8.
-
-Usage
-=====
-
-Initialisation
---------------
-
-Applications should initialise Colorama using:
-
-.. code-block:: python
-
-    from colorama import init
-    init()
-
-On Windows, calling ``init()`` will filter ANSI escape sequences out of any
-text sent to ``stdout`` or ``stderr``, and replace them with equivalent Win32
-calls.
-
-On other platforms, calling ``init()`` has no effect (unless you request other
-optional functionality; see "Init Keyword Args", below). By design, this permits
-applications to call ``init()`` unconditionally on all platforms, after which
-ANSI output should just work.
-
-To stop using colorama before your program exits, simply call ``deinit()``.
-This will restore ``stdout`` and ``stderr`` to their original values, so that
-Colorama is disabled. To resume using Colorama again, call ``reinit()``; it is
-cheaper to calling ``init()`` again (but does the same thing).
-
-
-Colored Output
---------------
-
-Cross-platform printing of colored text can then be done using Colorama's
-constant shorthand for ANSI escape sequences:
-
-.. code-block:: python
-
-    from colorama import Fore, Back, Style
-    print(Fore.RED + 'some red text')
-    print(Back.GREEN + 'and with a green background')
-    print(Style.DIM + 'and in dim text')
-    print(Style.RESET_ALL)
-    print('back to normal now')
-
-...or simply by manually printing ANSI sequences from your own code:
-
-.. code-block:: python
-
-    print('\033[31m' + 'some red text')
-    print('\033[39m') # and reset to default color
-
-...or, Colorama can be used happily in conjunction with existing ANSI libraries
-such as Termcolor:
-
-.. code-block:: python
-
-    from colorama import init
-    from termcolor import colored
-
-    # use Colorama to make Termcolor work on Windows too
-    init()
-
-    # then use Termcolor for all colored text output
-    print(colored('Hello, World!', 'green', 'on_red'))
-
-Available formatting constants are::
-
-    Fore: BLACK, RED, GREEN, YELLOW, BLUE, MAGENTA, CYAN, WHITE, RESET.
-    Back: BLACK, RED, GREEN, YELLOW, BLUE, MAGENTA, CYAN, WHITE, RESET.
-    Style: DIM, NORMAL, BRIGHT, RESET_ALL
-
-``Style.RESET_ALL`` resets foreground, background, and brightness. Colorama will
-perform this reset automatically on program exit.
-
-
-Cursor Positioning
-------------------
-
-ANSI codes to reposition the cursor are supported. See ``demos/demo06.py`` for
-an example of how to generate them.
-
-
-Init Keyword Args
------------------
-
-``init()`` accepts some ``**kwargs`` to override default behaviour.
-
-init(autoreset=False):
-    If you find yourself repeatedly sending reset sequences to turn off color
-    changes at the end of every print, then ``init(autoreset=True)`` will
-    automate that:
-
-    .. code-block:: python
-
-        from colorama import init
-        init(autoreset=True)
-        print(Fore.RED + 'some red text')
-        print('automatically back to default color again')
-
-init(strip=None):
-    Pass ``True`` or ``False`` to override whether ansi codes should be
-    stripped from the output. The default behaviour is to strip if on Windows
-    or if output is redirected (not a tty).
-
-init(convert=None):
-    Pass ``True`` or ``False`` to override whether to convert ANSI codes in the
-    output into win32 calls. The default behaviour is to convert if on Windows
-    and output is to a tty (terminal).
-
-init(wrap=True):
-    On Windows, colorama works by replacing ``sys.stdout`` and ``sys.stderr``
-    with proxy objects, which override the ``.write()`` method to do their work.
-    If this wrapping causes you problems, then this can be disabled by passing
-    ``init(wrap=False)``. The default behaviour is to wrap if ``autoreset`` or
-    ``strip`` or ``convert`` are True.
-
-    When wrapping is disabled, colored printing on non-Windows platforms will
-    continue to work as normal. To do cross-platform colored output, you can
-    use Colorama's ``AnsiToWin32`` proxy directly:
-
-    .. code-block:: python
-
-        import sys
-        from colorama import init, AnsiToWin32
-        init(wrap=False)
-        stream = AnsiToWin32(sys.stderr).stream
-
-        # Python 2
-        print >>stream, Fore.BLUE + 'blue text on stderr'
-
-        # Python 3
-        print(Fore.BLUE + 'blue text on stderr', file=stream)
-
-
-Installation
-=======================
-colorama is currently installable from PyPI:
-
-    pip install colorama
-
-colorama also can be installed by the conda package manager:
-
-    conda install -c anaconda colorama 
-
-
-Status & Known Problems
-=======================
-
-I've personally only tested it on Windows XP (CMD, Console2), Ubuntu
-(gnome-terminal, xterm), and OS X.
-
-Some presumably valid ANSI sequences aren't recognised (see details below),
-but to my knowledge nobody has yet complained about this. Puzzling.
-
-See outstanding issues and wishlist:
-https://github.com/tartley/colorama/issues
-
-If anything doesn't work for you, or doesn't do what you expected or hoped for,
-I'd love to hear about it on that issues list, would be delighted by patches,
-and would be happy to grant commit access to anyone who submits a working patch
-or two.
-
-
-Recognised ANSI Sequences
-=========================
-
-ANSI sequences generally take the form:
-
-    ESC [ <param> ; <param> ... <command>
-
-Where ``<param>`` is an integer, and ``<command>`` is a single letter. Zero or
-more params are passed to a ``<command>``. If no params are passed, it is
-generally synonymous with passing a single zero. No spaces exist in the
-sequence; they have been inserted here simply to read more easily.
-
-The only ANSI sequences that colorama converts into win32 calls are::
-
-    ESC [ 0 m       # reset all (colors and brightness)
-    ESC [ 1 m       # bright
-    ESC [ 2 m       # dim (looks same as normal brightness)
-    ESC [ 22 m      # normal brightness
-
-    # FOREGROUND:
-    ESC [ 30 m      # black
-    ESC [ 31 m      # red
-    ESC [ 32 m      # green
-    ESC [ 33 m      # yellow
-    ESC [ 34 m      # blue
-    ESC [ 35 m      # magenta
-    ESC [ 36 m      # cyan
-    ESC [ 37 m      # white
-    ESC [ 39 m      # reset
-
-    # BACKGROUND
-    ESC [ 40 m      # black
-    ESC [ 41 m      # red
-    ESC [ 42 m      # green
-    ESC [ 43 m      # yellow
-    ESC [ 44 m      # blue
-    ESC [ 45 m      # magenta
-    ESC [ 46 m      # cyan
-    ESC [ 47 m      # white
-    ESC [ 49 m      # reset
-
-    # cursor positioning
-    ESC [ y;x H     # position cursor at x across, y down
-    ESC [ y;x f     # position cursor at x across, y down
-    ESC [ n A       # move cursor n lines up
-    ESC [ n B       # move cursor n lines down
-    ESC [ n C       # move cursor n characters forward
-    ESC [ n D       # move cursor n characters backward
-
-    # clear the screen
-    ESC [ mode J    # clear the screen
-
-    # clear the line
-    ESC [ mode K    # clear the line
-
-Multiple numeric params to the ``'m'`` command can be combined into a single
-sequence::
-
-    ESC [ 36 ; 45 ; 1 m     # bright cyan text on magenta background
-
-All other ANSI sequences of the form ``ESC [ <param> ; <param> ... <command>``
-are silently stripped from the output on Windows.
-
-Any other form of ANSI sequence, such as single-character codes or alternative
-initial characters, are not recognised or stripped. It would be cool to add
-them though. Let me know if it would be useful for you, via the Issues on
-GitHub.
-
-
-Development
-===========
-
-Help and fixes welcome!
-
-Running tests requires:
-
-- Michael Foord's ``mock`` module to be installed.
-- Tests are written using 2010-era updates to ``unittest``
-
-To run tests::
-
-   python -m unittest discover -p *_test.py
-
-This, like a few other handy commands, is captured in a ``Makefile``.
-
-If you use nose to run the tests, you must pass the ``-s`` flag; otherwise,
-``nosetests`` applies its own proxy to ``stdout``, which confuses the unit
-tests.
-
-
-Professional support
-====================
-
-.. |tideliftlogo| image:: https://cdn2.hubspot.net/hubfs/4008838/website/logos/logos_for_download/Tidelift_primary-shorthand-logo.png
-   :alt: Tidelift
-   :target: https://tidelift.com/subscription/pkg/pypi-colorama?utm_source=pypi-colorama&utm_medium=referral&utm_campaign=readme
-
-.. list-table::
-   :widths: 10 100
-
-   * - |tideliftlogo|
-     - Professional support for colorama is available as part of the
-       `Tidelift Subscription`_.
-       Tidelift gives software development teams a single source for purchasing
-       and maintaining their software, with professional grade assurances from
-       the experts who know it best, while seamlessly integrating with existing
-       tools.
-
-.. _Tidelift Subscription: https://tidelift.com/subscription/pkg/pypi-colorama?utm_source=pypi-colorama&utm_medium=referral&utm_campaign=readme
-
-
-Thanks
-======
-* Marc Schlaich (schlamar) for a ``setup.py`` fix for Python2.5.
-* Marc Abramowitz, reported & fixed a crash on exit with closed ``stdout``,
-  providing a solution to issue #7's setuptools/distutils debate,
-  and other fixes.
-* User 'eryksun', for guidance on correctly instantiating ``ctypes.windll``.
-* Matthew McCormick for politely pointing out a longstanding crash on non-Win.
-* Ben Hoyt, for a magnificent fix under 64-bit Windows.
-* Jesse at Empty Square for submitting a fix for examples in the README.
-* User 'jamessp', an observant documentation fix for cursor positioning.
-* User 'vaal1239', Dave Mckee & Lackner Kristof for a tiny but much-needed Win7
-  fix.
-* Julien Stuyck, for wisely suggesting Python3 compatible updates to README.
-* Daniel Griffith for multiple fabulous patches.
-* Oscar Lesta for a valuable fix to stop ANSI chars being sent to non-tty
-  output.
-* Roger Binns, for many suggestions, valuable feedback, & bug reports.
-* Tim Golden for thought and much appreciated feedback on the initial idea.
-* User 'Zearin' for updates to the README file.
-* John Szakmeister for adding support for light colors
-* Charles Merriam for adding documentation to demos
-* Jurko for a fix on 64-bit Windows CPython2.5 w/o ctypes
-* Florian Bruhin for a fix when stdout or stderr are None
-* Thomas Weininger for fixing ValueError on Windows
-* Remi Rampin for better Github integration and fixes to the README file
-* Simeon Visser for closing a file handle using 'with' and updating classifiers
-  to include Python 3.3 and 3.4
-* Andy Neff for fixing RESET of LIGHT_EX colors.
-* Jonathan Hartley for the initial idea and implementation.
-
-
diff --git a/venv/Lib/site-packages/colorama-0.4.3.dist-info/RECORD b/venv/Lib/site-packages/colorama-0.4.3.dist-info/RECORD
deleted file mode 100644
index 64d8939..0000000
--- a/venv/Lib/site-packages/colorama-0.4.3.dist-info/RECORD
+++ /dev/null
@@ -1,18 +0,0 @@
-colorama-0.4.3.dist-info/INSTALLER,sha256=zuuue4knoyJ-UwPPXg8fezS7VCrXJQrAP7zeNuwvFQg,4
-colorama-0.4.3.dist-info/LICENSE.txt,sha256=ysNcAmhuXQSlpxQL-zs25zrtSWZW6JEQLkKIhteTAxg,1491
-colorama-0.4.3.dist-info/METADATA,sha256=-ovqULHfBHs9pV2e_Ua8-w2VSVLno-6x36SXSTsWvSc,14432
-colorama-0.4.3.dist-info/RECORD,,
-colorama-0.4.3.dist-info/WHEEL,sha256=8zNYZbwQSXoB9IfXOjPfeNwvAsALAjffgk27FqvCWbo,110
-colorama-0.4.3.dist-info/top_level.txt,sha256=_Kx6-Cni2BT1PEATPhrSRxo0d7kSgfBbHf5o7IF1ABw,9
-colorama/__init__.py,sha256=DqjXH9URVP3IJwmMt7peYw50ns1RNAymIB9-XdPEFV8,239
-colorama/__pycache__/__init__.cpython-37.pyc,,
-colorama/__pycache__/ansi.cpython-37.pyc,,
-colorama/__pycache__/ansitowin32.cpython-37.pyc,,
-colorama/__pycache__/initialise.cpython-37.pyc,,
-colorama/__pycache__/win32.cpython-37.pyc,,
-colorama/__pycache__/winterm.cpython-37.pyc,,
-colorama/ansi.py,sha256=Fi0un-QLqRm-v7o_nKiOqyC8PapBJK7DLV_q9LKtTO0,2524
-colorama/ansitowin32.py,sha256=u8QaqdqS_xYSfNkPM1eRJLHz6JMWPodaJaP0mxgHCDc,10462
-colorama/initialise.py,sha256=PprovDNxMTrvoNHFcL2NZjpH2XzDc8BLxLxiErfUl4k,1915
-colorama/win32.py,sha256=bJ8Il9jwaBN5BJ8bmN6FoYZ1QYuMKv2j8fGrXh7TJjw,5404
-colorama/winterm.py,sha256=2y_2b7Zsv34feAsP67mLOVc-Bgq51mdYGo571VprlrM,6438
diff --git a/venv/Lib/site-packages/colorama-0.4.3.dist-info/WHEEL b/venv/Lib/site-packages/colorama-0.4.3.dist-info/WHEEL
deleted file mode 100644
index 8b701e9..0000000
--- a/venv/Lib/site-packages/colorama-0.4.3.dist-info/WHEEL
+++ /dev/null
@@ -1,6 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.33.6)
-Root-Is-Purelib: true
-Tag: py2-none-any
-Tag: py3-none-any
-
diff --git a/venv/Lib/site-packages/colorama-0.4.3.dist-info/top_level.txt b/venv/Lib/site-packages/colorama-0.4.3.dist-info/top_level.txt
deleted file mode 100644
index 3fcfb51..0000000
--- a/venv/Lib/site-packages/colorama-0.4.3.dist-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-colorama
diff --git a/venv/Lib/site-packages/colorama/__init__.py b/venv/Lib/site-packages/colorama/__init__.py
deleted file mode 100644
index 34c263c..0000000
--- a/venv/Lib/site-packages/colorama/__init__.py
+++ /dev/null
@@ -1,6 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-from .initialise import init, deinit, reinit, colorama_text
-from .ansi import Fore, Back, Style, Cursor
-from .ansitowin32 import AnsiToWin32
-
-__version__ = '0.4.3'
diff --git a/venv/Lib/site-packages/colorama/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/colorama/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 270deaf..0000000
--- a/venv/Lib/site-packages/colorama/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/colorama/__pycache__/ansi.cpython-37.pyc b/venv/Lib/site-packages/colorama/__pycache__/ansi.cpython-37.pyc
deleted file mode 100644
index c0942e2..0000000
--- a/venv/Lib/site-packages/colorama/__pycache__/ansi.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/colorama/__pycache__/ansitowin32.cpython-37.pyc b/venv/Lib/site-packages/colorama/__pycache__/ansitowin32.cpython-37.pyc
deleted file mode 100644
index 152004e..0000000
--- a/venv/Lib/site-packages/colorama/__pycache__/ansitowin32.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/colorama/__pycache__/initialise.cpython-37.pyc b/venv/Lib/site-packages/colorama/__pycache__/initialise.cpython-37.pyc
deleted file mode 100644
index 671073a..0000000
--- a/venv/Lib/site-packages/colorama/__pycache__/initialise.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/colorama/__pycache__/win32.cpython-37.pyc b/venv/Lib/site-packages/colorama/__pycache__/win32.cpython-37.pyc
deleted file mode 100644
index 2982108..0000000
--- a/venv/Lib/site-packages/colorama/__pycache__/win32.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/colorama/__pycache__/winterm.cpython-37.pyc b/venv/Lib/site-packages/colorama/__pycache__/winterm.cpython-37.pyc
deleted file mode 100644
index 1ebf75c..0000000
--- a/venv/Lib/site-packages/colorama/__pycache__/winterm.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/colorama/ansi.py b/venv/Lib/site-packages/colorama/ansi.py
deleted file mode 100644
index 7877658..0000000
--- a/venv/Lib/site-packages/colorama/ansi.py
+++ /dev/null
@@ -1,102 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-'''
-This module generates ANSI character codes to printing colors to terminals.
-See: http://en.wikipedia.org/wiki/ANSI_escape_code
-'''
-
-CSI = '\033['
-OSC = '\033]'
-BEL = '\007'
-
-
-def code_to_chars(code):
-    return CSI + str(code) + 'm'
-
-def set_title(title):
-    return OSC + '2;' + title + BEL
-
-def clear_screen(mode=2):
-    return CSI + str(mode) + 'J'
-
-def clear_line(mode=2):
-    return CSI + str(mode) + 'K'
-
-
-class AnsiCodes(object):
-    def __init__(self):
-        # the subclasses declare class attributes which are numbers.
-        # Upon instantiation we define instance attributes, which are the same
-        # as the class attributes but wrapped with the ANSI escape sequence
-        for name in dir(self):
-            if not name.startswith('_'):
-                value = getattr(self, name)
-                setattr(self, name, code_to_chars(value))
-
-
-class AnsiCursor(object):
-    def UP(self, n=1):
-        return CSI + str(n) + 'A'
-    def DOWN(self, n=1):
-        return CSI + str(n) + 'B'
-    def FORWARD(self, n=1):
-        return CSI + str(n) + 'C'
-    def BACK(self, n=1):
-        return CSI + str(n) + 'D'
-    def POS(self, x=1, y=1):
-        return CSI + str(y) + ';' + str(x) + 'H'
-
-
-class AnsiFore(AnsiCodes):
-    BLACK           = 30
-    RED             = 31
-    GREEN           = 32
-    YELLOW          = 33
-    BLUE            = 34
-    MAGENTA         = 35
-    CYAN            = 36
-    WHITE           = 37
-    RESET           = 39
-
-    # These are fairly well supported, but not part of the standard.
-    LIGHTBLACK_EX   = 90
-    LIGHTRED_EX     = 91
-    LIGHTGREEN_EX   = 92
-    LIGHTYELLOW_EX  = 93
-    LIGHTBLUE_EX    = 94
-    LIGHTMAGENTA_EX = 95
-    LIGHTCYAN_EX    = 96
-    LIGHTWHITE_EX   = 97
-
-
-class AnsiBack(AnsiCodes):
-    BLACK           = 40
-    RED             = 41
-    GREEN           = 42
-    YELLOW          = 43
-    BLUE            = 44
-    MAGENTA         = 45
-    CYAN            = 46
-    WHITE           = 47
-    RESET           = 49
-
-    # These are fairly well supported, but not part of the standard.
-    LIGHTBLACK_EX   = 100
-    LIGHTRED_EX     = 101
-    LIGHTGREEN_EX   = 102
-    LIGHTYELLOW_EX  = 103
-    LIGHTBLUE_EX    = 104
-    LIGHTMAGENTA_EX = 105
-    LIGHTCYAN_EX    = 106
-    LIGHTWHITE_EX   = 107
-
-
-class AnsiStyle(AnsiCodes):
-    BRIGHT    = 1
-    DIM       = 2
-    NORMAL    = 22
-    RESET_ALL = 0
-
-Fore   = AnsiFore()
-Back   = AnsiBack()
-Style  = AnsiStyle()
-Cursor = AnsiCursor()
diff --git a/venv/Lib/site-packages/colorama/ansitowin32.py b/venv/Lib/site-packages/colorama/ansitowin32.py
deleted file mode 100644
index 359c92b..0000000
--- a/venv/Lib/site-packages/colorama/ansitowin32.py
+++ /dev/null
@@ -1,257 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-import re
-import sys
-import os
-
-from .ansi import AnsiFore, AnsiBack, AnsiStyle, Style
-from .winterm import WinTerm, WinColor, WinStyle
-from .win32 import windll, winapi_test
-
-
-winterm = None
-if windll is not None:
-    winterm = WinTerm()
-
-
-class StreamWrapper(object):
-    '''
-    Wraps a stream (such as stdout), acting as a transparent proxy for all
-    attribute access apart from method 'write()', which is delegated to our
-    Converter instance.
-    '''
-    def __init__(self, wrapped, converter):
-        # double-underscore everything to prevent clashes with names of
-        # attributes on the wrapped stream object.
-        self.__wrapped = wrapped
-        self.__convertor = converter
-
-    def __getattr__(self, name):
-        return getattr(self.__wrapped, name)
-
-    def __enter__(self, *args, **kwargs):
-        # special method lookup bypasses __getattr__/__getattribute__, see
-        # https://stackoverflow.com/questions/12632894/why-doesnt-getattr-work-with-exit
-        # thus, contextlib magic methods are not proxied via __getattr__
-        return self.__wrapped.__enter__(*args, **kwargs)
-
-    def __exit__(self, *args, **kwargs):
-        return self.__wrapped.__exit__(*args, **kwargs)
-
-    def write(self, text):
-        self.__convertor.write(text)
-
-    def isatty(self):
-        stream = self.__wrapped
-        if 'PYCHARM_HOSTED' in os.environ:
-            if stream is not None and (stream is sys.__stdout__ or stream is sys.__stderr__):
-                return True
-        try:
-            stream_isatty = stream.isatty
-        except AttributeError:
-            return False
-        else:
-            return stream_isatty()
-
-    @property
-    def closed(self):
-        stream = self.__wrapped
-        try:
-            return stream.closed
-        except AttributeError:
-            return True
-
-
-class AnsiToWin32(object):
-    '''
-    Implements a 'write()' method which, on Windows, will strip ANSI character
-    sequences from the text, and if outputting to a tty, will convert them into
-    win32 function calls.
-    '''
-    ANSI_CSI_RE = re.compile('\001?\033\\[((?:\\d|;)*)([a-zA-Z])\002?')   # Control Sequence Introducer
-    ANSI_OSC_RE = re.compile('\001?\033\\]((?:.|;)*?)(\x07)\002?')        # Operating System Command
-
-    def __init__(self, wrapped, convert=None, strip=None, autoreset=False):
-        # The wrapped stream (normally sys.stdout or sys.stderr)
-        self.wrapped = wrapped
-
-        # should we reset colors to defaults after every .write()
-        self.autoreset = autoreset
-
-        # create the proxy wrapping our output stream
-        self.stream = StreamWrapper(wrapped, self)
-
-        on_windows = os.name == 'nt'
-        # We test if the WinAPI works, because even if we are on Windows
-        # we may be using a terminal that doesn't support the WinAPI
-        # (e.g. Cygwin Terminal). In this case it's up to the terminal
-        # to support the ANSI codes.
-        conversion_supported = on_windows and winapi_test()
-
-        # should we strip ANSI sequences from our output?
-        if strip is None:
-            strip = conversion_supported or (not self.stream.closed and not self.stream.isatty())
-        self.strip = strip
-
-        # should we should convert ANSI sequences into win32 calls?
-        if convert is None:
-            convert = conversion_supported and not self.stream.closed and self.stream.isatty()
-        self.convert = convert
-
-        # dict of ansi codes to win32 functions and parameters
-        self.win32_calls = self.get_win32_calls()
-
-        # are we wrapping stderr?
-        self.on_stderr = self.wrapped is sys.stderr
-
-    def should_wrap(self):
-        '''
-        True if this class is actually needed. If false, then the output
-        stream will not be affected, nor will win32 calls be issued, so
-        wrapping stdout is not actually required. This will generally be
-        False on non-Windows platforms, unless optional functionality like
-        autoreset has been requested using kwargs to init()
-        '''
-        return self.convert or self.strip or self.autoreset
-
-    def get_win32_calls(self):
-        if self.convert and winterm:
-            return {
-                AnsiStyle.RESET_ALL: (winterm.reset_all, ),
-                AnsiStyle.BRIGHT: (winterm.style, WinStyle.BRIGHT),
-                AnsiStyle.DIM: (winterm.style, WinStyle.NORMAL),
-                AnsiStyle.NORMAL: (winterm.style, WinStyle.NORMAL),
-                AnsiFore.BLACK: (winterm.fore, WinColor.BLACK),
-                AnsiFore.RED: (winterm.fore, WinColor.RED),
-                AnsiFore.GREEN: (winterm.fore, WinColor.GREEN),
-                AnsiFore.YELLOW: (winterm.fore, WinColor.YELLOW),
-                AnsiFore.BLUE: (winterm.fore, WinColor.BLUE),
-                AnsiFore.MAGENTA: (winterm.fore, WinColor.MAGENTA),
-                AnsiFore.CYAN: (winterm.fore, WinColor.CYAN),
-                AnsiFore.WHITE: (winterm.fore, WinColor.GREY),
-                AnsiFore.RESET: (winterm.fore, ),
-                AnsiFore.LIGHTBLACK_EX: (winterm.fore, WinColor.BLACK, True),
-                AnsiFore.LIGHTRED_EX: (winterm.fore, WinColor.RED, True),
-                AnsiFore.LIGHTGREEN_EX: (winterm.fore, WinColor.GREEN, True),
-                AnsiFore.LIGHTYELLOW_EX: (winterm.fore, WinColor.YELLOW, True),
-                AnsiFore.LIGHTBLUE_EX: (winterm.fore, WinColor.BLUE, True),
-                AnsiFore.LIGHTMAGENTA_EX: (winterm.fore, WinColor.MAGENTA, True),
-                AnsiFore.LIGHTCYAN_EX: (winterm.fore, WinColor.CYAN, True),
-                AnsiFore.LIGHTWHITE_EX: (winterm.fore, WinColor.GREY, True),
-                AnsiBack.BLACK: (winterm.back, WinColor.BLACK),
-                AnsiBack.RED: (winterm.back, WinColor.RED),
-                AnsiBack.GREEN: (winterm.back, WinColor.GREEN),
-                AnsiBack.YELLOW: (winterm.back, WinColor.YELLOW),
-                AnsiBack.BLUE: (winterm.back, WinColor.BLUE),
-                AnsiBack.MAGENTA: (winterm.back, WinColor.MAGENTA),
-                AnsiBack.CYAN: (winterm.back, WinColor.CYAN),
-                AnsiBack.WHITE: (winterm.back, WinColor.GREY),
-                AnsiBack.RESET: (winterm.back, ),
-                AnsiBack.LIGHTBLACK_EX: (winterm.back, WinColor.BLACK, True),
-                AnsiBack.LIGHTRED_EX: (winterm.back, WinColor.RED, True),
-                AnsiBack.LIGHTGREEN_EX: (winterm.back, WinColor.GREEN, True),
-                AnsiBack.LIGHTYELLOW_EX: (winterm.back, WinColor.YELLOW, True),
-                AnsiBack.LIGHTBLUE_EX: (winterm.back, WinColor.BLUE, True),
-                AnsiBack.LIGHTMAGENTA_EX: (winterm.back, WinColor.MAGENTA, True),
-                AnsiBack.LIGHTCYAN_EX: (winterm.back, WinColor.CYAN, True),
-                AnsiBack.LIGHTWHITE_EX: (winterm.back, WinColor.GREY, True),
-            }
-        return dict()
-
-    def write(self, text):
-        if self.strip or self.convert:
-            self.write_and_convert(text)
-        else:
-            self.wrapped.write(text)
-            self.wrapped.flush()
-        if self.autoreset:
-            self.reset_all()
-
-
-    def reset_all(self):
-        if self.convert:
-            self.call_win32('m', (0,))
-        elif not self.strip and not self.stream.closed:
-            self.wrapped.write(Style.RESET_ALL)
-
-
-    def write_and_convert(self, text):
-        '''
-        Write the given text to our wrapped stream, stripping any ANSI
-        sequences from the text, and optionally converting them into win32
-        calls.
-        '''
-        cursor = 0
-        text = self.convert_osc(text)
-        for match in self.ANSI_CSI_RE.finditer(text):
-            start, end = match.span()
-            self.write_plain_text(text, cursor, start)
-            self.convert_ansi(*match.groups())
-            cursor = end
-        self.write_plain_text(text, cursor, len(text))
-
-
-    def write_plain_text(self, text, start, end):
-        if start < end:
-            self.wrapped.write(text[start:end])
-            self.wrapped.flush()
-
-
-    def convert_ansi(self, paramstring, command):
-        if self.convert:
-            params = self.extract_params(command, paramstring)
-            self.call_win32(command, params)
-
-
-    def extract_params(self, command, paramstring):
-        if command in 'Hf':
-            params = tuple(int(p) if len(p) != 0 else 1 for p in paramstring.split(';'))
-            while len(params) < 2:
-                # defaults:
-                params = params + (1,)
-        else:
-            params = tuple(int(p) for p in paramstring.split(';') if len(p) != 0)
-            if len(params) == 0:
-                # defaults:
-                if command in 'JKm':
-                    params = (0,)
-                elif command in 'ABCD':
-                    params = (1,)
-
-        return params
-
-
-    def call_win32(self, command, params):
-        if command == 'm':
-            for param in params:
-                if param in self.win32_calls:
-                    func_args = self.win32_calls[param]
-                    func = func_args[0]
-                    args = func_args[1:]
-                    kwargs = dict(on_stderr=self.on_stderr)
-                    func(*args, **kwargs)
-        elif command in 'J':
-            winterm.erase_screen(params[0], on_stderr=self.on_stderr)
-        elif command in 'K':
-            winterm.erase_line(params[0], on_stderr=self.on_stderr)
-        elif command in 'Hf':     # cursor position - absolute
-            winterm.set_cursor_position(params, on_stderr=self.on_stderr)
-        elif command in 'ABCD':   # cursor position - relative
-            n = params[0]
-            # A - up, B - down, C - forward, D - back
-            x, y = {'A': (0, -n), 'B': (0, n), 'C': (n, 0), 'D': (-n, 0)}[command]
-            winterm.cursor_adjust(x, y, on_stderr=self.on_stderr)
-
-
-    def convert_osc(self, text):
-        for match in self.ANSI_OSC_RE.finditer(text):
-            start, end = match.span()
-            text = text[:start] + text[end:]
-            paramstring, command = match.groups()
-            if command in '\x07':       # \x07 = BEL
-                params = paramstring.split(";")
-                # 0 - change title and icon (we will only change title)
-                # 1 - change icon (we don't support this)
-                # 2 - change title
-                if params[0] in '02':
-                    winterm.set_title(params[1])
-        return text
diff --git a/venv/Lib/site-packages/colorama/initialise.py b/venv/Lib/site-packages/colorama/initialise.py
deleted file mode 100644
index 430d066..0000000
--- a/venv/Lib/site-packages/colorama/initialise.py
+++ /dev/null
@@ -1,80 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-import atexit
-import contextlib
-import sys
-
-from .ansitowin32 import AnsiToWin32
-
-
-orig_stdout = None
-orig_stderr = None
-
-wrapped_stdout = None
-wrapped_stderr = None
-
-atexit_done = False
-
-
-def reset_all():
-    if AnsiToWin32 is not None:    # Issue #74: objects might become None at exit
-        AnsiToWin32(orig_stdout).reset_all()
-
-
-def init(autoreset=False, convert=None, strip=None, wrap=True):
-
-    if not wrap and any([autoreset, convert, strip]):
-        raise ValueError('wrap=False conflicts with any other arg=True')
-
-    global wrapped_stdout, wrapped_stderr
-    global orig_stdout, orig_stderr
-
-    orig_stdout = sys.stdout
-    orig_stderr = sys.stderr
-
-    if sys.stdout is None:
-        wrapped_stdout = None
-    else:
-        sys.stdout = wrapped_stdout = \
-            wrap_stream(orig_stdout, convert, strip, autoreset, wrap)
-    if sys.stderr is None:
-        wrapped_stderr = None
-    else:
-        sys.stderr = wrapped_stderr = \
-            wrap_stream(orig_stderr, convert, strip, autoreset, wrap)
-
-    global atexit_done
-    if not atexit_done:
-        atexit.register(reset_all)
-        atexit_done = True
-
-
-def deinit():
-    if orig_stdout is not None:
-        sys.stdout = orig_stdout
-    if orig_stderr is not None:
-        sys.stderr = orig_stderr
-
-
-@contextlib.contextmanager
-def colorama_text(*args, **kwargs):
-    init(*args, **kwargs)
-    try:
-        yield
-    finally:
-        deinit()
-
-
-def reinit():
-    if wrapped_stdout is not None:
-        sys.stdout = wrapped_stdout
-    if wrapped_stderr is not None:
-        sys.stderr = wrapped_stderr
-
-
-def wrap_stream(stream, convert, strip, autoreset, wrap):
-    if wrap:
-        wrapper = AnsiToWin32(stream,
-            convert=convert, strip=strip, autoreset=autoreset)
-        if wrapper.should_wrap():
-            stream = wrapper.stream
-    return stream
diff --git a/venv/Lib/site-packages/colorama/win32.py b/venv/Lib/site-packages/colorama/win32.py
deleted file mode 100644
index c2d8360..0000000
--- a/venv/Lib/site-packages/colorama/win32.py
+++ /dev/null
@@ -1,152 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-
-# from winbase.h
-STDOUT = -11
-STDERR = -12
-
-try:
-    import ctypes
-    from ctypes import LibraryLoader
-    windll = LibraryLoader(ctypes.WinDLL)
-    from ctypes import wintypes
-except (AttributeError, ImportError):
-    windll = None
-    SetConsoleTextAttribute = lambda *_: None
-    winapi_test = lambda *_: None
-else:
-    from ctypes import byref, Structure, c_char, POINTER
-
-    COORD = wintypes._COORD
-
-    class CONSOLE_SCREEN_BUFFER_INFO(Structure):
-        """struct in wincon.h."""
-        _fields_ = [
-            ("dwSize", COORD),
-            ("dwCursorPosition", COORD),
-            ("wAttributes", wintypes.WORD),
-            ("srWindow", wintypes.SMALL_RECT),
-            ("dwMaximumWindowSize", COORD),
-        ]
-        def __str__(self):
-            return '(%d,%d,%d,%d,%d,%d,%d,%d,%d,%d,%d)' % (
-                self.dwSize.Y, self.dwSize.X
-                , self.dwCursorPosition.Y, self.dwCursorPosition.X
-                , self.wAttributes
-                , self.srWindow.Top, self.srWindow.Left, self.srWindow.Bottom, self.srWindow.Right
-                , self.dwMaximumWindowSize.Y, self.dwMaximumWindowSize.X
-            )
-
-    _GetStdHandle = windll.kernel32.GetStdHandle
-    _GetStdHandle.argtypes = [
-        wintypes.DWORD,
-    ]
-    _GetStdHandle.restype = wintypes.HANDLE
-
-    _GetConsoleScreenBufferInfo = windll.kernel32.GetConsoleScreenBufferInfo
-    _GetConsoleScreenBufferInfo.argtypes = [
-        wintypes.HANDLE,
-        POINTER(CONSOLE_SCREEN_BUFFER_INFO),
-    ]
-    _GetConsoleScreenBufferInfo.restype = wintypes.BOOL
-
-    _SetConsoleTextAttribute = windll.kernel32.SetConsoleTextAttribute
-    _SetConsoleTextAttribute.argtypes = [
-        wintypes.HANDLE,
-        wintypes.WORD,
-    ]
-    _SetConsoleTextAttribute.restype = wintypes.BOOL
-
-    _SetConsoleCursorPosition = windll.kernel32.SetConsoleCursorPosition
-    _SetConsoleCursorPosition.argtypes = [
-        wintypes.HANDLE,
-        COORD,
-    ]
-    _SetConsoleCursorPosition.restype = wintypes.BOOL
-
-    _FillConsoleOutputCharacterA = windll.kernel32.FillConsoleOutputCharacterA
-    _FillConsoleOutputCharacterA.argtypes = [
-        wintypes.HANDLE,
-        c_char,
-        wintypes.DWORD,
-        COORD,
-        POINTER(wintypes.DWORD),
-    ]
-    _FillConsoleOutputCharacterA.restype = wintypes.BOOL
-
-    _FillConsoleOutputAttribute = windll.kernel32.FillConsoleOutputAttribute
-    _FillConsoleOutputAttribute.argtypes = [
-        wintypes.HANDLE,
-        wintypes.WORD,
-        wintypes.DWORD,
-        COORD,
-        POINTER(wintypes.DWORD),
-    ]
-    _FillConsoleOutputAttribute.restype = wintypes.BOOL
-
-    _SetConsoleTitleW = windll.kernel32.SetConsoleTitleW
-    _SetConsoleTitleW.argtypes = [
-        wintypes.LPCWSTR
-    ]
-    _SetConsoleTitleW.restype = wintypes.BOOL
-
-    def _winapi_test(handle):
-        csbi = CONSOLE_SCREEN_BUFFER_INFO()
-        success = _GetConsoleScreenBufferInfo(
-            handle, byref(csbi))
-        return bool(success)
-
-    def winapi_test():
-        return any(_winapi_test(h) for h in
-                   (_GetStdHandle(STDOUT), _GetStdHandle(STDERR)))
-
-    def GetConsoleScreenBufferInfo(stream_id=STDOUT):
-        handle = _GetStdHandle(stream_id)
-        csbi = CONSOLE_SCREEN_BUFFER_INFO()
-        success = _GetConsoleScreenBufferInfo(
-            handle, byref(csbi))
-        return csbi
-
-    def SetConsoleTextAttribute(stream_id, attrs):
-        handle = _GetStdHandle(stream_id)
-        return _SetConsoleTextAttribute(handle, attrs)
-
-    def SetConsoleCursorPosition(stream_id, position, adjust=True):
-        position = COORD(*position)
-        # If the position is out of range, do nothing.
-        if position.Y <= 0 or position.X <= 0:
-            return
-        # Adjust for Windows' SetConsoleCursorPosition:
-        #    1. being 0-based, while ANSI is 1-based.
-        #    2. expecting (x,y), while ANSI uses (y,x).
-        adjusted_position = COORD(position.Y - 1, position.X - 1)
-        if adjust:
-            # Adjust for viewport's scroll position
-            sr = GetConsoleScreenBufferInfo(STDOUT).srWindow
-            adjusted_position.Y += sr.Top
-            adjusted_position.X += sr.Left
-        # Resume normal processing
-        handle = _GetStdHandle(stream_id)
-        return _SetConsoleCursorPosition(handle, adjusted_position)
-
-    def FillConsoleOutputCharacter(stream_id, char, length, start):
-        handle = _GetStdHandle(stream_id)
-        char = c_char(char.encode())
-        length = wintypes.DWORD(length)
-        num_written = wintypes.DWORD(0)
-        # Note that this is hard-coded for ANSI (vs wide) bytes.
-        success = _FillConsoleOutputCharacterA(
-            handle, char, length, start, byref(num_written))
-        return num_written.value
-
-    def FillConsoleOutputAttribute(stream_id, attr, length, start):
-        ''' FillConsoleOutputAttribute( hConsole, csbi.wAttributes, dwConSize, coordScreen, &cCharsWritten )'''
-        handle = _GetStdHandle(stream_id)
-        attribute = wintypes.WORD(attr)
-        length = wintypes.DWORD(length)
-        num_written = wintypes.DWORD(0)
-        # Note that this is hard-coded for ANSI (vs wide) bytes.
-        return _FillConsoleOutputAttribute(
-            handle, attribute, length, start, byref(num_written))
-
-    def SetConsoleTitle(title):
-        return _SetConsoleTitleW(title)
diff --git a/venv/Lib/site-packages/colorama/winterm.py b/venv/Lib/site-packages/colorama/winterm.py
deleted file mode 100644
index 0fdb4ec..0000000
--- a/venv/Lib/site-packages/colorama/winterm.py
+++ /dev/null
@@ -1,169 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-from . import win32
-
-
-# from wincon.h
-class WinColor(object):
-    BLACK   = 0
-    BLUE    = 1
-    GREEN   = 2
-    CYAN    = 3
-    RED     = 4
-    MAGENTA = 5
-    YELLOW  = 6
-    GREY    = 7
-
-# from wincon.h
-class WinStyle(object):
-    NORMAL              = 0x00 # dim text, dim background
-    BRIGHT              = 0x08 # bright text, dim background
-    BRIGHT_BACKGROUND   = 0x80 # dim text, bright background
-
-class WinTerm(object):
-
-    def __init__(self):
-        self._default = win32.GetConsoleScreenBufferInfo(win32.STDOUT).wAttributes
-        self.set_attrs(self._default)
-        self._default_fore = self._fore
-        self._default_back = self._back
-        self._default_style = self._style
-        # In order to emulate LIGHT_EX in windows, we borrow the BRIGHT style.
-        # So that LIGHT_EX colors and BRIGHT style do not clobber each other,
-        # we track them separately, since LIGHT_EX is overwritten by Fore/Back
-        # and BRIGHT is overwritten by Style codes.
-        self._light = 0
-
-    def get_attrs(self):
-        return self._fore + self._back * 16 + (self._style | self._light)
-
-    def set_attrs(self, value):
-        self._fore = value & 7
-        self._back = (value >> 4) & 7
-        self._style = value & (WinStyle.BRIGHT | WinStyle.BRIGHT_BACKGROUND)
-
-    def reset_all(self, on_stderr=None):
-        self.set_attrs(self._default)
-        self.set_console(attrs=self._default)
-        self._light = 0
-
-    def fore(self, fore=None, light=False, on_stderr=False):
-        if fore is None:
-            fore = self._default_fore
-        self._fore = fore
-        # Emulate LIGHT_EX with BRIGHT Style
-        if light:
-            self._light |= WinStyle.BRIGHT
-        else:
-            self._light &= ~WinStyle.BRIGHT
-        self.set_console(on_stderr=on_stderr)
-
-    def back(self, back=None, light=False, on_stderr=False):
-        if back is None:
-            back = self._default_back
-        self._back = back
-        # Emulate LIGHT_EX with BRIGHT_BACKGROUND Style
-        if light:
-            self._light |= WinStyle.BRIGHT_BACKGROUND
-        else:
-            self._light &= ~WinStyle.BRIGHT_BACKGROUND
-        self.set_console(on_stderr=on_stderr)
-
-    def style(self, style=None, on_stderr=False):
-        if style is None:
-            style = self._default_style
-        self._style = style
-        self.set_console(on_stderr=on_stderr)
-
-    def set_console(self, attrs=None, on_stderr=False):
-        if attrs is None:
-            attrs = self.get_attrs()
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        win32.SetConsoleTextAttribute(handle, attrs)
-
-    def get_position(self, handle):
-        position = win32.GetConsoleScreenBufferInfo(handle).dwCursorPosition
-        # Because Windows coordinates are 0-based,
-        # and win32.SetConsoleCursorPosition expects 1-based.
-        position.X += 1
-        position.Y += 1
-        return position
-
-    def set_cursor_position(self, position=None, on_stderr=False):
-        if position is None:
-            # I'm not currently tracking the position, so there is no default.
-            # position = self.get_position()
-            return
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        win32.SetConsoleCursorPosition(handle, position)
-
-    def cursor_adjust(self, x, y, on_stderr=False):
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        position = self.get_position(handle)
-        adjusted_position = (position.Y + y, position.X + x)
-        win32.SetConsoleCursorPosition(handle, adjusted_position, adjust=False)
-
-    def erase_screen(self, mode=0, on_stderr=False):
-        # 0 should clear from the cursor to the end of the screen.
-        # 1 should clear from the cursor to the beginning of the screen.
-        # 2 should clear the entire screen, and move cursor to (1,1)
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        csbi = win32.GetConsoleScreenBufferInfo(handle)
-        # get the number of character cells in the current buffer
-        cells_in_screen = csbi.dwSize.X * csbi.dwSize.Y
-        # get number of character cells before current cursor position
-        cells_before_cursor = csbi.dwSize.X * csbi.dwCursorPosition.Y + csbi.dwCursorPosition.X
-        if mode == 0:
-            from_coord = csbi.dwCursorPosition
-            cells_to_erase = cells_in_screen - cells_before_cursor
-        elif mode == 1:
-            from_coord = win32.COORD(0, 0)
-            cells_to_erase = cells_before_cursor
-        elif mode == 2:
-            from_coord = win32.COORD(0, 0)
-            cells_to_erase = cells_in_screen
-        else:
-            # invalid mode
-            return
-        # fill the entire screen with blanks
-        win32.FillConsoleOutputCharacter(handle, ' ', cells_to_erase, from_coord)
-        # now set the buffer's attributes accordingly
-        win32.FillConsoleOutputAttribute(handle, self.get_attrs(), cells_to_erase, from_coord)
-        if mode == 2:
-            # put the cursor where needed
-            win32.SetConsoleCursorPosition(handle, (1, 1))
-
-    def erase_line(self, mode=0, on_stderr=False):
-        # 0 should clear from the cursor to the end of the line.
-        # 1 should clear from the cursor to the beginning of the line.
-        # 2 should clear the entire line.
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        csbi = win32.GetConsoleScreenBufferInfo(handle)
-        if mode == 0:
-            from_coord = csbi.dwCursorPosition
-            cells_to_erase = csbi.dwSize.X - csbi.dwCursorPosition.X
-        elif mode == 1:
-            from_coord = win32.COORD(0, csbi.dwCursorPosition.Y)
-            cells_to_erase = csbi.dwCursorPosition.X
-        elif mode == 2:
-            from_coord = win32.COORD(0, csbi.dwCursorPosition.Y)
-            cells_to_erase = csbi.dwSize.X
-        else:
-            # invalid mode
-            return
-        # fill the entire screen with blanks
-        win32.FillConsoleOutputCharacter(handle, ' ', cells_to_erase, from_coord)
-        # now set the buffer's attributes accordingly
-        win32.FillConsoleOutputAttribute(handle, self.get_attrs(), cells_to_erase, from_coord)
-
-    def set_title(self, title):
-        win32.SetConsoleTitle(title)
diff --git a/venv/Lib/site-packages/easy-install.pth b/venv/Lib/site-packages/easy-install.pth
deleted file mode 100644
index b74fe2e..0000000
--- a/venv/Lib/site-packages/easy-install.pth
+++ /dev/null
@@ -1,2 +0,0 @@
-./setuptools-40.8.0-py3.7.egg
-./pip-19.0.3-py3.7.egg
diff --git a/venv/Lib/site-packages/isort-4.3.21.dist-info/INSTALLER b/venv/Lib/site-packages/isort-4.3.21.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/isort-4.3.21.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/isort-4.3.21.dist-info/LICENSE b/venv/Lib/site-packages/isort-4.3.21.dist-info/LICENSE
deleted file mode 100644
index b5083a5..0000000
--- a/venv/Lib/site-packages/isort-4.3.21.dist-info/LICENSE
+++ /dev/null
@@ -1,21 +0,0 @@
-The MIT License (MIT)
-
-Copyright (c) 2013 Timothy Edmund Crosley
-
-Permission is hereby granted, free of charge, to any person obtaining a copy
-of this software and associated documentation files (the "Software"), to deal
-in the Software without restriction, including without limitation the rights
-to use, copy, modify, merge, publish, distribute, sublicense, and/or sell
-copies of the Software, and to permit persons to whom the Software is
-furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in
-all copies or substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR
-IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF MERCHANTABILITY,
-FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL THE
-AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER
-LIABILITY, WHETHER IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING FROM,
-OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR OTHER DEALINGS IN
-THE SOFTWARE.
diff --git a/venv/Lib/site-packages/isort-4.3.21.dist-info/METADATA b/venv/Lib/site-packages/isort-4.3.21.dist-info/METADATA
deleted file mode 100644
index fbc7f6c..0000000
--- a/venv/Lib/site-packages/isort-4.3.21.dist-info/METADATA
+++ /dev/null
@@ -1,697 +0,0 @@
-Metadata-Version: 2.1
-Name: isort
-Version: 4.3.21
-Summary: A Python utility / library to sort Python imports.
-Home-page: https://github.com/timothycrosley/isort
-Author: Timothy Crosley
-Author-email: timothy.crosley@gmail.com
-License: MIT
-Keywords: Refactor,Python,Python2,Python3,Refactoring,Imports,Sort,Clean
-Platform: UNKNOWN
-Classifier: Development Status :: 6 - Mature
-Classifier: Intended Audience :: Developers
-Classifier: Natural Language :: English
-Classifier: Environment :: Console
-Classifier: License :: OSI Approved :: MIT License
-Classifier: Programming Language :: Python
-Classifier: Programming Language :: Python :: 2
-Classifier: Programming Language :: Python :: 2.7
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.4
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: Implementation :: CPython
-Classifier: Programming Language :: Python :: Implementation :: PyPy
-Classifier: Topic :: Software Development :: Libraries
-Classifier: Topic :: Utilities
-Requires-Python: >=2.7, !=3.0.*, !=3.1.*, !=3.2.*, !=3.3.*
-Requires-Dist: futures ; python_version < "3.2"
-Requires-Dist: backports.functools-lru-cache ; python_version < "3.2"
-Provides-Extra: pipfile
-Requires-Dist: pipreqs ; extra == 'pipfile'
-Requires-Dist: requirementslib ; extra == 'pipfile'
-Provides-Extra: pyproject
-Requires-Dist: toml ; extra == 'pyproject'
-Provides-Extra: requirements
-Requires-Dist: pipreqs ; extra == 'requirements'
-Requires-Dist: pip-api ; extra == 'requirements'
-Provides-Extra: xdg_home
-Requires-Dist: appdirs (>=1.4.0) ; extra == 'xdg_home'
-
-.. image:: https://raw.github.com/timothycrosley/isort/master/logo.png
-    :alt: isort
-
-########
-
-.. image:: https://badge.fury.io/py/isort.svg
-    :target: https://badge.fury.io/py/isort
-    :alt: PyPI version
-
-.. image:: https://travis-ci.org/timothycrosley/isort.svg?branch=master
-    :target: https://travis-ci.org/timothycrosley/isort
-    :alt: Build Status
-
-
-.. image:: https://coveralls.io/repos/timothycrosley/isort/badge.svg?branch=release%2F2.6.0&service=github
-  :target: https://coveralls.io/github/timothycrosley/isort?branch=release%2F2.6.0
-  :alt: Coverage
-
-.. image:: https://img.shields.io/github/license/mashape/apistatus.svg
-    :target: https://pypi.org/project/hug/
-    :alt: License
-
-.. image:: https://badges.gitter.im/Join%20Chat.svg
-   :alt: Join the chat at https://gitter.im/timothycrosley/isort
-   :target: https://gitter.im/timothycrosley/isort?utm_source=badge&utm_medium=badge&utm_campaign=pr-badge&utm_content=badge
-
-.. image:: https://pepy.tech/badge/isort
-    :alt: Downloads
-    :target: https://pepy.tech/project/isort
-
-isort your python imports for you so you don't have to.
-
-isort is a Python utility / library to sort imports alphabetically, and automatically separated into sections.
-It provides a command line utility, Python library and `plugins for various editors <https://github.com/timothycrosley/isort/wiki/isort-Plugins>`_ to quickly sort all your imports.
-It currently cleanly supports Python 2.7 and 3.4+ without any dependencies.
-
-.. image:: https://raw.github.com/timothycrosley/isort/develop/example.gif
-   :alt: Example Usage
-
-Before isort:
-
-.. code-block:: python
-
-    from my_lib import Object
-
-    print("Hey")
-
-    import os
-
-    from my_lib import Object3
-
-    from my_lib import Object2
-
-    import sys
-
-    from third_party import lib15, lib1, lib2, lib3, lib4, lib5, lib6, lib7, lib8, lib9, lib10, lib11, lib12, lib13, lib14
-
-    import sys
-
-    from __future__ import absolute_import
-
-    from third_party import lib3
-
-    print("yo")
-
-After isort:
-
-.. code-block:: python
-
-    from __future__ import absolute_import
-
-    import os
-    import sys
-
-    from third_party import (lib1, lib2, lib3, lib4, lib5, lib6, lib7, lib8,
-                             lib9, lib10, lib11, lib12, lib13, lib14, lib15)
-
-    from my_lib import Object, Object2, Object3
-
-    print("Hey")
-    print("yo")
-
-Installing isort
-================
-
-Installing isort is as simple as:
-
-.. code-block:: bash
-
-    pip install isort
-
-Install isort with requirements.txt support:
-
-.. code-block:: bash
-
-    pip install isort[requirements]
-
-Install isort with Pipfile support:
-
-.. code-block:: bash
-
-    pip install isort[pipfile]
-
-Install isort with both formats support:
-
-.. code-block:: bash
-
-    pip install isort[requirements,pipfile]
-
-Using isort
-===========
-
-**From the command line**:
-
-.. code-block:: bash
-
-    isort mypythonfile.py mypythonfile2.py
-
-or recursively:
-
-.. code-block:: bash
-
-    isort -rc .
-
-*which is equivalent to:*
-
-.. code-block:: bash
-
-    isort **/*.py
-
-or to see the proposed changes without applying them:
-
-.. code-block:: bash
-
-    isort mypythonfile.py --diff
-
-Finally, to atomically run isort against a project, only applying changes if they don't introduce syntax errors do:
-
-.. code-block:: bash
-
-    isort -rc --atomic .
-
-(Note: this is disabled by default as it keeps isort from being able to run against code written using a different version of Python)
-
-**From within Python**:
-
-.. code-block:: bash
-
-    from isort import SortImports
-
-    SortImports("pythonfile.py")
-
-or:
-
-.. code-block:: bash
-
-    from isort import SortImports
-
-    new_contents = SortImports(file_contents=old_contents).output
-
-**From within Kate:**
-
-.. code-block:: bash
-
-    ctrl+[
-
-or:
-
-.. code-block:: bash
-
-    menu > Python > Sort Imports
-
-Installing isort's Kate plugin
-==============================
-
-For KDE 4.13+ / Pate 2.0+:
-
-.. code-block:: bash
-
-    wget https://raw.github.com/timothycrosley/isort/master/kate_plugin/isort_plugin.py --output-document ~/.kde/share/apps/kate/pate/isort_plugin.py
-    wget https://raw.github.com/timothycrosley/isort/master/kate_plugin/isort_plugin_ui.rc --output-document ~/.kde/share/apps/kate/pate/isort_plugin_ui.rc
-    wget https://raw.github.com/timothycrosley/isort/master/kate_plugin/katepart_isort.desktop --output-document ~/.kde/share/kde4/services/katepart_isort.desktop
-
-For all older versions:
-
-.. code-block:: bash
-
-    wget https://raw.github.com/timothycrosley/isort/master/kate_plugin/isort_plugin_old.py --output-document ~/.kde/share/apps/kate/pate/isort_plugin.py
-
-You will then need to restart kate and enable Python Plugins as well as the isort plugin itself.
-
-Installing isort's for your preferred text editor
-=================================================
-
-Several plugins have been written that enable to use isort from within a variety of text-editors.
-You can find a full list of them `on the isort wiki <https://github.com/timothycrosley/isort/wiki/isort-Plugins>`_.
-Additionally, I will enthusiastically accept pull requests that include plugins for other text editors
-and add documentation for them as I am notified.
-
-How does isort work?
-====================
-
-isort parses specified files for global level import lines (imports outside of try / except blocks, functions, etc..)
-and puts them all at the top of the file grouped together by the type of import:
-
-- Future
-- Python Standard Library
-- Third Party
-- Current Python Project
-- Explicitly Local (. before import, as in: ``from . import x``)
-- Custom Separate Sections (Defined by forced_separate list in configuration file)
-- Custom Sections (Defined by sections list in configuration file)
-
-Inside of each section the imports are sorted alphabetically. isort automatically removes duplicate python imports,
-and wraps long from imports to the specified line length (defaults to 79).
-
-When will isort not work?
-=========================
-
-If you ever have the situation where you need to have a try / except block in the middle of top-level imports or if
-your import order is directly linked to precedence.
-
-For example: a common practice in Django settings files is importing * from various settings files to form
-a new settings file. In this case if any of the imports change order you are changing the settings definition itself.
-
-However, you can configure isort to skip over just these files - or even to force certain imports to the top.
-
-Configuring isort
-=================
-
-If you find the default isort settings do not work well for your project, isort provides several ways to adjust
-the behavior.
-
-To configure isort for a single user create a ``~/.isort.cfg`` or ``$XDG_CONFIG_HOME/isort.cfg`` file:
-
-.. code-block:: ini
-
-    [settings]
-    line_length=120
-    force_to_top=file1.py,file2.py
-    skip=file3.py,file4.py
-    known_future_library=future,pies
-    known_standard_library=std,std2
-    known_third_party=randomthirdparty
-    known_first_party=mylib1,mylib2
-    indent='    '
-    multi_line_output=3
-    length_sort=1
-    forced_separate=django.contrib,django.utils
-    default_section=FIRSTPARTY
-    no_lines_before=LOCALFOLDER
-
-Additionally, you can specify project level configuration simply by placing a ``.isort.cfg`` file at the root of your
-project. isort will look up to 25 directories up, from the file it is ran against, to find a project specific configuration.
-
-Or, if you prefer, you can add an ``isort`` or ``tool:isort`` section to your project's ``setup.cfg`` or ``tox.ini`` file with any desired settings.
-
-You can also add your desired settings under a ``[tool.isort]`` section in your ``pyproject.toml`` file.
-
-You can then override any of these settings by using command line arguments, or by passing in override values to the
-SortImports class.
-
-Finally, as of version 3.0 isort supports editorconfig files using the standard syntax defined here:
-https://editorconfig.org/
-
-Meaning you place any standard isort configuration parameters within a .editorconfig file under the ``*.py`` section
-and they will be honored.
-
-For a full list of isort settings and their meanings `take a look at the isort wiki <https://github.com/timothycrosley/isort/wiki/isort-Settings>`_.
-
-Multi line output modes
-=======================
-
-You will notice above the "multi_line_output" setting. This setting defines how from imports wrap when they extend
-past the line_length limit and has 6 possible settings:
-
-**0 - Grid**
-
-.. code-block:: python
-
-    from third_party import (lib1, lib2, lib3,
-                             lib4, lib5, ...)
-
-**1 - Vertical**
-
-.. code-block:: python
-
-    from third_party import (lib1,
-                             lib2,
-                             lib3
-                             lib4,
-                             lib5,
-                             ...)
-
-**2 - Hanging Indent**
-
-.. code-block:: python
-
-    from third_party import \
-        lib1, lib2, lib3, \
-        lib4, lib5, lib6
-
-**3 - Vertical Hanging Indent**
-
-.. code-block:: python
-
-    from third_party import (
-        lib1,
-        lib2,
-        lib3,
-        lib4,
-    )
-
-**4 - Hanging Grid**
-
-.. code-block:: python
-
-    from third_party import (
-        lib1, lib2, lib3, lib4,
-        lib5, ...)
-
-**5 - Hanging Grid Grouped**
-
-.. code-block:: python
-
-    from third_party import (
-        lib1, lib2, lib3, lib4,
-        lib5, ...
-    )
-
-**6 - Hanging Grid Grouped, No Trailing Comma**
-
-In Mode 5 isort leaves a single extra space to maintain consistency of output when a comma is added at the end.
-Mode 6 is the same - except that no extra space is maintained leading to the possibility of lines one character longer.
-You can enforce a trailing comma by using this in conjunction with `-tc` or `trailing_comma: True`.
-
-.. code-block:: python
-
-    from third_party import (
-        lib1, lib2, lib3, lib4,
-        lib5
-    )
-
-**7 - NOQA**
-
-.. code-block:: python
-
-    from third_party import lib1, lib2, lib3, ...  # NOQA
-
-Alternatively, you can set ``force_single_line`` to ``True`` (``-sl`` on the command line) and every import will appear on its
-own line:
-
-.. code-block:: python
-
-    from third_party import lib1
-    from third_party import lib2
-    from third_party import lib3
-    ...
-
-Note: to change the how constant indents appear - simply change the indent property with the following accepted formats:
-
-*   Number of spaces you would like. For example: 4 would cause standard 4 space indentation.
-*   Tab
-*   A verbatim string with quotes around it.
-
-For example:
-
-.. code-block:: python
-
-    "    "
-
-is equivalent to 4.
-
-For the import styles that use parentheses, you can control whether or not to
-include a trailing comma after the last import with the ``include_trailing_comma``
-option (defaults to ``False``).
-
-Intelligently Balanced Multi-line Imports
-=========================================
-
-As of isort 3.1.0 support for balanced multi-line imports has been added.
-With this enabled isort will dynamically change the import length to the one that produces the most balanced grid,
-while staying below the maximum import length defined.
-
-Example:
-
-.. code-block:: python
-
-    from __future__ import (absolute_import, division,
-                            print_function, unicode_literals)
-
-Will be produced instead of:
-
-.. code-block:: python
-
-    from __future__ import (absolute_import, division, print_function,
-                            unicode_literals)
-
-To enable this set ``balanced_wrapping`` to ``True`` in your config or pass the ``-e`` option into the command line utility.
-
-Custom Sections and Ordering
-============================
-
-You can change the section order with ``sections`` option from the default of:
-
-.. code-block:: ini
-
-    FUTURE,STDLIB,THIRDPARTY,FIRSTPARTY,LOCALFOLDER
-
-to your preference:
-
-.. code-block:: ini
-
-    sections=FUTURE,STDLIB,FIRSTPARTY,THIRDPARTY,LOCALFOLDER
-
-You also can define your own sections and their order.
-
-Example:
-
-.. code-block:: ini
-
-    known_django=django
-    known_pandas=pandas,numpy
-    sections=FUTURE,STDLIB,DJANGO,THIRDPARTY,PANDAS,FIRSTPARTY,LOCALFOLDER
-
-would create two new sections with the specified known modules.
-
-The ``no_lines_before`` option will prevent the listed sections from being split from the previous section by an empty line.
-
-Example:
-
-.. code-block:: ini
-
-   sections=FUTURE,STDLIB,THIRDPARTY,FIRSTPARTY,LOCALFOLDER
-   no_lines_before=LOCALFOLDER
-
-would produce a section with both FIRSTPARTY and LOCALFOLDER modules combined.
-
-Auto-comment import sections
-============================
-
-Some projects prefer to have import sections uniquely titled to aid in identifying the sections quickly
-when visually scanning. isort can automate this as well. To do this simply set the ``import_heading_{section_name}``
-setting for each section you wish to have auto commented - to the desired comment.
-
-For Example:
-
-.. code-block:: ini
-
-    import_heading_stdlib=Standard Library
-    import_heading_firstparty=My Stuff
-
-Would lead to output looking like the following:
-
-.. code-block:: python
-
-    # Standard Library
-    import os
-    import sys
-
-    import django.settings
-
-    # My Stuff
-    import myproject.test
-
-Ordering by import length
-=========================
-
-isort also makes it easy to sort your imports by length, simply by setting the ``length_sort`` option to ``True``.
-This will result in the following output style:
-
-.. code-block:: python
-
-    from evn.util import (
-        Pool,
-        Dict,
-        Options,
-        Constant,
-        DecayDict,
-        UnexpectedCodePath,
-    )
-
-It is also possible to opt-in to sorting imports by length for only specific
-sections by using ``length_sort_`` followed by the section name as a
-configuration item, e.g.::
-
-    length_sort_stdlib=1
-
-Skip processing of imports (outside of configuration)
-=====================================================
-
-To make isort ignore a single import simply add a comment at the end of the import line containing the text ``isort:skip``:
-
-.. code-block:: python
-
-    import module  # isort:skip
-
-or:
-
-.. code-block:: python
-
-    from xyz import (abc,  # isort:skip
-                     yo,
-                     hey)
-
-To make isort skip an entire file simply add ``isort:skip_file`` to the module's doc string:
-
-.. code-block:: python
-
-    """ my_module.py
-        Best module ever
-
-       isort:skip_file
-    """
-
-    import b
-    import a
-
-Adding an import to multiple files
-==================================
-
-isort makes it easy to add an import statement across multiple files, while being assured it's correctly placed.
-
-From the command line:
-
-.. code-block:: bash
-
-    isort -a "from __future__ import print_function" *.py
-
-from within Kate:
-
-.. code-block::
-
-    ctrl+]
-
-or:
-
-.. code-block::
-
-    menu > Python > Add Import
-
-Removing an import from multiple files
-======================================
-
-isort also makes it easy to remove an import from multiple files, without having to be concerned with how it was originally
-formatted.
-
-From the command line:
-
-.. code-block:: bash
-
-    isort -rm "os.system" *.py
-
-from within Kate:
-
-.. code-block::
-
-    ctrl+shift+]
-
-or:
-
-.. code-block::
-
-    menu > Python > Remove Import
-
-Using isort to verify code
-==========================
-
-The ``--check-only`` option
----------------------------
-
-isort can also be used to used to verify that code is correctly formatted by running it with ``-c``.
-Any files that contain incorrectly sorted and/or formatted imports will be outputted to ``stderr``.
-
-.. code-block:: bash
-
-    isort **/*.py -c -vb
-
-    SUCCESS: /home/timothy/Projects/Open_Source/isort/isort_kate_plugin.py Everything Looks Good!
-    ERROR: /home/timothy/Projects/Open_Source/isort/isort/isort.py Imports are incorrectly sorted.
-
-One great place this can be used is with a pre-commit git hook, such as this one by @acdha:
-
-https://gist.github.com/acdha/8717683
-
-This can help to ensure a certain level of code quality throughout a project.
-
-
-Git hook
---------
-
-isort provides a hook function that can be integrated into your Git pre-commit script to check
-Python code before committing.
-
-To cause the commit to fail if there are isort errors (strict mode), include the following in
-``.git/hooks/pre-commit``:
-
-.. code-block:: python
-
-    #!/usr/bin/env python
-    import sys
-    from isort.hooks import git_hook
-
-    sys.exit(git_hook(strict=True, modify=True))
-
-If you just want to display warnings, but allow the commit to happen anyway, call ``git_hook`` without
-the `strict` parameter. If you want to display warnings, but not also fix the code, call ``git_hook`` without
-the `modify` parameter.
-
-Setuptools integration
-----------------------
-
-Upon installation, isort enables a ``setuptools`` command that checks Python files
-declared by your project.
-
-Running ``python setup.py isort`` on the command line will check the files
-listed in your ``py_modules`` and ``packages``.  If any warning is found,
-the command will exit with an error code:
-
-.. code-block:: bash
-
-    $ python setup.py isort
-
-Also, to allow users to be able to use the command without having to install
-isort themselves, add isort to the setup_requires of your ``setup()`` like so:
-
-.. code-block:: python
-
-    setup(
-        name="project",
-        packages=["project"],
-
-        setup_requires=[
-            "isort"
-        ]
-    )
-
-
-Why isort?
-==========
-
-isort simply stands for import sort. It was originally called "sortImports" however I got tired of typing the extra
-characters and came to the realization camelCase is not pythonic.
-
-I wrote isort because in an organization I used to work in the manager came in one day and decided all code must
-have alphabetically sorted imports. The code base was huge - and he meant for us to do it by hand. However, being a
-programmer - I'm too lazy to spend 8 hours mindlessly performing a function, but not too lazy to spend 16
-hours automating it. I was given permission to open source sortImports and here we are :)
-
---------------------------------------------
-
-Thanks and I hope you find isort useful!
-
-~Timothy Crosley
-
-
diff --git a/venv/Lib/site-packages/isort-4.3.21.dist-info/RECORD b/venv/Lib/site-packages/isort-4.3.21.dist-info/RECORD
deleted file mode 100644
index fbe22ff..0000000
--- a/venv/Lib/site-packages/isort-4.3.21.dist-info/RECORD
+++ /dev/null
@@ -1,30 +0,0 @@
-../../Scripts/isort.exe,sha256=LehBbE3s782QB5Pj-GAeCX3qPl-km1TABLOXedSMAcE,102790
-isort-4.3.21.dist-info/INSTALLER,sha256=zuuue4knoyJ-UwPPXg8fezS7VCrXJQrAP7zeNuwvFQg,4
-isort-4.3.21.dist-info/LICENSE,sha256=BjKUABw9Uj26y6ud1UrCKZgnVsyvWSylMkCysM3YIGU,1089
-isort-4.3.21.dist-info/METADATA,sha256=8fY1DuLOn_UnCH58A8AcsCUZpYWeLCsQF-n-GIXlxOM,19749
-isort-4.3.21.dist-info/RECORD,,
-isort-4.3.21.dist-info/WHEEL,sha256=h_aVn5OB2IERUjMbi2pucmR_zzWJtk303YXvhh60NJ8,110
-isort-4.3.21.dist-info/entry_points.txt,sha256=2M99eSFpnteDm3ekW8jya2a3A0-vFntKdT1fP93Tyks,148
-isort-4.3.21.dist-info/top_level.txt,sha256=mrBLoVpJnQWBbnMOSdzkjN1E9Z-e3Zd-MRlo88bstUk,6
-isort/__init__.py,sha256=_DTTMASePJCqsKnRJPf_YgFv5ZJOHg1uPLkrQHcqA2c,1380
-isort/__main__.py,sha256=9tThPqyOnY86bHaxJ0WciTd-rfKN3O-PQoNGBO2xhio,205
-isort/__pycache__/__init__.cpython-37.pyc,,
-isort/__pycache__/__main__.cpython-37.pyc,,
-isort/__pycache__/finders.cpython-37.pyc,,
-isort/__pycache__/hooks.cpython-37.pyc,,
-isort/__pycache__/isort.cpython-37.pyc,,
-isort/__pycache__/main.cpython-37.pyc,,
-isort/__pycache__/natural.cpython-37.pyc,,
-isort/__pycache__/pie_slice.cpython-37.pyc,,
-isort/__pycache__/pylama_isort.cpython-37.pyc,,
-isort/__pycache__/settings.cpython-37.pyc,,
-isort/__pycache__/utils.cpython-37.pyc,,
-isort/finders.py,sha256=0w39ygCFuOv40OHixflrOv_Xna8K78usa5ySwS9GkWE,13185
-isort/hooks.py,sha256=GcyPMF7raq3B1z4ubbzIWoMiY5DePDni0Nct5U87uMQ,3230
-isort/isort.py,sha256=krLW0QgwnVjUD3hYTpQmWkMa5TDEZxx6AbX80vlVNoA,53910
-isort/main.py,sha256=rS7dAu_0T-8Jxi3sDWu00IOjt4j0r3vJi6bXZn6RnQg,21974
-isort/natural.py,sha256=hlcWsGKfIUC4Atjp5IIqDCmg1madY6ave9oNiTGjJ0Q,1794
-isort/pie_slice.py,sha256=hO6l1XocvGAd8XTR8526r-G7XIncUQB53_DHQ4AZEYI,5612
-isort/pylama_isort.py,sha256=wF6NOEVuibme0l-5pH9pCW1j4vGaFamuwll494TnzDI,785
-isort/settings.py,sha256=4_Jf-9GaBy9fi6UJctLqesIAMAegWekRIJdJmH5TBNE,17452
-isort/utils.py,sha256=KtazEoeX9XmtcrUGP6xl5lBX7Ye2N08ACGaWxiGcIaE,1344
diff --git a/venv/Lib/site-packages/isort-4.3.21.dist-info/WHEEL b/venv/Lib/site-packages/isort-4.3.21.dist-info/WHEEL
deleted file mode 100644
index 78e6f69..0000000
--- a/venv/Lib/site-packages/isort-4.3.21.dist-info/WHEEL
+++ /dev/null
@@ -1,6 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.33.4)
-Root-Is-Purelib: true
-Tag: py2-none-any
-Tag: py3-none-any
-
diff --git a/venv/Lib/site-packages/isort-4.3.21.dist-info/entry_points.txt b/venv/Lib/site-packages/isort-4.3.21.dist-info/entry_points.txt
deleted file mode 100644
index 3a77a18..0000000
--- a/venv/Lib/site-packages/isort-4.3.21.dist-info/entry_points.txt
+++ /dev/null
@@ -1,9 +0,0 @@
-[console_scripts]
-isort = isort.main:main
-
-[distutils.commands]
-isort = isort.main:ISortCommand
-
-[pylama.linter]
-isort = isort.pylama_isort:Linter
-
diff --git a/venv/Lib/site-packages/isort-4.3.21.dist-info/top_level.txt b/venv/Lib/site-packages/isort-4.3.21.dist-info/top_level.txt
deleted file mode 100644
index 2a79243..0000000
--- a/venv/Lib/site-packages/isort-4.3.21.dist-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-isort
diff --git a/venv/Lib/site-packages/isort/__init__.py b/venv/Lib/site-packages/isort/__init__.py
deleted file mode 100644
index 9a0a073..0000000
--- a/venv/Lib/site-packages/isort/__init__.py
+++ /dev/null
@@ -1,28 +0,0 @@
-"""__init__.py.
-
-Defines the isort module to include the SortImports utility class as well as any defined settings.
-
-Copyright (C) 2013  Timothy Edmund Crosley
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of this software and associated
-documentation files (the "Software"), to deal in the Software without restriction, including without limitation
-the rights to use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of the Software, and
-to permit persons to whom the Software is furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all copies or
-substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED
-TO THE WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL
-THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF
-CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-OTHER DEALINGS IN THE SOFTWARE.
-
-"""
-
-from __future__ import absolute_import, division, print_function, unicode_literals
-
-from . import settings  # noqa: F401
-from .isort import SortImports  # noqa: F401
-
-__version__ = "4.3.21"
diff --git a/venv/Lib/site-packages/isort/__main__.py b/venv/Lib/site-packages/isort/__main__.py
deleted file mode 100644
index 91cc154..0000000
--- a/venv/Lib/site-packages/isort/__main__.py
+++ /dev/null
@@ -1,9 +0,0 @@
-from __future__ import absolute_import
-
-from isort.pie_slice import apply_changes_to_python_environment
-
-apply_changes_to_python_environment()
-
-from isort.main import main  # noqa: E402 isort:skip
-
-main()
diff --git a/venv/Lib/site-packages/isort/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 041c992..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/__main__.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/__main__.cpython-37.pyc
deleted file mode 100644
index 63b2c4d..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/__main__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/finders.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/finders.cpython-37.pyc
deleted file mode 100644
index a579698..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/finders.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/hooks.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/hooks.cpython-37.pyc
deleted file mode 100644
index 509a974..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/hooks.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/isort.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/isort.cpython-37.pyc
deleted file mode 100644
index fce8cbf..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/isort.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/main.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/main.cpython-37.pyc
deleted file mode 100644
index efb6118..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/main.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/natural.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/natural.cpython-37.pyc
deleted file mode 100644
index 4eb1b12..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/natural.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/pie_slice.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/pie_slice.cpython-37.pyc
deleted file mode 100644
index f024ebb..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/pie_slice.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/pylama_isort.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/pylama_isort.cpython-37.pyc
deleted file mode 100644
index f2bbef1..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/pylama_isort.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/settings.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/settings.cpython-37.pyc
deleted file mode 100644
index d8a295d..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/settings.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/isort/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index d50b861..0000000
--- a/venv/Lib/site-packages/isort/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/isort/finders.py b/venv/Lib/site-packages/isort/finders.py
deleted file mode 100644
index 225bd12..0000000
--- a/venv/Lib/site-packages/isort/finders.py
+++ /dev/null
@@ -1,382 +0,0 @@
-"""Finders try to find right section for passed module name
-"""
-from __future__ import absolute_import, division, print_function, unicode_literals
-
-import inspect
-import os
-import os.path
-import re
-import sys
-import sysconfig
-from fnmatch import fnmatch
-from glob import glob
-
-from .pie_slice import PY2
-from .utils import chdir, exists_case_sensitive
-
-try:
-    from pipreqs import pipreqs
-except ImportError:
-    pipreqs = None
-
-try:
-    from pip_api import parse_requirements
-except ImportError:
-    parse_requirements = None
-
-try:
-    from requirementslib import Pipfile
-except ImportError:
-    Pipfile = None
-
-try:
-    from functools import lru_cache
-except ImportError:
-    from backports.functools_lru_cache import lru_cache
-
-
-KNOWN_SECTION_MAPPING = {
-    'STDLIB': 'STANDARD_LIBRARY',
-    'FUTURE': 'FUTURE_LIBRARY',
-    'FIRSTPARTY': 'FIRST_PARTY',
-    'THIRDPARTY': 'THIRD_PARTY',
-}
-
-
-class BaseFinder(object):
-    def __init__(self, config, sections):
-        self.config = config
-        self.sections = sections
-
-
-class ForcedSeparateFinder(BaseFinder):
-    def find(self, module_name):
-        for forced_separate in self.config['forced_separate']:
-            # Ensure all forced_separate patterns will match to end of string
-            path_glob = forced_separate
-            if not forced_separate.endswith('*'):
-                path_glob = '%s*' % forced_separate
-
-            if fnmatch(module_name, path_glob) or fnmatch(module_name, '.' + path_glob):
-                return forced_separate
-
-
-class LocalFinder(BaseFinder):
-    def find(self, module_name):
-        if module_name.startswith("."):
-            return self.sections.LOCALFOLDER
-
-
-class KnownPatternFinder(BaseFinder):
-    def __init__(self, config, sections):
-        super(KnownPatternFinder, self).__init__(config, sections)
-
-        self.known_patterns = []
-        for placement in reversed(self.sections):
-            known_placement = KNOWN_SECTION_MAPPING.get(placement, placement)
-            config_key = 'known_{0}'.format(known_placement.lower())
-            known_patterns = self.config.get(config_key, [])
-            known_patterns = [
-                pattern
-                for known_pattern in known_patterns
-                for pattern in self._parse_known_pattern(known_pattern)
-            ]
-            for known_pattern in known_patterns:
-                regexp = '^' + known_pattern.replace('*', '.*').replace('?', '.?') + '$'
-                self.known_patterns.append((re.compile(regexp), placement))
-
-    @staticmethod
-    def _is_package(path):
-        """
-        Evaluates if path is a python package
-        """
-        if PY2:
-            return os.path.exists(os.path.join(path, '__init__.py'))
-        else:
-            return os.path.isdir(path)
-
-    def _parse_known_pattern(self, pattern):
-        """
-        Expand pattern if identified as a directory and return found sub packages
-        """
-        if pattern.endswith(os.path.sep):
-            patterns = [
-                filename
-                for filename in os.listdir(pattern)
-                if self._is_package(os.path.join(pattern, filename))
-            ]
-        else:
-            patterns = [pattern]
-
-        return patterns
-
-    def find(self, module_name):
-        # Try to find most specific placement instruction match (if any)
-        parts = module_name.split('.')
-        module_names_to_check = ('.'.join(parts[:first_k]) for first_k in range(len(parts), 0, -1))
-        for module_name_to_check in module_names_to_check:
-            for pattern, placement in self.known_patterns:
-                if pattern.match(module_name_to_check):
-                    return placement
-
-
-class PathFinder(BaseFinder):
-    def __init__(self, config, sections):
-        super(PathFinder, self).__init__(config, sections)
-
-        # restore the original import path (i.e. not the path to bin/isort)
-        self.paths = [os.getcwd()]
-
-        # virtual env
-        self.virtual_env = self.config.get('virtual_env') or os.environ.get('VIRTUAL_ENV')
-        if self.virtual_env:
-            self.virtual_env = os.path.realpath(self.virtual_env)
-        self.virtual_env_src = False
-        if self.virtual_env:
-            self.virtual_env_src = '{0}/src/'.format(self.virtual_env)
-            for path in glob('{0}/lib/python*/site-packages'.format(self.virtual_env)):
-                if path not in self.paths:
-                    self.paths.append(path)
-            for path in glob('{0}/lib/python*/*/site-packages'.format(self.virtual_env)):
-                if path not in self.paths:
-                    self.paths.append(path)
-            for path in glob('{0}/src/*'.format(self.virtual_env)):
-                if os.path.isdir(path):
-                    self.paths.append(path)
-
-        # conda
-        self.conda_env = self.config.get('conda_env') or os.environ.get('CONDA_PREFIX')
-        if self.conda_env:
-            self.conda_env = os.path.realpath(self.conda_env)
-            for path in glob('{0}/lib/python*/site-packages'.format(self.conda_env)):
-                if path not in self.paths:
-                    self.paths.append(path)
-            for path in glob('{0}/lib/python*/*/site-packages'.format(self.conda_env)):
-                if path not in self.paths:
-                    self.paths.append(path)
-
-        # handle case-insensitive paths on windows
-        self.stdlib_lib_prefix = os.path.normcase(sysconfig.get_paths()['stdlib'])
-        if self.stdlib_lib_prefix not in self.paths:
-            self.paths.append(self.stdlib_lib_prefix)
-
-        # handle compiled libraries
-        self.ext_suffix = sysconfig.get_config_var("EXT_SUFFIX") or ".so"
-
-        # add system paths
-        for path in sys.path[1:]:
-            if path not in self.paths:
-                self.paths.append(path)
-
-    def find(self, module_name):
-        for prefix in self.paths:
-            package_path = "/".join((prefix, module_name.split(".")[0]))
-            is_module = (exists_case_sensitive(package_path + ".py") or
-                         exists_case_sensitive(package_path + ".so") or
-                         exists_case_sensitive(package_path + self.ext_suffix) or
-                         exists_case_sensitive(package_path + "/__init__.py"))
-            is_package = exists_case_sensitive(package_path) and os.path.isdir(package_path)
-            if is_module or is_package:
-                if 'site-packages' in prefix:
-                    return self.sections.THIRDPARTY
-                if 'dist-packages' in prefix:
-                    return self.sections.THIRDPARTY
-                if self.virtual_env and self.virtual_env_src in prefix:
-                    return self.sections.THIRDPARTY
-                if self.conda_env and self.conda_env in prefix:
-                    return self.sections.THIRDPARTY
-                if os.path.normcase(prefix).startswith(self.stdlib_lib_prefix):
-                    return self.sections.STDLIB
-                return self.config['default_section']
-
-
-class ReqsBaseFinder(BaseFinder):
-    def __init__(self, config, sections, path='.'):
-        super(ReqsBaseFinder, self).__init__(config, sections)
-        self.path = path
-        if self.enabled:
-            self.mapping = self._load_mapping()
-            self.names = self._load_names()
-
-    @staticmethod
-    def _load_mapping():
-        """Return list of mappings `package_name -> module_name`
-
-        Example:
-            django-haystack -> haystack
-        """
-        if not pipreqs:
-            return
-        path = os.path.dirname(inspect.getfile(pipreqs))
-        path = os.path.join(path, 'mapping')
-        with open(path) as f:
-            # pypi_name: import_name
-            return dict(line.strip().split(":")[::-1] for line in f)
-
-    def _load_names(self):
-        """Return list of thirdparty modules from requirements
-        """
-        names = []
-        for path in self._get_files():
-            for name in self._get_names(path):
-                names.append(self._normalize_name(name))
-        return names
-
-    @staticmethod
-    def _get_parents(path):
-        prev = ''
-        while path != prev:
-            prev = path
-            yield path
-            path = os.path.dirname(path)
-
-    def _get_files(self):
-        """Return paths to all requirements files
-        """
-        path = os.path.abspath(self.path)
-        if os.path.isfile(path):
-            path = os.path.dirname(path)
-
-        for path in self._get_parents(path):
-            for file_path in self._get_files_from_dir(path):
-                yield file_path
-
-    def _normalize_name(self, name):
-        """Convert package name to module name
-
-        Examples:
-            Django -> django
-            django-haystack -> haystack
-            Flask-RESTFul -> flask_restful
-        """
-        if self.mapping:
-            name = self.mapping.get(name, name)
-        return name.lower().replace('-', '_')
-
-    def find(self, module_name):
-        # required lib not installed yet
-        if not self.enabled:
-            return
-
-        module_name, _sep, _submodules = module_name.partition('.')
-        module_name = module_name.lower()
-        if not module_name:
-            return
-
-        for name in self.names:
-            if module_name == name:
-                return self.sections.THIRDPARTY
-
-
-class RequirementsFinder(ReqsBaseFinder):
-    exts = ('.txt', '.in')
-    enabled = bool(parse_requirements)
-
-    def _get_files_from_dir(self, path):
-        """Return paths to requirements files from passed dir.
-        """
-        return RequirementsFinder._get_files_from_dir_cached(path)
-
-    @classmethod
-    @lru_cache(maxsize=16)
-    def _get_files_from_dir_cached(cls, path):
-        result = []
-
-        for fname in os.listdir(path):
-            if 'requirements' not in fname:
-                continue
-            full_path = os.path.join(path, fname)
-
-            # *requirements*/*.{txt,in}
-            if os.path.isdir(full_path):
-                for subfile_name in os.listdir(path):
-                    for ext in cls.exts:
-                        if subfile_name.endswith(ext):
-                            result.append(os.path.join(path, subfile_name))
-                continue
-
-            # *requirements*.{txt,in}
-            if os.path.isfile(full_path):
-                for ext in cls.exts:
-                    if fname.endswith(ext):
-                        result.append(full_path)
-                        break
-
-        return result
-
-    def _get_names(self, path):
-        """Load required packages from path to requirements file
-        """
-        return RequirementsFinder._get_names_cached(path)
-
-    @classmethod
-    @lru_cache(maxsize=16)
-    def _get_names_cached(cls, path):
-        results = []
-
-        with chdir(os.path.dirname(path)):
-            requirements = parse_requirements(path)
-            for req in requirements.values():
-                if req.name:
-                    results.append(req.name)
-
-        return results
-
-
-class PipfileFinder(ReqsBaseFinder):
-    enabled = bool(Pipfile)
-
-    def _get_names(self, path):
-        with chdir(path):
-            project = Pipfile.load(path)
-            for req in project.packages:
-                yield req.name
-
-    def _get_files_from_dir(self, path):
-        if 'Pipfile' in os.listdir(path):
-            yield path
-
-
-class DefaultFinder(BaseFinder):
-    def find(self, module_name):
-        return self.config['default_section']
-
-
-class FindersManager(object):
-    finders = (
-        ForcedSeparateFinder,
-        LocalFinder,
-        KnownPatternFinder,
-        PathFinder,
-        PipfileFinder,
-        RequirementsFinder,
-        DefaultFinder,
-    )
-
-    def __init__(self, config, sections, finders=None):
-        self.verbose = config.get('verbose', False)
-
-        finders = self.finders if finders is None else finders
-        self.finders = []
-        for finder in finders:
-            try:
-                self.finders.append(finder(config, sections))
-            except Exception as exception:
-                # if one finder fails to instantiate isort can continue using the rest
-                if self.verbose:
-                    print('{} encountered an error ({}) during instantiation and cannot be used'.format(finder.__name__,
-                                                                                                        str(exception)))
-        self.finders = tuple(self.finders)
-
-    def find(self, module_name):
-        for finder in self.finders:
-            try:
-                section = finder.find(module_name)
-            except Exception as exception:
-                # isort has to be able to keep trying to identify the correct import section even if one approach fails
-                if self.verbose:
-                    print('{} encountered an error ({}) while trying to identify the {} module'.format(finder.__name__,
-                                                                                                       str(exception),
-                                                                                                       module_name))
-            if section is not None:
-                return section
diff --git a/venv/Lib/site-packages/isort/hooks.py b/venv/Lib/site-packages/isort/hooks.py
deleted file mode 100644
index 16a16e1..0000000
--- a/venv/Lib/site-packages/isort/hooks.py
+++ /dev/null
@@ -1,91 +0,0 @@
-"""isort.py.
-
-Defines a git hook to allow pre-commit warnings and errors about import order.
-
-usage:
-    exit_code = git_hook(strict=True|False, modify=True|False)
-
-Copyright (C) 2015  Helen Sherwood-Taylor
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of this software and associated
-documentation files (the "Software"), to deal in the Software without restriction, including without limitation
-the rights to use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of the Software, and
-to permit persons to whom the Software is furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all copies or
-substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED
-TO THE WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL
-THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF
-CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-OTHER DEALINGS IN THE SOFTWARE.
-
-"""
-import subprocess
-
-from isort import SortImports
-
-
-def get_output(command):
-    """
-    Run a command and return raw output
-
-    :param str command: the command to run
-    :returns: the stdout output of the command
-    """
-    return subprocess.check_output(command.split())
-
-
-def get_lines(command):
-    """
-    Run a command and return lines of output
-
-    :param str command: the command to run
-    :returns: list of whitespace-stripped lines output by command
-    """
-    stdout = get_output(command)
-    return [line.strip().decode('utf-8') for line in stdout.splitlines()]
-
-
-def git_hook(strict=False, modify=False):
-    """
-    Git pre-commit hook to check staged files for isort errors
-
-    :param bool strict - if True, return number of errors on exit,
-        causing the hook to fail. If False, return zero so it will
-        just act as a warning.
-    :param bool modify - if True, fix the sources if they are not
-        sorted properly. If False, only report result without
-        modifying anything.
-
-    :return number of errors if in strict mode, 0 otherwise.
-    """
-
-    # Get list of files modified and staged
-    diff_cmd = "git diff-index --cached --name-only --diff-filter=ACMRTUXB HEAD"
-    files_modified = get_lines(diff_cmd)
-
-    errors = 0
-    for filename in files_modified:
-        if filename.endswith('.py'):
-            # Get the staged contents of the file
-            staged_cmd = "git show :%s" % filename
-            staged_contents = get_output(staged_cmd)
-
-            sort = SortImports(
-                file_path=filename,
-                file_contents=staged_contents.decode(),
-                check=True
-            )
-
-            if sort.incorrectly_sorted:
-                errors += 1
-                if modify:
-                    SortImports(
-                        file_path=filename,
-                        file_contents=staged_contents.decode(),
-                        check=False,
-                    )
-
-    return errors if strict else 0
diff --git a/venv/Lib/site-packages/isort/isort.py b/venv/Lib/site-packages/isort/isort.py
deleted file mode 100644
index 245e53f..0000000
--- a/venv/Lib/site-packages/isort/isort.py
+++ /dev/null
@@ -1,1060 +0,0 @@
-"""isort.py.
-
-Exposes a simple library to sort through imports within Python code
-
-usage:
-    SortImports(file_name)
-or:
-    sorted = SortImports(file_contents=file_contents).output
-
-Copyright (C) 2013  Timothy Edmund Crosley
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of this software and associated
-documentation files (the "Software"), to deal in the Software without restriction, including without limitation
-the rights to use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of the Software, and
-to permit persons to whom the Software is furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all copies or
-substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED
-TO THE WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL
-THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF
-CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-OTHER DEALINGS IN THE SOFTWARE.
-
-"""
-from __future__ import absolute_import, division, print_function, unicode_literals
-
-import codecs
-import copy
-import io
-import itertools
-import os
-import re
-import sys
-from collections import OrderedDict, namedtuple
-from datetime import datetime
-from difflib import unified_diff
-
-from . import settings
-from .finders import FindersManager
-from .natural import nsorted
-from .pie_slice import input
-
-
-class SortImports(object):
-    incorrectly_sorted = False
-    skipped = False
-
-    def __init__(self, file_path=None, file_contents=None, file_=None, write_to_stdout=False, check=False,
-                 show_diff=False, settings_path=None, ask_to_apply=False, run_path='', check_skip=True,
-                 extension=None, **setting_overrides):
-        if not settings_path and file_path:
-            settings_path = os.path.dirname(os.path.abspath(file_path))
-        settings_path = settings_path or os.getcwd()
-
-        self.config = settings.from_path(settings_path).copy()
-        for key, value in setting_overrides.items():
-            access_key = key.replace('not_', '').lower()
-            # The sections config needs to retain order and can't be converted to a set.
-            if access_key != 'sections' and type(self.config.get(access_key)) in (list, tuple):
-                if key.startswith('not_'):
-                    self.config[access_key] = list(set(self.config[access_key]).difference(value))
-                else:
-                    self.config[access_key] = list(set(self.config[access_key]).union(value))
-            else:
-                self.config[key] = value
-
-        if self.config['force_alphabetical_sort']:
-            self.config.update({'force_alphabetical_sort_within_sections': True,
-                                'no_sections': True,
-                                'lines_between_types': 1,
-                                'from_first': True})
-
-        indent = str(self.config['indent'])
-        if indent.isdigit():
-            indent = " " * int(indent)
-        else:
-            indent = indent.strip("'").strip('"')
-            if indent.lower() == "tab":
-                indent = "\t"
-        self.config['indent'] = indent
-
-        self.config['comment_prefix'] = self.config['comment_prefix'].strip("'").strip('"')
-
-        self.place_imports = {}
-        self.import_placements = {}
-        self.remove_imports = [self._format_simplified(removal) for removal in self.config['remove_imports']]
-        self.add_imports = [self._format_natural(addition) for addition in self.config['add_imports']]
-        self._section_comments = ["# " + value for key, value in self.config.items() if
-                                  key.startswith('import_heading') and value]
-
-        self.file_encoding = 'utf-8'
-        file_name = file_path
-        self.file_path = file_path or ""
-        if file_path:
-            file_path = os.path.abspath(file_path)
-            if check_skip:
-                if run_path and file_path.startswith(run_path):
-                    file_name = file_path.replace(run_path, '',  1)
-                else:
-                    file_name = file_path
-                    run_path = ''
-
-                if settings.should_skip(file_name, self.config, run_path):
-                    self.skipped = True
-                    if self.config['verbose']:
-                        print("WARNING: {0} was skipped as it's listed in 'skip' setting"
-                            " or matches a glob in 'skip_glob' setting".format(file_path))
-                    file_contents = None
-            if not self.skipped and not file_contents:
-                with io.open(file_path, 'rb') as f:
-                    file_encoding = coding_check(f)
-                with io.open(file_path, encoding=file_encoding, newline='') as file_to_import_sort:
-                    try:
-                        file_contents = file_to_import_sort.read()
-                        self.file_path = file_path
-                        self.file_encoding = file_encoding
-                        encoding_success = True
-                    except UnicodeDecodeError:
-                        encoding_success = False
-
-                if not encoding_success:
-                    with io.open(file_path, newline='') as file_to_import_sort:
-                        try:
-                            file_contents = file_to_import_sort.read()
-                            self.file_path = file_path
-                            self.file_encoding = file_to_import_sort.encoding
-                        except UnicodeDecodeError:
-                            encoding_success = False
-                            file_contents = None
-                            self.skipped = True
-                            if self.config['verbose']:
-                                print("WARNING: {} was skipped as it couldn't be opened with the given "
-                                      "{} encoding or {} fallback encoding".format(file_path,
-                                                                                   self.file_encoding,
-                                                                                   file_to_import_sort.encoding))
-        elif file_:
-            try:
-                file_.seek(0)
-                self.file_encoding = coding_check(file_)
-                file_.seek(0)
-            except (io.UnsupportedOperation, IOError):
-                pass
-            reader = codecs.getreader(self.file_encoding)
-            file_contents = reader(file_).read()
-
-        # try to decode file_contents
-        if file_contents:
-            try:
-                basestring
-                # python 2
-                need_decode = (str, bytes)
-            except NameError:
-                # python 3
-                need_decode = bytes
-
-            if isinstance(file_contents, need_decode):
-                file_contents = file_contents.decode(coding_check(file_contents.splitlines()))
-
-        if file_contents is None or ("isort:" + "skip_file") in file_contents:
-            self.skipped = True
-            self.output = None
-            if write_to_stdout and file_contents:
-                sys.stdout.write(file_contents)
-            return
-
-        if self.config['line_ending']:
-            self.line_separator = self.config['line_ending']
-        else:
-            if '\r\n' in file_contents:
-                self.line_separator = '\r\n'
-            elif '\r' in file_contents:
-                self.line_separator = '\r'
-            else:
-                self.line_separator = '\n'
-        self.in_lines = file_contents.split(self.line_separator)
-        self.original_length = len(self.in_lines)
-        if (self.original_length > 1 or self.in_lines[:1] not in ([], [""])) or self.config['force_adds']:
-            for add_import in self.add_imports:
-                self.in_lines.append(add_import)
-        self.number_of_lines = len(self.in_lines)
-
-        if not extension:
-            self.extension = file_name.split('.')[-1] if file_name else "py"
-        else:
-            self.extension = extension
-
-        self.out_lines = []
-        self.comments = {'from': {}, 'straight': {}, 'nested': {}, 'above': {'straight': {}, 'from': {}}}
-        self.imports = OrderedDict()
-        self.as_map = {}
-
-        section_names = self.config['sections']
-        self.sections = namedtuple('Sections', section_names)(*[name for name in section_names])
-        for section in itertools.chain(self.sections, self.config['forced_separate']):
-            self.imports[section] = {'straight': OrderedDict(), 'from': OrderedDict()}
-
-        self.finder = FindersManager(config=self.config, sections=self.sections)
-
-        self.index = 0
-        self.import_index = -1
-        self._first_comment_index_start = -1
-        self._first_comment_index_end = -1
-        self._parse()
-        if self.import_index != -1:
-            self._add_formatted_imports()
-        self.length_change = len(self.out_lines) - self.original_length
-        while self.out_lines and self.out_lines[-1].strip() == "":
-            self.out_lines.pop(-1)
-        self.out_lines.append("")
-        self.output = self.line_separator.join(self.out_lines)
-        if self.config['atomic']:
-            try:
-                compile(self._strip_top_comments(self.out_lines, self.line_separator), self.file_path, 'exec', 0, 1)
-            except SyntaxError:
-                self.output = file_contents
-                self.incorrectly_sorted = True
-                try:
-                    compile(self._strip_top_comments(self.in_lines, self.line_separator), self.file_path, 'exec', 0, 1)
-                    print("ERROR: {0} isort would have introduced syntax errors, please report to the project!".
-                          format(self.file_path))
-                except SyntaxError:
-                    print("ERROR: {0} File contains syntax errors.".format(self.file_path))
-
-                return
-        if check:
-            check_output = self.output
-            check_against = file_contents
-            if self.config['ignore_whitespace']:
-                check_output = check_output.replace(self.line_separator, "").replace(" ", "").replace("\x0c", "")
-                check_against = check_against.replace(self.line_separator, "").replace(" ", "").replace("\x0c", "")
-
-            if check_output.strip() == check_against.strip():
-                if self.config['verbose']:
-                    print("SUCCESS: {0} Everything Looks Good!".format(self.file_path))
-                return
-
-            print("ERROR: {0} Imports are incorrectly sorted.".format(self.file_path))
-            self.incorrectly_sorted = True
-        if show_diff or self.config['show_diff']:
-            self._show_diff(file_contents)
-        elif write_to_stdout:
-            if sys.version_info[0] < 3:
-                self.output = self.output.encode(self.file_encoding)
-            sys.stdout.write(self.output)
-        elif file_name and not check:
-            if self.output == file_contents:
-                return
-
-            if ask_to_apply:
-                self._show_diff(file_contents)
-                answer = None
-                while answer not in ('yes', 'y', 'no', 'n', 'quit', 'q'):
-                    answer = input("Apply suggested changes to '{0}' [y/n/q]? ".format(self.file_path)).lower()
-                    if answer in ('no', 'n'):
-                        return
-                    if answer in ('quit', 'q'):
-                        sys.exit(1)
-            with io.open(self.file_path, encoding=self.file_encoding, mode='w', newline='') as output_file:
-                if not self.config['quiet']:
-                    print("Fixing {0}".format(self.file_path))
-                output_file.write(self.output)
-
-    @property
-    def correctly_sorted(self):
-        return not self.incorrectly_sorted
-
-    def _show_diff(self, file_contents):
-        for line in unified_diff(
-            file_contents.splitlines(1),
-            self.output.splitlines(1),
-            fromfile=self.file_path + ':before',
-            tofile=self.file_path + ':after',
-            fromfiledate=str(datetime.fromtimestamp(os.path.getmtime(self.file_path))
-                             if self.file_path else datetime.now()),
-            tofiledate=str(datetime.now())
-        ):
-            sys.stdout.write(line)
-
-    @staticmethod
-    def _strip_top_comments(lines, line_separator):
-        """Strips # comments that exist at the top of the given lines"""
-        lines = copy.copy(lines)
-        while lines and lines[0].startswith("#"):
-            lines = lines[1:]
-        return line_separator.join(lines)
-
-    def place_module(self, module_name):
-        """Tries to determine if a module is a python std import, third party import, or project code:
-
-        if it can't determine - it assumes it is project code
-
-        """
-        return self.finder.find(module_name)
-
-    def _get_line(self):
-        """Returns the current line from the file while incrementing the index."""
-        line = self.in_lines[self.index]
-        self.index += 1
-        return line
-
-    @staticmethod
-    def _import_type(line):
-        """If the current line is an import line it will return its type (from or straight)"""
-        if "isort:skip" in line:
-            return
-        elif line.startswith('import '):
-            return "straight"
-        elif line.startswith('from '):
-            return "from"
-
-    def _at_end(self):
-        """returns True if we are at the end of the file."""
-        return self.index == self.number_of_lines
-
-    @staticmethod
-    def _module_key(module_name, config, sub_imports=False, ignore_case=False, section_name=None):
-        match = re.match(r'^(\.+)\s*(.*)', module_name)
-        if match:
-            sep = ' ' if config['reverse_relative'] else '_'
-            module_name = sep.join(match.groups())
-
-        prefix = ""
-        if ignore_case:
-            module_name = str(module_name).lower()
-        else:
-            module_name = str(module_name)
-
-        if sub_imports and config['order_by_type']:
-            if module_name.isupper() and len(module_name) > 1:
-                prefix = "A"
-            elif module_name[0:1].isupper():
-                prefix = "B"
-            else:
-                prefix = "C"
-        if not config['case_sensitive']:
-            module_name = module_name.lower()
-        if section_name is None or 'length_sort_' + str(section_name).lower() not in config:
-            length_sort = config['length_sort']
-        else:
-            length_sort = config['length_sort_' + str(section_name).lower()]
-        return "{0}{1}{2}".format(module_name in config['force_to_top'] and "A" or "B", prefix,
-                                  length_sort and (str(len(module_name)) + ":" + module_name) or module_name)
-
-    def _add_comments(self, comments, original_string=""):
-        """
-            Returns a string with comments added if ignore_comments is not set.
-        """
-
-        if not self.config['ignore_comments']:
-            return comments and "{0}{1} {2}".format(self._strip_comments(original_string)[0],
-                                                    self.config['comment_prefix'],
-                                                    "; ".join(comments)) or original_string
-
-        return comments and self._strip_comments(original_string)[0]
-
-    def _wrap(self, line):
-        """
-            Returns an import wrapped to the specified line-length, if possible.
-        """
-        wrap_mode = self.config['multi_line_output']
-        if len(line) > self.config['line_length'] and wrap_mode != settings.WrapModes.NOQA:
-            line_without_comment = line
-            comment = None
-            if '#' in line:
-                line_without_comment, comment = line.split('#', 1)
-            for splitter in ("import ", ".", "as "):
-                exp = r"\b" + re.escape(splitter) + r"\b"
-                if re.search(exp, line_without_comment) and not line_without_comment.strip().startswith(splitter):
-                    line_parts = re.split(exp, line_without_comment)
-                    if comment:
-                        line_parts[-1] = '{0}#{1}'.format(line_parts[-1], comment)
-                    next_line = []
-                    while (len(line) + 2) > (self.config['wrap_length'] or self.config['line_length']) and line_parts:
-                        next_line.append(line_parts.pop())
-                        line = splitter.join(line_parts)
-                    if not line:
-                        line = next_line.pop()
-
-                    cont_line = self._wrap(self.config['indent'] + splitter.join(next_line).lstrip())
-                    if self.config['use_parentheses']:
-                        if splitter == "as ":
-                            output = "{0}{1}{2}".format(line, splitter, cont_line.lstrip())
-                        else:
-                            output = "{0}{1}({2}{3}{4}{5})".format(
-                                line, splitter, self.line_separator, cont_line,
-                                "," if self.config['include_trailing_comma'] else "",
-                                self.line_separator if wrap_mode in (settings.WrapModes.VERTICAL_HANGING_INDENT,
-                                                                     settings.WrapModes.VERTICAL_GRID_GROUPED)
-                                else "")
-                        lines = output.split(self.line_separator)
-                        if self.config['comment_prefix'] in lines[-1] and lines[-1].endswith(')'):
-                            line, comment = lines[-1].split(self.config['comment_prefix'], 1)
-                            lines[-1] = line + ')' + self.config['comment_prefix'] + comment[:-1]
-                        return self.line_separator.join(lines)
-                    return "{0}{1}\\{2}{3}".format(line, splitter, self.line_separator, cont_line)
-        elif len(line) > self.config['line_length'] and wrap_mode == settings.WrapModes.NOQA:
-            if "# NOQA" not in line:
-                return "{0}{1} NOQA".format(line, self.config['comment_prefix'])
-
-        return line
-
-    def _add_straight_imports(self, straight_modules, section, section_output):
-        for module in straight_modules:
-            if module in self.remove_imports:
-                continue
-
-            if module in self.as_map:
-                import_definition = ''
-                if self.config['keep_direct_and_as_imports']:
-                    import_definition = "import {0}\n".format(module)
-                import_definition += "import {0} as {1}".format(module, self.as_map[module])
-            else:
-                import_definition = "import {0}".format(module)
-
-            comments_above = self.comments['above']['straight'].pop(module, None)
-            if comments_above:
-                section_output.extend(comments_above)
-            section_output.append(self._add_comments(self.comments['straight'].get(module), import_definition))
-
-    def _add_from_imports(self, from_modules, section, section_output, ignore_case):
-        for module in from_modules:
-            if module in self.remove_imports:
-                continue
-
-            import_start = "from {0} import ".format(module)
-            from_imports = list(self.imports[section]['from'][module])
-            if not self.config['no_inline_sort'] or self.config['force_single_line']:
-                from_imports = nsorted(from_imports, key=lambda key: self._module_key(key, self.config, True, ignore_case, section_name=section))
-            if self.remove_imports:
-                from_imports = [line for line in from_imports if not "{0}.{1}".format(module, line) in
-                                self.remove_imports]
-
-            sub_modules = ['{0}.{1}'.format(module, from_import) for from_import in from_imports]
-            as_imports = {
-                from_import: "{0} as {1}".format(from_import, self.as_map[sub_module])
-                for from_import, sub_module in zip(from_imports, sub_modules)
-                if sub_module in self.as_map
-            }
-            if self.config['combine_as_imports'] and not ("*" in from_imports and self.config['combine_star']):
-                for from_import in copy.copy(from_imports):
-                    if from_import in as_imports:
-                        from_imports[from_imports.index(from_import)] = as_imports.pop(from_import)
-
-            while from_imports:
-                comments = self.comments['from'].pop(module, ())
-                if "*" in from_imports and self.config['combine_star']:
-                    import_statement = self._wrap(self._add_comments(comments, "{0}*".format(import_start)))
-                    from_imports = None
-                elif self.config['force_single_line']:
-                    import_statements = []
-                    while from_imports:
-                        from_import = from_imports.pop(0)
-                        if from_import in as_imports:
-                            from_comments = self.comments['straight'].get('{}.{}'.format(module, from_import))
-                            import_statements.append(self._add_comments(from_comments,
-                                                     self._wrap(import_start + as_imports[from_import])))
-                            continue
-                        single_import_line = self._add_comments(comments, import_start + from_import)
-                        comment = self.comments['nested'].get(module, {}).pop(from_import, None)
-                        if comment:
-                            single_import_line += "{0} {1}".format(comments and ";" or self.config['comment_prefix'],
-                                                                   comment)
-                        import_statements.append(self._wrap(single_import_line))
-                        comments = None
-                    import_statement = self.line_separator.join(import_statements)
-                else:
-                    while from_imports and from_imports[0] in as_imports:
-                        from_import = from_imports.pop(0)
-                        from_comments = self.comments['straight'].get('{}.{}'.format(module, from_import))
-                        above_comments = self.comments['above']['from'].pop(module, None)
-                        if above_comments:
-                            section_output.extend(above_comments)
-
-                        section_output.append(self._add_comments(from_comments,
-                                                                 self._wrap(import_start + as_imports[from_import])))
-
-                    star_import = False
-                    if "*" in from_imports:
-                        section_output.append(self._add_comments(comments, "{0}*".format(import_start)))
-                        from_imports.remove('*')
-                        star_import = True
-                        comments = None
-
-                    for from_import in copy.copy(from_imports):
-                        if from_import in as_imports:
-                            continue
-                        comment = self.comments['nested'].get(module, {}).pop(from_import, None)
-                        if comment:
-                            single_import_line = self._add_comments(comments, import_start + from_import)
-                            single_import_line += "{0} {1}".format(comments and ";" or self.config['comment_prefix'],
-                                                                   comment)
-                            above_comments = self.comments['above']['from'].pop(module, None)
-                            if above_comments:
-                                section_output.extend(above_comments)
-                            section_output.append(self._wrap(single_import_line))
-                            from_imports.remove(from_import)
-                            comments = None
-
-                    from_import_section = []
-                    while from_imports and from_imports[0] not in as_imports:
-                        from_import_section.append(from_imports.pop(0))
-                    if star_import:
-                        import_statement = import_start + (", ").join(from_import_section)
-                    else:
-                        import_statement = self._add_comments(comments, import_start + (", ").join(from_import_section))
-                    if not from_import_section:
-                        import_statement = ""
-
-                    do_multiline_reformat = False
-
-                    force_grid_wrap = self.config['force_grid_wrap']
-                    if force_grid_wrap and len(from_import_section) >= force_grid_wrap:
-                        do_multiline_reformat = True
-
-                    if len(import_statement) > self.config['line_length'] and len(from_import_section) > 1:
-                        do_multiline_reformat = True
-
-                    # If line too long AND have imports AND we are NOT using GRID or VERTICAL wrap modes
-                    if (len(import_statement) > self.config['line_length'] and len(from_import_section) > 0 and
-                            self.config['multi_line_output'] not in (1, 0)):
-                        do_multiline_reformat = True
-
-                    if do_multiline_reformat:
-                        import_statement = self._multi_line_reformat(import_start, from_import_section, comments)
-                        if self.config['multi_line_output'] == 0:
-                            self.config['multi_line_output'] = 4
-                            try:
-                                other_import_statement = self._multi_line_reformat(import_start, from_import_section, comments)
-                                if (max(len(x)
-                                        for x in import_statement.split('\n')) > self.config['line_length']):
-                                    import_statement = other_import_statement
-                            finally:
-                                self.config['multi_line_output'] = 0
-                    if not do_multiline_reformat and len(import_statement) > self.config['line_length']:
-                        import_statement = self._wrap(import_statement)
-
-                if import_statement:
-                    above_comments = self.comments['above']['from'].pop(module, None)
-                    if above_comments:
-                        section_output.extend(above_comments)
-                    section_output.append(import_statement)
-
-    def _multi_line_reformat(self, import_start, from_imports, comments):
-        output_mode = settings.WrapModes._fields[self.config['multi_line_output']].lower()
-        formatter = getattr(self, "_output_" + output_mode, self._output_grid)
-        dynamic_indent = " " * (len(import_start) + 1)
-        indent = self.config['indent']
-        line_length = self.config['wrap_length'] or self.config['line_length']
-        import_statement = formatter(import_start, copy.copy(from_imports),
-                                     dynamic_indent, indent, line_length, comments)
-        if self.config['balanced_wrapping']:
-            lines = import_statement.split(self.line_separator)
-            line_count = len(lines)
-            if len(lines) > 1:
-                minimum_length = min(len(line) for line in lines[:-1])
-            else:
-                minimum_length = 0
-            new_import_statement = import_statement
-            while (len(lines[-1]) < minimum_length and
-                    len(lines) == line_count and line_length > 10):
-                import_statement = new_import_statement
-                line_length -= 1
-                new_import_statement = formatter(import_start, copy.copy(from_imports),
-                                                dynamic_indent, indent, line_length, comments)
-                lines = new_import_statement.split(self.line_separator)
-        if import_statement.count(self.line_separator) == 0:
-            return self._wrap(import_statement)
-        return import_statement
-
-    def _add_formatted_imports(self):
-        """Adds the imports back to the file.
-
-        (at the index of the first import) sorted alphabetically and split between groups
-
-        """
-        sort_ignore_case = self.config['force_alphabetical_sort_within_sections']
-        sections = itertools.chain(self.sections, self.config['forced_separate'])
-
-        if self.config['no_sections']:
-            self.imports['no_sections'] = {'straight': [], 'from': {}}
-            for section in sections:
-                self.imports['no_sections']['straight'].extend(self.imports[section].get('straight', []))
-                self.imports['no_sections']['from'].update(self.imports[section].get('from', {}))
-            sections = ('no_sections', )
-
-        output = []
-        pending_lines_before = False
-        for section in sections:
-            straight_modules = self.imports[section]['straight']
-            straight_modules = nsorted(straight_modules, key=lambda key: self._module_key(key, self.config, section_name=section))
-            from_modules = self.imports[section]['from']
-            from_modules = nsorted(from_modules, key=lambda key: self._module_key(key, self.config, section_name=section))
-
-            section_output = []
-            if self.config['from_first']:
-                self._add_from_imports(from_modules, section, section_output, sort_ignore_case)
-                if self.config['lines_between_types'] and from_modules and straight_modules:
-                    section_output.extend([''] * self.config['lines_between_types'])
-                self._add_straight_imports(straight_modules, section, section_output)
-            else:
-                self._add_straight_imports(straight_modules, section, section_output)
-                if self.config['lines_between_types'] and from_modules and straight_modules:
-                    section_output.extend([''] * self.config['lines_between_types'])
-                self._add_from_imports(from_modules, section, section_output, sort_ignore_case)
-
-            if self.config['force_sort_within_sections']:
-                def by_module(line):
-                    section = 'B'
-                    if line.startswith('#'):
-                        return 'AA'
-
-                    line = re.sub('^from ', '', line)
-                    line = re.sub('^import ', '', line)
-                    if line.split(' ')[0] in self.config['force_to_top']:
-                        section = 'A'
-                    if not self.config['order_by_type']:
-                        line = line.lower()
-                    return '{0}{1}'.format(section, line)
-                section_output = nsorted(section_output, key=by_module)
-
-            section_name = section
-            no_lines_before = section_name in self.config['no_lines_before']
-
-            if section_output:
-                if section_name in self.place_imports:
-                    self.place_imports[section_name] = section_output
-                    continue
-
-                section_title = self.config.get('import_heading_' + str(section_name).lower(), '')
-                if section_title:
-                    section_comment = "# {0}".format(section_title)
-                    if section_comment not in self.out_lines[0:1] and section_comment not in self.in_lines[0:1]:
-                        section_output.insert(0, section_comment)
-
-                if pending_lines_before or not no_lines_before:
-                    output += ([''] * self.config['lines_between_sections'])
-
-                output += section_output
-
-                pending_lines_before = False
-            else:
-                pending_lines_before = pending_lines_before or not no_lines_before
-
-        while output and output[-1].strip() == '':
-            output.pop()
-        while output and output[0].strip() == '':
-            output.pop(0)
-
-        output_at = 0
-        if self.import_index < self.original_length:
-            output_at = self.import_index
-        elif self._first_comment_index_end != -1 and self._first_comment_index_start <= 2:
-            output_at = self._first_comment_index_end
-        self.out_lines[output_at:0] = output
-
-        imports_tail = output_at + len(output)
-        while [character.strip() for character in self.out_lines[imports_tail: imports_tail + 1]] == [""]:
-            self.out_lines.pop(imports_tail)
-
-        if len(self.out_lines) > imports_tail:
-            next_construct = ""
-            self._in_quote = False
-            tail = self.out_lines[imports_tail:]
-
-            for index, line in enumerate(tail):
-                in_quote = self._in_quote
-                if not self._skip_line(line) and line.strip():
-                    if line.strip().startswith("#") and len(tail) > (index + 1) and tail[index + 1].strip():
-                        continue
-                    next_construct = line
-                    break
-                elif not in_quote:
-                    parts = line.split()
-                    if len(parts) >= 3 and parts[1] == '=' and "'" not in parts[0] and '"' not in parts[0]:
-                        next_construct = line
-                        break
-
-            if self.config['lines_after_imports'] != -1:
-                self.out_lines[imports_tail:0] = ["" for line in range(self.config['lines_after_imports'])]
-            elif self.extension != "pyi" and (next_construct.startswith("def ") or
-                                              next_construct.startswith("class ") or
-                                              next_construct.startswith("@") or
-                                              next_construct.startswith("async def")):
-                self.out_lines[imports_tail:0] = ["", ""]
-            else:
-                self.out_lines[imports_tail:0] = [""]
-
-        if self.place_imports:
-            new_out_lines = []
-            for index, line in enumerate(self.out_lines):
-                new_out_lines.append(line)
-                if line in self.import_placements:
-                    new_out_lines.extend(self.place_imports[self.import_placements[line]])
-                    if len(self.out_lines) <= index or self.out_lines[index + 1].strip() != "":
-                        new_out_lines.append("")
-            self.out_lines = new_out_lines
-
-    def _output_grid(self, statement, imports, white_space, indent, line_length, comments):
-        statement += "(" + imports.pop(0)
-        while imports:
-            next_import = imports.pop(0)
-            next_statement = self._add_comments(comments, statement + ", " + next_import)
-            if len(next_statement.split(self.line_separator)[-1]) + 1 > line_length:
-                lines = ['{0}{1}'.format(white_space, next_import.split(" ")[0])]
-                for part in next_import.split(" ")[1:]:
-                    new_line = '{0} {1}'.format(lines[-1], part)
-                    if len(new_line) + 1 > line_length:
-                        lines.append('{0}{1}'.format(white_space, part))
-                    else:
-                        lines[-1] = new_line
-                next_import = self.line_separator.join(lines)
-                statement = (self._add_comments(comments, "{0},".format(statement)) +
-                             "{0}{1}".format(self.line_separator, next_import))
-                comments = None
-            else:
-                statement += ", " + next_import
-        return statement + ("," if self.config['include_trailing_comma'] else "") + ")"
-
-    def _output_vertical(self, statement, imports, white_space, indent, line_length, comments):
-        first_import = self._add_comments(comments, imports.pop(0) + ",") + self.line_separator + white_space
-        return "{0}({1}{2}{3})".format(
-            statement,
-            first_import,
-            ("," + self.line_separator + white_space).join(imports),
-            "," if self.config['include_trailing_comma'] else "",
-        )
-
-    def _output_hanging_indent(self, statement, imports, white_space, indent, line_length, comments):
-        statement += imports.pop(0)
-        while imports:
-            next_import = imports.pop(0)
-            next_statement = self._add_comments(comments, statement + ", " + next_import)
-            if len(next_statement.split(self.line_separator)[-1]) + 3 > line_length:
-                next_statement = (self._add_comments(comments, "{0}, \\".format(statement)) +
-                                  "{0}{1}{2}".format(self.line_separator, indent, next_import))
-                comments = None
-            statement = next_statement
-        return statement
-
-    def _output_vertical_hanging_indent(self, statement, imports, white_space, indent, line_length, comments):
-        return "{0}({1}{2}{3}{4}{5}{2})".format(
-            statement,
-            self._add_comments(comments),
-            self.line_separator,
-            indent,
-            ("," + self.line_separator + indent).join(imports),
-            "," if self.config['include_trailing_comma'] else "",
-         )
-
-    def _output_vertical_grid_common(self, statement, imports, white_space, indent, line_length, comments,
-                                     need_trailing_char):
-        statement += self._add_comments(comments, "(") + self.line_separator + indent + imports.pop(0)
-        while imports:
-            next_import = imports.pop(0)
-            next_statement = "{0}, {1}".format(statement, next_import)
-            current_line_length = len(next_statement.split(self.line_separator)[-1])
-            if imports or need_trailing_char:
-                # If we have more imports we need to account for a comma after this import
-                # We might also need to account for a closing ) we're going to add.
-                current_line_length += 1
-            if current_line_length > line_length:
-                next_statement = "{0},{1}{2}{3}".format(statement, self.line_separator, indent, next_import)
-            statement = next_statement
-        if self.config['include_trailing_comma']:
-            statement += ','
-        return statement
-
-    def _output_vertical_grid(self, statement, imports, white_space, indent, line_length, comments):
-        return self._output_vertical_grid_common(statement, imports, white_space, indent, line_length, comments,
-                                                 True) + ")"
-
-    def _output_vertical_grid_grouped(self, statement, imports, white_space, indent, line_length, comments):
-        return self._output_vertical_grid_common(statement, imports, white_space, indent, line_length, comments,
-                                                 True) + self.line_separator + ")"
-
-    def _output_vertical_grid_grouped_no_comma(self, statement, imports, white_space, indent, line_length, comments):
-        return self._output_vertical_grid_common(statement, imports, white_space, indent, line_length, comments,
-                                                 False) + self.line_separator + ")"
-
-    def _output_noqa(self, statement, imports, white_space, indent, line_length, comments):
-        retval = '{0}{1}'.format(statement, ', '.join(imports))
-        comment_str = ' '.join(comments)
-        if comments:
-            if len(retval) + len(self.config['comment_prefix']) + 1 + len(comment_str) <= line_length:
-                return '{0}{1} {2}'.format(retval, self.config['comment_prefix'], comment_str)
-        else:
-            if len(retval) <= line_length:
-                return retval
-        if comments:
-            if "NOQA" in comments:
-                return '{0}{1} {2}'.format(retval, self.config['comment_prefix'], comment_str)
-            else:
-                return '{0}{1} NOQA {2}'.format(retval, self.config['comment_prefix'], comment_str)
-        else:
-            return '{0}{1} NOQA'.format(retval, self.config['comment_prefix'])
-
-    @staticmethod
-    def _strip_comments(line, comments=None):
-        """Removes comments from import line."""
-        if comments is None:
-            comments = []
-
-        new_comments = False
-        comment_start = line.find("#")
-        if comment_start != -1:
-            comments.append(line[comment_start + 1:].strip())
-            new_comments = True
-            line = line[:comment_start]
-
-        return line, comments, new_comments
-
-    @staticmethod
-    def _format_simplified(import_line):
-        import_line = import_line.strip()
-        if import_line.startswith("from "):
-            import_line = import_line.replace("from ", "")
-            import_line = import_line.replace(" import ", ".")
-        elif import_line.startswith("import "):
-            import_line = import_line.replace("import ", "")
-
-        return import_line
-
-    @staticmethod
-    def _format_natural(import_line):
-        import_line = import_line.strip()
-        if not import_line.startswith("from ") and not import_line.startswith("import "):
-            if "." not in import_line:
-                return "import {0}".format(import_line)
-            parts = import_line.split(".")
-            end = parts.pop(-1)
-            return "from {0} import {1}".format(".".join(parts), end)
-
-        return import_line
-
-    def _skip_line(self, line):
-        skip_line = self._in_quote
-        if self.index == 1 and line.startswith("#"):
-            self._in_top_comment = True
-            return True
-        elif self._in_top_comment:
-            if not line.startswith("#") or line in self._section_comments:
-                self._in_top_comment = False
-                self._first_comment_index_end = self.index - 1
-
-        if '"' in line or "'" in line:
-            index = 0
-            if self._first_comment_index_start == -1 and (line.startswith('"') or line.startswith("'")):
-                self._first_comment_index_start = self.index
-            while index < len(line):
-                if line[index] == "\\":
-                    index += 1
-                elif self._in_quote:
-                    if line[index:index + len(self._in_quote)] == self._in_quote:
-                        self._in_quote = False
-                        if self._first_comment_index_end < self._first_comment_index_start:
-                            self._first_comment_index_end = self.index
-                elif line[index] in ("'", '"'):
-                    long_quote = line[index:index + 3]
-                    if long_quote in ('"""', "'''"):
-                        self._in_quote = long_quote
-                        index += 2
-                    else:
-                        self._in_quote = line[index]
-                elif line[index] == "#":
-                    break
-                index += 1
-
-        return skip_line or self._in_quote or self._in_top_comment
-
-    def _strip_syntax(self, import_string):
-        import_string = import_string.replace("_import", "[[i]]")
-        for remove_syntax in ['\\', '(', ')', ',']:
-            import_string = import_string.replace(remove_syntax, " ")
-        import_list = import_string.split()
-        for key in ('from', 'import'):
-            if key in import_list:
-                import_list.remove(key)
-        import_string = ' '.join(import_list)
-        import_string = import_string.replace("[[i]]", "_import")
-        return import_string.replace("{ ", "{|").replace(" }", "|}")
-
-    def _parse(self):
-        """Parses a python file taking out and categorizing imports."""
-        self._in_quote = False
-        self._in_top_comment = False
-        while not self._at_end():
-            raw_line = line = self._get_line()
-            line = line.replace("from.import ", "from . import ")
-            line = line.replace("\t", " ").replace('import*', 'import *')
-            line = line.replace(" .import ", " . import ")
-            statement_index = self.index
-            skip_line = self._skip_line(line)
-
-            if line in self._section_comments and not skip_line:
-                if self.import_index == -1:
-                    self.import_index = self.index - 1
-                continue
-
-            if "isort:imports-" in line and line.startswith("#"):
-                section = line.split("isort:imports-")[-1].split()[0].upper()
-                self.place_imports[section] = []
-                self.import_placements[line] = section
-
-            if ";" in line:
-                for part in (part.strip() for part in line.split(";")):
-                    if part and not part.startswith("from ") and not part.startswith("import "):
-                        skip_line = True
-
-            import_type = self._import_type(line)
-            if not import_type or skip_line:
-                self.out_lines.append(raw_line)
-                continue
-
-            for line in (line.strip() for line in line.split(";")):
-                import_type = self._import_type(line)
-                if not import_type:
-                    self.out_lines.append(line)
-                    continue
-
-                if self.import_index == -1:
-                    self.import_index = self.index - 1
-                nested_comments = {}
-                import_string, comments, new_comments = self._strip_comments(line)
-                stripped_line = [part for part in self._strip_syntax(import_string).strip().split(" ") if part]
-                if import_type == "from" and len(stripped_line) == 2 and stripped_line[1] != "*" and new_comments:
-                    nested_comments[stripped_line[-1]] = comments[0]
-
-                if "(" in line.split("#")[0] and not self._at_end():
-                    while not line.strip().endswith(")") and not self._at_end():
-                        line, comments, new_comments = self._strip_comments(self._get_line(), comments)
-                        stripped_line = self._strip_syntax(line).strip()
-                        if import_type == "from" and stripped_line and " " not in stripped_line and new_comments:
-                            nested_comments[stripped_line] = comments[-1]
-                        import_string += self.line_separator + line
-                else:
-                    while line.strip().endswith("\\"):
-                        line, comments, new_comments = self._strip_comments(self._get_line(), comments)
-
-                        # Still need to check for parentheses after an escaped line
-                        if "(" in line.split("#")[0] and ")" not in line.split("#")[0] and not self._at_end():
-                            stripped_line = self._strip_syntax(line).strip()
-                            if import_type == "from" and stripped_line and " " not in stripped_line and new_comments:
-                                nested_comments[stripped_line] = comments[-1]
-                            import_string += self.line_separator + line
-
-                            while not line.strip().endswith(")") and not self._at_end():
-                                line, comments, new_comments = self._strip_comments(self._get_line(), comments)
-                                stripped_line = self._strip_syntax(line).strip()
-                                if import_type == "from" and stripped_line and " " not in stripped_line and new_comments:
-                                    nested_comments[stripped_line] = comments[-1]
-                                import_string += self.line_separator + line
-
-                        stripped_line = self._strip_syntax(line).strip()
-                        if import_type == "from" and stripped_line and " " not in stripped_line and new_comments:
-                            nested_comments[stripped_line] = comments[-1]
-                        if import_string.strip().endswith(" import") or line.strip().startswith("import "):
-                            import_string += self.line_separator + line
-                        else:
-                            import_string = import_string.rstrip().rstrip("\\") + " " + line.lstrip()
-
-                if import_type == "from":
-                    import_string = import_string.replace("import(", "import (")
-                    parts = import_string.split(" import ")
-                    from_import = parts[0].split(" ")
-                    import_string = " import ".join([from_import[0] + " " + "".join(from_import[1:])] + parts[1:])
-
-                imports = [item.replace("{|", "{ ").replace("|}", " }") for item in
-                           self._strip_syntax(import_string).split()]
-                if "as" in imports and (imports.index('as') + 1) < len(imports):
-                    while "as" in imports:
-                        index = imports.index('as')
-                        if import_type == "from":
-                            module = imports[0] + "." + imports[index - 1]
-                            self.as_map[module] = imports[index + 1]
-                        else:
-                            module = imports[index - 1]
-                            self.as_map[module] = imports[index + 1]
-                        if not self.config['combine_as_imports']:
-                            self.comments['straight'][module] = comments
-                            comments = []
-                        del imports[index:index + 2]
-                if import_type == "from":
-                    import_from = imports.pop(0)
-                    placed_module = self.place_module(import_from)
-                    if self.config['verbose']:
-                        print("from-type place_module for %s returned %s" % (import_from, placed_module))
-                    if placed_module == '':
-                        print(
-                            "WARNING: could not place module {0} of line {1} --"
-                            " Do you need to define a default section?".format(import_from, line)
-                        )
-                    root = self.imports[placed_module][import_type]
-                    for import_name in imports:
-                        associated_comment = nested_comments.get(import_name)
-                        if associated_comment:
-                            self.comments['nested'].setdefault(import_from, {})[import_name] = associated_comment
-                            comments.pop(comments.index(associated_comment))
-                    if comments:
-                        self.comments['from'].setdefault(import_from, []).extend(comments)
-
-                    if len(self.out_lines) > max(self.import_index, self._first_comment_index_end + 1, 1) - 1:
-                        last = self.out_lines and self.out_lines[-1].rstrip() or ""
-                        while (last.startswith("#") and not last.endswith('"""') and not last.endswith("'''") and
-                               'isort:imports-' not in last):
-                            self.comments['above']['from'].setdefault(import_from, []).insert(0, self.out_lines.pop(-1))
-                            if len(self.out_lines) > max(self.import_index - 1, self._first_comment_index_end + 1, 1) - 1:
-                                last = self.out_lines[-1].rstrip()
-                            else:
-                                last = ""
-                        if statement_index - 1 == self.import_index:
-                            self.import_index -= len(self.comments['above']['from'].get(import_from, []))
-
-                    if import_from not in root:
-                        root[import_from] = OrderedDict()
-                    root[import_from].update((module, None) for module in imports)
-                else:
-                    for module in imports:
-                        if comments:
-                            self.comments['straight'][module] = comments
-                            comments = None
-
-                        if len(self.out_lines) > max(self.import_index, self._first_comment_index_end + 1, 1) - 1:
-
-                            last = self.out_lines and self.out_lines[-1].rstrip() or ""
-                            while (last.startswith("#") and not last.endswith('"""') and not last.endswith("'''") and
-                                   'isort:imports-' not in last):
-                                self.comments['above']['straight'].setdefault(module, []).insert(0,
-                                                                                                 self.out_lines.pop(-1))
-                                if len(self.out_lines) > 0 and len(self.out_lines) != self._first_comment_index_end:
-                                    last = self.out_lines[-1].rstrip()
-                                else:
-                                    last = ""
-                            if self.index - 1 == self.import_index:
-                                self.import_index -= len(self.comments['above']['straight'].get(module, []))
-                        placed_module = self.place_module(module)
-                        if self.config['verbose']:
-                            print("else-type place_module for %s returned %s" % (module, placed_module))
-                        if placed_module == '':
-                            print(
-                                "WARNING: could not place module {0} of line {1} --"
-                                " Do you need to define a default section?".format(import_from, line)
-                            )
-                        self.imports[placed_module][import_type][module] = None
-
-
-def coding_check(lines, default='utf-8'):
-
-    # see https://www.python.org/dev/peps/pep-0263/
-    pattern = re.compile(br'coding[:=]\s*([-\w.]+)')
-
-    for line_number, line in enumerate(lines, 1):
-        groups = re.findall(pattern, line)
-        if groups:
-            return groups[0].decode('ascii')
-        if line_number > 2:
-            break
-
-    return default
diff --git a/venv/Lib/site-packages/isort/main.py b/venv/Lib/site-packages/isort/main.py
deleted file mode 100644
index fe36d11..0000000
--- a/venv/Lib/site-packages/isort/main.py
+++ /dev/null
@@ -1,401 +0,0 @@
-'''  Tool for sorting imports alphabetically, and automatically separated into sections.
-
-Copyright (C) 2013  Timothy Edmund Crosley
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of this software and associated
-documentation files (the "Software"), to deal in the Software without restriction, including without limitation
-the rights to use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of the Software, and
-to permit persons to whom the Software is furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all copies or
-substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED
-TO THE WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL
-THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF
-CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-OTHER DEALINGS IN THE SOFTWARE.
-
-'''
-from __future__ import absolute_import, division, print_function, unicode_literals
-
-import argparse
-import functools
-import glob
-import os
-import re
-import sys
-
-import setuptools
-
-from isort import SortImports, __version__
-from isort.settings import DEFAULT_SECTIONS, WrapModes, default, from_path, should_skip
-
-INTRO = r"""
-/#######################################################################\
-
-     `sMMy`
-     .yyyy-                                                      `
-    ##soos##                                                    ./o.
-          `     ``..-..`         ``...`.``         `   ```` ``-ssso```
-     .s:-y-   .+osssssso/.     ./ossss+:so+:`    :+o-`/osso:+sssssssso/
-     .s::y-   osss+.``.``     -ssss+-.`-ossso`   ssssso/::..::+ssss:::.
-     .s::y-   /ssss+//:-.`   `ssss+     `ssss+   sssso`       :ssss`
-     .s::y-   `-/+oossssso/  `ssss/      sssso   ssss/        :ssss`
-     .y-/y-       ````:ssss`  ossso.    :ssss:   ssss/        :ssss.
-     `/so:`    `-//::/osss+   `+ssss+-/ossso:    /sso-        `osssso/.
-       \/      `-/oooo++/-      .:/++:/++/-`      ..           `://++/.
-
-
-         isort your Python imports for you so you don't have to
-
-                            VERSION {0}
-
-\########################################################################/
-""".format(__version__)
-
-shebang_re = re.compile(br'^#!.*\bpython[23w]?\b')
-
-
-def is_python_file(path):
-    _root, ext = os.path.splitext(path)
-    if ext in ('.py', '.pyi'):
-        return True
-    if ext in ('.pex', ):
-        return False
-
-    # Skip editor backup files.
-    if path.endswith('~'):
-        return False
-
-    try:
-        with open(path, 'rb') as fp:
-            line = fp.readline(100)
-    except IOError:
-        return False
-    else:
-        return bool(shebang_re.match(line))
-
-
-class SortAttempt(object):
-    def __init__(self, incorrectly_sorted, skipped):
-        self.incorrectly_sorted = incorrectly_sorted
-        self.skipped = skipped
-
-
-def sort_imports(file_name, **arguments):
-    try:
-        result = SortImports(file_name, **arguments)
-        return SortAttempt(result.incorrectly_sorted, result.skipped)
-    except IOError as e:
-        print("WARNING: Unable to parse file {0} due to {1}".format(file_name, e))
-        return None
-
-
-def iter_source_code(paths, config, skipped):
-    """Iterate over all Python source files defined in paths."""
-    if 'not_skip' in config:
-        config['skip'] = list(set(config['skip']).difference(config['not_skip']))
-
-    for path in paths:
-        if os.path.isdir(path):
-            for dirpath, dirnames, filenames in os.walk(path, topdown=True, followlinks=True):
-                for dirname in list(dirnames):
-                    if should_skip(dirname, config, dirpath):
-                        skipped.append(dirname)
-                        dirnames.remove(dirname)
-                for filename in filenames:
-                    filepath = os.path.join(dirpath, filename)
-                    if is_python_file(filepath):
-                        relative_file = os.path.relpath(filepath, path)
-                        if should_skip(relative_file, config, path):
-                            skipped.append(filename)
-                        else:
-                            yield filepath
-        else:
-            yield path
-
-
-class ISortCommand(setuptools.Command):
-    """The :class:`ISortCommand` class is used by setuptools to perform
-    imports checks on registered modules.
-    """
-
-    description = "Run isort on modules registered in setuptools"
-    user_options = []
-
-    def initialize_options(self):
-        default_settings = default.copy()
-        for key, value in default_settings.items():
-            setattr(self, key, value)
-
-    def finalize_options(self):
-        "Get options from config files."
-        self.arguments = {}
-        computed_settings = from_path(os.getcwd())
-        for key, value in computed_settings.items():
-            self.arguments[key] = value
-
-    def distribution_files(self):
-        """Find distribution packages."""
-        # This is verbatim from flake8
-        if self.distribution.packages:
-            package_dirs = self.distribution.package_dir or {}
-            for package in self.distribution.packages:
-                pkg_dir = package
-                if package in package_dirs:
-                    pkg_dir = package_dirs[package]
-                elif '' in package_dirs:
-                    pkg_dir = package_dirs[''] + os.path.sep + pkg_dir
-                yield pkg_dir.replace('.', os.path.sep)
-
-        if self.distribution.py_modules:
-            for filename in self.distribution.py_modules:
-                yield "%s.py" % filename
-        # Don't miss the setup.py file itself
-        yield "setup.py"
-
-    def run(self):
-        arguments = self.arguments
-        wrong_sorted_files = False
-        arguments['check'] = True
-        for path in self.distribution_files():
-            for python_file in glob.iglob(os.path.join(path, '*.py')):
-                try:
-                    incorrectly_sorted = SortImports(python_file, **arguments).incorrectly_sorted
-                    if incorrectly_sorted:
-                        wrong_sorted_files = True
-                except IOError as e:
-                    print("WARNING: Unable to parse file {0} due to {1}".format(python_file, e))
-        if wrong_sorted_files:
-            sys.exit(1)
-
-
-def parse_args(argv=None):
-    parser = argparse.ArgumentParser(description='Sort Python import definitions alphabetically '
-                                                 'within logical sections. Run with no arguments to run '
-                                                 'interactively. Run with `-` as the first argument to read from '
-                                                 'stdin. Otherwise provide a list of files to sort.')
-    inline_args_group = parser.add_mutually_exclusive_group()
-    parser.add_argument('-a', '--add-import', dest='add_imports', action='append',
-                        help='Adds the specified import line to all files, '
-                             'automatically determining correct placement.')
-    parser.add_argument('-ac', '--atomic', dest='atomic', action='store_true',
-                        help="Ensures the output doesn't save if the resulting file contains syntax errors.")
-    parser.add_argument('-af', '--force-adds', dest='force_adds', action='store_true',
-                        help='Forces import adds even if the original file is empty.')
-    parser.add_argument('-b', '--builtin', dest='known_standard_library', action='append',
-                        help='Force sortImports to recognize a module as part of the python standard library.')
-    parser.add_argument('-c', '--check-only', action='store_true', dest="check",
-                        help='Checks the file for unsorted / unformatted imports and prints them to the '
-                             'command line without modifying the file.')
-    parser.add_argument('-ca', '--combine-as', dest='combine_as_imports', action='store_true',
-                        help="Combines as imports on the same line.")
-    parser.add_argument('-cs', '--combine-star', dest='combine_star', action='store_true',
-                        help="Ensures that if a star import is present, nothing else is imported from that namespace.")
-    parser.add_argument('-d', '--stdout', help='Force resulting output to stdout, instead of in-place.',
-                        dest='write_to_stdout', action='store_true')
-    parser.add_argument('-df', '--diff', dest='show_diff', action='store_true',
-                        help="Prints a diff of all the changes isort would make to a file, instead of "
-                             "changing it in place")
-    parser.add_argument('-ds', '--no-sections', help='Put all imports into the same section bucket', dest='no_sections',
-                        action='store_true')
-    parser.add_argument('-dt', '--dont-order-by-type', dest='dont_order_by_type',
-                        action='store_true', help='Only order imports alphabetically, do not attempt type ordering')
-    parser.add_argument('-e', '--balanced', dest='balanced_wrapping', action='store_true',
-                        help='Balances wrapping to produce the most consistent line length possible')
-    parser.add_argument('-f', '--future', dest='known_future_library', action='append',
-                        help='Force sortImports to recognize a module as part of the future compatibility libraries.')
-    parser.add_argument('-fas', '--force-alphabetical-sort', action='store_true', dest="force_alphabetical_sort",
-                        help='Force all imports to be sorted as a single section')
-    parser.add_argument('-fass', '--force-alphabetical-sort-within-sections', action='store_true',
-                        dest="force_alphabetical_sort", help='Force all imports to be sorted alphabetically within a '
-                                                             'section')
-    parser.add_argument('-ff', '--from-first', dest='from_first',
-                        help="Switches the typical ordering preference, showing from imports first then straight ones.")
-    parser.add_argument('-fgw', '--force-grid-wrap', nargs='?', const=2, type=int, dest="force_grid_wrap",
-                        help='Force number of from imports (defaults to 2) to be grid wrapped regardless of line '
-                             'length')
-    parser.add_argument('-fss', '--force-sort-within-sections', action='store_true', dest="force_sort_within_sections",
-                        help='Force imports to be sorted by module, independent of import_type')
-    parser.add_argument('-i', '--indent', help='String to place for indents defaults to "    " (4 spaces).',
-                        dest='indent', type=str)
-    parser.add_argument('-j', '--jobs', help='Number of files to process in parallel.',
-                        dest='jobs', type=int)
-    parser.add_argument('-k', '--keep-direct-and-as', dest='keep_direct_and_as_imports', action='store_true',
-                        help="Turns off default behavior that removes direct imports when as imports exist.")
-    parser.add_argument('-l', '--lines', help='[Deprecated] The max length of an import line (used for wrapping '
-                        'long imports).',
-                        dest='line_length', type=int)
-    parser.add_argument('-lai', '--lines-after-imports', dest='lines_after_imports', type=int)
-    parser.add_argument('-lbt', '--lines-between-types', dest='lines_between_types', type=int)
-    parser.add_argument('-le', '--line-ending', dest='line_ending',
-                        help="Forces line endings to the specified value. If not set, values will be guessed per-file.")
-    parser.add_argument('-ls', '--length-sort', help='Sort imports by their string length.',
-                        dest='length_sort', action='store_true')
-    parser.add_argument('-m', '--multi-line', dest='multi_line_output', type=int, choices=range(len(WrapModes)),
-                        help='Multi line output (0-grid, 1-vertical, 2-hanging, 3-vert-hanging, 4-vert-grid, '
-                        '5-vert-grid-grouped, 6-vert-grid-grouped-no-comma).')
-    inline_args_group.add_argument('-nis', '--no-inline-sort', dest='no_inline_sort', action='store_true',
-                        help='Leaves `from` imports with multiple imports \'as-is\' (e.g. `from foo import a, c ,b`).')
-    parser.add_argument('-nlb', '--no-lines-before', help='Sections which should not be split with previous by empty lines',
-                        dest='no_lines_before', action='append')
-    parser.add_argument('-ns', '--dont-skip', help='Files that sort imports should never skip over.',
-                        dest='not_skip', action='append')
-    parser.add_argument('-o', '--thirdparty', dest='known_third_party', action='append',
-                        help='Force sortImports to recognize a module as being part of a third party library.')
-    parser.add_argument('-ot', '--order-by-type', dest='order_by_type',
-                        action='store_true', help='Order imports by type in addition to alphabetically')
-    parser.add_argument('-p', '--project', dest='known_first_party', action='append',
-                        help='Force sortImports to recognize a module as being part of the current python project.')
-    parser.add_argument('-q', '--quiet', action='store_true', dest="quiet",
-                        help='Shows extra quiet output, only errors are outputted.')
-    parser.add_argument('-r', dest='ambiguous_r_flag', action='store_true')
-    parser.add_argument('-rm', '--remove-import', dest='remove_imports', action='append',
-                        help='Removes the specified import from all files.')
-    parser.add_argument('-rr', '--reverse-relative', dest='reverse_relative', action='store_true',
-                        help='Reverse order of relative imports.')
-    parser.add_argument('-rc', '--recursive', dest='recursive', action='store_true',
-                        help='Recursively look for Python files of which to sort imports')
-    parser.add_argument('-s', '--skip', help='Files that sort imports should skip over. If you want to skip multiple '
-                        'files you should specify twice: --skip file1 --skip file2.', dest='skip', action='append')
-    parser.add_argument('-sd', '--section-default', dest='default_section',
-                        help='Sets the default section for imports (by default FIRSTPARTY) options: ' +
-                        str(DEFAULT_SECTIONS))
-    parser.add_argument('-sg', '--skip-glob', help='Files that sort imports should skip over.', dest='skip_glob',
-                        action='append')
-    inline_args_group.add_argument('-sl', '--force-single-line-imports', dest='force_single_line', action='store_true',
-                        help='Forces all from imports to appear on their own line')
-    parser.add_argument('-sp', '--settings-path', dest="settings_path",
-                        help='Explicitly set the settings path instead of auto determining based on file location.')
-    parser.add_argument('-t', '--top', help='Force specific imports to the top of their appropriate section.',
-                        dest='force_to_top', action='append')
-    parser.add_argument('-tc', '--trailing-comma', dest='include_trailing_comma', action='store_true',
-                        help='Includes a trailing comma on multi line imports that include parentheses.')
-    parser.add_argument('-up', '--use-parentheses', dest='use_parentheses', action='store_true',
-                        help='Use parenthesis for line continuation on length limit instead of slashes.')
-    parser.add_argument('-v', '--version', action='store_true', dest='show_version')
-    parser.add_argument('-vb', '--verbose', action='store_true', dest="verbose",
-                        help='Shows verbose output, such as when files are skipped or when a check is successful.')
-    parser.add_argument('--virtual-env', dest='virtual_env',
-                        help='Virtual environment to use for determining whether a package is third-party')
-    parser.add_argument('--conda-env', dest='conda_env',
-                        help='Conda environment to use for determining whether a package is third-party')
-    parser.add_argument('-vn', '--version-number', action='version', version=__version__,
-                        help='Returns just the current version number without the logo')
-    parser.add_argument('-w', '--line-width', help='The max length of an import line (used for wrapping long imports).',
-                        dest='line_length', type=int)
-    parser.add_argument('-wl', '--wrap-length', dest='wrap_length',
-                        help="Specifies how long lines that are wrapped should be, if not set line_length is used.")
-    parser.add_argument('-ws', '--ignore-whitespace', action='store_true', dest="ignore_whitespace",
-                        help='Tells isort to ignore whitespace differences when --check-only is being used.')
-    parser.add_argument('-y', '--apply', dest='apply', action='store_true',
-                        help='Tells isort to apply changes recursively without asking')
-    parser.add_argument('--unsafe', dest='unsafe', action='store_true',
-                        help='Tells isort to look for files in standard library directories, etc. '
-                             'where it may not be safe to operate in')
-    parser.add_argument('--case-sensitive', dest='case_sensitive', action='store_true',
-                        help='Tells isort to include casing when sorting module names')
-    parser.add_argument('--filter-files', dest='filter_files', action='store_true',
-                        help='Tells isort to filter files even when they are explicitly passed in as part of the command')
-    parser.add_argument('files', nargs='*', help='One or more Python source files that need their imports sorted.')
-
-    arguments = {key: value for key, value in vars(parser.parse_args(argv)).items() if value}
-    if 'dont_order_by_type' in arguments:
-        arguments['order_by_type'] = False
-    if arguments.pop('unsafe', False):
-        arguments['safety_excludes'] = False
-    return arguments
-
-
-def main(argv=None):
-    arguments = parse_args(argv)
-    if arguments.get('show_version'):
-        print(INTRO)
-        return
-
-    if arguments.get('ambiguous_r_flag'):
-        print('ERROR: Deprecated -r flag set. This flag has been replaced with -rm to remove ambiguity between it and '
-              '-rc for recursive')
-        sys.exit(1)
-
-    arguments['check_skip'] = False
-    if 'settings_path' in arguments:
-        sp = arguments['settings_path']
-        arguments['settings_path'] = os.path.abspath(sp) if os.path.isdir(sp) else os.path.dirname(os.path.abspath(sp))
-        if not os.path.isdir(arguments['settings_path']):
-            print("WARNING: settings_path dir does not exist: {0}".format(arguments['settings_path']))
-
-    if 'virtual_env' in arguments:
-        venv = arguments['virtual_env']
-        arguments['virtual_env'] = os.path.abspath(venv)
-        if not os.path.isdir(arguments['virtual_env']):
-            print("WARNING: virtual_env dir does not exist: {0}".format(arguments['virtual_env']))
-
-    file_names = arguments.pop('files', [])
-    if file_names == ['-']:
-        try:
-            # python 3
-            file_ = sys.stdin.buffer
-        except AttributeError:
-            # python 2
-            file_ = sys.stdin
-        SortImports(file_=file_, write_to_stdout=True, **arguments)
-    else:
-        if not file_names:
-            file_names = ['.']
-            arguments['recursive'] = True
-            if not arguments.get('apply', False):
-                arguments['ask_to_apply'] = True
-
-        config = from_path(arguments.get('settings_path', '') or os.path.abspath(file_names[0]) or os.getcwd()).copy()
-        config.update(arguments)
-        wrong_sorted_files = False
-        skipped = []
-
-        if config.get('filter_files'):
-            filtered_files = []
-            for file_name in file_names:
-                if should_skip(file_name, config):
-                    skipped.append(file_name)
-                else:
-                    filtered_files.append(file_name)
-            file_names = filtered_files
-
-        if arguments.get('recursive', False):
-            file_names = iter_source_code(file_names, config, skipped)
-        num_skipped = 0
-        if config['verbose'] or config.get('show_logo', False):
-            print(INTRO)
-
-        jobs = arguments.get('jobs')
-        if jobs:
-            import multiprocessing
-            executor = multiprocessing.Pool(jobs)
-            attempt_iterator = executor.imap(functools.partial(sort_imports, **arguments), file_names)
-        else:
-            attempt_iterator = (sort_imports(file_name, **arguments) for file_name in file_names)
-
-        for sort_attempt in attempt_iterator:
-            if not sort_attempt:
-                continue
-            incorrectly_sorted = sort_attempt.incorrectly_sorted
-            if arguments.get('check', False) and incorrectly_sorted:
-                wrong_sorted_files = True
-            if sort_attempt.skipped:
-                num_skipped += 1
-
-        if wrong_sorted_files:
-            sys.exit(1)
-
-        num_skipped += len(skipped)
-        if num_skipped and not arguments.get('quiet', False):
-            if config['verbose']:
-                for was_skipped in skipped:
-                    print("WARNING: {0} was skipped as it's listed in 'skip' setting"
-                        " or matches a glob in 'skip_glob' setting".format(was_skipped))
-            print("Skipped {0} files".format(num_skipped))
-
-
-if __name__ == "__main__":
-    main()
diff --git a/venv/Lib/site-packages/isort/natural.py b/venv/Lib/site-packages/isort/natural.py
deleted file mode 100644
index c02b42c..0000000
--- a/venv/Lib/site-packages/isort/natural.py
+++ /dev/null
@@ -1,47 +0,0 @@
-"""isort/natural.py.
-
-Enables sorting strings that contain numbers naturally
-
-usage:
-    natural.nsorted(list)
-
-Copyright (C) 2013  Timothy Edmund Crosley
-
-Implementation originally from @HappyLeapSecond stack overflow user in response to:
-   https://stackoverflow.com/questions/5967500/how-to-correctly-sort-a-string-with-a-number-inside
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of this software and associated
-documentation files (the "Software"), to deal in the Software without restriction, including without limitation
-the rights to use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of the Software, and
-to permit persons to whom the Software is furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all copies or
-substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED
-TO THE WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL
-THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF
-CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-OTHER DEALINGS IN THE SOFTWARE.
-
-"""
-import re
-
-
-def _atoi(text):
-    return int(text) if text.isdigit() else text
-
-
-def _natural_keys(text):
-    return [_atoi(c) for c in re.split(r'(\d+)', text)]
-
-
-def nsorted(to_sort, key=None):
-    """Returns a naturally sorted list"""
-    if key is None:
-        key_callback = _natural_keys
-    else:
-        def key_callback(item):
-            return _natural_keys(key(item))
-
-    return sorted(to_sort, key=key_callback)
diff --git a/venv/Lib/site-packages/isort/pie_slice.py b/venv/Lib/site-packages/isort/pie_slice.py
deleted file mode 100644
index 569ea76..0000000
--- a/venv/Lib/site-packages/isort/pie_slice.py
+++ /dev/null
@@ -1,154 +0,0 @@
-"""pie_slice/overrides.py.
-
-Overrides Python syntax to conform to the Python3 version as much as possible using a '*' import
-
-Copyright (C) 2013  Timothy Edmund Crosley
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of this software and associated
-documentation files (the "Software"), to deal in the Software without restriction, including without limitation
-the rights to use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of the Software, and
-to permit persons to whom the Software is furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all copies or
-substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED
-TO THE WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL
-THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF
-CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-OTHER DEALINGS IN THE SOFTWARE.
-
-"""
-from __future__ import absolute_import
-
-import collections
-import sys
-
-__version__ = "1.1.0"
-
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-VERSION = sys.version_info
-
-__all__ = ['PY2', 'PY3', 'lru_cache', 'apply_changes_to_python_environment']
-
-
-if PY3:
-    input = input
-
-    def apply_changes_to_python_environment():
-        pass
-else:
-    input = raw_input  # noqa: F821
-
-    python_environment_changes_applied = False
-
-    import sys
-    stdout = sys.stdout
-    stderr = sys.stderr
-
-    def apply_changes_to_python_environment():
-        global python_environment_changes_applied
-        if python_environment_changes_applied or sys.getdefaultencoding() == 'utf-8':
-            python_environment_changes_applied = True
-            return
-
-        try:
-            reload(sys)
-            sys.stdout = stdout
-            sys.stderr = stderr
-            sys.setdefaultencoding('utf-8')
-        except NameError:  # Python 3
-            sys.exit('This should not happen!')
-
-        python_environment_changes_applied = True
-
-
-if sys.version_info < (3, 2):
-    try:
-        from threading import Lock
-    except ImportError:
-        from dummy_threading import Lock
-
-    from functools import wraps
-
-    _CacheInfo = collections.namedtuple("CacheInfo", "hits misses maxsize currsize")
-
-    def lru_cache(maxsize=100):
-        """Least-recently-used cache decorator.
-        Taking from: https://github.com/MiCHiLU/python-functools32/blob/master/functools32/functools32.py
-        with slight modifications.
-        If *maxsize* is set to None, the LRU features are disabled and the cache
-        can grow without bound.
-        Arguments to the cached function must be hashable.
-        View the cache statistics named tuple (hits, misses, maxsize, currsize) with
-        f.cache_info().  Clear the cache and statistics with f.cache_clear().
-        Access the underlying function with f.__wrapped__.
-        See: https://en.wikipedia.org/wiki/Cache_algorithms#Least_Recently_Used
-
-        """
-        def decorating_function(user_function, tuple=tuple, sorted=sorted, len=len, KeyError=KeyError):
-            hits, misses = [0], [0]
-            kwd_mark = (object(),)          # separates positional and keyword args
-            lock = Lock()
-
-            if maxsize is None:
-                CACHE = {}
-
-                @wraps(user_function)
-                def wrapper(*args, **kwds):
-                    key = args
-                    if kwds:
-                        key += kwd_mark + tuple(sorted(kwds.items()))
-                    try:
-                        result = CACHE[key]
-                        hits[0] += 1
-                        return result
-                    except KeyError:
-                        pass
-                    result = user_function(*args, **kwds)
-                    CACHE[key] = result
-                    misses[0] += 1
-                    return result
-            else:
-                CACHE = collections.OrderedDict()
-
-                @wraps(user_function)
-                def wrapper(*args, **kwds):
-                    key = args
-                    if kwds:
-                        key += kwd_mark + tuple(sorted(kwds.items()))
-                    with lock:
-                        cached = CACHE.get(key, None)
-                        if cached:
-                            del CACHE[key]
-                            CACHE[key] = cached
-                            hits[0] += 1
-                            return cached
-                    result = user_function(*args, **kwds)
-                    with lock:
-                        CACHE[key] = result     # record recent use of this key
-                        misses[0] += 1
-                        while len(CACHE) > maxsize:
-                            CACHE.popitem(last=False)
-                    return result
-
-            def cache_info():
-                """Report CACHE statistics."""
-                with lock:
-                    return _CacheInfo(hits[0], misses[0], maxsize, len(CACHE))
-
-            def cache_clear():
-                """Clear the CACHE and CACHE statistics."""
-                with lock:
-                    CACHE.clear()
-                    hits[0] = misses[0] = 0
-
-            wrapper.cache_info = cache_info
-            wrapper.cache_clear = cache_clear
-            return wrapper
-
-        return decorating_function
-
-else:
-    from functools import lru_cache
diff --git a/venv/Lib/site-packages/isort/pylama_isort.py b/venv/Lib/site-packages/isort/pylama_isort.py
deleted file mode 100644
index 6fa235f..0000000
--- a/venv/Lib/site-packages/isort/pylama_isort.py
+++ /dev/null
@@ -1,29 +0,0 @@
-import os
-import sys
-
-from pylama.lint import Linter as BaseLinter
-
-from .isort import SortImports
-
-
-class Linter(BaseLinter):
-
-    def allow(self, path):
-        """Determine if this path should be linted."""
-        return path.endswith('.py')
-
-    def run(self, path, **meta):
-        """Lint the file. Return an array of error dicts if appropriate."""
-        with open(os.devnull, 'w') as devnull:
-            # Suppress isort messages
-            sys.stdout = devnull
-
-            if SortImports(path, check=True).incorrectly_sorted:
-                return [{
-                    'lnum': 0,
-                    'col': 0,
-                    'text': 'Incorrectly sorted imports.',
-                    'type': 'ISORT'
-                }]
-            else:
-                return []
diff --git a/venv/Lib/site-packages/isort/settings.py b/venv/Lib/site-packages/isort/settings.py
deleted file mode 100644
index a69471e..0000000
--- a/venv/Lib/site-packages/isort/settings.py
+++ /dev/null
@@ -1,356 +0,0 @@
-"""isort/settings.py.
-
-Defines how the default settings for isort should be loaded
-
-(First from the default setting dictionary at the top of the file, then overridden by any settings
- in ~/.isort.cfg or $XDG_CONFIG_HOME/isort.cfg if there are any)
-
-Copyright (C) 2013  Timothy Edmund Crosley
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of this software and associated
-documentation files (the "Software"), to deal in the Software without restriction, including without limitation
-the rights to use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of the Software, and
-to permit persons to whom the Software is furnished to do so, subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all copies or
-substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED
-TO THE WARRANTIES OF MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL
-THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF
-CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-OTHER DEALINGS IN THE SOFTWARE.
-
-"""
-from __future__ import absolute_import, division, print_function, unicode_literals
-
-import fnmatch
-import io
-import os
-import posixpath
-import re
-import sys
-import warnings
-from collections import namedtuple
-from distutils.util import strtobool
-
-from .pie_slice import lru_cache
-from .utils import difference, union
-
-try:
-    import configparser
-except ImportError:
-    import ConfigParser as configparser
-
-try:
-    import toml
-except ImportError:
-    toml = False
-
-try:
-    import appdirs
-    if appdirs.system == 'darwin':
-        appdirs.system = 'linux2'
-except ImportError:
-    appdirs = None
-
-MAX_CONFIG_SEARCH_DEPTH = 25  # The number of parent directories isort will look for a config file within
-DEFAULT_SECTIONS = ('FUTURE', 'STDLIB', 'THIRDPARTY', 'FIRSTPARTY', 'LOCALFOLDER')
-
-safety_exclude_re = re.compile(
-    r"/(\.eggs|\.git|\.hg|\.mypy_cache|\.nox|\.tox|\.venv|_build|buck-out|build|dist|\.pants\.d"
-    r"|lib/python[0-9].[0-9]+)/"
-)
-
-WrapModes = ('GRID', 'VERTICAL', 'HANGING_INDENT', 'VERTICAL_HANGING_INDENT', 'VERTICAL_GRID', 'VERTICAL_GRID_GROUPED',
-             'VERTICAL_GRID_GROUPED_NO_COMMA', 'NOQA')
-WrapModes = namedtuple('WrapModes', WrapModes)(*range(len(WrapModes)))
-
-# Note that none of these lists must be complete as they are simply fallbacks for when included auto-detection fails.
-default = {'force_to_top': [],
-           'skip': [],
-           'skip_glob': [],
-           'line_length': 79,
-           'wrap_length': 0,
-           'line_ending': None,
-           'sections': DEFAULT_SECTIONS,
-           'no_sections': False,
-           'known_future_library': ['__future__'],
-           'known_standard_library': ['AL', 'BaseHTTPServer', 'Bastion', 'CGIHTTPServer', 'Carbon', 'ColorPicker',
-                                      'ConfigParser', 'Cookie', 'DEVICE', 'DocXMLRPCServer', 'EasyDialogs', 'FL',
-                                      'FrameWork', 'GL', 'HTMLParser', 'MacOS', 'MimeWriter', 'MiniAEFrame', 'Nav',
-                                      'PixMapWrapper', 'Queue', 'SUNAUDIODEV', 'ScrolledText', 'SimpleHTTPServer',
-                                      'SimpleXMLRPCServer', 'SocketServer', 'StringIO', 'Tix', 'Tkinter', 'UserDict',
-                                      'UserList', 'UserString', 'W', '__builtin__', 'abc', 'aepack', 'aetools',
-                                      'aetypes', 'aifc', 'al', 'anydbm', 'applesingle', 'argparse', 'array', 'ast',
-                                      'asynchat', 'asyncio', 'asyncore', 'atexit', 'audioop', 'autoGIL', 'base64',
-                                      'bdb', 'binascii', 'binhex', 'bisect', 'bsddb', 'buildtools', 'builtins',
-                                      'bz2', 'cPickle', 'cProfile', 'cStringIO', 'calendar', 'cd', 'cfmfile', 'cgi',
-                                      'cgitb', 'chunk', 'cmath', 'cmd', 'code', 'codecs', 'codeop', 'collections',
-                                      'colorsys', 'commands', 'compileall', 'compiler', 'concurrent', 'configparser',
-                                      'contextlib', 'contextvars', 'cookielib', 'copy', 'copy_reg', 'copyreg', 'crypt', 'csv',
-                                      'ctypes', 'curses', 'dataclasses', 'datetime', 'dbhash', 'dbm', 'decimal', 'difflib',
-                                      'dircache', 'dis', 'distutils', 'dl', 'doctest', 'dumbdbm', 'dummy_thread',
-                                      'dummy_threading', 'email', 'encodings', 'ensurepip', 'enum', 'errno',
-                                      'exceptions', 'faulthandler', 'fcntl', 'filecmp', 'fileinput', 'findertools',
-                                      'fl', 'flp', 'fm', 'fnmatch', 'formatter', 'fpectl', 'fpformat', 'fractions',
-                                      'ftplib', 'functools', 'future_builtins', 'gc', 'gdbm', 'gensuitemodule',
-                                      'getopt', 'getpass', 'gettext', 'gl', 'glob', 'grp', 'gzip', 'hashlib',
-                                      'heapq', 'hmac', 'hotshot', 'html', 'htmlentitydefs', 'htmllib', 'http',
-                                      'httplib', 'ic', 'icopen', 'imageop', 'imaplib', 'imgfile', 'imghdr', 'imp',
-                                      'importlib', 'imputil', 'inspect', 'io', 'ipaddress', 'itertools', 'jpeg',
-                                      'json', 'keyword', 'lib2to3', 'linecache', 'locale', 'logging', 'lzma',
-                                      'macerrors', 'macostools', 'macpath', 'macresource', 'mailbox', 'mailcap',
-                                      'marshal', 'math', 'md5', 'mhlib', 'mimetools', 'mimetypes', 'mimify', 'mmap',
-                                      'modulefinder', 'msilib', 'msvcrt', 'multifile', 'multiprocessing', 'mutex',
-                                      'netrc', 'new', 'nis', 'nntplib', 'numbers', 'operator', 'optparse', 'os',
-                                      'ossaudiodev', 'parser', 'pathlib', 'pdb', 'pickle', 'pickletools', 'pipes',
-                                      'pkgutil', 'platform', 'plistlib', 'popen2', 'poplib', 'posix', 'posixfile',
-                                      'pprint', 'profile', 'pstats', 'pty', 'pwd', 'py_compile', 'pyclbr', 'pydoc',
-                                      'queue', 'quopri', 'random', 're', 'readline', 'reprlib', 'resource', 'rexec',
-                                      'rfc822', 'rlcompleter', 'robotparser', 'runpy', 'sched', 'secrets', 'select',
-                                      'selectors', 'sets', 'sgmllib', 'sha', 'shelve', 'shlex', 'shutil', 'signal',
-                                      'site', 'sitecustomize', 'smtpd', 'smtplib', 'sndhdr', 'socket', 'socketserver',
-                                      'spwd', 'sqlite3', 'ssl', 'stat', 'statistics', 'statvfs', 'string', 'stringprep',
-                                      'struct', 'subprocess', 'sunau', 'sunaudiodev', 'symbol', 'symtable', 'sys',
-                                      'sysconfig', 'syslog', 'tabnanny', 'tarfile', 'telnetlib', 'tempfile', 'termios',
-                                      'test', 'textwrap', 'this', 'thread', 'threading', 'time', 'timeit', 'tkinter',
-                                      'token', 'tokenize', 'trace', 'traceback', 'tracemalloc', 'ttk', 'tty', 'turtle',
-                                      'turtledemo', 'types', 'typing', 'unicodedata', 'unittest', 'urllib', 'urllib2',
-                                      'urlparse', 'usercustomize', 'uu', 'uuid', 'venv', 'videoreader',
-                                      'warnings', 'wave', 'weakref', 'webbrowser', 'whichdb', 'winreg', 'winsound',
-                                      'wsgiref', 'xdrlib', 'xml', 'xmlrpc', 'xmlrpclib', 'zipapp', 'zipfile',
-                                      'zipimport', 'zlib'],
-           'known_third_party': ['google.appengine.api'],
-           'known_first_party': [],
-           'multi_line_output': WrapModes.GRID,
-           'forced_separate': [],
-           'indent': ' ' * 4,
-           'comment_prefix': '  #',
-           'length_sort': False,
-           'add_imports': [],
-           'remove_imports': [],
-           'reverse_relative': False,
-           'force_single_line': False,
-           'default_section': 'FIRSTPARTY',
-           'import_heading_future': '',
-           'import_heading_stdlib': '',
-           'import_heading_thirdparty': '',
-           'import_heading_firstparty': '',
-           'import_heading_localfolder': '',
-           'balanced_wrapping': False,
-           'use_parentheses': False,
-           'order_by_type': True,
-           'atomic': False,
-           'lines_after_imports': -1,
-           'lines_between_sections': 1,
-           'lines_between_types': 0,
-           'combine_as_imports': False,
-           'combine_star': False,
-           'keep_direct_and_as_imports': False,
-           'include_trailing_comma': False,
-           'from_first': False,
-           'verbose': False,
-           'quiet': False,
-           'force_adds': False,
-           'force_alphabetical_sort_within_sections': False,
-           'force_alphabetical_sort': False,
-           'force_grid_wrap': 0,
-           'force_sort_within_sections': False,
-           'show_diff': False,
-           'ignore_whitespace': False,
-           'no_lines_before': [],
-           'no_inline_sort': False,
-           'ignore_comments': False,
-           'safety_excludes': True,
-           'case_sensitive': False}
-
-
-@lru_cache()
-def from_path(path):
-    computed_settings = default.copy()
-    isort_defaults = ['~/.isort.cfg']
-    if appdirs:
-        isort_defaults = [appdirs.user_config_dir('isort.cfg')] + isort_defaults
-
-    _update_settings_with_config(path, '.editorconfig', ['~/.editorconfig'], ('*', '*.py', '**.py'), computed_settings)
-    _update_settings_with_config(path, 'pyproject.toml', [], ('tool.isort', ), computed_settings)
-    _update_settings_with_config(path, '.isort.cfg', isort_defaults, ('settings', 'isort'), computed_settings)
-    _update_settings_with_config(path, 'setup.cfg', [], ('isort', 'tool:isort'), computed_settings)
-    _update_settings_with_config(path, 'tox.ini', [], ('isort', 'tool:isort'), computed_settings)
-    return computed_settings
-
-
-def _update_settings_with_config(path, name, default, sections, computed_settings):
-    editor_config_file = None
-    for potential_settings_path in default:
-        expanded = os.path.expanduser(potential_settings_path)
-        if os.path.exists(expanded):
-            editor_config_file = expanded
-            break
-
-    tries = 0
-    current_directory = path
-    while current_directory and tries < MAX_CONFIG_SEARCH_DEPTH:
-        potential_path = os.path.join(current_directory, str(name))
-        if os.path.exists(potential_path):
-            editor_config_file = potential_path
-            break
-
-        new_directory = os.path.split(current_directory)[0]
-        if current_directory == new_directory:
-            break
-        current_directory = new_directory
-        tries += 1
-
-    if editor_config_file and os.path.exists(editor_config_file):
-        _update_with_config_file(editor_config_file, sections, computed_settings)
-
-
-def _update_with_config_file(file_path, sections, computed_settings):
-    cwd = os.path.dirname(file_path)
-    settings = _get_config_data(file_path, sections).copy()
-    if not settings:
-        return
-
-    if file_path.endswith('.editorconfig'):
-        indent_style = settings.pop('indent_style', '').strip()
-        indent_size = settings.pop('indent_size', '').strip()
-        if indent_size == "tab":
-            indent_size = settings.pop('tab_width', '').strip()
-
-        if indent_style == 'space':
-            computed_settings['indent'] = ' ' * (indent_size and int(indent_size) or 4)
-        elif indent_style == 'tab':
-            computed_settings['indent'] = '\t' * (indent_size and int(indent_size) or 1)
-
-        max_line_length = settings.pop('max_line_length', '').strip()
-        if max_line_length:
-            computed_settings['line_length'] = float('inf') if max_line_length == 'off' else int(max_line_length)
-
-    for key, value in settings.items():
-        access_key = key.replace('not_', '').lower()
-        existing_value_type = type(default.get(access_key, ''))
-        if existing_value_type in (list, tuple):
-            # sections has fixed order values; no adding or substraction from any set
-            if access_key == 'sections':
-                computed_settings[access_key] = tuple(_as_list(value))
-            else:
-                existing_data = set(computed_settings.get(access_key, default.get(access_key)))
-                if key.startswith('not_'):
-                    computed_settings[access_key] = difference(existing_data, _as_list(value))
-                elif key.startswith('known_'):
-                    computed_settings[access_key] = union(existing_data, _abspaths(cwd, _as_list(value)))
-                else:
-                    computed_settings[access_key] = union(existing_data, _as_list(value))
-        elif existing_value_type == bool:
-            # Only some configuration formats support native boolean values.
-            if not isinstance(value, bool):
-                value = bool(strtobool(value))
-            computed_settings[access_key] = value
-        elif key.startswith('known_'):
-            computed_settings[access_key] = list(_abspaths(cwd, _as_list(value)))
-        elif key == 'force_grid_wrap':
-            try:
-                result = existing_value_type(value)
-            except ValueError:
-                # backwards compat
-                result = default.get(access_key) if value.lower().strip() == 'false' else 2
-            computed_settings[access_key] = result
-        else:
-            computed_settings[access_key] = existing_value_type(value)
-
-
-def _as_list(value):
-    if not isinstance(value, list):
-        value = value.replace('\n', ',').split(',')
-
-    return filter(bool, [item.strip() for item in value])
-
-
-def _abspaths(cwd, values):
-    paths = [
-        os.path.join(cwd, value)
-        if not value.startswith(os.path.sep) and value.endswith(os.path.sep)
-        else value
-        for value in values
-    ]
-    return paths
-
-
-@lru_cache()
-def _get_config_data(file_path, sections):
-    settings = {}
-
-    with io.open(file_path) as config_file:
-        if file_path.endswith('.toml'):
-            if toml:
-                config = toml.load(config_file)
-                for section in sections:
-                    config_section = config
-                    for key in section.split('.'):
-                        config_section = config_section.get(key, {})
-                    settings.update(config_section)
-            else:
-                if '[tool.isort]' in config_file.read():
-                    warnings.warn("Found {} with [tool.isort] section, but toml package is not installed. "
-                                  "To configure isort with {}, install with 'isort[pyproject]'.".format(file_path,
-                                                                                                        file_path))
-        else:
-            if file_path.endswith('.editorconfig'):
-                line = '\n'
-                last_position = config_file.tell()
-                while line:
-                    line = config_file.readline()
-                    if '[' in line:
-                        config_file.seek(last_position)
-                        break
-                    last_position = config_file.tell()
-
-            if sys.version_info >= (3, 2):
-                config = configparser.ConfigParser(strict=False)
-                config.read_file(config_file)
-            else:
-                config = configparser.SafeConfigParser()
-                config.readfp(config_file)
-
-            for section in sections:
-                if config.has_section(section):
-                    settings.update(config.items(section))
-
-    return settings
-
-
-def should_skip(filename, config, path=''):
-    """Returns True if the file and/or folder should be skipped based on the passed in settings."""
-    os_path = os.path.join(path, filename)
-
-    normalized_path = os_path.replace('\\', '/')
-    if normalized_path[1:2] == ':':
-        normalized_path = normalized_path[2:]
-
-    if path and config['safety_excludes']:
-        check_exclude = '/' + filename.replace('\\', '/') + '/'
-        if path and os.path.basename(path) in ('lib', ):
-            check_exclude = '/' + os.path.basename(path) + check_exclude
-        if safety_exclude_re.search(check_exclude):
-            return True
-
-    for skip_path in config['skip']:
-        if posixpath.abspath(normalized_path) == posixpath.abspath(skip_path.replace('\\', '/')):
-            return True
-
-    position = os.path.split(filename)
-    while position[1]:
-        if position[1] in config['skip']:
-            return True
-        position = os.path.split(position[0])
-
-    for glob in config['skip_glob']:
-        if fnmatch.fnmatch(filename, glob) or fnmatch.fnmatch('/' + filename, glob):
-            return True
-
-    if not (os.path.isfile(os_path) or os.path.isdir(os_path) or os.path.islink(os_path)):
-        return True
-
-    return False
diff --git a/venv/Lib/site-packages/isort/utils.py b/venv/Lib/site-packages/isort/utils.py
deleted file mode 100644
index ce4e588..0000000
--- a/venv/Lib/site-packages/isort/utils.py
+++ /dev/null
@@ -1,53 +0,0 @@
-import os
-import sys
-from contextlib import contextmanager
-
-
-def exists_case_sensitive(path):
-    """
-    Returns if the given path exists and also matches the case on Windows.
-
-    When finding files that can be imported, it is important for the cases to match because while
-    file os.path.exists("module.py") and os.path.exists("MODULE.py") both return True on Windows, Python
-    can only import using the case of the real file.
-    """
-    result = os.path.exists(path)
-    if (sys.platform.startswith('win') or sys.platform == 'darwin') and result:
-        directory, basename = os.path.split(path)
-        result = basename in os.listdir(directory)
-    return result
-
-
-@contextmanager
-def chdir(path):
-    """Context manager for changing dir and restoring previous workdir after exit.
-    """
-    curdir = os.getcwd()
-    os.chdir(path)
-    try:
-        yield
-    finally:
-        os.chdir(curdir)
-
-
-def union(a, b):
-    """ Return a list of items that are in `a` or `b`
-    """
-    u = []
-    for item in a:
-        if item not in u:
-            u.append(item)
-    for item in b:
-        if item not in u:
-            u.append(item)
-    return u
-
-
-def difference(a, b):
-    """ Return a list of items from `a` that are not in `b`.
-    """
-    d = []
-    for item in a:
-        if item not in b:
-            d.append(item)
-    return d
diff --git a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/AUTHORS.rst b/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/AUTHORS.rst
deleted file mode 100644
index dbc0324..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/AUTHORS.rst
+++ /dev/null
@@ -1,10 +0,0 @@
-
-Authors
-=======
-
-* Ionel Cristian Mărieș - https://blog.ionelmc.ro
-* Alvin Chow - https://github.com/alvinchow86
-* Astrum Kuo - https://github.com/xowenx
-* Erik M. Bray - http://iguananaut.net
-* Ran Benita - https://github.com/bluetech
-* "hugovk" - https://github.com/hugovk
diff --git a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/INSTALLER b/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/LICENSE b/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/LICENSE
deleted file mode 100644
index de39b84..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/LICENSE
+++ /dev/null
@@ -1,21 +0,0 @@
-BSD 2-Clause License
-
-Copyright (c) 2014-2019, Ionel Cristian Mărieș
-All rights reserved.
-
-Redistribution and use in source and binary forms, with or without modification, are permitted provided that the
-following conditions are met:
-
-1. Redistributions of source code must retain the above copyright notice, this list of conditions and the following
-disclaimer.
-
-2. Redistributions in binary form must reproduce the above copyright notice, this list of conditions and the following
-disclaimer in the documentation and/or other materials provided with the distribution.
-
-THIS SOFTWARE IS PROVIDED BY THE COPYRIGHT HOLDERS AND CONTRIBUTORS "AS IS" AND ANY EXPRESS OR IMPLIED WARRANTIES,
-INCLUDING, BUT NOT LIMITED TO, THE IMPLIED WARRANTIES OF MERCHANTABILITY AND FITNESS FOR A PARTICULAR PURPOSE ARE
-DISCLAIMED. IN NO EVENT SHALL THE COPYRIGHT HOLDER OR CONTRIBUTORS BE LIABLE FOR ANY DIRECT, INDIRECT, INCIDENTAL,
-SPECIAL, EXEMPLARY, OR CONSEQUENTIAL DAMAGES (INCLUDING, BUT NOT LIMITED TO, PROCUREMENT OF SUBSTITUTE GOODS OR
-SERVICES; LOSS OF USE, DATA, OR PROFITS; OR BUSINESS INTERRUPTION) HOWEVER CAUSED AND ON ANY THEORY OF LIABILITY,
-WHETHER IN CONTRACT, STRICT LIABILITY, OR TORT (INCLUDING NEGLIGENCE OR OTHERWISE) ARISING IN ANY WAY OUT OF THE USE OF
-THIS SOFTWARE, EVEN IF ADVISED OF THE POSSIBILITY OF SUCH DAMAGE.
diff --git a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/METADATA b/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/METADATA
deleted file mode 100644
index 6b4b830..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/METADATA
+++ /dev/null
@@ -1,166 +0,0 @@
-Metadata-Version: 2.1
-Name: lazy-object-proxy
-Version: 1.4.3
-Summary: A fast and thorough lazy object proxy.
-Home-page: https://github.com/ionelmc/python-lazy-object-proxy
-Author: Ionel Cristian Mărieș
-Author-email: contact@ionelmc.ro
-License: BSD-2-Clause
-Project-URL: Documentation, https://python-lazy-object-proxy.readthedocs.io/
-Project-URL: Changelog, https://python-lazy-object-proxy.readthedocs.io/en/latest/changelog.html
-Project-URL: Issue Tracker, https://github.com/ionelmc/python-lazy-object-proxy/issues
-Platform: UNKNOWN
-Classifier: Development Status :: 5 - Production/Stable
-Classifier: Intended Audience :: Developers
-Classifier: License :: OSI Approved :: BSD License
-Classifier: Operating System :: Unix
-Classifier: Operating System :: POSIX
-Classifier: Operating System :: Microsoft :: Windows
-Classifier: Programming Language :: Python
-Classifier: Programming Language :: Python :: 2.7
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.4
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: 3.8
-Classifier: Programming Language :: Python :: Implementation :: CPython
-Classifier: Programming Language :: Python :: Implementation :: PyPy
-Classifier: Topic :: Utilities
-Requires-Python: >=2.7, !=3.0.*, !=3.1.*, !=3.2.*, !=3.3.*
-
-========
-Overview
-========
-
-
-
-A fast and thorough lazy object proxy.
-
-* Free software: BSD 2-Clause License
-
-Note that this is based on `wrapt`_'s ObjectProxy with one big change: it calls a function the first time the proxy object is
-used, while `wrapt.ObjectProxy` just forwards the method calls to the target object.
-
-In other words, you use `lazy-object-proxy` when you only have the object way later and you use `wrapt.ObjectProxy` when you
-want to override few methods (by subclassing) and forward everything else to the target object.
-
-Example::
-
-    import lazy_object_proxy
-
-    def expensive_func():
-        from time import sleep
-        print('starting calculation')
-        # just as example for a very slow computation
-        sleep(2)
-        print('finished calculation')
-        # return the result of the calculation
-        return 10
-
-    obj = lazy_object_proxy.Proxy(expensive_func)
-    # function is called only when object is actually used
-    print(obj)  # now expensive_func is called
-
-    print(obj)  # the result without calling the expensive_func
-
-Installation
-============
-
-::
-
-    pip install lazy-object-proxy
-
-Documentation
-=============
-
-https://python-lazy-object-proxy.readthedocs.io/
-
-Development
-===========
-
-To run the all tests run::
-
-    tox
-
-Acknowledgements
-================
-
-This project is based on some code from `wrapt`_ as you can see in the git history.
-
-.. _wrapt: https://github.com/GrahamDumpleton/wrapt
-
-
-Changelog
-=========
-
-1.4.3 (2019-10-26)
-------------------
-
-* Added binary wheels for Python 3.8.
-* Fixed license metadata.
-
-1.4.2 (2019-08-22)
-------------------
-
-* Included a ``pyproject.toml`` to allow users install the sdist with old python/setuptools, as the
-  setuptools-scm dep will be fetched by pip instead of setuptools.
-  Fixes `#30 <https://github.com/ionelmc/python-lazy-object-proxy/issues/30>`_.
-
-1.4.1 (2019-05-10)
-------------------
-
-* Fixed wheels being built with ``-coverage`` cflags. No more issues about bogus ``cext.gcda`` files.
-* Removed useless C file from wheels.
-* Changed ``setup.py`` to use setuptools-scm.
-
-1.4.0 (2019-05-05)
-------------------
-
-* Fixed ``__mod__`` for the slots backend. Contributed by Ran Benita in
-  `#28 <https://github.com/ionelmc/python-lazy-object-proxy/pull/28>`_.
-* Dropped support for Python 2.6 and 3.3. Contributed by "hugovk" in
-  `#24 <https://github.com/ionelmc/python-lazy-object-proxy/pull/24>`_.
-
-1.3.1 (2017-05-05)
-------------------
-
-* Fix broken release (``sdist`` had a broken ``MANIFEST.in``).
-
-1.3.0 (2017-05-02)
-------------------
-
-* Speed up arithmetic operations involving ``cext.Proxy`` subclasses.
-
-1.2.2 (2016-04-14)
-------------------
-
-* Added `manylinux <https://www.python.org/dev/peps/pep-0513/>`_ wheels.
-* Minor cleanup in readme.
-
-1.2.1 (2015-08-18)
-------------------
-
-* Fix a memory leak (the wrapped object would get bogus references). Contributed by Astrum Kuo in
-  `#10 <https://github.com/ionelmc/python-lazy-object-proxy/pull/10>`_.
-
-1.2.0 (2015-07-06)
-------------------
-
-* Don't instantiate the object when __repr__ is called. This aids with debugging (allows one to see exactly in
-  what state the proxy is).
-
-1.1.0 (2015-07-05)
-------------------
-
-* Added support for pickling. The pickled value is going to be the wrapped object *without* any Proxy container.
-* Fixed a memory management issue in the C extension (reference cycles weren't garbage collected due to improper
-  handling in the C extension). Contributed by Alvin Chow in
-  `#8 <https://github.com/ionelmc/python-lazy-object-proxy/pull/8>`_.
-
-1.0.2 (2015-04-11)
------------------------------------------
-
-* First release on PyPI.
-
-
diff --git a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/RECORD b/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/RECORD
deleted file mode 100644
index e07e94d..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/RECORD
+++ /dev/null
@@ -1,20 +0,0 @@
-lazy_object_proxy-1.4.3.dist-info/AUTHORS.rst,sha256=8CeCjODba0S8UczLyZBPhpO_J6NMZ9Hz_fE1A1uNe9Y,278
-lazy_object_proxy-1.4.3.dist-info/INSTALLER,sha256=zuuue4knoyJ-UwPPXg8fezS7VCrXJQrAP7zeNuwvFQg,4
-lazy_object_proxy-1.4.3.dist-info/LICENSE,sha256=W-1KNkH2bsSNuN7SNqKV8z2H0CkxXzYXZVhUzw1wxUA,1329
-lazy_object_proxy-1.4.3.dist-info/METADATA,sha256=Y2X63wcFbQT4yI3zKpRFwfpA_TCpB6U79MPmRGCMJT0,5088
-lazy_object_proxy-1.4.3.dist-info/RECORD,,
-lazy_object_proxy-1.4.3.dist-info/WHEEL,sha256=uaZe_9gV-4T_d4AskuIQkCgcY8wMc0UXsVFnf0_mBGs,106
-lazy_object_proxy-1.4.3.dist-info/top_level.txt,sha256=UNH-FQB-j_8bYqPz3gD90kHvaC42TQqY0thHSnbaa0k,18
-lazy_object_proxy/__init__.py,sha256=pMqxzToF24DuzOltm-Q8nZ3jNDXOaSQcJmiNArdUrlU,410
-lazy_object_proxy/__pycache__/__init__.cpython-37.pyc,,
-lazy_object_proxy/__pycache__/_version.cpython-37.pyc,,
-lazy_object_proxy/__pycache__/compat.cpython-37.pyc,,
-lazy_object_proxy/__pycache__/simple.cpython-37.pyc,,
-lazy_object_proxy/__pycache__/slots.cpython-37.pyc,,
-lazy_object_proxy/__pycache__/utils.cpython-37.pyc,,
-lazy_object_proxy/_version.py,sha256=KsdHOInxnNuaG_C69nBloPsRbSiniucSfNG8eBgw8yc,120
-lazy_object_proxy/cext.cp37-win_amd64.pyd,sha256=W0Ps706HlNLprmldUashETxgGaQoq6_A5J4w0PPuoJw,31744
-lazy_object_proxy/compat.py,sha256=DY3HbKwbrbeKY6tkXRNRLJ1go6HJb8HUwWqyw3T5g_g,196
-lazy_object_proxy/simple.py,sha256=guacy8_QbJeBs7vXpPPVoDVkDNXOZ86xyS1dtAeKvOs,8216
-lazy_object_proxy/slots.py,sha256=9DilWUINScpZN26NwmRtscTtaqaEwtCfIoriLq5Nz24,11359
-lazy_object_proxy/utils.py,sha256=x4XTrtlp_mDTWO_EOq_ILIOv2Qol8RLMnRm5M8l3OfU,291
diff --git a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/WHEEL b/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/WHEEL
deleted file mode 100644
index c4dd0f9..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/WHEEL
+++ /dev/null
@@ -1,5 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.33.6)
-Root-Is-Purelib: false
-Tag: cp37-cp37m-win_amd64
-
diff --git a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/top_level.txt b/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/top_level.txt
deleted file mode 100644
index bdf032e..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy-1.4.3.dist-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-lazy_object_proxy
diff --git a/venv/Lib/site-packages/lazy_object_proxy/__init__.py b/venv/Lib/site-packages/lazy_object_proxy/__init__.py
deleted file mode 100644
index e9a9a76..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/__init__.py
+++ /dev/null
@@ -1,23 +0,0 @@
-try:
-    import copy_reg as copyreg
-except ImportError:
-    import copyreg
-
-from .utils import identity
-
-copyreg.constructor(identity)
-
-try:
-    from .cext import Proxy
-    from .cext import identity
-except ImportError:
-    from .slots import Proxy
-else:
-    copyreg.constructor(identity)
-
-try:
-    from ._version import version as __version__
-except ImportError:
-    __version__ = '1.4.3'
-
-__all__ = "Proxy",
diff --git a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/lazy_object_proxy/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 0e3505d..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/_version.cpython-37.pyc b/venv/Lib/site-packages/lazy_object_proxy/__pycache__/_version.cpython-37.pyc
deleted file mode 100644
index 5774aa3..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/_version.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/compat.cpython-37.pyc b/venv/Lib/site-packages/lazy_object_proxy/__pycache__/compat.cpython-37.pyc
deleted file mode 100644
index efb5ab0..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/simple.cpython-37.pyc b/venv/Lib/site-packages/lazy_object_proxy/__pycache__/simple.cpython-37.pyc
deleted file mode 100644
index 261981a..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/simple.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/slots.cpython-37.pyc b/venv/Lib/site-packages/lazy_object_proxy/__pycache__/slots.cpython-37.pyc
deleted file mode 100644
index 9b76e90..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/slots.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/lazy_object_proxy/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index 6958b01..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/lazy_object_proxy/_version.py b/venv/Lib/site-packages/lazy_object_proxy/_version.py
deleted file mode 100644
index 3136771..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/_version.py
+++ /dev/null
@@ -1,4 +0,0 @@
-# coding: utf-8
-# file generated by setuptools_scm
-# don't change, don't track in version control
-version = '1.4.3'
diff --git a/venv/Lib/site-packages/lazy_object_proxy/cext.cp37-win_amd64.pyd b/venv/Lib/site-packages/lazy_object_proxy/cext.cp37-win_amd64.pyd
deleted file mode 100644
index 516e3f8..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/cext.cp37-win_amd64.pyd
+++ /dev/null
diff --git a/venv/Lib/site-packages/lazy_object_proxy/compat.py b/venv/Lib/site-packages/lazy_object_proxy/compat.py
deleted file mode 100644
index dc6edfa..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/compat.py
+++ /dev/null
@@ -1,9 +0,0 @@
-import sys
-
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-
-
-def with_metaclass(meta, *bases):
-    """Create a base class with a metaclass."""
-    return meta("NewBase", bases, {})
diff --git a/venv/Lib/site-packages/lazy_object_proxy/simple.py b/venv/Lib/site-packages/lazy_object_proxy/simple.py
deleted file mode 100644
index 24b1339..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/simple.py
+++ /dev/null
@@ -1,246 +0,0 @@
-import operator
-
-from .compat import PY2
-from .compat import PY3
-from .compat import with_metaclass
-from .utils import cached_property
-from .utils import identity
-
-
-def make_proxy_method(code):
-    def proxy_wrapper(self, *args):
-        return code(self.__wrapped__, *args)
-
-    return proxy_wrapper
-
-
-class _ProxyMethods(object):
-    # We use properties to override the values of __module__ and
-    # __doc__. If we add these in ObjectProxy, the derived class
-    # __dict__ will still be setup to have string variants of these
-    # attributes and the rules of descriptors means that they appear to
-    # take precedence over the properties in the base class. To avoid
-    # that, we copy the properties into the derived class type itself
-    # via a meta class. In that way the properties will always take
-    # precedence.
-
-    @property
-    def __module__(self):
-        return self.__wrapped__.__module__
-
-    @__module__.setter
-    def __module__(self, value):
-        self.__wrapped__.__module__ = value
-
-    @property
-    def __doc__(self):
-        return self.__wrapped__.__doc__
-
-    @__doc__.setter
-    def __doc__(self, value):
-        self.__wrapped__.__doc__ = value
-
-    # Need to also propagate the special __weakref__ attribute for case
-    # where decorating classes which will define this. If do not define
-    # it and use a function like inspect.getmembers() on a decorator
-    # class it will fail. This can't be in the derived classes.
-
-    @property
-    def __weakref__(self):
-        return self.__wrapped__.__weakref__
-
-
-class _ProxyMetaType(type):
-    def __new__(cls, name, bases, dictionary):
-        # Copy our special properties into the class so that they
-        # always take precedence over attributes of the same name added
-        # during construction of a derived class. This is to save
-        # duplicating the implementation for them in all derived classes.
-
-        dictionary.update(vars(_ProxyMethods))
-        dictionary.pop('__dict__')
-
-        return type.__new__(cls, name, bases, dictionary)
-
-
-class Proxy(with_metaclass(_ProxyMetaType)):
-    __factory__ = None
-
-    def __init__(self, factory):
-        self.__dict__['__factory__'] = factory
-
-    @cached_property
-    def __wrapped__(self):
-        self = self.__dict__
-        if '__factory__' in self:
-            factory = self['__factory__']
-            return factory()
-        else:
-            raise ValueError("Proxy hasn't been initiated: __factory__ is missing.")
-
-    __name__ = property(make_proxy_method(operator.attrgetter('__name__')))
-    __class__ = property(make_proxy_method(operator.attrgetter('__class__')))
-    __annotations__ = property(make_proxy_method(operator.attrgetter('__anotations__')))
-    __dir__ = make_proxy_method(dir)
-    __str__ = make_proxy_method(str)
-
-    if PY3:
-        __bytes__ = make_proxy_method(bytes)
-
-    def __repr__(self, __getattr__=object.__getattribute__):
-        if '__wrapped__' in self.__dict__:
-            return '<{} at 0x{:x} wrapping {!r} at 0x{:x} with factory {!r}>'.format(
-                type(self).__name__, id(self),
-                self.__wrapped__, id(self.__wrapped__),
-                self.__factory__
-            )
-        else:
-            return '<{} at 0x{:x} with factory {!r}>'.format(
-                type(self).__name__, id(self),
-                self.__factory__
-            )
-
-    __reversed__ = make_proxy_method(reversed)
-
-    if PY3:
-        __round__ = make_proxy_method(round)
-
-    __lt__ = make_proxy_method(operator.lt)
-    __le__ = make_proxy_method(operator.le)
-    __eq__ = make_proxy_method(operator.eq)
-    __ne__ = make_proxy_method(operator.ne)
-    __gt__ = make_proxy_method(operator.gt)
-    __ge__ = make_proxy_method(operator.ge)
-    __hash__ = make_proxy_method(hash)
-    __nonzero__ = make_proxy_method(bool)
-    __bool__ = make_proxy_method(bool)
-
-    def __setattr__(self, name, value):
-        if hasattr(type(self), name):
-            self.__dict__[name] = value
-        else:
-            setattr(self.__wrapped__, name, value)
-
-    def __getattr__(self, name):
-        if name in ('__wrapped__', '__factory__'):
-            raise AttributeError(name)
-        else:
-            return getattr(self.__wrapped__, name)
-
-    def __delattr__(self, name):
-        if hasattr(type(self), name):
-            del self.__dict__[name]
-        else:
-            delattr(self.__wrapped__, name)
-
-    __add__ = make_proxy_method(operator.add)
-    __sub__ = make_proxy_method(operator.sub)
-    __mul__ = make_proxy_method(operator.mul)
-    __div__ = make_proxy_method(operator.div if PY2 else operator.truediv)
-    __truediv__ = make_proxy_method(operator.truediv)
-    __floordiv__ = make_proxy_method(operator.floordiv)
-    __mod__ = make_proxy_method(operator.mod)
-    __divmod__ = make_proxy_method(divmod)
-    __pow__ = make_proxy_method(pow)
-    __lshift__ = make_proxy_method(operator.lshift)
-    __rshift__ = make_proxy_method(operator.rshift)
-    __and__ = make_proxy_method(operator.and_)
-    __xor__ = make_proxy_method(operator.xor)
-    __or__ = make_proxy_method(operator.or_)
-
-    def __radd__(self, other):
-        return other + self.__wrapped__
-
-    def __rsub__(self, other):
-        return other - self.__wrapped__
-
-    def __rmul__(self, other):
-        return other * self.__wrapped__
-
-    def __rdiv__(self, other):
-        return operator.div(other, self.__wrapped__)
-
-    def __rtruediv__(self, other):
-        return operator.truediv(other, self.__wrapped__)
-
-    def __rfloordiv__(self, other):
-        return other // self.__wrapped__
-
-    def __rmod__(self, other):
-        return other % self.__wrapped__
-
-    def __rdivmod__(self, other):
-        return divmod(other, self.__wrapped__)
-
-    def __rpow__(self, other, *args):
-        return pow(other, self.__wrapped__, *args)
-
-    def __rlshift__(self, other):
-        return other << self.__wrapped__
-
-    def __rrshift__(self, other):
-        return other >> self.__wrapped__
-
-    def __rand__(self, other):
-        return other & self.__wrapped__
-
-    def __rxor__(self, other):
-        return other ^ self.__wrapped__
-
-    def __ror__(self, other):
-        return other | self.__wrapped__
-
-    __iadd__ = make_proxy_method(operator.iadd)
-    __isub__ = make_proxy_method(operator.isub)
-    __imul__ = make_proxy_method(operator.imul)
-    __idiv__ = make_proxy_method(operator.idiv if PY2 else operator.itruediv)
-    __itruediv__ = make_proxy_method(operator.itruediv)
-    __ifloordiv__ = make_proxy_method(operator.ifloordiv)
-    __imod__ = make_proxy_method(operator.imod)
-    __ipow__ = make_proxy_method(operator.ipow)
-    __ilshift__ = make_proxy_method(operator.ilshift)
-    __irshift__ = make_proxy_method(operator.irshift)
-    __iand__ = make_proxy_method(operator.iand)
-    __ixor__ = make_proxy_method(operator.ixor)
-    __ior__ = make_proxy_method(operator.ior)
-    __neg__ = make_proxy_method(operator.neg)
-    __pos__ = make_proxy_method(operator.pos)
-    __abs__ = make_proxy_method(operator.abs)
-    __invert__ = make_proxy_method(operator.invert)
-
-    __int__ = make_proxy_method(int)
-
-    if PY2:
-        __long__ = make_proxy_method(long)  # noqa
-
-    __float__ = make_proxy_method(float)
-    __oct__ = make_proxy_method(oct)
-    __hex__ = make_proxy_method(hex)
-    __index__ = make_proxy_method(operator.index)
-    __len__ = make_proxy_method(len)
-    __contains__ = make_proxy_method(operator.contains)
-    __getitem__ = make_proxy_method(operator.getitem)
-    __setitem__ = make_proxy_method(operator.setitem)
-    __delitem__ = make_proxy_method(operator.delitem)
-
-    if PY2:
-        __getslice__ = make_proxy_method(operator.getslice)
-        __setslice__ = make_proxy_method(operator.setslice)
-        __delslice__ = make_proxy_method(operator.delslice)
-
-    def __enter__(self):
-        return self.__wrapped__.__enter__()
-
-    def __exit__(self, *args, **kwargs):
-        return self.__wrapped__.__exit__(*args, **kwargs)
-
-    __iter__ = make_proxy_method(iter)
-
-    def __call__(self, *args, **kwargs):
-        return self.__wrapped__(*args, **kwargs)
-
-    def __reduce__(self):
-        return identity, (self.__wrapped__,)
-
-    def __reduce_ex__(self, protocol):
-        return identity, (self.__wrapped__,)
diff --git a/venv/Lib/site-packages/lazy_object_proxy/slots.py b/venv/Lib/site-packages/lazy_object_proxy/slots.py
deleted file mode 100644
index efb08db..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/slots.py
+++ /dev/null
@@ -1,414 +0,0 @@
-import operator
-
-from .compat import PY2
-from .compat import PY3
-from .compat import with_metaclass
-from .utils import identity
-
-
-class _ProxyMethods(object):
-    # We use properties to override the values of __module__ and
-    # __doc__. If we add these in ObjectProxy, the derived class
-    # __dict__ will still be setup to have string variants of these
-    # attributes and the rules of descriptors means that they appear to
-    # take precedence over the properties in the base class. To avoid
-    # that, we copy the properties into the derived class type itself
-    # via a meta class. In that way the properties will always take
-    # precedence.
-
-    @property
-    def __module__(self):
-        return self.__wrapped__.__module__
-
-    @__module__.setter
-    def __module__(self, value):
-        self.__wrapped__.__module__ = value
-
-    @property
-    def __doc__(self):
-        return self.__wrapped__.__doc__
-
-    @__doc__.setter
-    def __doc__(self, value):
-        self.__wrapped__.__doc__ = value
-
-    # We similar use a property for __dict__. We need __dict__ to be
-    # explicit to ensure that vars() works as expected.
-
-    @property
-    def __dict__(self):
-        return self.__wrapped__.__dict__
-
-    # Need to also propagate the special __weakref__ attribute for case
-    # where decorating classes which will define this. If do not define
-    # it and use a function like inspect.getmembers() on a decorator
-    # class it will fail. This can't be in the derived classes.
-
-    @property
-    def __weakref__(self):
-        return self.__wrapped__.__weakref__
-
-
-class _ProxyMetaType(type):
-    def __new__(cls, name, bases, dictionary):
-        # Copy our special properties into the class so that they
-        # always take precedence over attributes of the same name added
-        # during construction of a derived class. This is to save
-        # duplicating the implementation for them in all derived classes.
-
-        dictionary.update(vars(_ProxyMethods))
-
-        return type.__new__(cls, name, bases, dictionary)
-
-
-class Proxy(with_metaclass(_ProxyMetaType)):
-    """
-    A proxy implementation in pure Python, using slots. You can subclass this to add
-    local methods or attributes, or enable __dict__.
-
-    The most important internals:
-
-    * ``__factory__`` is the callback that "materializes" the object we proxy to.
-    * ``__target__`` will contain the object we proxy to, once it's "materialized".
-    * ``__wrapped__`` is a property that does either:
-
-      * return ``__target__`` if it's set.
-      * calls ``__factory__``, saves result to ``__target__`` and returns said result.
-    """
-
-    __slots__ = '__target__', '__factory__'
-
-    def __init__(self, factory):
-        object.__setattr__(self, '__factory__', factory)
-
-    @property
-    def __wrapped__(self, __getattr__=object.__getattribute__, __setattr__=object.__setattr__,
-                    __delattr__=object.__delattr__):
-        try:
-            return __getattr__(self, '__target__')
-        except AttributeError:
-            try:
-                factory = __getattr__(self, '__factory__')
-            except AttributeError:
-                raise ValueError("Proxy hasn't been initiated: __factory__ is missing.")
-            target = factory()
-            __setattr__(self, '__target__', target)
-            return target
-
-    @__wrapped__.deleter
-    def __wrapped__(self, __delattr__=object.__delattr__):
-        __delattr__(self, '__target__')
-
-    @__wrapped__.setter
-    def __wrapped__(self, target, __setattr__=object.__setattr__):
-        __setattr__(self, '__target__', target)
-
-    @property
-    def __name__(self):
-        return self.__wrapped__.__name__
-
-    @__name__.setter
-    def __name__(self, value):
-        self.__wrapped__.__name__ = value
-
-    @property
-    def __class__(self):
-        return self.__wrapped__.__class__
-
-    @__class__.setter  # noqa
-    def __class__(self, value):
-        self.__wrapped__.__class__ = value
-
-    @property
-    def __annotations__(self):
-        return self.__wrapped__.__anotations__
-
-    @__annotations__.setter
-    def __annotations__(self, value):
-        self.__wrapped__.__annotations__ = value
-
-    def __dir__(self):
-        return dir(self.__wrapped__)
-
-    def __str__(self):
-        return str(self.__wrapped__)
-
-    if PY3:
-        def __bytes__(self):
-            return bytes(self.__wrapped__)
-
-    def __repr__(self, __getattr__=object.__getattribute__):
-        try:
-            target = __getattr__(self, '__target__')
-        except AttributeError:
-            return '<{} at 0x{:x} with factory {!r}>'.format(
-                type(self).__name__, id(self),
-                self.__factory__
-            )
-        else:
-            return '<{} at 0x{:x} wrapping {!r} at 0x{:x} with factory {!r}>'.format(
-                type(self).__name__, id(self),
-                target, id(target),
-                self.__factory__
-            )
-
-    def __reversed__(self):
-        return reversed(self.__wrapped__)
-
-    if PY3:
-        def __round__(self):
-            return round(self.__wrapped__)
-
-    def __lt__(self, other):
-        return self.__wrapped__ < other
-
-    def __le__(self, other):
-        return self.__wrapped__ <= other
-
-    def __eq__(self, other):
-        return self.__wrapped__ == other
-
-    def __ne__(self, other):
-        return self.__wrapped__ != other
-
-    def __gt__(self, other):
-        return self.__wrapped__ > other
-
-    def __ge__(self, other):
-        return self.__wrapped__ >= other
-
-    def __hash__(self):
-        return hash(self.__wrapped__)
-
-    def __nonzero__(self):
-        return bool(self.__wrapped__)
-
-    def __bool__(self):
-        return bool(self.__wrapped__)
-
-    def __setattr__(self, name, value, __setattr__=object.__setattr__):
-        if hasattr(type(self), name):
-            __setattr__(self, name, value)
-        else:
-            setattr(self.__wrapped__, name, value)
-
-    def __getattr__(self, name):
-        if name in ('__wrapped__', '__factory__'):
-            raise AttributeError(name)
-        else:
-            return getattr(self.__wrapped__, name)
-
-    def __delattr__(self, name, __delattr__=object.__delattr__):
-        if hasattr(type(self), name):
-            __delattr__(self, name)
-        else:
-            delattr(self.__wrapped__, name)
-
-    def __add__(self, other):
-        return self.__wrapped__ + other
-
-    def __sub__(self, other):
-        return self.__wrapped__ - other
-
-    def __mul__(self, other):
-        return self.__wrapped__ * other
-
-    def __div__(self, other):
-        return operator.div(self.__wrapped__, other)
-
-    def __truediv__(self, other):
-        return operator.truediv(self.__wrapped__, other)
-
-    def __floordiv__(self, other):
-        return self.__wrapped__ // other
-
-    def __mod__(self, other):
-        return self.__wrapped__ % other
-
-    def __divmod__(self, other):
-        return divmod(self.__wrapped__, other)
-
-    def __pow__(self, other, *args):
-        return pow(self.__wrapped__, other, *args)
-
-    def __lshift__(self, other):
-        return self.__wrapped__ << other
-
-    def __rshift__(self, other):
-        return self.__wrapped__ >> other
-
-    def __and__(self, other):
-        return self.__wrapped__ & other
-
-    def __xor__(self, other):
-        return self.__wrapped__ ^ other
-
-    def __or__(self, other):
-        return self.__wrapped__ | other
-
-    def __radd__(self, other):
-        return other + self.__wrapped__
-
-    def __rsub__(self, other):
-        return other - self.__wrapped__
-
-    def __rmul__(self, other):
-        return other * self.__wrapped__
-
-    def __rdiv__(self, other):
-        return operator.div(other, self.__wrapped__)
-
-    def __rtruediv__(self, other):
-        return operator.truediv(other, self.__wrapped__)
-
-    def __rfloordiv__(self, other):
-        return other // self.__wrapped__
-
-    def __rmod__(self, other):
-        return other % self.__wrapped__
-
-    def __rdivmod__(self, other):
-        return divmod(other, self.__wrapped__)
-
-    def __rpow__(self, other, *args):
-        return pow(other, self.__wrapped__, *args)
-
-    def __rlshift__(self, other):
-        return other << self.__wrapped__
-
-    def __rrshift__(self, other):
-        return other >> self.__wrapped__
-
-    def __rand__(self, other):
-        return other & self.__wrapped__
-
-    def __rxor__(self, other):
-        return other ^ self.__wrapped__
-
-    def __ror__(self, other):
-        return other | self.__wrapped__
-
-    def __iadd__(self, other):
-        self.__wrapped__ += other
-        return self
-
-    def __isub__(self, other):
-        self.__wrapped__ -= other
-        return self
-
-    def __imul__(self, other):
-        self.__wrapped__ *= other
-        return self
-
-    def __idiv__(self, other):
-        self.__wrapped__ = operator.idiv(self.__wrapped__, other)
-        return self
-
-    def __itruediv__(self, other):
-        self.__wrapped__ = operator.itruediv(self.__wrapped__, other)
-        return self
-
-    def __ifloordiv__(self, other):
-        self.__wrapped__ //= other
-        return self
-
-    def __imod__(self, other):
-        self.__wrapped__ %= other
-        return self
-
-    def __ipow__(self, other):
-        self.__wrapped__ **= other
-        return self
-
-    def __ilshift__(self, other):
-        self.__wrapped__ <<= other
-        return self
-
-    def __irshift__(self, other):
-        self.__wrapped__ >>= other
-        return self
-
-    def __iand__(self, other):
-        self.__wrapped__ &= other
-        return self
-
-    def __ixor__(self, other):
-        self.__wrapped__ ^= other
-        return self
-
-    def __ior__(self, other):
-        self.__wrapped__ |= other
-        return self
-
-    def __neg__(self):
-        return -self.__wrapped__
-
-    def __pos__(self):
-        return +self.__wrapped__
-
-    def __abs__(self):
-        return abs(self.__wrapped__)
-
-    def __invert__(self):
-        return ~self.__wrapped__
-
-    def __int__(self):
-        return int(self.__wrapped__)
-
-    if PY2:
-        def __long__(self):
-            return long(self.__wrapped__)  # noqa
-
-    def __float__(self):
-        return float(self.__wrapped__)
-
-    def __oct__(self):
-        return oct(self.__wrapped__)
-
-    def __hex__(self):
-        return hex(self.__wrapped__)
-
-    def __index__(self):
-        return operator.index(self.__wrapped__)
-
-    def __len__(self):
-        return len(self.__wrapped__)
-
-    def __contains__(self, value):
-        return value in self.__wrapped__
-
-    def __getitem__(self, key):
-        return self.__wrapped__[key]
-
-    def __setitem__(self, key, value):
-        self.__wrapped__[key] = value
-
-    def __delitem__(self, key):
-        del self.__wrapped__[key]
-
-    def __getslice__(self, i, j):
-        return self.__wrapped__[i:j]
-
-    def __setslice__(self, i, j, value):
-        self.__wrapped__[i:j] = value
-
-    def __delslice__(self, i, j):
-        del self.__wrapped__[i:j]
-
-    def __enter__(self):
-        return self.__wrapped__.__enter__()
-
-    def __exit__(self, *args, **kwargs):
-        return self.__wrapped__.__exit__(*args, **kwargs)
-
-    def __iter__(self):
-        return iter(self.__wrapped__)
-
-    def __call__(self, *args, **kwargs):
-        return self.__wrapped__(*args, **kwargs)
-
-    def __reduce__(self):
-        return identity, (self.__wrapped__,)
-
-    def __reduce_ex__(self, protocol):
-        return identity, (self.__wrapped__,)
diff --git a/venv/Lib/site-packages/lazy_object_proxy/utils.py b/venv/Lib/site-packages/lazy_object_proxy/utils.py
deleted file mode 100644
index ceb3050..0000000
--- a/venv/Lib/site-packages/lazy_object_proxy/utils.py
+++ /dev/null
@@ -1,13 +0,0 @@
-def identity(obj):
-    return obj
-
-
-class cached_property(object):
-    def __init__(self, func):
-        self.func = func
-
-    def __get__(self, obj, cls):
-        if obj is None:
-            return self
-        value = obj.__dict__[self.func.__name__] = self.func(obj)
-        return value
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/DESCRIPTION.rst b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/DESCRIPTION.rst
deleted file mode 100644
index de61068..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/DESCRIPTION.rst
+++ /dev/null
@@ -1,152 +0,0 @@
-McCabe complexity checker
-=========================
-
-Ned's script to check McCabe complexity.
-
-This module provides a plugin for ``flake8``, the Python code checker.
-
-
-Installation
-------------
-
-You can install, upgrade, uninstall ``mccabe`` with these commands::
-
-  $ pip install mccabe
-  $ pip install --upgrade mccabe
-  $ pip uninstall mccabe
-
-
-Standalone script
------------------
-
-The complexity checker can be used directly::
-
-  $ python -m mccabe --min 5 mccabe.py
-  ("185:1: 'PathGraphingAstVisitor.visitIf'", 5)
-  ("71:1: 'PathGraph.to_dot'", 5)
-  ("245:1: 'McCabeChecker.run'", 5)
-  ("283:1: 'main'", 7)
-  ("203:1: 'PathGraphingAstVisitor.visitTryExcept'", 5)
-  ("257:1: 'get_code_complexity'", 5)
-
-
-Plugin for Flake8
------------------
-
-When both ``flake8 2.0`` and ``mccabe`` are installed, the plugin is
-available in ``flake8``::
-
-  $ flake8 --version
-  2.0 (pep8: 1.4.2, pyflakes: 0.6.1, mccabe: 0.2)
-
-By default the plugin is disabled.  Use the ``--max-complexity`` switch to
-enable it.  It will emit a warning if the McCabe complexity of a function is
-higher that the value::
-
-    $ flake8 --max-complexity 10 coolproject
-    ...
-    coolproject/mod.py:1204:1: C901 'CoolFactory.prepare' is too complex (14)
-
-This feature is quite useful to detect over-complex code.  According to McCabe,
-anything that goes beyond 10 is too complex.
-
-
-Links
------
-
-* Feedback and ideas: http://mail.python.org/mailman/listinfo/code-quality
-
-* Cyclomatic complexity: http://en.wikipedia.org/wiki/Cyclomatic_complexity.
-
-* Ned Batchelder's script:
-  http://nedbatchelder.com/blog/200803/python_code_complexity_microtool.html
-
-
-Changes
--------
-
-0.6.1 - 2017-01-26
-``````````````````
-
-* Fix signature for ``PathGraphingAstVisitor.default`` to match the signature
-  for ``ASTVisitor``
-
-0.6.0 - 2017-01-23
-``````````````````
-
-* Add support for Python 3.6
-
-* Fix handling for missing statement types
-
-0.5.3 - 2016-12-14
-``````````````````
-
-* Report actual column number of violation instead of the start of the line
-
-0.5.2 - 2016-07-31
-``````````````````
-
-* When opening files ourselves, make sure we always name the file variable
-
-0.5.1 - 2016-07-28
-``````````````````
-
-* Set default maximum complexity to -1 on the class itself
-
-0.5.0 - 2016-05-30
-``````````````````
-
-* PyCon 2016 PDX release
-
-* Add support for Flake8 3.0
-
-0.4.0 - 2016-01-27
-``````````````````
-
-* Stop testing on Python 3.2
-
-* Add support for async/await keywords on Python 3.5 from PEP 0492
-
-0.3.1 - 2015-06-14
-``````````````````
-
-* Include ``test_mccabe.py`` in releases.
-
-* Always coerce the ``max_complexity`` value from Flake8's entry-point to an
-  integer.
-
-0.3 - 2014-12-17
-````````````````
-
-* Computation was wrong: the mccabe complexity starts at 1, not 2.
-
-* The ``max-complexity`` value is now inclusive.  E.g.: if the
-  value is 10 and the reported complexity is 10, then it passes.
-
-* Add tests.
-
-
-0.2.1 - 2013-04-03
-``````````````````
-
-* Do not require ``setuptools`` in setup.py.  It works around an issue
-  with ``pip`` and Python 3.
-
-
-0.2 - 2013-02-22
-````````````````
-
-* Rename project to ``mccabe``.
-
-* Provide ``flake8.extension`` setuptools entry point.
-
-* Read ``max-complexity`` from the configuration file.
-
-* Rename argument ``min_complexity`` to ``threshold``.
-
-
-0.1 - 2013-02-11
-````````````````
-* First release
-
-
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/INSTALLER b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/METADATA b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/METADATA
deleted file mode 100644
index f22645f..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/METADATA
+++ /dev/null
@@ -1,178 +0,0 @@
-Metadata-Version: 2.0
-Name: mccabe
-Version: 0.6.1
-Summary: McCabe checker, plugin for flake8
-Home-page: https://github.com/pycqa/mccabe
-Author: Ian Cordasco
-Author-email: graffatcolmingov@gmail.com
-License: Expat license
-Keywords: flake8 mccabe
-Platform: UNKNOWN
-Classifier: Development Status :: 5 - Production/Stable
-Classifier: Environment :: Console
-Classifier: Intended Audience :: Developers
-Classifier: License :: OSI Approved :: MIT License
-Classifier: Operating System :: OS Independent
-Classifier: Programming Language :: Python
-Classifier: Programming Language :: Python :: 2
-Classifier: Programming Language :: Python :: 2.7
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.3
-Classifier: Programming Language :: Python :: 3.4
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Topic :: Software Development :: Libraries :: Python Modules
-Classifier: Topic :: Software Development :: Quality Assurance
-
-McCabe complexity checker
-=========================
-
-Ned's script to check McCabe complexity.
-
-This module provides a plugin for ``flake8``, the Python code checker.
-
-
-Installation
-------------
-
-You can install, upgrade, uninstall ``mccabe`` with these commands::
-
-  $ pip install mccabe
-  $ pip install --upgrade mccabe
-  $ pip uninstall mccabe
-
-
-Standalone script
------------------
-
-The complexity checker can be used directly::
-
-  $ python -m mccabe --min 5 mccabe.py
-  ("185:1: 'PathGraphingAstVisitor.visitIf'", 5)
-  ("71:1: 'PathGraph.to_dot'", 5)
-  ("245:1: 'McCabeChecker.run'", 5)
-  ("283:1: 'main'", 7)
-  ("203:1: 'PathGraphingAstVisitor.visitTryExcept'", 5)
-  ("257:1: 'get_code_complexity'", 5)
-
-
-Plugin for Flake8
------------------
-
-When both ``flake8 2.0`` and ``mccabe`` are installed, the plugin is
-available in ``flake8``::
-
-  $ flake8 --version
-  2.0 (pep8: 1.4.2, pyflakes: 0.6.1, mccabe: 0.2)
-
-By default the plugin is disabled.  Use the ``--max-complexity`` switch to
-enable it.  It will emit a warning if the McCabe complexity of a function is
-higher that the value::
-
-    $ flake8 --max-complexity 10 coolproject
-    ...
-    coolproject/mod.py:1204:1: C901 'CoolFactory.prepare' is too complex (14)
-
-This feature is quite useful to detect over-complex code.  According to McCabe,
-anything that goes beyond 10 is too complex.
-
-
-Links
------
-
-* Feedback and ideas: http://mail.python.org/mailman/listinfo/code-quality
-
-* Cyclomatic complexity: http://en.wikipedia.org/wiki/Cyclomatic_complexity.
-
-* Ned Batchelder's script:
-  http://nedbatchelder.com/blog/200803/python_code_complexity_microtool.html
-
-
-Changes
--------
-
-0.6.1 - 2017-01-26
-``````````````````
-
-* Fix signature for ``PathGraphingAstVisitor.default`` to match the signature
-  for ``ASTVisitor``
-
-0.6.0 - 2017-01-23
-``````````````````
-
-* Add support for Python 3.6
-
-* Fix handling for missing statement types
-
-0.5.3 - 2016-12-14
-``````````````````
-
-* Report actual column number of violation instead of the start of the line
-
-0.5.2 - 2016-07-31
-``````````````````
-
-* When opening files ourselves, make sure we always name the file variable
-
-0.5.1 - 2016-07-28
-``````````````````
-
-* Set default maximum complexity to -1 on the class itself
-
-0.5.0 - 2016-05-30
-``````````````````
-
-* PyCon 2016 PDX release
-
-* Add support for Flake8 3.0
-
-0.4.0 - 2016-01-27
-``````````````````
-
-* Stop testing on Python 3.2
-
-* Add support for async/await keywords on Python 3.5 from PEP 0492
-
-0.3.1 - 2015-06-14
-``````````````````
-
-* Include ``test_mccabe.py`` in releases.
-
-* Always coerce the ``max_complexity`` value from Flake8's entry-point to an
-  integer.
-
-0.3 - 2014-12-17
-````````````````
-
-* Computation was wrong: the mccabe complexity starts at 1, not 2.
-
-* The ``max-complexity`` value is now inclusive.  E.g.: if the
-  value is 10 and the reported complexity is 10, then it passes.
-
-* Add tests.
-
-
-0.2.1 - 2013-04-03
-``````````````````
-
-* Do not require ``setuptools`` in setup.py.  It works around an issue
-  with ``pip`` and Python 3.
-
-
-0.2 - 2013-02-22
-````````````````
-
-* Rename project to ``mccabe``.
-
-* Provide ``flake8.extension`` setuptools entry point.
-
-* Read ``max-complexity`` from the configuration file.
-
-* Rename argument ``min_complexity`` to ``threshold``.
-
-
-0.1 - 2013-02-11
-````````````````
-* First release
-
-
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/RECORD b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/RECORD
deleted file mode 100644
index 91abd1a..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/RECORD
+++ /dev/null
@@ -1,10 +0,0 @@
-__pycache__/mccabe.cpython-37.pyc,,
-mccabe-0.6.1.dist-info/DESCRIPTION.rst,sha256=lGHJ-Y3IviuP3DRqLL_TXPUr3wJ2GZ8XJkAV6ve3O58,3302
-mccabe-0.6.1.dist-info/INSTALLER,sha256=zuuue4knoyJ-UwPPXg8fezS7VCrXJQrAP7zeNuwvFQg,4
-mccabe-0.6.1.dist-info/METADATA,sha256=jawnTfTVrlzBSmeI-cTXSRIwIlijODtZdj-padBqIv0,4324
-mccabe-0.6.1.dist-info/RECORD,,
-mccabe-0.6.1.dist-info/WHEEL,sha256=o2k-Qa-RMNIJmUdIc7KU6VWR_ErNRbWNlxDIpl7lm34,110
-mccabe-0.6.1.dist-info/entry_points.txt,sha256=N2NH182GXTUyTm8r8XMgadb9C-CRa5dUr1k8OC91uGE,47
-mccabe-0.6.1.dist-info/metadata.json,sha256=e508OR4t6_G7h7eO2C6NHlHQqVpPZZH1_DlAPrVECYM,1218
-mccabe-0.6.1.dist-info/top_level.txt,sha256=21cXuqZE-lpcfAqqANvX9EjI1ED1p8zcViv064u3RKA,7
-mccabe.py,sha256=XPMywdQshG_5nSjckb-OzNqnCQuXQvy3FTClspKwGQA,10693
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/WHEEL b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/WHEEL
deleted file mode 100644
index 8b6dd1b..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/WHEEL
+++ /dev/null
@@ -1,6 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.29.0)
-Root-Is-Purelib: true
-Tag: py2-none-any
-Tag: py3-none-any
-
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/entry_points.txt b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/entry_points.txt
deleted file mode 100644
index cc6645b..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/entry_points.txt
+++ /dev/null
@@ -1,3 +0,0 @@
-[flake8.extension]
-C90 = mccabe:McCabeChecker
-
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/metadata.json b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/metadata.json
deleted file mode 100644
index ae04d8f..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/metadata.json
+++ /dev/null
@@ -1 +0,0 @@
-{"classifiers": ["Development Status :: 5 - Production/Stable", "Environment :: Console", "Intended Audience :: Developers", "License :: OSI Approved :: MIT License", "Operating System :: OS Independent", "Programming Language :: Python", "Programming Language :: Python :: 2", "Programming Language :: Python :: 2.7", "Programming Language :: Python :: 3", "Programming Language :: Python :: 3.3", "Programming Language :: Python :: 3.4", "Programming Language :: Python :: 3.5", "Programming Language :: Python :: 3.6", "Topic :: Software Development :: Libraries :: Python Modules", "Topic :: Software Development :: Quality Assurance"], "extensions": {"python.details": {"contacts": [{"email": "graffatcolmingov@gmail.com", "name": "Ian Cordasco", "role": "author"}], "document_names": {"description": "DESCRIPTION.rst"}, "project_urls": {"Home": "https://github.com/pycqa/mccabe"}}, "python.exports": {"flake8.extension": {"C90": "mccabe:McCabeChecker"}}}, "generator": "bdist_wheel (0.29.0)", "keywords": ["flake8", "mccabe"], "license": "Expat license", "metadata_version": "2.0", "name": "mccabe", "summary": "McCabe checker, plugin for flake8", "test_requires": [{"requires": ["pytest"]}], "version": "0.6.1"}
\ No newline at end of file
diff --git a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/top_level.txt b/venv/Lib/site-packages/mccabe-0.6.1.dist-info/top_level.txt
deleted file mode 100644
index 8831b36..0000000
--- a/venv/Lib/site-packages/mccabe-0.6.1.dist-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-mccabe
diff --git a/venv/Lib/site-packages/mccabe.py b/venv/Lib/site-packages/mccabe.py
deleted file mode 100644
index c0cda75..0000000
--- a/venv/Lib/site-packages/mccabe.py
+++ /dev/null
@@ -1,347 +0,0 @@
-""" Meager code path measurement tool.
-    Ned Batchelder
-    http://nedbatchelder.com/blog/200803/python_code_complexity_microtool.html
-    MIT License.
-"""
-from __future__ import with_statement
-
-import optparse
-import sys
-import tokenize
-
-from collections import defaultdict
-try:
-    import ast
-    from ast import iter_child_nodes
-except ImportError:   # Python 2.5
-    from flake8.util import ast, iter_child_nodes
-
-__version__ = '0.6.1'
-
-
-class ASTVisitor(object):
-    """Performs a depth-first walk of the AST."""
-
-    def __init__(self):
-        self.node = None
-        self._cache = {}
-
-    def default(self, node, *args):
-        for child in iter_child_nodes(node):
-            self.dispatch(child, *args)
-
-    def dispatch(self, node, *args):
-        self.node = node
-        klass = node.__class__
-        meth = self._cache.get(klass)
-        if meth is None:
-            className = klass.__name__
-            meth = getattr(self.visitor, 'visit' + className, self.default)
-            self._cache[klass] = meth
-        return meth(node, *args)
-
-    def preorder(self, tree, visitor, *args):
-        """Do preorder walk of tree using visitor"""
-        self.visitor = visitor
-        visitor.visit = self.dispatch
-        self.dispatch(tree, *args)  # XXX *args make sense?
-
-
-class PathNode(object):
-    def __init__(self, name, look="circle"):
-        self.name = name
-        self.look = look
-
-    def to_dot(self):
-        print('node [shape=%s,label="%s"] %d;' % (
-            self.look, self.name, self.dot_id()))
-
-    def dot_id(self):
-        return id(self)
-
-
-class PathGraph(object):
-    def __init__(self, name, entity, lineno, column=0):
-        self.name = name
-        self.entity = entity
-        self.lineno = lineno
-        self.column = column
-        self.nodes = defaultdict(list)
-
-    def connect(self, n1, n2):
-        self.nodes[n1].append(n2)
-        # Ensure that the destination node is always counted.
-        self.nodes[n2] = []
-
-    def to_dot(self):
-        print('subgraph {')
-        for node in self.nodes:
-            node.to_dot()
-        for node, nexts in self.nodes.items():
-            for next in nexts:
-                print('%s -- %s;' % (node.dot_id(), next.dot_id()))
-        print('}')
-
-    def complexity(self):
-        """ Return the McCabe complexity for the graph.
-            V-E+2
-        """
-        num_edges = sum([len(n) for n in self.nodes.values()])
-        num_nodes = len(self.nodes)
-        return num_edges - num_nodes + 2
-
-
-class PathGraphingAstVisitor(ASTVisitor):
-    """ A visitor for a parsed Abstract Syntax Tree which finds executable
-        statements.
-    """
-
-    def __init__(self):
-        super(PathGraphingAstVisitor, self).__init__()
-        self.classname = ""
-        self.graphs = {}
-        self.reset()
-
-    def reset(self):
-        self.graph = None
-        self.tail = None
-
-    def dispatch_list(self, node_list):
-        for node in node_list:
-            self.dispatch(node)
-
-    def visitFunctionDef(self, node):
-
-        if self.classname:
-            entity = '%s%s' % (self.classname, node.name)
-        else:
-            entity = node.name
-
-        name = '%d:%d: %r' % (node.lineno, node.col_offset, entity)
-
-        if self.graph is not None:
-            # closure
-            pathnode = self.appendPathNode(name)
-            self.tail = pathnode
-            self.dispatch_list(node.body)
-            bottom = PathNode("", look='point')
-            self.graph.connect(self.tail, bottom)
-            self.graph.connect(pathnode, bottom)
-            self.tail = bottom
-        else:
-            self.graph = PathGraph(name, entity, node.lineno, node.col_offset)
-            pathnode = PathNode(name)
-            self.tail = pathnode
-            self.dispatch_list(node.body)
-            self.graphs["%s%s" % (self.classname, node.name)] = self.graph
-            self.reset()
-
-    visitAsyncFunctionDef = visitFunctionDef
-
-    def visitClassDef(self, node):
-        old_classname = self.classname
-        self.classname += node.name + "."
-        self.dispatch_list(node.body)
-        self.classname = old_classname
-
-    def appendPathNode(self, name):
-        if not self.tail:
-            return
-        pathnode = PathNode(name)
-        self.graph.connect(self.tail, pathnode)
-        self.tail = pathnode
-        return pathnode
-
-    def visitSimpleStatement(self, node):
-        if node.lineno is None:
-            lineno = 0
-        else:
-            lineno = node.lineno
-        name = "Stmt %d" % lineno
-        self.appendPathNode(name)
-
-    def default(self, node, *args):
-        if isinstance(node, ast.stmt):
-            self.visitSimpleStatement(node)
-        else:
-            super(PathGraphingAstVisitor, self).default(node, *args)
-
-    def visitLoop(self, node):
-        name = "Loop %d" % node.lineno
-        self._subgraph(node, name)
-
-    visitAsyncFor = visitFor = visitWhile = visitLoop
-
-    def visitIf(self, node):
-        name = "If %d" % node.lineno
-        self._subgraph(node, name)
-
-    def _subgraph(self, node, name, extra_blocks=()):
-        """create the subgraphs representing any `if` and `for` statements"""
-        if self.graph is None:
-            # global loop
-            self.graph = PathGraph(name, name, node.lineno, node.col_offset)
-            pathnode = PathNode(name)
-            self._subgraph_parse(node, pathnode, extra_blocks)
-            self.graphs["%s%s" % (self.classname, name)] = self.graph
-            self.reset()
-        else:
-            pathnode = self.appendPathNode(name)
-            self._subgraph_parse(node, pathnode, extra_blocks)
-
-    def _subgraph_parse(self, node, pathnode, extra_blocks):
-        """parse the body and any `else` block of `if` and `for` statements"""
-        loose_ends = []
-        self.tail = pathnode
-        self.dispatch_list(node.body)
-        loose_ends.append(self.tail)
-        for extra in extra_blocks:
-            self.tail = pathnode
-            self.dispatch_list(extra.body)
-            loose_ends.append(self.tail)
-        if node.orelse:
-            self.tail = pathnode
-            self.dispatch_list(node.orelse)
-            loose_ends.append(self.tail)
-        else:
-            loose_ends.append(pathnode)
-        if pathnode:
-            bottom = PathNode("", look='point')
-            for le in loose_ends:
-                self.graph.connect(le, bottom)
-            self.tail = bottom
-
-    def visitTryExcept(self, node):
-        name = "TryExcept %d" % node.lineno
-        self._subgraph(node, name, extra_blocks=node.handlers)
-
-    visitTry = visitTryExcept
-
-    def visitWith(self, node):
-        name = "With %d" % node.lineno
-        self.appendPathNode(name)
-        self.dispatch_list(node.body)
-
-    visitAsyncWith = visitWith
-
-
-class McCabeChecker(object):
-    """McCabe cyclomatic complexity checker."""
-    name = 'mccabe'
-    version = __version__
-    _code = 'C901'
-    _error_tmpl = "C901 %r is too complex (%d)"
-    max_complexity = -1
-
-    def __init__(self, tree, filename):
-        self.tree = tree
-
-    @classmethod
-    def add_options(cls, parser):
-        flag = '--max-complexity'
-        kwargs = {
-            'default': -1,
-            'action': 'store',
-            'type': 'int',
-            'help': 'McCabe complexity threshold',
-            'parse_from_config': 'True',
-        }
-        config_opts = getattr(parser, 'config_options', None)
-        if isinstance(config_opts, list):
-            # Flake8 2.x
-            kwargs.pop('parse_from_config')
-            parser.add_option(flag, **kwargs)
-            parser.config_options.append('max-complexity')
-        else:
-            parser.add_option(flag, **kwargs)
-
-    @classmethod
-    def parse_options(cls, options):
-        cls.max_complexity = int(options.max_complexity)
-
-    def run(self):
-        if self.max_complexity < 0:
-            return
-        visitor = PathGraphingAstVisitor()
-        visitor.preorder(self.tree, visitor)
-        for graph in visitor.graphs.values():
-            if graph.complexity() > self.max_complexity:
-                text = self._error_tmpl % (graph.entity, graph.complexity())
-                yield graph.lineno, graph.column, text, type(self)
-
-
-def get_code_complexity(code, threshold=7, filename='stdin'):
-    try:
-        tree = compile(code, filename, "exec", ast.PyCF_ONLY_AST)
-    except SyntaxError:
-        e = sys.exc_info()[1]
-        sys.stderr.write("Unable to parse %s: %s\n" % (filename, e))
-        return 0
-
-    complx = []
-    McCabeChecker.max_complexity = threshold
-    for lineno, offset, text, check in McCabeChecker(tree, filename).run():
-        complx.append('%s:%d:1: %s' % (filename, lineno, text))
-
-    if len(complx) == 0:
-        return 0
-    print('\n'.join(complx))
-    return len(complx)
-
-
-def get_module_complexity(module_path, threshold=7):
-    """Returns the complexity of a module"""
-    with open(module_path, "rU") as mod:
-        code = mod.read()
-    return get_code_complexity(code, threshold, filename=module_path)
-
-
-def _read(filename):
-    if (2, 5) < sys.version_info < (3, 0):
-        with open(filename, 'rU') as f:
-            return f.read()
-    elif (3, 0) <= sys.version_info < (4, 0):
-        """Read the source code."""
-        try:
-            with open(filename, 'rb') as f:
-                (encoding, _) = tokenize.detect_encoding(f.readline)
-        except (LookupError, SyntaxError, UnicodeError):
-            # Fall back if file encoding is improperly declared
-            with open(filename, encoding='latin-1') as f:
-                return f.read()
-        with open(filename, 'r', encoding=encoding) as f:
-            return f.read()
-
-
-def main(argv=None):
-    if argv is None:
-        argv = sys.argv[1:]
-    opar = optparse.OptionParser()
-    opar.add_option("-d", "--dot", dest="dot",
-                    help="output a graphviz dot file", action="store_true")
-    opar.add_option("-m", "--min", dest="threshold",
-                    help="minimum complexity for output", type="int",
-                    default=1)
-
-    options, args = opar.parse_args(argv)
-
-    code = _read(args[0])
-    tree = compile(code, args[0], "exec", ast.PyCF_ONLY_AST)
-    visitor = PathGraphingAstVisitor()
-    visitor.preorder(tree, visitor)
-
-    if options.dot:
-        print('graph {')
-        for graph in visitor.graphs.values():
-            if (not options.threshold or
-                    graph.complexity() >= options.threshold):
-                graph.to_dot()
-        print('}')
-    else:
-        for graph in visitor.graphs.values():
-            if graph.complexity() >= options.threshold:
-                print(graph.name, graph.complexity())
-
-
-if __name__ == '__main__':
-    main(sys.argv[1:])
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/PKG-INFO b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/PKG-INFO
deleted file mode 100644
index 0b410a2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/PKG-INFO
+++ /dev/null
@@ -1,73 +0,0 @@
-Metadata-Version: 1.2
-Name: pip
-Version: 19.0.3
-Summary: The PyPA recommended tool for installing Python packages.
-Home-page: https://pip.pypa.io/
-Author: The pip developers
-Author-email: pypa-dev@groups.google.com
-License: MIT
-Description: pip - The Python Package Installer
-        ==================================
-        
-        .. image:: https://img.shields.io/pypi/v/pip.svg
-           :target: https://pypi.org/project/pip/
-        
-        .. image:: https://readthedocs.org/projects/pip/badge/?version=latest
-           :target: https://pip.pypa.io/en/latest
-        
-        pip is the `package installer`_ for Python. You can use pip to install packages from the `Python Package Index`_ and other indexes.
-        
-        Please take a look at our documentation for how to install and use pip:
-        
-        * `Installation`_
-        * `Usage`_
-        * `Release notes`_
-        
-        If you find bugs, need help, or want to talk to the developers please use our mailing lists or chat rooms:
-        
-        * `Issue tracking`_
-        * `Discourse channel`_
-        * `User IRC`_
-        
-        If you want to get involved head over to GitHub to get the source code and feel free to jump on the developer mailing lists and chat rooms:
-        
-        * `GitHub page`_
-        * `Dev mailing list`_
-        * `Dev IRC`_
-        
-        Code of Conduct
-        ---------------
-        
-        Everyone interacting in the pip project's codebases, issue trackers, chat
-        rooms, and mailing lists is expected to follow the `PyPA Code of Conduct`_.
-        
-        .. _package installer: https://packaging.python.org/en/latest/current/
-        .. _Python Package Index: https://pypi.org
-        .. _Installation: https://pip.pypa.io/en/stable/installing.html
-        .. _Usage: https://pip.pypa.io/en/stable/
-        .. _Release notes: https://pip.pypa.io/en/stable/news.html
-        .. _GitHub page: https://github.com/pypa/pip
-        .. _Issue tracking: https://github.com/pypa/pip/issues
-        .. _Discourse channel: https://discuss.python.org/c/packaging
-        .. _Dev mailing list: https://groups.google.com/forum/#!forum/pypa-dev
-        .. _User IRC: https://webchat.freenode.net/?channels=%23pypa
-        .. _Dev IRC: https://webchat.freenode.net/?channels=%23pypa-dev
-        .. _PyPA Code of Conduct: https://www.pypa.io/en/latest/code-of-conduct/
-        
-Keywords: distutils easy_install egg setuptools wheel virtualenv
-Platform: UNKNOWN
-Classifier: Development Status :: 5 - Production/Stable
-Classifier: Intended Audience :: Developers
-Classifier: License :: OSI Approved :: MIT License
-Classifier: Topic :: Software Development :: Build Tools
-Classifier: Programming Language :: Python
-Classifier: Programming Language :: Python :: 2
-Classifier: Programming Language :: Python :: 2.7
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.4
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: Implementation :: CPython
-Classifier: Programming Language :: Python :: Implementation :: PyPy
-Requires-Python: >=2.7,!=3.0.*,!=3.1.*,!=3.2.*,!=3.3.*
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/SOURCES.txt b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/SOURCES.txt
deleted file mode 100644
index eb4810d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/SOURCES.txt
+++ /dev/null
@@ -1,391 +0,0 @@
-AUTHORS.txt
-LICENSE.txt
-MANIFEST.in
-NEWS.rst
-README.rst
-pyproject.toml
-setup.cfg
-setup.py
-docs/pip_sphinxext.py
-docs/html/conf.py
-docs/html/cookbook.rst
-docs/html/index.rst
-docs/html/installing.rst
-docs/html/logic.rst
-docs/html/news.rst
-docs/html/quickstart.rst
-docs/html/usage.rst
-docs/html/user_guide.rst
-docs/html/development/configuration.rst
-docs/html/development/contributing.rst
-docs/html/development/getting-started.rst
-docs/html/development/index.rst
-docs/html/development/release-process.rst
-docs/html/development/vendoring-policy.rst
-docs/html/reference/index.rst
-docs/html/reference/pip.rst
-docs/html/reference/pip_check.rst
-docs/html/reference/pip_config.rst
-docs/html/reference/pip_download.rst
-docs/html/reference/pip_freeze.rst
-docs/html/reference/pip_hash.rst
-docs/html/reference/pip_install.rst
-docs/html/reference/pip_list.rst
-docs/html/reference/pip_search.rst
-docs/html/reference/pip_show.rst
-docs/html/reference/pip_uninstall.rst
-docs/html/reference/pip_wheel.rst
-docs/man/index.rst
-docs/man/commands/check.rst
-docs/man/commands/config.rst
-docs/man/commands/download.rst
-docs/man/commands/freeze.rst
-docs/man/commands/hash.rst
-docs/man/commands/help.rst
-docs/man/commands/install.rst
-docs/man/commands/list.rst
-docs/man/commands/search.rst
-docs/man/commands/show.rst
-docs/man/commands/uninstall.rst
-docs/man/commands/wheel.rst
-src/pip/__init__.py
-src/pip/__main__.py
-src/pip.egg-info/PKG-INFO
-src/pip.egg-info/SOURCES.txt
-src/pip.egg-info/dependency_links.txt
-src/pip.egg-info/entry_points.txt
-src/pip.egg-info/not-zip-safe
-src/pip.egg-info/top_level.txt
-src/pip/_internal/__init__.py
-src/pip/_internal/build_env.py
-src/pip/_internal/cache.py
-src/pip/_internal/configuration.py
-src/pip/_internal/download.py
-src/pip/_internal/exceptions.py
-src/pip/_internal/index.py
-src/pip/_internal/locations.py
-src/pip/_internal/pep425tags.py
-src/pip/_internal/pyproject.py
-src/pip/_internal/resolve.py
-src/pip/_internal/wheel.py
-src/pip/_internal/cli/__init__.py
-src/pip/_internal/cli/autocompletion.py
-src/pip/_internal/cli/base_command.py
-src/pip/_internal/cli/cmdoptions.py
-src/pip/_internal/cli/main_parser.py
-src/pip/_internal/cli/parser.py
-src/pip/_internal/cli/status_codes.py
-src/pip/_internal/commands/__init__.py
-src/pip/_internal/commands/check.py
-src/pip/_internal/commands/completion.py
-src/pip/_internal/commands/configuration.py
-src/pip/_internal/commands/download.py
-src/pip/_internal/commands/freeze.py
-src/pip/_internal/commands/hash.py
-src/pip/_internal/commands/help.py
-src/pip/_internal/commands/install.py
-src/pip/_internal/commands/list.py
-src/pip/_internal/commands/search.py
-src/pip/_internal/commands/show.py
-src/pip/_internal/commands/uninstall.py
-src/pip/_internal/commands/wheel.py
-src/pip/_internal/models/__init__.py
-src/pip/_internal/models/candidate.py
-src/pip/_internal/models/format_control.py
-src/pip/_internal/models/index.py
-src/pip/_internal/models/link.py
-src/pip/_internal/operations/__init__.py
-src/pip/_internal/operations/check.py
-src/pip/_internal/operations/freeze.py
-src/pip/_internal/operations/prepare.py
-src/pip/_internal/req/__init__.py
-src/pip/_internal/req/constructors.py
-src/pip/_internal/req/req_file.py
-src/pip/_internal/req/req_install.py
-src/pip/_internal/req/req_set.py
-src/pip/_internal/req/req_tracker.py
-src/pip/_internal/req/req_uninstall.py
-src/pip/_internal/utils/__init__.py
-src/pip/_internal/utils/appdirs.py
-src/pip/_internal/utils/compat.py
-src/pip/_internal/utils/deprecation.py
-src/pip/_internal/utils/encoding.py
-src/pip/_internal/utils/filesystem.py
-src/pip/_internal/utils/glibc.py
-src/pip/_internal/utils/hashes.py
-src/pip/_internal/utils/logging.py
-src/pip/_internal/utils/misc.py
-src/pip/_internal/utils/models.py
-src/pip/_internal/utils/outdated.py
-src/pip/_internal/utils/packaging.py
-src/pip/_internal/utils/setuptools_build.py
-src/pip/_internal/utils/temp_dir.py
-src/pip/_internal/utils/typing.py
-src/pip/_internal/utils/ui.py
-src/pip/_internal/vcs/__init__.py
-src/pip/_internal/vcs/bazaar.py
-src/pip/_internal/vcs/git.py
-src/pip/_internal/vcs/mercurial.py
-src/pip/_internal/vcs/subversion.py
-src/pip/_vendor/README.rst
-src/pip/_vendor/__init__.py
-src/pip/_vendor/appdirs.LICENSE.txt
-src/pip/_vendor/appdirs.py
-src/pip/_vendor/distro.LICENSE
-src/pip/_vendor/distro.py
-src/pip/_vendor/ipaddress.LICENSE
-src/pip/_vendor/ipaddress.py
-src/pip/_vendor/pyparsing.LICENSE
-src/pip/_vendor/pyparsing.py
-src/pip/_vendor/retrying.LICENSE
-src/pip/_vendor/retrying.py
-src/pip/_vendor/six.LICENSE
-src/pip/_vendor/six.py
-src/pip/_vendor/vendor.txt
-src/pip/_vendor/cachecontrol/LICENSE.txt
-src/pip/_vendor/cachecontrol/__init__.py
-src/pip/_vendor/cachecontrol/_cmd.py
-src/pip/_vendor/cachecontrol/adapter.py
-src/pip/_vendor/cachecontrol/cache.py
-src/pip/_vendor/cachecontrol/compat.py
-src/pip/_vendor/cachecontrol/controller.py
-src/pip/_vendor/cachecontrol/filewrapper.py
-src/pip/_vendor/cachecontrol/heuristics.py
-src/pip/_vendor/cachecontrol/serialize.py
-src/pip/_vendor/cachecontrol/wrapper.py
-src/pip/_vendor/cachecontrol/caches/__init__.py
-src/pip/_vendor/cachecontrol/caches/file_cache.py
-src/pip/_vendor/cachecontrol/caches/redis_cache.py
-src/pip/_vendor/certifi/LICENSE
-src/pip/_vendor/certifi/__init__.py
-src/pip/_vendor/certifi/__main__.py
-src/pip/_vendor/certifi/cacert.pem
-src/pip/_vendor/certifi/core.py
-src/pip/_vendor/chardet/LICENSE
-src/pip/_vendor/chardet/__init__.py
-src/pip/_vendor/chardet/big5freq.py
-src/pip/_vendor/chardet/big5prober.py
-src/pip/_vendor/chardet/chardistribution.py
-src/pip/_vendor/chardet/charsetgroupprober.py
-src/pip/_vendor/chardet/charsetprober.py
-src/pip/_vendor/chardet/codingstatemachine.py
-src/pip/_vendor/chardet/compat.py
-src/pip/_vendor/chardet/cp949prober.py
-src/pip/_vendor/chardet/enums.py
-src/pip/_vendor/chardet/escprober.py
-src/pip/_vendor/chardet/escsm.py
-src/pip/_vendor/chardet/eucjpprober.py
-src/pip/_vendor/chardet/euckrfreq.py
-src/pip/_vendor/chardet/euckrprober.py
-src/pip/_vendor/chardet/euctwfreq.py
-src/pip/_vendor/chardet/euctwprober.py
-src/pip/_vendor/chardet/gb2312freq.py
-src/pip/_vendor/chardet/gb2312prober.py
-src/pip/_vendor/chardet/hebrewprober.py
-src/pip/_vendor/chardet/jisfreq.py
-src/pip/_vendor/chardet/jpcntx.py
-src/pip/_vendor/chardet/langbulgarianmodel.py
-src/pip/_vendor/chardet/langcyrillicmodel.py
-src/pip/_vendor/chardet/langgreekmodel.py
-src/pip/_vendor/chardet/langhebrewmodel.py
-src/pip/_vendor/chardet/langhungarianmodel.py
-src/pip/_vendor/chardet/langthaimodel.py
-src/pip/_vendor/chardet/langturkishmodel.py
-src/pip/_vendor/chardet/latin1prober.py
-src/pip/_vendor/chardet/mbcharsetprober.py
-src/pip/_vendor/chardet/mbcsgroupprober.py
-src/pip/_vendor/chardet/mbcssm.py
-src/pip/_vendor/chardet/sbcharsetprober.py
-src/pip/_vendor/chardet/sbcsgroupprober.py
-src/pip/_vendor/chardet/sjisprober.py
-src/pip/_vendor/chardet/universaldetector.py
-src/pip/_vendor/chardet/utf8prober.py
-src/pip/_vendor/chardet/version.py
-src/pip/_vendor/chardet/cli/__init__.py
-src/pip/_vendor/chardet/cli/chardetect.py
-src/pip/_vendor/colorama/LICENSE.txt
-src/pip/_vendor/colorama/__init__.py
-src/pip/_vendor/colorama/ansi.py
-src/pip/_vendor/colorama/ansitowin32.py
-src/pip/_vendor/colorama/initialise.py
-src/pip/_vendor/colorama/win32.py
-src/pip/_vendor/colorama/winterm.py
-src/pip/_vendor/distlib/LICENSE.txt
-src/pip/_vendor/distlib/__init__.py
-src/pip/_vendor/distlib/compat.py
-src/pip/_vendor/distlib/database.py
-src/pip/_vendor/distlib/index.py
-src/pip/_vendor/distlib/locators.py
-src/pip/_vendor/distlib/manifest.py
-src/pip/_vendor/distlib/markers.py
-src/pip/_vendor/distlib/metadata.py
-src/pip/_vendor/distlib/resources.py
-src/pip/_vendor/distlib/scripts.py
-src/pip/_vendor/distlib/t32.exe
-src/pip/_vendor/distlib/t64.exe
-src/pip/_vendor/distlib/util.py
-src/pip/_vendor/distlib/version.py
-src/pip/_vendor/distlib/w32.exe
-src/pip/_vendor/distlib/w64.exe
-src/pip/_vendor/distlib/wheel.py
-src/pip/_vendor/distlib/_backport/__init__.py
-src/pip/_vendor/distlib/_backport/misc.py
-src/pip/_vendor/distlib/_backport/shutil.py
-src/pip/_vendor/distlib/_backport/sysconfig.cfg
-src/pip/_vendor/distlib/_backport/sysconfig.py
-src/pip/_vendor/distlib/_backport/tarfile.py
-src/pip/_vendor/html5lib/LICENSE
-src/pip/_vendor/html5lib/__init__.py
-src/pip/_vendor/html5lib/_ihatexml.py
-src/pip/_vendor/html5lib/_inputstream.py
-src/pip/_vendor/html5lib/_tokenizer.py
-src/pip/_vendor/html5lib/_utils.py
-src/pip/_vendor/html5lib/constants.py
-src/pip/_vendor/html5lib/html5parser.py
-src/pip/_vendor/html5lib/serializer.py
-src/pip/_vendor/html5lib/_trie/__init__.py
-src/pip/_vendor/html5lib/_trie/_base.py
-src/pip/_vendor/html5lib/_trie/datrie.py
-src/pip/_vendor/html5lib/_trie/py.py
-src/pip/_vendor/html5lib/filters/__init__.py
-src/pip/_vendor/html5lib/filters/alphabeticalattributes.py
-src/pip/_vendor/html5lib/filters/base.py
-src/pip/_vendor/html5lib/filters/inject_meta_charset.py
-src/pip/_vendor/html5lib/filters/lint.py
-src/pip/_vendor/html5lib/filters/optionaltags.py
-src/pip/_vendor/html5lib/filters/sanitizer.py
-src/pip/_vendor/html5lib/filters/whitespace.py
-src/pip/_vendor/html5lib/treeadapters/__init__.py
-src/pip/_vendor/html5lib/treeadapters/genshi.py
-src/pip/_vendor/html5lib/treeadapters/sax.py
-src/pip/_vendor/html5lib/treebuilders/__init__.py
-src/pip/_vendor/html5lib/treebuilders/base.py
-src/pip/_vendor/html5lib/treebuilders/dom.py
-src/pip/_vendor/html5lib/treebuilders/etree.py
-src/pip/_vendor/html5lib/treebuilders/etree_lxml.py
-src/pip/_vendor/html5lib/treewalkers/__init__.py
-src/pip/_vendor/html5lib/treewalkers/base.py
-src/pip/_vendor/html5lib/treewalkers/dom.py
-src/pip/_vendor/html5lib/treewalkers/etree.py
-src/pip/_vendor/html5lib/treewalkers/etree_lxml.py
-src/pip/_vendor/html5lib/treewalkers/genshi.py
-src/pip/_vendor/idna/LICENSE.rst
-src/pip/_vendor/idna/__init__.py
-src/pip/_vendor/idna/codec.py
-src/pip/_vendor/idna/compat.py
-src/pip/_vendor/idna/core.py
-src/pip/_vendor/idna/idnadata.py
-src/pip/_vendor/idna/intranges.py
-src/pip/_vendor/idna/package_data.py
-src/pip/_vendor/idna/uts46data.py
-src/pip/_vendor/lockfile/LICENSE
-src/pip/_vendor/lockfile/__init__.py
-src/pip/_vendor/lockfile/linklockfile.py
-src/pip/_vendor/lockfile/mkdirlockfile.py
-src/pip/_vendor/lockfile/pidlockfile.py
-src/pip/_vendor/lockfile/sqlitelockfile.py
-src/pip/_vendor/lockfile/symlinklockfile.py
-src/pip/_vendor/msgpack/COPYING
-src/pip/_vendor/msgpack/__init__.py
-src/pip/_vendor/msgpack/_version.py
-src/pip/_vendor/msgpack/exceptions.py
-src/pip/_vendor/msgpack/fallback.py
-src/pip/_vendor/packaging/LICENSE
-src/pip/_vendor/packaging/LICENSE.APACHE
-src/pip/_vendor/packaging/LICENSE.BSD
-src/pip/_vendor/packaging/__about__.py
-src/pip/_vendor/packaging/__init__.py
-src/pip/_vendor/packaging/_compat.py
-src/pip/_vendor/packaging/_structures.py
-src/pip/_vendor/packaging/markers.py
-src/pip/_vendor/packaging/requirements.py
-src/pip/_vendor/packaging/specifiers.py
-src/pip/_vendor/packaging/utils.py
-src/pip/_vendor/packaging/version.py
-src/pip/_vendor/pep517/LICENSE
-src/pip/_vendor/pep517/__init__.py
-src/pip/_vendor/pep517/_in_process.py
-src/pip/_vendor/pep517/build.py
-src/pip/_vendor/pep517/check.py
-src/pip/_vendor/pep517/colorlog.py
-src/pip/_vendor/pep517/compat.py
-src/pip/_vendor/pep517/envbuild.py
-src/pip/_vendor/pep517/wrappers.py
-src/pip/_vendor/pkg_resources/LICENSE
-src/pip/_vendor/pkg_resources/__init__.py
-src/pip/_vendor/pkg_resources/py31compat.py
-src/pip/_vendor/progress/LICENSE
-src/pip/_vendor/progress/__init__.py
-src/pip/_vendor/progress/bar.py
-src/pip/_vendor/progress/counter.py
-src/pip/_vendor/progress/helpers.py
-src/pip/_vendor/progress/spinner.py
-src/pip/_vendor/pytoml/LICENSE
-src/pip/_vendor/pytoml/__init__.py
-src/pip/_vendor/pytoml/core.py
-src/pip/_vendor/pytoml/parser.py
-src/pip/_vendor/pytoml/test.py
-src/pip/_vendor/pytoml/utils.py
-src/pip/_vendor/pytoml/writer.py
-src/pip/_vendor/requests/LICENSE
-src/pip/_vendor/requests/__init__.py
-src/pip/_vendor/requests/__version__.py
-src/pip/_vendor/requests/_internal_utils.py
-src/pip/_vendor/requests/adapters.py
-src/pip/_vendor/requests/api.py
-src/pip/_vendor/requests/auth.py
-src/pip/_vendor/requests/certs.py
-src/pip/_vendor/requests/compat.py
-src/pip/_vendor/requests/cookies.py
-src/pip/_vendor/requests/exceptions.py
-src/pip/_vendor/requests/help.py
-src/pip/_vendor/requests/hooks.py
-src/pip/_vendor/requests/models.py
-src/pip/_vendor/requests/packages.py
-src/pip/_vendor/requests/sessions.py
-src/pip/_vendor/requests/status_codes.py
-src/pip/_vendor/requests/structures.py
-src/pip/_vendor/requests/utils.py
-src/pip/_vendor/urllib3/LICENSE.txt
-src/pip/_vendor/urllib3/__init__.py
-src/pip/_vendor/urllib3/_collections.py
-src/pip/_vendor/urllib3/connection.py
-src/pip/_vendor/urllib3/connectionpool.py
-src/pip/_vendor/urllib3/exceptions.py
-src/pip/_vendor/urllib3/fields.py
-src/pip/_vendor/urllib3/filepost.py
-src/pip/_vendor/urllib3/poolmanager.py
-src/pip/_vendor/urllib3/request.py
-src/pip/_vendor/urllib3/response.py
-src/pip/_vendor/urllib3/contrib/__init__.py
-src/pip/_vendor/urllib3/contrib/_appengine_environ.py
-src/pip/_vendor/urllib3/contrib/appengine.py
-src/pip/_vendor/urllib3/contrib/ntlmpool.py
-src/pip/_vendor/urllib3/contrib/pyopenssl.py
-src/pip/_vendor/urllib3/contrib/securetransport.py
-src/pip/_vendor/urllib3/contrib/socks.py
-src/pip/_vendor/urllib3/contrib/_securetransport/__init__.py
-src/pip/_vendor/urllib3/contrib/_securetransport/bindings.py
-src/pip/_vendor/urllib3/contrib/_securetransport/low_level.py
-src/pip/_vendor/urllib3/packages/__init__.py
-src/pip/_vendor/urllib3/packages/six.py
-src/pip/_vendor/urllib3/packages/backports/__init__.py
-src/pip/_vendor/urllib3/packages/backports/makefile.py
-src/pip/_vendor/urllib3/packages/ssl_match_hostname/__init__.py
-src/pip/_vendor/urllib3/packages/ssl_match_hostname/_implementation.py
-src/pip/_vendor/urllib3/util/__init__.py
-src/pip/_vendor/urllib3/util/connection.py
-src/pip/_vendor/urllib3/util/queue.py
-src/pip/_vendor/urllib3/util/request.py
-src/pip/_vendor/urllib3/util/response.py
-src/pip/_vendor/urllib3/util/retry.py
-src/pip/_vendor/urllib3/util/ssl_.py
-src/pip/_vendor/urllib3/util/timeout.py
-src/pip/_vendor/urllib3/util/url.py
-src/pip/_vendor/urllib3/util/wait.py
-src/pip/_vendor/webencodings/LICENSE
-src/pip/_vendor/webencodings/__init__.py
-src/pip/_vendor/webencodings/labels.py
-src/pip/_vendor/webencodings/mklabels.py
-src/pip/_vendor/webencodings/tests.py
-src/pip/_vendor/webencodings/x_user_defined.py
\ No newline at end of file
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/dependency_links.txt b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/dependency_links.txt
deleted file mode 100644
index 8b13789..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/dependency_links.txt
+++ /dev/null
@@ -1 +0,0 @@
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/entry_points.txt b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/entry_points.txt
deleted file mode 100644
index f5809cb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/entry_points.txt
+++ /dev/null
@@ -1,5 +0,0 @@
-[console_scripts]
-pip = pip._internal:main
-pip3 = pip._internal:main
-pip3.7 = pip._internal:main
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/not-zip-safe b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/not-zip-safe
deleted file mode 100644
index 8b13789..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/not-zip-safe
+++ /dev/null
@@ -1 +0,0 @@
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/top_level.txt b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/top_level.txt
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/EGG-INFO/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__init__.py
deleted file mode 100644
index f48c1ca..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__init__.py
+++ /dev/null
@@ -1 +0,0 @@
-__version__ = "19.0.3"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__main__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__main__.py
deleted file mode 100644
index 0c223f8..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__main__.py
+++ /dev/null
@@ -1,19 +0,0 @@
-from __future__ import absolute_import
-
-import os
-import sys
-
-# If we are running from a wheel, add the wheel to sys.path
-# This allows the usage python pip-*.whl/pip install pip-*.whl
-if __package__ == '':
-    # __file__ is pip-*.whl/pip/__main__.py
-    # first dirname call strips of '/__main__.py', second strips off '/pip'
-    # Resulting path is the name of the wheel itself
-    # Add that to sys.path so we can import pip
-    path = os.path.dirname(os.path.dirname(__file__))
-    sys.path.insert(0, path)
-
-from pip._internal import main as _main  # isort:skip # noqa
-
-if __name__ == '__main__':
-    sys.exit(_main())
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index e942a3d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__pycache__/__main__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__pycache__/__main__.cpython-37.pyc
deleted file mode 100644
index 3ab0d17..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/__pycache__/__main__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__init__.py
deleted file mode 100644
index 276124d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__init__.py
+++ /dev/null
@@ -1,78 +0,0 @@
-#!/usr/bin/env python
-from __future__ import absolute_import
-
-import locale
-import logging
-import os
-import warnings
-
-import sys
-
-# 2016-06-17 barry@debian.org: urllib3 1.14 added optional support for socks,
-# but if invoked (i.e. imported), it will issue a warning to stderr if socks
-# isn't available.  requests unconditionally imports urllib3's socks contrib
-# module, triggering this warning.  The warning breaks DEP-8 tests (because of
-# the stderr output) and is just plain annoying in normal usage.  I don't want
-# to add socks as yet another dependency for pip, nor do I want to allow-stder
-# in the DEP-8 tests, so just suppress the warning.  pdb tells me this has to
-# be done before the import of pip.vcs.
-from pip._vendor.urllib3.exceptions import DependencyWarning
-warnings.filterwarnings("ignore", category=DependencyWarning)  # noqa
-
-# We want to inject the use of SecureTransport as early as possible so that any
-# references or sessions or what have you are ensured to have it, however we
-# only want to do this in the case that we're running on macOS and the linked
-# OpenSSL is too old to handle TLSv1.2
-try:
-    import ssl
-except ImportError:
-    pass
-else:
-    # Checks for OpenSSL 1.0.1 on MacOS
-    if sys.platform == "darwin" and ssl.OPENSSL_VERSION_NUMBER < 0x1000100f:
-        try:
-            from pip._vendor.urllib3.contrib import securetransport
-        except (ImportError, OSError):
-            pass
-        else:
-            securetransport.inject_into_urllib3()
-
-from pip._internal.cli.autocompletion import autocomplete
-from pip._internal.cli.main_parser import parse_command
-from pip._internal.commands import commands_dict
-from pip._internal.exceptions import PipError
-from pip._internal.utils import deprecation
-from pip._internal.vcs import git, mercurial, subversion, bazaar  # noqa
-from pip._vendor.urllib3.exceptions import InsecureRequestWarning
-
-logger = logging.getLogger(__name__)
-
-# Hide the InsecureRequestWarning from urllib3
-warnings.filterwarnings("ignore", category=InsecureRequestWarning)
-
-
-def main(args=None):
-    if args is None:
-        args = sys.argv[1:]
-
-    # Configure our deprecation warnings to be sent through loggers
-    deprecation.install_warning_logger()
-
-    autocomplete()
-
-    try:
-        cmd_name, cmd_args = parse_command(args)
-    except PipError as exc:
-        sys.stderr.write("ERROR: %s" % exc)
-        sys.stderr.write(os.linesep)
-        sys.exit(1)
-
-    # Needed for locale.getpreferredencoding(False) to work
-    # in pip._internal.utils.encoding.auto_decode
-    try:
-        locale.setlocale(locale.LC_ALL, '')
-    except locale.Error as e:
-        # setlocale can apparently crash if locale are uninitialized
-        logger.debug("Ignoring error %s when setting locale", e)
-    command = commands_dict[cmd_name](isolated=("--isolated" in cmd_args))
-    return command.main(cmd_args)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 652b82d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/build_env.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/build_env.cpython-37.pyc
deleted file mode 100644
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/build_env.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/cache.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/cache.cpython-37.pyc
deleted file mode 100644
index 317369b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/cache.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/configuration.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/configuration.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/index.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/index.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/locations.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/locations.cpython-37.pyc
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index a1dc40a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/locations.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/pep425tags.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/pep425tags.cpython-37.pyc
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/pep425tags.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/pyproject.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/pyproject.cpython-37.pyc
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+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/resolve.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/resolve.cpython-37.pyc
deleted file mode 100644
index ca401eb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/resolve.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/wheel.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/wheel.cpython-37.pyc
deleted file mode 100644
index 037cf93..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/__pycache__/wheel.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/build_env.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/build_env.py
deleted file mode 100644
index d744cc7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/build_env.py
+++ /dev/null
@@ -1,215 +0,0 @@
-"""Build Environment used for isolation during sdist building
-"""
-
-import logging
-import os
-import sys
-import textwrap
-from collections import OrderedDict
-from distutils.sysconfig import get_python_lib
-from sysconfig import get_paths
-
-from pip._vendor.pkg_resources import Requirement, VersionConflict, WorkingSet
-
-from pip import __file__ as pip_location
-from pip._internal.utils.misc import call_subprocess
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.utils.ui import open_spinner
-
-if MYPY_CHECK_RUNNING:
-    from typing import Tuple, Set, Iterable, Optional, List  # noqa: F401
-    from pip._internal.index import PackageFinder  # noqa: F401
-
-logger = logging.getLogger(__name__)
-
-
-class _Prefix:
-
-    def __init__(self, path):
-        # type: (str) -> None
-        self.path = path
-        self.setup = False
-        self.bin_dir = get_paths(
-            'nt' if os.name == 'nt' else 'posix_prefix',
-            vars={'base': path, 'platbase': path}
-        )['scripts']
-        # Note: prefer distutils' sysconfig to get the
-        # library paths so PyPy is correctly supported.
-        purelib = get_python_lib(plat_specific=False, prefix=path)
-        platlib = get_python_lib(plat_specific=True, prefix=path)
-        if purelib == platlib:
-            self.lib_dirs = [purelib]
-        else:
-            self.lib_dirs = [purelib, platlib]
-
-
-class BuildEnvironment(object):
-    """Creates and manages an isolated environment to install build deps
-    """
-
-    def __init__(self):
-        # type: () -> None
-        self._temp_dir = TempDirectory(kind="build-env")
-        self._temp_dir.create()
-
-        self._prefixes = OrderedDict((
-            (name, _Prefix(os.path.join(self._temp_dir.path, name)))
-            for name in ('normal', 'overlay')
-        ))
-
-        self._bin_dirs = []  # type: List[str]
-        self._lib_dirs = []  # type: List[str]
-        for prefix in reversed(list(self._prefixes.values())):
-            self._bin_dirs.append(prefix.bin_dir)
-            self._lib_dirs.extend(prefix.lib_dirs)
-
-        # Customize site to:
-        # - ensure .pth files are honored
-        # - prevent access to system site packages
-        system_sites = {
-            os.path.normcase(site) for site in (
-                get_python_lib(plat_specific=False),
-                get_python_lib(plat_specific=True),
-            )
-        }
-        self._site_dir = os.path.join(self._temp_dir.path, 'site')
-        if not os.path.exists(self._site_dir):
-            os.mkdir(self._site_dir)
-        with open(os.path.join(self._site_dir, 'sitecustomize.py'), 'w') as fp:
-            fp.write(textwrap.dedent(
-                '''
-                import os, site, sys
-
-                # First, drop system-sites related paths.
-                original_sys_path = sys.path[:]
-                known_paths = set()
-                for path in {system_sites!r}:
-                    site.addsitedir(path, known_paths=known_paths)
-                system_paths = set(
-                    os.path.normcase(path)
-                    for path in sys.path[len(original_sys_path):]
-                )
-                original_sys_path = [
-                    path for path in original_sys_path
-                    if os.path.normcase(path) not in system_paths
-                ]
-                sys.path = original_sys_path
-
-                # Second, add lib directories.
-                # ensuring .pth file are processed.
-                for path in {lib_dirs!r}:
-                    assert not path in sys.path
-                    site.addsitedir(path)
-                '''
-            ).format(system_sites=system_sites, lib_dirs=self._lib_dirs))
-
-    def __enter__(self):
-        self._save_env = {
-            name: os.environ.get(name, None)
-            for name in ('PATH', 'PYTHONNOUSERSITE', 'PYTHONPATH')
-        }
-
-        path = self._bin_dirs[:]
-        old_path = self._save_env['PATH']
-        if old_path:
-            path.extend(old_path.split(os.pathsep))
-
-        pythonpath = [self._site_dir]
-
-        os.environ.update({
-            'PATH': os.pathsep.join(path),
-            'PYTHONNOUSERSITE': '1',
-            'PYTHONPATH': os.pathsep.join(pythonpath),
-        })
-
-    def __exit__(self, exc_type, exc_val, exc_tb):
-        for varname, old_value in self._save_env.items():
-            if old_value is None:
-                os.environ.pop(varname, None)
-            else:
-                os.environ[varname] = old_value
-
-    def cleanup(self):
-        # type: () -> None
-        self._temp_dir.cleanup()
-
-    def check_requirements(self, reqs):
-        # type: (Iterable[str]) -> Tuple[Set[Tuple[str, str]], Set[str]]
-        """Return 2 sets:
-            - conflicting requirements: set of (installed, wanted) reqs tuples
-            - missing requirements: set of reqs
-        """
-        missing = set()
-        conflicting = set()
-        if reqs:
-            ws = WorkingSet(self._lib_dirs)
-            for req in reqs:
-                try:
-                    if ws.find(Requirement.parse(req)) is None:
-                        missing.add(req)
-                except VersionConflict as e:
-                    conflicting.add((str(e.args[0].as_requirement()),
-                                     str(e.args[1])))
-        return conflicting, missing
-
-    def install_requirements(
-        self,
-        finder,  # type: PackageFinder
-        requirements,  # type: Iterable[str]
-        prefix_as_string,  # type: str
-        message  # type: Optional[str]
-    ):
-        # type: (...) -> None
-        prefix = self._prefixes[prefix_as_string]
-        assert not prefix.setup
-        prefix.setup = True
-        if not requirements:
-            return
-        args = [
-            sys.executable, os.path.dirname(pip_location), 'install',
-            '--ignore-installed', '--no-user', '--prefix', prefix.path,
-            '--no-warn-script-location',
-        ]  # type: List[str]
-        if logger.getEffectiveLevel() <= logging.DEBUG:
-            args.append('-v')
-        for format_control in ('no_binary', 'only_binary'):
-            formats = getattr(finder.format_control, format_control)
-            args.extend(('--' + format_control.replace('_', '-'),
-                         ','.join(sorted(formats or {':none:'}))))
-        if finder.index_urls:
-            args.extend(['-i', finder.index_urls[0]])
-            for extra_index in finder.index_urls[1:]:
-                args.extend(['--extra-index-url', extra_index])
-        else:
-            args.append('--no-index')
-        for link in finder.find_links:
-            args.extend(['--find-links', link])
-        for _, host, _ in finder.secure_origins:
-            args.extend(['--trusted-host', host])
-        if finder.allow_all_prereleases:
-            args.append('--pre')
-        args.append('--')
-        args.extend(requirements)
-        with open_spinner(message) as spinner:
-            call_subprocess(args, show_stdout=False, spinner=spinner)
-
-
-class NoOpBuildEnvironment(BuildEnvironment):
-    """A no-op drop-in replacement for BuildEnvironment
-    """
-
-    def __init__(self):
-        pass
-
-    def __enter__(self):
-        pass
-
-    def __exit__(self, exc_type, exc_val, exc_tb):
-        pass
-
-    def cleanup(self):
-        pass
-
-    def install_requirements(self, finder, requirements, prefix, message):
-        raise NotImplementedError()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cache.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cache.py
deleted file mode 100644
index eb295c4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cache.py
+++ /dev/null
@@ -1,224 +0,0 @@
-"""Cache Management
-"""
-
-import errno
-import hashlib
-import logging
-import os
-
-from pip._vendor.packaging.utils import canonicalize_name
-
-from pip._internal.download import path_to_url
-from pip._internal.models.link import Link
-from pip._internal.utils.compat import expanduser
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.wheel import InvalidWheelFilename, Wheel
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional, Set, List, Any  # noqa: F401
-    from pip._internal.index import FormatControl  # noqa: F401
-
-logger = logging.getLogger(__name__)
-
-
-class Cache(object):
-    """An abstract class - provides cache directories for data from links
-
-
-        :param cache_dir: The root of the cache.
-        :param format_control: An object of FormatControl class to limit
-            binaries being read from the cache.
-        :param allowed_formats: which formats of files the cache should store.
-            ('binary' and 'source' are the only allowed values)
-    """
-
-    def __init__(self, cache_dir, format_control, allowed_formats):
-        # type: (str, FormatControl, Set[str]) -> None
-        super(Cache, self).__init__()
-        self.cache_dir = expanduser(cache_dir) if cache_dir else None
-        self.format_control = format_control
-        self.allowed_formats = allowed_formats
-
-        _valid_formats = {"source", "binary"}
-        assert self.allowed_formats.union(_valid_formats) == _valid_formats
-
-    def _get_cache_path_parts(self, link):
-        # type: (Link) -> List[str]
-        """Get parts of part that must be os.path.joined with cache_dir
-        """
-
-        # We want to generate an url to use as our cache key, we don't want to
-        # just re-use the URL because it might have other items in the fragment
-        # and we don't care about those.
-        key_parts = [link.url_without_fragment]
-        if link.hash_name is not None and link.hash is not None:
-            key_parts.append("=".join([link.hash_name, link.hash]))
-        key_url = "#".join(key_parts)
-
-        # Encode our key url with sha224, we'll use this because it has similar
-        # security properties to sha256, but with a shorter total output (and
-        # thus less secure). However the differences don't make a lot of
-        # difference for our use case here.
-        hashed = hashlib.sha224(key_url.encode()).hexdigest()
-
-        # We want to nest the directories some to prevent having a ton of top
-        # level directories where we might run out of sub directories on some
-        # FS.
-        parts = [hashed[:2], hashed[2:4], hashed[4:6], hashed[6:]]
-
-        return parts
-
-    def _get_candidates(self, link, package_name):
-        # type: (Link, Optional[str]) -> List[Any]
-        can_not_cache = (
-            not self.cache_dir or
-            not package_name or
-            not link
-        )
-        if can_not_cache:
-            return []
-
-        canonical_name = canonicalize_name(package_name)
-        formats = self.format_control.get_allowed_formats(
-            canonical_name
-        )
-        if not self.allowed_formats.intersection(formats):
-            return []
-
-        root = self.get_path_for_link(link)
-        try:
-            return os.listdir(root)
-        except OSError as err:
-            if err.errno in {errno.ENOENT, errno.ENOTDIR}:
-                return []
-            raise
-
-    def get_path_for_link(self, link):
-        # type: (Link) -> str
-        """Return a directory to store cached items in for link.
-        """
-        raise NotImplementedError()
-
-    def get(self, link, package_name):
-        # type: (Link, Optional[str]) -> Link
-        """Returns a link to a cached item if it exists, otherwise returns the
-        passed link.
-        """
-        raise NotImplementedError()
-
-    def _link_for_candidate(self, link, candidate):
-        # type: (Link, str) -> Link
-        root = self.get_path_for_link(link)
-        path = os.path.join(root, candidate)
-
-        return Link(path_to_url(path))
-
-    def cleanup(self):
-        # type: () -> None
-        pass
-
-
-class SimpleWheelCache(Cache):
-    """A cache of wheels for future installs.
-    """
-
-    def __init__(self, cache_dir, format_control):
-        # type: (str, FormatControl) -> None
-        super(SimpleWheelCache, self).__init__(
-            cache_dir, format_control, {"binary"}
-        )
-
-    def get_path_for_link(self, link):
-        # type: (Link) -> str
-        """Return a directory to store cached wheels for link
-
-        Because there are M wheels for any one sdist, we provide a directory
-        to cache them in, and then consult that directory when looking up
-        cache hits.
-
-        We only insert things into the cache if they have plausible version
-        numbers, so that we don't contaminate the cache with things that were
-        not unique. E.g. ./package might have dozens of installs done for it
-        and build a version of 0.0...and if we built and cached a wheel, we'd
-        end up using the same wheel even if the source has been edited.
-
-        :param link: The link of the sdist for which this will cache wheels.
-        """
-        parts = self._get_cache_path_parts(link)
-
-        # Store wheels within the root cache_dir
-        return os.path.join(self.cache_dir, "wheels", *parts)
-
-    def get(self, link, package_name):
-        # type: (Link, Optional[str]) -> Link
-        candidates = []
-
-        for wheel_name in self._get_candidates(link, package_name):
-            try:
-                wheel = Wheel(wheel_name)
-            except InvalidWheelFilename:
-                continue
-            if not wheel.supported():
-                # Built for a different python/arch/etc
-                continue
-            candidates.append((wheel.support_index_min(), wheel_name))
-
-        if not candidates:
-            return link
-
-        return self._link_for_candidate(link, min(candidates)[1])
-
-
-class EphemWheelCache(SimpleWheelCache):
-    """A SimpleWheelCache that creates it's own temporary cache directory
-    """
-
-    def __init__(self, format_control):
-        # type: (FormatControl) -> None
-        self._temp_dir = TempDirectory(kind="ephem-wheel-cache")
-        self._temp_dir.create()
-
-        super(EphemWheelCache, self).__init__(
-            self._temp_dir.path, format_control
-        )
-
-    def cleanup(self):
-        # type: () -> None
-        self._temp_dir.cleanup()
-
-
-class WheelCache(Cache):
-    """Wraps EphemWheelCache and SimpleWheelCache into a single Cache
-
-    This Cache allows for gracefully degradation, using the ephem wheel cache
-    when a certain link is not found in the simple wheel cache first.
-    """
-
-    def __init__(self, cache_dir, format_control):
-        # type: (str, FormatControl) -> None
-        super(WheelCache, self).__init__(
-            cache_dir, format_control, {'binary'}
-        )
-        self._wheel_cache = SimpleWheelCache(cache_dir, format_control)
-        self._ephem_cache = EphemWheelCache(format_control)
-
-    def get_path_for_link(self, link):
-        # type: (Link) -> str
-        return self._wheel_cache.get_path_for_link(link)
-
-    def get_ephem_path_for_link(self, link):
-        # type: (Link) -> str
-        return self._ephem_cache.get_path_for_link(link)
-
-    def get(self, link, package_name):
-        # type: (Link, Optional[str]) -> Link
-        retval = self._wheel_cache.get(link, package_name)
-        if retval is link:
-            retval = self._ephem_cache.get(link, package_name)
-        return retval
-
-    def cleanup(self):
-        # type: () -> None
-        self._wheel_cache.cleanup()
-        self._ephem_cache.cleanup()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__init__.py
deleted file mode 100644
index e589bb9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__init__.py
+++ /dev/null
@@ -1,4 +0,0 @@
-"""Subpackage containing all of pip's command line interface related code
-"""
-
-# This file intentionally does not import submodules
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 2a9f1c0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/autocompletion.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/autocompletion.cpython-37.pyc
deleted file mode 100644
index 5368708..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/autocompletion.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/base_command.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/base_command.cpython-37.pyc
deleted file mode 100644
index 0a13ac6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/base_command.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/cmdoptions.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/cmdoptions.cpython-37.pyc
deleted file mode 100644
index 79e406d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/cmdoptions.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/main_parser.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/main_parser.cpython-37.pyc
deleted file mode 100644
index b4248f2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/main_parser.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/parser.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/parser.cpython-37.pyc
deleted file mode 100644
index cb35c86..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/parser.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/status_codes.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/status_codes.cpython-37.pyc
deleted file mode 100644
index 217d9ca..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/__pycache__/status_codes.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/autocompletion.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/autocompletion.py
deleted file mode 100644
index 0a04199..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/autocompletion.py
+++ /dev/null
@@ -1,152 +0,0 @@
-"""Logic that powers autocompletion installed by ``pip completion``.
-"""
-
-import optparse
-import os
-import sys
-
-from pip._internal.cli.main_parser import create_main_parser
-from pip._internal.commands import commands_dict, get_summaries
-from pip._internal.utils.misc import get_installed_distributions
-
-
-def autocomplete():
-    """Entry Point for completion of main and subcommand options.
-    """
-    # Don't complete if user hasn't sourced bash_completion file.
-    if 'PIP_AUTO_COMPLETE' not in os.environ:
-        return
-    cwords = os.environ['COMP_WORDS'].split()[1:]
-    cword = int(os.environ['COMP_CWORD'])
-    try:
-        current = cwords[cword - 1]
-    except IndexError:
-        current = ''
-
-    subcommands = [cmd for cmd, summary in get_summaries()]
-    options = []
-    # subcommand
-    try:
-        subcommand_name = [w for w in cwords if w in subcommands][0]
-    except IndexError:
-        subcommand_name = None
-
-    parser = create_main_parser()
-    # subcommand options
-    if subcommand_name:
-        # special case: 'help' subcommand has no options
-        if subcommand_name == 'help':
-            sys.exit(1)
-        # special case: list locally installed dists for show and uninstall
-        should_list_installed = (
-            subcommand_name in ['show', 'uninstall'] and
-            not current.startswith('-')
-        )
-        if should_list_installed:
-            installed = []
-            lc = current.lower()
-            for dist in get_installed_distributions(local_only=True):
-                if dist.key.startswith(lc) and dist.key not in cwords[1:]:
-                    installed.append(dist.key)
-            # if there are no dists installed, fall back to option completion
-            if installed:
-                for dist in installed:
-                    print(dist)
-                sys.exit(1)
-
-        subcommand = commands_dict[subcommand_name]()
-
-        for opt in subcommand.parser.option_list_all:
-            if opt.help != optparse.SUPPRESS_HELP:
-                for opt_str in opt._long_opts + opt._short_opts:
-                    options.append((opt_str, opt.nargs))
-
-        # filter out previously specified options from available options
-        prev_opts = [x.split('=')[0] for x in cwords[1:cword - 1]]
-        options = [(x, v) for (x, v) in options if x not in prev_opts]
-        # filter options by current input
-        options = [(k, v) for k, v in options if k.startswith(current)]
-        # get completion type given cwords and available subcommand options
-        completion_type = get_path_completion_type(
-            cwords, cword, subcommand.parser.option_list_all,
-        )
-        # get completion files and directories if ``completion_type`` is
-        # ``<file>``, ``<dir>`` or ``<path>``
-        if completion_type:
-            options = auto_complete_paths(current, completion_type)
-            options = ((opt, 0) for opt in options)
-        for option in options:
-            opt_label = option[0]
-            # append '=' to options which require args
-            if option[1] and option[0][:2] == "--":
-                opt_label += '='
-            print(opt_label)
-    else:
-        # show main parser options only when necessary
-
-        opts = [i.option_list for i in parser.option_groups]
-        opts.append(parser.option_list)
-        opts = (o for it in opts for o in it)
-        if current.startswith('-'):
-            for opt in opts:
-                if opt.help != optparse.SUPPRESS_HELP:
-                    subcommands += opt._long_opts + opt._short_opts
-        else:
-            # get completion type given cwords and all available options
-            completion_type = get_path_completion_type(cwords, cword, opts)
-            if completion_type:
-                subcommands = auto_complete_paths(current, completion_type)
-
-        print(' '.join([x for x in subcommands if x.startswith(current)]))
-    sys.exit(1)
-
-
-def get_path_completion_type(cwords, cword, opts):
-    """Get the type of path completion (``file``, ``dir``, ``path`` or None)
-
-    :param cwords: same as the environmental variable ``COMP_WORDS``
-    :param cword: same as the environmental variable ``COMP_CWORD``
-    :param opts: The available options to check
-    :return: path completion type (``file``, ``dir``, ``path`` or None)
-    """
-    if cword < 2 or not cwords[cword - 2].startswith('-'):
-        return
-    for opt in opts:
-        if opt.help == optparse.SUPPRESS_HELP:
-            continue
-        for o in str(opt).split('/'):
-            if cwords[cword - 2].split('=')[0] == o:
-                if not opt.metavar or any(
-                        x in ('path', 'file', 'dir')
-                        for x in opt.metavar.split('/')):
-                    return opt.metavar
-
-
-def auto_complete_paths(current, completion_type):
-    """If ``completion_type`` is ``file`` or ``path``, list all regular files
-    and directories starting with ``current``; otherwise only list directories
-    starting with ``current``.
-
-    :param current: The word to be completed
-    :param completion_type: path completion type(`file`, `path` or `dir`)i
-    :return: A generator of regular files and/or directories
-    """
-    directory, filename = os.path.split(current)
-    current_path = os.path.abspath(directory)
-    # Don't complete paths if they can't be accessed
-    if not os.access(current_path, os.R_OK):
-        return
-    filename = os.path.normcase(filename)
-    # list all files that start with ``filename``
-    file_list = (x for x in os.listdir(current_path)
-                 if os.path.normcase(x).startswith(filename))
-    for f in file_list:
-        opt = os.path.join(current_path, f)
-        comp_file = os.path.normcase(os.path.join(directory, f))
-        # complete regular files when there is not ``<dir>`` after option
-        # complete directories when there is ``<file>``, ``<path>`` or
-        # ``<dir>``after option
-        if completion_type != 'dir' and os.path.isfile(opt):
-            yield comp_file
-        elif os.path.isdir(opt):
-            yield os.path.join(comp_file, '')
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/base_command.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/base_command.py
deleted file mode 100644
index 3ceea49..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/base_command.py
+++ /dev/null
@@ -1,341 +0,0 @@
-"""Base Command class, and related routines"""
-from __future__ import absolute_import, print_function
-
-import logging
-import logging.config
-import optparse
-import os
-import platform
-import sys
-import traceback
-
-from pip._internal.cli import cmdoptions
-from pip._internal.cli.parser import (
-    ConfigOptionParser, UpdatingDefaultsHelpFormatter,
-)
-from pip._internal.cli.status_codes import (
-    ERROR, PREVIOUS_BUILD_DIR_ERROR, SUCCESS, UNKNOWN_ERROR,
-    VIRTUALENV_NOT_FOUND,
-)
-from pip._internal.download import PipSession
-from pip._internal.exceptions import (
-    BadCommand, CommandError, InstallationError, PreviousBuildDirError,
-    UninstallationError,
-)
-from pip._internal.index import PackageFinder
-from pip._internal.locations import running_under_virtualenv
-from pip._internal.req.constructors import (
-    install_req_from_editable, install_req_from_line,
-)
-from pip._internal.req.req_file import parse_requirements
-from pip._internal.utils.deprecation import deprecated
-from pip._internal.utils.logging import BrokenStdoutLoggingError, setup_logging
-from pip._internal.utils.misc import (
-    get_prog, normalize_path, redact_password_from_url,
-)
-from pip._internal.utils.outdated import pip_version_check
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional, List, Tuple, Any  # noqa: F401
-    from optparse import Values  # noqa: F401
-    from pip._internal.cache import WheelCache  # noqa: F401
-    from pip._internal.req.req_set import RequirementSet  # noqa: F401
-
-__all__ = ['Command']
-
-logger = logging.getLogger(__name__)
-
-
-class Command(object):
-    name = None  # type: Optional[str]
-    usage = None  # type: Optional[str]
-    hidden = False  # type: bool
-    ignore_require_venv = False  # type: bool
-
-    def __init__(self, isolated=False):
-        # type: (bool) -> None
-        parser_kw = {
-            'usage': self.usage,
-            'prog': '%s %s' % (get_prog(), self.name),
-            'formatter': UpdatingDefaultsHelpFormatter(),
-            'add_help_option': False,
-            'name': self.name,
-            'description': self.__doc__,
-            'isolated': isolated,
-        }
-
-        self.parser = ConfigOptionParser(**parser_kw)
-
-        # Commands should add options to this option group
-        optgroup_name = '%s Options' % self.name.capitalize()
-        self.cmd_opts = optparse.OptionGroup(self.parser, optgroup_name)
-
-        # Add the general options
-        gen_opts = cmdoptions.make_option_group(
-            cmdoptions.general_group,
-            self.parser,
-        )
-        self.parser.add_option_group(gen_opts)
-
-    def run(self, options, args):
-        # type: (Values, List[Any]) -> Any
-        raise NotImplementedError
-
-    def _build_session(self, options, retries=None, timeout=None):
-        # type: (Values, Optional[int], Optional[int]) -> PipSession
-        session = PipSession(
-            cache=(
-                normalize_path(os.path.join(options.cache_dir, "http"))
-                if options.cache_dir else None
-            ),
-            retries=retries if retries is not None else options.retries,
-            insecure_hosts=options.trusted_hosts,
-        )
-
-        # Handle custom ca-bundles from the user
-        if options.cert:
-            session.verify = options.cert
-
-        # Handle SSL client certificate
-        if options.client_cert:
-            session.cert = options.client_cert
-
-        # Handle timeouts
-        if options.timeout or timeout:
-            session.timeout = (
-                timeout if timeout is not None else options.timeout
-            )
-
-        # Handle configured proxies
-        if options.proxy:
-            session.proxies = {
-                "http": options.proxy,
-                "https": options.proxy,
-            }
-
-        # Determine if we can prompt the user for authentication or not
-        session.auth.prompting = not options.no_input
-
-        return session
-
-    def parse_args(self, args):
-        # type: (List[str]) -> Tuple
-        # factored out for testability
-        return self.parser.parse_args(args)
-
-    def main(self, args):
-        # type: (List[str]) -> int
-        options, args = self.parse_args(args)
-
-        # Set verbosity so that it can be used elsewhere.
-        self.verbosity = options.verbose - options.quiet
-
-        level_number = setup_logging(
-            verbosity=self.verbosity,
-            no_color=options.no_color,
-            user_log_file=options.log,
-        )
-
-        if sys.version_info[:2] == (3, 4):
-            deprecated(
-                "Python 3.4 support has been deprecated. pip 19.1 will be the "
-                "last one supporting it. Please upgrade your Python as Python "
-                "3.4 won't be maintained after March 2019 (cf PEP 429).",
-                replacement=None,
-                gone_in='19.2',
-            )
-        elif sys.version_info[:2] == (2, 7):
-            message = (
-                "A future version of pip will drop support for Python 2.7."
-            )
-            if platform.python_implementation() == "CPython":
-                message = (
-                    "Python 2.7 will reach the end of its life on January "
-                    "1st, 2020. Please upgrade your Python as Python 2.7 "
-                    "won't be maintained after that date. "
-                ) + message
-            deprecated(message, replacement=None, gone_in=None)
-
-        # TODO: Try to get these passing down from the command?
-        #       without resorting to os.environ to hold these.
-        #       This also affects isolated builds and it should.
-
-        if options.no_input:
-            os.environ['PIP_NO_INPUT'] = '1'
-
-        if options.exists_action:
-            os.environ['PIP_EXISTS_ACTION'] = ' '.join(options.exists_action)
-
-        if options.require_venv and not self.ignore_require_venv:
-            # If a venv is required check if it can really be found
-            if not running_under_virtualenv():
-                logger.critical(
-                    'Could not find an activated virtualenv (required).'
-                )
-                sys.exit(VIRTUALENV_NOT_FOUND)
-
-        try:
-            status = self.run(options, args)
-            # FIXME: all commands should return an exit status
-            # and when it is done, isinstance is not needed anymore
-            if isinstance(status, int):
-                return status
-        except PreviousBuildDirError as exc:
-            logger.critical(str(exc))
-            logger.debug('Exception information:', exc_info=True)
-
-            return PREVIOUS_BUILD_DIR_ERROR
-        except (InstallationError, UninstallationError, BadCommand) as exc:
-            logger.critical(str(exc))
-            logger.debug('Exception information:', exc_info=True)
-
-            return ERROR
-        except CommandError as exc:
-            logger.critical('ERROR: %s', exc)
-            logger.debug('Exception information:', exc_info=True)
-
-            return ERROR
-        except BrokenStdoutLoggingError:
-            # Bypass our logger and write any remaining messages to stderr
-            # because stdout no longer works.
-            print('ERROR: Pipe to stdout was broken', file=sys.stderr)
-            if level_number <= logging.DEBUG:
-                traceback.print_exc(file=sys.stderr)
-
-            return ERROR
-        except KeyboardInterrupt:
-            logger.critical('Operation cancelled by user')
-            logger.debug('Exception information:', exc_info=True)
-
-            return ERROR
-        except BaseException:
-            logger.critical('Exception:', exc_info=True)
-
-            return UNKNOWN_ERROR
-        finally:
-            allow_version_check = (
-                # Does this command have the index_group options?
-                hasattr(options, "no_index") and
-                # Is this command allowed to perform this check?
-                not (options.disable_pip_version_check or options.no_index)
-            )
-            # Check if we're using the latest version of pip available
-            if allow_version_check:
-                session = self._build_session(
-                    options,
-                    retries=0,
-                    timeout=min(5, options.timeout)
-                )
-                with session:
-                    pip_version_check(session, options)
-
-            # Shutdown the logging module
-            logging.shutdown()
-
-        return SUCCESS
-
-
-class RequirementCommand(Command):
-
-    @staticmethod
-    def populate_requirement_set(requirement_set,  # type: RequirementSet
-                                 args,             # type: List[str]
-                                 options,          # type: Values
-                                 finder,           # type: PackageFinder
-                                 session,          # type: PipSession
-                                 name,             # type: str
-                                 wheel_cache       # type: Optional[WheelCache]
-                                 ):
-        # type: (...) -> None
-        """
-        Marshal cmd line args into a requirement set.
-        """
-        # NOTE: As a side-effect, options.require_hashes and
-        #       requirement_set.require_hashes may be updated
-
-        for filename in options.constraints:
-            for req_to_add in parse_requirements(
-                    filename,
-                    constraint=True, finder=finder, options=options,
-                    session=session, wheel_cache=wheel_cache):
-                req_to_add.is_direct = True
-                requirement_set.add_requirement(req_to_add)
-
-        for req in args:
-            req_to_add = install_req_from_line(
-                req, None, isolated=options.isolated_mode,
-                use_pep517=options.use_pep517,
-                wheel_cache=wheel_cache
-            )
-            req_to_add.is_direct = True
-            requirement_set.add_requirement(req_to_add)
-
-        for req in options.editables:
-            req_to_add = install_req_from_editable(
-                req,
-                isolated=options.isolated_mode,
-                use_pep517=options.use_pep517,
-                wheel_cache=wheel_cache
-            )
-            req_to_add.is_direct = True
-            requirement_set.add_requirement(req_to_add)
-
-        for filename in options.requirements:
-            for req_to_add in parse_requirements(
-                    filename,
-                    finder=finder, options=options, session=session,
-                    wheel_cache=wheel_cache,
-                    use_pep517=options.use_pep517):
-                req_to_add.is_direct = True
-                requirement_set.add_requirement(req_to_add)
-        # If --require-hashes was a line in a requirements file, tell
-        # RequirementSet about it:
-        requirement_set.require_hashes = options.require_hashes
-
-        if not (args or options.editables or options.requirements):
-            opts = {'name': name}
-            if options.find_links:
-                raise CommandError(
-                    'You must give at least one requirement to %(name)s '
-                    '(maybe you meant "pip %(name)s %(links)s"?)' %
-                    dict(opts, links=' '.join(options.find_links)))
-            else:
-                raise CommandError(
-                    'You must give at least one requirement to %(name)s '
-                    '(see "pip help %(name)s")' % opts)
-
-    def _build_package_finder(
-        self,
-        options,               # type: Values
-        session,               # type: PipSession
-        platform=None,         # type: Optional[str]
-        python_versions=None,  # type: Optional[List[str]]
-        abi=None,              # type: Optional[str]
-        implementation=None    # type: Optional[str]
-    ):
-        # type: (...) -> PackageFinder
-        """
-        Create a package finder appropriate to this requirement command.
-        """
-        index_urls = [options.index_url] + options.extra_index_urls
-        if options.no_index:
-            logger.debug(
-                'Ignoring indexes: %s',
-                ','.join(redact_password_from_url(url) for url in index_urls),
-            )
-            index_urls = []
-
-        return PackageFinder(
-            find_links=options.find_links,
-            format_control=options.format_control,
-            index_urls=index_urls,
-            trusted_hosts=options.trusted_hosts,
-            allow_all_prereleases=options.pre,
-            session=session,
-            platform=platform,
-            versions=python_versions,
-            abi=abi,
-            implementation=implementation,
-            prefer_binary=options.prefer_binary,
-        )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/cmdoptions.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/cmdoptions.py
deleted file mode 100644
index 5cf5ee9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/cmdoptions.py
+++ /dev/null
@@ -1,809 +0,0 @@
-"""
-shared options and groups
-
-The principle here is to define options once, but *not* instantiate them
-globally. One reason being that options with action='append' can carry state
-between parses. pip parses general options twice internally, and shouldn't
-pass on state. To be consistent, all options will follow this design.
-
-"""
-from __future__ import absolute_import
-
-import textwrap
-import warnings
-from distutils.util import strtobool
-from functools import partial
-from optparse import SUPPRESS_HELP, Option, OptionGroup
-
-from pip._internal.exceptions import CommandError
-from pip._internal.locations import USER_CACHE_DIR, src_prefix
-from pip._internal.models.format_control import FormatControl
-from pip._internal.models.index import PyPI
-from pip._internal.utils.hashes import STRONG_HASHES
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.utils.ui import BAR_TYPES
-
-if MYPY_CHECK_RUNNING:
-    from typing import Any, Callable, Dict, List, Optional, Union  # noqa: F401
-    from optparse import OptionParser, Values  # noqa: F401
-    from pip._internal.cli.parser import ConfigOptionParser  # noqa: F401
-
-
-def raise_option_error(parser, option, msg):
-    """
-    Raise an option parsing error using parser.error().
-
-    Args:
-      parser: an OptionParser instance.
-      option: an Option instance.
-      msg: the error text.
-    """
-    msg = '{} error: {}'.format(option, msg)
-    msg = textwrap.fill(' '.join(msg.split()))
-    parser.error(msg)
-
-
-def make_option_group(group, parser):
-    # type: (Dict[str, Any], ConfigOptionParser) -> OptionGroup
-    """
-    Return an OptionGroup object
-    group  -- assumed to be dict with 'name' and 'options' keys
-    parser -- an optparse Parser
-    """
-    option_group = OptionGroup(parser, group['name'])
-    for option in group['options']:
-        option_group.add_option(option())
-    return option_group
-
-
-def check_install_build_global(options, check_options=None):
-    # type: (Values, Optional[Values]) -> None
-    """Disable wheels if per-setup.py call options are set.
-
-    :param options: The OptionParser options to update.
-    :param check_options: The options to check, if not supplied defaults to
-        options.
-    """
-    if check_options is None:
-        check_options = options
-
-    def getname(n):
-        return getattr(check_options, n, None)
-    names = ["build_options", "global_options", "install_options"]
-    if any(map(getname, names)):
-        control = options.format_control
-        control.disallow_binaries()
-        warnings.warn(
-            'Disabling all use of wheels due to the use of --build-options '
-            '/ --global-options / --install-options.', stacklevel=2,
-        )
-
-
-def check_dist_restriction(options, check_target=False):
-    # type: (Values, bool) -> None
-    """Function for determining if custom platform options are allowed.
-
-    :param options: The OptionParser options.
-    :param check_target: Whether or not to check if --target is being used.
-    """
-    dist_restriction_set = any([
-        options.python_version,
-        options.platform,
-        options.abi,
-        options.implementation,
-    ])
-
-    binary_only = FormatControl(set(), {':all:'})
-    sdist_dependencies_allowed = (
-        options.format_control != binary_only and
-        not options.ignore_dependencies
-    )
-
-    # Installations or downloads using dist restrictions must not combine
-    # source distributions and dist-specific wheels, as they are not
-    # gauranteed to be locally compatible.
-    if dist_restriction_set and sdist_dependencies_allowed:
-        raise CommandError(
-            "When restricting platform and interpreter constraints using "
-            "--python-version, --platform, --abi, or --implementation, "
-            "either --no-deps must be set, or --only-binary=:all: must be "
-            "set and --no-binary must not be set (or must be set to "
-            ":none:)."
-        )
-
-    if check_target:
-        if dist_restriction_set and not options.target_dir:
-            raise CommandError(
-                "Can not use any platform or abi specific options unless "
-                "installing via '--target'"
-            )
-
-
-###########
-# options #
-###########
-
-help_ = partial(
-    Option,
-    '-h', '--help',
-    dest='help',
-    action='help',
-    help='Show help.',
-)  # type: Callable[..., Option]
-
-isolated_mode = partial(
-    Option,
-    "--isolated",
-    dest="isolated_mode",
-    action="store_true",
-    default=False,
-    help=(
-        "Run pip in an isolated mode, ignoring environment variables and user "
-        "configuration."
-    ),
-)  # type: Callable[..., Option]
-
-require_virtualenv = partial(
-    Option,
-    # Run only if inside a virtualenv, bail if not.
-    '--require-virtualenv', '--require-venv',
-    dest='require_venv',
-    action='store_true',
-    default=False,
-    help=SUPPRESS_HELP
-)  # type: Callable[..., Option]
-
-verbose = partial(
-    Option,
-    '-v', '--verbose',
-    dest='verbose',
-    action='count',
-    default=0,
-    help='Give more output. Option is additive, and can be used up to 3 times.'
-)  # type: Callable[..., Option]
-
-no_color = partial(
-    Option,
-    '--no-color',
-    dest='no_color',
-    action='store_true',
-    default=False,
-    help="Suppress colored output",
-)  # type: Callable[..., Option]
-
-version = partial(
-    Option,
-    '-V', '--version',
-    dest='version',
-    action='store_true',
-    help='Show version and exit.',
-)  # type: Callable[..., Option]
-
-quiet = partial(
-    Option,
-    '-q', '--quiet',
-    dest='quiet',
-    action='count',
-    default=0,
-    help=(
-        'Give less output. Option is additive, and can be used up to 3'
-        ' times (corresponding to WARNING, ERROR, and CRITICAL logging'
-        ' levels).'
-    ),
-)  # type: Callable[..., Option]
-
-progress_bar = partial(
-    Option,
-    '--progress-bar',
-    dest='progress_bar',
-    type='choice',
-    choices=list(BAR_TYPES.keys()),
-    default='on',
-    help=(
-        'Specify type of progress to be displayed [' +
-        '|'.join(BAR_TYPES.keys()) + '] (default: %default)'
-    ),
-)  # type: Callable[..., Option]
-
-log = partial(
-    Option,
-    "--log", "--log-file", "--local-log",
-    dest="log",
-    metavar="path",
-    help="Path to a verbose appending log."
-)  # type: Callable[..., Option]
-
-no_input = partial(
-    Option,
-    # Don't ask for input
-    '--no-input',
-    dest='no_input',
-    action='store_true',
-    default=False,
-    help=SUPPRESS_HELP
-)  # type: Callable[..., Option]
-
-proxy = partial(
-    Option,
-    '--proxy',
-    dest='proxy',
-    type='str',
-    default='',
-    help="Specify a proxy in the form [user:passwd@]proxy.server:port."
-)  # type: Callable[..., Option]
-
-retries = partial(
-    Option,
-    '--retries',
-    dest='retries',
-    type='int',
-    default=5,
-    help="Maximum number of retries each connection should attempt "
-         "(default %default times).",
-)  # type: Callable[..., Option]
-
-timeout = partial(
-    Option,
-    '--timeout', '--default-timeout',
-    metavar='sec',
-    dest='timeout',
-    type='float',
-    default=15,
-    help='Set the socket timeout (default %default seconds).',
-)  # type: Callable[..., Option]
-
-skip_requirements_regex = partial(
-    Option,
-    # A regex to be used to skip requirements
-    '--skip-requirements-regex',
-    dest='skip_requirements_regex',
-    type='str',
-    default='',
-    help=SUPPRESS_HELP,
-)  # type: Callable[..., Option]
-
-
-def exists_action():
-    # type: () -> Option
-    return Option(
-        # Option when path already exist
-        '--exists-action',
-        dest='exists_action',
-        type='choice',
-        choices=['s', 'i', 'w', 'b', 'a'],
-        default=[],
-        action='append',
-        metavar='action',
-        help="Default action when a path already exists: "
-             "(s)witch, (i)gnore, (w)ipe, (b)ackup, (a)bort).",
-    )
-
-
-cert = partial(
-    Option,
-    '--cert',
-    dest='cert',
-    type='str',
-    metavar='path',
-    help="Path to alternate CA bundle.",
-)  # type: Callable[..., Option]
-
-client_cert = partial(
-    Option,
-    '--client-cert',
-    dest='client_cert',
-    type='str',
-    default=None,
-    metavar='path',
-    help="Path to SSL client certificate, a single file containing the "
-         "private key and the certificate in PEM format.",
-)  # type: Callable[..., Option]
-
-index_url = partial(
-    Option,
-    '-i', '--index-url', '--pypi-url',
-    dest='index_url',
-    metavar='URL',
-    default=PyPI.simple_url,
-    help="Base URL of Python Package Index (default %default). "
-         "This should point to a repository compliant with PEP 503 "
-         "(the simple repository API) or a local directory laid out "
-         "in the same format.",
-)  # type: Callable[..., Option]
-
-
-def extra_index_url():
-    return Option(
-        '--extra-index-url',
-        dest='extra_index_urls',
-        metavar='URL',
-        action='append',
-        default=[],
-        help="Extra URLs of package indexes to use in addition to "
-             "--index-url. Should follow the same rules as "
-             "--index-url.",
-    )
-
-
-no_index = partial(
-    Option,
-    '--no-index',
-    dest='no_index',
-    action='store_true',
-    default=False,
-    help='Ignore package index (only looking at --find-links URLs instead).',
-)  # type: Callable[..., Option]
-
-
-def find_links():
-    # type: () -> Option
-    return Option(
-        '-f', '--find-links',
-        dest='find_links',
-        action='append',
-        default=[],
-        metavar='url',
-        help="If a url or path to an html file, then parse for links to "
-             "archives. If a local path or file:// url that's a directory, "
-             "then look for archives in the directory listing.",
-    )
-
-
-def trusted_host():
-    # type: () -> Option
-    return Option(
-        "--trusted-host",
-        dest="trusted_hosts",
-        action="append",
-        metavar="HOSTNAME",
-        default=[],
-        help="Mark this host as trusted, even though it does not have valid "
-             "or any HTTPS.",
-    )
-
-
-def constraints():
-    # type: () -> Option
-    return Option(
-        '-c', '--constraint',
-        dest='constraints',
-        action='append',
-        default=[],
-        metavar='file',
-        help='Constrain versions using the given constraints file. '
-        'This option can be used multiple times.'
-    )
-
-
-def requirements():
-    # type: () -> Option
-    return Option(
-        '-r', '--requirement',
-        dest='requirements',
-        action='append',
-        default=[],
-        metavar='file',
-        help='Install from the given requirements file. '
-        'This option can be used multiple times.'
-    )
-
-
-def editable():
-    # type: () -> Option
-    return Option(
-        '-e', '--editable',
-        dest='editables',
-        action='append',
-        default=[],
-        metavar='path/url',
-        help=('Install a project in editable mode (i.e. setuptools '
-              '"develop mode") from a local project path or a VCS url.'),
-    )
-
-
-src = partial(
-    Option,
-    '--src', '--source', '--source-dir', '--source-directory',
-    dest='src_dir',
-    metavar='dir',
-    default=src_prefix,
-    help='Directory to check out editable projects into. '
-    'The default in a virtualenv is "<venv path>/src". '
-    'The default for global installs is "<current dir>/src".'
-)  # type: Callable[..., Option]
-
-
-def _get_format_control(values, option):
-    # type: (Values, Option) -> Any
-    """Get a format_control object."""
-    return getattr(values, option.dest)
-
-
-def _handle_no_binary(option, opt_str, value, parser):
-    # type: (Option, str, str, OptionParser) -> None
-    existing = _get_format_control(parser.values, option)
-    FormatControl.handle_mutual_excludes(
-        value, existing.no_binary, existing.only_binary,
-    )
-
-
-def _handle_only_binary(option, opt_str, value, parser):
-    # type: (Option, str, str, OptionParser) -> None
-    existing = _get_format_control(parser.values, option)
-    FormatControl.handle_mutual_excludes(
-        value, existing.only_binary, existing.no_binary,
-    )
-
-
-def no_binary():
-    # type: () -> Option
-    format_control = FormatControl(set(), set())
-    return Option(
-        "--no-binary", dest="format_control", action="callback",
-        callback=_handle_no_binary, type="str",
-        default=format_control,
-        help="Do not use binary packages. Can be supplied multiple times, and "
-             "each time adds to the existing value. Accepts either :all: to "
-             "disable all binary packages, :none: to empty the set, or one or "
-             "more package names with commas between them. Note that some "
-             "packages are tricky to compile and may fail to install when "
-             "this option is used on them.",
-    )
-
-
-def only_binary():
-    # type: () -> Option
-    format_control = FormatControl(set(), set())
-    return Option(
-        "--only-binary", dest="format_control", action="callback",
-        callback=_handle_only_binary, type="str",
-        default=format_control,
-        help="Do not use source packages. Can be supplied multiple times, and "
-             "each time adds to the existing value. Accepts either :all: to "
-             "disable all source packages, :none: to empty the set, or one or "
-             "more package names with commas between them. Packages without "
-             "binary distributions will fail to install when this option is "
-             "used on them.",
-    )
-
-
-platform = partial(
-    Option,
-    '--platform',
-    dest='platform',
-    metavar='platform',
-    default=None,
-    help=("Only use wheels compatible with <platform>. "
-          "Defaults to the platform of the running system."),
-)  # type: Callable[..., Option]
-
-
-python_version = partial(
-    Option,
-    '--python-version',
-    dest='python_version',
-    metavar='python_version',
-    default=None,
-    help=("Only use wheels compatible with Python "
-          "interpreter version <version>. If not specified, then the "
-          "current system interpreter minor version is used. A major "
-          "version (e.g. '2') can be specified to match all "
-          "minor revs of that major version.  A minor version "
-          "(e.g. '34') can also be specified."),
-)  # type: Callable[..., Option]
-
-
-implementation = partial(
-    Option,
-    '--implementation',
-    dest='implementation',
-    metavar='implementation',
-    default=None,
-    help=("Only use wheels compatible with Python "
-          "implementation <implementation>, e.g. 'pp', 'jy', 'cp', "
-          " or 'ip'. If not specified, then the current "
-          "interpreter implementation is used.  Use 'py' to force "
-          "implementation-agnostic wheels."),
-)  # type: Callable[..., Option]
-
-
-abi = partial(
-    Option,
-    '--abi',
-    dest='abi',
-    metavar='abi',
-    default=None,
-    help=("Only use wheels compatible with Python "
-          "abi <abi>, e.g. 'pypy_41'.  If not specified, then the "
-          "current interpreter abi tag is used.  Generally "
-          "you will need to specify --implementation, "
-          "--platform, and --python-version when using "
-          "this option."),
-)  # type: Callable[..., Option]
-
-
-def prefer_binary():
-    # type: () -> Option
-    return Option(
-        "--prefer-binary",
-        dest="prefer_binary",
-        action="store_true",
-        default=False,
-        help="Prefer older binary packages over newer source packages."
-    )
-
-
-cache_dir = partial(
-    Option,
-    "--cache-dir",
-    dest="cache_dir",
-    default=USER_CACHE_DIR,
-    metavar="dir",
-    help="Store the cache data in <dir>."
-)  # type: Callable[..., Option]
-
-
-def no_cache_dir_callback(option, opt, value, parser):
-    """
-    Process a value provided for the --no-cache-dir option.
-
-    This is an optparse.Option callback for the --no-cache-dir option.
-    """
-    # The value argument will be None if --no-cache-dir is passed via the
-    # command-line, since the option doesn't accept arguments.  However,
-    # the value can be non-None if the option is triggered e.g. by an
-    # environment variable, like PIP_NO_CACHE_DIR=true.
-    if value is not None:
-        # Then parse the string value to get argument error-checking.
-        try:
-            strtobool(value)
-        except ValueError as exc:
-            raise_option_error(parser, option=option, msg=str(exc))
-
-    # Originally, setting PIP_NO_CACHE_DIR to a value that strtobool()
-    # converted to 0 (like "false" or "no") caused cache_dir to be disabled
-    # rather than enabled (logic would say the latter).  Thus, we disable
-    # the cache directory not just on values that parse to True, but (for
-    # backwards compatibility reasons) also on values that parse to False.
-    # In other words, always set it to False if the option is provided in
-    # some (valid) form.
-    parser.values.cache_dir = False
-
-
-no_cache = partial(
-    Option,
-    "--no-cache-dir",
-    dest="cache_dir",
-    action="callback",
-    callback=no_cache_dir_callback,
-    help="Disable the cache.",
-)  # type: Callable[..., Option]
-
-no_deps = partial(
-    Option,
-    '--no-deps', '--no-dependencies',
-    dest='ignore_dependencies',
-    action='store_true',
-    default=False,
-    help="Don't install package dependencies.",
-)  # type: Callable[..., Option]
-
-build_dir = partial(
-    Option,
-    '-b', '--build', '--build-dir', '--build-directory',
-    dest='build_dir',
-    metavar='dir',
-    help='Directory to unpack packages into and build in. Note that '
-         'an initial build still takes place in a temporary directory. '
-         'The location of temporary directories can be controlled by setting '
-         'the TMPDIR environment variable (TEMP on Windows) appropriately. '
-         'When passed, build directories are not cleaned in case of failures.'
-)  # type: Callable[..., Option]
-
-ignore_requires_python = partial(
-    Option,
-    '--ignore-requires-python',
-    dest='ignore_requires_python',
-    action='store_true',
-    help='Ignore the Requires-Python information.'
-)  # type: Callable[..., Option]
-
-no_build_isolation = partial(
-    Option,
-    '--no-build-isolation',
-    dest='build_isolation',
-    action='store_false',
-    default=True,
-    help='Disable isolation when building a modern source distribution. '
-         'Build dependencies specified by PEP 518 must be already installed '
-         'if this option is used.'
-)  # type: Callable[..., Option]
-
-
-def no_use_pep517_callback(option, opt, value, parser):
-    """
-    Process a value provided for the --no-use-pep517 option.
-
-    This is an optparse.Option callback for the no_use_pep517 option.
-    """
-    # Since --no-use-pep517 doesn't accept arguments, the value argument
-    # will be None if --no-use-pep517 is passed via the command-line.
-    # However, the value can be non-None if the option is triggered e.g.
-    # by an environment variable, for example "PIP_NO_USE_PEP517=true".
-    if value is not None:
-        msg = """A value was passed for --no-use-pep517,
-        probably using either the PIP_NO_USE_PEP517 environment variable
-        or the "no-use-pep517" config file option. Use an appropriate value
-        of the PIP_USE_PEP517 environment variable or the "use-pep517"
-        config file option instead.
-        """
-        raise_option_error(parser, option=option, msg=msg)
-
-    # Otherwise, --no-use-pep517 was passed via the command-line.
-    parser.values.use_pep517 = False
-
-
-use_pep517 = partial(
-    Option,
-    '--use-pep517',
-    dest='use_pep517',
-    action='store_true',
-    default=None,
-    help='Use PEP 517 for building source distributions '
-         '(use --no-use-pep517 to force legacy behaviour).'
-)  # type: Any
-
-no_use_pep517 = partial(
-    Option,
-    '--no-use-pep517',
-    dest='use_pep517',
-    action='callback',
-    callback=no_use_pep517_callback,
-    default=None,
-    help=SUPPRESS_HELP
-)  # type: Any
-
-install_options = partial(
-    Option,
-    '--install-option',
-    dest='install_options',
-    action='append',
-    metavar='options',
-    help="Extra arguments to be supplied to the setup.py install "
-         "command (use like --install-option=\"--install-scripts=/usr/local/"
-         "bin\"). Use multiple --install-option options to pass multiple "
-         "options to setup.py install. If you are using an option with a "
-         "directory path, be sure to use absolute path.",
-)  # type: Callable[..., Option]
-
-global_options = partial(
-    Option,
-    '--global-option',
-    dest='global_options',
-    action='append',
-    metavar='options',
-    help="Extra global options to be supplied to the setup.py "
-         "call before the install command.",
-)  # type: Callable[..., Option]
-
-no_clean = partial(
-    Option,
-    '--no-clean',
-    action='store_true',
-    default=False,
-    help="Don't clean up build directories."
-)  # type: Callable[..., Option]
-
-pre = partial(
-    Option,
-    '--pre',
-    action='store_true',
-    default=False,
-    help="Include pre-release and development versions. By default, "
-         "pip only finds stable versions.",
-)  # type: Callable[..., Option]
-
-disable_pip_version_check = partial(
-    Option,
-    "--disable-pip-version-check",
-    dest="disable_pip_version_check",
-    action="store_true",
-    default=False,
-    help="Don't periodically check PyPI to determine whether a new version "
-         "of pip is available for download. Implied with --no-index.",
-)  # type: Callable[..., Option]
-
-
-# Deprecated, Remove later
-always_unzip = partial(
-    Option,
-    '-Z', '--always-unzip',
-    dest='always_unzip',
-    action='store_true',
-    help=SUPPRESS_HELP,
-)  # type: Callable[..., Option]
-
-
-def _merge_hash(option, opt_str, value, parser):
-    # type: (Option, str, str, OptionParser) -> None
-    """Given a value spelled "algo:digest", append the digest to a list
-    pointed to in a dict by the algo name."""
-    if not parser.values.hashes:
-        parser.values.hashes = {}  # type: ignore
-    try:
-        algo, digest = value.split(':', 1)
-    except ValueError:
-        parser.error('Arguments to %s must be a hash name '
-                     'followed by a value, like --hash=sha256:abcde...' %
-                     opt_str)
-    if algo not in STRONG_HASHES:
-        parser.error('Allowed hash algorithms for %s are %s.' %
-                     (opt_str, ', '.join(STRONG_HASHES)))
-    parser.values.hashes.setdefault(algo, []).append(digest)
-
-
-hash = partial(
-    Option,
-    '--hash',
-    # Hash values eventually end up in InstallRequirement.hashes due to
-    # __dict__ copying in process_line().
-    dest='hashes',
-    action='callback',
-    callback=_merge_hash,
-    type='string',
-    help="Verify that the package's archive matches this "
-         'hash before installing. Example: --hash=sha256:abcdef...',
-)  # type: Callable[..., Option]
-
-
-require_hashes = partial(
-    Option,
-    '--require-hashes',
-    dest='require_hashes',
-    action='store_true',
-    default=False,
-    help='Require a hash to check each requirement against, for '
-         'repeatable installs. This option is implied when any package in a '
-         'requirements file has a --hash option.',
-)  # type: Callable[..., Option]
-
-
-##########
-# groups #
-##########
-
-general_group = {
-    'name': 'General Options',
-    'options': [
-        help_,
-        isolated_mode,
-        require_virtualenv,
-        verbose,
-        version,
-        quiet,
-        log,
-        no_input,
-        proxy,
-        retries,
-        timeout,
-        skip_requirements_regex,
-        exists_action,
-        trusted_host,
-        cert,
-        client_cert,
-        cache_dir,
-        no_cache,
-        disable_pip_version_check,
-        no_color,
-    ]
-}  # type: Dict[str, Any]
-
-index_group = {
-    'name': 'Package Index Options',
-    'options': [
-        index_url,
-        extra_index_url,
-        no_index,
-        find_links,
-    ]
-}  # type: Dict[str, Any]
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/main_parser.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/main_parser.py
deleted file mode 100644
index b17c749..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/main_parser.py
+++ /dev/null
@@ -1,104 +0,0 @@
-"""A single place for constructing and exposing the main parser
-"""
-
-import os
-import sys
-
-from pip import __version__
-from pip._internal.cli import cmdoptions
-from pip._internal.cli.parser import (
-    ConfigOptionParser, UpdatingDefaultsHelpFormatter,
-)
-from pip._internal.commands import (
-    commands_dict, get_similar_commands, get_summaries,
-)
-from pip._internal.exceptions import CommandError
-from pip._internal.utils.misc import get_prog
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Tuple, List  # noqa: F401
-
-
-__all__ = ["create_main_parser", "parse_command"]
-
-
-def create_main_parser():
-    # type: () -> ConfigOptionParser
-    """Creates and returns the main parser for pip's CLI
-    """
-
-    parser_kw = {
-        'usage': '\n%prog <command> [options]',
-        'add_help_option': False,
-        'formatter': UpdatingDefaultsHelpFormatter(),
-        'name': 'global',
-        'prog': get_prog(),
-    }
-
-    parser = ConfigOptionParser(**parser_kw)
-    parser.disable_interspersed_args()
-
-    pip_pkg_dir = os.path.abspath(os.path.join(
-        os.path.dirname(__file__), "..", "..",
-    ))
-    parser.version = 'pip %s from %s (python %s)' % (
-        __version__, pip_pkg_dir, sys.version[:3],
-    )
-
-    # add the general options
-    gen_opts = cmdoptions.make_option_group(cmdoptions.general_group, parser)
-    parser.add_option_group(gen_opts)
-
-    # so the help formatter knows
-    parser.main = True  # type: ignore
-
-    # create command listing for description
-    command_summaries = get_summaries()
-    description = [''] + ['%-27s %s' % (i, j) for i, j in command_summaries]
-    parser.description = '\n'.join(description)
-
-    return parser
-
-
-def parse_command(args):
-    # type: (List[str]) -> Tuple[str, List[str]]
-    parser = create_main_parser()
-
-    # Note: parser calls disable_interspersed_args(), so the result of this
-    # call is to split the initial args into the general options before the
-    # subcommand and everything else.
-    # For example:
-    #  args: ['--timeout=5', 'install', '--user', 'INITools']
-    #  general_options: ['--timeout==5']
-    #  args_else: ['install', '--user', 'INITools']
-    general_options, args_else = parser.parse_args(args)
-
-    # --version
-    if general_options.version:
-        sys.stdout.write(parser.version)  # type: ignore
-        sys.stdout.write(os.linesep)
-        sys.exit()
-
-    # pip || pip help -> print_help()
-    if not args_else or (args_else[0] == 'help' and len(args_else) == 1):
-        parser.print_help()
-        sys.exit()
-
-    # the subcommand name
-    cmd_name = args_else[0]
-
-    if cmd_name not in commands_dict:
-        guess = get_similar_commands(cmd_name)
-
-        msg = ['unknown command "%s"' % cmd_name]
-        if guess:
-            msg.append('maybe you meant "%s"' % guess)
-
-        raise CommandError(' - '.join(msg))
-
-    # all the args without the subcommand
-    cmd_args = args[:]
-    cmd_args.remove(cmd_name)
-
-    return cmd_name, cmd_args
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/parser.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/parser.py
deleted file mode 100644
index e1eaac4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/parser.py
+++ /dev/null
@@ -1,261 +0,0 @@
-"""Base option parser setup"""
-from __future__ import absolute_import
-
-import logging
-import optparse
-import sys
-import textwrap
-from distutils.util import strtobool
-
-from pip._vendor.six import string_types
-
-from pip._internal.cli.status_codes import UNKNOWN_ERROR
-from pip._internal.configuration import Configuration, ConfigurationError
-from pip._internal.utils.compat import get_terminal_size
-
-logger = logging.getLogger(__name__)
-
-
-class PrettyHelpFormatter(optparse.IndentedHelpFormatter):
-    """A prettier/less verbose help formatter for optparse."""
-
-    def __init__(self, *args, **kwargs):
-        # help position must be aligned with __init__.parseopts.description
-        kwargs['max_help_position'] = 30
-        kwargs['indent_increment'] = 1
-        kwargs['width'] = get_terminal_size()[0] - 2
-        optparse.IndentedHelpFormatter.__init__(self, *args, **kwargs)
-
-    def format_option_strings(self, option):
-        return self._format_option_strings(option, ' <%s>', ', ')
-
-    def _format_option_strings(self, option, mvarfmt=' <%s>', optsep=', '):
-        """
-        Return a comma-separated list of option strings and metavars.
-
-        :param option:  tuple of (short opt, long opt), e.g: ('-f', '--format')
-        :param mvarfmt: metavar format string - evaluated as mvarfmt % metavar
-        :param optsep:  separator
-        """
-        opts = []
-
-        if option._short_opts:
-            opts.append(option._short_opts[0])
-        if option._long_opts:
-            opts.append(option._long_opts[0])
-        if len(opts) > 1:
-            opts.insert(1, optsep)
-
-        if option.takes_value():
-            metavar = option.metavar or option.dest.lower()
-            opts.append(mvarfmt % metavar.lower())
-
-        return ''.join(opts)
-
-    def format_heading(self, heading):
-        if heading == 'Options':
-            return ''
-        return heading + ':\n'
-
-    def format_usage(self, usage):
-        """
-        Ensure there is only one newline between usage and the first heading
-        if there is no description.
-        """
-        msg = '\nUsage: %s\n' % self.indent_lines(textwrap.dedent(usage), "  ")
-        return msg
-
-    def format_description(self, description):
-        # leave full control over description to us
-        if description:
-            if hasattr(self.parser, 'main'):
-                label = 'Commands'
-            else:
-                label = 'Description'
-            # some doc strings have initial newlines, some don't
-            description = description.lstrip('\n')
-            # some doc strings have final newlines and spaces, some don't
-            description = description.rstrip()
-            # dedent, then reindent
-            description = self.indent_lines(textwrap.dedent(description), "  ")
-            description = '%s:\n%s\n' % (label, description)
-            return description
-        else:
-            return ''
-
-    def format_epilog(self, epilog):
-        # leave full control over epilog to us
-        if epilog:
-            return epilog
-        else:
-            return ''
-
-    def indent_lines(self, text, indent):
-        new_lines = [indent + line for line in text.split('\n')]
-        return "\n".join(new_lines)
-
-
-class UpdatingDefaultsHelpFormatter(PrettyHelpFormatter):
-    """Custom help formatter for use in ConfigOptionParser.
-
-    This is updates the defaults before expanding them, allowing
-    them to show up correctly in the help listing.
-    """
-
-    def expand_default(self, option):
-        if self.parser is not None:
-            self.parser._update_defaults(self.parser.defaults)
-        return optparse.IndentedHelpFormatter.expand_default(self, option)
-
-
-class CustomOptionParser(optparse.OptionParser):
-
-    def insert_option_group(self, idx, *args, **kwargs):
-        """Insert an OptionGroup at a given position."""
-        group = self.add_option_group(*args, **kwargs)
-
-        self.option_groups.pop()
-        self.option_groups.insert(idx, group)
-
-        return group
-
-    @property
-    def option_list_all(self):
-        """Get a list of all options, including those in option groups."""
-        res = self.option_list[:]
-        for i in self.option_groups:
-            res.extend(i.option_list)
-
-        return res
-
-
-class ConfigOptionParser(CustomOptionParser):
-    """Custom option parser which updates its defaults by checking the
-    configuration files and environmental variables"""
-
-    def __init__(self, *args, **kwargs):
-        self.name = kwargs.pop('name')
-
-        isolated = kwargs.pop("isolated", False)
-        self.config = Configuration(isolated)
-
-        assert self.name
-        optparse.OptionParser.__init__(self, *args, **kwargs)
-
-    def check_default(self, option, key, val):
-        try:
-            return option.check_value(key, val)
-        except optparse.OptionValueError as exc:
-            print("An error occurred during configuration: %s" % exc)
-            sys.exit(3)
-
-    def _get_ordered_configuration_items(self):
-        # Configuration gives keys in an unordered manner. Order them.
-        override_order = ["global", self.name, ":env:"]
-
-        # Pool the options into different groups
-        section_items = {name: [] for name in override_order}
-        for section_key, val in self.config.items():
-            # ignore empty values
-            if not val:
-                logger.debug(
-                    "Ignoring configuration key '%s' as it's value is empty.",
-                    section_key
-                )
-                continue
-
-            section, key = section_key.split(".", 1)
-            if section in override_order:
-                section_items[section].append((key, val))
-
-        # Yield each group in their override order
-        for section in override_order:
-            for key, val in section_items[section]:
-                yield key, val
-
-    def _update_defaults(self, defaults):
-        """Updates the given defaults with values from the config files and
-        the environ. Does a little special handling for certain types of
-        options (lists)."""
-
-        # Accumulate complex default state.
-        self.values = optparse.Values(self.defaults)
-        late_eval = set()
-        # Then set the options with those values
-        for key, val in self._get_ordered_configuration_items():
-            # '--' because configuration supports only long names
-            option = self.get_option('--' + key)
-
-            # Ignore options not present in this parser. E.g. non-globals put
-            # in [global] by users that want them to apply to all applicable
-            # commands.
-            if option is None:
-                continue
-
-            if option.action in ('store_true', 'store_false', 'count'):
-                try:
-                    val = strtobool(val)
-                except ValueError:
-                    error_msg = invalid_config_error_message(
-                        option.action, key, val
-                    )
-                    self.error(error_msg)
-
-            elif option.action == 'append':
-                val = val.split()
-                val = [self.check_default(option, key, v) for v in val]
-            elif option.action == 'callback':
-                late_eval.add(option.dest)
-                opt_str = option.get_opt_string()
-                val = option.convert_value(opt_str, val)
-                # From take_action
-                args = option.callback_args or ()
-                kwargs = option.callback_kwargs or {}
-                option.callback(option, opt_str, val, self, *args, **kwargs)
-            else:
-                val = self.check_default(option, key, val)
-
-            defaults[option.dest] = val
-
-        for key in late_eval:
-            defaults[key] = getattr(self.values, key)
-        self.values = None
-        return defaults
-
-    def get_default_values(self):
-        """Overriding to make updating the defaults after instantiation of
-        the option parser possible, _update_defaults() does the dirty work."""
-        if not self.process_default_values:
-            # Old, pre-Optik 1.5 behaviour.
-            return optparse.Values(self.defaults)
-
-        # Load the configuration, or error out in case of an error
-        try:
-            self.config.load()
-        except ConfigurationError as err:
-            self.exit(UNKNOWN_ERROR, str(err))
-
-        defaults = self._update_defaults(self.defaults.copy())  # ours
-        for option in self._get_all_options():
-            default = defaults.get(option.dest)
-            if isinstance(default, string_types):
-                opt_str = option.get_opt_string()
-                defaults[option.dest] = option.check_value(opt_str, default)
-        return optparse.Values(defaults)
-
-    def error(self, msg):
-        self.print_usage(sys.stderr)
-        self.exit(UNKNOWN_ERROR, "%s\n" % msg)
-
-
-def invalid_config_error_message(action, key, val):
-    """Returns a better error message when invalid configuration option
-    is provided."""
-    if action in ('store_true', 'store_false'):
-        return ("{0} is not a valid value for {1} option, "
-                "please specify a boolean value like yes/no, "
-                "true/false or 1/0 instead.").format(val, key)
-
-    return ("{0} is not a valid value for {1} option, "
-            "please specify a numerical value like 1/0 "
-            "instead.").format(val, key)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/status_codes.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/status_codes.py
deleted file mode 100644
index 275360a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/cli/status_codes.py
+++ /dev/null
@@ -1,8 +0,0 @@
-from __future__ import absolute_import
-
-SUCCESS = 0
-ERROR = 1
-UNKNOWN_ERROR = 2
-VIRTUALENV_NOT_FOUND = 3
-PREVIOUS_BUILD_DIR_ERROR = 4
-NO_MATCHES_FOUND = 23
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__init__.py
deleted file mode 100644
index c7d1da3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__init__.py
+++ /dev/null
@@ -1,79 +0,0 @@
-"""
-Package containing all pip commands
-"""
-from __future__ import absolute_import
-
-from pip._internal.commands.completion import CompletionCommand
-from pip._internal.commands.configuration import ConfigurationCommand
-from pip._internal.commands.download import DownloadCommand
-from pip._internal.commands.freeze import FreezeCommand
-from pip._internal.commands.hash import HashCommand
-from pip._internal.commands.help import HelpCommand
-from pip._internal.commands.list import ListCommand
-from pip._internal.commands.check import CheckCommand
-from pip._internal.commands.search import SearchCommand
-from pip._internal.commands.show import ShowCommand
-from pip._internal.commands.install import InstallCommand
-from pip._internal.commands.uninstall import UninstallCommand
-from pip._internal.commands.wheel import WheelCommand
-
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import List, Type  # noqa: F401
-    from pip._internal.cli.base_command import Command  # noqa: F401
-
-commands_order = [
-    InstallCommand,
-    DownloadCommand,
-    UninstallCommand,
-    FreezeCommand,
-    ListCommand,
-    ShowCommand,
-    CheckCommand,
-    ConfigurationCommand,
-    SearchCommand,
-    WheelCommand,
-    HashCommand,
-    CompletionCommand,
-    HelpCommand,
-]  # type: List[Type[Command]]
-
-commands_dict = {c.name: c for c in commands_order}
-
-
-def get_summaries(ordered=True):
-    """Yields sorted (command name, command summary) tuples."""
-
-    if ordered:
-        cmditems = _sort_commands(commands_dict, commands_order)
-    else:
-        cmditems = commands_dict.items()
-
-    for name, command_class in cmditems:
-        yield (name, command_class.summary)
-
-
-def get_similar_commands(name):
-    """Command name auto-correct."""
-    from difflib import get_close_matches
-
-    name = name.lower()
-
-    close_commands = get_close_matches(name, commands_dict.keys())
-
-    if close_commands:
-        return close_commands[0]
-    else:
-        return False
-
-
-def _sort_commands(cmddict, order):
-    def keyfn(key):
-        try:
-            return order.index(key[1])
-        except ValueError:
-            # unordered items should come last
-            return 0xff
-
-    return sorted(cmddict.items(), key=keyfn)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 81f2d6a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/check.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/check.cpython-37.pyc
deleted file mode 100644
index 4cf332a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/check.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/completion.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/completion.cpython-37.pyc
deleted file mode 100644
index 2f10e9a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/completion.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/configuration.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/configuration.cpython-37.pyc
deleted file mode 100644
index b33e6c9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/configuration.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/download.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/download.cpython-37.pyc
deleted file mode 100644
index 8c02ceb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/download.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/freeze.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/freeze.cpython-37.pyc
deleted file mode 100644
index 351ab9f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/freeze.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/hash.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/hash.cpython-37.pyc
deleted file mode 100644
index 2b6183f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/hash.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/help.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/help.cpython-37.pyc
deleted file mode 100644
index 0eaefaf..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/help.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/install.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/install.cpython-37.pyc
deleted file mode 100644
index 4587dd5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/install.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/list.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/list.cpython-37.pyc
deleted file mode 100644
index 219febe..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/list.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/search.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/search.cpython-37.pyc
deleted file mode 100644
index 7809bf0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/search.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/show.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/show.cpython-37.pyc
deleted file mode 100644
index bb07126..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/show.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/uninstall.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/uninstall.cpython-37.pyc
deleted file mode 100644
index b528ae4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/uninstall.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/wheel.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/wheel.cpython-37.pyc
deleted file mode 100644
index 8198357..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/__pycache__/wheel.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/check.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/check.py
deleted file mode 100644
index 801cecc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/check.py
+++ /dev/null
@@ -1,41 +0,0 @@
-import logging
-
-from pip._internal.cli.base_command import Command
-from pip._internal.operations.check import (
-    check_package_set, create_package_set_from_installed,
-)
-
-logger = logging.getLogger(__name__)
-
-
-class CheckCommand(Command):
-    """Verify installed packages have compatible dependencies."""
-    name = 'check'
-    usage = """
-      %prog [options]"""
-    summary = 'Verify installed packages have compatible dependencies.'
-
-    def run(self, options, args):
-        package_set, parsing_probs = create_package_set_from_installed()
-        missing, conflicting = check_package_set(package_set)
-
-        for project_name in missing:
-            version = package_set[project_name].version
-            for dependency in missing[project_name]:
-                logger.info(
-                    "%s %s requires %s, which is not installed.",
-                    project_name, version, dependency[0],
-                )
-
-        for project_name in conflicting:
-            version = package_set[project_name].version
-            for dep_name, dep_version, req in conflicting[project_name]:
-                logger.info(
-                    "%s %s has requirement %s, but you have %s %s.",
-                    project_name, version, req, dep_name, dep_version,
-                )
-
-        if missing or conflicting or parsing_probs:
-            return 1
-        else:
-            logger.info("No broken requirements found.")
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/completion.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/completion.py
deleted file mode 100644
index 2fcdd39..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/completion.py
+++ /dev/null
@@ -1,94 +0,0 @@
-from __future__ import absolute_import
-
-import sys
-import textwrap
-
-from pip._internal.cli.base_command import Command
-from pip._internal.utils.misc import get_prog
-
-BASE_COMPLETION = """
-# pip %(shell)s completion start%(script)s# pip %(shell)s completion end
-"""
-
-COMPLETION_SCRIPTS = {
-    'bash': """
-        _pip_completion()
-        {
-            COMPREPLY=( $( COMP_WORDS="${COMP_WORDS[*]}" \\
-                           COMP_CWORD=$COMP_CWORD \\
-                           PIP_AUTO_COMPLETE=1 $1 ) )
-        }
-        complete -o default -F _pip_completion %(prog)s
-    """,
-    'zsh': """
-        function _pip_completion {
-          local words cword
-          read -Ac words
-          read -cn cword
-          reply=( $( COMP_WORDS="$words[*]" \\
-                     COMP_CWORD=$(( cword-1 )) \\
-                     PIP_AUTO_COMPLETE=1 $words[1] ) )
-        }
-        compctl -K _pip_completion %(prog)s
-    """,
-    'fish': """
-        function __fish_complete_pip
-            set -lx COMP_WORDS (commandline -o) ""
-            set -lx COMP_CWORD ( \\
-                math (contains -i -- (commandline -t) $COMP_WORDS)-1 \\
-            )
-            set -lx PIP_AUTO_COMPLETE 1
-            string split \\  -- (eval $COMP_WORDS[1])
-        end
-        complete -fa "(__fish_complete_pip)" -c %(prog)s
-    """,
-}
-
-
-class CompletionCommand(Command):
-    """A helper command to be used for command completion."""
-    name = 'completion'
-    summary = 'A helper command used for command completion.'
-    ignore_require_venv = True
-
-    def __init__(self, *args, **kw):
-        super(CompletionCommand, self).__init__(*args, **kw)
-
-        cmd_opts = self.cmd_opts
-
-        cmd_opts.add_option(
-            '--bash', '-b',
-            action='store_const',
-            const='bash',
-            dest='shell',
-            help='Emit completion code for bash')
-        cmd_opts.add_option(
-            '--zsh', '-z',
-            action='store_const',
-            const='zsh',
-            dest='shell',
-            help='Emit completion code for zsh')
-        cmd_opts.add_option(
-            '--fish', '-f',
-            action='store_const',
-            const='fish',
-            dest='shell',
-            help='Emit completion code for fish')
-
-        self.parser.insert_option_group(0, cmd_opts)
-
-    def run(self, options, args):
-        """Prints the completion code of the given shell"""
-        shells = COMPLETION_SCRIPTS.keys()
-        shell_options = ['--' + shell for shell in sorted(shells)]
-        if options.shell in shells:
-            script = textwrap.dedent(
-                COMPLETION_SCRIPTS.get(options.shell, '') % {
-                    'prog': get_prog(),
-                }
-            )
-            print(BASE_COMPLETION % {'script': script, 'shell': options.shell})
-        else:
-            sys.stderr.write(
-                'ERROR: You must pass %s\n' % ' or '.join(shell_options)
-            )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/configuration.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/configuration.py
deleted file mode 100644
index 826c08d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/configuration.py
+++ /dev/null
@@ -1,227 +0,0 @@
-import logging
-import os
-import subprocess
-
-from pip._internal.cli.base_command import Command
-from pip._internal.cli.status_codes import ERROR, SUCCESS
-from pip._internal.configuration import Configuration, kinds
-from pip._internal.exceptions import PipError
-from pip._internal.locations import venv_config_file
-from pip._internal.utils.misc import get_prog
-
-logger = logging.getLogger(__name__)
-
-
-class ConfigurationCommand(Command):
-    """Manage local and global configuration.
-
-        Subcommands:
-
-        list: List the active configuration (or from the file specified)
-        edit: Edit the configuration file in an editor
-        get: Get the value associated with name
-        set: Set the name=value
-        unset: Unset the value associated with name
-
-        If none of --user, --global and --venv are passed, a virtual
-        environment configuration file is used if one is active and the file
-        exists. Otherwise, all modifications happen on the to the user file by
-        default.
-    """
-
-    name = 'config'
-    usage = """
-        %prog [<file-option>] list
-        %prog [<file-option>] [--editor <editor-path>] edit
-
-        %prog [<file-option>] get name
-        %prog [<file-option>] set name value
-        %prog [<file-option>] unset name
-    """
-
-    summary = "Manage local and global configuration."
-
-    def __init__(self, *args, **kwargs):
-        super(ConfigurationCommand, self).__init__(*args, **kwargs)
-
-        self.configuration = None
-
-        self.cmd_opts.add_option(
-            '--editor',
-            dest='editor',
-            action='store',
-            default=None,
-            help=(
-                'Editor to use to edit the file. Uses VISUAL or EDITOR '
-                'environment variables if not provided.'
-            )
-        )
-
-        self.cmd_opts.add_option(
-            '--global',
-            dest='global_file',
-            action='store_true',
-            default=False,
-            help='Use the system-wide configuration file only'
-        )
-
-        self.cmd_opts.add_option(
-            '--user',
-            dest='user_file',
-            action='store_true',
-            default=False,
-            help='Use the user configuration file only'
-        )
-
-        self.cmd_opts.add_option(
-            '--venv',
-            dest='venv_file',
-            action='store_true',
-            default=False,
-            help='Use the virtualenv configuration file only'
-        )
-
-        self.parser.insert_option_group(0, self.cmd_opts)
-
-    def run(self, options, args):
-        handlers = {
-            "list": self.list_values,
-            "edit": self.open_in_editor,
-            "get": self.get_name,
-            "set": self.set_name_value,
-            "unset": self.unset_name
-        }
-
-        # Determine action
-        if not args or args[0] not in handlers:
-            logger.error("Need an action ({}) to perform.".format(
-                ", ".join(sorted(handlers)))
-            )
-            return ERROR
-
-        action = args[0]
-
-        # Determine which configuration files are to be loaded
-        #    Depends on whether the command is modifying.
-        try:
-            load_only = self._determine_file(
-                options, need_value=(action in ["get", "set", "unset", "edit"])
-            )
-        except PipError as e:
-            logger.error(e.args[0])
-            return ERROR
-
-        # Load a new configuration
-        self.configuration = Configuration(
-            isolated=options.isolated_mode, load_only=load_only
-        )
-        self.configuration.load()
-
-        # Error handling happens here, not in the action-handlers.
-        try:
-            handlers[action](options, args[1:])
-        except PipError as e:
-            logger.error(e.args[0])
-            return ERROR
-
-        return SUCCESS
-
-    def _determine_file(self, options, need_value):
-        file_options = {
-            kinds.USER: options.user_file,
-            kinds.GLOBAL: options.global_file,
-            kinds.VENV: options.venv_file
-        }
-
-        if sum(file_options.values()) == 0:
-            if not need_value:
-                return None
-            # Default to user, unless there's a virtualenv file.
-            elif os.path.exists(venv_config_file):
-                return kinds.VENV
-            else:
-                return kinds.USER
-        elif sum(file_options.values()) == 1:
-            # There's probably a better expression for this.
-            return [key for key in file_options if file_options[key]][0]
-
-        raise PipError(
-            "Need exactly one file to operate upon "
-            "(--user, --venv, --global) to perform."
-        )
-
-    def list_values(self, options, args):
-        self._get_n_args(args, "list", n=0)
-
-        for key, value in sorted(self.configuration.items()):
-            logger.info("%s=%r", key, value)
-
-    def get_name(self, options, args):
-        key = self._get_n_args(args, "get [name]", n=1)
-        value = self.configuration.get_value(key)
-
-        logger.info("%s", value)
-
-    def set_name_value(self, options, args):
-        key, value = self._get_n_args(args, "set [name] [value]", n=2)
-        self.configuration.set_value(key, value)
-
-        self._save_configuration()
-
-    def unset_name(self, options, args):
-        key = self._get_n_args(args, "unset [name]", n=1)
-        self.configuration.unset_value(key)
-
-        self._save_configuration()
-
-    def open_in_editor(self, options, args):
-        editor = self._determine_editor(options)
-
-        fname = self.configuration.get_file_to_edit()
-        if fname is None:
-            raise PipError("Could not determine appropriate file.")
-
-        try:
-            subprocess.check_call([editor, fname])
-        except subprocess.CalledProcessError as e:
-            raise PipError(
-                "Editor Subprocess exited with exit code {}"
-                .format(e.returncode)
-            )
-
-    def _get_n_args(self, args, example, n):
-        """Helper to make sure the command got the right number of arguments
-        """
-        if len(args) != n:
-            msg = (
-                'Got unexpected number of arguments, expected {}. '
-                '(example: "{} config {}")'
-            ).format(n, get_prog(), example)
-            raise PipError(msg)
-
-        if n == 1:
-            return args[0]
-        else:
-            return args
-
-    def _save_configuration(self):
-        # We successfully ran a modifying command. Need to save the
-        # configuration.
-        try:
-            self.configuration.save()
-        except Exception:
-            logger.error(
-                "Unable to save configuration. Please report this as a bug.",
-                exc_info=1
-            )
-            raise PipError("Internal Error.")
-
-    def _determine_editor(self, options):
-        if options.editor is not None:
-            return options.editor
-        elif "VISUAL" in os.environ:
-            return os.environ["VISUAL"]
-        elif "EDITOR" in os.environ:
-            return os.environ["EDITOR"]
-        else:
-            raise PipError("Could not determine editor to use.")
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/download.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/download.py
deleted file mode 100644
index a57e4bc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/download.py
+++ /dev/null
@@ -1,176 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import os
-
-from pip._internal.cli import cmdoptions
-from pip._internal.cli.base_command import RequirementCommand
-from pip._internal.operations.prepare import RequirementPreparer
-from pip._internal.req import RequirementSet
-from pip._internal.req.req_tracker import RequirementTracker
-from pip._internal.resolve import Resolver
-from pip._internal.utils.filesystem import check_path_owner
-from pip._internal.utils.misc import ensure_dir, normalize_path
-from pip._internal.utils.temp_dir import TempDirectory
-
-logger = logging.getLogger(__name__)
-
-
-class DownloadCommand(RequirementCommand):
-    """
-    Download packages from:
-
-    - PyPI (and other indexes) using requirement specifiers.
-    - VCS project urls.
-    - Local project directories.
-    - Local or remote source archives.
-
-    pip also supports downloading from "requirements files", which provide
-    an easy way to specify a whole environment to be downloaded.
-    """
-    name = 'download'
-
-    usage = """
-      %prog [options] <requirement specifier> [package-index-options] ...
-      %prog [options] -r <requirements file> [package-index-options] ...
-      %prog [options] <vcs project url> ...
-      %prog [options] <local project path> ...
-      %prog [options] <archive url/path> ..."""
-
-    summary = 'Download packages.'
-
-    def __init__(self, *args, **kw):
-        super(DownloadCommand, self).__init__(*args, **kw)
-
-        cmd_opts = self.cmd_opts
-
-        cmd_opts.add_option(cmdoptions.constraints())
-        cmd_opts.add_option(cmdoptions.requirements())
-        cmd_opts.add_option(cmdoptions.build_dir())
-        cmd_opts.add_option(cmdoptions.no_deps())
-        cmd_opts.add_option(cmdoptions.global_options())
-        cmd_opts.add_option(cmdoptions.no_binary())
-        cmd_opts.add_option(cmdoptions.only_binary())
-        cmd_opts.add_option(cmdoptions.prefer_binary())
-        cmd_opts.add_option(cmdoptions.src())
-        cmd_opts.add_option(cmdoptions.pre())
-        cmd_opts.add_option(cmdoptions.no_clean())
-        cmd_opts.add_option(cmdoptions.require_hashes())
-        cmd_opts.add_option(cmdoptions.progress_bar())
-        cmd_opts.add_option(cmdoptions.no_build_isolation())
-        cmd_opts.add_option(cmdoptions.use_pep517())
-        cmd_opts.add_option(cmdoptions.no_use_pep517())
-
-        cmd_opts.add_option(
-            '-d', '--dest', '--destination-dir', '--destination-directory',
-            dest='download_dir',
-            metavar='dir',
-            default=os.curdir,
-            help=("Download packages into <dir>."),
-        )
-
-        cmd_opts.add_option(cmdoptions.platform())
-        cmd_opts.add_option(cmdoptions.python_version())
-        cmd_opts.add_option(cmdoptions.implementation())
-        cmd_opts.add_option(cmdoptions.abi())
-
-        index_opts = cmdoptions.make_option_group(
-            cmdoptions.index_group,
-            self.parser,
-        )
-
-        self.parser.insert_option_group(0, index_opts)
-        self.parser.insert_option_group(0, cmd_opts)
-
-    def run(self, options, args):
-        options.ignore_installed = True
-        # editable doesn't really make sense for `pip download`, but the bowels
-        # of the RequirementSet code require that property.
-        options.editables = []
-
-        if options.python_version:
-            python_versions = [options.python_version]
-        else:
-            python_versions = None
-
-        cmdoptions.check_dist_restriction(options)
-
-        options.src_dir = os.path.abspath(options.src_dir)
-        options.download_dir = normalize_path(options.download_dir)
-
-        ensure_dir(options.download_dir)
-
-        with self._build_session(options) as session:
-            finder = self._build_package_finder(
-                options=options,
-                session=session,
-                platform=options.platform,
-                python_versions=python_versions,
-                abi=options.abi,
-                implementation=options.implementation,
-            )
-            build_delete = (not (options.no_clean or options.build_dir))
-            if options.cache_dir and not check_path_owner(options.cache_dir):
-                logger.warning(
-                    "The directory '%s' or its parent directory is not owned "
-                    "by the current user and caching wheels has been "
-                    "disabled. check the permissions and owner of that "
-                    "directory. If executing pip with sudo, you may want "
-                    "sudo's -H flag.",
-                    options.cache_dir,
-                )
-                options.cache_dir = None
-
-            with RequirementTracker() as req_tracker, TempDirectory(
-                options.build_dir, delete=build_delete, kind="download"
-            ) as directory:
-
-                requirement_set = RequirementSet(
-                    require_hashes=options.require_hashes,
-                )
-                self.populate_requirement_set(
-                    requirement_set,
-                    args,
-                    options,
-                    finder,
-                    session,
-                    self.name,
-                    None
-                )
-
-                preparer = RequirementPreparer(
-                    build_dir=directory.path,
-                    src_dir=options.src_dir,
-                    download_dir=options.download_dir,
-                    wheel_download_dir=None,
-                    progress_bar=options.progress_bar,
-                    build_isolation=options.build_isolation,
-                    req_tracker=req_tracker,
-                )
-
-                resolver = Resolver(
-                    preparer=preparer,
-                    finder=finder,
-                    session=session,
-                    wheel_cache=None,
-                    use_user_site=False,
-                    upgrade_strategy="to-satisfy-only",
-                    force_reinstall=False,
-                    ignore_dependencies=options.ignore_dependencies,
-                    ignore_requires_python=False,
-                    ignore_installed=True,
-                    isolated=options.isolated_mode,
-                )
-                resolver.resolve(requirement_set)
-
-                downloaded = ' '.join([
-                    req.name for req in requirement_set.successfully_downloaded
-                ])
-                if downloaded:
-                    logger.info('Successfully downloaded %s', downloaded)
-
-                # Clean up
-                if not options.no_clean:
-                    requirement_set.cleanup_files()
-
-        return requirement_set
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/freeze.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/freeze.py
deleted file mode 100644
index dc9c53a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/freeze.py
+++ /dev/null
@@ -1,96 +0,0 @@
-from __future__ import absolute_import
-
-import sys
-
-from pip._internal.cache import WheelCache
-from pip._internal.cli.base_command import Command
-from pip._internal.models.format_control import FormatControl
-from pip._internal.operations.freeze import freeze
-from pip._internal.utils.compat import stdlib_pkgs
-
-DEV_PKGS = {'pip', 'setuptools', 'distribute', 'wheel'}
-
-
-class FreezeCommand(Command):
-    """
-    Output installed packages in requirements format.
-
-    packages are listed in a case-insensitive sorted order.
-    """
-    name = 'freeze'
-    usage = """
-      %prog [options]"""
-    summary = 'Output installed packages in requirements format.'
-    log_streams = ("ext://sys.stderr", "ext://sys.stderr")
-
-    def __init__(self, *args, **kw):
-        super(FreezeCommand, self).__init__(*args, **kw)
-
-        self.cmd_opts.add_option(
-            '-r', '--requirement',
-            dest='requirements',
-            action='append',
-            default=[],
-            metavar='file',
-            help="Use the order in the given requirements file and its "
-                 "comments when generating output. This option can be "
-                 "used multiple times.")
-        self.cmd_opts.add_option(
-            '-f', '--find-links',
-            dest='find_links',
-            action='append',
-            default=[],
-            metavar='URL',
-            help='URL for finding packages, which will be added to the '
-                 'output.')
-        self.cmd_opts.add_option(
-            '-l', '--local',
-            dest='local',
-            action='store_true',
-            default=False,
-            help='If in a virtualenv that has global access, do not output '
-                 'globally-installed packages.')
-        self.cmd_opts.add_option(
-            '--user',
-            dest='user',
-            action='store_true',
-            default=False,
-            help='Only output packages installed in user-site.')
-        self.cmd_opts.add_option(
-            '--all',
-            dest='freeze_all',
-            action='store_true',
-            help='Do not skip these packages in the output:'
-                 ' %s' % ', '.join(DEV_PKGS))
-        self.cmd_opts.add_option(
-            '--exclude-editable',
-            dest='exclude_editable',
-            action='store_true',
-            help='Exclude editable package from output.')
-
-        self.parser.insert_option_group(0, self.cmd_opts)
-
-    def run(self, options, args):
-        format_control = FormatControl(set(), set())
-        wheel_cache = WheelCache(options.cache_dir, format_control)
-        skip = set(stdlib_pkgs)
-        if not options.freeze_all:
-            skip.update(DEV_PKGS)
-
-        freeze_kwargs = dict(
-            requirement=options.requirements,
-            find_links=options.find_links,
-            local_only=options.local,
-            user_only=options.user,
-            skip_regex=options.skip_requirements_regex,
-            isolated=options.isolated_mode,
-            wheel_cache=wheel_cache,
-            skip=skip,
-            exclude_editable=options.exclude_editable,
-        )
-
-        try:
-            for line in freeze(**freeze_kwargs):
-                sys.stdout.write(line + '\n')
-        finally:
-            wheel_cache.cleanup()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/hash.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/hash.py
deleted file mode 100644
index 423440e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/hash.py
+++ /dev/null
@@ -1,57 +0,0 @@
-from __future__ import absolute_import
-
-import hashlib
-import logging
-import sys
-
-from pip._internal.cli.base_command import Command
-from pip._internal.cli.status_codes import ERROR
-from pip._internal.utils.hashes import FAVORITE_HASH, STRONG_HASHES
-from pip._internal.utils.misc import read_chunks
-
-logger = logging.getLogger(__name__)
-
-
-class HashCommand(Command):
-    """
-    Compute a hash of a local package archive.
-
-    These can be used with --hash in a requirements file to do repeatable
-    installs.
-
-    """
-    name = 'hash'
-    usage = '%prog [options] <file> ...'
-    summary = 'Compute hashes of package archives.'
-    ignore_require_venv = True
-
-    def __init__(self, *args, **kw):
-        super(HashCommand, self).__init__(*args, **kw)
-        self.cmd_opts.add_option(
-            '-a', '--algorithm',
-            dest='algorithm',
-            choices=STRONG_HASHES,
-            action='store',
-            default=FAVORITE_HASH,
-            help='The hash algorithm to use: one of %s' %
-                 ', '.join(STRONG_HASHES))
-        self.parser.insert_option_group(0, self.cmd_opts)
-
-    def run(self, options, args):
-        if not args:
-            self.parser.print_usage(sys.stderr)
-            return ERROR
-
-        algorithm = options.algorithm
-        for path in args:
-            logger.info('%s:\n--hash=%s:%s',
-                        path, algorithm, _hash_of_file(path, algorithm))
-
-
-def _hash_of_file(path, algorithm):
-    """Return the hash digest of a file."""
-    with open(path, 'rb') as archive:
-        hash = hashlib.new(algorithm)
-        for chunk in read_chunks(archive):
-            hash.update(chunk)
-    return hash.hexdigest()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/help.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/help.py
deleted file mode 100644
index 49a81cb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/help.py
+++ /dev/null
@@ -1,37 +0,0 @@
-from __future__ import absolute_import
-
-from pip._internal.cli.base_command import Command
-from pip._internal.cli.status_codes import SUCCESS
-from pip._internal.exceptions import CommandError
-
-
-class HelpCommand(Command):
-    """Show help for commands"""
-    name = 'help'
-    usage = """
-      %prog <command>"""
-    summary = 'Show help for commands.'
-    ignore_require_venv = True
-
-    def run(self, options, args):
-        from pip._internal.commands import commands_dict, get_similar_commands
-
-        try:
-            # 'pip help' with no args is handled by pip.__init__.parseopt()
-            cmd_name = args[0]  # the command we need help for
-        except IndexError:
-            return SUCCESS
-
-        if cmd_name not in commands_dict:
-            guess = get_similar_commands(cmd_name)
-
-            msg = ['unknown command "%s"' % cmd_name]
-            if guess:
-                msg.append('maybe you meant "%s"' % guess)
-
-            raise CommandError(' - '.join(msg))
-
-        command = commands_dict[cmd_name]()
-        command.parser.print_help()
-
-        return SUCCESS
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/install.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/install.py
deleted file mode 100644
index 1c244d2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/install.py
+++ /dev/null
@@ -1,566 +0,0 @@
-from __future__ import absolute_import
-
-import errno
-import logging
-import operator
-import os
-import shutil
-from optparse import SUPPRESS_HELP
-
-from pip._vendor import pkg_resources
-
-from pip._internal.cache import WheelCache
-from pip._internal.cli import cmdoptions
-from pip._internal.cli.base_command import RequirementCommand
-from pip._internal.cli.status_codes import ERROR
-from pip._internal.exceptions import (
-    CommandError, InstallationError, PreviousBuildDirError,
-)
-from pip._internal.locations import distutils_scheme, virtualenv_no_global
-from pip._internal.operations.check import check_install_conflicts
-from pip._internal.operations.prepare import RequirementPreparer
-from pip._internal.req import RequirementSet, install_given_reqs
-from pip._internal.req.req_tracker import RequirementTracker
-from pip._internal.resolve import Resolver
-from pip._internal.utils.filesystem import check_path_owner
-from pip._internal.utils.misc import (
-    ensure_dir, get_installed_version,
-    protect_pip_from_modification_on_windows,
-)
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.wheel import WheelBuilder
-
-logger = logging.getLogger(__name__)
-
-
-class InstallCommand(RequirementCommand):
-    """
-    Install packages from:
-
-    - PyPI (and other indexes) using requirement specifiers.
-    - VCS project urls.
-    - Local project directories.
-    - Local or remote source archives.
-
-    pip also supports installing from "requirements files", which provide
-    an easy way to specify a whole environment to be installed.
-    """
-    name = 'install'
-
-    usage = """
-      %prog [options] <requirement specifier> [package-index-options] ...
-      %prog [options] -r <requirements file> [package-index-options] ...
-      %prog [options] [-e] <vcs project url> ...
-      %prog [options] [-e] <local project path> ...
-      %prog [options] <archive url/path> ..."""
-
-    summary = 'Install packages.'
-
-    def __init__(self, *args, **kw):
-        super(InstallCommand, self).__init__(*args, **kw)
-
-        cmd_opts = self.cmd_opts
-
-        cmd_opts.add_option(cmdoptions.requirements())
-        cmd_opts.add_option(cmdoptions.constraints())
-        cmd_opts.add_option(cmdoptions.no_deps())
-        cmd_opts.add_option(cmdoptions.pre())
-
-        cmd_opts.add_option(cmdoptions.editable())
-        cmd_opts.add_option(
-            '-t', '--target',
-            dest='target_dir',
-            metavar='dir',
-            default=None,
-            help='Install packages into <dir>. '
-                 'By default this will not replace existing files/folders in '
-                 '<dir>. Use --upgrade to replace existing packages in <dir> '
-                 'with new versions.'
-        )
-        cmd_opts.add_option(cmdoptions.platform())
-        cmd_opts.add_option(cmdoptions.python_version())
-        cmd_opts.add_option(cmdoptions.implementation())
-        cmd_opts.add_option(cmdoptions.abi())
-
-        cmd_opts.add_option(
-            '--user',
-            dest='use_user_site',
-            action='store_true',
-            help="Install to the Python user install directory for your "
-                 "platform. Typically ~/.local/, or %APPDATA%\\Python on "
-                 "Windows. (See the Python documentation for site.USER_BASE "
-                 "for full details.)")
-        cmd_opts.add_option(
-            '--no-user',
-            dest='use_user_site',
-            action='store_false',
-            help=SUPPRESS_HELP)
-        cmd_opts.add_option(
-            '--root',
-            dest='root_path',
-            metavar='dir',
-            default=None,
-            help="Install everything relative to this alternate root "
-                 "directory.")
-        cmd_opts.add_option(
-            '--prefix',
-            dest='prefix_path',
-            metavar='dir',
-            default=None,
-            help="Installation prefix where lib, bin and other top-level "
-                 "folders are placed")
-
-        cmd_opts.add_option(cmdoptions.build_dir())
-
-        cmd_opts.add_option(cmdoptions.src())
-
-        cmd_opts.add_option(
-            '-U', '--upgrade',
-            dest='upgrade',
-            action='store_true',
-            help='Upgrade all specified packages to the newest available '
-                 'version. The handling of dependencies depends on the '
-                 'upgrade-strategy used.'
-        )
-
-        cmd_opts.add_option(
-            '--upgrade-strategy',
-            dest='upgrade_strategy',
-            default='only-if-needed',
-            choices=['only-if-needed', 'eager'],
-            help='Determines how dependency upgrading should be handled '
-                 '[default: %default]. '
-                 '"eager" - dependencies are upgraded regardless of '
-                 'whether the currently installed version satisfies the '
-                 'requirements of the upgraded package(s). '
-                 '"only-if-needed" -  are upgraded only when they do not '
-                 'satisfy the requirements of the upgraded package(s).'
-        )
-
-        cmd_opts.add_option(
-            '--force-reinstall',
-            dest='force_reinstall',
-            action='store_true',
-            help='Reinstall all packages even if they are already '
-                 'up-to-date.')
-
-        cmd_opts.add_option(
-            '-I', '--ignore-installed',
-            dest='ignore_installed',
-            action='store_true',
-            help='Ignore the installed packages (reinstalling instead).')
-
-        cmd_opts.add_option(cmdoptions.ignore_requires_python())
-        cmd_opts.add_option(cmdoptions.no_build_isolation())
-        cmd_opts.add_option(cmdoptions.use_pep517())
-        cmd_opts.add_option(cmdoptions.no_use_pep517())
-
-        cmd_opts.add_option(cmdoptions.install_options())
-        cmd_opts.add_option(cmdoptions.global_options())
-
-        cmd_opts.add_option(
-            "--compile",
-            action="store_true",
-            dest="compile",
-            default=True,
-            help="Compile Python source files to bytecode",
-        )
-
-        cmd_opts.add_option(
-            "--no-compile",
-            action="store_false",
-            dest="compile",
-            help="Do not compile Python source files to bytecode",
-        )
-
-        cmd_opts.add_option(
-            "--no-warn-script-location",
-            action="store_false",
-            dest="warn_script_location",
-            default=True,
-            help="Do not warn when installing scripts outside PATH",
-        )
-        cmd_opts.add_option(
-            "--no-warn-conflicts",
-            action="store_false",
-            dest="warn_about_conflicts",
-            default=True,
-            help="Do not warn about broken dependencies",
-        )
-
-        cmd_opts.add_option(cmdoptions.no_binary())
-        cmd_opts.add_option(cmdoptions.only_binary())
-        cmd_opts.add_option(cmdoptions.prefer_binary())
-        cmd_opts.add_option(cmdoptions.no_clean())
-        cmd_opts.add_option(cmdoptions.require_hashes())
-        cmd_opts.add_option(cmdoptions.progress_bar())
-
-        index_opts = cmdoptions.make_option_group(
-            cmdoptions.index_group,
-            self.parser,
-        )
-
-        self.parser.insert_option_group(0, index_opts)
-        self.parser.insert_option_group(0, cmd_opts)
-
-    def run(self, options, args):
-        cmdoptions.check_install_build_global(options)
-        upgrade_strategy = "to-satisfy-only"
-        if options.upgrade:
-            upgrade_strategy = options.upgrade_strategy
-
-        if options.build_dir:
-            options.build_dir = os.path.abspath(options.build_dir)
-
-        cmdoptions.check_dist_restriction(options, check_target=True)
-
-        if options.python_version:
-            python_versions = [options.python_version]
-        else:
-            python_versions = None
-
-        options.src_dir = os.path.abspath(options.src_dir)
-        install_options = options.install_options or []
-        if options.use_user_site:
-            if options.prefix_path:
-                raise CommandError(
-                    "Can not combine '--user' and '--prefix' as they imply "
-                    "different installation locations"
-                )
-            if virtualenv_no_global():
-                raise InstallationError(
-                    "Can not perform a '--user' install. User site-packages "
-                    "are not visible in this virtualenv."
-                )
-            install_options.append('--user')
-            install_options.append('--prefix=')
-
-        target_temp_dir = TempDirectory(kind="target")
-        if options.target_dir:
-            options.ignore_installed = True
-            options.target_dir = os.path.abspath(options.target_dir)
-            if (os.path.exists(options.target_dir) and not
-                    os.path.isdir(options.target_dir)):
-                raise CommandError(
-                    "Target path exists but is not a directory, will not "
-                    "continue."
-                )
-
-            # Create a target directory for using with the target option
-            target_temp_dir.create()
-            install_options.append('--home=' + target_temp_dir.path)
-
-        global_options = options.global_options or []
-
-        with self._build_session(options) as session:
-            finder = self._build_package_finder(
-                options=options,
-                session=session,
-                platform=options.platform,
-                python_versions=python_versions,
-                abi=options.abi,
-                implementation=options.implementation,
-            )
-            build_delete = (not (options.no_clean or options.build_dir))
-            wheel_cache = WheelCache(options.cache_dir, options.format_control)
-
-            if options.cache_dir and not check_path_owner(options.cache_dir):
-                logger.warning(
-                    "The directory '%s' or its parent directory is not owned "
-                    "by the current user and caching wheels has been "
-                    "disabled. check the permissions and owner of that "
-                    "directory. If executing pip with sudo, you may want "
-                    "sudo's -H flag.",
-                    options.cache_dir,
-                )
-                options.cache_dir = None
-
-            with RequirementTracker() as req_tracker, TempDirectory(
-                options.build_dir, delete=build_delete, kind="install"
-            ) as directory:
-                requirement_set = RequirementSet(
-                    require_hashes=options.require_hashes,
-                    check_supported_wheels=not options.target_dir,
-                )
-
-                try:
-                    self.populate_requirement_set(
-                        requirement_set, args, options, finder, session,
-                        self.name, wheel_cache
-                    )
-                    preparer = RequirementPreparer(
-                        build_dir=directory.path,
-                        src_dir=options.src_dir,
-                        download_dir=None,
-                        wheel_download_dir=None,
-                        progress_bar=options.progress_bar,
-                        build_isolation=options.build_isolation,
-                        req_tracker=req_tracker,
-                    )
-
-                    resolver = Resolver(
-                        preparer=preparer,
-                        finder=finder,
-                        session=session,
-                        wheel_cache=wheel_cache,
-                        use_user_site=options.use_user_site,
-                        upgrade_strategy=upgrade_strategy,
-                        force_reinstall=options.force_reinstall,
-                        ignore_dependencies=options.ignore_dependencies,
-                        ignore_requires_python=options.ignore_requires_python,
-                        ignore_installed=options.ignore_installed,
-                        isolated=options.isolated_mode,
-                        use_pep517=options.use_pep517
-                    )
-                    resolver.resolve(requirement_set)
-
-                    protect_pip_from_modification_on_windows(
-                        modifying_pip=requirement_set.has_requirement("pip")
-                    )
-
-                    # Consider legacy and PEP517-using requirements separately
-                    legacy_requirements = []
-                    pep517_requirements = []
-                    for req in requirement_set.requirements.values():
-                        if req.use_pep517:
-                            pep517_requirements.append(req)
-                        else:
-                            legacy_requirements.append(req)
-
-                    # We don't build wheels for legacy requirements if we
-                    # don't have wheel installed or we don't have a cache dir
-                    try:
-                        import wheel  # noqa: F401
-                        build_legacy = bool(options.cache_dir)
-                    except ImportError:
-                        build_legacy = False
-
-                    wb = WheelBuilder(
-                        finder, preparer, wheel_cache,
-                        build_options=[], global_options=[],
-                    )
-
-                    # Always build PEP 517 requirements
-                    build_failures = wb.build(
-                        pep517_requirements,
-                        session=session, autobuilding=True
-                    )
-
-                    if build_legacy:
-                        # We don't care about failures building legacy
-                        # requirements, as we'll fall through to a direct
-                        # install for those.
-                        wb.build(
-                            legacy_requirements,
-                            session=session, autobuilding=True
-                        )
-
-                    # If we're using PEP 517, we cannot do a direct install
-                    # so we fail here.
-                    if build_failures:
-                        raise InstallationError(
-                            "Could not build wheels for {} which use"
-                            " PEP 517 and cannot be installed directly".format(
-                                ", ".join(r.name for r in build_failures)))
-
-                    to_install = resolver.get_installation_order(
-                        requirement_set
-                    )
-
-                    # Consistency Checking of the package set we're installing.
-                    should_warn_about_conflicts = (
-                        not options.ignore_dependencies and
-                        options.warn_about_conflicts
-                    )
-                    if should_warn_about_conflicts:
-                        self._warn_about_conflicts(to_install)
-
-                    # Don't warn about script install locations if
-                    # --target has been specified
-                    warn_script_location = options.warn_script_location
-                    if options.target_dir:
-                        warn_script_location = False
-
-                    installed = install_given_reqs(
-                        to_install,
-                        install_options,
-                        global_options,
-                        root=options.root_path,
-                        home=target_temp_dir.path,
-                        prefix=options.prefix_path,
-                        pycompile=options.compile,
-                        warn_script_location=warn_script_location,
-                        use_user_site=options.use_user_site,
-                    )
-
-                    lib_locations = get_lib_location_guesses(
-                        user=options.use_user_site,
-                        home=target_temp_dir.path,
-                        root=options.root_path,
-                        prefix=options.prefix_path,
-                        isolated=options.isolated_mode,
-                    )
-                    working_set = pkg_resources.WorkingSet(lib_locations)
-
-                    reqs = sorted(installed, key=operator.attrgetter('name'))
-                    items = []
-                    for req in reqs:
-                        item = req.name
-                        try:
-                            installed_version = get_installed_version(
-                                req.name, working_set=working_set
-                            )
-                            if installed_version:
-                                item += '-' + installed_version
-                        except Exception:
-                            pass
-                        items.append(item)
-                    installed = ' '.join(items)
-                    if installed:
-                        logger.info('Successfully installed %s', installed)
-                except EnvironmentError as error:
-                    show_traceback = (self.verbosity >= 1)
-
-                    message = create_env_error_message(
-                        error, show_traceback, options.use_user_site,
-                    )
-                    logger.error(message, exc_info=show_traceback)
-
-                    return ERROR
-                except PreviousBuildDirError:
-                    options.no_clean = True
-                    raise
-                finally:
-                    # Clean up
-                    if not options.no_clean:
-                        requirement_set.cleanup_files()
-                        wheel_cache.cleanup()
-
-        if options.target_dir:
-            self._handle_target_dir(
-                options.target_dir, target_temp_dir, options.upgrade
-            )
-        return requirement_set
-
-    def _handle_target_dir(self, target_dir, target_temp_dir, upgrade):
-        ensure_dir(target_dir)
-
-        # Checking both purelib and platlib directories for installed
-        # packages to be moved to target directory
-        lib_dir_list = []
-
-        with target_temp_dir:
-            # Checking both purelib and platlib directories for installed
-            # packages to be moved to target directory
-            scheme = distutils_scheme('', home=target_temp_dir.path)
-            purelib_dir = scheme['purelib']
-            platlib_dir = scheme['platlib']
-            data_dir = scheme['data']
-
-            if os.path.exists(purelib_dir):
-                lib_dir_list.append(purelib_dir)
-            if os.path.exists(platlib_dir) and platlib_dir != purelib_dir:
-                lib_dir_list.append(platlib_dir)
-            if os.path.exists(data_dir):
-                lib_dir_list.append(data_dir)
-
-            for lib_dir in lib_dir_list:
-                for item in os.listdir(lib_dir):
-                    if lib_dir == data_dir:
-                        ddir = os.path.join(data_dir, item)
-                        if any(s.startswith(ddir) for s in lib_dir_list[:-1]):
-                            continue
-                    target_item_dir = os.path.join(target_dir, item)
-                    if os.path.exists(target_item_dir):
-                        if not upgrade:
-                            logger.warning(
-                                'Target directory %s already exists. Specify '
-                                '--upgrade to force replacement.',
-                                target_item_dir
-                            )
-                            continue
-                        if os.path.islink(target_item_dir):
-                            logger.warning(
-                                'Target directory %s already exists and is '
-                                'a link. Pip will not automatically replace '
-                                'links, please remove if replacement is '
-                                'desired.',
-                                target_item_dir
-                            )
-                            continue
-                        if os.path.isdir(target_item_dir):
-                            shutil.rmtree(target_item_dir)
-                        else:
-                            os.remove(target_item_dir)
-
-                    shutil.move(
-                        os.path.join(lib_dir, item),
-                        target_item_dir
-                    )
-
-    def _warn_about_conflicts(self, to_install):
-        try:
-            package_set, _dep_info = check_install_conflicts(to_install)
-        except Exception:
-            logger.error("Error checking for conflicts.", exc_info=True)
-            return
-        missing, conflicting = _dep_info
-
-        # NOTE: There is some duplication here from pip check
-        for project_name in missing:
-            version = package_set[project_name][0]
-            for dependency in missing[project_name]:
-                logger.critical(
-                    "%s %s requires %s, which is not installed.",
-                    project_name, version, dependency[1],
-                )
-
-        for project_name in conflicting:
-            version = package_set[project_name][0]
-            for dep_name, dep_version, req in conflicting[project_name]:
-                logger.critical(
-                    "%s %s has requirement %s, but you'll have %s %s which is "
-                    "incompatible.",
-                    project_name, version, req, dep_name, dep_version,
-                )
-
-
-def get_lib_location_guesses(*args, **kwargs):
-    scheme = distutils_scheme('', *args, **kwargs)
-    return [scheme['purelib'], scheme['platlib']]
-
-
-def create_env_error_message(error, show_traceback, using_user_site):
-    """Format an error message for an EnvironmentError
-
-    It may occur anytime during the execution of the install command.
-    """
-    parts = []
-
-    # Mention the error if we are not going to show a traceback
-    parts.append("Could not install packages due to an EnvironmentError")
-    if not show_traceback:
-        parts.append(": ")
-        parts.append(str(error))
-    else:
-        parts.append(".")
-
-    # Spilt the error indication from a helper message (if any)
-    parts[-1] += "\n"
-
-    # Suggest useful actions to the user:
-    #  (1) using user site-packages or (2) verifying the permissions
-    if error.errno == errno.EACCES:
-        user_option_part = "Consider using the `--user` option"
-        permissions_part = "Check the permissions"
-
-        if not using_user_site:
-            parts.extend([
-                user_option_part, " or ",
-                permissions_part.lower(),
-            ])
-        else:
-            parts.append(permissions_part)
-        parts.append(".\n")
-
-    return "".join(parts).strip() + "\n"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/list.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/list.py
deleted file mode 100644
index a640274..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/list.py
+++ /dev/null
@@ -1,301 +0,0 @@
-from __future__ import absolute_import
-
-import json
-import logging
-
-from pip._vendor import six
-from pip._vendor.six.moves import zip_longest
-
-from pip._internal.cli import cmdoptions
-from pip._internal.cli.base_command import Command
-from pip._internal.exceptions import CommandError
-from pip._internal.index import PackageFinder
-from pip._internal.utils.misc import (
-    dist_is_editable, get_installed_distributions,
-)
-from pip._internal.utils.packaging import get_installer
-
-logger = logging.getLogger(__name__)
-
-
-class ListCommand(Command):
-    """
-    List installed packages, including editables.
-
-    Packages are listed in a case-insensitive sorted order.
-    """
-    name = 'list'
-    usage = """
-      %prog [options]"""
-    summary = 'List installed packages.'
-
-    def __init__(self, *args, **kw):
-        super(ListCommand, self).__init__(*args, **kw)
-
-        cmd_opts = self.cmd_opts
-
-        cmd_opts.add_option(
-            '-o', '--outdated',
-            action='store_true',
-            default=False,
-            help='List outdated packages')
-        cmd_opts.add_option(
-            '-u', '--uptodate',
-            action='store_true',
-            default=False,
-            help='List uptodate packages')
-        cmd_opts.add_option(
-            '-e', '--editable',
-            action='store_true',
-            default=False,
-            help='List editable projects.')
-        cmd_opts.add_option(
-            '-l', '--local',
-            action='store_true',
-            default=False,
-            help=('If in a virtualenv that has global access, do not list '
-                  'globally-installed packages.'),
-        )
-        self.cmd_opts.add_option(
-            '--user',
-            dest='user',
-            action='store_true',
-            default=False,
-            help='Only output packages installed in user-site.')
-
-        cmd_opts.add_option(
-            '--pre',
-            action='store_true',
-            default=False,
-            help=("Include pre-release and development versions. By default, "
-                  "pip only finds stable versions."),
-        )
-
-        cmd_opts.add_option(
-            '--format',
-            action='store',
-            dest='list_format',
-            default="columns",
-            choices=('columns', 'freeze', 'json'),
-            help="Select the output format among: columns (default), freeze, "
-                 "or json",
-        )
-
-        cmd_opts.add_option(
-            '--not-required',
-            action='store_true',
-            dest='not_required',
-            help="List packages that are not dependencies of "
-                 "installed packages.",
-        )
-
-        cmd_opts.add_option(
-            '--exclude-editable',
-            action='store_false',
-            dest='include_editable',
-            help='Exclude editable package from output.',
-        )
-        cmd_opts.add_option(
-            '--include-editable',
-            action='store_true',
-            dest='include_editable',
-            help='Include editable package from output.',
-            default=True,
-        )
-        index_opts = cmdoptions.make_option_group(
-            cmdoptions.index_group, self.parser
-        )
-
-        self.parser.insert_option_group(0, index_opts)
-        self.parser.insert_option_group(0, cmd_opts)
-
-    def _build_package_finder(self, options, index_urls, session):
-        """
-        Create a package finder appropriate to this list command.
-        """
-        return PackageFinder(
-            find_links=options.find_links,
-            index_urls=index_urls,
-            allow_all_prereleases=options.pre,
-            trusted_hosts=options.trusted_hosts,
-            session=session,
-        )
-
-    def run(self, options, args):
-        if options.outdated and options.uptodate:
-            raise CommandError(
-                "Options --outdated and --uptodate cannot be combined.")
-
-        packages = get_installed_distributions(
-            local_only=options.local,
-            user_only=options.user,
-            editables_only=options.editable,
-            include_editables=options.include_editable,
-        )
-
-        # get_not_required must be called firstly in order to find and
-        # filter out all dependencies correctly. Otherwise a package
-        # can't be identified as requirement because some parent packages
-        # could be filtered out before.
-        if options.not_required:
-            packages = self.get_not_required(packages, options)
-
-        if options.outdated:
-            packages = self.get_outdated(packages, options)
-        elif options.uptodate:
-            packages = self.get_uptodate(packages, options)
-
-        self.output_package_listing(packages, options)
-
-    def get_outdated(self, packages, options):
-        return [
-            dist for dist in self.iter_packages_latest_infos(packages, options)
-            if dist.latest_version > dist.parsed_version
-        ]
-
-    def get_uptodate(self, packages, options):
-        return [
-            dist for dist in self.iter_packages_latest_infos(packages, options)
-            if dist.latest_version == dist.parsed_version
-        ]
-
-    def get_not_required(self, packages, options):
-        dep_keys = set()
-        for dist in packages:
-            dep_keys.update(requirement.key for requirement in dist.requires())
-        return {pkg for pkg in packages if pkg.key not in dep_keys}
-
-    def iter_packages_latest_infos(self, packages, options):
-        index_urls = [options.index_url] + options.extra_index_urls
-        if options.no_index:
-            logger.debug('Ignoring indexes: %s', ','.join(index_urls))
-            index_urls = []
-
-        with self._build_session(options) as session:
-            finder = self._build_package_finder(options, index_urls, session)
-
-            for dist in packages:
-                typ = 'unknown'
-                all_candidates = finder.find_all_candidates(dist.key)
-                if not options.pre:
-                    # Remove prereleases
-                    all_candidates = [candidate for candidate in all_candidates
-                                      if not candidate.version.is_prerelease]
-
-                if not all_candidates:
-                    continue
-                best_candidate = max(all_candidates,
-                                     key=finder._candidate_sort_key)
-                remote_version = best_candidate.version
-                if best_candidate.location.is_wheel:
-                    typ = 'wheel'
-                else:
-                    typ = 'sdist'
-                # This is dirty but makes the rest of the code much cleaner
-                dist.latest_version = remote_version
-                dist.latest_filetype = typ
-                yield dist
-
-    def output_package_listing(self, packages, options):
-        packages = sorted(
-            packages,
-            key=lambda dist: dist.project_name.lower(),
-        )
-        if options.list_format == 'columns' and packages:
-            data, header = format_for_columns(packages, options)
-            self.output_package_listing_columns(data, header)
-        elif options.list_format == 'freeze':
-            for dist in packages:
-                if options.verbose >= 1:
-                    logger.info("%s==%s (%s)", dist.project_name,
-                                dist.version, dist.location)
-                else:
-                    logger.info("%s==%s", dist.project_name, dist.version)
-        elif options.list_format == 'json':
-            logger.info(format_for_json(packages, options))
-
-    def output_package_listing_columns(self, data, header):
-        # insert the header first: we need to know the size of column names
-        if len(data) > 0:
-            data.insert(0, header)
-
-        pkg_strings, sizes = tabulate(data)
-
-        # Create and add a separator.
-        if len(data) > 0:
-            pkg_strings.insert(1, " ".join(map(lambda x: '-' * x, sizes)))
-
-        for val in pkg_strings:
-            logger.info(val)
-
-
-def tabulate(vals):
-    # From pfmoore on GitHub:
-    # https://github.com/pypa/pip/issues/3651#issuecomment-216932564
-    assert len(vals) > 0
-
-    sizes = [0] * max(len(x) for x in vals)
-    for row in vals:
-        sizes = [max(s, len(str(c))) for s, c in zip_longest(sizes, row)]
-
-    result = []
-    for row in vals:
-        display = " ".join([str(c).ljust(s) if c is not None else ''
-                            for s, c in zip_longest(sizes, row)])
-        result.append(display)
-
-    return result, sizes
-
-
-def format_for_columns(pkgs, options):
-    """
-    Convert the package data into something usable
-    by output_package_listing_columns.
-    """
-    running_outdated = options.outdated
-    # Adjust the header for the `pip list --outdated` case.
-    if running_outdated:
-        header = ["Package", "Version", "Latest", "Type"]
-    else:
-        header = ["Package", "Version"]
-
-    data = []
-    if options.verbose >= 1 or any(dist_is_editable(x) for x in pkgs):
-        header.append("Location")
-    if options.verbose >= 1:
-        header.append("Installer")
-
-    for proj in pkgs:
-        # if we're working on the 'outdated' list, separate out the
-        # latest_version and type
-        row = [proj.project_name, proj.version]
-
-        if running_outdated:
-            row.append(proj.latest_version)
-            row.append(proj.latest_filetype)
-
-        if options.verbose >= 1 or dist_is_editable(proj):
-            row.append(proj.location)
-        if options.verbose >= 1:
-            row.append(get_installer(proj))
-
-        data.append(row)
-
-    return data, header
-
-
-def format_for_json(packages, options):
-    data = []
-    for dist in packages:
-        info = {
-            'name': dist.project_name,
-            'version': six.text_type(dist.version),
-        }
-        if options.verbose >= 1:
-            info['location'] = dist.location
-            info['installer'] = get_installer(dist)
-        if options.outdated:
-            info['latest_version'] = six.text_type(dist.latest_version)
-            info['latest_filetype'] = dist.latest_filetype
-        data.append(info)
-    return json.dumps(data)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/search.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/search.py
deleted file mode 100644
index c157a31..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/search.py
+++ /dev/null
@@ -1,135 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import sys
-import textwrap
-from collections import OrderedDict
-
-from pip._vendor import pkg_resources
-from pip._vendor.packaging.version import parse as parse_version
-# NOTE: XMLRPC Client is not annotated in typeshed as on 2017-07-17, which is
-#       why we ignore the type on this import
-from pip._vendor.six.moves import xmlrpc_client  # type: ignore
-
-from pip._internal.cli.base_command import Command
-from pip._internal.cli.status_codes import NO_MATCHES_FOUND, SUCCESS
-from pip._internal.download import PipXmlrpcTransport
-from pip._internal.exceptions import CommandError
-from pip._internal.models.index import PyPI
-from pip._internal.utils.compat import get_terminal_size
-from pip._internal.utils.logging import indent_log
-
-logger = logging.getLogger(__name__)
-
-
-class SearchCommand(Command):
-    """Search for PyPI packages whose name or summary contains <query>."""
-    name = 'search'
-    usage = """
-      %prog [options] <query>"""
-    summary = 'Search PyPI for packages.'
-    ignore_require_venv = True
-
-    def __init__(self, *args, **kw):
-        super(SearchCommand, self).__init__(*args, **kw)
-        self.cmd_opts.add_option(
-            '-i', '--index',
-            dest='index',
-            metavar='URL',
-            default=PyPI.pypi_url,
-            help='Base URL of Python Package Index (default %default)')
-
-        self.parser.insert_option_group(0, self.cmd_opts)
-
-    def run(self, options, args):
-        if not args:
-            raise CommandError('Missing required argument (search query).')
-        query = args
-        pypi_hits = self.search(query, options)
-        hits = transform_hits(pypi_hits)
-
-        terminal_width = None
-        if sys.stdout.isatty():
-            terminal_width = get_terminal_size()[0]
-
-        print_results(hits, terminal_width=terminal_width)
-        if pypi_hits:
-            return SUCCESS
-        return NO_MATCHES_FOUND
-
-    def search(self, query, options):
-        index_url = options.index
-        with self._build_session(options) as session:
-            transport = PipXmlrpcTransport(index_url, session)
-            pypi = xmlrpc_client.ServerProxy(index_url, transport)
-            hits = pypi.search({'name': query, 'summary': query}, 'or')
-            return hits
-
-
-def transform_hits(hits):
-    """
-    The list from pypi is really a list of versions. We want a list of
-    packages with the list of versions stored inline. This converts the
-    list from pypi into one we can use.
-    """
-    packages = OrderedDict()
-    for hit in hits:
-        name = hit['name']
-        summary = hit['summary']
-        version = hit['version']
-
-        if name not in packages.keys():
-            packages[name] = {
-                'name': name,
-                'summary': summary,
-                'versions': [version],
-            }
-        else:
-            packages[name]['versions'].append(version)
-
-            # if this is the highest version, replace summary and score
-            if version == highest_version(packages[name]['versions']):
-                packages[name]['summary'] = summary
-
-    return list(packages.values())
-
-
-def print_results(hits, name_column_width=None, terminal_width=None):
-    if not hits:
-        return
-    if name_column_width is None:
-        name_column_width = max([
-            len(hit['name']) + len(highest_version(hit.get('versions', ['-'])))
-            for hit in hits
-        ]) + 4
-
-    installed_packages = [p.project_name for p in pkg_resources.working_set]
-    for hit in hits:
-        name = hit['name']
-        summary = hit['summary'] or ''
-        latest = highest_version(hit.get('versions', ['-']))
-        if terminal_width is not None:
-            target_width = terminal_width - name_column_width - 5
-            if target_width > 10:
-                # wrap and indent summary to fit terminal
-                summary = textwrap.wrap(summary, target_width)
-                summary = ('\n' + ' ' * (name_column_width + 3)).join(summary)
-
-        line = '%-*s - %s' % (name_column_width,
-                              '%s (%s)' % (name, latest), summary)
-        try:
-            logger.info(line)
-            if name in installed_packages:
-                dist = pkg_resources.get_distribution(name)
-                with indent_log():
-                    if dist.version == latest:
-                        logger.info('INSTALLED: %s (latest)', dist.version)
-                    else:
-                        logger.info('INSTALLED: %s', dist.version)
-                        logger.info('LATEST:    %s', latest)
-        except UnicodeEncodeError:
-            pass
-
-
-def highest_version(versions):
-    return max(versions, key=parse_version)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/show.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/show.py
deleted file mode 100644
index f92c9bc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/show.py
+++ /dev/null
@@ -1,168 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import os
-from email.parser import FeedParser  # type: ignore
-
-from pip._vendor import pkg_resources
-from pip._vendor.packaging.utils import canonicalize_name
-
-from pip._internal.cli.base_command import Command
-from pip._internal.cli.status_codes import ERROR, SUCCESS
-
-logger = logging.getLogger(__name__)
-
-
-class ShowCommand(Command):
-    """
-    Show information about one or more installed packages.
-
-    The output is in RFC-compliant mail header format.
-    """
-    name = 'show'
-    usage = """
-      %prog [options] <package> ..."""
-    summary = 'Show information about installed packages.'
-    ignore_require_venv = True
-
-    def __init__(self, *args, **kw):
-        super(ShowCommand, self).__init__(*args, **kw)
-        self.cmd_opts.add_option(
-            '-f', '--files',
-            dest='files',
-            action='store_true',
-            default=False,
-            help='Show the full list of installed files for each package.')
-
-        self.parser.insert_option_group(0, self.cmd_opts)
-
-    def run(self, options, args):
-        if not args:
-            logger.warning('ERROR: Please provide a package name or names.')
-            return ERROR
-        query = args
-
-        results = search_packages_info(query)
-        if not print_results(
-                results, list_files=options.files, verbose=options.verbose):
-            return ERROR
-        return SUCCESS
-
-
-def search_packages_info(query):
-    """
-    Gather details from installed distributions. Print distribution name,
-    version, location, and installed files. Installed files requires a
-    pip generated 'installed-files.txt' in the distributions '.egg-info'
-    directory.
-    """
-    installed = {}
-    for p in pkg_resources.working_set:
-        installed[canonicalize_name(p.project_name)] = p
-
-    query_names = [canonicalize_name(name) for name in query]
-
-    for dist in [installed[pkg] for pkg in query_names if pkg in installed]:
-        package = {
-            'name': dist.project_name,
-            'version': dist.version,
-            'location': dist.location,
-            'requires': [dep.project_name for dep in dist.requires()],
-        }
-        file_list = None
-        metadata = None
-        if isinstance(dist, pkg_resources.DistInfoDistribution):
-            # RECORDs should be part of .dist-info metadatas
-            if dist.has_metadata('RECORD'):
-                lines = dist.get_metadata_lines('RECORD')
-                paths = [l.split(',')[0] for l in lines]
-                paths = [os.path.join(dist.location, p) for p in paths]
-                file_list = [os.path.relpath(p, dist.location) for p in paths]
-
-            if dist.has_metadata('METADATA'):
-                metadata = dist.get_metadata('METADATA')
-        else:
-            # Otherwise use pip's log for .egg-info's
-            if dist.has_metadata('installed-files.txt'):
-                paths = dist.get_metadata_lines('installed-files.txt')
-                paths = [os.path.join(dist.egg_info, p) for p in paths]
-                file_list = [os.path.relpath(p, dist.location) for p in paths]
-
-            if dist.has_metadata('PKG-INFO'):
-                metadata = dist.get_metadata('PKG-INFO')
-
-        if dist.has_metadata('entry_points.txt'):
-            entry_points = dist.get_metadata_lines('entry_points.txt')
-            package['entry_points'] = entry_points
-
-        if dist.has_metadata('INSTALLER'):
-            for line in dist.get_metadata_lines('INSTALLER'):
-                if line.strip():
-                    package['installer'] = line.strip()
-                    break
-
-        # @todo: Should pkg_resources.Distribution have a
-        # `get_pkg_info` method?
-        feed_parser = FeedParser()
-        feed_parser.feed(metadata)
-        pkg_info_dict = feed_parser.close()
-        for key in ('metadata-version', 'summary',
-                    'home-page', 'author', 'author-email', 'license'):
-            package[key] = pkg_info_dict.get(key)
-
-        # It looks like FeedParser cannot deal with repeated headers
-        classifiers = []
-        for line in metadata.splitlines():
-            if line.startswith('Classifier: '):
-                classifiers.append(line[len('Classifier: '):])
-        package['classifiers'] = classifiers
-
-        if file_list:
-            package['files'] = sorted(file_list)
-        yield package
-
-
-def print_results(distributions, list_files=False, verbose=False):
-    """
-    Print the informations from installed distributions found.
-    """
-    results_printed = False
-    for i, dist in enumerate(distributions):
-        results_printed = True
-        if i > 0:
-            logger.info("---")
-
-        name = dist.get('name', '')
-        required_by = [
-            pkg.project_name for pkg in pkg_resources.working_set
-            if name in [required.name for required in pkg.requires()]
-        ]
-
-        logger.info("Name: %s", name)
-        logger.info("Version: %s", dist.get('version', ''))
-        logger.info("Summary: %s", dist.get('summary', ''))
-        logger.info("Home-page: %s", dist.get('home-page', ''))
-        logger.info("Author: %s", dist.get('author', ''))
-        logger.info("Author-email: %s", dist.get('author-email', ''))
-        logger.info("License: %s", dist.get('license', ''))
-        logger.info("Location: %s", dist.get('location', ''))
-        logger.info("Requires: %s", ', '.join(dist.get('requires', [])))
-        logger.info("Required-by: %s", ', '.join(required_by))
-
-        if verbose:
-            logger.info("Metadata-Version: %s",
-                        dist.get('metadata-version', ''))
-            logger.info("Installer: %s", dist.get('installer', ''))
-            logger.info("Classifiers:")
-            for classifier in dist.get('classifiers', []):
-                logger.info("  %s", classifier)
-            logger.info("Entry-points:")
-            for entry in dist.get('entry_points', []):
-                logger.info("  %s", entry.strip())
-        if list_files:
-            logger.info("Files:")
-            for line in dist.get('files', []):
-                logger.info("  %s", line.strip())
-            if "files" not in dist:
-                logger.info("Cannot locate installed-files.txt")
-    return results_printed
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/uninstall.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/uninstall.py
deleted file mode 100644
index 0cd6f54..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/uninstall.py
+++ /dev/null
@@ -1,78 +0,0 @@
-from __future__ import absolute_import
-
-from pip._vendor.packaging.utils import canonicalize_name
-
-from pip._internal.cli.base_command import Command
-from pip._internal.exceptions import InstallationError
-from pip._internal.req import parse_requirements
-from pip._internal.req.constructors import install_req_from_line
-from pip._internal.utils.misc import protect_pip_from_modification_on_windows
-
-
-class UninstallCommand(Command):
-    """
-    Uninstall packages.
-
-    pip is able to uninstall most installed packages. Known exceptions are:
-
-    - Pure distutils packages installed with ``python setup.py install``, which
-      leave behind no metadata to determine what files were installed.
-    - Script wrappers installed by ``python setup.py develop``.
-    """
-    name = 'uninstall'
-    usage = """
-      %prog [options] <package> ...
-      %prog [options] -r <requirements file> ..."""
-    summary = 'Uninstall packages.'
-
-    def __init__(self, *args, **kw):
-        super(UninstallCommand, self).__init__(*args, **kw)
-        self.cmd_opts.add_option(
-            '-r', '--requirement',
-            dest='requirements',
-            action='append',
-            default=[],
-            metavar='file',
-            help='Uninstall all the packages listed in the given requirements '
-                 'file.  This option can be used multiple times.',
-        )
-        self.cmd_opts.add_option(
-            '-y', '--yes',
-            dest='yes',
-            action='store_true',
-            help="Don't ask for confirmation of uninstall deletions.")
-
-        self.parser.insert_option_group(0, self.cmd_opts)
-
-    def run(self, options, args):
-        with self._build_session(options) as session:
-            reqs_to_uninstall = {}
-            for name in args:
-                req = install_req_from_line(
-                    name, isolated=options.isolated_mode,
-                )
-                if req.name:
-                    reqs_to_uninstall[canonicalize_name(req.name)] = req
-            for filename in options.requirements:
-                for req in parse_requirements(
-                        filename,
-                        options=options,
-                        session=session):
-                    if req.name:
-                        reqs_to_uninstall[canonicalize_name(req.name)] = req
-            if not reqs_to_uninstall:
-                raise InstallationError(
-                    'You must give at least one requirement to %(name)s (see '
-                    '"pip help %(name)s")' % dict(name=self.name)
-                )
-
-            protect_pip_from_modification_on_windows(
-                modifying_pip="pip" in reqs_to_uninstall
-            )
-
-            for req in reqs_to_uninstall.values():
-                uninstall_pathset = req.uninstall(
-                    auto_confirm=options.yes, verbose=self.verbosity > 0,
-                )
-                if uninstall_pathset:
-                    uninstall_pathset.commit()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/wheel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/wheel.py
deleted file mode 100644
index cd72a3d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/commands/wheel.py
+++ /dev/null
@@ -1,186 +0,0 @@
-# -*- coding: utf-8 -*-
-from __future__ import absolute_import
-
-import logging
-import os
-
-from pip._internal.cache import WheelCache
-from pip._internal.cli import cmdoptions
-from pip._internal.cli.base_command import RequirementCommand
-from pip._internal.exceptions import CommandError, PreviousBuildDirError
-from pip._internal.operations.prepare import RequirementPreparer
-from pip._internal.req import RequirementSet
-from pip._internal.req.req_tracker import RequirementTracker
-from pip._internal.resolve import Resolver
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.wheel import WheelBuilder
-
-logger = logging.getLogger(__name__)
-
-
-class WheelCommand(RequirementCommand):
-    """
-    Build Wheel archives for your requirements and dependencies.
-
-    Wheel is a built-package format, and offers the advantage of not
-    recompiling your software during every install. For more details, see the
-    wheel docs: https://wheel.readthedocs.io/en/latest/
-
-    Requirements: setuptools>=0.8, and wheel.
-
-    'pip wheel' uses the bdist_wheel setuptools extension from the wheel
-    package to build individual wheels.
-
-    """
-
-    name = 'wheel'
-    usage = """
-      %prog [options] <requirement specifier> ...
-      %prog [options] -r <requirements file> ...
-      %prog [options] [-e] <vcs project url> ...
-      %prog [options] [-e] <local project path> ...
-      %prog [options] <archive url/path> ..."""
-
-    summary = 'Build wheels from your requirements.'
-
-    def __init__(self, *args, **kw):
-        super(WheelCommand, self).__init__(*args, **kw)
-
-        cmd_opts = self.cmd_opts
-
-        cmd_opts.add_option(
-            '-w', '--wheel-dir',
-            dest='wheel_dir',
-            metavar='dir',
-            default=os.curdir,
-            help=("Build wheels into <dir>, where the default is the "
-                  "current working directory."),
-        )
-        cmd_opts.add_option(cmdoptions.no_binary())
-        cmd_opts.add_option(cmdoptions.only_binary())
-        cmd_opts.add_option(cmdoptions.prefer_binary())
-        cmd_opts.add_option(
-            '--build-option',
-            dest='build_options',
-            metavar='options',
-            action='append',
-            help="Extra arguments to be supplied to 'setup.py bdist_wheel'.",
-        )
-        cmd_opts.add_option(cmdoptions.no_build_isolation())
-        cmd_opts.add_option(cmdoptions.use_pep517())
-        cmd_opts.add_option(cmdoptions.no_use_pep517())
-        cmd_opts.add_option(cmdoptions.constraints())
-        cmd_opts.add_option(cmdoptions.editable())
-        cmd_opts.add_option(cmdoptions.requirements())
-        cmd_opts.add_option(cmdoptions.src())
-        cmd_opts.add_option(cmdoptions.ignore_requires_python())
-        cmd_opts.add_option(cmdoptions.no_deps())
-        cmd_opts.add_option(cmdoptions.build_dir())
-        cmd_opts.add_option(cmdoptions.progress_bar())
-
-        cmd_opts.add_option(
-            '--global-option',
-            dest='global_options',
-            action='append',
-            metavar='options',
-            help="Extra global options to be supplied to the setup.py "
-            "call before the 'bdist_wheel' command.")
-
-        cmd_opts.add_option(
-            '--pre',
-            action='store_true',
-            default=False,
-            help=("Include pre-release and development versions. By default, "
-                  "pip only finds stable versions."),
-        )
-
-        cmd_opts.add_option(cmdoptions.no_clean())
-        cmd_opts.add_option(cmdoptions.require_hashes())
-
-        index_opts = cmdoptions.make_option_group(
-            cmdoptions.index_group,
-            self.parser,
-        )
-
-        self.parser.insert_option_group(0, index_opts)
-        self.parser.insert_option_group(0, cmd_opts)
-
-    def run(self, options, args):
-        cmdoptions.check_install_build_global(options)
-
-        index_urls = [options.index_url] + options.extra_index_urls
-        if options.no_index:
-            logger.debug('Ignoring indexes: %s', ','.join(index_urls))
-            index_urls = []
-
-        if options.build_dir:
-            options.build_dir = os.path.abspath(options.build_dir)
-
-        options.src_dir = os.path.abspath(options.src_dir)
-
-        with self._build_session(options) as session:
-            finder = self._build_package_finder(options, session)
-            build_delete = (not (options.no_clean or options.build_dir))
-            wheel_cache = WheelCache(options.cache_dir, options.format_control)
-
-            with RequirementTracker() as req_tracker, TempDirectory(
-                options.build_dir, delete=build_delete, kind="wheel"
-            ) as directory:
-
-                requirement_set = RequirementSet(
-                    require_hashes=options.require_hashes,
-                )
-
-                try:
-                    self.populate_requirement_set(
-                        requirement_set, args, options, finder, session,
-                        self.name, wheel_cache
-                    )
-
-                    preparer = RequirementPreparer(
-                        build_dir=directory.path,
-                        src_dir=options.src_dir,
-                        download_dir=None,
-                        wheel_download_dir=options.wheel_dir,
-                        progress_bar=options.progress_bar,
-                        build_isolation=options.build_isolation,
-                        req_tracker=req_tracker,
-                    )
-
-                    resolver = Resolver(
-                        preparer=preparer,
-                        finder=finder,
-                        session=session,
-                        wheel_cache=wheel_cache,
-                        use_user_site=False,
-                        upgrade_strategy="to-satisfy-only",
-                        force_reinstall=False,
-                        ignore_dependencies=options.ignore_dependencies,
-                        ignore_requires_python=options.ignore_requires_python,
-                        ignore_installed=True,
-                        isolated=options.isolated_mode,
-                        use_pep517=options.use_pep517
-                    )
-                    resolver.resolve(requirement_set)
-
-                    # build wheels
-                    wb = WheelBuilder(
-                        finder, preparer, wheel_cache,
-                        build_options=options.build_options or [],
-                        global_options=options.global_options or [],
-                        no_clean=options.no_clean,
-                    )
-                    build_failures = wb.build(
-                        requirement_set.requirements.values(), session=session,
-                    )
-                    if len(build_failures) != 0:
-                        raise CommandError(
-                            "Failed to build one or more wheels"
-                        )
-                except PreviousBuildDirError:
-                    options.no_clean = True
-                    raise
-                finally:
-                    if not options.no_clean:
-                        requirement_set.cleanup_files()
-                        wheel_cache.cleanup()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/configuration.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/configuration.py
deleted file mode 100644
index fe6df9b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/configuration.py
+++ /dev/null
@@ -1,387 +0,0 @@
-"""Configuration management setup
-
-Some terminology:
-- name
-  As written in config files.
-- value
-  Value associated with a name
-- key
-  Name combined with it's section (section.name)
-- variant
-  A single word describing where the configuration key-value pair came from
-"""
-
-import locale
-import logging
-import os
-
-from pip._vendor import six
-from pip._vendor.six.moves import configparser
-
-from pip._internal.exceptions import (
-    ConfigurationError, ConfigurationFileCouldNotBeLoaded,
-)
-from pip._internal.locations import (
-    legacy_config_file, new_config_file, running_under_virtualenv,
-    site_config_files, venv_config_file,
-)
-from pip._internal.utils.misc import ensure_dir, enum
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Any, Dict, Iterable, List, NewType, Optional, Tuple
-    )
-
-    RawConfigParser = configparser.RawConfigParser  # Shorthand
-    Kind = NewType("Kind", str)
-
-logger = logging.getLogger(__name__)
-
-
-# NOTE: Maybe use the optionx attribute to normalize keynames.
-def _normalize_name(name):
-    # type: (str) -> str
-    """Make a name consistent regardless of source (environment or file)
-    """
-    name = name.lower().replace('_', '-')
-    if name.startswith('--'):
-        name = name[2:]  # only prefer long opts
-    return name
-
-
-def _disassemble_key(name):
-    # type: (str) -> List[str]
-    return name.split(".", 1)
-
-
-# The kinds of configurations there are.
-kinds = enum(
-    USER="user",        # User Specific
-    GLOBAL="global",    # System Wide
-    VENV="venv",        # Virtual Environment Specific
-    ENV="env",          # from PIP_CONFIG_FILE
-    ENV_VAR="env-var",  # from Environment Variables
-)
-
-
-class Configuration(object):
-    """Handles management of configuration.
-
-    Provides an interface to accessing and managing configuration files.
-
-    This class converts provides an API that takes "section.key-name" style
-    keys and stores the value associated with it as "key-name" under the
-    section "section".
-
-    This allows for a clean interface wherein the both the section and the
-    key-name are preserved in an easy to manage form in the configuration files
-    and the data stored is also nice.
-    """
-
-    def __init__(self, isolated, load_only=None):
-        # type: (bool, Kind) -> None
-        super(Configuration, self).__init__()
-
-        _valid_load_only = [kinds.USER, kinds.GLOBAL, kinds.VENV, None]
-        if load_only not in _valid_load_only:
-            raise ConfigurationError(
-                "Got invalid value for load_only - should be one of {}".format(
-                    ", ".join(map(repr, _valid_load_only[:-1]))
-                )
-            )
-        self.isolated = isolated  # type: bool
-        self.load_only = load_only  # type: Optional[Kind]
-
-        # The order here determines the override order.
-        self._override_order = [
-            kinds.GLOBAL, kinds.USER, kinds.VENV, kinds.ENV, kinds.ENV_VAR
-        ]
-
-        self._ignore_env_names = ["version", "help"]
-
-        # Because we keep track of where we got the data from
-        self._parsers = {
-            variant: [] for variant in self._override_order
-        }  # type: Dict[Kind, List[Tuple[str, RawConfigParser]]]
-        self._config = {
-            variant: {} for variant in self._override_order
-        }  # type: Dict[Kind, Dict[str, Any]]
-        self._modified_parsers = []  # type: List[Tuple[str, RawConfigParser]]
-
-    def load(self):
-        # type: () -> None
-        """Loads configuration from configuration files and environment
-        """
-        self._load_config_files()
-        if not self.isolated:
-            self._load_environment_vars()
-
-    def get_file_to_edit(self):
-        # type: () -> Optional[str]
-        """Returns the file with highest priority in configuration
-        """
-        assert self.load_only is not None, \
-            "Need to be specified a file to be editing"
-
-        try:
-            return self._get_parser_to_modify()[0]
-        except IndexError:
-            return None
-
-    def items(self):
-        # type: () -> Iterable[Tuple[str, Any]]
-        """Returns key-value pairs like dict.items() representing the loaded
-        configuration
-        """
-        return self._dictionary.items()
-
-    def get_value(self, key):
-        # type: (str) -> Any
-        """Get a value from the configuration.
-        """
-        try:
-            return self._dictionary[key]
-        except KeyError:
-            raise ConfigurationError("No such key - {}".format(key))
-
-    def set_value(self, key, value):
-        # type: (str, Any) -> None
-        """Modify a value in the configuration.
-        """
-        self._ensure_have_load_only()
-
-        fname, parser = self._get_parser_to_modify()
-
-        if parser is not None:
-            section, name = _disassemble_key(key)
-
-            # Modify the parser and the configuration
-            if not parser.has_section(section):
-                parser.add_section(section)
-            parser.set(section, name, value)
-
-        self._config[self.load_only][key] = value
-        self._mark_as_modified(fname, parser)
-
-    def unset_value(self, key):
-        # type: (str) -> None
-        """Unset a value in the configuration.
-        """
-        self._ensure_have_load_only()
-
-        if key not in self._config[self.load_only]:
-            raise ConfigurationError("No such key - {}".format(key))
-
-        fname, parser = self._get_parser_to_modify()
-
-        if parser is not None:
-            section, name = _disassemble_key(key)
-
-            # Remove the key in the parser
-            modified_something = False
-            if parser.has_section(section):
-                # Returns whether the option was removed or not
-                modified_something = parser.remove_option(section, name)
-
-            if modified_something:
-                # name removed from parser, section may now be empty
-                section_iter = iter(parser.items(section))
-                try:
-                    val = six.next(section_iter)
-                except StopIteration:
-                    val = None
-
-                if val is None:
-                    parser.remove_section(section)
-
-                self._mark_as_modified(fname, parser)
-            else:
-                raise ConfigurationError(
-                    "Fatal Internal error [id=1]. Please report as a bug."
-                )
-
-        del self._config[self.load_only][key]
-
-    def save(self):
-        # type: () -> None
-        """Save the currentin-memory state.
-        """
-        self._ensure_have_load_only()
-
-        for fname, parser in self._modified_parsers:
-            logger.info("Writing to %s", fname)
-
-            # Ensure directory exists.
-            ensure_dir(os.path.dirname(fname))
-
-            with open(fname, "w") as f:
-                parser.write(f)  # type: ignore
-
-    #
-    # Private routines
-    #
-
-    def _ensure_have_load_only(self):
-        # type: () -> None
-        if self.load_only is None:
-            raise ConfigurationError("Needed a specific file to be modifying.")
-        logger.debug("Will be working with %s variant only", self.load_only)
-
-    @property
-    def _dictionary(self):
-        # type: () -> Dict[str, Any]
-        """A dictionary representing the loaded configuration.
-        """
-        # NOTE: Dictionaries are not populated if not loaded. So, conditionals
-        #       are not needed here.
-        retval = {}
-
-        for variant in self._override_order:
-            retval.update(self._config[variant])
-
-        return retval
-
-    def _load_config_files(self):
-        # type: () -> None
-        """Loads configuration from configuration files
-        """
-        config_files = dict(self._iter_config_files())
-        if config_files[kinds.ENV][0:1] == [os.devnull]:
-            logger.debug(
-                "Skipping loading configuration files due to "
-                "environment's PIP_CONFIG_FILE being os.devnull"
-            )
-            return
-
-        for variant, files in config_files.items():
-            for fname in files:
-                # If there's specific variant set in `load_only`, load only
-                # that variant, not the others.
-                if self.load_only is not None and variant != self.load_only:
-                    logger.debug(
-                        "Skipping file '%s' (variant: %s)", fname, variant
-                    )
-                    continue
-
-                parser = self._load_file(variant, fname)
-
-                # Keeping track of the parsers used
-                self._parsers[variant].append((fname, parser))
-
-    def _load_file(self, variant, fname):
-        # type: (Kind, str) -> RawConfigParser
-        logger.debug("For variant '%s', will try loading '%s'", variant, fname)
-        parser = self._construct_parser(fname)
-
-        for section in parser.sections():
-            items = parser.items(section)
-            self._config[variant].update(self._normalized_keys(section, items))
-
-        return parser
-
-    def _construct_parser(self, fname):
-        # type: (str) -> RawConfigParser
-        parser = configparser.RawConfigParser()
-        # If there is no such file, don't bother reading it but create the
-        # parser anyway, to hold the data.
-        # Doing this is useful when modifying and saving files, where we don't
-        # need to construct a parser.
-        if os.path.exists(fname):
-            try:
-                parser.read(fname)
-            except UnicodeDecodeError:
-                # See https://github.com/pypa/pip/issues/4963
-                raise ConfigurationFileCouldNotBeLoaded(
-                    reason="contains invalid {} characters".format(
-                        locale.getpreferredencoding(False)
-                    ),
-                    fname=fname,
-                )
-            except configparser.Error as error:
-                # See https://github.com/pypa/pip/issues/4893
-                raise ConfigurationFileCouldNotBeLoaded(error=error)
-        return parser
-
-    def _load_environment_vars(self):
-        # type: () -> None
-        """Loads configuration from environment variables
-        """
-        self._config[kinds.ENV_VAR].update(
-            self._normalized_keys(":env:", self._get_environ_vars())
-        )
-
-    def _normalized_keys(self, section, items):
-        # type: (str, Iterable[Tuple[str, Any]]) -> Dict[str, Any]
-        """Normalizes items to construct a dictionary with normalized keys.
-
-        This routine is where the names become keys and are made the same
-        regardless of source - configuration files or environment.
-        """
-        normalized = {}
-        for name, val in items:
-            key = section + "." + _normalize_name(name)
-            normalized[key] = val
-        return normalized
-
-    def _get_environ_vars(self):
-        # type: () -> Iterable[Tuple[str, str]]
-        """Returns a generator with all environmental vars with prefix PIP_"""
-        for key, val in os.environ.items():
-            should_be_yielded = (
-                key.startswith("PIP_") and
-                key[4:].lower() not in self._ignore_env_names
-            )
-            if should_be_yielded:
-                yield key[4:].lower(), val
-
-    # XXX: This is patched in the tests.
-    def _iter_config_files(self):
-        # type: () -> Iterable[Tuple[Kind, List[str]]]
-        """Yields variant and configuration files associated with it.
-
-        This should be treated like items of a dictionary.
-        """
-        # SMELL: Move the conditions out of this function
-
-        # environment variables have the lowest priority
-        config_file = os.environ.get('PIP_CONFIG_FILE', None)
-        if config_file is not None:
-            yield kinds.ENV, [config_file]
-        else:
-            yield kinds.ENV, []
-
-        # at the base we have any global configuration
-        yield kinds.GLOBAL, list(site_config_files)
-
-        # per-user configuration next
-        should_load_user_config = not self.isolated and not (
-            config_file and os.path.exists(config_file)
-        )
-        if should_load_user_config:
-            # The legacy config file is overridden by the new config file
-            yield kinds.USER, [legacy_config_file, new_config_file]
-
-        # finally virtualenv configuration first trumping others
-        if running_under_virtualenv():
-            yield kinds.VENV, [venv_config_file]
-
-    def _get_parser_to_modify(self):
-        # type: () -> Tuple[str, RawConfigParser]
-        # Determine which parser to modify
-        parsers = self._parsers[self.load_only]
-        if not parsers:
-            # This should not happen if everything works correctly.
-            raise ConfigurationError(
-                "Fatal Internal error [id=2]. Please report as a bug."
-            )
-
-        # Use the highest priority parser.
-        return parsers[-1]
-
-    # XXX: This is patched in the tests.
-    def _mark_as_modified(self, fname, parser):
-        # type: (str, RawConfigParser) -> None
-        file_parser_tuple = (fname, parser)
-        if file_parser_tuple not in self._modified_parsers:
-            self._modified_parsers.append(file_parser_tuple)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/download.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/download.py
deleted file mode 100644
index 2bbe176..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/download.py
+++ /dev/null
@@ -1,971 +0,0 @@
-from __future__ import absolute_import
-
-import cgi
-import email.utils
-import getpass
-import json
-import logging
-import mimetypes
-import os
-import platform
-import re
-import shutil
-import sys
-
-from pip._vendor import requests, six, urllib3
-from pip._vendor.cachecontrol import CacheControlAdapter
-from pip._vendor.cachecontrol.caches import FileCache
-from pip._vendor.lockfile import LockError
-from pip._vendor.requests.adapters import BaseAdapter, HTTPAdapter
-from pip._vendor.requests.auth import AuthBase, HTTPBasicAuth
-from pip._vendor.requests.models import CONTENT_CHUNK_SIZE, Response
-from pip._vendor.requests.structures import CaseInsensitiveDict
-from pip._vendor.requests.utils import get_netrc_auth
-# NOTE: XMLRPC Client is not annotated in typeshed as on 2017-07-17, which is
-#       why we ignore the type on this import
-from pip._vendor.six.moves import xmlrpc_client  # type: ignore
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-from pip._vendor.six.moves.urllib import request as urllib_request
-from pip._vendor.urllib3.util import IS_PYOPENSSL
-
-import pip
-from pip._internal.exceptions import HashMismatch, InstallationError
-from pip._internal.locations import write_delete_marker_file
-from pip._internal.models.index import PyPI
-from pip._internal.utils.encoding import auto_decode
-from pip._internal.utils.filesystem import check_path_owner
-from pip._internal.utils.glibc import libc_ver
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import (
-    ARCHIVE_EXTENSIONS, ask_path_exists, backup_dir, call_subprocess, consume,
-    display_path, format_size, get_installed_version, rmtree,
-    split_auth_from_netloc, splitext, unpack_file,
-)
-from pip._internal.utils.setuptools_build import SETUPTOOLS_SHIM
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.utils.ui import DownloadProgressProvider
-from pip._internal.vcs import vcs
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Optional, Tuple, Dict, IO, Text, Union
-    )
-    from pip._internal.models.link import Link  # noqa: F401
-    from pip._internal.utils.hashes import Hashes  # noqa: F401
-    from pip._internal.vcs import AuthInfo  # noqa: F401
-
-try:
-    import ssl  # noqa
-except ImportError:
-    ssl = None
-
-HAS_TLS = (ssl is not None) or IS_PYOPENSSL
-
-__all__ = ['get_file_content',
-           'is_url', 'url_to_path', 'path_to_url',
-           'is_archive_file', 'unpack_vcs_link',
-           'unpack_file_url', 'is_vcs_url', 'is_file_url',
-           'unpack_http_url', 'unpack_url']
-
-
-logger = logging.getLogger(__name__)
-
-
-def user_agent():
-    """
-    Return a string representing the user agent.
-    """
-    data = {
-        "installer": {"name": "pip", "version": pip.__version__},
-        "python": platform.python_version(),
-        "implementation": {
-            "name": platform.python_implementation(),
-        },
-    }
-
-    if data["implementation"]["name"] == 'CPython':
-        data["implementation"]["version"] = platform.python_version()
-    elif data["implementation"]["name"] == 'PyPy':
-        if sys.pypy_version_info.releaselevel == 'final':
-            pypy_version_info = sys.pypy_version_info[:3]
-        else:
-            pypy_version_info = sys.pypy_version_info
-        data["implementation"]["version"] = ".".join(
-            [str(x) for x in pypy_version_info]
-        )
-    elif data["implementation"]["name"] == 'Jython':
-        # Complete Guess
-        data["implementation"]["version"] = platform.python_version()
-    elif data["implementation"]["name"] == 'IronPython':
-        # Complete Guess
-        data["implementation"]["version"] = platform.python_version()
-
-    if sys.platform.startswith("linux"):
-        from pip._vendor import distro
-        distro_infos = dict(filter(
-            lambda x: x[1],
-            zip(["name", "version", "id"], distro.linux_distribution()),
-        ))
-        libc = dict(filter(
-            lambda x: x[1],
-            zip(["lib", "version"], libc_ver()),
-        ))
-        if libc:
-            distro_infos["libc"] = libc
-        if distro_infos:
-            data["distro"] = distro_infos
-
-    if sys.platform.startswith("darwin") and platform.mac_ver()[0]:
-        data["distro"] = {"name": "macOS", "version": platform.mac_ver()[0]}
-
-    if platform.system():
-        data.setdefault("system", {})["name"] = platform.system()
-
-    if platform.release():
-        data.setdefault("system", {})["release"] = platform.release()
-
-    if platform.machine():
-        data["cpu"] = platform.machine()
-
-    if HAS_TLS:
-        data["openssl_version"] = ssl.OPENSSL_VERSION
-
-    setuptools_version = get_installed_version("setuptools")
-    if setuptools_version is not None:
-        data["setuptools_version"] = setuptools_version
-
-    return "{data[installer][name]}/{data[installer][version]} {json}".format(
-        data=data,
-        json=json.dumps(data, separators=(",", ":"), sort_keys=True),
-    )
-
-
-class MultiDomainBasicAuth(AuthBase):
-
-    def __init__(self, prompting=True):
-        # type: (bool) -> None
-        self.prompting = prompting
-        self.passwords = {}  # type: Dict[str, AuthInfo]
-
-    def __call__(self, req):
-        parsed = urllib_parse.urlparse(req.url)
-
-        # Split the credentials from the netloc.
-        netloc, url_user_password = split_auth_from_netloc(parsed.netloc)
-
-        # Set the url of the request to the url without any credentials
-        req.url = urllib_parse.urlunparse(parsed[:1] + (netloc,) + parsed[2:])
-
-        # Use any stored credentials that we have for this netloc
-        username, password = self.passwords.get(netloc, (None, None))
-
-        # Use the credentials embedded in the url if we have none stored
-        if username is None:
-            username, password = url_user_password
-
-        # Get creds from netrc if we still don't have them
-        if username is None and password is None:
-            netrc_auth = get_netrc_auth(req.url)
-            username, password = netrc_auth if netrc_auth else (None, None)
-
-        if username or password:
-            # Store the username and password
-            self.passwords[netloc] = (username, password)
-
-            # Send the basic auth with this request
-            req = HTTPBasicAuth(username or "", password or "")(req)
-
-        # Attach a hook to handle 401 responses
-        req.register_hook("response", self.handle_401)
-
-        return req
-
-    def handle_401(self, resp, **kwargs):
-        # We only care about 401 responses, anything else we want to just
-        #   pass through the actual response
-        if resp.status_code != 401:
-            return resp
-
-        # We are not able to prompt the user so simply return the response
-        if not self.prompting:
-            return resp
-
-        parsed = urllib_parse.urlparse(resp.url)
-
-        # Prompt the user for a new username and password
-        username = six.moves.input("User for %s: " % parsed.netloc)
-        password = getpass.getpass("Password: ")
-
-        # Store the new username and password to use for future requests
-        if username or password:
-            self.passwords[parsed.netloc] = (username, password)
-
-        # Consume content and release the original connection to allow our new
-        #   request to reuse the same one.
-        resp.content
-        resp.raw.release_conn()
-
-        # Add our new username and password to the request
-        req = HTTPBasicAuth(username or "", password or "")(resp.request)
-        req.register_hook("response", self.warn_on_401)
-
-        # Send our new request
-        new_resp = resp.connection.send(req, **kwargs)
-        new_resp.history.append(resp)
-
-        return new_resp
-
-    def warn_on_401(self, resp, **kwargs):
-        # warn user that they provided incorrect credentials
-        if resp.status_code == 401:
-            logger.warning('401 Error, Credentials not correct for %s',
-                           resp.request.url)
-
-
-class LocalFSAdapter(BaseAdapter):
-
-    def send(self, request, stream=None, timeout=None, verify=None, cert=None,
-             proxies=None):
-        pathname = url_to_path(request.url)
-
-        resp = Response()
-        resp.status_code = 200
-        resp.url = request.url
-
-        try:
-            stats = os.stat(pathname)
-        except OSError as exc:
-            resp.status_code = 404
-            resp.raw = exc
-        else:
-            modified = email.utils.formatdate(stats.st_mtime, usegmt=True)
-            content_type = mimetypes.guess_type(pathname)[0] or "text/plain"
-            resp.headers = CaseInsensitiveDict({
-                "Content-Type": content_type,
-                "Content-Length": stats.st_size,
-                "Last-Modified": modified,
-            })
-
-            resp.raw = open(pathname, "rb")
-            resp.close = resp.raw.close
-
-        return resp
-
-    def close(self):
-        pass
-
-
-class SafeFileCache(FileCache):
-    """
-    A file based cache which is safe to use even when the target directory may
-    not be accessible or writable.
-    """
-
-    def __init__(self, *args, **kwargs):
-        super(SafeFileCache, self).__init__(*args, **kwargs)
-
-        # Check to ensure that the directory containing our cache directory
-        # is owned by the user current executing pip. If it does not exist
-        # we will check the parent directory until we find one that does exist.
-        # If it is not owned by the user executing pip then we will disable
-        # the cache and log a warning.
-        if not check_path_owner(self.directory):
-            logger.warning(
-                "The directory '%s' or its parent directory is not owned by "
-                "the current user and the cache has been disabled. Please "
-                "check the permissions and owner of that directory. If "
-                "executing pip with sudo, you may want sudo's -H flag.",
-                self.directory,
-            )
-
-            # Set our directory to None to disable the Cache
-            self.directory = None
-
-    def get(self, *args, **kwargs):
-        # If we don't have a directory, then the cache should be a no-op.
-        if self.directory is None:
-            return
-
-        try:
-            return super(SafeFileCache, self).get(*args, **kwargs)
-        except (LockError, OSError, IOError):
-            # We intentionally silence this error, if we can't access the cache
-            # then we can just skip caching and process the request as if
-            # caching wasn't enabled.
-            pass
-
-    def set(self, *args, **kwargs):
-        # If we don't have a directory, then the cache should be a no-op.
-        if self.directory is None:
-            return
-
-        try:
-            return super(SafeFileCache, self).set(*args, **kwargs)
-        except (LockError, OSError, IOError):
-            # We intentionally silence this error, if we can't access the cache
-            # then we can just skip caching and process the request as if
-            # caching wasn't enabled.
-            pass
-
-    def delete(self, *args, **kwargs):
-        # If we don't have a directory, then the cache should be a no-op.
-        if self.directory is None:
-            return
-
-        try:
-            return super(SafeFileCache, self).delete(*args, **kwargs)
-        except (LockError, OSError, IOError):
-            # We intentionally silence this error, if we can't access the cache
-            # then we can just skip caching and process the request as if
-            # caching wasn't enabled.
-            pass
-
-
-class InsecureHTTPAdapter(HTTPAdapter):
-
-    def cert_verify(self, conn, url, verify, cert):
-        conn.cert_reqs = 'CERT_NONE'
-        conn.ca_certs = None
-
-
-class PipSession(requests.Session):
-
-    timeout = None  # type: Optional[int]
-
-    def __init__(self, *args, **kwargs):
-        retries = kwargs.pop("retries", 0)
-        cache = kwargs.pop("cache", None)
-        insecure_hosts = kwargs.pop("insecure_hosts", [])
-
-        super(PipSession, self).__init__(*args, **kwargs)
-
-        # Attach our User Agent to the request
-        self.headers["User-Agent"] = user_agent()
-
-        # Attach our Authentication handler to the session
-        self.auth = MultiDomainBasicAuth()
-
-        # Create our urllib3.Retry instance which will allow us to customize
-        # how we handle retries.
-        retries = urllib3.Retry(
-            # Set the total number of retries that a particular request can
-            # have.
-            total=retries,
-
-            # A 503 error from PyPI typically means that the Fastly -> Origin
-            # connection got interrupted in some way. A 503 error in general
-            # is typically considered a transient error so we'll go ahead and
-            # retry it.
-            # A 500 may indicate transient error in Amazon S3
-            # A 520 or 527 - may indicate transient error in CloudFlare
-            status_forcelist=[500, 503, 520, 527],
-
-            # Add a small amount of back off between failed requests in
-            # order to prevent hammering the service.
-            backoff_factor=0.25,
-        )
-
-        # We want to _only_ cache responses on securely fetched origins. We do
-        # this because we can't validate the response of an insecurely fetched
-        # origin, and we don't want someone to be able to poison the cache and
-        # require manual eviction from the cache to fix it.
-        if cache:
-            secure_adapter = CacheControlAdapter(
-                cache=SafeFileCache(cache, use_dir_lock=True),
-                max_retries=retries,
-            )
-        else:
-            secure_adapter = HTTPAdapter(max_retries=retries)
-
-        # Our Insecure HTTPAdapter disables HTTPS validation. It does not
-        # support caching (see above) so we'll use it for all http:// URLs as
-        # well as any https:// host that we've marked as ignoring TLS errors
-        # for.
-        insecure_adapter = InsecureHTTPAdapter(max_retries=retries)
-
-        self.mount("https://", secure_adapter)
-        self.mount("http://", insecure_adapter)
-
-        # Enable file:// urls
-        self.mount("file://", LocalFSAdapter())
-
-        # We want to use a non-validating adapter for any requests which are
-        # deemed insecure.
-        for host in insecure_hosts:
-            self.mount("https://{}/".format(host), insecure_adapter)
-
-    def request(self, method, url, *args, **kwargs):
-        # Allow setting a default timeout on a session
-        kwargs.setdefault("timeout", self.timeout)
-
-        # Dispatch the actual request
-        return super(PipSession, self).request(method, url, *args, **kwargs)
-
-
-def get_file_content(url, comes_from=None, session=None):
-    # type: (str, Optional[str], Optional[PipSession]) -> Tuple[str, Text]
-    """Gets the content of a file; it may be a filename, file: URL, or
-    http: URL.  Returns (location, content).  Content is unicode.
-
-    :param url:         File path or url.
-    :param comes_from:  Origin description of requirements.
-    :param session:     Instance of pip.download.PipSession.
-    """
-    if session is None:
-        raise TypeError(
-            "get_file_content() missing 1 required keyword argument: 'session'"
-        )
-
-    match = _scheme_re.search(url)
-    if match:
-        scheme = match.group(1).lower()
-        if (scheme == 'file' and comes_from and
-                comes_from.startswith('http')):
-            raise InstallationError(
-                'Requirements file %s references URL %s, which is local'
-                % (comes_from, url))
-        if scheme == 'file':
-            path = url.split(':', 1)[1]
-            path = path.replace('\\', '/')
-            match = _url_slash_drive_re.match(path)
-            if match:
-                path = match.group(1) + ':' + path.split('|', 1)[1]
-            path = urllib_parse.unquote(path)
-            if path.startswith('/'):
-                path = '/' + path.lstrip('/')
-            url = path
-        else:
-            # FIXME: catch some errors
-            resp = session.get(url)
-            resp.raise_for_status()
-            return resp.url, resp.text
-    try:
-        with open(url, 'rb') as f:
-            content = auto_decode(f.read())
-    except IOError as exc:
-        raise InstallationError(
-            'Could not open requirements file: %s' % str(exc)
-        )
-    return url, content
-
-
-_scheme_re = re.compile(r'^(http|https|file):', re.I)
-_url_slash_drive_re = re.compile(r'/*([a-z])\|', re.I)
-
-
-def is_url(name):
-    # type: (Union[str, Text]) -> bool
-    """Returns true if the name looks like a URL"""
-    if ':' not in name:
-        return False
-    scheme = name.split(':', 1)[0].lower()
-    return scheme in ['http', 'https', 'file', 'ftp'] + vcs.all_schemes
-
-
-def url_to_path(url):
-    # type: (str) -> str
-    """
-    Convert a file: URL to a path.
-    """
-    assert url.startswith('file:'), (
-        "You can only turn file: urls into filenames (not %r)" % url)
-
-    _, netloc, path, _, _ = urllib_parse.urlsplit(url)
-
-    # if we have a UNC path, prepend UNC share notation
-    if netloc:
-        netloc = '\\\\' + netloc
-
-    path = urllib_request.url2pathname(netloc + path)
-    return path
-
-
-def path_to_url(path):
-    # type: (Union[str, Text]) -> str
-    """
-    Convert a path to a file: URL.  The path will be made absolute and have
-    quoted path parts.
-    """
-    path = os.path.normpath(os.path.abspath(path))
-    url = urllib_parse.urljoin('file:', urllib_request.pathname2url(path))
-    return url
-
-
-def is_archive_file(name):
-    # type: (str) -> bool
-    """Return True if `name` is a considered as an archive file."""
-    ext = splitext(name)[1].lower()
-    if ext in ARCHIVE_EXTENSIONS:
-        return True
-    return False
-
-
-def unpack_vcs_link(link, location):
-    vcs_backend = _get_used_vcs_backend(link)
-    vcs_backend.unpack(location)
-
-
-def _get_used_vcs_backend(link):
-    for backend in vcs.backends:
-        if link.scheme in backend.schemes:
-            vcs_backend = backend(link.url)
-            return vcs_backend
-
-
-def is_vcs_url(link):
-    # type: (Link) -> bool
-    return bool(_get_used_vcs_backend(link))
-
-
-def is_file_url(link):
-    # type: (Link) -> bool
-    return link.url.lower().startswith('file:')
-
-
-def is_dir_url(link):
-    # type: (Link) -> bool
-    """Return whether a file:// Link points to a directory.
-
-    ``link`` must not have any other scheme but file://. Call is_file_url()
-    first.
-
-    """
-    link_path = url_to_path(link.url_without_fragment)
-    return os.path.isdir(link_path)
-
-
-def _progress_indicator(iterable, *args, **kwargs):
-    return iterable
-
-
-def _download_url(
-    resp,  # type: Response
-    link,  # type: Link
-    content_file,  # type: IO
-    hashes,  # type: Hashes
-    progress_bar  # type: str
-):
-    # type: (...) -> None
-    try:
-        total_length = int(resp.headers['content-length'])
-    except (ValueError, KeyError, TypeError):
-        total_length = 0
-
-    cached_resp = getattr(resp, "from_cache", False)
-    if logger.getEffectiveLevel() > logging.INFO:
-        show_progress = False
-    elif cached_resp:
-        show_progress = False
-    elif total_length > (40 * 1000):
-        show_progress = True
-    elif not total_length:
-        show_progress = True
-    else:
-        show_progress = False
-
-    show_url = link.show_url
-
-    def resp_read(chunk_size):
-        try:
-            # Special case for urllib3.
-            for chunk in resp.raw.stream(
-                    chunk_size,
-                    # We use decode_content=False here because we don't
-                    # want urllib3 to mess with the raw bytes we get
-                    # from the server. If we decompress inside of
-                    # urllib3 then we cannot verify the checksum
-                    # because the checksum will be of the compressed
-                    # file. This breakage will only occur if the
-                    # server adds a Content-Encoding header, which
-                    # depends on how the server was configured:
-                    # - Some servers will notice that the file isn't a
-                    #   compressible file and will leave the file alone
-                    #   and with an empty Content-Encoding
-                    # - Some servers will notice that the file is
-                    #   already compressed and will leave the file
-                    #   alone and will add a Content-Encoding: gzip
-                    #   header
-                    # - Some servers won't notice anything at all and
-                    #   will take a file that's already been compressed
-                    #   and compress it again and set the
-                    #   Content-Encoding: gzip header
-                    #
-                    # By setting this not to decode automatically we
-                    # hope to eliminate problems with the second case.
-                    decode_content=False):
-                yield chunk
-        except AttributeError:
-            # Standard file-like object.
-            while True:
-                chunk = resp.raw.read(chunk_size)
-                if not chunk:
-                    break
-                yield chunk
-
-    def written_chunks(chunks):
-        for chunk in chunks:
-            content_file.write(chunk)
-            yield chunk
-
-    progress_indicator = _progress_indicator
-
-    if link.netloc == PyPI.netloc:
-        url = show_url
-    else:
-        url = link.url_without_fragment
-
-    if show_progress:  # We don't show progress on cached responses
-        progress_indicator = DownloadProgressProvider(progress_bar,
-                                                      max=total_length)
-        if total_length:
-            logger.info("Downloading %s (%s)", url, format_size(total_length))
-        else:
-            logger.info("Downloading %s", url)
-    elif cached_resp:
-        logger.info("Using cached %s", url)
-    else:
-        logger.info("Downloading %s", url)
-
-    logger.debug('Downloading from URL %s', link)
-
-    downloaded_chunks = written_chunks(
-        progress_indicator(
-            resp_read(CONTENT_CHUNK_SIZE),
-            CONTENT_CHUNK_SIZE
-        )
-    )
-    if hashes:
-        hashes.check_against_chunks(downloaded_chunks)
-    else:
-        consume(downloaded_chunks)
-
-
-def _copy_file(filename, location, link):
-    copy = True
-    download_location = os.path.join(location, link.filename)
-    if os.path.exists(download_location):
-        response = ask_path_exists(
-            'The file %s exists. (i)gnore, (w)ipe, (b)ackup, (a)abort' %
-            display_path(download_location), ('i', 'w', 'b', 'a'))
-        if response == 'i':
-            copy = False
-        elif response == 'w':
-            logger.warning('Deleting %s', display_path(download_location))
-            os.remove(download_location)
-        elif response == 'b':
-            dest_file = backup_dir(download_location)
-            logger.warning(
-                'Backing up %s to %s',
-                display_path(download_location),
-                display_path(dest_file),
-            )
-            shutil.move(download_location, dest_file)
-        elif response == 'a':
-            sys.exit(-1)
-    if copy:
-        shutil.copy(filename, download_location)
-        logger.info('Saved %s', display_path(download_location))
-
-
-def unpack_http_url(
-    link,  # type: Link
-    location,  # type: str
-    download_dir=None,  # type: Optional[str]
-    session=None,  # type: Optional[PipSession]
-    hashes=None,  # type: Optional[Hashes]
-    progress_bar="on"  # type: str
-):
-    # type: (...) -> None
-    if session is None:
-        raise TypeError(
-            "unpack_http_url() missing 1 required keyword argument: 'session'"
-        )
-
-    with TempDirectory(kind="unpack") as temp_dir:
-        # If a download dir is specified, is the file already downloaded there?
-        already_downloaded_path = None
-        if download_dir:
-            already_downloaded_path = _check_download_dir(link,
-                                                          download_dir,
-                                                          hashes)
-
-        if already_downloaded_path:
-            from_path = already_downloaded_path
-            content_type = mimetypes.guess_type(from_path)[0]
-        else:
-            # let's download to a tmp dir
-            from_path, content_type = _download_http_url(link,
-                                                         session,
-                                                         temp_dir.path,
-                                                         hashes,
-                                                         progress_bar)
-
-        # unpack the archive to the build dir location. even when only
-        # downloading archives, they have to be unpacked to parse dependencies
-        unpack_file(from_path, location, content_type, link)
-
-        # a download dir is specified; let's copy the archive there
-        if download_dir and not already_downloaded_path:
-            _copy_file(from_path, download_dir, link)
-
-        if not already_downloaded_path:
-            os.unlink(from_path)
-
-
-def unpack_file_url(
-    link,  # type: Link
-    location,  # type: str
-    download_dir=None,  # type: Optional[str]
-    hashes=None  # type: Optional[Hashes]
-):
-    # type: (...) -> None
-    """Unpack link into location.
-
-    If download_dir is provided and link points to a file, make a copy
-    of the link file inside download_dir.
-    """
-    link_path = url_to_path(link.url_without_fragment)
-
-    # If it's a url to a local directory
-    if is_dir_url(link):
-        if os.path.isdir(location):
-            rmtree(location)
-        shutil.copytree(link_path, location, symlinks=True)
-        if download_dir:
-            logger.info('Link is a directory, ignoring download_dir')
-        return
-
-    # If --require-hashes is off, `hashes` is either empty, the
-    # link's embedded hash, or MissingHashes; it is required to
-    # match. If --require-hashes is on, we are satisfied by any
-    # hash in `hashes` matching: a URL-based or an option-based
-    # one; no internet-sourced hash will be in `hashes`.
-    if hashes:
-        hashes.check_against_path(link_path)
-
-    # If a download dir is specified, is the file already there and valid?
-    already_downloaded_path = None
-    if download_dir:
-        already_downloaded_path = _check_download_dir(link,
-                                                      download_dir,
-                                                      hashes)
-
-    if already_downloaded_path:
-        from_path = already_downloaded_path
-    else:
-        from_path = link_path
-
-    content_type = mimetypes.guess_type(from_path)[0]
-
-    # unpack the archive to the build dir location. even when only downloading
-    # archives, they have to be unpacked to parse dependencies
-    unpack_file(from_path, location, content_type, link)
-
-    # a download dir is specified and not already downloaded
-    if download_dir and not already_downloaded_path:
-        _copy_file(from_path, download_dir, link)
-
-
-def _copy_dist_from_dir(link_path, location):
-    """Copy distribution files in `link_path` to `location`.
-
-    Invoked when user requests to install a local directory. E.g.:
-
-        pip install .
-        pip install ~/dev/git-repos/python-prompt-toolkit
-
-    """
-
-    # Note: This is currently VERY SLOW if you have a lot of data in the
-    # directory, because it copies everything with `shutil.copytree`.
-    # What it should really do is build an sdist and install that.
-    # See https://github.com/pypa/pip/issues/2195
-
-    if os.path.isdir(location):
-        rmtree(location)
-
-    # build an sdist
-    setup_py = 'setup.py'
-    sdist_args = [sys.executable]
-    sdist_args.append('-c')
-    sdist_args.append(SETUPTOOLS_SHIM % setup_py)
-    sdist_args.append('sdist')
-    sdist_args += ['--dist-dir', location]
-    logger.info('Running setup.py sdist for %s', link_path)
-
-    with indent_log():
-        call_subprocess(sdist_args, cwd=link_path, show_stdout=False)
-
-    # unpack sdist into `location`
-    sdist = os.path.join(location, os.listdir(location)[0])
-    logger.info('Unpacking sdist %s into %s', sdist, location)
-    unpack_file(sdist, location, content_type=None, link=None)
-
-
-class PipXmlrpcTransport(xmlrpc_client.Transport):
-    """Provide a `xmlrpclib.Transport` implementation via a `PipSession`
-    object.
-    """
-
-    def __init__(self, index_url, session, use_datetime=False):
-        xmlrpc_client.Transport.__init__(self, use_datetime)
-        index_parts = urllib_parse.urlparse(index_url)
-        self._scheme = index_parts.scheme
-        self._session = session
-
-    def request(self, host, handler, request_body, verbose=False):
-        parts = (self._scheme, host, handler, None, None, None)
-        url = urllib_parse.urlunparse(parts)
-        try:
-            headers = {'Content-Type': 'text/xml'}
-            response = self._session.post(url, data=request_body,
-                                          headers=headers, stream=True)
-            response.raise_for_status()
-            self.verbose = verbose
-            return self.parse_response(response.raw)
-        except requests.HTTPError as exc:
-            logger.critical(
-                "HTTP error %s while getting %s",
-                exc.response.status_code, url,
-            )
-            raise
-
-
-def unpack_url(
-    link,  # type: Optional[Link]
-    location,  # type: Optional[str]
-    download_dir=None,  # type: Optional[str]
-    only_download=False,  # type: bool
-    session=None,  # type: Optional[PipSession]
-    hashes=None,  # type: Optional[Hashes]
-    progress_bar="on"  # type: str
-):
-    # type: (...) -> None
-    """Unpack link.
-       If link is a VCS link:
-         if only_download, export into download_dir and ignore location
-          else unpack into location
-       for other types of link:
-         - unpack into location
-         - if download_dir, copy the file into download_dir
-         - if only_download, mark location for deletion
-
-    :param hashes: A Hashes object, one of whose embedded hashes must match,
-        or HashMismatch will be raised. If the Hashes is empty, no matches are
-        required, and unhashable types of requirements (like VCS ones, which
-        would ordinarily raise HashUnsupported) are allowed.
-    """
-    # non-editable vcs urls
-    if is_vcs_url(link):
-        unpack_vcs_link(link, location)
-
-    # file urls
-    elif is_file_url(link):
-        unpack_file_url(link, location, download_dir, hashes=hashes)
-
-    # http urls
-    else:
-        if session is None:
-            session = PipSession()
-
-        unpack_http_url(
-            link,
-            location,
-            download_dir,
-            session,
-            hashes=hashes,
-            progress_bar=progress_bar
-        )
-    if only_download:
-        write_delete_marker_file(location)
-
-
-def _download_http_url(
-    link,  # type: Link
-    session,  # type: PipSession
-    temp_dir,  # type: str
-    hashes,  # type: Hashes
-    progress_bar  # type: str
-):
-    # type: (...) -> Tuple[str, str]
-    """Download link url into temp_dir using provided session"""
-    target_url = link.url.split('#', 1)[0]
-    try:
-        resp = session.get(
-            target_url,
-            # We use Accept-Encoding: identity here because requests
-            # defaults to accepting compressed responses. This breaks in
-            # a variety of ways depending on how the server is configured.
-            # - Some servers will notice that the file isn't a compressible
-            #   file and will leave the file alone and with an empty
-            #   Content-Encoding
-            # - Some servers will notice that the file is already
-            #   compressed and will leave the file alone and will add a
-            #   Content-Encoding: gzip header
-            # - Some servers won't notice anything at all and will take
-            #   a file that's already been compressed and compress it again
-            #   and set the Content-Encoding: gzip header
-            # By setting this to request only the identity encoding We're
-            # hoping to eliminate the third case. Hopefully there does not
-            # exist a server which when given a file will notice it is
-            # already compressed and that you're not asking for a
-            # compressed file and will then decompress it before sending
-            # because if that's the case I don't think it'll ever be
-            # possible to make this work.
-            headers={"Accept-Encoding": "identity"},
-            stream=True,
-        )
-        resp.raise_for_status()
-    except requests.HTTPError as exc:
-        logger.critical(
-            "HTTP error %s while getting %s", exc.response.status_code, link,
-        )
-        raise
-
-    content_type = resp.headers.get('content-type', '')
-    filename = link.filename  # fallback
-    # Have a look at the Content-Disposition header for a better guess
-    content_disposition = resp.headers.get('content-disposition')
-    if content_disposition:
-        type, params = cgi.parse_header(content_disposition)
-        # We use ``or`` here because we don't want to use an "empty" value
-        # from the filename param.
-        filename = params.get('filename') or filename
-    ext = splitext(filename)[1]
-    if not ext:
-        ext = mimetypes.guess_extension(content_type)
-        if ext:
-            filename += ext
-    if not ext and link.url != resp.url:
-        ext = os.path.splitext(resp.url)[1]
-        if ext:
-            filename += ext
-    file_path = os.path.join(temp_dir, filename)
-    with open(file_path, 'wb') as content_file:
-        _download_url(resp, link, content_file, hashes, progress_bar)
-    return file_path, content_type
-
-
-def _check_download_dir(link, download_dir, hashes):
-    # type: (Link, str, Hashes) -> Optional[str]
-    """ Check download_dir for previously downloaded file with correct hash
-        If a correct file is found return its path else None
-    """
-    download_path = os.path.join(download_dir, link.filename)
-    if os.path.exists(download_path):
-        # If already downloaded, does its hash match?
-        logger.info('File was already downloaded %s', download_path)
-        if hashes:
-            try:
-                hashes.check_against_path(download_path)
-            except HashMismatch:
-                logger.warning(
-                    'Previously-downloaded file %s has bad hash. '
-                    'Re-downloading.',
-                    download_path
-                )
-                os.unlink(download_path)
-                return None
-        return download_path
-    return None
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/exceptions.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/exceptions.py
deleted file mode 100644
index 38ceeea..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/exceptions.py
+++ /dev/null
@@ -1,274 +0,0 @@
-"""Exceptions used throughout package"""
-from __future__ import absolute_import
-
-from itertools import chain, groupby, repeat
-
-from pip._vendor.six import iteritems
-
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional  # noqa: F401
-    from pip._internal.req.req_install import InstallRequirement  # noqa: F401
-
-
-class PipError(Exception):
-    """Base pip exception"""
-
-
-class ConfigurationError(PipError):
-    """General exception in configuration"""
-
-
-class InstallationError(PipError):
-    """General exception during installation"""
-
-
-class UninstallationError(PipError):
-    """General exception during uninstallation"""
-
-
-class DistributionNotFound(InstallationError):
-    """Raised when a distribution cannot be found to satisfy a requirement"""
-
-
-class RequirementsFileParseError(InstallationError):
-    """Raised when a general error occurs parsing a requirements file line."""
-
-
-class BestVersionAlreadyInstalled(PipError):
-    """Raised when the most up-to-date version of a package is already
-    installed."""
-
-
-class BadCommand(PipError):
-    """Raised when virtualenv or a command is not found"""
-
-
-class CommandError(PipError):
-    """Raised when there is an error in command-line arguments"""
-
-
-class PreviousBuildDirError(PipError):
-    """Raised when there's a previous conflicting build directory"""
-
-
-class InvalidWheelFilename(InstallationError):
-    """Invalid wheel filename."""
-
-
-class UnsupportedWheel(InstallationError):
-    """Unsupported wheel."""
-
-
-class HashErrors(InstallationError):
-    """Multiple HashError instances rolled into one for reporting"""
-
-    def __init__(self):
-        self.errors = []
-
-    def append(self, error):
-        self.errors.append(error)
-
-    def __str__(self):
-        lines = []
-        self.errors.sort(key=lambda e: e.order)
-        for cls, errors_of_cls in groupby(self.errors, lambda e: e.__class__):
-            lines.append(cls.head)
-            lines.extend(e.body() for e in errors_of_cls)
-        if lines:
-            return '\n'.join(lines)
-
-    def __nonzero__(self):
-        return bool(self.errors)
-
-    def __bool__(self):
-        return self.__nonzero__()
-
-
-class HashError(InstallationError):
-    """
-    A failure to verify a package against known-good hashes
-
-    :cvar order: An int sorting hash exception classes by difficulty of
-        recovery (lower being harder), so the user doesn't bother fretting
-        about unpinned packages when he has deeper issues, like VCS
-        dependencies, to deal with. Also keeps error reports in a
-        deterministic order.
-    :cvar head: A section heading for display above potentially many
-        exceptions of this kind
-    :ivar req: The InstallRequirement that triggered this error. This is
-        pasted on after the exception is instantiated, because it's not
-        typically available earlier.
-
-    """
-    req = None  # type: Optional[InstallRequirement]
-    head = ''
-
-    def body(self):
-        """Return a summary of me for display under the heading.
-
-        This default implementation simply prints a description of the
-        triggering requirement.
-
-        :param req: The InstallRequirement that provoked this error, with
-            populate_link() having already been called
-
-        """
-        return '    %s' % self._requirement_name()
-
-    def __str__(self):
-        return '%s\n%s' % (self.head, self.body())
-
-    def _requirement_name(self):
-        """Return a description of the requirement that triggered me.
-
-        This default implementation returns long description of the req, with
-        line numbers
-
-        """
-        return str(self.req) if self.req else 'unknown package'
-
-
-class VcsHashUnsupported(HashError):
-    """A hash was provided for a version-control-system-based requirement, but
-    we don't have a method for hashing those."""
-
-    order = 0
-    head = ("Can't verify hashes for these requirements because we don't "
-            "have a way to hash version control repositories:")
-
-
-class DirectoryUrlHashUnsupported(HashError):
-    """A hash was provided for a version-control-system-based requirement, but
-    we don't have a method for hashing those."""
-
-    order = 1
-    head = ("Can't verify hashes for these file:// requirements because they "
-            "point to directories:")
-
-
-class HashMissing(HashError):
-    """A hash was needed for a requirement but is absent."""
-
-    order = 2
-    head = ('Hashes are required in --require-hashes mode, but they are '
-            'missing from some requirements. Here is a list of those '
-            'requirements along with the hashes their downloaded archives '
-            'actually had. Add lines like these to your requirements files to '
-            'prevent tampering. (If you did not enable --require-hashes '
-            'manually, note that it turns on automatically when any package '
-            'has a hash.)')
-
-    def __init__(self, gotten_hash):
-        """
-        :param gotten_hash: The hash of the (possibly malicious) archive we
-            just downloaded
-        """
-        self.gotten_hash = gotten_hash
-
-    def body(self):
-        # Dodge circular import.
-        from pip._internal.utils.hashes import FAVORITE_HASH
-
-        package = None
-        if self.req:
-            # In the case of URL-based requirements, display the original URL
-            # seen in the requirements file rather than the package name,
-            # so the output can be directly copied into the requirements file.
-            package = (self.req.original_link if self.req.original_link
-                       # In case someone feeds something downright stupid
-                       # to InstallRequirement's constructor.
-                       else getattr(self.req, 'req', None))
-        return '    %s --hash=%s:%s' % (package or 'unknown package',
-                                        FAVORITE_HASH,
-                                        self.gotten_hash)
-
-
-class HashUnpinned(HashError):
-    """A requirement had a hash specified but was not pinned to a specific
-    version."""
-
-    order = 3
-    head = ('In --require-hashes mode, all requirements must have their '
-            'versions pinned with ==. These do not:')
-
-
-class HashMismatch(HashError):
-    """
-    Distribution file hash values don't match.
-
-    :ivar package_name: The name of the package that triggered the hash
-        mismatch. Feel free to write to this after the exception is raise to
-        improve its error message.
-
-    """
-    order = 4
-    head = ('THESE PACKAGES DO NOT MATCH THE HASHES FROM THE REQUIREMENTS '
-            'FILE. If you have updated the package versions, please update '
-            'the hashes. Otherwise, examine the package contents carefully; '
-            'someone may have tampered with them.')
-
-    def __init__(self, allowed, gots):
-        """
-        :param allowed: A dict of algorithm names pointing to lists of allowed
-            hex digests
-        :param gots: A dict of algorithm names pointing to hashes we
-            actually got from the files under suspicion
-        """
-        self.allowed = allowed
-        self.gots = gots
-
-    def body(self):
-        return '    %s:\n%s' % (self._requirement_name(),
-                                self._hash_comparison())
-
-    def _hash_comparison(self):
-        """
-        Return a comparison of actual and expected hash values.
-
-        Example::
-
-               Expected sha256 abcdeabcdeabcdeabcdeabcdeabcdeabcdeabcdeabcde
-                            or 123451234512345123451234512345123451234512345
-                    Got        bcdefbcdefbcdefbcdefbcdefbcdefbcdefbcdefbcdef
-
-        """
-        def hash_then_or(hash_name):
-            # For now, all the decent hashes have 6-char names, so we can get
-            # away with hard-coding space literals.
-            return chain([hash_name], repeat('    or'))
-
-        lines = []
-        for hash_name, expecteds in iteritems(self.allowed):
-            prefix = hash_then_or(hash_name)
-            lines.extend(('        Expected %s %s' % (next(prefix), e))
-                         for e in expecteds)
-            lines.append('             Got        %s\n' %
-                         self.gots[hash_name].hexdigest())
-            prefix = '    or'
-        return '\n'.join(lines)
-
-
-class UnsupportedPythonVersion(InstallationError):
-    """Unsupported python version according to Requires-Python package
-    metadata."""
-
-
-class ConfigurationFileCouldNotBeLoaded(ConfigurationError):
-    """When there are errors while loading a configuration file
-    """
-
-    def __init__(self, reason="could not be loaded", fname=None, error=None):
-        super(ConfigurationFileCouldNotBeLoaded, self).__init__(error)
-        self.reason = reason
-        self.fname = fname
-        self.error = error
-
-    def __str__(self):
-        if self.fname is not None:
-            message_part = " in {}.".format(self.fname)
-        else:
-            assert self.error is not None
-            message_part = ".\n{}\n".format(self.error.message)
-        return "Configuration file {}{}".format(self.reason, message_part)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/index.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/index.py
deleted file mode 100644
index 9eda3a3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/index.py
+++ /dev/null
@@ -1,990 +0,0 @@
-"""Routines related to PyPI, indexes"""
-from __future__ import absolute_import
-
-import cgi
-import itertools
-import logging
-import mimetypes
-import os
-import posixpath
-import re
-import sys
-from collections import namedtuple
-
-from pip._vendor import html5lib, requests, six
-from pip._vendor.distlib.compat import unescape
-from pip._vendor.packaging import specifiers
-from pip._vendor.packaging.utils import canonicalize_name
-from pip._vendor.packaging.version import parse as parse_version
-from pip._vendor.requests.exceptions import RetryError, SSLError
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-from pip._vendor.six.moves.urllib import request as urllib_request
-
-from pip._internal.download import HAS_TLS, is_url, path_to_url, url_to_path
-from pip._internal.exceptions import (
-    BestVersionAlreadyInstalled, DistributionNotFound, InvalidWheelFilename,
-    UnsupportedWheel,
-)
-from pip._internal.models.candidate import InstallationCandidate
-from pip._internal.models.format_control import FormatControl
-from pip._internal.models.index import PyPI
-from pip._internal.models.link import Link
-from pip._internal.pep425tags import get_supported
-from pip._internal.utils.compat import ipaddress
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import (
-    ARCHIVE_EXTENSIONS, SUPPORTED_EXTENSIONS, WHEEL_EXTENSION, normalize_path,
-    redact_password_from_url,
-)
-from pip._internal.utils.packaging import check_requires_python
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.wheel import Wheel
-
-if MYPY_CHECK_RUNNING:
-    from logging import Logger  # noqa: F401
-    from typing import (  # noqa: F401
-        Tuple, Optional, Any, List, Union, Callable, Set, Sequence,
-        Iterable, MutableMapping
-    )
-    from pip._vendor.packaging.version import _BaseVersion  # noqa: F401
-    from pip._vendor.requests import Response  # noqa: F401
-    from pip._internal.req import InstallRequirement  # noqa: F401
-    from pip._internal.download import PipSession  # noqa: F401
-
-    SecureOrigin = Tuple[str, str, Optional[str]]
-    BuildTag = Tuple[Any, ...]  # either emply tuple or Tuple[int, str]
-    CandidateSortingKey = Tuple[int, _BaseVersion, BuildTag, Optional[int]]
-
-__all__ = ['FormatControl', 'PackageFinder']
-
-
-SECURE_ORIGINS = [
-    # protocol, hostname, port
-    # Taken from Chrome's list of secure origins (See: http://bit.ly/1qrySKC)
-    ("https", "*", "*"),
-    ("*", "localhost", "*"),
-    ("*", "127.0.0.0/8", "*"),
-    ("*", "::1/128", "*"),
-    ("file", "*", None),
-    # ssh is always secure.
-    ("ssh", "*", "*"),
-]  # type: List[SecureOrigin]
-
-
-logger = logging.getLogger(__name__)
-
-
-def _match_vcs_scheme(url):
-    # type: (str) -> Optional[str]
-    """Look for VCS schemes in the URL.
-
-    Returns the matched VCS scheme, or None if there's no match.
-    """
-    from pip._internal.vcs import VcsSupport
-    for scheme in VcsSupport.schemes:
-        if url.lower().startswith(scheme) and url[len(scheme)] in '+:':
-            return scheme
-    return None
-
-
-def _is_url_like_archive(url):
-    # type: (str) -> bool
-    """Return whether the URL looks like an archive.
-    """
-    filename = Link(url).filename
-    for bad_ext in ARCHIVE_EXTENSIONS:
-        if filename.endswith(bad_ext):
-            return True
-    return False
-
-
-class _NotHTML(Exception):
-    def __init__(self, content_type, request_desc):
-        # type: (str, str) -> None
-        super(_NotHTML, self).__init__(content_type, request_desc)
-        self.content_type = content_type
-        self.request_desc = request_desc
-
-
-def _ensure_html_header(response):
-    # type: (Response) -> None
-    """Check the Content-Type header to ensure the response contains HTML.
-
-    Raises `_NotHTML` if the content type is not text/html.
-    """
-    content_type = response.headers.get("Content-Type", "")
-    if not content_type.lower().startswith("text/html"):
-        raise _NotHTML(content_type, response.request.method)
-
-
-class _NotHTTP(Exception):
-    pass
-
-
-def _ensure_html_response(url, session):
-    # type: (str, PipSession) -> None
-    """Send a HEAD request to the URL, and ensure the response contains HTML.
-
-    Raises `_NotHTTP` if the URL is not available for a HEAD request, or
-    `_NotHTML` if the content type is not text/html.
-    """
-    scheme, netloc, path, query, fragment = urllib_parse.urlsplit(url)
-    if scheme not in {'http', 'https'}:
-        raise _NotHTTP()
-
-    resp = session.head(url, allow_redirects=True)
-    resp.raise_for_status()
-
-    _ensure_html_header(resp)
-
-
-def _get_html_response(url, session):
-    # type: (str, PipSession) -> Response
-    """Access an HTML page with GET, and return the response.
-
-    This consists of three parts:
-
-    1. If the URL looks suspiciously like an archive, send a HEAD first to
-       check the Content-Type is HTML, to avoid downloading a large file.
-       Raise `_NotHTTP` if the content type cannot be determined, or
-       `_NotHTML` if it is not HTML.
-    2. Actually perform the request. Raise HTTP exceptions on network failures.
-    3. Check the Content-Type header to make sure we got HTML, and raise
-       `_NotHTML` otherwise.
-    """
-    if _is_url_like_archive(url):
-        _ensure_html_response(url, session=session)
-
-    logger.debug('Getting page %s', url)
-
-    resp = session.get(
-        url,
-        headers={
-            "Accept": "text/html",
-            # We don't want to blindly returned cached data for
-            # /simple/, because authors generally expecting that
-            # twine upload && pip install will function, but if
-            # they've done a pip install in the last ~10 minutes
-            # it won't. Thus by setting this to zero we will not
-            # blindly use any cached data, however the benefit of
-            # using max-age=0 instead of no-cache, is that we will
-            # still support conditional requests, so we will still
-            # minimize traffic sent in cases where the page hasn't
-            # changed at all, we will just always incur the round
-            # trip for the conditional GET now instead of only
-            # once per 10 minutes.
-            # For more information, please see pypa/pip#5670.
-            "Cache-Control": "max-age=0",
-        },
-    )
-    resp.raise_for_status()
-
-    # The check for archives above only works if the url ends with
-    # something that looks like an archive. However that is not a
-    # requirement of an url. Unless we issue a HEAD request on every
-    # url we cannot know ahead of time for sure if something is HTML
-    # or not. However we can check after we've downloaded it.
-    _ensure_html_header(resp)
-
-    return resp
-
-
-def _handle_get_page_fail(
-    link,  # type: Link
-    reason,  # type: Union[str, Exception]
-    meth=None  # type: Optional[Callable[..., None]]
-):
-    # type: (...) -> None
-    if meth is None:
-        meth = logger.debug
-    meth("Could not fetch URL %s: %s - skipping", link, reason)
-
-
-def _get_html_page(link, session=None):
-    # type: (Link, Optional[PipSession]) -> Optional[HTMLPage]
-    if session is None:
-        raise TypeError(
-            "_get_html_page() missing 1 required keyword argument: 'session'"
-        )
-
-    url = link.url.split('#', 1)[0]
-
-    # Check for VCS schemes that do not support lookup as web pages.
-    vcs_scheme = _match_vcs_scheme(url)
-    if vcs_scheme:
-        logger.debug('Cannot look at %s URL %s', vcs_scheme, link)
-        return None
-
-    # Tack index.html onto file:// URLs that point to directories
-    scheme, _, path, _, _, _ = urllib_parse.urlparse(url)
-    if (scheme == 'file' and os.path.isdir(urllib_request.url2pathname(path))):
-        # add trailing slash if not present so urljoin doesn't trim
-        # final segment
-        if not url.endswith('/'):
-            url += '/'
-        url = urllib_parse.urljoin(url, 'index.html')
-        logger.debug(' file: URL is directory, getting %s', url)
-
-    try:
-        resp = _get_html_response(url, session=session)
-    except _NotHTTP as exc:
-        logger.debug(
-            'Skipping page %s because it looks like an archive, and cannot '
-            'be checked by HEAD.', link,
-        )
-    except _NotHTML as exc:
-        logger.debug(
-            'Skipping page %s because the %s request got Content-Type: %s',
-            link, exc.request_desc, exc.content_type,
-        )
-    except requests.HTTPError as exc:
-        _handle_get_page_fail(link, exc)
-    except RetryError as exc:
-        _handle_get_page_fail(link, exc)
-    except SSLError as exc:
-        reason = "There was a problem confirming the ssl certificate: "
-        reason += str(exc)
-        _handle_get_page_fail(link, reason, meth=logger.info)
-    except requests.ConnectionError as exc:
-        _handle_get_page_fail(link, "connection error: %s" % exc)
-    except requests.Timeout:
-        _handle_get_page_fail(link, "timed out")
-    else:
-        return HTMLPage(resp.content, resp.url, resp.headers)
-    return None
-
-
-class PackageFinder(object):
-    """This finds packages.
-
-    This is meant to match easy_install's technique for looking for
-    packages, by reading pages and looking for appropriate links.
-    """
-
-    def __init__(
-        self,
-        find_links,  # type: List[str]
-        index_urls,  # type: List[str]
-        allow_all_prereleases=False,  # type: bool
-        trusted_hosts=None,  # type: Optional[Iterable[str]]
-        session=None,  # type: Optional[PipSession]
-        format_control=None,  # type: Optional[FormatControl]
-        platform=None,  # type: Optional[str]
-        versions=None,  # type: Optional[List[str]]
-        abi=None,  # type: Optional[str]
-        implementation=None,  # type: Optional[str]
-        prefer_binary=False  # type: bool
-    ):
-        # type: (...) -> None
-        """Create a PackageFinder.
-
-        :param format_control: A FormatControl object or None. Used to control
-            the selection of source packages / binary packages when consulting
-            the index and links.
-        :param platform: A string or None. If None, searches for packages
-            that are supported by the current system. Otherwise, will find
-            packages that can be built on the platform passed in. These
-            packages will only be downloaded for distribution: they will
-            not be built locally.
-        :param versions: A list of strings or None. This is passed directly
-            to pep425tags.py in the get_supported() method.
-        :param abi: A string or None. This is passed directly
-            to pep425tags.py in the get_supported() method.
-        :param implementation: A string or None. This is passed directly
-            to pep425tags.py in the get_supported() method.
-        """
-        if session is None:
-            raise TypeError(
-                "PackageFinder() missing 1 required keyword argument: "
-                "'session'"
-            )
-
-        # Build find_links. If an argument starts with ~, it may be
-        # a local file relative to a home directory. So try normalizing
-        # it and if it exists, use the normalized version.
-        # This is deliberately conservative - it might be fine just to
-        # blindly normalize anything starting with a ~...
-        self.find_links = []  # type: List[str]
-        for link in find_links:
-            if link.startswith('~'):
-                new_link = normalize_path(link)
-                if os.path.exists(new_link):
-                    link = new_link
-            self.find_links.append(link)
-
-        self.index_urls = index_urls
-
-        # These are boring links that have already been logged somehow:
-        self.logged_links = set()  # type: Set[Link]
-
-        self.format_control = format_control or FormatControl(set(), set())
-
-        # Domains that we won't emit warnings for when not using HTTPS
-        self.secure_origins = [
-            ("*", host, "*")
-            for host in (trusted_hosts if trusted_hosts else [])
-        ]  # type: List[SecureOrigin]
-
-        # Do we want to allow _all_ pre-releases?
-        self.allow_all_prereleases = allow_all_prereleases
-
-        # The Session we'll use to make requests
-        self.session = session
-
-        # The valid tags to check potential found wheel candidates against
-        self.valid_tags = get_supported(
-            versions=versions,
-            platform=platform,
-            abi=abi,
-            impl=implementation,
-        )
-
-        # Do we prefer old, but valid, binary dist over new source dist
-        self.prefer_binary = prefer_binary
-
-        # If we don't have TLS enabled, then WARN if anyplace we're looking
-        # relies on TLS.
-        if not HAS_TLS:
-            for link in itertools.chain(self.index_urls, self.find_links):
-                parsed = urllib_parse.urlparse(link)
-                if parsed.scheme == "https":
-                    logger.warning(
-                        "pip is configured with locations that require "
-                        "TLS/SSL, however the ssl module in Python is not "
-                        "available."
-                    )
-                    break
-
-    def get_formatted_locations(self):
-        # type: () -> str
-        lines = []
-        if self.index_urls and self.index_urls != [PyPI.simple_url]:
-            lines.append(
-                "Looking in indexes: {}".format(", ".join(
-                    redact_password_from_url(url) for url in self.index_urls))
-            )
-        if self.find_links:
-            lines.append(
-                "Looking in links: {}".format(", ".join(self.find_links))
-            )
-        return "\n".join(lines)
-
-    @staticmethod
-    def _sort_locations(locations, expand_dir=False):
-        # type: (Sequence[str], bool) -> Tuple[List[str], List[str]]
-        """
-        Sort locations into "files" (archives) and "urls", and return
-        a pair of lists (files,urls)
-        """
-        files = []
-        urls = []
-
-        # puts the url for the given file path into the appropriate list
-        def sort_path(path):
-            url = path_to_url(path)
-            if mimetypes.guess_type(url, strict=False)[0] == 'text/html':
-                urls.append(url)
-            else:
-                files.append(url)
-
-        for url in locations:
-
-            is_local_path = os.path.exists(url)
-            is_file_url = url.startswith('file:')
-
-            if is_local_path or is_file_url:
-                if is_local_path:
-                    path = url
-                else:
-                    path = url_to_path(url)
-                if os.path.isdir(path):
-                    if expand_dir:
-                        path = os.path.realpath(path)
-                        for item in os.listdir(path):
-                            sort_path(os.path.join(path, item))
-                    elif is_file_url:
-                        urls.append(url)
-                    else:
-                        logger.warning(
-                            "Path '{0}' is ignored: "
-                            "it is a directory.".format(path),
-                        )
-                elif os.path.isfile(path):
-                    sort_path(path)
-                else:
-                    logger.warning(
-                        "Url '%s' is ignored: it is neither a file "
-                        "nor a directory.", url,
-                    )
-            elif is_url(url):
-                # Only add url with clear scheme
-                urls.append(url)
-            else:
-                logger.warning(
-                    "Url '%s' is ignored. It is either a non-existing "
-                    "path or lacks a specific scheme.", url,
-                )
-
-        return files, urls
-
-    def _candidate_sort_key(self, candidate):
-        # type: (InstallationCandidate) -> CandidateSortingKey
-        """
-        Function used to generate link sort key for link tuples.
-        The greater the return value, the more preferred it is.
-        If not finding wheels, then sorted by version only.
-        If finding wheels, then the sort order is by version, then:
-          1. existing installs
-          2. wheels ordered via Wheel.support_index_min(self.valid_tags)
-          3. source archives
-        If prefer_binary was set, then all wheels are sorted above sources.
-        Note: it was considered to embed this logic into the Link
-              comparison operators, but then different sdist links
-              with the same version, would have to be considered equal
-        """
-        support_num = len(self.valid_tags)
-        build_tag = tuple()  # type: BuildTag
-        binary_preference = 0
-        if candidate.location.is_wheel:
-            # can raise InvalidWheelFilename
-            wheel = Wheel(candidate.location.filename)
-            if not wheel.supported(self.valid_tags):
-                raise UnsupportedWheel(
-                    "%s is not a supported wheel for this platform. It "
-                    "can't be sorted." % wheel.filename
-                )
-            if self.prefer_binary:
-                binary_preference = 1
-            pri = -(wheel.support_index_min(self.valid_tags))
-            if wheel.build_tag is not None:
-                match = re.match(r'^(\d+)(.*)$', wheel.build_tag)
-                build_tag_groups = match.groups()
-                build_tag = (int(build_tag_groups[0]), build_tag_groups[1])
-        else:  # sdist
-            pri = -(support_num)
-        return (binary_preference, candidate.version, build_tag, pri)
-
-    def _validate_secure_origin(self, logger, location):
-        # type: (Logger, Link) -> bool
-        # Determine if this url used a secure transport mechanism
-        parsed = urllib_parse.urlparse(str(location))
-        origin = (parsed.scheme, parsed.hostname, parsed.port)
-
-        # The protocol to use to see if the protocol matches.
-        # Don't count the repository type as part of the protocol: in
-        # cases such as "git+ssh", only use "ssh". (I.e., Only verify against
-        # the last scheme.)
-        protocol = origin[0].rsplit('+', 1)[-1]
-
-        # Determine if our origin is a secure origin by looking through our
-        # hardcoded list of secure origins, as well as any additional ones
-        # configured on this PackageFinder instance.
-        for secure_origin in (SECURE_ORIGINS + self.secure_origins):
-            if protocol != secure_origin[0] and secure_origin[0] != "*":
-                continue
-
-            try:
-                # We need to do this decode dance to ensure that we have a
-                # unicode object, even on Python 2.x.
-                addr = ipaddress.ip_address(
-                    origin[1]
-                    if (
-                        isinstance(origin[1], six.text_type) or
-                        origin[1] is None
-                    )
-                    else origin[1].decode("utf8")
-                )
-                network = ipaddress.ip_network(
-                    secure_origin[1]
-                    if isinstance(secure_origin[1], six.text_type)
-                    # setting secure_origin[1] to proper Union[bytes, str]
-                    # creates problems in other places
-                    else secure_origin[1].decode("utf8")  # type: ignore
-                )
-            except ValueError:
-                # We don't have both a valid address or a valid network, so
-                # we'll check this origin against hostnames.
-                if (origin[1] and
-                        origin[1].lower() != secure_origin[1].lower() and
-                        secure_origin[1] != "*"):
-                    continue
-            else:
-                # We have a valid address and network, so see if the address
-                # is contained within the network.
-                if addr not in network:
-                    continue
-
-            # Check to see if the port patches
-            if (origin[2] != secure_origin[2] and
-                    secure_origin[2] != "*" and
-                    secure_origin[2] is not None):
-                continue
-
-            # If we've gotten here, then this origin matches the current
-            # secure origin and we should return True
-            return True
-
-        # If we've gotten to this point, then the origin isn't secure and we
-        # will not accept it as a valid location to search. We will however
-        # log a warning that we are ignoring it.
-        logger.warning(
-            "The repository located at %s is not a trusted or secure host and "
-            "is being ignored. If this repository is available via HTTPS we "
-            "recommend you use HTTPS instead, otherwise you may silence "
-            "this warning and allow it anyway with '--trusted-host %s'.",
-            parsed.hostname,
-            parsed.hostname,
-        )
-
-        return False
-
-    def _get_index_urls_locations(self, project_name):
-        # type: (str) -> List[str]
-        """Returns the locations found via self.index_urls
-
-        Checks the url_name on the main (first in the list) index and
-        use this url_name to produce all locations
-        """
-
-        def mkurl_pypi_url(url):
-            loc = posixpath.join(
-                url,
-                urllib_parse.quote(canonicalize_name(project_name)))
-            # For maximum compatibility with easy_install, ensure the path
-            # ends in a trailing slash.  Although this isn't in the spec
-            # (and PyPI can handle it without the slash) some other index
-            # implementations might break if they relied on easy_install's
-            # behavior.
-            if not loc.endswith('/'):
-                loc = loc + '/'
-            return loc
-
-        return [mkurl_pypi_url(url) for url in self.index_urls]
-
-    def find_all_candidates(self, project_name):
-        # type: (str) -> List[Optional[InstallationCandidate]]
-        """Find all available InstallationCandidate for project_name
-
-        This checks index_urls and find_links.
-        All versions found are returned as an InstallationCandidate list.
-
-        See _link_package_versions for details on which files are accepted
-        """
-        index_locations = self._get_index_urls_locations(project_name)
-        index_file_loc, index_url_loc = self._sort_locations(index_locations)
-        fl_file_loc, fl_url_loc = self._sort_locations(
-            self.find_links, expand_dir=True,
-        )
-
-        file_locations = (Link(url) for url in itertools.chain(
-            index_file_loc, fl_file_loc,
-        ))
-
-        # We trust every url that the user has given us whether it was given
-        #   via --index-url or --find-links.
-        # We want to filter out any thing which does not have a secure origin.
-        url_locations = [
-            link for link in itertools.chain(
-                (Link(url) for url in index_url_loc),
-                (Link(url) for url in fl_url_loc),
-            )
-            if self._validate_secure_origin(logger, link)
-        ]
-
-        logger.debug('%d location(s) to search for versions of %s:',
-                     len(url_locations), project_name)
-
-        for location in url_locations:
-            logger.debug('* %s', location)
-
-        canonical_name = canonicalize_name(project_name)
-        formats = self.format_control.get_allowed_formats(canonical_name)
-        search = Search(project_name, canonical_name, formats)
-        find_links_versions = self._package_versions(
-            # We trust every directly linked archive in find_links
-            (Link(url, '-f') for url in self.find_links),
-            search
-        )
-
-        page_versions = []
-        for page in self._get_pages(url_locations, project_name):
-            logger.debug('Analyzing links from page %s', page.url)
-            with indent_log():
-                page_versions.extend(
-                    self._package_versions(page.iter_links(), search)
-                )
-
-        file_versions = self._package_versions(file_locations, search)
-        if file_versions:
-            file_versions.sort(reverse=True)
-            logger.debug(
-                'Local files found: %s',
-                ', '.join([
-                    url_to_path(candidate.location.url)
-                    for candidate in file_versions
-                ])
-            )
-
-        # This is an intentional priority ordering
-        return file_versions + find_links_versions + page_versions
-
-    def find_requirement(self, req, upgrade):
-        # type: (InstallRequirement, bool) -> Optional[Link]
-        """Try to find a Link matching req
-
-        Expects req, an InstallRequirement and upgrade, a boolean
-        Returns a Link if found,
-        Raises DistributionNotFound or BestVersionAlreadyInstalled otherwise
-        """
-        all_candidates = self.find_all_candidates(req.name)
-
-        # Filter out anything which doesn't match our specifier
-        compatible_versions = set(
-            req.specifier.filter(
-                # We turn the version object into a str here because otherwise
-                # when we're debundled but setuptools isn't, Python will see
-                # packaging.version.Version and
-                # pkg_resources._vendor.packaging.version.Version as different
-                # types. This way we'll use a str as a common data interchange
-                # format. If we stop using the pkg_resources provided specifier
-                # and start using our own, we can drop the cast to str().
-                [str(c.version) for c in all_candidates],
-                prereleases=(
-                    self.allow_all_prereleases
-                    if self.allow_all_prereleases else None
-                ),
-            )
-        )
-        applicable_candidates = [
-            # Again, converting to str to deal with debundling.
-            c for c in all_candidates if str(c.version) in compatible_versions
-        ]
-
-        if applicable_candidates:
-            best_candidate = max(applicable_candidates,
-                                 key=self._candidate_sort_key)
-        else:
-            best_candidate = None
-
-        if req.satisfied_by is not None:
-            installed_version = parse_version(req.satisfied_by.version)
-        else:
-            installed_version = None
-
-        if installed_version is None and best_candidate is None:
-            logger.critical(
-                'Could not find a version that satisfies the requirement %s '
-                '(from versions: %s)',
-                req,
-                ', '.join(
-                    sorted(
-                        {str(c.version) for c in all_candidates},
-                        key=parse_version,
-                    )
-                )
-            )
-
-            raise DistributionNotFound(
-                'No matching distribution found for %s' % req
-            )
-
-        best_installed = False
-        if installed_version and (
-                best_candidate is None or
-                best_candidate.version <= installed_version):
-            best_installed = True
-
-        if not upgrade and installed_version is not None:
-            if best_installed:
-                logger.debug(
-                    'Existing installed version (%s) is most up-to-date and '
-                    'satisfies requirement',
-                    installed_version,
-                )
-            else:
-                logger.debug(
-                    'Existing installed version (%s) satisfies requirement '
-                    '(most up-to-date version is %s)',
-                    installed_version,
-                    best_candidate.version,
-                )
-            return None
-
-        if best_installed:
-            # We have an existing version, and its the best version
-            logger.debug(
-                'Installed version (%s) is most up-to-date (past versions: '
-                '%s)',
-                installed_version,
-                ', '.join(sorted(compatible_versions, key=parse_version)) or
-                "none",
-            )
-            raise BestVersionAlreadyInstalled
-
-        logger.debug(
-            'Using version %s (newest of versions: %s)',
-            best_candidate.version,
-            ', '.join(sorted(compatible_versions, key=parse_version))
-        )
-        return best_candidate.location
-
-    def _get_pages(self, locations, project_name):
-        # type: (Iterable[Link], str) -> Iterable[HTMLPage]
-        """
-        Yields (page, page_url) from the given locations, skipping
-        locations that have errors.
-        """
-        seen = set()  # type: Set[Link]
-        for location in locations:
-            if location in seen:
-                continue
-            seen.add(location)
-
-            page = _get_html_page(location, session=self.session)
-            if page is None:
-                continue
-
-            yield page
-
-    _py_version_re = re.compile(r'-py([123]\.?[0-9]?)$')
-
-    def _sort_links(self, links):
-        # type: (Iterable[Link]) -> List[Link]
-        """
-        Returns elements of links in order, non-egg links first, egg links
-        second, while eliminating duplicates
-        """
-        eggs, no_eggs = [], []
-        seen = set()  # type: Set[Link]
-        for link in links:
-            if link not in seen:
-                seen.add(link)
-                if link.egg_fragment:
-                    eggs.append(link)
-                else:
-                    no_eggs.append(link)
-        return no_eggs + eggs
-
-    def _package_versions(
-        self,
-        links,  # type: Iterable[Link]
-        search  # type: Search
-    ):
-        # type: (...) -> List[Optional[InstallationCandidate]]
-        result = []
-        for link in self._sort_links(links):
-            v = self._link_package_versions(link, search)
-            if v is not None:
-                result.append(v)
-        return result
-
-    def _log_skipped_link(self, link, reason):
-        # type: (Link, str) -> None
-        if link not in self.logged_links:
-            logger.debug('Skipping link %s; %s', link, reason)
-            self.logged_links.add(link)
-
-    def _link_package_versions(self, link, search):
-        # type: (Link, Search) -> Optional[InstallationCandidate]
-        """Return an InstallationCandidate or None"""
-        version = None
-        if link.egg_fragment:
-            egg_info = link.egg_fragment
-            ext = link.ext
-        else:
-            egg_info, ext = link.splitext()
-            if not ext:
-                self._log_skipped_link(link, 'not a file')
-                return None
-            if ext not in SUPPORTED_EXTENSIONS:
-                self._log_skipped_link(
-                    link, 'unsupported archive format: %s' % ext,
-                )
-                return None
-            if "binary" not in search.formats and ext == WHEEL_EXTENSION:
-                self._log_skipped_link(
-                    link, 'No binaries permitted for %s' % search.supplied,
-                )
-                return None
-            if "macosx10" in link.path and ext == '.zip':
-                self._log_skipped_link(link, 'macosx10 one')
-                return None
-            if ext == WHEEL_EXTENSION:
-                try:
-                    wheel = Wheel(link.filename)
-                except InvalidWheelFilename:
-                    self._log_skipped_link(link, 'invalid wheel filename')
-                    return None
-                if canonicalize_name(wheel.name) != search.canonical:
-                    self._log_skipped_link(
-                        link, 'wrong project name (not %s)' % search.supplied)
-                    return None
-
-                if not wheel.supported(self.valid_tags):
-                    self._log_skipped_link(
-                        link, 'it is not compatible with this Python')
-                    return None
-
-                version = wheel.version
-
-        # This should be up by the search.ok_binary check, but see issue 2700.
-        if "source" not in search.formats and ext != WHEEL_EXTENSION:
-            self._log_skipped_link(
-                link, 'No sources permitted for %s' % search.supplied,
-            )
-            return None
-
-        if not version:
-            version = _egg_info_matches(egg_info, search.canonical)
-        if not version:
-            self._log_skipped_link(
-                link, 'Missing project version for %s' % search.supplied)
-            return None
-
-        match = self._py_version_re.search(version)
-        if match:
-            version = version[:match.start()]
-            py_version = match.group(1)
-            if py_version != sys.version[:3]:
-                self._log_skipped_link(
-                    link, 'Python version is incorrect')
-                return None
-        try:
-            support_this_python = check_requires_python(link.requires_python)
-        except specifiers.InvalidSpecifier:
-            logger.debug("Package %s has an invalid Requires-Python entry: %s",
-                         link.filename, link.requires_python)
-            support_this_python = True
-
-        if not support_this_python:
-            logger.debug("The package %s is incompatible with the python "
-                         "version in use. Acceptable python versions are: %s",
-                         link, link.requires_python)
-            return None
-        logger.debug('Found link %s, version: %s', link, version)
-
-        return InstallationCandidate(search.supplied, version, link)
-
-
-def _find_name_version_sep(egg_info, canonical_name):
-    # type: (str, str) -> int
-    """Find the separator's index based on the package's canonical name.
-
-    `egg_info` must be an egg info string for the given package, and
-    `canonical_name` must be the package's canonical name.
-
-    This function is needed since the canonicalized name does not necessarily
-    have the same length as the egg info's name part. An example::
-
-    >>> egg_info = 'foo__bar-1.0'
-    >>> canonical_name = 'foo-bar'
-    >>> _find_name_version_sep(egg_info, canonical_name)
-    8
-    """
-    # Project name and version must be separated by one single dash. Find all
-    # occurrences of dashes; if the string in front of it matches the canonical
-    # name, this is the one separating the name and version parts.
-    for i, c in enumerate(egg_info):
-        if c != "-":
-            continue
-        if canonicalize_name(egg_info[:i]) == canonical_name:
-            return i
-    raise ValueError("{} does not match {}".format(egg_info, canonical_name))
-
-
-def _egg_info_matches(egg_info, canonical_name):
-    # type: (str, str) -> Optional[str]
-    """Pull the version part out of a string.
-
-    :param egg_info: The string to parse. E.g. foo-2.1
-    :param canonical_name: The canonicalized name of the package this
-        belongs to.
-    """
-    try:
-        version_start = _find_name_version_sep(egg_info, canonical_name) + 1
-    except ValueError:
-        return None
-    version = egg_info[version_start:]
-    if not version:
-        return None
-    return version
-
-
-def _determine_base_url(document, page_url):
-    """Determine the HTML document's base URL.
-
-    This looks for a ``<base>`` tag in the HTML document. If present, its href
-    attribute denotes the base URL of anchor tags in the document. If there is
-    no such tag (or if it does not have a valid href attribute), the HTML
-    file's URL is used as the base URL.
-
-    :param document: An HTML document representation. The current
-        implementation expects the result of ``html5lib.parse()``.
-    :param page_url: The URL of the HTML document.
-    """
-    for base in document.findall(".//base"):
-        href = base.get("href")
-        if href is not None:
-            return href
-    return page_url
-
-
-def _get_encoding_from_headers(headers):
-    """Determine if we have any encoding information in our headers.
-    """
-    if headers and "Content-Type" in headers:
-        content_type, params = cgi.parse_header(headers["Content-Type"])
-        if "charset" in params:
-            return params['charset']
-    return None
-
-
-_CLEAN_LINK_RE = re.compile(r'[^a-z0-9$&+,/:;=?@.#%_\\|-]', re.I)
-
-
-def _clean_link(url):
-    # type: (str) -> str
-    """Makes sure a link is fully encoded.  That is, if a ' ' shows up in
-    the link, it will be rewritten to %20 (while not over-quoting
-    % or other characters)."""
-    return _CLEAN_LINK_RE.sub(lambda match: '%%%2x' % ord(match.group(0)), url)
-
-
-class HTMLPage(object):
-    """Represents one page, along with its URL"""
-
-    def __init__(self, content, url, headers=None):
-        # type: (bytes, str, MutableMapping[str, str]) -> None
-        self.content = content
-        self.url = url
-        self.headers = headers
-
-    def __str__(self):
-        return redact_password_from_url(self.url)
-
-    def iter_links(self):
-        # type: () -> Iterable[Link]
-        """Yields all links in the page"""
-        document = html5lib.parse(
-            self.content,
-            transport_encoding=_get_encoding_from_headers(self.headers),
-            namespaceHTMLElements=False,
-        )
-        base_url = _determine_base_url(document, self.url)
-        for anchor in document.findall(".//a"):
-            if anchor.get("href"):
-                href = anchor.get("href")
-                url = _clean_link(urllib_parse.urljoin(base_url, href))
-                pyrequire = anchor.get('data-requires-python')
-                pyrequire = unescape(pyrequire) if pyrequire else None
-                yield Link(url, self.url, requires_python=pyrequire)
-
-
-Search = namedtuple('Search', 'supplied canonical formats')
-"""Capture key aspects of a search.
-
-:attribute supplied: The user supplied package.
-:attribute canonical: The canonical package name.
-:attribute formats: The formats allowed for this package. Should be a set
-    with 'binary' or 'source' or both in it.
-"""
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/locations.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/locations.py
deleted file mode 100644
index c6e2a3e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/locations.py
+++ /dev/null
@@ -1,211 +0,0 @@
-"""Locations where we look for configs, install stuff, etc"""
-from __future__ import absolute_import
-
-import os
-import os.path
-import platform
-import site
-import sys
-import sysconfig
-from distutils import sysconfig as distutils_sysconfig
-from distutils.command.install import SCHEME_KEYS  # type: ignore
-
-from pip._internal.utils import appdirs
-from pip._internal.utils.compat import WINDOWS, expanduser
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Any, Union, Dict, List, Optional  # noqa: F401
-
-
-# Application Directories
-USER_CACHE_DIR = appdirs.user_cache_dir("pip")
-
-
-DELETE_MARKER_MESSAGE = '''\
-This file is placed here by pip to indicate the source was put
-here by pip.
-
-Once this package is successfully installed this source code will be
-deleted (unless you remove this file).
-'''
-PIP_DELETE_MARKER_FILENAME = 'pip-delete-this-directory.txt'
-
-
-def write_delete_marker_file(directory):
-    # type: (str) -> None
-    """
-    Write the pip delete marker file into this directory.
-    """
-    filepath = os.path.join(directory, PIP_DELETE_MARKER_FILENAME)
-    with open(filepath, 'w') as marker_fp:
-        marker_fp.write(DELETE_MARKER_MESSAGE)
-
-
-def running_under_virtualenv():
-    # type: () -> bool
-    """
-    Return True if we're running inside a virtualenv, False otherwise.
-
-    """
-    if hasattr(sys, 'real_prefix'):
-        return True
-    elif sys.prefix != getattr(sys, "base_prefix", sys.prefix):
-        return True
-
-    return False
-
-
-def virtualenv_no_global():
-    # type: () -> bool
-    """
-    Return True if in a venv and no system site packages.
-    """
-    # this mirrors the logic in virtualenv.py for locating the
-    # no-global-site-packages.txt file
-    site_mod_dir = os.path.dirname(os.path.abspath(site.__file__))
-    no_global_file = os.path.join(site_mod_dir, 'no-global-site-packages.txt')
-    if running_under_virtualenv() and os.path.isfile(no_global_file):
-        return True
-    else:
-        return False
-
-
-if running_under_virtualenv():
-    src_prefix = os.path.join(sys.prefix, 'src')
-else:
-    # FIXME: keep src in cwd for now (it is not a temporary folder)
-    try:
-        src_prefix = os.path.join(os.getcwd(), 'src')
-    except OSError:
-        # In case the current working directory has been renamed or deleted
-        sys.exit(
-            "The folder you are executing pip from can no longer be found."
-        )
-
-# under macOS + virtualenv sys.prefix is not properly resolved
-# it is something like /path/to/python/bin/..
-# Note: using realpath due to tmp dirs on OSX being symlinks
-src_prefix = os.path.abspath(src_prefix)
-
-# FIXME doesn't account for venv linked to global site-packages
-
-site_packages = sysconfig.get_path("purelib")  # type: Optional[str]
-
-# This is because of a bug in PyPy's sysconfig module, see
-# https://bitbucket.org/pypy/pypy/issues/2506/sysconfig-returns-incorrect-paths
-# for more information.
-if platform.python_implementation().lower() == "pypy":
-    site_packages = distutils_sysconfig.get_python_lib()
-try:
-    # Use getusersitepackages if this is present, as it ensures that the
-    # value is initialised properly.
-    user_site = site.getusersitepackages()
-except AttributeError:
-    user_site = site.USER_SITE
-user_dir = expanduser('~')
-if WINDOWS:
-    bin_py = os.path.join(sys.prefix, 'Scripts')
-    bin_user = os.path.join(user_site, 'Scripts')
-    # buildout uses 'bin' on Windows too?
-    if not os.path.exists(bin_py):
-        bin_py = os.path.join(sys.prefix, 'bin')
-        bin_user = os.path.join(user_site, 'bin')
-
-    config_basename = 'pip.ini'
-
-    legacy_storage_dir = os.path.join(user_dir, 'pip')
-    legacy_config_file = os.path.join(
-        legacy_storage_dir,
-        config_basename,
-    )
-else:
-    bin_py = os.path.join(sys.prefix, 'bin')
-    bin_user = os.path.join(user_site, 'bin')
-
-    config_basename = 'pip.conf'
-
-    legacy_storage_dir = os.path.join(user_dir, '.pip')
-    legacy_config_file = os.path.join(
-        legacy_storage_dir,
-        config_basename,
-    )
-    # Forcing to use /usr/local/bin for standard macOS framework installs
-    # Also log to ~/Library/Logs/ for use with the Console.app log viewer
-    if sys.platform[:6] == 'darwin' and sys.prefix[:16] == '/System/Library/':
-        bin_py = '/usr/local/bin'
-
-site_config_files = [
-    os.path.join(path, config_basename)
-    for path in appdirs.site_config_dirs('pip')
-]
-
-venv_config_file = os.path.join(sys.prefix, config_basename)
-new_config_file = os.path.join(appdirs.user_config_dir("pip"), config_basename)
-
-
-def distutils_scheme(dist_name, user=False, home=None, root=None,
-                     isolated=False, prefix=None):
-    # type:(str, bool, str, str, bool, str) -> dict
-    """
-    Return a distutils install scheme
-    """
-    from distutils.dist import Distribution
-
-    scheme = {}
-
-    if isolated:
-        extra_dist_args = {"script_args": ["--no-user-cfg"]}
-    else:
-        extra_dist_args = {}
-    dist_args = {'name': dist_name}  # type: Dict[str, Union[str, List[str]]]
-    dist_args.update(extra_dist_args)
-
-    d = Distribution(dist_args)
-    # Ignoring, typeshed issue reported python/typeshed/issues/2567
-    d.parse_config_files()
-    # NOTE: Ignoring type since mypy can't find attributes on 'Command'
-    i = d.get_command_obj('install', create=True)  # type: Any
-    assert i is not None
-    # NOTE: setting user or home has the side-effect of creating the home dir
-    # or user base for installations during finalize_options()
-    # ideally, we'd prefer a scheme class that has no side-effects.
-    assert not (user and prefix), "user={} prefix={}".format(user, prefix)
-    i.user = user or i.user
-    if user:
-        i.prefix = ""
-    i.prefix = prefix or i.prefix
-    i.home = home or i.home
-    i.root = root or i.root
-    i.finalize_options()
-    for key in SCHEME_KEYS:
-        scheme[key] = getattr(i, 'install_' + key)
-
-    # install_lib specified in setup.cfg should install *everything*
-    # into there (i.e. it takes precedence over both purelib and
-    # platlib).  Note, i.install_lib is *always* set after
-    # finalize_options(); we only want to override here if the user
-    # has explicitly requested it hence going back to the config
-
-    # Ignoring, typeshed issue reported python/typeshed/issues/2567
-    if 'install_lib' in d.get_option_dict('install'):  # type: ignore
-        scheme.update(dict(purelib=i.install_lib, platlib=i.install_lib))
-
-    if running_under_virtualenv():
-        scheme['headers'] = os.path.join(
-            sys.prefix,
-            'include',
-            'site',
-            'python' + sys.version[:3],
-            dist_name,
-        )
-
-        if root is not None:
-            path_no_drive = os.path.splitdrive(
-                os.path.abspath(scheme["headers"]))[1]
-            scheme["headers"] = os.path.join(
-                root,
-                path_no_drive[1:],
-            )
-
-    return scheme
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__init__.py
deleted file mode 100644
index 7855226..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__init__.py
+++ /dev/null
@@ -1,2 +0,0 @@
-"""A package that contains models that represent entities.
-"""
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 8b92b6b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/candidate.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/candidate.cpython-37.pyc
deleted file mode 100644
index 445bffe..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/candidate.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/format_control.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/format_control.cpython-37.pyc
deleted file mode 100644
index 304897a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/format_control.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/index.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/index.cpython-37.pyc
deleted file mode 100644
index cad3ad0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/index.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/link.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/link.cpython-37.pyc
deleted file mode 100644
index e74697d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/__pycache__/link.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/candidate.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/candidate.py
deleted file mode 100644
index 4475458..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/candidate.py
+++ /dev/null
@@ -1,31 +0,0 @@
-from pip._vendor.packaging.version import parse as parse_version
-
-from pip._internal.utils.models import KeyBasedCompareMixin
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from pip._vendor.packaging.version import _BaseVersion  # noqa: F401
-    from pip._internal.models.link import Link  # noqa: F401
-    from typing import Any, Union  # noqa: F401
-
-
-class InstallationCandidate(KeyBasedCompareMixin):
-    """Represents a potential "candidate" for installation.
-    """
-
-    def __init__(self, project, version, location):
-        # type: (Any, str, Link) -> None
-        self.project = project
-        self.version = parse_version(version)  # type: _BaseVersion
-        self.location = location
-
-        super(InstallationCandidate, self).__init__(
-            key=(self.project, self.version, self.location),
-            defining_class=InstallationCandidate
-        )
-
-    def __repr__(self):
-        # type: () -> str
-        return "<InstallationCandidate({!r}, {!r}, {!r})>".format(
-            self.project, self.version, self.location,
-        )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/format_control.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/format_control.py
deleted file mode 100644
index 971a391..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/format_control.py
+++ /dev/null
@@ -1,73 +0,0 @@
-from pip._vendor.packaging.utils import canonicalize_name
-
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional, Set, FrozenSet  # noqa: F401
-
-
-class FormatControl(object):
-    """Helper for managing formats from which a package can be installed.
-    """
-
-    def __init__(self, no_binary=None, only_binary=None):
-        # type: (Optional[Set], Optional[Set]) -> None
-        if no_binary is None:
-            no_binary = set()
-        if only_binary is None:
-            only_binary = set()
-
-        self.no_binary = no_binary
-        self.only_binary = only_binary
-
-    def __eq__(self, other):
-        return self.__dict__ == other.__dict__
-
-    def __ne__(self, other):
-        return not self.__eq__(other)
-
-    def __repr__(self):
-        return "{}({}, {})".format(
-            self.__class__.__name__,
-            self.no_binary,
-            self.only_binary
-        )
-
-    @staticmethod
-    def handle_mutual_excludes(value, target, other):
-        # type: (str, Optional[Set], Optional[Set]) -> None
-        new = value.split(',')
-        while ':all:' in new:
-            other.clear()
-            target.clear()
-            target.add(':all:')
-            del new[:new.index(':all:') + 1]
-            # Without a none, we want to discard everything as :all: covers it
-            if ':none:' not in new:
-                return
-        for name in new:
-            if name == ':none:':
-                target.clear()
-                continue
-            name = canonicalize_name(name)
-            other.discard(name)
-            target.add(name)
-
-    def get_allowed_formats(self, canonical_name):
-        # type: (str) -> FrozenSet
-        result = {"binary", "source"}
-        if canonical_name in self.only_binary:
-            result.discard('source')
-        elif canonical_name in self.no_binary:
-            result.discard('binary')
-        elif ':all:' in self.only_binary:
-            result.discard('source')
-        elif ':all:' in self.no_binary:
-            result.discard('binary')
-        return frozenset(result)
-
-    def disallow_binaries(self):
-        # type: () -> None
-        self.handle_mutual_excludes(
-            ':all:', self.no_binary, self.only_binary,
-        )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/index.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/index.py
deleted file mode 100644
index ead1efb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/index.py
+++ /dev/null
@@ -1,31 +0,0 @@
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-
-
-class PackageIndex(object):
-    """Represents a Package Index and provides easier access to endpoints
-    """
-
-    def __init__(self, url, file_storage_domain):
-        # type: (str, str) -> None
-        super(PackageIndex, self).__init__()
-        self.url = url
-        self.netloc = urllib_parse.urlsplit(url).netloc
-        self.simple_url = self._url_for_path('simple')
-        self.pypi_url = self._url_for_path('pypi')
-
-        # This is part of a temporary hack used to block installs of PyPI
-        # packages which depend on external urls only necessary until PyPI can
-        # block such packages themselves
-        self.file_storage_domain = file_storage_domain
-
-    def _url_for_path(self, path):
-        # type: (str) -> str
-        return urllib_parse.urljoin(self.url, path)
-
-
-PyPI = PackageIndex(
-    'https://pypi.org/', file_storage_domain='files.pythonhosted.org'
-)
-TestPyPI = PackageIndex(
-    'https://test.pypi.org/', file_storage_domain='test-files.pythonhosted.org'
-)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/link.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/link.py
deleted file mode 100644
index ad2f93e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/models/link.py
+++ /dev/null
@@ -1,163 +0,0 @@
-import posixpath
-import re
-
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-
-from pip._internal.download import path_to_url
-from pip._internal.utils.misc import (
-    WHEEL_EXTENSION, redact_password_from_url, splitext,
-)
-from pip._internal.utils.models import KeyBasedCompareMixin
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional, Tuple, Union, Text  # noqa: F401
-    from pip._internal.index import HTMLPage  # noqa: F401
-
-
-class Link(KeyBasedCompareMixin):
-    """Represents a parsed link from a Package Index's simple URL
-    """
-
-    def __init__(self, url, comes_from=None, requires_python=None):
-        # type: (str, Optional[Union[str, HTMLPage]], Optional[str]) -> None
-        """
-        url:
-            url of the resource pointed to (href of the link)
-        comes_from:
-            instance of HTMLPage where the link was found, or string.
-        requires_python:
-            String containing the `Requires-Python` metadata field, specified
-            in PEP 345. This may be specified by a data-requires-python
-            attribute in the HTML link tag, as described in PEP 503.
-        """
-
-        # url can be a UNC windows share
-        if url.startswith('\\\\'):
-            url = path_to_url(url)
-
-        self.url = url
-        self.comes_from = comes_from
-        self.requires_python = requires_python if requires_python else None
-
-        super(Link, self).__init__(
-            key=(self.url),
-            defining_class=Link
-        )
-
-    def __str__(self):
-        if self.requires_python:
-            rp = ' (requires-python:%s)' % self.requires_python
-        else:
-            rp = ''
-        if self.comes_from:
-            return '%s (from %s)%s' % (redact_password_from_url(self.url),
-                                       self.comes_from, rp)
-        else:
-            return redact_password_from_url(str(self.url))
-
-    def __repr__(self):
-        return '<Link %s>' % self
-
-    @property
-    def filename(self):
-        # type: () -> str
-        _, netloc, path, _, _ = urllib_parse.urlsplit(self.url)
-        name = posixpath.basename(path.rstrip('/')) or netloc
-        name = urllib_parse.unquote(name)
-        assert name, ('URL %r produced no filename' % self.url)
-        return name
-
-    @property
-    def scheme(self):
-        # type: () -> str
-        return urllib_parse.urlsplit(self.url)[0]
-
-    @property
-    def netloc(self):
-        # type: () -> str
-        return urllib_parse.urlsplit(self.url)[1]
-
-    @property
-    def path(self):
-        # type: () -> str
-        return urllib_parse.unquote(urllib_parse.urlsplit(self.url)[2])
-
-    def splitext(self):
-        # type: () -> Tuple[str, str]
-        return splitext(posixpath.basename(self.path.rstrip('/')))
-
-    @property
-    def ext(self):
-        # type: () -> str
-        return self.splitext()[1]
-
-    @property
-    def url_without_fragment(self):
-        # type: () -> str
-        scheme, netloc, path, query, fragment = urllib_parse.urlsplit(self.url)
-        return urllib_parse.urlunsplit((scheme, netloc, path, query, None))
-
-    _egg_fragment_re = re.compile(r'[#&]egg=([^&]*)')
-
-    @property
-    def egg_fragment(self):
-        # type: () -> Optional[str]
-        match = self._egg_fragment_re.search(self.url)
-        if not match:
-            return None
-        return match.group(1)
-
-    _subdirectory_fragment_re = re.compile(r'[#&]subdirectory=([^&]*)')
-
-    @property
-    def subdirectory_fragment(self):
-        # type: () -> Optional[str]
-        match = self._subdirectory_fragment_re.search(self.url)
-        if not match:
-            return None
-        return match.group(1)
-
-    _hash_re = re.compile(
-        r'(sha1|sha224|sha384|sha256|sha512|md5)=([a-f0-9]+)'
-    )
-
-    @property
-    def hash(self):
-        # type: () -> Optional[str]
-        match = self._hash_re.search(self.url)
-        if match:
-            return match.group(2)
-        return None
-
-    @property
-    def hash_name(self):
-        # type: () -> Optional[str]
-        match = self._hash_re.search(self.url)
-        if match:
-            return match.group(1)
-        return None
-
-    @property
-    def show_url(self):
-        # type: () -> Optional[str]
-        return posixpath.basename(self.url.split('#', 1)[0].split('?', 1)[0])
-
-    @property
-    def is_wheel(self):
-        # type: () -> bool
-        return self.ext == WHEEL_EXTENSION
-
-    @property
-    def is_artifact(self):
-        # type: () -> bool
-        """
-        Determines if this points to an actual artifact (e.g. a tarball) or if
-        it points to an "abstract" thing like a path or a VCS location.
-        """
-        from pip._internal.vcs import vcs
-
-        if self.scheme in vcs.all_schemes:
-            return False
-
-        return True
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 07a1eb7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/check.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/check.cpython-37.pyc
deleted file mode 100644
index a85fd1b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/check.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/freeze.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/freeze.cpython-37.pyc
deleted file mode 100644
index 7d8bed4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/freeze.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/prepare.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/prepare.cpython-37.pyc
deleted file mode 100644
index 952f933..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/__pycache__/prepare.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/check.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/check.py
deleted file mode 100644
index 0b56eda..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/check.py
+++ /dev/null
@@ -1,155 +0,0 @@
-"""Validation of dependencies of packages
-"""
-
-import logging
-from collections import namedtuple
-
-from pip._vendor.packaging.utils import canonicalize_name
-from pip._vendor.pkg_resources import RequirementParseError
-
-from pip._internal.operations.prepare import make_abstract_dist
-from pip._internal.utils.misc import get_installed_distributions
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-logger = logging.getLogger(__name__)
-
-if MYPY_CHECK_RUNNING:
-    from pip._internal.req.req_install import InstallRequirement  # noqa: F401
-    from typing import (  # noqa: F401
-        Any, Callable, Dict, Optional, Set, Tuple, List
-    )
-
-    # Shorthands
-    PackageSet = Dict[str, 'PackageDetails']
-    Missing = Tuple[str, Any]
-    Conflicting = Tuple[str, str, Any]
-
-    MissingDict = Dict[str, List[Missing]]
-    ConflictingDict = Dict[str, List[Conflicting]]
-    CheckResult = Tuple[MissingDict, ConflictingDict]
-
-PackageDetails = namedtuple('PackageDetails', ['version', 'requires'])
-
-
-def create_package_set_from_installed(**kwargs):
-    # type: (**Any) -> Tuple[PackageSet, bool]
-    """Converts a list of distributions into a PackageSet.
-    """
-    # Default to using all packages installed on the system
-    if kwargs == {}:
-        kwargs = {"local_only": False, "skip": ()}
-
-    package_set = {}
-    problems = False
-    for dist in get_installed_distributions(**kwargs):
-        name = canonicalize_name(dist.project_name)
-        try:
-            package_set[name] = PackageDetails(dist.version, dist.requires())
-        except RequirementParseError as e:
-            # Don't crash on broken metadata
-            logging.warning("Error parsing requirements for %s: %s", name, e)
-            problems = True
-    return package_set, problems
-
-
-def check_package_set(package_set, should_ignore=None):
-    # type: (PackageSet, Optional[Callable[[str], bool]]) -> CheckResult
-    """Check if a package set is consistent
-
-    If should_ignore is passed, it should be a callable that takes a
-    package name and returns a boolean.
-    """
-    if should_ignore is None:
-        def should_ignore(name):
-            return False
-
-    missing = dict()
-    conflicting = dict()
-
-    for package_name in package_set:
-        # Info about dependencies of package_name
-        missing_deps = set()  # type: Set[Missing]
-        conflicting_deps = set()  # type: Set[Conflicting]
-
-        if should_ignore(package_name):
-            continue
-
-        for req in package_set[package_name].requires:
-            name = canonicalize_name(req.project_name)  # type: str
-
-            # Check if it's missing
-            if name not in package_set:
-                missed = True
-                if req.marker is not None:
-                    missed = req.marker.evaluate()
-                if missed:
-                    missing_deps.add((name, req))
-                continue
-
-            # Check if there's a conflict
-            version = package_set[name].version  # type: str
-            if not req.specifier.contains(version, prereleases=True):
-                conflicting_deps.add((name, version, req))
-
-        if missing_deps:
-            missing[package_name] = sorted(missing_deps, key=str)
-        if conflicting_deps:
-            conflicting[package_name] = sorted(conflicting_deps, key=str)
-
-    return missing, conflicting
-
-
-def check_install_conflicts(to_install):
-    # type: (List[InstallRequirement]) -> Tuple[PackageSet, CheckResult]
-    """For checking if the dependency graph would be consistent after \
-    installing given requirements
-    """
-    # Start from the current state
-    package_set, _ = create_package_set_from_installed()
-    # Install packages
-    would_be_installed = _simulate_installation_of(to_install, package_set)
-
-    # Only warn about directly-dependent packages; create a whitelist of them
-    whitelist = _create_whitelist(would_be_installed, package_set)
-
-    return (
-        package_set,
-        check_package_set(
-            package_set, should_ignore=lambda name: name not in whitelist
-        )
-    )
-
-
-def _simulate_installation_of(to_install, package_set):
-    # type: (List[InstallRequirement], PackageSet) -> Set[str]
-    """Computes the version of packages after installing to_install.
-    """
-
-    # Keep track of packages that were installed
-    installed = set()
-
-    # Modify it as installing requirement_set would (assuming no errors)
-    for inst_req in to_install:
-        dist = make_abstract_dist(inst_req).dist()
-        name = canonicalize_name(dist.key)
-        package_set[name] = PackageDetails(dist.version, dist.requires())
-
-        installed.add(name)
-
-    return installed
-
-
-def _create_whitelist(would_be_installed, package_set):
-    # type: (Set[str], PackageSet) -> Set[str]
-    packages_affected = set(would_be_installed)
-
-    for package_name in package_set:
-        if package_name in packages_affected:
-            continue
-
-        for req in package_set[package_name].requires:
-            if canonicalize_name(req.name) in packages_affected:
-                packages_affected.add(package_name)
-                break
-
-    return packages_affected
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/freeze.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/freeze.py
deleted file mode 100644
index 388bb73..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/freeze.py
+++ /dev/null
@@ -1,247 +0,0 @@
-from __future__ import absolute_import
-
-import collections
-import logging
-import os
-import re
-
-from pip._vendor import six
-from pip._vendor.packaging.utils import canonicalize_name
-from pip._vendor.pkg_resources import RequirementParseError
-
-from pip._internal.exceptions import BadCommand, InstallationError
-from pip._internal.req.constructors import (
-    install_req_from_editable, install_req_from_line,
-)
-from pip._internal.req.req_file import COMMENT_RE
-from pip._internal.utils.misc import (
-    dist_is_editable, get_installed_distributions,
-)
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Iterator, Optional, List, Container, Set, Dict, Tuple, Iterable, Union
-    )
-    from pip._internal.cache import WheelCache  # noqa: F401
-    from pip._vendor.pkg_resources import (  # noqa: F401
-        Distribution, Requirement
-    )
-
-    RequirementInfo = Tuple[Optional[Union[str, Requirement]], bool, List[str]]
-
-
-logger = logging.getLogger(__name__)
-
-
-def freeze(
-    requirement=None,  # type: Optional[List[str]]
-    find_links=None,  # type: Optional[List[str]]
-    local_only=None,  # type: Optional[bool]
-    user_only=None,  # type: Optional[bool]
-    skip_regex=None,  # type: Optional[str]
-    isolated=False,  # type: bool
-    wheel_cache=None,  # type: Optional[WheelCache]
-    exclude_editable=False,  # type: bool
-    skip=()  # type: Container[str]
-):
-    # type: (...) -> Iterator[str]
-    find_links = find_links or []
-    skip_match = None
-
-    if skip_regex:
-        skip_match = re.compile(skip_regex).search
-
-    for link in find_links:
-        yield '-f %s' % link
-    installations = {}  # type: Dict[str, FrozenRequirement]
-    for dist in get_installed_distributions(local_only=local_only,
-                                            skip=(),
-                                            user_only=user_only):
-        try:
-            req = FrozenRequirement.from_dist(dist)
-        except RequirementParseError:
-            logger.warning(
-                "Could not parse requirement: %s",
-                dist.project_name
-            )
-            continue
-        if exclude_editable and req.editable:
-            continue
-        installations[req.name] = req
-
-    if requirement:
-        # the options that don't get turned into an InstallRequirement
-        # should only be emitted once, even if the same option is in multiple
-        # requirements files, so we need to keep track of what has been emitted
-        # so that we don't emit it again if it's seen again
-        emitted_options = set()  # type: Set[str]
-        # keep track of which files a requirement is in so that we can
-        # give an accurate warning if a requirement appears multiple times.
-        req_files = collections.defaultdict(list)  # type: Dict[str, List[str]]
-        for req_file_path in requirement:
-            with open(req_file_path) as req_file:
-                for line in req_file:
-                    if (not line.strip() or
-                            line.strip().startswith('#') or
-                            (skip_match and skip_match(line)) or
-                            line.startswith((
-                                '-r', '--requirement',
-                                '-Z', '--always-unzip',
-                                '-f', '--find-links',
-                                '-i', '--index-url',
-                                '--pre',
-                                '--trusted-host',
-                                '--process-dependency-links',
-                                '--extra-index-url'))):
-                        line = line.rstrip()
-                        if line not in emitted_options:
-                            emitted_options.add(line)
-                            yield line
-                        continue
-
-                    if line.startswith('-e') or line.startswith('--editable'):
-                        if line.startswith('-e'):
-                            line = line[2:].strip()
-                        else:
-                            line = line[len('--editable'):].strip().lstrip('=')
-                        line_req = install_req_from_editable(
-                            line,
-                            isolated=isolated,
-                            wheel_cache=wheel_cache,
-                        )
-                    else:
-                        line_req = install_req_from_line(
-                            COMMENT_RE.sub('', line).strip(),
-                            isolated=isolated,
-                            wheel_cache=wheel_cache,
-                        )
-
-                    if not line_req.name:
-                        logger.info(
-                            "Skipping line in requirement file [%s] because "
-                            "it's not clear what it would install: %s",
-                            req_file_path, line.strip(),
-                        )
-                        logger.info(
-                            "  (add #egg=PackageName to the URL to avoid"
-                            " this warning)"
-                        )
-                    elif line_req.name not in installations:
-                        # either it's not installed, or it is installed
-                        # but has been processed already
-                        if not req_files[line_req.name]:
-                            logger.warning(
-                                "Requirement file [%s] contains %s, but "
-                                "package %r is not installed",
-                                req_file_path,
-                                COMMENT_RE.sub('', line).strip(), line_req.name
-                            )
-                        else:
-                            req_files[line_req.name].append(req_file_path)
-                    else:
-                        yield str(installations[line_req.name]).rstrip()
-                        del installations[line_req.name]
-                        req_files[line_req.name].append(req_file_path)
-
-        # Warn about requirements that were included multiple times (in a
-        # single requirements file or in different requirements files).
-        for name, files in six.iteritems(req_files):
-            if len(files) > 1:
-                logger.warning("Requirement %s included multiple times [%s]",
-                               name, ', '.join(sorted(set(files))))
-
-        yield(
-            '## The following requirements were added by '
-            'pip freeze:'
-        )
-    for installation in sorted(
-            installations.values(), key=lambda x: x.name.lower()):
-        if canonicalize_name(installation.name) not in skip:
-            yield str(installation).rstrip()
-
-
-def get_requirement_info(dist):
-    # type: (Distribution) -> RequirementInfo
-    """
-    Compute and return values (req, editable, comments) for use in
-    FrozenRequirement.from_dist().
-    """
-    if not dist_is_editable(dist):
-        return (None, False, [])
-
-    location = os.path.normcase(os.path.abspath(dist.location))
-
-    from pip._internal.vcs import vcs, RemoteNotFoundError
-    vc_type = vcs.get_backend_type(location)
-
-    if not vc_type:
-        req = dist.as_requirement()
-        logger.debug(
-            'No VCS found for editable requirement {!r} in: {!r}', req,
-            location,
-        )
-        comments = [
-            '# Editable install with no version control ({})'.format(req)
-        ]
-        return (location, True, comments)
-
-    try:
-        req = vc_type.get_src_requirement(location, dist.project_name)
-    except RemoteNotFoundError:
-        req = dist.as_requirement()
-        comments = [
-            '# Editable {} install with no remote ({})'.format(
-                vc_type.__name__, req,
-            )
-        ]
-        return (location, True, comments)
-
-    except BadCommand:
-        logger.warning(
-            'cannot determine version of editable source in %s '
-            '(%s command not found in path)',
-            location,
-            vc_type.name,
-        )
-        return (None, True, [])
-
-    except InstallationError as exc:
-        logger.warning(
-            "Error when trying to get requirement for VCS system %s, "
-            "falling back to uneditable format", exc
-        )
-    else:
-        if req is not None:
-            return (req, True, [])
-
-    logger.warning(
-        'Could not determine repository location of %s', location
-    )
-    comments = ['## !! Could not determine repository location']
-
-    return (None, False, comments)
-
-
-class FrozenRequirement(object):
-    def __init__(self, name, req, editable, comments=()):
-        # type: (str, Union[str, Requirement], bool, Iterable[str]) -> None
-        self.name = name
-        self.req = req
-        self.editable = editable
-        self.comments = comments
-
-    @classmethod
-    def from_dist(cls, dist):
-        # type: (Distribution) -> FrozenRequirement
-        req, editable, comments = get_requirement_info(dist)
-        if req is None:
-            req = dist.as_requirement()
-
-        return cls(dist.project_name, req, editable, comments=comments)
-
-    def __str__(self):
-        req = self.req
-        if self.editable:
-            req = '-e %s' % req
-        return '\n'.join(list(self.comments) + [str(req)]) + '\n'
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/prepare.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/prepare.py
deleted file mode 100644
index 4f31dd5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/operations/prepare.py
+++ /dev/null
@@ -1,413 +0,0 @@
-"""Prepares a distribution for installation
-"""
-
-import logging
-import os
-
-from pip._vendor import pkg_resources, requests
-
-from pip._internal.build_env import BuildEnvironment
-from pip._internal.download import (
-    is_dir_url, is_file_url, is_vcs_url, unpack_url, url_to_path,
-)
-from pip._internal.exceptions import (
-    DirectoryUrlHashUnsupported, HashUnpinned, InstallationError,
-    PreviousBuildDirError, VcsHashUnsupported,
-)
-from pip._internal.utils.compat import expanduser
-from pip._internal.utils.hashes import MissingHashes
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import display_path, normalize_path
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.vcs import vcs
-
-if MYPY_CHECK_RUNNING:
-    from typing import Any, Optional  # noqa: F401
-    from pip._internal.req.req_install import InstallRequirement  # noqa: F401
-    from pip._internal.index import PackageFinder  # noqa: F401
-    from pip._internal.download import PipSession  # noqa: F401
-    from pip._internal.req.req_tracker import RequirementTracker  # noqa: F401
-
-logger = logging.getLogger(__name__)
-
-
-def make_abstract_dist(req):
-    # type: (InstallRequirement) -> DistAbstraction
-    """Factory to make an abstract dist object.
-
-    Preconditions: Either an editable req with a source_dir, or satisfied_by or
-    a wheel link, or a non-editable req with a source_dir.
-
-    :return: A concrete DistAbstraction.
-    """
-    if req.editable:
-        return IsSDist(req)
-    elif req.link and req.link.is_wheel:
-        return IsWheel(req)
-    else:
-        return IsSDist(req)
-
-
-class DistAbstraction(object):
-    """Abstracts out the wheel vs non-wheel Resolver.resolve() logic.
-
-    The requirements for anything installable are as follows:
-     - we must be able to determine the requirement name
-       (or we can't correctly handle the non-upgrade case).
-     - we must be able to generate a list of run-time dependencies
-       without installing any additional packages (or we would
-       have to either burn time by doing temporary isolated installs
-       or alternatively violate pips 'don't start installing unless
-       all requirements are available' rule - neither of which are
-       desirable).
-     - for packages with setup requirements, we must also be able
-       to determine their requirements without installing additional
-       packages (for the same reason as run-time dependencies)
-     - we must be able to create a Distribution object exposing the
-       above metadata.
-    """
-
-    def __init__(self, req):
-        # type: (InstallRequirement) -> None
-        self.req = req  # type: InstallRequirement
-
-    def dist(self):
-        # type: () -> Any
-        """Return a setuptools Dist object."""
-        raise NotImplementedError
-
-    def prep_for_dist(self, finder, build_isolation):
-        # type: (PackageFinder, bool) -> Any
-        """Ensure that we can get a Dist for this requirement."""
-        raise NotImplementedError
-
-
-class IsWheel(DistAbstraction):
-
-    def dist(self):
-        # type: () -> pkg_resources.Distribution
-        return list(pkg_resources.find_distributions(
-            self.req.source_dir))[0]
-
-    def prep_for_dist(self, finder, build_isolation):
-        # type: (PackageFinder, bool) -> Any
-        # FIXME:https://github.com/pypa/pip/issues/1112
-        pass
-
-
-class IsSDist(DistAbstraction):
-
-    def dist(self):
-        return self.req.get_dist()
-
-    def prep_for_dist(self, finder, build_isolation):
-        # type: (PackageFinder, bool) -> None
-        # Prepare for building. We need to:
-        #   1. Load pyproject.toml (if it exists)
-        #   2. Set up the build environment
-
-        self.req.load_pyproject_toml()
-        should_isolate = self.req.use_pep517 and build_isolation
-
-        def _raise_conflicts(conflicting_with, conflicting_reqs):
-            raise InstallationError(
-                "Some build dependencies for %s conflict with %s: %s." % (
-                    self.req, conflicting_with, ', '.join(
-                        '%s is incompatible with %s' % (installed, wanted)
-                        for installed, wanted in sorted(conflicting))))
-
-        if should_isolate:
-            # Isolate in a BuildEnvironment and install the build-time
-            # requirements.
-            self.req.build_env = BuildEnvironment()
-            self.req.build_env.install_requirements(
-                finder, self.req.pyproject_requires, 'overlay',
-                "Installing build dependencies"
-            )
-            conflicting, missing = self.req.build_env.check_requirements(
-                self.req.requirements_to_check
-            )
-            if conflicting:
-                _raise_conflicts("PEP 517/518 supported requirements",
-                                 conflicting)
-            if missing:
-                logger.warning(
-                    "Missing build requirements in pyproject.toml for %s.",
-                    self.req,
-                )
-                logger.warning(
-                    "The project does not specify a build backend, and "
-                    "pip cannot fall back to setuptools without %s.",
-                    " and ".join(map(repr, sorted(missing)))
-                )
-            # Install any extra build dependencies that the backend requests.
-            # This must be done in a second pass, as the pyproject.toml
-            # dependencies must be installed before we can call the backend.
-            with self.req.build_env:
-                # We need to have the env active when calling the hook.
-                self.req.spin_message = "Getting requirements to build wheel"
-                reqs = self.req.pep517_backend.get_requires_for_build_wheel()
-            conflicting, missing = self.req.build_env.check_requirements(reqs)
-            if conflicting:
-                _raise_conflicts("the backend dependencies", conflicting)
-            self.req.build_env.install_requirements(
-                finder, missing, 'normal',
-                "Installing backend dependencies"
-            )
-
-        self.req.prepare_metadata()
-        self.req.assert_source_matches_version()
-
-
-class Installed(DistAbstraction):
-
-    def dist(self):
-        # type: () -> pkg_resources.Distribution
-        return self.req.satisfied_by
-
-    def prep_for_dist(self, finder, build_isolation):
-        # type: (PackageFinder, bool) -> Any
-        pass
-
-
-class RequirementPreparer(object):
-    """Prepares a Requirement
-    """
-
-    def __init__(
-        self,
-        build_dir,  # type: str
-        download_dir,  # type: Optional[str]
-        src_dir,  # type: str
-        wheel_download_dir,  # type: Optional[str]
-        progress_bar,  # type: str
-        build_isolation,  # type: bool
-        req_tracker  # type: RequirementTracker
-    ):
-        # type: (...) -> None
-        super(RequirementPreparer, self).__init__()
-
-        self.src_dir = src_dir
-        self.build_dir = build_dir
-        self.req_tracker = req_tracker
-
-        # Where still packed archives should be written to. If None, they are
-        # not saved, and are deleted immediately after unpacking.
-        self.download_dir = download_dir
-
-        # Where still-packed .whl files should be written to. If None, they are
-        # written to the download_dir parameter. Separate to download_dir to
-        # permit only keeping wheel archives for pip wheel.
-        if wheel_download_dir:
-            wheel_download_dir = normalize_path(wheel_download_dir)
-        self.wheel_download_dir = wheel_download_dir
-
-        # NOTE
-        # download_dir and wheel_download_dir overlap semantically and may
-        # be combined if we're willing to have non-wheel archives present in
-        # the wheelhouse output by 'pip wheel'.
-
-        self.progress_bar = progress_bar
-
-        # Is build isolation allowed?
-        self.build_isolation = build_isolation
-
-    @property
-    def _download_should_save(self):
-        # type: () -> bool
-        # TODO: Modify to reduce indentation needed
-        if self.download_dir:
-            self.download_dir = expanduser(self.download_dir)
-            if os.path.exists(self.download_dir):
-                return True
-            else:
-                logger.critical('Could not find download directory')
-                raise InstallationError(
-                    "Could not find or access download directory '%s'"
-                    % display_path(self.download_dir))
-        return False
-
-    def prepare_linked_requirement(
-        self,
-        req,  # type: InstallRequirement
-        session,  # type: PipSession
-        finder,  # type: PackageFinder
-        upgrade_allowed,  # type: bool
-        require_hashes  # type: bool
-    ):
-        # type: (...) -> DistAbstraction
-        """Prepare a requirement that would be obtained from req.link
-        """
-        # TODO: Breakup into smaller functions
-        if req.link and req.link.scheme == 'file':
-            path = url_to_path(req.link.url)
-            logger.info('Processing %s', display_path(path))
-        else:
-            logger.info('Collecting %s', req)
-
-        with indent_log():
-            # @@ if filesystem packages are not marked
-            # editable in a req, a non deterministic error
-            # occurs when the script attempts to unpack the
-            # build directory
-            req.ensure_has_source_dir(self.build_dir)
-            # If a checkout exists, it's unwise to keep going.  version
-            # inconsistencies are logged later, but do not fail the
-            # installation.
-            # FIXME: this won't upgrade when there's an existing
-            # package unpacked in `req.source_dir`
-            # package unpacked in `req.source_dir`
-            if os.path.exists(os.path.join(req.source_dir, 'setup.py')):
-                raise PreviousBuildDirError(
-                    "pip can't proceed with requirements '%s' due to a"
-                    " pre-existing build directory (%s). This is "
-                    "likely due to a previous installation that failed"
-                    ". pip is being responsible and not assuming it "
-                    "can delete this. Please delete it and try again."
-                    % (req, req.source_dir)
-                )
-            req.populate_link(finder, upgrade_allowed, require_hashes)
-
-            # We can't hit this spot and have populate_link return None.
-            # req.satisfied_by is None here (because we're
-            # guarded) and upgrade has no impact except when satisfied_by
-            # is not None.
-            # Then inside find_requirement existing_applicable -> False
-            # If no new versions are found, DistributionNotFound is raised,
-            # otherwise a result is guaranteed.
-            assert req.link
-            link = req.link
-
-            # Now that we have the real link, we can tell what kind of
-            # requirements we have and raise some more informative errors
-            # than otherwise. (For example, we can raise VcsHashUnsupported
-            # for a VCS URL rather than HashMissing.)
-            if require_hashes:
-                # We could check these first 2 conditions inside
-                # unpack_url and save repetition of conditions, but then
-                # we would report less-useful error messages for
-                # unhashable requirements, complaining that there's no
-                # hash provided.
-                if is_vcs_url(link):
-                    raise VcsHashUnsupported()
-                elif is_file_url(link) and is_dir_url(link):
-                    raise DirectoryUrlHashUnsupported()
-                if not req.original_link and not req.is_pinned:
-                    # Unpinned packages are asking for trouble when a new
-                    # version is uploaded. This isn't a security check, but
-                    # it saves users a surprising hash mismatch in the
-                    # future.
-                    #
-                    # file:/// URLs aren't pinnable, so don't complain
-                    # about them not being pinned.
-                    raise HashUnpinned()
-
-            hashes = req.hashes(trust_internet=not require_hashes)
-            if require_hashes and not hashes:
-                # Known-good hashes are missing for this requirement, so
-                # shim it with a facade object that will provoke hash
-                # computation and then raise a HashMissing exception
-                # showing the user what the hash should be.
-                hashes = MissingHashes()
-
-            try:
-                download_dir = self.download_dir
-                # We always delete unpacked sdists after pip ran.
-                autodelete_unpacked = True
-                if req.link.is_wheel and self.wheel_download_dir:
-                    # when doing 'pip wheel` we download wheels to a
-                    # dedicated dir.
-                    download_dir = self.wheel_download_dir
-                if req.link.is_wheel:
-                    if download_dir:
-                        # When downloading, we only unpack wheels to get
-                        # metadata.
-                        autodelete_unpacked = True
-                    else:
-                        # When installing a wheel, we use the unpacked
-                        # wheel.
-                        autodelete_unpacked = False
-                unpack_url(
-                    req.link, req.source_dir,
-                    download_dir, autodelete_unpacked,
-                    session=session, hashes=hashes,
-                    progress_bar=self.progress_bar
-                )
-            except requests.HTTPError as exc:
-                logger.critical(
-                    'Could not install requirement %s because of error %s',
-                    req,
-                    exc,
-                )
-                raise InstallationError(
-                    'Could not install requirement %s because of HTTP '
-                    'error %s for URL %s' %
-                    (req, exc, req.link)
-                )
-            abstract_dist = make_abstract_dist(req)
-            with self.req_tracker.track(req):
-                abstract_dist.prep_for_dist(finder, self.build_isolation)
-            if self._download_should_save:
-                # Make a .zip of the source_dir we already created.
-                if req.link.scheme in vcs.all_schemes:
-                    req.archive(self.download_dir)
-        return abstract_dist
-
-    def prepare_editable_requirement(
-        self,
-        req,  # type: InstallRequirement
-        require_hashes,  # type: bool
-        use_user_site,  # type: bool
-        finder  # type: PackageFinder
-    ):
-        # type: (...) -> DistAbstraction
-        """Prepare an editable requirement
-        """
-        assert req.editable, "cannot prepare a non-editable req as editable"
-
-        logger.info('Obtaining %s', req)
-
-        with indent_log():
-            if require_hashes:
-                raise InstallationError(
-                    'The editable requirement %s cannot be installed when '
-                    'requiring hashes, because there is no single file to '
-                    'hash.' % req
-                )
-            req.ensure_has_source_dir(self.src_dir)
-            req.update_editable(not self._download_should_save)
-
-            abstract_dist = make_abstract_dist(req)
-            with self.req_tracker.track(req):
-                abstract_dist.prep_for_dist(finder, self.build_isolation)
-
-            if self._download_should_save:
-                req.archive(self.download_dir)
-            req.check_if_exists(use_user_site)
-
-        return abstract_dist
-
-    def prepare_installed_requirement(self, req, require_hashes, skip_reason):
-        # type: (InstallRequirement, bool, Optional[str]) -> DistAbstraction
-        """Prepare an already-installed requirement
-        """
-        assert req.satisfied_by, "req should have been satisfied but isn't"
-        assert skip_reason is not None, (
-            "did not get skip reason skipped but req.satisfied_by "
-            "is set to %r" % (req.satisfied_by,)
-        )
-        logger.info(
-            'Requirement %s: %s (%s)',
-            skip_reason, req, req.satisfied_by.version
-        )
-        with indent_log():
-            if require_hashes:
-                logger.debug(
-                    'Since it is already installed, we are trusting this '
-                    'package without checking its hash. To ensure a '
-                    'completely repeatable environment, install into an '
-                    'empty virtualenv.'
-                )
-            abstract_dist = Installed(req)
-
-        return abstract_dist
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/pep425tags.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/pep425tags.py
deleted file mode 100644
index 1e782d1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/pep425tags.py
+++ /dev/null
@@ -1,381 +0,0 @@
-"""Generate and work with PEP 425 Compatibility Tags."""
-from __future__ import absolute_import
-
-import distutils.util
-import logging
-import platform
-import re
-import sys
-import sysconfig
-import warnings
-from collections import OrderedDict
-
-import pip._internal.utils.glibc
-from pip._internal.utils.compat import get_extension_suffixes
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Tuple, Callable, List, Optional, Union, Dict
-    )
-
-    Pep425Tag = Tuple[str, str, str]
-
-logger = logging.getLogger(__name__)
-
-_osx_arch_pat = re.compile(r'(.+)_(\d+)_(\d+)_(.+)')
-
-
-def get_config_var(var):
-    # type: (str) -> Optional[str]
-    try:
-        return sysconfig.get_config_var(var)
-    except IOError as e:  # Issue #1074
-        warnings.warn("{}".format(e), RuntimeWarning)
-        return None
-
-
-def get_abbr_impl():
-    # type: () -> str
-    """Return abbreviated implementation name."""
-    if hasattr(sys, 'pypy_version_info'):
-        pyimpl = 'pp'
-    elif sys.platform.startswith('java'):
-        pyimpl = 'jy'
-    elif sys.platform == 'cli':
-        pyimpl = 'ip'
-    else:
-        pyimpl = 'cp'
-    return pyimpl
-
-
-def get_impl_ver():
-    # type: () -> str
-    """Return implementation version."""
-    impl_ver = get_config_var("py_version_nodot")
-    if not impl_ver or get_abbr_impl() == 'pp':
-        impl_ver = ''.join(map(str, get_impl_version_info()))
-    return impl_ver
-
-
-def get_impl_version_info():
-    # type: () -> Tuple[int, ...]
-    """Return sys.version_info-like tuple for use in decrementing the minor
-    version."""
-    if get_abbr_impl() == 'pp':
-        # as per https://github.com/pypa/pip/issues/2882
-        # attrs exist only on pypy
-        return (sys.version_info[0],
-                sys.pypy_version_info.major,  # type: ignore
-                sys.pypy_version_info.minor)  # type: ignore
-    else:
-        return sys.version_info[0], sys.version_info[1]
-
-
-def get_impl_tag():
-    # type: () -> str
-    """
-    Returns the Tag for this specific implementation.
-    """
-    return "{}{}".format(get_abbr_impl(), get_impl_ver())
-
-
-def get_flag(var, fallback, expected=True, warn=True):
-    # type: (str, Callable[..., bool], Union[bool, int], bool) -> bool
-    """Use a fallback method for determining SOABI flags if the needed config
-    var is unset or unavailable."""
-    val = get_config_var(var)
-    if val is None:
-        if warn:
-            logger.debug("Config variable '%s' is unset, Python ABI tag may "
-                         "be incorrect", var)
-        return fallback()
-    return val == expected
-
-
-def get_abi_tag():
-    # type: () -> Optional[str]
-    """Return the ABI tag based on SOABI (if available) or emulate SOABI
-    (CPython 2, PyPy)."""
-    soabi = get_config_var('SOABI')
-    impl = get_abbr_impl()
-    if not soabi and impl in {'cp', 'pp'} and hasattr(sys, 'maxunicode'):
-        d = ''
-        m = ''
-        u = ''
-        if get_flag('Py_DEBUG',
-                    lambda: hasattr(sys, 'gettotalrefcount'),
-                    warn=(impl == 'cp')):
-            d = 'd'
-        if get_flag('WITH_PYMALLOC',
-                    lambda: impl == 'cp',
-                    warn=(impl == 'cp')):
-            m = 'm'
-        if get_flag('Py_UNICODE_SIZE',
-                    lambda: sys.maxunicode == 0x10ffff,
-                    expected=4,
-                    warn=(impl == 'cp' and
-                          sys.version_info < (3, 3))) \
-                and sys.version_info < (3, 3):
-            u = 'u'
-        abi = '%s%s%s%s%s' % (impl, get_impl_ver(), d, m, u)
-    elif soabi and soabi.startswith('cpython-'):
-        abi = 'cp' + soabi.split('-')[1]
-    elif soabi:
-        abi = soabi.replace('.', '_').replace('-', '_')
-    else:
-        abi = None
-    return abi
-
-
-def _is_running_32bit():
-    # type: () -> bool
-    return sys.maxsize == 2147483647
-
-
-def get_platform():
-    # type: () -> str
-    """Return our platform name 'win32', 'linux_x86_64'"""
-    if sys.platform == 'darwin':
-        # distutils.util.get_platform() returns the release based on the value
-        # of MACOSX_DEPLOYMENT_TARGET on which Python was built, which may
-        # be significantly older than the user's current machine.
-        release, _, machine = platform.mac_ver()
-        split_ver = release.split('.')
-
-        if machine == "x86_64" and _is_running_32bit():
-            machine = "i386"
-        elif machine == "ppc64" and _is_running_32bit():
-            machine = "ppc"
-
-        return 'macosx_{}_{}_{}'.format(split_ver[0], split_ver[1], machine)
-
-    # XXX remove distutils dependency
-    result = distutils.util.get_platform().replace('.', '_').replace('-', '_')
-    if result == "linux_x86_64" and _is_running_32bit():
-        # 32 bit Python program (running on a 64 bit Linux): pip should only
-        # install and run 32 bit compiled extensions in that case.
-        result = "linux_i686"
-
-    return result
-
-
-def is_manylinux1_compatible():
-    # type: () -> bool
-    # Only Linux, and only x86-64 / i686
-    if get_platform() not in {"linux_x86_64", "linux_i686"}:
-        return False
-
-    # Check for presence of _manylinux module
-    try:
-        import _manylinux
-        return bool(_manylinux.manylinux1_compatible)
-    except (ImportError, AttributeError):
-        # Fall through to heuristic check below
-        pass
-
-    # Check glibc version. CentOS 5 uses glibc 2.5.
-    return pip._internal.utils.glibc.have_compatible_glibc(2, 5)
-
-
-def is_manylinux2010_compatible():
-    # type: () -> bool
-    # Only Linux, and only x86-64 / i686
-    if get_platform() not in {"linux_x86_64", "linux_i686"}:
-        return False
-
-    # Check for presence of _manylinux module
-    try:
-        import _manylinux
-        return bool(_manylinux.manylinux2010_compatible)
-    except (ImportError, AttributeError):
-        # Fall through to heuristic check below
-        pass
-
-    # Check glibc version. CentOS 6 uses glibc 2.12.
-    return pip._internal.utils.glibc.have_compatible_glibc(2, 12)
-
-
-def get_darwin_arches(major, minor, machine):
-    # type: (int, int, str) -> List[str]
-    """Return a list of supported arches (including group arches) for
-    the given major, minor and machine architecture of an macOS machine.
-    """
-    arches = []
-
-    def _supports_arch(major, minor, arch):
-        # type: (int, int, str) -> bool
-        # Looking at the application support for macOS versions in the chart
-        # provided by https://en.wikipedia.org/wiki/OS_X#Versions it appears
-        # our timeline looks roughly like:
-        #
-        # 10.0 - Introduces ppc support.
-        # 10.4 - Introduces ppc64, i386, and x86_64 support, however the ppc64
-        #        and x86_64 support is CLI only, and cannot be used for GUI
-        #        applications.
-        # 10.5 - Extends ppc64 and x86_64 support to cover GUI applications.
-        # 10.6 - Drops support for ppc64
-        # 10.7 - Drops support for ppc
-        #
-        # Given that we do not know if we're installing a CLI or a GUI
-        # application, we must be conservative and assume it might be a GUI
-        # application and behave as if ppc64 and x86_64 support did not occur
-        # until 10.5.
-        #
-        # Note: The above information is taken from the "Application support"
-        #       column in the chart not the "Processor support" since I believe
-        #       that we care about what instruction sets an application can use
-        #       not which processors the OS supports.
-        if arch == 'ppc':
-            return (major, minor) <= (10, 5)
-        if arch == 'ppc64':
-            return (major, minor) == (10, 5)
-        if arch == 'i386':
-            return (major, minor) >= (10, 4)
-        if arch == 'x86_64':
-            return (major, minor) >= (10, 5)
-        if arch in groups:
-            for garch in groups[arch]:
-                if _supports_arch(major, minor, garch):
-                    return True
-        return False
-
-    groups = OrderedDict([
-        ("fat", ("i386", "ppc")),
-        ("intel", ("x86_64", "i386")),
-        ("fat64", ("x86_64", "ppc64")),
-        ("fat32", ("x86_64", "i386", "ppc")),
-    ])  # type: Dict[str, Tuple[str, ...]]
-
-    if _supports_arch(major, minor, machine):
-        arches.append(machine)
-
-    for garch in groups:
-        if machine in groups[garch] and _supports_arch(major, minor, garch):
-            arches.append(garch)
-
-    arches.append('universal')
-
-    return arches
-
-
-def get_all_minor_versions_as_strings(version_info):
-    # type: (Tuple[int, ...]) -> List[str]
-    versions = []
-    major = version_info[:-1]
-    # Support all previous minor Python versions.
-    for minor in range(version_info[-1], -1, -1):
-        versions.append(''.join(map(str, major + (minor,))))
-    return versions
-
-
-def get_supported(
-    versions=None,  # type: Optional[List[str]]
-    noarch=False,  # type: bool
-    platform=None,  # type: Optional[str]
-    impl=None,  # type: Optional[str]
-    abi=None  # type: Optional[str]
-):
-    # type: (...) -> List[Pep425Tag]
-    """Return a list of supported tags for each version specified in
-    `versions`.
-
-    :param versions: a list of string versions, of the form ["33", "32"],
-        or None. The first version will be assumed to support our ABI.
-    :param platform: specify the exact platform you want valid
-        tags for, or None. If None, use the local system platform.
-    :param impl: specify the exact implementation you want valid
-        tags for, or None. If None, use the local interpreter impl.
-    :param abi: specify the exact abi you want valid
-        tags for, or None. If None, use the local interpreter abi.
-    """
-    supported = []
-
-    # Versions must be given with respect to the preference
-    if versions is None:
-        version_info = get_impl_version_info()
-        versions = get_all_minor_versions_as_strings(version_info)
-
-    impl = impl or get_abbr_impl()
-
-    abis = []  # type: List[str]
-
-    abi = abi or get_abi_tag()
-    if abi:
-        abis[0:0] = [abi]
-
-    abi3s = set()
-    for suffix in get_extension_suffixes():
-        if suffix.startswith('.abi'):
-            abi3s.add(suffix.split('.', 2)[1])
-
-    abis.extend(sorted(list(abi3s)))
-
-    abis.append('none')
-
-    if not noarch:
-        arch = platform or get_platform()
-        arch_prefix, arch_sep, arch_suffix = arch.partition('_')
-        if arch.startswith('macosx'):
-            # support macosx-10.6-intel on macosx-10.9-x86_64
-            match = _osx_arch_pat.match(arch)
-            if match:
-                name, major, minor, actual_arch = match.groups()
-                tpl = '{}_{}_%i_%s'.format(name, major)
-                arches = []
-                for m in reversed(range(int(minor) + 1)):
-                    for a in get_darwin_arches(int(major), m, actual_arch):
-                        arches.append(tpl % (m, a))
-            else:
-                # arch pattern didn't match (?!)
-                arches = [arch]
-        elif arch_prefix == 'manylinux2010':
-            # manylinux1 wheels run on most manylinux2010 systems with the
-            # exception of wheels depending on ncurses. PEP 571 states
-            # manylinux1 wheels should be considered manylinux2010 wheels:
-            # https://www.python.org/dev/peps/pep-0571/#backwards-compatibility-with-manylinux1-wheels
-            arches = [arch, 'manylinux1' + arch_sep + arch_suffix]
-        elif platform is None:
-            arches = []
-            if is_manylinux2010_compatible():
-                arches.append('manylinux2010' + arch_sep + arch_suffix)
-            if is_manylinux1_compatible():
-                arches.append('manylinux1' + arch_sep + arch_suffix)
-            arches.append(arch)
-        else:
-            arches = [arch]
-
-        # Current version, current API (built specifically for our Python):
-        for abi in abis:
-            for arch in arches:
-                supported.append(('%s%s' % (impl, versions[0]), abi, arch))
-
-        # abi3 modules compatible with older version of Python
-        for version in versions[1:]:
-            # abi3 was introduced in Python 3.2
-            if version in {'31', '30'}:
-                break
-            for abi in abi3s:   # empty set if not Python 3
-                for arch in arches:
-                    supported.append(("%s%s" % (impl, version), abi, arch))
-
-        # Has binaries, does not use the Python API:
-        for arch in arches:
-            supported.append(('py%s' % (versions[0][0]), 'none', arch))
-
-    # No abi / arch, but requires our implementation:
-    supported.append(('%s%s' % (impl, versions[0]), 'none', 'any'))
-    # Tagged specifically as being cross-version compatible
-    # (with just the major version specified)
-    supported.append(('%s%s' % (impl, versions[0][0]), 'none', 'any'))
-
-    # No abi / arch, generic Python
-    for i, version in enumerate(versions):
-        supported.append(('py%s' % (version,), 'none', 'any'))
-        if i == 0:
-            supported.append(('py%s' % (version[0]), 'none', 'any'))
-
-    return supported
-
-
-implementation_tag = get_impl_tag()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/pyproject.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/pyproject.py
deleted file mode 100644
index 8d739a6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/pyproject.py
+++ /dev/null
@@ -1,171 +0,0 @@
-from __future__ import absolute_import
-
-import io
-import os
-import sys
-
-from pip._vendor import pytoml, six
-
-from pip._internal.exceptions import InstallationError
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Any, Tuple, Optional, List  # noqa: F401
-
-
-def _is_list_of_str(obj):
-    # type: (Any) -> bool
-    return (
-        isinstance(obj, list) and
-        all(isinstance(item, six.string_types) for item in obj)
-    )
-
-
-def make_pyproject_path(setup_py_dir):
-    # type: (str) -> str
-    path = os.path.join(setup_py_dir, 'pyproject.toml')
-
-    # Python2 __file__ should not be unicode
-    if six.PY2 and isinstance(path, six.text_type):
-        path = path.encode(sys.getfilesystemencoding())
-
-    return path
-
-
-def load_pyproject_toml(
-    use_pep517,  # type: Optional[bool]
-    pyproject_toml,  # type: str
-    setup_py,  # type: str
-    req_name  # type: str
-):
-    # type: (...) -> Optional[Tuple[List[str], str, List[str]]]
-    """Load the pyproject.toml file.
-
-    Parameters:
-        use_pep517 - Has the user requested PEP 517 processing? None
-                     means the user hasn't explicitly specified.
-        pyproject_toml - Location of the project's pyproject.toml file
-        setup_py - Location of the project's setup.py file
-        req_name - The name of the requirement we're processing (for
-                   error reporting)
-
-    Returns:
-        None if we should use the legacy code path, otherwise a tuple
-        (
-            requirements from pyproject.toml,
-            name of PEP 517 backend,
-            requirements we should check are installed after setting
-                up the build environment
-        )
-    """
-    has_pyproject = os.path.isfile(pyproject_toml)
-    has_setup = os.path.isfile(setup_py)
-
-    if has_pyproject:
-        with io.open(pyproject_toml, encoding="utf-8") as f:
-            pp_toml = pytoml.load(f)
-        build_system = pp_toml.get("build-system")
-    else:
-        build_system = None
-
-    # The following cases must use PEP 517
-    # We check for use_pep517 being non-None and falsey because that means
-    # the user explicitly requested --no-use-pep517.  The value 0 as
-    # opposed to False can occur when the value is provided via an
-    # environment variable or config file option (due to the quirk of
-    # strtobool() returning an integer in pip's configuration code).
-    if has_pyproject and not has_setup:
-        if use_pep517 is not None and not use_pep517:
-            raise InstallationError(
-                "Disabling PEP 517 processing is invalid: "
-                "project does not have a setup.py"
-            )
-        use_pep517 = True
-    elif build_system and "build-backend" in build_system:
-        if use_pep517 is not None and not use_pep517:
-            raise InstallationError(
-                "Disabling PEP 517 processing is invalid: "
-                "project specifies a build backend of {} "
-                "in pyproject.toml".format(
-                    build_system["build-backend"]
-                )
-            )
-        use_pep517 = True
-
-    # If we haven't worked out whether to use PEP 517 yet,
-    # and the user hasn't explicitly stated a preference,
-    # we do so if the project has a pyproject.toml file.
-    elif use_pep517 is None:
-        use_pep517 = has_pyproject
-
-    # At this point, we know whether we're going to use PEP 517.
-    assert use_pep517 is not None
-
-    # If we're using the legacy code path, there is nothing further
-    # for us to do here.
-    if not use_pep517:
-        return None
-
-    if build_system is None:
-        # Either the user has a pyproject.toml with no build-system
-        # section, or the user has no pyproject.toml, but has opted in
-        # explicitly via --use-pep517.
-        # In the absence of any explicit backend specification, we
-        # assume the setuptools backend that most closely emulates the
-        # traditional direct setup.py execution, and require wheel and
-        # a version of setuptools that supports that backend.
-
-        build_system = {
-            "requires": ["setuptools>=40.8.0", "wheel"],
-            "build-backend": "setuptools.build_meta:__legacy__",
-        }
-
-    # If we're using PEP 517, we have build system information (either
-    # from pyproject.toml, or defaulted by the code above).
-    # Note that at this point, we do not know if the user has actually
-    # specified a backend, though.
-    assert build_system is not None
-
-    # Ensure that the build-system section in pyproject.toml conforms
-    # to PEP 518.
-    error_template = (
-        "{package} has a pyproject.toml file that does not comply "
-        "with PEP 518: {reason}"
-    )
-
-    # Specifying the build-system table but not the requires key is invalid
-    if "requires" not in build_system:
-        raise InstallationError(
-            error_template.format(package=req_name, reason=(
-                "it has a 'build-system' table but not "
-                "'build-system.requires' which is mandatory in the table"
-            ))
-        )
-
-    # Error out if requires is not a list of strings
-    requires = build_system["requires"]
-    if not _is_list_of_str(requires):
-        raise InstallationError(error_template.format(
-            package=req_name,
-            reason="'build-system.requires' is not a list of strings.",
-        ))
-
-    backend = build_system.get("build-backend")
-    check = []  # type: List[str]
-    if backend is None:
-        # If the user didn't specify a backend, we assume they want to use
-        # the setuptools backend. But we can't be sure they have included
-        # a version of setuptools which supplies the backend, or wheel
-        # (which is needed by the backend) in their requirements. So we
-        # make a note to check that those requirements are present once
-        # we have set up the environment.
-        # This is quite a lot of work to check for a very specific case. But
-        # the problem is, that case is potentially quite common - projects that
-        # adopted PEP 518 early for the ability to specify requirements to
-        # execute setup.py, but never considered needing to mention the build
-        # tools themselves. The original PEP 518 code had a similar check (but
-        # implemented in a different way).
-        backend = "setuptools.build_meta:__legacy__"
-        check = ["setuptools>=40.8.0", "wheel"]
-
-    return (requires, backend, check)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__init__.py
deleted file mode 100644
index 5e4eb92..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__init__.py
+++ /dev/null
@@ -1,77 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-
-from .req_install import InstallRequirement
-from .req_set import RequirementSet
-from .req_file import parse_requirements
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import List, Sequence  # noqa: F401
-
-__all__ = [
-    "RequirementSet", "InstallRequirement",
-    "parse_requirements", "install_given_reqs",
-]
-
-logger = logging.getLogger(__name__)
-
-
-def install_given_reqs(
-    to_install,  # type: List[InstallRequirement]
-    install_options,  # type: List[str]
-    global_options=(),  # type: Sequence[str]
-    *args, **kwargs
-):
-    # type: (...) -> List[InstallRequirement]
-    """
-    Install everything in the given list.
-
-    (to be called after having downloaded and unpacked the packages)
-    """
-
-    if to_install:
-        logger.info(
-            'Installing collected packages: %s',
-            ', '.join([req.name for req in to_install]),
-        )
-
-    with indent_log():
-        for requirement in to_install:
-            if requirement.conflicts_with:
-                logger.info(
-                    'Found existing installation: %s',
-                    requirement.conflicts_with,
-                )
-                with indent_log():
-                    uninstalled_pathset = requirement.uninstall(
-                        auto_confirm=True
-                    )
-            try:
-                requirement.install(
-                    install_options,
-                    global_options,
-                    *args,
-                    **kwargs
-                )
-            except Exception:
-                should_rollback = (
-                    requirement.conflicts_with and
-                    not requirement.install_succeeded
-                )
-                # if install did not succeed, rollback previous uninstall
-                if should_rollback:
-                    uninstalled_pathset.rollback()
-                raise
-            else:
-                should_commit = (
-                    requirement.conflicts_with and
-                    requirement.install_succeeded
-                )
-                if should_commit:
-                    uninstalled_pathset.commit()
-            requirement.remove_temporary_source()
-
-    return to_install
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 3d591d3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/constructors.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/constructors.cpython-37.pyc
deleted file mode 100644
index b60d743..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/constructors.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_file.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_file.cpython-37.pyc
deleted file mode 100644
index d5eb5fc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_file.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_install.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_install.cpython-37.pyc
deleted file mode 100644
index ef28d33..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_install.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_set.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_set.cpython-37.pyc
deleted file mode 100644
index c6e6d28..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_set.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_tracker.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_tracker.cpython-37.pyc
deleted file mode 100644
index f054d9f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_tracker.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_uninstall.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_uninstall.cpython-37.pyc
deleted file mode 100644
index 9aca886..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/__pycache__/req_uninstall.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/constructors.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/constructors.py
deleted file mode 100644
index 1eed1dd..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/constructors.py
+++ /dev/null
@@ -1,339 +0,0 @@
-"""Backing implementation for InstallRequirement's various constructors
-
-The idea here is that these formed a major chunk of InstallRequirement's size
-so, moving them and support code dedicated to them outside of that class
-helps creates for better understandability for the rest of the code.
-
-These are meant to be used elsewhere within pip to create instances of
-InstallRequirement.
-"""
-
-import logging
-import os
-import re
-
-from pip._vendor.packaging.markers import Marker
-from pip._vendor.packaging.requirements import InvalidRequirement, Requirement
-from pip._vendor.packaging.specifiers import Specifier
-from pip._vendor.pkg_resources import RequirementParseError, parse_requirements
-
-from pip._internal.download import (
-    is_archive_file, is_url, path_to_url, url_to_path,
-)
-from pip._internal.exceptions import InstallationError
-from pip._internal.models.index import PyPI, TestPyPI
-from pip._internal.models.link import Link
-from pip._internal.pyproject import make_pyproject_path
-from pip._internal.req.req_install import InstallRequirement
-from pip._internal.utils.misc import is_installable_dir
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.vcs import vcs
-from pip._internal.wheel import Wheel
-
-if MYPY_CHECK_RUNNING:
-    from typing import (   # noqa: F401
-        Optional, Tuple, Set, Any, Union, Text, Dict,
-    )
-    from pip._internal.cache import WheelCache  # noqa: F401
-
-
-__all__ = [
-    "install_req_from_editable", "install_req_from_line",
-    "parse_editable"
-]
-
-logger = logging.getLogger(__name__)
-operators = Specifier._operators.keys()
-
-
-def _strip_extras(path):
-    # type: (str) -> Tuple[str, Optional[str]]
-    m = re.match(r'^(.+)(\[[^\]]+\])$', path)
-    extras = None
-    if m:
-        path_no_extras = m.group(1)
-        extras = m.group(2)
-    else:
-        path_no_extras = path
-
-    return path_no_extras, extras
-
-
-def parse_editable(editable_req):
-    # type: (str) -> Tuple[Optional[str], str, Optional[Set[str]]]
-    """Parses an editable requirement into:
-        - a requirement name
-        - an URL
-        - extras
-        - editable options
-    Accepted requirements:
-        svn+http://blahblah@rev#egg=Foobar[baz]&subdirectory=version_subdir
-        .[some_extra]
-    """
-
-    url = editable_req
-
-    # If a file path is specified with extras, strip off the extras.
-    url_no_extras, extras = _strip_extras(url)
-
-    if os.path.isdir(url_no_extras):
-        if not os.path.exists(os.path.join(url_no_extras, 'setup.py')):
-            msg = (
-                'File "setup.py" not found. Directory cannot be installed '
-                'in editable mode: {}'.format(os.path.abspath(url_no_extras))
-            )
-            pyproject_path = make_pyproject_path(url_no_extras)
-            if os.path.isfile(pyproject_path):
-                msg += (
-                    '\n(A "pyproject.toml" file was found, but editable '
-                    'mode currently requires a setup.py based build.)'
-                )
-            raise InstallationError(msg)
-
-        # Treating it as code that has already been checked out
-        url_no_extras = path_to_url(url_no_extras)
-
-    if url_no_extras.lower().startswith('file:'):
-        package_name = Link(url_no_extras).egg_fragment
-        if extras:
-            return (
-                package_name,
-                url_no_extras,
-                Requirement("placeholder" + extras.lower()).extras,
-            )
-        else:
-            return package_name, url_no_extras, None
-
-    for version_control in vcs:
-        if url.lower().startswith('%s:' % version_control):
-            url = '%s+%s' % (version_control, url)
-            break
-
-    if '+' not in url:
-        raise InstallationError(
-            '%s should either be a path to a local project or a VCS url '
-            'beginning with svn+, git+, hg+, or bzr+' %
-            editable_req
-        )
-
-    vc_type = url.split('+', 1)[0].lower()
-
-    if not vcs.get_backend(vc_type):
-        error_message = 'For --editable=%s only ' % editable_req + \
-            ', '.join([backend.name + '+URL' for backend in vcs.backends]) + \
-            ' is currently supported'
-        raise InstallationError(error_message)
-
-    package_name = Link(url).egg_fragment
-    if not package_name:
-        raise InstallationError(
-            "Could not detect requirement name for '%s', please specify one "
-            "with #egg=your_package_name" % editable_req
-        )
-    return package_name, url, None
-
-
-def deduce_helpful_msg(req):
-    # type: (str) -> str
-    """Returns helpful msg in case requirements file does not exist,
-    or cannot be parsed.
-
-    :params req: Requirements file path
-    """
-    msg = ""
-    if os.path.exists(req):
-        msg = " It does exist."
-        # Try to parse and check if it is a requirements file.
-        try:
-            with open(req, 'r') as fp:
-                # parse first line only
-                next(parse_requirements(fp.read()))
-                msg += " The argument you provided " + \
-                    "(%s) appears to be a" % (req) + \
-                    " requirements file. If that is the" + \
-                    " case, use the '-r' flag to install" + \
-                    " the packages specified within it."
-        except RequirementParseError:
-            logger.debug("Cannot parse '%s' as requirements \
-            file" % (req), exc_info=True)
-    else:
-        msg += " File '%s' does not exist." % (req)
-    return msg
-
-
-# ---- The actual constructors follow ----
-
-
-def install_req_from_editable(
-    editable_req,  # type: str
-    comes_from=None,  # type: Optional[str]
-    use_pep517=None,  # type: Optional[bool]
-    isolated=False,  # type: bool
-    options=None,  # type: Optional[Dict[str, Any]]
-    wheel_cache=None,  # type: Optional[WheelCache]
-    constraint=False  # type: bool
-):
-    # type: (...) -> InstallRequirement
-    name, url, extras_override = parse_editable(editable_req)
-    if url.startswith('file:'):
-        source_dir = url_to_path(url)
-    else:
-        source_dir = None
-
-    if name is not None:
-        try:
-            req = Requirement(name)
-        except InvalidRequirement:
-            raise InstallationError("Invalid requirement: '%s'" % name)
-    else:
-        req = None
-    return InstallRequirement(
-        req, comes_from, source_dir=source_dir,
-        editable=True,
-        link=Link(url),
-        constraint=constraint,
-        use_pep517=use_pep517,
-        isolated=isolated,
-        options=options if options else {},
-        wheel_cache=wheel_cache,
-        extras=extras_override or (),
-    )
-
-
-def install_req_from_line(
-    name,  # type: str
-    comes_from=None,  # type: Optional[Union[str, InstallRequirement]]
-    use_pep517=None,  # type: Optional[bool]
-    isolated=False,  # type: bool
-    options=None,  # type: Optional[Dict[str, Any]]
-    wheel_cache=None,  # type: Optional[WheelCache]
-    constraint=False  # type: bool
-):
-    # type: (...) -> InstallRequirement
-    """Creates an InstallRequirement from a name, which might be a
-    requirement, directory containing 'setup.py', filename, or URL.
-    """
-    if is_url(name):
-        marker_sep = '; '
-    else:
-        marker_sep = ';'
-    if marker_sep in name:
-        name, markers_as_string = name.split(marker_sep, 1)
-        markers_as_string = markers_as_string.strip()
-        if not markers_as_string:
-            markers = None
-        else:
-            markers = Marker(markers_as_string)
-    else:
-        markers = None
-    name = name.strip()
-    req_as_string = None
-    path = os.path.normpath(os.path.abspath(name))
-    link = None
-    extras_as_string = None
-
-    if is_url(name):
-        link = Link(name)
-    else:
-        p, extras_as_string = _strip_extras(path)
-        looks_like_dir = os.path.isdir(p) and (
-            os.path.sep in name or
-            (os.path.altsep is not None and os.path.altsep in name) or
-            name.startswith('.')
-        )
-        if looks_like_dir:
-            if not is_installable_dir(p):
-                raise InstallationError(
-                    "Directory %r is not installable. Neither 'setup.py' "
-                    "nor 'pyproject.toml' found." % name
-                )
-            link = Link(path_to_url(p))
-        elif is_archive_file(p):
-            if not os.path.isfile(p):
-                logger.warning(
-                    'Requirement %r looks like a filename, but the '
-                    'file does not exist',
-                    name
-                )
-            link = Link(path_to_url(p))
-
-    # it's a local file, dir, or url
-    if link:
-        # Handle relative file URLs
-        if link.scheme == 'file' and re.search(r'\.\./', link.url):
-            link = Link(
-                path_to_url(os.path.normpath(os.path.abspath(link.path))))
-        # wheel file
-        if link.is_wheel:
-            wheel = Wheel(link.filename)  # can raise InvalidWheelFilename
-            req_as_string = "%s==%s" % (wheel.name, wheel.version)
-        else:
-            # set the req to the egg fragment.  when it's not there, this
-            # will become an 'unnamed' requirement
-            req_as_string = link.egg_fragment
-
-    # a requirement specifier
-    else:
-        req_as_string = name
-
-    if extras_as_string:
-        extras = Requirement("placeholder" + extras_as_string.lower()).extras
-    else:
-        extras = ()
-    if req_as_string is not None:
-        try:
-            req = Requirement(req_as_string)
-        except InvalidRequirement:
-            if os.path.sep in req_as_string:
-                add_msg = "It looks like a path."
-                add_msg += deduce_helpful_msg(req_as_string)
-            elif ('=' in req_as_string and
-                  not any(op in req_as_string for op in operators)):
-                add_msg = "= is not a valid operator. Did you mean == ?"
-            else:
-                add_msg = ""
-            raise InstallationError(
-                "Invalid requirement: '%s'\n%s" % (req_as_string, add_msg)
-            )
-    else:
-        req = None
-
-    return InstallRequirement(
-        req, comes_from, link=link, markers=markers,
-        use_pep517=use_pep517, isolated=isolated,
-        options=options if options else {},
-        wheel_cache=wheel_cache,
-        constraint=constraint,
-        extras=extras,
-    )
-
-
-def install_req_from_req_string(
-    req_string,  # type: str
-    comes_from=None,  # type: Optional[InstallRequirement]
-    isolated=False,  # type: bool
-    wheel_cache=None,  # type: Optional[WheelCache]
-    use_pep517=None  # type: Optional[bool]
-):
-    # type: (...) -> InstallRequirement
-    try:
-        req = Requirement(req_string)
-    except InvalidRequirement:
-        raise InstallationError("Invalid requirement: '%s'" % req)
-
-    domains_not_allowed = [
-        PyPI.file_storage_domain,
-        TestPyPI.file_storage_domain,
-    ]
-    if req.url and comes_from.link.netloc in domains_not_allowed:
-        # Explicitly disallow pypi packages that depend on external urls
-        raise InstallationError(
-            "Packages installed from PyPI cannot depend on packages "
-            "which are not also hosted on PyPI.\n"
-            "%s depends on %s " % (comes_from.name, req)
-        )
-
-    return InstallRequirement(
-        req, comes_from, isolated=isolated, wheel_cache=wheel_cache,
-        use_pep517=use_pep517
-    )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_file.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_file.py
deleted file mode 100644
index 726f2f6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_file.py
+++ /dev/null
@@ -1,382 +0,0 @@
-"""
-Requirements file parsing
-"""
-
-from __future__ import absolute_import
-
-import optparse
-import os
-import re
-import shlex
-import sys
-
-from pip._vendor.six.moves import filterfalse
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-
-from pip._internal.cli import cmdoptions
-from pip._internal.download import get_file_content
-from pip._internal.exceptions import RequirementsFileParseError
-from pip._internal.req.constructors import (
-    install_req_from_editable, install_req_from_line,
-)
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Iterator, Tuple, Optional, List, Callable, Text
-    )
-    from pip._internal.req import InstallRequirement  # noqa: F401
-    from pip._internal.cache import WheelCache  # noqa: F401
-    from pip._internal.index import PackageFinder  # noqa: F401
-    from pip._internal.download import PipSession  # noqa: F401
-
-    ReqFileLines = Iterator[Tuple[int, Text]]
-
-__all__ = ['parse_requirements']
-
-SCHEME_RE = re.compile(r'^(http|https|file):', re.I)
-COMMENT_RE = re.compile(r'(^|\s)+#.*$')
-
-# Matches environment variable-style values in '${MY_VARIABLE_1}' with the
-# variable name consisting of only uppercase letters, digits or the '_'
-# (underscore). This follows the POSIX standard defined in IEEE Std 1003.1,
-# 2013 Edition.
-ENV_VAR_RE = re.compile(r'(?P<var>\$\{(?P<name>[A-Z0-9_]+)\})')
-
-SUPPORTED_OPTIONS = [
-    cmdoptions.constraints,
-    cmdoptions.editable,
-    cmdoptions.requirements,
-    cmdoptions.no_index,
-    cmdoptions.index_url,
-    cmdoptions.find_links,
-    cmdoptions.extra_index_url,
-    cmdoptions.always_unzip,
-    cmdoptions.no_binary,
-    cmdoptions.only_binary,
-    cmdoptions.pre,
-    cmdoptions.trusted_host,
-    cmdoptions.require_hashes,
-]  # type: List[Callable[..., optparse.Option]]
-
-# options to be passed to requirements
-SUPPORTED_OPTIONS_REQ = [
-    cmdoptions.install_options,
-    cmdoptions.global_options,
-    cmdoptions.hash,
-]  # type: List[Callable[..., optparse.Option]]
-
-# the 'dest' string values
-SUPPORTED_OPTIONS_REQ_DEST = [str(o().dest) for o in SUPPORTED_OPTIONS_REQ]
-
-
-def parse_requirements(
-    filename,  # type: str
-    finder=None,  # type: Optional[PackageFinder]
-    comes_from=None,  # type: Optional[str]
-    options=None,  # type: Optional[optparse.Values]
-    session=None,  # type: Optional[PipSession]
-    constraint=False,  # type: bool
-    wheel_cache=None,  # type: Optional[WheelCache]
-    use_pep517=None  # type: Optional[bool]
-):
-    # type: (...) -> Iterator[InstallRequirement]
-    """Parse a requirements file and yield InstallRequirement instances.
-
-    :param filename:    Path or url of requirements file.
-    :param finder:      Instance of pip.index.PackageFinder.
-    :param comes_from:  Origin description of requirements.
-    :param options:     cli options.
-    :param session:     Instance of pip.download.PipSession.
-    :param constraint:  If true, parsing a constraint file rather than
-        requirements file.
-    :param wheel_cache: Instance of pip.wheel.WheelCache
-    :param use_pep517:  Value of the --use-pep517 option.
-    """
-    if session is None:
-        raise TypeError(
-            "parse_requirements() missing 1 required keyword argument: "
-            "'session'"
-        )
-
-    _, content = get_file_content(
-        filename, comes_from=comes_from, session=session
-    )
-
-    lines_enum = preprocess(content, options)
-
-    for line_number, line in lines_enum:
-        req_iter = process_line(line, filename, line_number, finder,
-                                comes_from, options, session, wheel_cache,
-                                use_pep517=use_pep517, constraint=constraint)
-        for req in req_iter:
-            yield req
-
-
-def preprocess(content, options):
-    # type: (Text, Optional[optparse.Values]) -> ReqFileLines
-    """Split, filter, and join lines, and return a line iterator
-
-    :param content: the content of the requirements file
-    :param options: cli options
-    """
-    lines_enum = enumerate(content.splitlines(), start=1)  # type: ReqFileLines
-    lines_enum = join_lines(lines_enum)
-    lines_enum = ignore_comments(lines_enum)
-    lines_enum = skip_regex(lines_enum, options)
-    lines_enum = expand_env_variables(lines_enum)
-    return lines_enum
-
-
-def process_line(
-    line,  # type: Text
-    filename,  # type: str
-    line_number,  # type: int
-    finder=None,  # type: Optional[PackageFinder]
-    comes_from=None,  # type: Optional[str]
-    options=None,  # type: Optional[optparse.Values]
-    session=None,  # type: Optional[PipSession]
-    wheel_cache=None,  # type: Optional[WheelCache]
-    use_pep517=None,  # type: Optional[bool]
-    constraint=False  # type: bool
-):
-    # type: (...) -> Iterator[InstallRequirement]
-    """Process a single requirements line; This can result in creating/yielding
-    requirements, or updating the finder.
-
-    For lines that contain requirements, the only options that have an effect
-    are from SUPPORTED_OPTIONS_REQ, and they are scoped to the
-    requirement. Other options from SUPPORTED_OPTIONS may be present, but are
-    ignored.
-
-    For lines that do not contain requirements, the only options that have an
-    effect are from SUPPORTED_OPTIONS. Options from SUPPORTED_OPTIONS_REQ may
-    be present, but are ignored. These lines may contain multiple options
-    (although our docs imply only one is supported), and all our parsed and
-    affect the finder.
-
-    :param constraint: If True, parsing a constraints file.
-    :param options: OptionParser options that we may update
-    """
-    parser = build_parser(line)
-    defaults = parser.get_default_values()
-    defaults.index_url = None
-    if finder:
-        defaults.format_control = finder.format_control
-    args_str, options_str = break_args_options(line)
-    # Prior to 2.7.3, shlex cannot deal with unicode entries
-    if sys.version_info < (2, 7, 3):
-        # https://github.com/python/mypy/issues/1174
-        options_str = options_str.encode('utf8')  # type: ignore
-    # https://github.com/python/mypy/issues/1174
-    opts, _ = parser.parse_args(
-        shlex.split(options_str), defaults)  # type: ignore
-
-    # preserve for the nested code path
-    line_comes_from = '%s %s (line %s)' % (
-        '-c' if constraint else '-r', filename, line_number,
-    )
-
-    # yield a line requirement
-    if args_str:
-        isolated = options.isolated_mode if options else False
-        if options:
-            cmdoptions.check_install_build_global(options, opts)
-        # get the options that apply to requirements
-        req_options = {}
-        for dest in SUPPORTED_OPTIONS_REQ_DEST:
-            if dest in opts.__dict__ and opts.__dict__[dest]:
-                req_options[dest] = opts.__dict__[dest]
-        yield install_req_from_line(
-            args_str, line_comes_from, constraint=constraint,
-            use_pep517=use_pep517,
-            isolated=isolated, options=req_options, wheel_cache=wheel_cache
-        )
-
-    # yield an editable requirement
-    elif opts.editables:
-        isolated = options.isolated_mode if options else False
-        yield install_req_from_editable(
-            opts.editables[0], comes_from=line_comes_from,
-            use_pep517=use_pep517,
-            constraint=constraint, isolated=isolated, wheel_cache=wheel_cache
-        )
-
-    # parse a nested requirements file
-    elif opts.requirements or opts.constraints:
-        if opts.requirements:
-            req_path = opts.requirements[0]
-            nested_constraint = False
-        else:
-            req_path = opts.constraints[0]
-            nested_constraint = True
-        # original file is over http
-        if SCHEME_RE.search(filename):
-            # do a url join so relative paths work
-            req_path = urllib_parse.urljoin(filename, req_path)
-        # original file and nested file are paths
-        elif not SCHEME_RE.search(req_path):
-            # do a join so relative paths work
-            req_path = os.path.join(os.path.dirname(filename), req_path)
-        # TODO: Why not use `comes_from='-r {} (line {})'` here as well?
-        parsed_reqs = parse_requirements(
-            req_path, finder, comes_from, options, session,
-            constraint=nested_constraint, wheel_cache=wheel_cache
-        )
-        for req in parsed_reqs:
-            yield req
-
-    # percolate hash-checking option upward
-    elif opts.require_hashes:
-        options.require_hashes = opts.require_hashes
-
-    # set finder options
-    elif finder:
-        if opts.index_url:
-            finder.index_urls = [opts.index_url]
-        if opts.no_index is True:
-            finder.index_urls = []
-        if opts.extra_index_urls:
-            finder.index_urls.extend(opts.extra_index_urls)
-        if opts.find_links:
-            # FIXME: it would be nice to keep track of the source
-            # of the find_links: support a find-links local path
-            # relative to a requirements file.
-            value = opts.find_links[0]
-            req_dir = os.path.dirname(os.path.abspath(filename))
-            relative_to_reqs_file = os.path.join(req_dir, value)
-            if os.path.exists(relative_to_reqs_file):
-                value = relative_to_reqs_file
-            finder.find_links.append(value)
-        if opts.pre:
-            finder.allow_all_prereleases = True
-        if opts.trusted_hosts:
-            finder.secure_origins.extend(
-                ("*", host, "*") for host in opts.trusted_hosts)
-
-
-def break_args_options(line):
-    # type: (Text) -> Tuple[str, Text]
-    """Break up the line into an args and options string.  We only want to shlex
-    (and then optparse) the options, not the args.  args can contain markers
-    which are corrupted by shlex.
-    """
-    tokens = line.split(' ')
-    args = []
-    options = tokens[:]
-    for token in tokens:
-        if token.startswith('-') or token.startswith('--'):
-            break
-        else:
-            args.append(token)
-            options.pop(0)
-    return ' '.join(args), ' '.join(options)  # type: ignore
-
-
-def build_parser(line):
-    # type: (Text) -> optparse.OptionParser
-    """
-    Return a parser for parsing requirement lines
-    """
-    parser = optparse.OptionParser(add_help_option=False)
-
-    option_factories = SUPPORTED_OPTIONS + SUPPORTED_OPTIONS_REQ
-    for option_factory in option_factories:
-        option = option_factory()
-        parser.add_option(option)
-
-    # By default optparse sys.exits on parsing errors. We want to wrap
-    # that in our own exception.
-    def parser_exit(self, msg):
-        # add offending line
-        msg = 'Invalid requirement: %s\n%s' % (line, msg)
-        raise RequirementsFileParseError(msg)
-    # NOTE: mypy disallows assigning to a method
-    #       https://github.com/python/mypy/issues/2427
-    parser.exit = parser_exit  # type: ignore
-
-    return parser
-
-
-def join_lines(lines_enum):
-    # type: (ReqFileLines) -> ReqFileLines
-    """Joins a line ending in '\' with the previous line (except when following
-    comments).  The joined line takes on the index of the first line.
-    """
-    primary_line_number = None
-    new_line = []  # type: List[Text]
-    for line_number, line in lines_enum:
-        if not line.endswith('\\') or COMMENT_RE.match(line):
-            if COMMENT_RE.match(line):
-                # this ensures comments are always matched later
-                line = ' ' + line
-            if new_line:
-                new_line.append(line)
-                yield primary_line_number, ''.join(new_line)
-                new_line = []
-            else:
-                yield line_number, line
-        else:
-            if not new_line:
-                primary_line_number = line_number
-            new_line.append(line.strip('\\'))
-
-    # last line contains \
-    if new_line:
-        yield primary_line_number, ''.join(new_line)
-
-    # TODO: handle space after '\'.
-
-
-def ignore_comments(lines_enum):
-    # type: (ReqFileLines) -> ReqFileLines
-    """
-    Strips comments and filter empty lines.
-    """
-    for line_number, line in lines_enum:
-        line = COMMENT_RE.sub('', line)
-        line = line.strip()
-        if line:
-            yield line_number, line
-
-
-def skip_regex(lines_enum, options):
-    # type: (ReqFileLines, Optional[optparse.Values]) -> ReqFileLines
-    """
-    Skip lines that match '--skip-requirements-regex' pattern
-
-    Note: the regex pattern is only built once
-    """
-    skip_regex = options.skip_requirements_regex if options else None
-    if skip_regex:
-        pattern = re.compile(skip_regex)
-        lines_enum = filterfalse(lambda e: pattern.search(e[1]), lines_enum)
-    return lines_enum
-
-
-def expand_env_variables(lines_enum):
-    # type: (ReqFileLines) -> ReqFileLines
-    """Replace all environment variables that can be retrieved via `os.getenv`.
-
-    The only allowed format for environment variables defined in the
-    requirement file is `${MY_VARIABLE_1}` to ensure two things:
-
-    1. Strings that contain a `$` aren't accidentally (partially) expanded.
-    2. Ensure consistency across platforms for requirement files.
-
-    These points are the result of a discusssion on the `github pull
-    request #3514 <https://github.com/pypa/pip/pull/3514>`_.
-
-    Valid characters in variable names follow the `POSIX standard
-    <http://pubs.opengroup.org/onlinepubs/9699919799/>`_ and are limited
-    to uppercase letter, digits and the `_` (underscore).
-    """
-    for line_number, line in lines_enum:
-        for env_var, var_name in ENV_VAR_RE.findall(line):
-            value = os.getenv(var_name)
-            if not value:
-                continue
-
-            line = line.replace(env_var, value)
-
-        yield line_number, line
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_install.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_install.py
deleted file mode 100644
index a4834b0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_install.py
+++ /dev/null
@@ -1,1021 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import os
-import shutil
-import sys
-import sysconfig
-import zipfile
-from distutils.util import change_root
-
-from pip._vendor import pkg_resources, six
-from pip._vendor.packaging.requirements import Requirement
-from pip._vendor.packaging.utils import canonicalize_name
-from pip._vendor.packaging.version import Version
-from pip._vendor.packaging.version import parse as parse_version
-from pip._vendor.pep517.wrappers import Pep517HookCaller
-
-from pip._internal import wheel
-from pip._internal.build_env import NoOpBuildEnvironment
-from pip._internal.exceptions import InstallationError
-from pip._internal.locations import (
-    PIP_DELETE_MARKER_FILENAME, running_under_virtualenv,
-)
-from pip._internal.models.link import Link
-from pip._internal.pyproject import load_pyproject_toml, make_pyproject_path
-from pip._internal.req.req_uninstall import UninstallPathSet
-from pip._internal.utils.compat import native_str
-from pip._internal.utils.hashes import Hashes
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import (
-    _make_build_dir, ask_path_exists, backup_dir, call_subprocess,
-    display_path, dist_in_site_packages, dist_in_usersite, ensure_dir,
-    get_installed_version, redact_password_from_url, rmtree,
-)
-from pip._internal.utils.packaging import get_metadata
-from pip._internal.utils.setuptools_build import SETUPTOOLS_SHIM
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.utils.ui import open_spinner
-from pip._internal.vcs import vcs
-from pip._internal.wheel import move_wheel_files
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Optional, Iterable, List, Union, Any, Text, Sequence, Dict
-    )
-    from pip._internal.build_env import BuildEnvironment  # noqa: F401
-    from pip._internal.cache import WheelCache  # noqa: F401
-    from pip._internal.index import PackageFinder  # noqa: F401
-    from pip._vendor.pkg_resources import Distribution  # noqa: F401
-    from pip._vendor.packaging.specifiers import SpecifierSet  # noqa: F401
-    from pip._vendor.packaging.markers import Marker  # noqa: F401
-
-
-logger = logging.getLogger(__name__)
-
-
-class InstallRequirement(object):
-    """
-    Represents something that may be installed later on, may have information
-    about where to fetch the relavant requirement and also contains logic for
-    installing the said requirement.
-    """
-
-    def __init__(
-        self,
-        req,  # type: Optional[Requirement]
-        comes_from,  # type: Optional[Union[str, InstallRequirement]]
-        source_dir=None,  # type: Optional[str]
-        editable=False,  # type: bool
-        link=None,  # type: Optional[Link]
-        update=True,  # type: bool
-        markers=None,  # type: Optional[Marker]
-        use_pep517=None,  # type: Optional[bool]
-        isolated=False,  # type: bool
-        options=None,  # type: Optional[Dict[str, Any]]
-        wheel_cache=None,  # type: Optional[WheelCache]
-        constraint=False,  # type: bool
-        extras=()  # type: Iterable[str]
-    ):
-        # type: (...) -> None
-        assert req is None or isinstance(req, Requirement), req
-        self.req = req
-        self.comes_from = comes_from
-        self.constraint = constraint
-        if source_dir is not None:
-            self.source_dir = os.path.normpath(os.path.abspath(source_dir))
-        else:
-            self.source_dir = None
-        self.editable = editable
-
-        self._wheel_cache = wheel_cache
-        if link is None and req and req.url:
-            # PEP 508 URL requirement
-            link = Link(req.url)
-        self.link = self.original_link = link
-
-        if extras:
-            self.extras = extras
-        elif req:
-            self.extras = {
-                pkg_resources.safe_extra(extra) for extra in req.extras
-            }
-        else:
-            self.extras = set()
-        if markers is None and req:
-            markers = req.marker
-        self.markers = markers
-
-        self._egg_info_path = None  # type: Optional[str]
-        # This holds the pkg_resources.Distribution object if this requirement
-        # is already available:
-        self.satisfied_by = None
-        # This hold the pkg_resources.Distribution object if this requirement
-        # conflicts with another installed distribution:
-        self.conflicts_with = None
-        # Temporary build location
-        self._temp_build_dir = TempDirectory(kind="req-build")
-        # Used to store the global directory where the _temp_build_dir should
-        # have been created. Cf _correct_build_location method.
-        self._ideal_build_dir = None  # type: Optional[str]
-        # True if the editable should be updated:
-        self.update = update
-        # Set to True after successful installation
-        self.install_succeeded = None  # type: Optional[bool]
-        # UninstallPathSet of uninstalled distribution (for possible rollback)
-        self.uninstalled_pathset = None
-        self.options = options if options else {}
-        # Set to True after successful preparation of this requirement
-        self.prepared = False
-        self.is_direct = False
-
-        self.isolated = isolated
-        self.build_env = NoOpBuildEnvironment()  # type: BuildEnvironment
-
-        # For PEP 517, the directory where we request the project metadata
-        # gets stored. We need this to pass to build_wheel, so the backend
-        # can ensure that the wheel matches the metadata (see the PEP for
-        # details).
-        self.metadata_directory = None  # type: Optional[str]
-
-        # The static build requirements (from pyproject.toml)
-        self.pyproject_requires = None  # type: Optional[List[str]]
-
-        # Build requirements that we will check are available
-        self.requirements_to_check = []  # type: List[str]
-
-        # The PEP 517 backend we should use to build the project
-        self.pep517_backend = None  # type: Optional[Pep517HookCaller]
-
-        # Are we using PEP 517 for this requirement?
-        # After pyproject.toml has been loaded, the only valid values are True
-        # and False. Before loading, None is valid (meaning "use the default").
-        # Setting an explicit value before loading pyproject.toml is supported,
-        # but after loading this flag should be treated as read only.
-        self.use_pep517 = use_pep517
-
-    def __str__(self):
-        if self.req:
-            s = str(self.req)
-            if self.link:
-                s += ' from %s' % redact_password_from_url(self.link.url)
-        elif self.link:
-            s = redact_password_from_url(self.link.url)
-        else:
-            s = '<InstallRequirement>'
-        if self.satisfied_by is not None:
-            s += ' in %s' % display_path(self.satisfied_by.location)
-        if self.comes_from:
-            if isinstance(self.comes_from, six.string_types):
-                comes_from = self.comes_from
-            else:
-                comes_from = self.comes_from.from_path()
-            if comes_from:
-                s += ' (from %s)' % comes_from
-        return s
-
-    def __repr__(self):
-        return '<%s object: %s editable=%r>' % (
-            self.__class__.__name__, str(self), self.editable)
-
-    def populate_link(self, finder, upgrade, require_hashes):
-        # type: (PackageFinder, bool, bool) -> None
-        """Ensure that if a link can be found for this, that it is found.
-
-        Note that self.link may still be None - if Upgrade is False and the
-        requirement is already installed.
-
-        If require_hashes is True, don't use the wheel cache, because cached
-        wheels, always built locally, have different hashes than the files
-        downloaded from the index server and thus throw false hash mismatches.
-        Furthermore, cached wheels at present have undeterministic contents due
-        to file modification times.
-        """
-        if self.link is None:
-            self.link = finder.find_requirement(self, upgrade)
-        if self._wheel_cache is not None and not require_hashes:
-            old_link = self.link
-            self.link = self._wheel_cache.get(self.link, self.name)
-            if old_link != self.link:
-                logger.debug('Using cached wheel link: %s', self.link)
-
-    # Things that are valid for all kinds of requirements?
-    @property
-    def name(self):
-        # type: () -> Optional[str]
-        if self.req is None:
-            return None
-        return native_str(pkg_resources.safe_name(self.req.name))
-
-    @property
-    def specifier(self):
-        # type: () -> SpecifierSet
-        return self.req.specifier
-
-    @property
-    def is_pinned(self):
-        # type: () -> bool
-        """Return whether I am pinned to an exact version.
-
-        For example, some-package==1.2 is pinned; some-package>1.2 is not.
-        """
-        specifiers = self.specifier
-        return (len(specifiers) == 1 and
-                next(iter(specifiers)).operator in {'==', '==='})
-
-    @property
-    def installed_version(self):
-        return get_installed_version(self.name)
-
-    def match_markers(self, extras_requested=None):
-        # type: (Optional[Iterable[str]]) -> bool
-        if not extras_requested:
-            # Provide an extra to safely evaluate the markers
-            # without matching any extra
-            extras_requested = ('',)
-        if self.markers is not None:
-            return any(
-                self.markers.evaluate({'extra': extra})
-                for extra in extras_requested)
-        else:
-            return True
-
-    @property
-    def has_hash_options(self):
-        # type: () -> bool
-        """Return whether any known-good hashes are specified as options.
-
-        These activate --require-hashes mode; hashes specified as part of a
-        URL do not.
-
-        """
-        return bool(self.options.get('hashes', {}))
-
-    def hashes(self, trust_internet=True):
-        # type: (bool) -> Hashes
-        """Return a hash-comparer that considers my option- and URL-based
-        hashes to be known-good.
-
-        Hashes in URLs--ones embedded in the requirements file, not ones
-        downloaded from an index server--are almost peers with ones from
-        flags. They satisfy --require-hashes (whether it was implicitly or
-        explicitly activated) but do not activate it. md5 and sha224 are not
-        allowed in flags, which should nudge people toward good algos. We
-        always OR all hashes together, even ones from URLs.
-
-        :param trust_internet: Whether to trust URL-based (#md5=...) hashes
-            downloaded from the internet, as by populate_link()
-
-        """
-        good_hashes = self.options.get('hashes', {}).copy()
-        link = self.link if trust_internet else self.original_link
-        if link and link.hash:
-            good_hashes.setdefault(link.hash_name, []).append(link.hash)
-        return Hashes(good_hashes)
-
-    def from_path(self):
-        # type: () -> Optional[str]
-        """Format a nice indicator to show where this "comes from"
-        """
-        if self.req is None:
-            return None
-        s = str(self.req)
-        if self.comes_from:
-            if isinstance(self.comes_from, six.string_types):
-                comes_from = self.comes_from
-            else:
-                comes_from = self.comes_from.from_path()
-            if comes_from:
-                s += '->' + comes_from
-        return s
-
-    def build_location(self, build_dir):
-        # type: (str) -> Optional[str]
-        assert build_dir is not None
-        if self._temp_build_dir.path is not None:
-            return self._temp_build_dir.path
-        if self.req is None:
-            # for requirement via a path to a directory: the name of the
-            # package is not available yet so we create a temp directory
-            # Once run_egg_info will have run, we'll be able
-            # to fix it via _correct_build_location
-            # Some systems have /tmp as a symlink which confuses custom
-            # builds (such as numpy). Thus, we ensure that the real path
-            # is returned.
-            self._temp_build_dir.create()
-            self._ideal_build_dir = build_dir
-
-            return self._temp_build_dir.path
-        if self.editable:
-            name = self.name.lower()
-        else:
-            name = self.name
-        # FIXME: Is there a better place to create the build_dir? (hg and bzr
-        # need this)
-        if not os.path.exists(build_dir):
-            logger.debug('Creating directory %s', build_dir)
-            _make_build_dir(build_dir)
-        return os.path.join(build_dir, name)
-
-    def _correct_build_location(self):
-        # type: () -> None
-        """Move self._temp_build_dir to self._ideal_build_dir/self.req.name
-
-        For some requirements (e.g. a path to a directory), the name of the
-        package is not available until we run egg_info, so the build_location
-        will return a temporary directory and store the _ideal_build_dir.
-
-        This is only called by self.run_egg_info to fix the temporary build
-        directory.
-        """
-        if self.source_dir is not None:
-            return
-        assert self.req is not None
-        assert self._temp_build_dir.path
-        assert (self._ideal_build_dir is not None and
-                self._ideal_build_dir.path)  # type: ignore
-        old_location = self._temp_build_dir.path
-        self._temp_build_dir.path = None
-
-        new_location = self.build_location(self._ideal_build_dir)
-        if os.path.exists(new_location):
-            raise InstallationError(
-                'A package already exists in %s; please remove it to continue'
-                % display_path(new_location))
-        logger.debug(
-            'Moving package %s from %s to new location %s',
-            self, display_path(old_location), display_path(new_location),
-        )
-        shutil.move(old_location, new_location)
-        self._temp_build_dir.path = new_location
-        self._ideal_build_dir = None
-        self.source_dir = os.path.normpath(os.path.abspath(new_location))
-        self._egg_info_path = None
-
-        # Correct the metadata directory, if it exists
-        if self.metadata_directory:
-            old_meta = self.metadata_directory
-            rel = os.path.relpath(old_meta, start=old_location)
-            new_meta = os.path.join(new_location, rel)
-            new_meta = os.path.normpath(os.path.abspath(new_meta))
-            self.metadata_directory = new_meta
-
-    def remove_temporary_source(self):
-        # type: () -> None
-        """Remove the source files from this requirement, if they are marked
-        for deletion"""
-        if self.source_dir and os.path.exists(
-                os.path.join(self.source_dir, PIP_DELETE_MARKER_FILENAME)):
-            logger.debug('Removing source in %s', self.source_dir)
-            rmtree(self.source_dir)
-        self.source_dir = None
-        self._temp_build_dir.cleanup()
-        self.build_env.cleanup()
-
-    def check_if_exists(self, use_user_site):
-        # type: (bool) -> bool
-        """Find an installed distribution that satisfies or conflicts
-        with this requirement, and set self.satisfied_by or
-        self.conflicts_with appropriately.
-        """
-        if self.req is None:
-            return False
-        try:
-            # get_distribution() will resolve the entire list of requirements
-            # anyway, and we've already determined that we need the requirement
-            # in question, so strip the marker so that we don't try to
-            # evaluate it.
-            no_marker = Requirement(str(self.req))
-            no_marker.marker = None
-            self.satisfied_by = pkg_resources.get_distribution(str(no_marker))
-            if self.editable and self.satisfied_by:
-                self.conflicts_with = self.satisfied_by
-                # when installing editables, nothing pre-existing should ever
-                # satisfy
-                self.satisfied_by = None
-                return True
-        except pkg_resources.DistributionNotFound:
-            return False
-        except pkg_resources.VersionConflict:
-            existing_dist = pkg_resources.get_distribution(
-                self.req.name
-            )
-            if use_user_site:
-                if dist_in_usersite(existing_dist):
-                    self.conflicts_with = existing_dist
-                elif (running_under_virtualenv() and
-                        dist_in_site_packages(existing_dist)):
-                    raise InstallationError(
-                        "Will not install to the user site because it will "
-                        "lack sys.path precedence to %s in %s" %
-                        (existing_dist.project_name, existing_dist.location)
-                    )
-            else:
-                self.conflicts_with = existing_dist
-        return True
-
-    # Things valid for wheels
-    @property
-    def is_wheel(self):
-        # type: () -> bool
-        if not self.link:
-            return False
-        return self.link.is_wheel
-
-    def move_wheel_files(
-        self,
-        wheeldir,  # type: str
-        root=None,  # type: Optional[str]
-        home=None,  # type: Optional[str]
-        prefix=None,  # type: Optional[str]
-        warn_script_location=True,  # type: bool
-        use_user_site=False,  # type: bool
-        pycompile=True  # type: bool
-    ):
-        # type: (...) -> None
-        move_wheel_files(
-            self.name, self.req, wheeldir,
-            user=use_user_site,
-            home=home,
-            root=root,
-            prefix=prefix,
-            pycompile=pycompile,
-            isolated=self.isolated,
-            warn_script_location=warn_script_location,
-        )
-
-    # Things valid for sdists
-    @property
-    def setup_py_dir(self):
-        # type: () -> str
-        return os.path.join(
-            self.source_dir,
-            self.link and self.link.subdirectory_fragment or '')
-
-    @property
-    def setup_py(self):
-        # type: () -> str
-        assert self.source_dir, "No source dir for %s" % self
-
-        setup_py = os.path.join(self.setup_py_dir, 'setup.py')
-
-        # Python2 __file__ should not be unicode
-        if six.PY2 and isinstance(setup_py, six.text_type):
-            setup_py = setup_py.encode(sys.getfilesystemencoding())
-
-        return setup_py
-
-    @property
-    def pyproject_toml(self):
-        # type: () -> str
-        assert self.source_dir, "No source dir for %s" % self
-
-        return make_pyproject_path(self.setup_py_dir)
-
-    def load_pyproject_toml(self):
-        # type: () -> None
-        """Load the pyproject.toml file.
-
-        After calling this routine, all of the attributes related to PEP 517
-        processing for this requirement have been set. In particular, the
-        use_pep517 attribute can be used to determine whether we should
-        follow the PEP 517 or legacy (setup.py) code path.
-        """
-        pep517_data = load_pyproject_toml(
-            self.use_pep517,
-            self.pyproject_toml,
-            self.setup_py,
-            str(self)
-        )
-
-        if pep517_data is None:
-            self.use_pep517 = False
-        else:
-            self.use_pep517 = True
-            requires, backend, check = pep517_data
-            self.requirements_to_check = check
-            self.pyproject_requires = requires
-            self.pep517_backend = Pep517HookCaller(self.setup_py_dir, backend)
-
-            # Use a custom function to call subprocesses
-            self.spin_message = ""
-
-            def runner(cmd, cwd=None, extra_environ=None):
-                with open_spinner(self.spin_message) as spinner:
-                    call_subprocess(
-                        cmd,
-                        cwd=cwd,
-                        extra_environ=extra_environ,
-                        show_stdout=False,
-                        spinner=spinner
-                    )
-                self.spin_message = ""
-
-            self.pep517_backend._subprocess_runner = runner
-
-    def prepare_metadata(self):
-        # type: () -> None
-        """Ensure that project metadata is available.
-
-        Under PEP 517, call the backend hook to prepare the metadata.
-        Under legacy processing, call setup.py egg-info.
-        """
-        assert self.source_dir
-
-        with indent_log():
-            if self.use_pep517:
-                self.prepare_pep517_metadata()
-            else:
-                self.run_egg_info()
-
-        if not self.req:
-            if isinstance(parse_version(self.metadata["Version"]), Version):
-                op = "=="
-            else:
-                op = "==="
-            self.req = Requirement(
-                "".join([
-                    self.metadata["Name"],
-                    op,
-                    self.metadata["Version"],
-                ])
-            )
-            self._correct_build_location()
-        else:
-            metadata_name = canonicalize_name(self.metadata["Name"])
-            if canonicalize_name(self.req.name) != metadata_name:
-                logger.warning(
-                    'Generating metadata for package %s '
-                    'produced metadata for project name %s. Fix your '
-                    '#egg=%s fragments.',
-                    self.name, metadata_name, self.name
-                )
-                self.req = Requirement(metadata_name)
-
-    def prepare_pep517_metadata(self):
-        # type: () -> None
-        assert self.pep517_backend is not None
-
-        metadata_dir = os.path.join(
-            self.setup_py_dir,
-            'pip-wheel-metadata'
-        )
-        ensure_dir(metadata_dir)
-
-        with self.build_env:
-            # Note that Pep517HookCaller implements a fallback for
-            # prepare_metadata_for_build_wheel, so we don't have to
-            # consider the possibility that this hook doesn't exist.
-            backend = self.pep517_backend
-            self.spin_message = "Preparing wheel metadata"
-            distinfo_dir = backend.prepare_metadata_for_build_wheel(
-                metadata_dir
-            )
-
-        self.metadata_directory = os.path.join(metadata_dir, distinfo_dir)
-
-    def run_egg_info(self):
-        # type: () -> None
-        if self.name:
-            logger.debug(
-                'Running setup.py (path:%s) egg_info for package %s',
-                self.setup_py, self.name,
-            )
-        else:
-            logger.debug(
-                'Running setup.py (path:%s) egg_info for package from %s',
-                self.setup_py, self.link,
-            )
-        script = SETUPTOOLS_SHIM % self.setup_py
-        base_cmd = [sys.executable, '-c', script]
-        if self.isolated:
-            base_cmd += ["--no-user-cfg"]
-        egg_info_cmd = base_cmd + ['egg_info']
-        # We can't put the .egg-info files at the root, because then the
-        # source code will be mistaken for an installed egg, causing
-        # problems
-        if self.editable:
-            egg_base_option = []  # type: List[str]
-        else:
-            egg_info_dir = os.path.join(self.setup_py_dir, 'pip-egg-info')
-            ensure_dir(egg_info_dir)
-            egg_base_option = ['--egg-base', 'pip-egg-info']
-        with self.build_env:
-            call_subprocess(
-                egg_info_cmd + egg_base_option,
-                cwd=self.setup_py_dir,
-                show_stdout=False,
-                command_desc='python setup.py egg_info')
-
-    @property
-    def egg_info_path(self):
-        # type: () -> str
-        if self._egg_info_path is None:
-            if self.editable:
-                base = self.source_dir
-            else:
-                base = os.path.join(self.setup_py_dir, 'pip-egg-info')
-            filenames = os.listdir(base)
-            if self.editable:
-                filenames = []
-                for root, dirs, files in os.walk(base):
-                    for dir in vcs.dirnames:
-                        if dir in dirs:
-                            dirs.remove(dir)
-                    # Iterate over a copy of ``dirs``, since mutating
-                    # a list while iterating over it can cause trouble.
-                    # (See https://github.com/pypa/pip/pull/462.)
-                    for dir in list(dirs):
-                        # Don't search in anything that looks like a virtualenv
-                        # environment
-                        if (
-                                os.path.lexists(
-                                    os.path.join(root, dir, 'bin', 'python')
-                                ) or
-                                os.path.exists(
-                                    os.path.join(
-                                        root, dir, 'Scripts', 'Python.exe'
-                                    )
-                                )):
-                            dirs.remove(dir)
-                        # Also don't search through tests
-                        elif dir == 'test' or dir == 'tests':
-                            dirs.remove(dir)
-                    filenames.extend([os.path.join(root, dir)
-                                      for dir in dirs])
-                filenames = [f for f in filenames if f.endswith('.egg-info')]
-
-            if not filenames:
-                raise InstallationError(
-                    "Files/directories not found in %s" % base
-                )
-            # if we have more than one match, we pick the toplevel one.  This
-            # can easily be the case if there is a dist folder which contains
-            # an extracted tarball for testing purposes.
-            if len(filenames) > 1:
-                filenames.sort(
-                    key=lambda x: x.count(os.path.sep) +
-                    (os.path.altsep and x.count(os.path.altsep) or 0)
-                )
-            self._egg_info_path = os.path.join(base, filenames[0])
-        return self._egg_info_path
-
-    @property
-    def metadata(self):
-        if not hasattr(self, '_metadata'):
-            self._metadata = get_metadata(self.get_dist())
-
-        return self._metadata
-
-    def get_dist(self):
-        # type: () -> Distribution
-        """Return a pkg_resources.Distribution for this requirement"""
-        if self.metadata_directory:
-            base_dir, distinfo = os.path.split(self.metadata_directory)
-            metadata = pkg_resources.PathMetadata(
-                base_dir, self.metadata_directory
-            )
-            dist_name = os.path.splitext(distinfo)[0]
-            typ = pkg_resources.DistInfoDistribution
-        else:
-            egg_info = self.egg_info_path.rstrip(os.path.sep)
-            base_dir = os.path.dirname(egg_info)
-            metadata = pkg_resources.PathMetadata(base_dir, egg_info)
-            dist_name = os.path.splitext(os.path.basename(egg_info))[0]
-            # https://github.com/python/mypy/issues/1174
-            typ = pkg_resources.Distribution  # type: ignore
-
-        return typ(
-            base_dir,
-            project_name=dist_name,
-            metadata=metadata,
-        )
-
-    def assert_source_matches_version(self):
-        # type: () -> None
-        assert self.source_dir
-        version = self.metadata['version']
-        if self.req.specifier and version not in self.req.specifier:
-            logger.warning(
-                'Requested %s, but installing version %s',
-                self,
-                version,
-            )
-        else:
-            logger.debug(
-                'Source in %s has version %s, which satisfies requirement %s',
-                display_path(self.source_dir),
-                version,
-                self,
-            )
-
-    # For both source distributions and editables
-    def ensure_has_source_dir(self, parent_dir):
-        # type: (str) -> str
-        """Ensure that a source_dir is set.
-
-        This will create a temporary build dir if the name of the requirement
-        isn't known yet.
-
-        :param parent_dir: The ideal pip parent_dir for the source_dir.
-            Generally src_dir for editables and build_dir for sdists.
-        :return: self.source_dir
-        """
-        if self.source_dir is None:
-            self.source_dir = self.build_location(parent_dir)
-        return self.source_dir
-
-    # For editable installations
-    def install_editable(
-        self,
-        install_options,  # type: List[str]
-        global_options=(),  # type: Sequence[str]
-        prefix=None  # type: Optional[str]
-    ):
-        # type: (...) -> None
-        logger.info('Running setup.py develop for %s', self.name)
-
-        if self.isolated:
-            global_options = list(global_options) + ["--no-user-cfg"]
-
-        if prefix:
-            prefix_param = ['--prefix={}'.format(prefix)]
-            install_options = list(install_options) + prefix_param
-
-        with indent_log():
-            # FIXME: should we do --install-headers here too?
-            with self.build_env:
-                call_subprocess(
-                    [
-                        sys.executable,
-                        '-c',
-                        SETUPTOOLS_SHIM % self.setup_py
-                    ] +
-                    list(global_options) +
-                    ['develop', '--no-deps'] +
-                    list(install_options),
-
-                    cwd=self.setup_py_dir,
-                    show_stdout=False,
-                )
-
-        self.install_succeeded = True
-
-    def update_editable(self, obtain=True):
-        # type: (bool) -> None
-        if not self.link:
-            logger.debug(
-                "Cannot update repository at %s; repository location is "
-                "unknown",
-                self.source_dir,
-            )
-            return
-        assert self.editable
-        assert self.source_dir
-        if self.link.scheme == 'file':
-            # Static paths don't get updated
-            return
-        assert '+' in self.link.url, "bad url: %r" % self.link.url
-        if not self.update:
-            return
-        vc_type, url = self.link.url.split('+', 1)
-        backend = vcs.get_backend(vc_type)
-        if backend:
-            vcs_backend = backend(self.link.url)
-            if obtain:
-                vcs_backend.obtain(self.source_dir)
-            else:
-                vcs_backend.export(self.source_dir)
-        else:
-            assert 0, (
-                'Unexpected version control type (in %s): %s'
-                % (self.link, vc_type))
-
-    # Top-level Actions
-    def uninstall(self, auto_confirm=False, verbose=False,
-                  use_user_site=False):
-        # type: (bool, bool, bool) -> Optional[UninstallPathSet]
-        """
-        Uninstall the distribution currently satisfying this requirement.
-
-        Prompts before removing or modifying files unless
-        ``auto_confirm`` is True.
-
-        Refuses to delete or modify files outside of ``sys.prefix`` -
-        thus uninstallation within a virtual environment can only
-        modify that virtual environment, even if the virtualenv is
-        linked to global site-packages.
-
-        """
-        if not self.check_if_exists(use_user_site):
-            logger.warning("Skipping %s as it is not installed.", self.name)
-            return None
-        dist = self.satisfied_by or self.conflicts_with
-
-        uninstalled_pathset = UninstallPathSet.from_dist(dist)
-        uninstalled_pathset.remove(auto_confirm, verbose)
-        return uninstalled_pathset
-
-    def _clean_zip_name(self, name, prefix):  # only used by archive.
-        assert name.startswith(prefix + os.path.sep), (
-            "name %r doesn't start with prefix %r" % (name, prefix)
-        )
-        name = name[len(prefix) + 1:]
-        name = name.replace(os.path.sep, '/')
-        return name
-
-    def _get_archive_name(self, path, parentdir, rootdir):
-        # type: (str, str, str) -> str
-        path = os.path.join(parentdir, path)
-        name = self._clean_zip_name(path, rootdir)
-        return self.name + '/' + name
-
-    # TODO: Investigate if this should be kept in InstallRequirement
-    #       Seems to be used only when VCS + downloads
-    def archive(self, build_dir):
-        # type: (str) -> None
-        assert self.source_dir
-        create_archive = True
-        archive_name = '%s-%s.zip' % (self.name, self.metadata["version"])
-        archive_path = os.path.join(build_dir, archive_name)
-        if os.path.exists(archive_path):
-            response = ask_path_exists(
-                'The file %s exists. (i)gnore, (w)ipe, (b)ackup, (a)bort ' %
-                display_path(archive_path), ('i', 'w', 'b', 'a'))
-            if response == 'i':
-                create_archive = False
-            elif response == 'w':
-                logger.warning('Deleting %s', display_path(archive_path))
-                os.remove(archive_path)
-            elif response == 'b':
-                dest_file = backup_dir(archive_path)
-                logger.warning(
-                    'Backing up %s to %s',
-                    display_path(archive_path),
-                    display_path(dest_file),
-                )
-                shutil.move(archive_path, dest_file)
-            elif response == 'a':
-                sys.exit(-1)
-        if create_archive:
-            zip = zipfile.ZipFile(
-                archive_path, 'w', zipfile.ZIP_DEFLATED,
-                allowZip64=True
-            )
-            dir = os.path.normcase(os.path.abspath(self.setup_py_dir))
-            for dirpath, dirnames, filenames in os.walk(dir):
-                if 'pip-egg-info' in dirnames:
-                    dirnames.remove('pip-egg-info')
-                for dirname in dirnames:
-                    dir_arcname = self._get_archive_name(dirname,
-                                                         parentdir=dirpath,
-                                                         rootdir=dir)
-                    zipdir = zipfile.ZipInfo(dir_arcname + '/')
-                    zipdir.external_attr = 0x1ED << 16  # 0o755
-                    zip.writestr(zipdir, '')
-                for filename in filenames:
-                    if filename == PIP_DELETE_MARKER_FILENAME:
-                        continue
-                    file_arcname = self._get_archive_name(filename,
-                                                          parentdir=dirpath,
-                                                          rootdir=dir)
-                    filename = os.path.join(dirpath, filename)
-                    zip.write(filename, file_arcname)
-            zip.close()
-            logger.info('Saved %s', display_path(archive_path))
-
-    def install(
-        self,
-        install_options,  # type: List[str]
-        global_options=None,  # type: Optional[Sequence[str]]
-        root=None,  # type: Optional[str]
-        home=None,  # type: Optional[str]
-        prefix=None,  # type: Optional[str]
-        warn_script_location=True,  # type: bool
-        use_user_site=False,  # type: bool
-        pycompile=True  # type: bool
-    ):
-        # type: (...) -> None
-        global_options = global_options if global_options is not None else []
-        if self.editable:
-            self.install_editable(
-                install_options, global_options, prefix=prefix,
-            )
-            return
-        if self.is_wheel:
-            version = wheel.wheel_version(self.source_dir)
-            wheel.check_compatibility(version, self.name)
-
-            self.move_wheel_files(
-                self.source_dir, root=root, prefix=prefix, home=home,
-                warn_script_location=warn_script_location,
-                use_user_site=use_user_site, pycompile=pycompile,
-            )
-            self.install_succeeded = True
-            return
-
-        # Extend the list of global and install options passed on to
-        # the setup.py call with the ones from the requirements file.
-        # Options specified in requirements file override those
-        # specified on the command line, since the last option given
-        # to setup.py is the one that is used.
-        global_options = list(global_options) + \
-            self.options.get('global_options', [])
-        install_options = list(install_options) + \
-            self.options.get('install_options', [])
-
-        if self.isolated:
-            # https://github.com/python/mypy/issues/1174
-            global_options = global_options + ["--no-user-cfg"]  # type: ignore
-
-        with TempDirectory(kind="record") as temp_dir:
-            record_filename = os.path.join(temp_dir.path, 'install-record.txt')
-            install_args = self.get_install_args(
-                global_options, record_filename, root, prefix, pycompile,
-            )
-            msg = 'Running setup.py install for %s' % (self.name,)
-            with open_spinner(msg) as spinner:
-                with indent_log():
-                    with self.build_env:
-                        call_subprocess(
-                            install_args + install_options,
-                            cwd=self.setup_py_dir,
-                            show_stdout=False,
-                            spinner=spinner,
-                        )
-
-            if not os.path.exists(record_filename):
-                logger.debug('Record file %s not found', record_filename)
-                return
-            self.install_succeeded = True
-
-            def prepend_root(path):
-                if root is None or not os.path.isabs(path):
-                    return path
-                else:
-                    return change_root(root, path)
-
-            with open(record_filename) as f:
-                for line in f:
-                    directory = os.path.dirname(line)
-                    if directory.endswith('.egg-info'):
-                        egg_info_dir = prepend_root(directory)
-                        break
-                else:
-                    logger.warning(
-                        'Could not find .egg-info directory in install record'
-                        ' for %s',
-                        self,
-                    )
-                    # FIXME: put the record somewhere
-                    # FIXME: should this be an error?
-                    return
-            new_lines = []
-            with open(record_filename) as f:
-                for line in f:
-                    filename = line.strip()
-                    if os.path.isdir(filename):
-                        filename += os.path.sep
-                    new_lines.append(
-                        os.path.relpath(prepend_root(filename), egg_info_dir)
-                    )
-            new_lines.sort()
-            ensure_dir(egg_info_dir)
-            inst_files_path = os.path.join(egg_info_dir, 'installed-files.txt')
-            with open(inst_files_path, 'w') as f:
-                f.write('\n'.join(new_lines) + '\n')
-
-    def get_install_args(
-        self,
-        global_options,  # type: Sequence[str]
-        record_filename,  # type: str
-        root,  # type: Optional[str]
-        prefix,  # type: Optional[str]
-        pycompile  # type: bool
-    ):
-        # type: (...) -> List[str]
-        install_args = [sys.executable, "-u"]
-        install_args.append('-c')
-        install_args.append(SETUPTOOLS_SHIM % self.setup_py)
-        install_args += list(global_options) + \
-            ['install', '--record', record_filename]
-        install_args += ['--single-version-externally-managed']
-
-        if root is not None:
-            install_args += ['--root', root]
-        if prefix is not None:
-            install_args += ['--prefix', prefix]
-
-        if pycompile:
-            install_args += ["--compile"]
-        else:
-            install_args += ["--no-compile"]
-
-        if running_under_virtualenv():
-            py_ver_str = 'python' + sysconfig.get_python_version()
-            install_args += ['--install-headers',
-                             os.path.join(sys.prefix, 'include', 'site',
-                                          py_ver_str, self.name)]
-
-        return install_args
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_set.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_set.py
deleted file mode 100644
index d1410e9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_set.py
+++ /dev/null
@@ -1,197 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-from collections import OrderedDict
-
-from pip._internal.exceptions import InstallationError
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.wheel import Wheel
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional, List, Tuple, Dict, Iterable  # noqa: F401
-    from pip._internal.req.req_install import InstallRequirement  # noqa: F401
-
-
-logger = logging.getLogger(__name__)
-
-
-class RequirementSet(object):
-
-    def __init__(self, require_hashes=False, check_supported_wheels=True):
-        # type: (bool, bool) -> None
-        """Create a RequirementSet.
-        """
-
-        self.requirements = OrderedDict()  # type: Dict[str, InstallRequirement]  # noqa: E501
-        self.require_hashes = require_hashes
-        self.check_supported_wheels = check_supported_wheels
-
-        # Mapping of alias: real_name
-        self.requirement_aliases = {}  # type: Dict[str, str]
-        self.unnamed_requirements = []  # type: List[InstallRequirement]
-        self.successfully_downloaded = []  # type: List[InstallRequirement]
-        self.reqs_to_cleanup = []  # type: List[InstallRequirement]
-
-    def __str__(self):
-        reqs = [req for req in self.requirements.values()
-                if not req.comes_from]
-        reqs.sort(key=lambda req: req.name.lower())
-        return ' '.join([str(req.req) for req in reqs])
-
-    def __repr__(self):
-        reqs = [req for req in self.requirements.values()]
-        reqs.sort(key=lambda req: req.name.lower())
-        reqs_str = ', '.join([str(req.req) for req in reqs])
-        return ('<%s object; %d requirement(s): %s>'
-                % (self.__class__.__name__, len(reqs), reqs_str))
-
-    def add_requirement(
-        self,
-        install_req,  # type: InstallRequirement
-        parent_req_name=None,  # type: Optional[str]
-        extras_requested=None  # type: Optional[Iterable[str]]
-    ):
-        # type: (...) -> Tuple[List[InstallRequirement], Optional[InstallRequirement]]  # noqa: E501
-        """Add install_req as a requirement to install.
-
-        :param parent_req_name: The name of the requirement that needed this
-            added. The name is used because when multiple unnamed requirements
-            resolve to the same name, we could otherwise end up with dependency
-            links that point outside the Requirements set. parent_req must
-            already be added. Note that None implies that this is a user
-            supplied requirement, vs an inferred one.
-        :param extras_requested: an iterable of extras used to evaluate the
-            environment markers.
-        :return: Additional requirements to scan. That is either [] if
-            the requirement is not applicable, or [install_req] if the
-            requirement is applicable and has just been added.
-        """
-        name = install_req.name
-
-        # If the markers do not match, ignore this requirement.
-        if not install_req.match_markers(extras_requested):
-            logger.info(
-                "Ignoring %s: markers '%s' don't match your environment",
-                name, install_req.markers,
-            )
-            return [], None
-
-        # If the wheel is not supported, raise an error.
-        # Should check this after filtering out based on environment markers to
-        # allow specifying different wheels based on the environment/OS, in a
-        # single requirements file.
-        if install_req.link and install_req.link.is_wheel:
-            wheel = Wheel(install_req.link.filename)
-            if self.check_supported_wheels and not wheel.supported():
-                raise InstallationError(
-                    "%s is not a supported wheel on this platform." %
-                    wheel.filename
-                )
-
-        # This next bit is really a sanity check.
-        assert install_req.is_direct == (parent_req_name is None), (
-            "a direct req shouldn't have a parent and also, "
-            "a non direct req should have a parent"
-        )
-
-        # Unnamed requirements are scanned again and the requirement won't be
-        # added as a dependency until after scanning.
-        if not name:
-            # url or path requirement w/o an egg fragment
-            self.unnamed_requirements.append(install_req)
-            return [install_req], None
-
-        try:
-            existing_req = self.get_requirement(name)
-        except KeyError:
-            existing_req = None
-
-        has_conflicting_requirement = (
-            parent_req_name is None and
-            existing_req and
-            not existing_req.constraint and
-            existing_req.extras == install_req.extras and
-            existing_req.req.specifier != install_req.req.specifier
-        )
-        if has_conflicting_requirement:
-            raise InstallationError(
-                "Double requirement given: %s (already in %s, name=%r)"
-                % (install_req, existing_req, name)
-            )
-
-        # When no existing requirement exists, add the requirement as a
-        # dependency and it will be scanned again after.
-        if not existing_req:
-            self.requirements[name] = install_req
-            # FIXME: what about other normalizations?  E.g., _ vs. -?
-            if name.lower() != name:
-                self.requirement_aliases[name.lower()] = name
-            # We'd want to rescan this requirements later
-            return [install_req], install_req
-
-        # Assume there's no need to scan, and that we've already
-        # encountered this for scanning.
-        if install_req.constraint or not existing_req.constraint:
-            return [], existing_req
-
-        does_not_satisfy_constraint = (
-            install_req.link and
-            not (
-                existing_req.link and
-                install_req.link.path == existing_req.link.path
-            )
-        )
-        if does_not_satisfy_constraint:
-            self.reqs_to_cleanup.append(install_req)
-            raise InstallationError(
-                "Could not satisfy constraints for '%s': "
-                "installation from path or url cannot be "
-                "constrained to a version" % name,
-            )
-        # If we're now installing a constraint, mark the existing
-        # object for real installation.
-        existing_req.constraint = False
-        existing_req.extras = tuple(sorted(
-            set(existing_req.extras) | set(install_req.extras)
-        ))
-        logger.debug(
-            "Setting %s extras to: %s",
-            existing_req, existing_req.extras,
-        )
-        # Return the existing requirement for addition to the parent and
-        # scanning again.
-        return [existing_req], existing_req
-
-    def has_requirement(self, project_name):
-        # type: (str) -> bool
-        name = project_name.lower()
-        if (name in self.requirements and
-           not self.requirements[name].constraint or
-           name in self.requirement_aliases and
-           not self.requirements[self.requirement_aliases[name]].constraint):
-            return True
-        return False
-
-    @property
-    def has_requirements(self):
-        # type: () -> List[InstallRequirement]
-        return list(req for req in self.requirements.values() if not
-                    req.constraint) or self.unnamed_requirements
-
-    def get_requirement(self, project_name):
-        # type: (str) -> InstallRequirement
-        for name in project_name, project_name.lower():
-            if name in self.requirements:
-                return self.requirements[name]
-            if name in self.requirement_aliases:
-                return self.requirements[self.requirement_aliases[name]]
-        raise KeyError("No project with the name %r" % project_name)
-
-    def cleanup_files(self):
-        # type: () -> None
-        """Clean up files, remove builds."""
-        logger.debug('Cleaning up...')
-        with indent_log():
-            for req in self.reqs_to_cleanup:
-                req.remove_temporary_source()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_tracker.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_tracker.py
deleted file mode 100644
index 82e084a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_tracker.py
+++ /dev/null
@@ -1,88 +0,0 @@
-from __future__ import absolute_import
-
-import contextlib
-import errno
-import hashlib
-import logging
-import os
-
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Set, Iterator  # noqa: F401
-    from pip._internal.req.req_install import InstallRequirement  # noqa: F401
-    from pip._internal.models.link import Link  # noqa: F401
-
-logger = logging.getLogger(__name__)
-
-
-class RequirementTracker(object):
-
-    def __init__(self):
-        # type: () -> None
-        self._root = os.environ.get('PIP_REQ_TRACKER')
-        if self._root is None:
-            self._temp_dir = TempDirectory(delete=False, kind='req-tracker')
-            self._temp_dir.create()
-            self._root = os.environ['PIP_REQ_TRACKER'] = self._temp_dir.path
-            logger.debug('Created requirements tracker %r', self._root)
-        else:
-            self._temp_dir = None
-            logger.debug('Re-using requirements tracker %r', self._root)
-        self._entries = set()  # type: Set[InstallRequirement]
-
-    def __enter__(self):
-        return self
-
-    def __exit__(self, exc_type, exc_val, exc_tb):
-        self.cleanup()
-
-    def _entry_path(self, link):
-        # type: (Link) -> str
-        hashed = hashlib.sha224(link.url_without_fragment.encode()).hexdigest()
-        return os.path.join(self._root, hashed)
-
-    def add(self, req):
-        # type: (InstallRequirement) -> None
-        link = req.link
-        info = str(req)
-        entry_path = self._entry_path(link)
-        try:
-            with open(entry_path) as fp:
-                # Error, these's already a build in progress.
-                raise LookupError('%s is already being built: %s'
-                                  % (link, fp.read()))
-        except IOError as e:
-            if e.errno != errno.ENOENT:
-                raise
-            assert req not in self._entries
-            with open(entry_path, 'w') as fp:
-                fp.write(info)
-            self._entries.add(req)
-            logger.debug('Added %s to build tracker %r', req, self._root)
-
-    def remove(self, req):
-        # type: (InstallRequirement) -> None
-        link = req.link
-        self._entries.remove(req)
-        os.unlink(self._entry_path(link))
-        logger.debug('Removed %s from build tracker %r', req, self._root)
-
-    def cleanup(self):
-        # type: () -> None
-        for req in set(self._entries):
-            self.remove(req)
-        remove = self._temp_dir is not None
-        if remove:
-            self._temp_dir.cleanup()
-        logger.debug('%s build tracker %r',
-                     'Removed' if remove else 'Cleaned',
-                     self._root)
-
-    @contextlib.contextmanager
-    def track(self, req):
-        # type: (InstallRequirement) -> Iterator[None]
-        self.add(req)
-        yield
-        self.remove(req)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_uninstall.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_uninstall.py
deleted file mode 100644
index c80959e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/req/req_uninstall.py
+++ /dev/null
@@ -1,596 +0,0 @@
-from __future__ import absolute_import
-
-import csv
-import functools
-import logging
-import os
-import sys
-import sysconfig
-
-from pip._vendor import pkg_resources
-
-from pip._internal.exceptions import UninstallationError
-from pip._internal.locations import bin_py, bin_user
-from pip._internal.utils.compat import WINDOWS, cache_from_source, uses_pycache
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import (
-    FakeFile, ask, dist_in_usersite, dist_is_local, egg_link_path, is_local,
-    normalize_path, renames, rmtree,
-)
-from pip._internal.utils.temp_dir import AdjacentTempDirectory, TempDirectory
-
-logger = logging.getLogger(__name__)
-
-
-def _script_names(dist, script_name, is_gui):
-    """Create the fully qualified name of the files created by
-    {console,gui}_scripts for the given ``dist``.
-    Returns the list of file names
-    """
-    if dist_in_usersite(dist):
-        bin_dir = bin_user
-    else:
-        bin_dir = bin_py
-    exe_name = os.path.join(bin_dir, script_name)
-    paths_to_remove = [exe_name]
-    if WINDOWS:
-        paths_to_remove.append(exe_name + '.exe')
-        paths_to_remove.append(exe_name + '.exe.manifest')
-        if is_gui:
-            paths_to_remove.append(exe_name + '-script.pyw')
-        else:
-            paths_to_remove.append(exe_name + '-script.py')
-    return paths_to_remove
-
-
-def _unique(fn):
-    @functools.wraps(fn)
-    def unique(*args, **kw):
-        seen = set()
-        for item in fn(*args, **kw):
-            if item not in seen:
-                seen.add(item)
-                yield item
-    return unique
-
-
-@_unique
-def uninstallation_paths(dist):
-    """
-    Yield all the uninstallation paths for dist based on RECORD-without-.py[co]
-
-    Yield paths to all the files in RECORD. For each .py file in RECORD, add
-    the .pyc and .pyo in the same directory.
-
-    UninstallPathSet.add() takes care of the __pycache__ .py[co].
-    """
-    r = csv.reader(FakeFile(dist.get_metadata_lines('RECORD')))
-    for row in r:
-        path = os.path.join(dist.location, row[0])
-        yield path
-        if path.endswith('.py'):
-            dn, fn = os.path.split(path)
-            base = fn[:-3]
-            path = os.path.join(dn, base + '.pyc')
-            yield path
-            path = os.path.join(dn, base + '.pyo')
-            yield path
-
-
-def compact(paths):
-    """Compact a path set to contain the minimal number of paths
-    necessary to contain all paths in the set. If /a/path/ and
-    /a/path/to/a/file.txt are both in the set, leave only the
-    shorter path."""
-
-    sep = os.path.sep
-    short_paths = set()
-    for path in sorted(paths, key=len):
-        should_skip = any(
-            path.startswith(shortpath.rstrip("*")) and
-            path[len(shortpath.rstrip("*").rstrip(sep))] == sep
-            for shortpath in short_paths
-        )
-        if not should_skip:
-            short_paths.add(path)
-    return short_paths
-
-
-def compress_for_rename(paths):
-    """Returns a set containing the paths that need to be renamed.
-
-    This set may include directories when the original sequence of paths
-    included every file on disk.
-    """
-    case_map = dict((os.path.normcase(p), p) for p in paths)
-    remaining = set(case_map)
-    unchecked = sorted(set(os.path.split(p)[0]
-                           for p in case_map.values()), key=len)
-    wildcards = set()
-
-    def norm_join(*a):
-        return os.path.normcase(os.path.join(*a))
-
-    for root in unchecked:
-        if any(os.path.normcase(root).startswith(w)
-               for w in wildcards):
-            # This directory has already been handled.
-            continue
-
-        all_files = set()
-        all_subdirs = set()
-        for dirname, subdirs, files in os.walk(root):
-            all_subdirs.update(norm_join(root, dirname, d)
-                               for d in subdirs)
-            all_files.update(norm_join(root, dirname, f)
-                             for f in files)
-        # If all the files we found are in our remaining set of files to
-        # remove, then remove them from the latter set and add a wildcard
-        # for the directory.
-        if not (all_files - remaining):
-            remaining.difference_update(all_files)
-            wildcards.add(root + os.sep)
-
-    return set(map(case_map.__getitem__, remaining)) | wildcards
-
-
-def compress_for_output_listing(paths):
-    """Returns a tuple of 2 sets of which paths to display to user
-
-    The first set contains paths that would be deleted. Files of a package
-    are not added and the top-level directory of the package has a '*' added
-    at the end - to signify that all it's contents are removed.
-
-    The second set contains files that would have been skipped in the above
-    folders.
-    """
-
-    will_remove = list(paths)
-    will_skip = set()
-
-    # Determine folders and files
-    folders = set()
-    files = set()
-    for path in will_remove:
-        if path.endswith(".pyc"):
-            continue
-        if path.endswith("__init__.py") or ".dist-info" in path:
-            folders.add(os.path.dirname(path))
-        files.add(path)
-
-    _normcased_files = set(map(os.path.normcase, files))
-
-    folders = compact(folders)
-
-    # This walks the tree using os.walk to not miss extra folders
-    # that might get added.
-    for folder in folders:
-        for dirpath, _, dirfiles in os.walk(folder):
-            for fname in dirfiles:
-                if fname.endswith(".pyc"):
-                    continue
-
-                file_ = os.path.join(dirpath, fname)
-                if (os.path.isfile(file_) and
-                        os.path.normcase(file_) not in _normcased_files):
-                    # We are skipping this file. Add it to the set.
-                    will_skip.add(file_)
-
-    will_remove = files | {
-        os.path.join(folder, "*") for folder in folders
-    }
-
-    return will_remove, will_skip
-
-
-class StashedUninstallPathSet(object):
-    """A set of file rename operations to stash files while
-    tentatively uninstalling them."""
-    def __init__(self):
-        # Mapping from source file root to [Adjacent]TempDirectory
-        # for files under that directory.
-        self._save_dirs = {}
-        # (old path, new path) tuples for each move that may need
-        # to be undone.
-        self._moves = []
-
-    def _get_directory_stash(self, path):
-        """Stashes a directory.
-
-        Directories are stashed adjacent to their original location if
-        possible, or else moved/copied into the user's temp dir."""
-
-        try:
-            save_dir = AdjacentTempDirectory(path)
-            save_dir.create()
-        except OSError:
-            save_dir = TempDirectory(kind="uninstall")
-            save_dir.create()
-        self._save_dirs[os.path.normcase(path)] = save_dir
-
-        return save_dir.path
-
-    def _get_file_stash(self, path):
-        """Stashes a file.
-
-        If no root has been provided, one will be created for the directory
-        in the user's temp directory."""
-        path = os.path.normcase(path)
-        head, old_head = os.path.dirname(path), None
-        save_dir = None
-
-        while head != old_head:
-            try:
-                save_dir = self._save_dirs[head]
-                break
-            except KeyError:
-                pass
-            head, old_head = os.path.dirname(head), head
-        else:
-            # Did not find any suitable root
-            head = os.path.dirname(path)
-            save_dir = TempDirectory(kind='uninstall')
-            save_dir.create()
-            self._save_dirs[head] = save_dir
-
-        relpath = os.path.relpath(path, head)
-        if relpath and relpath != os.path.curdir:
-            return os.path.join(save_dir.path, relpath)
-        return save_dir.path
-
-    def stash(self, path):
-        """Stashes the directory or file and returns its new location.
-        """
-        if os.path.isdir(path):
-            new_path = self._get_directory_stash(path)
-        else:
-            new_path = self._get_file_stash(path)
-
-        self._moves.append((path, new_path))
-        if os.path.isdir(path) and os.path.isdir(new_path):
-            # If we're moving a directory, we need to
-            # remove the destination first or else it will be
-            # moved to inside the existing directory.
-            # We just created new_path ourselves, so it will
-            # be removable.
-            os.rmdir(new_path)
-        renames(path, new_path)
-        return new_path
-
-    def commit(self):
-        """Commits the uninstall by removing stashed files."""
-        for _, save_dir in self._save_dirs.items():
-            save_dir.cleanup()
-        self._moves = []
-        self._save_dirs = {}
-
-    def rollback(self):
-        """Undoes the uninstall by moving stashed files back."""
-        for p in self._moves:
-            logging.info("Moving to %s\n from %s", *p)
-
-        for new_path, path in self._moves:
-            try:
-                logger.debug('Replacing %s from %s', new_path, path)
-                if os.path.isfile(new_path):
-                    os.unlink(new_path)
-                elif os.path.isdir(new_path):
-                    rmtree(new_path)
-                renames(path, new_path)
-            except OSError as ex:
-                logger.error("Failed to restore %s", new_path)
-                logger.debug("Exception: %s", ex)
-
-        self.commit()
-
-    @property
-    def can_rollback(self):
-        return bool(self._moves)
-
-
-class UninstallPathSet(object):
-    """A set of file paths to be removed in the uninstallation of a
-    requirement."""
-    def __init__(self, dist):
-        self.paths = set()
-        self._refuse = set()
-        self.pth = {}
-        self.dist = dist
-        self._moved_paths = StashedUninstallPathSet()
-
-    def _permitted(self, path):
-        """
-        Return True if the given path is one we are permitted to
-        remove/modify, False otherwise.
-
-        """
-        return is_local(path)
-
-    def add(self, path):
-        head, tail = os.path.split(path)
-
-        # we normalize the head to resolve parent directory symlinks, but not
-        # the tail, since we only want to uninstall symlinks, not their targets
-        path = os.path.join(normalize_path(head), os.path.normcase(tail))
-
-        if not os.path.exists(path):
-            return
-        if self._permitted(path):
-            self.paths.add(path)
-        else:
-            self._refuse.add(path)
-
-        # __pycache__ files can show up after 'installed-files.txt' is created,
-        # due to imports
-        if os.path.splitext(path)[1] == '.py' and uses_pycache:
-            self.add(cache_from_source(path))
-
-    def add_pth(self, pth_file, entry):
-        pth_file = normalize_path(pth_file)
-        if self._permitted(pth_file):
-            if pth_file not in self.pth:
-                self.pth[pth_file] = UninstallPthEntries(pth_file)
-            self.pth[pth_file].add(entry)
-        else:
-            self._refuse.add(pth_file)
-
-    def remove(self, auto_confirm=False, verbose=False):
-        """Remove paths in ``self.paths`` with confirmation (unless
-        ``auto_confirm`` is True)."""
-
-        if not self.paths:
-            logger.info(
-                "Can't uninstall '%s'. No files were found to uninstall.",
-                self.dist.project_name,
-            )
-            return
-
-        dist_name_version = (
-            self.dist.project_name + "-" + self.dist.version
-        )
-        logger.info('Uninstalling %s:', dist_name_version)
-
-        with indent_log():
-            if auto_confirm or self._allowed_to_proceed(verbose):
-                moved = self._moved_paths
-
-                for_rename = compress_for_rename(self.paths)
-
-                for path in sorted(compact(for_rename)):
-                    moved.stash(path)
-                    logger.debug('Removing file or directory %s', path)
-
-                for pth in self.pth.values():
-                    pth.remove()
-
-                logger.info('Successfully uninstalled %s', dist_name_version)
-
-    def _allowed_to_proceed(self, verbose):
-        """Display which files would be deleted and prompt for confirmation
-        """
-
-        def _display(msg, paths):
-            if not paths:
-                return
-
-            logger.info(msg)
-            with indent_log():
-                for path in sorted(compact(paths)):
-                    logger.info(path)
-
-        if not verbose:
-            will_remove, will_skip = compress_for_output_listing(self.paths)
-        else:
-            # In verbose mode, display all the files that are going to be
-            # deleted.
-            will_remove = list(self.paths)
-            will_skip = set()
-
-        _display('Would remove:', will_remove)
-        _display('Would not remove (might be manually added):', will_skip)
-        _display('Would not remove (outside of prefix):', self._refuse)
-        if verbose:
-            _display('Will actually move:', compress_for_rename(self.paths))
-
-        return ask('Proceed (y/n)? ', ('y', 'n')) == 'y'
-
-    def rollback(self):
-        """Rollback the changes previously made by remove()."""
-        if not self._moved_paths.can_rollback:
-            logger.error(
-                "Can't roll back %s; was not uninstalled",
-                self.dist.project_name,
-            )
-            return False
-        logger.info('Rolling back uninstall of %s', self.dist.project_name)
-        self._moved_paths.rollback()
-        for pth in self.pth.values():
-            pth.rollback()
-
-    def commit(self):
-        """Remove temporary save dir: rollback will no longer be possible."""
-        self._moved_paths.commit()
-
-    @classmethod
-    def from_dist(cls, dist):
-        dist_path = normalize_path(dist.location)
-        if not dist_is_local(dist):
-            logger.info(
-                "Not uninstalling %s at %s, outside environment %s",
-                dist.key,
-                dist_path,
-                sys.prefix,
-            )
-            return cls(dist)
-
-        if dist_path in {p for p in {sysconfig.get_path("stdlib"),
-                                     sysconfig.get_path("platstdlib")}
-                         if p}:
-            logger.info(
-                "Not uninstalling %s at %s, as it is in the standard library.",
-                dist.key,
-                dist_path,
-            )
-            return cls(dist)
-
-        paths_to_remove = cls(dist)
-        develop_egg_link = egg_link_path(dist)
-        develop_egg_link_egg_info = '{}.egg-info'.format(
-            pkg_resources.to_filename(dist.project_name))
-        egg_info_exists = dist.egg_info and os.path.exists(dist.egg_info)
-        # Special case for distutils installed package
-        distutils_egg_info = getattr(dist._provider, 'path', None)
-
-        # Uninstall cases order do matter as in the case of 2 installs of the
-        # same package, pip needs to uninstall the currently detected version
-        if (egg_info_exists and dist.egg_info.endswith('.egg-info') and
-                not dist.egg_info.endswith(develop_egg_link_egg_info)):
-            # if dist.egg_info.endswith(develop_egg_link_egg_info), we
-            # are in fact in the develop_egg_link case
-            paths_to_remove.add(dist.egg_info)
-            if dist.has_metadata('installed-files.txt'):
-                for installed_file in dist.get_metadata(
-                        'installed-files.txt').splitlines():
-                    path = os.path.normpath(
-                        os.path.join(dist.egg_info, installed_file)
-                    )
-                    paths_to_remove.add(path)
-            # FIXME: need a test for this elif block
-            # occurs with --single-version-externally-managed/--record outside
-            # of pip
-            elif dist.has_metadata('top_level.txt'):
-                if dist.has_metadata('namespace_packages.txt'):
-                    namespaces = dist.get_metadata('namespace_packages.txt')
-                else:
-                    namespaces = []
-                for top_level_pkg in [
-                        p for p
-                        in dist.get_metadata('top_level.txt').splitlines()
-                        if p and p not in namespaces]:
-                    path = os.path.join(dist.location, top_level_pkg)
-                    paths_to_remove.add(path)
-                    paths_to_remove.add(path + '.py')
-                    paths_to_remove.add(path + '.pyc')
-                    paths_to_remove.add(path + '.pyo')
-
-        elif distutils_egg_info:
-            raise UninstallationError(
-                "Cannot uninstall {!r}. It is a distutils installed project "
-                "and thus we cannot accurately determine which files belong "
-                "to it which would lead to only a partial uninstall.".format(
-                    dist.project_name,
-                )
-            )
-
-        elif dist.location.endswith('.egg'):
-            # package installed by easy_install
-            # We cannot match on dist.egg_name because it can slightly vary
-            # i.e. setuptools-0.6c11-py2.6.egg vs setuptools-0.6rc11-py2.6.egg
-            paths_to_remove.add(dist.location)
-            easy_install_egg = os.path.split(dist.location)[1]
-            easy_install_pth = os.path.join(os.path.dirname(dist.location),
-                                            'easy-install.pth')
-            paths_to_remove.add_pth(easy_install_pth, './' + easy_install_egg)
-
-        elif egg_info_exists and dist.egg_info.endswith('.dist-info'):
-            for path in uninstallation_paths(dist):
-                paths_to_remove.add(path)
-
-        elif develop_egg_link:
-            # develop egg
-            with open(develop_egg_link, 'r') as fh:
-                link_pointer = os.path.normcase(fh.readline().strip())
-            assert (link_pointer == dist.location), (
-                'Egg-link %s does not match installed location of %s '
-                '(at %s)' % (link_pointer, dist.project_name, dist.location)
-            )
-            paths_to_remove.add(develop_egg_link)
-            easy_install_pth = os.path.join(os.path.dirname(develop_egg_link),
-                                            'easy-install.pth')
-            paths_to_remove.add_pth(easy_install_pth, dist.location)
-
-        else:
-            logger.debug(
-                'Not sure how to uninstall: %s - Check: %s',
-                dist, dist.location,
-            )
-
-        # find distutils scripts= scripts
-        if dist.has_metadata('scripts') and dist.metadata_isdir('scripts'):
-            for script in dist.metadata_listdir('scripts'):
-                if dist_in_usersite(dist):
-                    bin_dir = bin_user
-                else:
-                    bin_dir = bin_py
-                paths_to_remove.add(os.path.join(bin_dir, script))
-                if WINDOWS:
-                    paths_to_remove.add(os.path.join(bin_dir, script) + '.bat')
-
-        # find console_scripts
-        _scripts_to_remove = []
-        console_scripts = dist.get_entry_map(group='console_scripts')
-        for name in console_scripts.keys():
-            _scripts_to_remove.extend(_script_names(dist, name, False))
-        # find gui_scripts
-        gui_scripts = dist.get_entry_map(group='gui_scripts')
-        for name in gui_scripts.keys():
-            _scripts_to_remove.extend(_script_names(dist, name, True))
-
-        for s in _scripts_to_remove:
-            paths_to_remove.add(s)
-
-        return paths_to_remove
-
-
-class UninstallPthEntries(object):
-    def __init__(self, pth_file):
-        if not os.path.isfile(pth_file):
-            raise UninstallationError(
-                "Cannot remove entries from nonexistent file %s" % pth_file
-            )
-        self.file = pth_file
-        self.entries = set()
-        self._saved_lines = None
-
-    def add(self, entry):
-        entry = os.path.normcase(entry)
-        # On Windows, os.path.normcase converts the entry to use
-        # backslashes.  This is correct for entries that describe absolute
-        # paths outside of site-packages, but all the others use forward
-        # slashes.
-        if WINDOWS and not os.path.splitdrive(entry)[0]:
-            entry = entry.replace('\\', '/')
-        self.entries.add(entry)
-
-    def remove(self):
-        logger.debug('Removing pth entries from %s:', self.file)
-        with open(self.file, 'rb') as fh:
-            # windows uses '\r\n' with py3k, but uses '\n' with py2.x
-            lines = fh.readlines()
-            self._saved_lines = lines
-        if any(b'\r\n' in line for line in lines):
-            endline = '\r\n'
-        else:
-            endline = '\n'
-        # handle missing trailing newline
-        if lines and not lines[-1].endswith(endline.encode("utf-8")):
-            lines[-1] = lines[-1] + endline.encode("utf-8")
-        for entry in self.entries:
-            try:
-                logger.debug('Removing entry: %s', entry)
-                lines.remove((entry + endline).encode("utf-8"))
-            except ValueError:
-                pass
-        with open(self.file, 'wb') as fh:
-            fh.writelines(lines)
-
-    def rollback(self):
-        if self._saved_lines is None:
-            logger.error(
-                'Cannot roll back changes to %s, none were made', self.file
-            )
-            return False
-        logger.debug('Rolling %s back to previous state', self.file)
-        with open(self.file, 'wb') as fh:
-            fh.writelines(self._saved_lines)
-        return True
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/resolve.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/resolve.py
deleted file mode 100644
index 33f572f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/resolve.py
+++ /dev/null
@@ -1,393 +0,0 @@
-"""Dependency Resolution
-
-The dependency resolution in pip is performed as follows:
-
-for top-level requirements:
-    a. only one spec allowed per project, regardless of conflicts or not.
-       otherwise a "double requirement" exception is raised
-    b. they override sub-dependency requirements.
-for sub-dependencies
-    a. "first found, wins" (where the order is breadth first)
-"""
-
-import logging
-from collections import defaultdict
-from itertools import chain
-
-from pip._internal.exceptions import (
-    BestVersionAlreadyInstalled, DistributionNotFound, HashError, HashErrors,
-    UnsupportedPythonVersion,
-)
-from pip._internal.req.constructors import install_req_from_req_string
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import dist_in_usersite, ensure_dir
-from pip._internal.utils.packaging import check_dist_requires_python
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional, DefaultDict, List, Set  # noqa: F401
-    from pip._internal.download import PipSession  # noqa: F401
-    from pip._internal.req.req_install import InstallRequirement  # noqa: F401
-    from pip._internal.index import PackageFinder  # noqa: F401
-    from pip._internal.req.req_set import RequirementSet  # noqa: F401
-    from pip._internal.operations.prepare import (  # noqa: F401
-        DistAbstraction, RequirementPreparer
-    )
-    from pip._internal.cache import WheelCache  # noqa: F401
-
-logger = logging.getLogger(__name__)
-
-
-class Resolver(object):
-    """Resolves which packages need to be installed/uninstalled to perform \
-    the requested operation without breaking the requirements of any package.
-    """
-
-    _allowed_strategies = {"eager", "only-if-needed", "to-satisfy-only"}
-
-    def __init__(
-        self,
-        preparer,  # type: RequirementPreparer
-        session,  # type: PipSession
-        finder,  # type: PackageFinder
-        wheel_cache,  # type: Optional[WheelCache]
-        use_user_site,  # type: bool
-        ignore_dependencies,  # type: bool
-        ignore_installed,  # type: bool
-        ignore_requires_python,  # type: bool
-        force_reinstall,  # type: bool
-        isolated,  # type: bool
-        upgrade_strategy,  # type: str
-        use_pep517=None  # type: Optional[bool]
-    ):
-        # type: (...) -> None
-        super(Resolver, self).__init__()
-        assert upgrade_strategy in self._allowed_strategies
-
-        self.preparer = preparer
-        self.finder = finder
-        self.session = session
-
-        # NOTE: This would eventually be replaced with a cache that can give
-        #       information about both sdist and wheels transparently.
-        self.wheel_cache = wheel_cache
-
-        # This is set in resolve
-        self.require_hashes = None  # type: Optional[bool]
-
-        self.upgrade_strategy = upgrade_strategy
-        self.force_reinstall = force_reinstall
-        self.isolated = isolated
-        self.ignore_dependencies = ignore_dependencies
-        self.ignore_installed = ignore_installed
-        self.ignore_requires_python = ignore_requires_python
-        self.use_user_site = use_user_site
-        self.use_pep517 = use_pep517
-
-        self._discovered_dependencies = \
-            defaultdict(list)  # type: DefaultDict[str, List]
-
-    def resolve(self, requirement_set):
-        # type: (RequirementSet) -> None
-        """Resolve what operations need to be done
-
-        As a side-effect of this method, the packages (and their dependencies)
-        are downloaded, unpacked and prepared for installation. This
-        preparation is done by ``pip.operations.prepare``.
-
-        Once PyPI has static dependency metadata available, it would be
-        possible to move the preparation to become a step separated from
-        dependency resolution.
-        """
-        # make the wheelhouse
-        if self.preparer.wheel_download_dir:
-            ensure_dir(self.preparer.wheel_download_dir)
-
-        # If any top-level requirement has a hash specified, enter
-        # hash-checking mode, which requires hashes from all.
-        root_reqs = (
-            requirement_set.unnamed_requirements +
-            list(requirement_set.requirements.values())
-        )
-        self.require_hashes = (
-            requirement_set.require_hashes or
-            any(req.has_hash_options for req in root_reqs)
-        )
-
-        # Display where finder is looking for packages
-        locations = self.finder.get_formatted_locations()
-        if locations:
-            logger.info(locations)
-
-        # Actually prepare the files, and collect any exceptions. Most hash
-        # exceptions cannot be checked ahead of time, because
-        # req.populate_link() needs to be called before we can make decisions
-        # based on link type.
-        discovered_reqs = []  # type: List[InstallRequirement]
-        hash_errors = HashErrors()
-        for req in chain(root_reqs, discovered_reqs):
-            try:
-                discovered_reqs.extend(
-                    self._resolve_one(requirement_set, req)
-                )
-            except HashError as exc:
-                exc.req = req
-                hash_errors.append(exc)
-
-        if hash_errors:
-            raise hash_errors
-
-    def _is_upgrade_allowed(self, req):
-        # type: (InstallRequirement) -> bool
-        if self.upgrade_strategy == "to-satisfy-only":
-            return False
-        elif self.upgrade_strategy == "eager":
-            return True
-        else:
-            assert self.upgrade_strategy == "only-if-needed"
-            return req.is_direct
-
-    def _set_req_to_reinstall(self, req):
-        # type: (InstallRequirement) -> None
-        """
-        Set a requirement to be installed.
-        """
-        # Don't uninstall the conflict if doing a user install and the
-        # conflict is not a user install.
-        if not self.use_user_site or dist_in_usersite(req.satisfied_by):
-            req.conflicts_with = req.satisfied_by
-        req.satisfied_by = None
-
-    # XXX: Stop passing requirement_set for options
-    def _check_skip_installed(self, req_to_install):
-        # type: (InstallRequirement) -> Optional[str]
-        """Check if req_to_install should be skipped.
-
-        This will check if the req is installed, and whether we should upgrade
-        or reinstall it, taking into account all the relevant user options.
-
-        After calling this req_to_install will only have satisfied_by set to
-        None if the req_to_install is to be upgraded/reinstalled etc. Any
-        other value will be a dist recording the current thing installed that
-        satisfies the requirement.
-
-        Note that for vcs urls and the like we can't assess skipping in this
-        routine - we simply identify that we need to pull the thing down,
-        then later on it is pulled down and introspected to assess upgrade/
-        reinstalls etc.
-
-        :return: A text reason for why it was skipped, or None.
-        """
-        if self.ignore_installed:
-            return None
-
-        req_to_install.check_if_exists(self.use_user_site)
-        if not req_to_install.satisfied_by:
-            return None
-
-        if self.force_reinstall:
-            self._set_req_to_reinstall(req_to_install)
-            return None
-
-        if not self._is_upgrade_allowed(req_to_install):
-            if self.upgrade_strategy == "only-if-needed":
-                return 'already satisfied, skipping upgrade'
-            return 'already satisfied'
-
-        # Check for the possibility of an upgrade.  For link-based
-        # requirements we have to pull the tree down and inspect to assess
-        # the version #, so it's handled way down.
-        if not req_to_install.link:
-            try:
-                self.finder.find_requirement(req_to_install, upgrade=True)
-            except BestVersionAlreadyInstalled:
-                # Then the best version is installed.
-                return 'already up-to-date'
-            except DistributionNotFound:
-                # No distribution found, so we squash the error.  It will
-                # be raised later when we re-try later to do the install.
-                # Why don't we just raise here?
-                pass
-
-        self._set_req_to_reinstall(req_to_install)
-        return None
-
-    def _get_abstract_dist_for(self, req):
-        # type: (InstallRequirement) -> DistAbstraction
-        """Takes a InstallRequirement and returns a single AbstractDist \
-        representing a prepared variant of the same.
-        """
-        assert self.require_hashes is not None, (
-            "require_hashes should have been set in Resolver.resolve()"
-        )
-
-        if req.editable:
-            return self.preparer.prepare_editable_requirement(
-                req, self.require_hashes, self.use_user_site, self.finder,
-            )
-
-        # satisfied_by is only evaluated by calling _check_skip_installed,
-        # so it must be None here.
-        assert req.satisfied_by is None
-        skip_reason = self._check_skip_installed(req)
-
-        if req.satisfied_by:
-            return self.preparer.prepare_installed_requirement(
-                req, self.require_hashes, skip_reason
-            )
-
-        upgrade_allowed = self._is_upgrade_allowed(req)
-        abstract_dist = self.preparer.prepare_linked_requirement(
-            req, self.session, self.finder, upgrade_allowed,
-            self.require_hashes
-        )
-
-        # NOTE
-        # The following portion is for determining if a certain package is
-        # going to be re-installed/upgraded or not and reporting to the user.
-        # This should probably get cleaned up in a future refactor.
-
-        # req.req is only avail after unpack for URL
-        # pkgs repeat check_if_exists to uninstall-on-upgrade
-        # (#14)
-        if not self.ignore_installed:
-            req.check_if_exists(self.use_user_site)
-
-        if req.satisfied_by:
-            should_modify = (
-                self.upgrade_strategy != "to-satisfy-only" or
-                self.force_reinstall or
-                self.ignore_installed or
-                req.link.scheme == 'file'
-            )
-            if should_modify:
-                self._set_req_to_reinstall(req)
-            else:
-                logger.info(
-                    'Requirement already satisfied (use --upgrade to upgrade):'
-                    ' %s', req,
-                )
-
-        return abstract_dist
-
-    def _resolve_one(
-        self,
-        requirement_set,  # type: RequirementSet
-        req_to_install  # type: InstallRequirement
-    ):
-        # type: (...) -> List[InstallRequirement]
-        """Prepare a single requirements file.
-
-        :return: A list of additional InstallRequirements to also install.
-        """
-        # Tell user what we are doing for this requirement:
-        # obtain (editable), skipping, processing (local url), collecting
-        # (remote url or package name)
-        if req_to_install.constraint or req_to_install.prepared:
-            return []
-
-        req_to_install.prepared = True
-
-        # register tmp src for cleanup in case something goes wrong
-        requirement_set.reqs_to_cleanup.append(req_to_install)
-
-        abstract_dist = self._get_abstract_dist_for(req_to_install)
-
-        # Parse and return dependencies
-        dist = abstract_dist.dist()
-        try:
-            check_dist_requires_python(dist)
-        except UnsupportedPythonVersion as err:
-            if self.ignore_requires_python:
-                logger.warning(err.args[0])
-            else:
-                raise
-
-        more_reqs = []  # type: List[InstallRequirement]
-
-        def add_req(subreq, extras_requested):
-            sub_install_req = install_req_from_req_string(
-                str(subreq),
-                req_to_install,
-                isolated=self.isolated,
-                wheel_cache=self.wheel_cache,
-                use_pep517=self.use_pep517
-            )
-            parent_req_name = req_to_install.name
-            to_scan_again, add_to_parent = requirement_set.add_requirement(
-                sub_install_req,
-                parent_req_name=parent_req_name,
-                extras_requested=extras_requested,
-            )
-            if parent_req_name and add_to_parent:
-                self._discovered_dependencies[parent_req_name].append(
-                    add_to_parent
-                )
-            more_reqs.extend(to_scan_again)
-
-        with indent_log():
-            # We add req_to_install before its dependencies, so that we
-            # can refer to it when adding dependencies.
-            if not requirement_set.has_requirement(req_to_install.name):
-                # 'unnamed' requirements will get added here
-                req_to_install.is_direct = True
-                requirement_set.add_requirement(
-                    req_to_install, parent_req_name=None,
-                )
-
-            if not self.ignore_dependencies:
-                if req_to_install.extras:
-                    logger.debug(
-                        "Installing extra requirements: %r",
-                        ','.join(req_to_install.extras),
-                    )
-                missing_requested = sorted(
-                    set(req_to_install.extras) - set(dist.extras)
-                )
-                for missing in missing_requested:
-                    logger.warning(
-                        '%s does not provide the extra \'%s\'',
-                        dist, missing
-                    )
-
-                available_requested = sorted(
-                    set(dist.extras) & set(req_to_install.extras)
-                )
-                for subreq in dist.requires(available_requested):
-                    add_req(subreq, extras_requested=available_requested)
-
-            if not req_to_install.editable and not req_to_install.satisfied_by:
-                # XXX: --no-install leads this to report 'Successfully
-                # downloaded' for only non-editable reqs, even though we took
-                # action on them.
-                requirement_set.successfully_downloaded.append(req_to_install)
-
-        return more_reqs
-
-    def get_installation_order(self, req_set):
-        # type: (RequirementSet) -> List[InstallRequirement]
-        """Create the installation order.
-
-        The installation order is topological - requirements are installed
-        before the requiring thing. We break cycles at an arbitrary point,
-        and make no other guarantees.
-        """
-        # The current implementation, which we may change at any point
-        # installs the user specified things in the order given, except when
-        # dependencies must come earlier to achieve topological order.
-        order = []
-        ordered_reqs = set()  # type: Set[InstallRequirement]
-
-        def schedule(req):
-            if req.satisfied_by or req in ordered_reqs:
-                return
-            if req.constraint:
-                return
-            ordered_reqs.add(req)
-            for dep in self._discovered_dependencies[req.name]:
-                schedule(dep)
-            order.append(req)
-
-        for install_req in req_set.requirements.values():
-            schedule(install_req)
-        return order
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__init__.py
deleted file mode 100644
index e69de29..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__init__.py
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 964b1b1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/appdirs.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/appdirs.cpython-37.pyc
deleted file mode 100644
index 7357554..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/appdirs.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/compat.cpython-37.pyc
deleted file mode 100644
index 8b19861..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/compat.cpython-37.pyc
+++ /dev/null
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deleted file mode 100644
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/deprecation.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/encoding.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/encoding.cpython-37.pyc
deleted file mode 100644
index d09bef0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/encoding.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/filesystem.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/filesystem.cpython-37.pyc
deleted file mode 100644
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/filesystem.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/glibc.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/glibc.cpython-37.pyc
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/glibc.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/hashes.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/hashes.cpython-37.pyc
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/hashes.cpython-37.pyc
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/misc.cpython-37.pyc
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deleted file mode 100644
index af6c672..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/packaging.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/setuptools_build.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/setuptools_build.cpython-37.pyc
deleted file mode 100644
index 96efb71..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/setuptools_build.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/temp_dir.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/temp_dir.cpython-37.pyc
deleted file mode 100644
index f2795a2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/temp_dir.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/typing.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/typing.cpython-37.pyc
deleted file mode 100644
index c512b9f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/typing.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/ui.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/ui.cpython-37.pyc
deleted file mode 100644
index d31671f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/__pycache__/ui.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/appdirs.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/appdirs.py
deleted file mode 100644
index 9af9fa7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/appdirs.py
+++ /dev/null
@@ -1,270 +0,0 @@
-"""
-This code was taken from https://github.com/ActiveState/appdirs and modified
-to suit our purposes.
-"""
-from __future__ import absolute_import
-
-import os
-import sys
-
-from pip._vendor.six import PY2, text_type
-
-from pip._internal.utils.compat import WINDOWS, expanduser
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        List, Union
-    )
-
-
-def user_cache_dir(appname):
-    # type: (str) -> str
-    r"""
-    Return full path to the user-specific cache dir for this application.
-
-        "appname" is the name of application.
-
-    Typical user cache directories are:
-        macOS:      ~/Library/Caches/<AppName>
-        Unix:       ~/.cache/<AppName> (XDG default)
-        Windows:    C:\Users\<username>\AppData\Local\<AppName>\Cache
-
-    On Windows the only suggestion in the MSDN docs is that local settings go
-    in the `CSIDL_LOCAL_APPDATA` directory. This is identical to the
-    non-roaming app data dir (the default returned by `user_data_dir`). Apps
-    typically put cache data somewhere *under* the given dir here. Some
-    examples:
-        ...\Mozilla\Firefox\Profiles\<ProfileName>\Cache
-        ...\Acme\SuperApp\Cache\1.0
-
-    OPINION: This function appends "Cache" to the `CSIDL_LOCAL_APPDATA` value.
-    """
-    if WINDOWS:
-        # Get the base path
-        path = os.path.normpath(_get_win_folder("CSIDL_LOCAL_APPDATA"))
-
-        # When using Python 2, return paths as bytes on Windows like we do on
-        # other operating systems. See helper function docs for more details.
-        if PY2 and isinstance(path, text_type):
-            path = _win_path_to_bytes(path)
-
-        # Add our app name and Cache directory to it
-        path = os.path.join(path, appname, "Cache")
-    elif sys.platform == "darwin":
-        # Get the base path
-        path = expanduser("~/Library/Caches")
-
-        # Add our app name to it
-        path = os.path.join(path, appname)
-    else:
-        # Get the base path
-        path = os.getenv("XDG_CACHE_HOME", expanduser("~/.cache"))
-
-        # Add our app name to it
-        path = os.path.join(path, appname)
-
-    return path
-
-
-def user_data_dir(appname, roaming=False):
-    # type: (str, bool) -> str
-    r"""
-    Return full path to the user-specific data dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "roaming" (boolean, default False) can be set True to use the Windows
-            roaming appdata directory. That means that for users on a Windows
-            network setup for roaming profiles, this user data will be
-            sync'd on login. See
-            <http://technet.microsoft.com/en-us/library/cc766489(WS.10).aspx>
-            for a discussion of issues.
-
-    Typical user data directories are:
-        macOS:                  ~/Library/Application Support/<AppName>
-                                if it exists, else ~/.config/<AppName>
-        Unix:                   ~/.local/share/<AppName>    # or in
-                                $XDG_DATA_HOME, if defined
-        Win XP (not roaming):   C:\Documents and Settings\<username>\ ...
-                                ...Application Data\<AppName>
-        Win XP (roaming):       C:\Documents and Settings\<username>\Local ...
-                                ...Settings\Application Data\<AppName>
-        Win 7  (not roaming):   C:\\Users\<username>\AppData\Local\<AppName>
-        Win 7  (roaming):       C:\\Users\<username>\AppData\Roaming\<AppName>
-
-    For Unix, we follow the XDG spec and support $XDG_DATA_HOME.
-    That means, by default "~/.local/share/<AppName>".
-    """
-    if WINDOWS:
-        const = roaming and "CSIDL_APPDATA" or "CSIDL_LOCAL_APPDATA"
-        path = os.path.join(os.path.normpath(_get_win_folder(const)), appname)
-    elif sys.platform == "darwin":
-        path = os.path.join(
-            expanduser('~/Library/Application Support/'),
-            appname,
-        ) if os.path.isdir(os.path.join(
-            expanduser('~/Library/Application Support/'),
-            appname,
-        )
-        ) else os.path.join(
-            expanduser('~/.config/'),
-            appname,
-        )
-    else:
-        path = os.path.join(
-            os.getenv('XDG_DATA_HOME', expanduser("~/.local/share")),
-            appname,
-        )
-
-    return path
-
-
-def user_config_dir(appname, roaming=True):
-    # type: (str, bool) -> str
-    """Return full path to the user-specific config dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "roaming" (boolean, default True) can be set False to not use the
-            Windows roaming appdata directory. That means that for users on a
-            Windows network setup for roaming profiles, this user data will be
-            sync'd on login. See
-            <http://technet.microsoft.com/en-us/library/cc766489(WS.10).aspx>
-            for a discussion of issues.
-
-    Typical user data directories are:
-        macOS:                  same as user_data_dir
-        Unix:                   ~/.config/<AppName>
-        Win *:                  same as user_data_dir
-
-    For Unix, we follow the XDG spec and support $XDG_CONFIG_HOME.
-    That means, by default "~/.config/<AppName>".
-    """
-    if WINDOWS:
-        path = user_data_dir(appname, roaming=roaming)
-    elif sys.platform == "darwin":
-        path = user_data_dir(appname)
-    else:
-        path = os.getenv('XDG_CONFIG_HOME', expanduser("~/.config"))
-        path = os.path.join(path, appname)
-
-    return path
-
-
-# for the discussion regarding site_config_dirs locations
-# see <https://github.com/pypa/pip/issues/1733>
-def site_config_dirs(appname):
-    # type: (str) -> List[str]
-    r"""Return a list of potential user-shared config dirs for this application.
-
-        "appname" is the name of application.
-
-    Typical user config directories are:
-        macOS:      /Library/Application Support/<AppName>/
-        Unix:       /etc or $XDG_CONFIG_DIRS[i]/<AppName>/ for each value in
-                    $XDG_CONFIG_DIRS
-        Win XP:     C:\Documents and Settings\All Users\Application ...
-                    ...Data\<AppName>\
-        Vista:      (Fail! "C:\ProgramData" is a hidden *system* directory
-                    on Vista.)
-        Win 7:      Hidden, but writeable on Win 7:
-                    C:\ProgramData\<AppName>\
-    """
-    if WINDOWS:
-        path = os.path.normpath(_get_win_folder("CSIDL_COMMON_APPDATA"))
-        pathlist = [os.path.join(path, appname)]
-    elif sys.platform == 'darwin':
-        pathlist = [os.path.join('/Library/Application Support', appname)]
-    else:
-        # try looking in $XDG_CONFIG_DIRS
-        xdg_config_dirs = os.getenv('XDG_CONFIG_DIRS', '/etc/xdg')
-        if xdg_config_dirs:
-            pathlist = [
-                os.path.join(expanduser(x), appname)
-                for x in xdg_config_dirs.split(os.pathsep)
-            ]
-        else:
-            pathlist = []
-
-        # always look in /etc directly as well
-        pathlist.append('/etc')
-
-    return pathlist
-
-
-# -- Windows support functions --
-
-def _get_win_folder_from_registry(csidl_name):
-    # type: (str) -> str
-    """
-    This is a fallback technique at best. I'm not sure if using the
-    registry for this guarantees us the correct answer for all CSIDL_*
-    names.
-    """
-    import _winreg
-
-    shell_folder_name = {
-        "CSIDL_APPDATA": "AppData",
-        "CSIDL_COMMON_APPDATA": "Common AppData",
-        "CSIDL_LOCAL_APPDATA": "Local AppData",
-    }[csidl_name]
-
-    key = _winreg.OpenKey(
-        _winreg.HKEY_CURRENT_USER,
-        r"Software\Microsoft\Windows\CurrentVersion\Explorer\Shell Folders"
-    )
-    directory, _type = _winreg.QueryValueEx(key, shell_folder_name)
-    return directory
-
-
-def _get_win_folder_with_ctypes(csidl_name):
-    # type: (str) -> str
-    csidl_const = {
-        "CSIDL_APPDATA": 26,
-        "CSIDL_COMMON_APPDATA": 35,
-        "CSIDL_LOCAL_APPDATA": 28,
-    }[csidl_name]
-
-    buf = ctypes.create_unicode_buffer(1024)
-    ctypes.windll.shell32.SHGetFolderPathW(None, csidl_const, None, 0, buf)
-
-    # Downgrade to short path name if have highbit chars. See
-    # <http://bugs.activestate.com/show_bug.cgi?id=85099>.
-    has_high_char = False
-    for c in buf:
-        if ord(c) > 255:
-            has_high_char = True
-            break
-    if has_high_char:
-        buf2 = ctypes.create_unicode_buffer(1024)
-        if ctypes.windll.kernel32.GetShortPathNameW(buf.value, buf2, 1024):
-            buf = buf2
-
-    return buf.value
-
-
-if WINDOWS:
-    try:
-        import ctypes
-        _get_win_folder = _get_win_folder_with_ctypes
-    except ImportError:
-        _get_win_folder = _get_win_folder_from_registry
-
-
-def _win_path_to_bytes(path):
-    """Encode Windows paths to bytes. Only used on Python 2.
-
-    Motivation is to be consistent with other operating systems where paths
-    are also returned as bytes. This avoids problems mixing bytes and Unicode
-    elsewhere in the codebase. For more details and discussion see
-    <https://github.com/pypa/pip/issues/3463>.
-
-    If encoding using ASCII and MBCS fails, return the original Unicode path.
-    """
-    for encoding in ('ASCII', 'MBCS'):
-        try:
-            return path.encode(encoding)
-        except (UnicodeEncodeError, LookupError):
-            pass
-    return path
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/compat.py
deleted file mode 100644
index 2d8b3bf..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/compat.py
+++ /dev/null
@@ -1,264 +0,0 @@
-"""Stuff that differs in different Python versions and platform
-distributions."""
-from __future__ import absolute_import, division
-
-import codecs
-import locale
-import logging
-import os
-import shutil
-import sys
-
-from pip._vendor.six import text_type
-
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Tuple, Text  # noqa: F401
-
-try:
-    import ipaddress
-except ImportError:
-    try:
-        from pip._vendor import ipaddress  # type: ignore
-    except ImportError:
-        import ipaddr as ipaddress  # type: ignore
-        ipaddress.ip_address = ipaddress.IPAddress  # type: ignore
-        ipaddress.ip_network = ipaddress.IPNetwork  # type: ignore
-
-
-__all__ = [
-    "ipaddress", "uses_pycache", "console_to_str", "native_str",
-    "get_path_uid", "stdlib_pkgs", "WINDOWS", "samefile", "get_terminal_size",
-    "get_extension_suffixes",
-]
-
-
-logger = logging.getLogger(__name__)
-
-if sys.version_info >= (3, 4):
-    uses_pycache = True
-    from importlib.util import cache_from_source
-else:
-    import imp
-
-    try:
-        cache_from_source = imp.cache_from_source  # type: ignore
-    except AttributeError:
-        # does not use __pycache__
-        cache_from_source = None
-
-    uses_pycache = cache_from_source is not None
-
-
-if sys.version_info >= (3, 5):
-    backslashreplace_decode = "backslashreplace"
-else:
-    # In version 3.4 and older, backslashreplace exists
-    # but does not support use for decoding.
-    # We implement our own replace handler for this
-    # situation, so that we can consistently use
-    # backslash replacement for all versions.
-    def backslashreplace_decode_fn(err):
-        raw_bytes = (err.object[i] for i in range(err.start, err.end))
-        if sys.version_info[0] == 2:
-            # Python 2 gave us characters - convert to numeric bytes
-            raw_bytes = (ord(b) for b in raw_bytes)
-        return u"".join(u"\\x%x" % c for c in raw_bytes), err.end
-    codecs.register_error(
-        "backslashreplace_decode",
-        backslashreplace_decode_fn,
-    )
-    backslashreplace_decode = "backslashreplace_decode"
-
-
-def console_to_str(data):
-    # type: (bytes) -> Text
-    """Return a string, safe for output, of subprocess output.
-
-    We assume the data is in the locale preferred encoding.
-    If it won't decode properly, we warn the user but decode as
-    best we can.
-
-    We also ensure that the output can be safely written to
-    standard output without encoding errors.
-    """
-
-    # First, get the encoding we assume. This is the preferred
-    # encoding for the locale, unless that is not found, or
-    # it is ASCII, in which case assume UTF-8
-    encoding = locale.getpreferredencoding()
-    if (not encoding) or codecs.lookup(encoding).name == "ascii":
-        encoding = "utf-8"
-
-    # Now try to decode the data - if we fail, warn the user and
-    # decode with replacement.
-    try:
-        decoded_data = data.decode(encoding)
-    except UnicodeDecodeError:
-        logger.warning(
-            "Subprocess output does not appear to be encoded as %s",
-            encoding,
-        )
-        decoded_data = data.decode(encoding, errors=backslashreplace_decode)
-
-    # Make sure we can print the output, by encoding it to the output
-    # encoding with replacement of unencodable characters, and then
-    # decoding again.
-    # We use stderr's encoding because it's less likely to be
-    # redirected and if we don't find an encoding we skip this
-    # step (on the assumption that output is wrapped by something
-    # that won't fail).
-    # The double getattr is to deal with the possibility that we're
-    # being called in a situation where sys.__stderr__ doesn't exist,
-    # or doesn't have an encoding attribute. Neither of these cases
-    # should occur in normal pip use, but there's no harm in checking
-    # in case people use pip in (unsupported) unusual situations.
-    output_encoding = getattr(getattr(sys, "__stderr__", None),
-                              "encoding", None)
-
-    if output_encoding:
-        output_encoded = decoded_data.encode(
-            output_encoding,
-            errors="backslashreplace"
-        )
-        decoded_data = output_encoded.decode(output_encoding)
-
-    return decoded_data
-
-
-if sys.version_info >= (3,):
-    def native_str(s, replace=False):
-        # type: (str, bool) -> str
-        if isinstance(s, bytes):
-            return s.decode('utf-8', 'replace' if replace else 'strict')
-        return s
-
-else:
-    def native_str(s, replace=False):
-        # type: (str, bool) -> str
-        # Replace is ignored -- unicode to UTF-8 can't fail
-        if isinstance(s, text_type):
-            return s.encode('utf-8')
-        return s
-
-
-def get_path_uid(path):
-    # type: (str) -> int
-    """
-    Return path's uid.
-
-    Does not follow symlinks:
-        https://github.com/pypa/pip/pull/935#discussion_r5307003
-
-    Placed this function in compat due to differences on AIX and
-    Jython, that should eventually go away.
-
-    :raises OSError: When path is a symlink or can't be read.
-    """
-    if hasattr(os, 'O_NOFOLLOW'):
-        fd = os.open(path, os.O_RDONLY | os.O_NOFOLLOW)
-        file_uid = os.fstat(fd).st_uid
-        os.close(fd)
-    else:  # AIX and Jython
-        # WARNING: time of check vulnerability, but best we can do w/o NOFOLLOW
-        if not os.path.islink(path):
-            # older versions of Jython don't have `os.fstat`
-            file_uid = os.stat(path).st_uid
-        else:
-            # raise OSError for parity with os.O_NOFOLLOW above
-            raise OSError(
-                "%s is a symlink; Will not return uid for symlinks" % path
-            )
-    return file_uid
-
-
-if sys.version_info >= (3, 4):
-    from importlib.machinery import EXTENSION_SUFFIXES
-
-    def get_extension_suffixes():
-        return EXTENSION_SUFFIXES
-else:
-    from imp import get_suffixes
-
-    def get_extension_suffixes():
-        return [suffix[0] for suffix in get_suffixes()]
-
-
-def expanduser(path):
-    # type: (str) -> str
-    """
-    Expand ~ and ~user constructions.
-
-    Includes a workaround for https://bugs.python.org/issue14768
-    """
-    expanded = os.path.expanduser(path)
-    if path.startswith('~/') and expanded.startswith('//'):
-        expanded = expanded[1:]
-    return expanded
-
-
-# packages in the stdlib that may have installation metadata, but should not be
-# considered 'installed'.  this theoretically could be determined based on
-# dist.location (py27:`sysconfig.get_paths()['stdlib']`,
-# py26:sysconfig.get_config_vars('LIBDEST')), but fear platform variation may
-# make this ineffective, so hard-coding
-stdlib_pkgs = {"python", "wsgiref", "argparse"}
-
-
-# windows detection, covers cpython and ironpython
-WINDOWS = (sys.platform.startswith("win") or
-           (sys.platform == 'cli' and os.name == 'nt'))
-
-
-def samefile(file1, file2):
-    # type: (str, str) -> bool
-    """Provide an alternative for os.path.samefile on Windows/Python2"""
-    if hasattr(os.path, 'samefile'):
-        return os.path.samefile(file1, file2)
-    else:
-        path1 = os.path.normcase(os.path.abspath(file1))
-        path2 = os.path.normcase(os.path.abspath(file2))
-        return path1 == path2
-
-
-if hasattr(shutil, 'get_terminal_size'):
-    def get_terminal_size():
-        # type: () -> Tuple[int, int]
-        """
-        Returns a tuple (x, y) representing the width(x) and the height(y)
-        in characters of the terminal window.
-        """
-        return tuple(shutil.get_terminal_size())  # type: ignore
-else:
-    def get_terminal_size():
-        # type: () -> Tuple[int, int]
-        """
-        Returns a tuple (x, y) representing the width(x) and the height(y)
-        in characters of the terminal window.
-        """
-        def ioctl_GWINSZ(fd):
-            try:
-                import fcntl
-                import termios
-                import struct
-                cr = struct.unpack_from(
-                    'hh',
-                    fcntl.ioctl(fd, termios.TIOCGWINSZ, '12345678')
-                )
-            except Exception:
-                return None
-            if cr == (0, 0):
-                return None
-            return cr
-        cr = ioctl_GWINSZ(0) or ioctl_GWINSZ(1) or ioctl_GWINSZ(2)
-        if not cr:
-            try:
-                fd = os.open(os.ctermid(), os.O_RDONLY)
-                cr = ioctl_GWINSZ(fd)
-                os.close(fd)
-            except Exception:
-                pass
-        if not cr:
-            cr = (os.environ.get('LINES', 25), os.environ.get('COLUMNS', 80))
-        return int(cr[1]), int(cr[0])
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/deprecation.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/deprecation.py
deleted file mode 100644
index 0beaf74..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/deprecation.py
+++ /dev/null
@@ -1,90 +0,0 @@
-"""
-A module that implements tooling to enable easy warnings about deprecations.
-"""
-from __future__ import absolute_import
-
-import logging
-import warnings
-
-from pip._vendor.packaging.version import parse
-
-from pip import __version__ as current_version
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Any, Optional  # noqa: F401
-
-
-class PipDeprecationWarning(Warning):
-    pass
-
-
-_original_showwarning = None  # type: Any
-
-
-# Warnings <-> Logging Integration
-def _showwarning(message, category, filename, lineno, file=None, line=None):
-    if file is not None:
-        if _original_showwarning is not None:
-            _original_showwarning(
-                message, category, filename, lineno, file, line,
-            )
-    elif issubclass(category, PipDeprecationWarning):
-        # We use a specially named logger which will handle all of the
-        # deprecation messages for pip.
-        logger = logging.getLogger("pip._internal.deprecations")
-        logger.warning(message)
-    else:
-        _original_showwarning(
-            message, category, filename, lineno, file, line,
-        )
-
-
-def install_warning_logger():
-    # type: () -> None
-    # Enable our Deprecation Warnings
-    warnings.simplefilter("default", PipDeprecationWarning, append=True)
-
-    global _original_showwarning
-
-    if _original_showwarning is None:
-        _original_showwarning = warnings.showwarning
-        warnings.showwarning = _showwarning
-
-
-def deprecated(reason, replacement, gone_in, issue=None):
-    # type: (str, Optional[str], Optional[str], Optional[int]) -> None
-    """Helper to deprecate existing functionality.
-
-    reason:
-        Textual reason shown to the user about why this functionality has
-        been deprecated.
-    replacement:
-        Textual suggestion shown to the user about what alternative
-        functionality they can use.
-    gone_in:
-        The version of pip does this functionality should get removed in.
-        Raises errors if pip's current version is greater than or equal to
-        this.
-    issue:
-        Issue number on the tracker that would serve as a useful place for
-        users to find related discussion and provide feedback.
-
-    Always pass replacement, gone_in and issue as keyword arguments for clarity
-    at the call site.
-    """
-
-    # Construct a nice message.
-    # This is purposely eagerly formatted as we want it to appear as if someone
-    # typed this entire message out.
-    message = "DEPRECATION: " + reason
-    if replacement is not None:
-        message += " A possible replacement is {}.".format(replacement)
-    if issue is not None:
-        url = "https://github.com/pypa/pip/issues/" + str(issue)
-        message += " You can find discussion regarding this at {}.".format(url)
-
-    # Raise as an error if it has to be removed.
-    if gone_in is not None and parse(current_version) >= parse(gone_in):
-        raise PipDeprecationWarning(message)
-    warnings.warn(message, category=PipDeprecationWarning, stacklevel=2)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/encoding.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/encoding.py
deleted file mode 100644
index d36defa..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/encoding.py
+++ /dev/null
@@ -1,39 +0,0 @@
-import codecs
-import locale
-import re
-import sys
-
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import List, Tuple, Text  # noqa: F401
-
-BOMS = [
-    (codecs.BOM_UTF8, 'utf8'),
-    (codecs.BOM_UTF16, 'utf16'),
-    (codecs.BOM_UTF16_BE, 'utf16-be'),
-    (codecs.BOM_UTF16_LE, 'utf16-le'),
-    (codecs.BOM_UTF32, 'utf32'),
-    (codecs.BOM_UTF32_BE, 'utf32-be'),
-    (codecs.BOM_UTF32_LE, 'utf32-le'),
-]  # type: List[Tuple[bytes, Text]]
-
-ENCODING_RE = re.compile(br'coding[:=]\s*([-\w.]+)')
-
-
-def auto_decode(data):
-    # type: (bytes) -> Text
-    """Check a bytes string for a BOM to correctly detect the encoding
-
-    Fallback to locale.getpreferredencoding(False) like open() on Python3"""
-    for bom, encoding in BOMS:
-        if data.startswith(bom):
-            return data[len(bom):].decode(encoding)
-    # Lets check the first two lines as in PEP263
-    for line in data.split(b'\n')[:2]:
-        if line[0:1] == b'#' and ENCODING_RE.search(line):
-            encoding = ENCODING_RE.search(line).groups()[0].decode('ascii')
-            return data.decode(encoding)
-    return data.decode(
-        locale.getpreferredencoding(False) or sys.getdefaultencoding(),
-    )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/filesystem.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/filesystem.py
deleted file mode 100644
index 1e6b033..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/filesystem.py
+++ /dev/null
@@ -1,30 +0,0 @@
-import os
-import os.path
-
-from pip._internal.utils.compat import get_path_uid
-
-
-def check_path_owner(path):
-    # type: (str) -> bool
-    # If we don't have a way to check the effective uid of this process, then
-    # we'll just assume that we own the directory.
-    if not hasattr(os, "geteuid"):
-        return True
-
-    previous = None
-    while path != previous:
-        if os.path.lexists(path):
-            # Check if path is writable by current user.
-            if os.geteuid() == 0:
-                # Special handling for root user in order to handle properly
-                # cases where users use sudo without -H flag.
-                try:
-                    path_uid = get_path_uid(path)
-                except OSError:
-                    return False
-                return path_uid == 0
-            else:
-                return os.access(path, os.W_OK)
-        else:
-            previous, path = path, os.path.dirname(path)
-    return False  # assume we don't own the path
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/glibc.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/glibc.py
deleted file mode 100644
index 8a51f69..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/glibc.py
+++ /dev/null
@@ -1,93 +0,0 @@
-from __future__ import absolute_import
-
-import ctypes
-import re
-import warnings
-
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional, Tuple  # noqa: F401
-
-
-def glibc_version_string():
-    # type: () -> Optional[str]
-    "Returns glibc version string, or None if not using glibc."
-
-    # ctypes.CDLL(None) internally calls dlopen(NULL), and as the dlopen
-    # manpage says, "If filename is NULL, then the returned handle is for the
-    # main program". This way we can let the linker do the work to figure out
-    # which libc our process is actually using.
-    process_namespace = ctypes.CDLL(None)
-    try:
-        gnu_get_libc_version = process_namespace.gnu_get_libc_version
-    except AttributeError:
-        # Symbol doesn't exist -> therefore, we are not linked to
-        # glibc.
-        return None
-
-    # Call gnu_get_libc_version, which returns a string like "2.5"
-    gnu_get_libc_version.restype = ctypes.c_char_p
-    version_str = gnu_get_libc_version()
-    # py2 / py3 compatibility:
-    if not isinstance(version_str, str):
-        version_str = version_str.decode("ascii")
-
-    return version_str
-
-
-# Separated out from have_compatible_glibc for easier unit testing
-def check_glibc_version(version_str, required_major, minimum_minor):
-    # type: (str, int, int) -> bool
-    # Parse string and check against requested version.
-    #
-    # We use a regexp instead of str.split because we want to discard any
-    # random junk that might come after the minor version -- this might happen
-    # in patched/forked versions of glibc (e.g. Linaro's version of glibc
-    # uses version strings like "2.20-2014.11"). See gh-3588.
-    m = re.match(r"(?P<major>[0-9]+)\.(?P<minor>[0-9]+)", version_str)
-    if not m:
-        warnings.warn("Expected glibc version with 2 components major.minor,"
-                      " got: %s" % version_str, RuntimeWarning)
-        return False
-    return (int(m.group("major")) == required_major and
-            int(m.group("minor")) >= minimum_minor)
-
-
-def have_compatible_glibc(required_major, minimum_minor):
-    # type: (int, int) -> bool
-    version_str = glibc_version_string()  # type: Optional[str]
-    if version_str is None:
-        return False
-    return check_glibc_version(version_str, required_major, minimum_minor)
-
-
-# platform.libc_ver regularly returns completely nonsensical glibc
-# versions. E.g. on my computer, platform says:
-#
-#   ~$ python2.7 -c 'import platform; print(platform.libc_ver())'
-#   ('glibc', '2.7')
-#   ~$ python3.5 -c 'import platform; print(platform.libc_ver())'
-#   ('glibc', '2.9')
-#
-# But the truth is:
-#
-#   ~$ ldd --version
-#   ldd (Debian GLIBC 2.22-11) 2.22
-#
-# This is unfortunate, because it means that the linehaul data on libc
-# versions that was generated by pip 8.1.2 and earlier is useless and
-# misleading. Solution: instead of using platform, use our code that actually
-# works.
-def libc_ver():
-    # type: () -> Tuple[str, str]
-    """Try to determine the glibc version
-
-    Returns a tuple of strings (lib, version) which default to empty strings
-    in case the lookup fails.
-    """
-    glibc_version = glibc_version_string()
-    if glibc_version is None:
-        return ("", "")
-    else:
-        return ("glibc", glibc_version)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/hashes.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/hashes.py
deleted file mode 100644
index c6df7a1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/hashes.py
+++ /dev/null
@@ -1,115 +0,0 @@
-from __future__ import absolute_import
-
-import hashlib
-
-from pip._vendor.six import iteritems, iterkeys, itervalues
-
-from pip._internal.exceptions import (
-    HashMismatch, HashMissing, InstallationError,
-)
-from pip._internal.utils.misc import read_chunks
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Dict, List, BinaryIO, NoReturn, Iterator
-    )
-    from pip._vendor.six import PY3
-    if PY3:
-        from hashlib import _Hash  # noqa: F401
-    else:
-        from hashlib import _hash as _Hash  # noqa: F401
-
-
-# The recommended hash algo of the moment. Change this whenever the state of
-# the art changes; it won't hurt backward compatibility.
-FAVORITE_HASH = 'sha256'
-
-
-# Names of hashlib algorithms allowed by the --hash option and ``pip hash``
-# Currently, those are the ones at least as collision-resistant as sha256.
-STRONG_HASHES = ['sha256', 'sha384', 'sha512']
-
-
-class Hashes(object):
-    """A wrapper that builds multiple hashes at once and checks them against
-    known-good values
-
-    """
-    def __init__(self, hashes=None):
-        # type: (Dict[str, List[str]]) -> None
-        """
-        :param hashes: A dict of algorithm names pointing to lists of allowed
-            hex digests
-        """
-        self._allowed = {} if hashes is None else hashes
-
-    def check_against_chunks(self, chunks):
-        # type: (Iterator[bytes]) -> None
-        """Check good hashes against ones built from iterable of chunks of
-        data.
-
-        Raise HashMismatch if none match.
-
-        """
-        gots = {}
-        for hash_name in iterkeys(self._allowed):
-            try:
-                gots[hash_name] = hashlib.new(hash_name)
-            except (ValueError, TypeError):
-                raise InstallationError('Unknown hash name: %s' % hash_name)
-
-        for chunk in chunks:
-            for hash in itervalues(gots):
-                hash.update(chunk)
-
-        for hash_name, got in iteritems(gots):
-            if got.hexdigest() in self._allowed[hash_name]:
-                return
-        self._raise(gots)
-
-    def _raise(self, gots):
-        # type: (Dict[str, _Hash]) -> NoReturn
-        raise HashMismatch(self._allowed, gots)
-
-    def check_against_file(self, file):
-        # type: (BinaryIO) -> None
-        """Check good hashes against a file-like object
-
-        Raise HashMismatch if none match.
-
-        """
-        return self.check_against_chunks(read_chunks(file))
-
-    def check_against_path(self, path):
-        # type: (str) -> None
-        with open(path, 'rb') as file:
-            return self.check_against_file(file)
-
-    def __nonzero__(self):
-        # type: () -> bool
-        """Return whether I know any known-good hashes."""
-        return bool(self._allowed)
-
-    def __bool__(self):
-        # type: () -> bool
-        return self.__nonzero__()
-
-
-class MissingHashes(Hashes):
-    """A workalike for Hashes used when we're missing a hash for a requirement
-
-    It computes the actual hash of the requirement and raises a HashMissing
-    exception showing it to the user.
-
-    """
-    def __init__(self):
-        # type: () -> None
-        """Don't offer the ``hashes`` kwarg."""
-        # Pass our favorite hash in to generate a "gotten hash". With the
-        # empty list, it will never match, so an error will always raise.
-        super(MissingHashes, self).__init__(hashes={FAVORITE_HASH: []})
-
-    def _raise(self, gots):
-        # type: (Dict[str, _Hash]) -> NoReturn
-        raise HashMissing(gots[FAVORITE_HASH].hexdigest())
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/logging.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/logging.py
deleted file mode 100644
index 579d696..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/logging.py
+++ /dev/null
@@ -1,318 +0,0 @@
-from __future__ import absolute_import
-
-import contextlib
-import errno
-import logging
-import logging.handlers
-import os
-import sys
-
-from pip._vendor.six import PY2
-
-from pip._internal.utils.compat import WINDOWS
-from pip._internal.utils.misc import ensure_dir
-
-try:
-    import threading
-except ImportError:
-    import dummy_threading as threading  # type: ignore
-
-
-try:
-    from pip._vendor import colorama
-# Lots of different errors can come from this, including SystemError and
-# ImportError.
-except Exception:
-    colorama = None
-
-
-_log_state = threading.local()
-_log_state.indentation = 0
-
-
-class BrokenStdoutLoggingError(Exception):
-    """
-    Raised if BrokenPipeError occurs for the stdout stream while logging.
-    """
-    pass
-
-
-# BrokenPipeError does not exist in Python 2 and, in addition, manifests
-# differently in Windows and non-Windows.
-if WINDOWS:
-    # In Windows, a broken pipe can show up as EINVAL rather than EPIPE:
-    # https://bugs.python.org/issue19612
-    # https://bugs.python.org/issue30418
-    if PY2:
-        def _is_broken_pipe_error(exc_class, exc):
-            """See the docstring for non-Windows Python 3 below."""
-            return (exc_class is IOError and
-                    exc.errno in (errno.EINVAL, errno.EPIPE))
-    else:
-        # In Windows, a broken pipe IOError became OSError in Python 3.
-        def _is_broken_pipe_error(exc_class, exc):
-            """See the docstring for non-Windows Python 3 below."""
-            return ((exc_class is BrokenPipeError) or  # noqa: F821
-                    (exc_class is OSError and
-                     exc.errno in (errno.EINVAL, errno.EPIPE)))
-elif PY2:
-    def _is_broken_pipe_error(exc_class, exc):
-        """See the docstring for non-Windows Python 3 below."""
-        return (exc_class is IOError and exc.errno == errno.EPIPE)
-else:
-    # Then we are in the non-Windows Python 3 case.
-    def _is_broken_pipe_error(exc_class, exc):
-        """
-        Return whether an exception is a broken pipe error.
-
-        Args:
-          exc_class: an exception class.
-          exc: an exception instance.
-        """
-        return (exc_class is BrokenPipeError)  # noqa: F821
-
-
-@contextlib.contextmanager
-def indent_log(num=2):
-    """
-    A context manager which will cause the log output to be indented for any
-    log messages emitted inside it.
-    """
-    _log_state.indentation += num
-    try:
-        yield
-    finally:
-        _log_state.indentation -= num
-
-
-def get_indentation():
-    return getattr(_log_state, 'indentation', 0)
-
-
-class IndentingFormatter(logging.Formatter):
-    def __init__(self, *args, **kwargs):
-        """
-        A logging.Formatter obeying containing indent_log contexts.
-
-        :param add_timestamp: A bool indicating output lines should be prefixed
-            with their record's timestamp.
-        """
-        self.add_timestamp = kwargs.pop("add_timestamp", False)
-        super(IndentingFormatter, self).__init__(*args, **kwargs)
-
-    def format(self, record):
-        """
-        Calls the standard formatter, but will indent all of the log messages
-        by our current indentation level.
-        """
-        formatted = super(IndentingFormatter, self).format(record)
-        prefix = ''
-        if self.add_timestamp:
-            prefix = self.formatTime(record, "%Y-%m-%dT%H:%M:%S ")
-        prefix += " " * get_indentation()
-        formatted = "".join([
-            prefix + line
-            for line in formatted.splitlines(True)
-        ])
-        return formatted
-
-
-def _color_wrap(*colors):
-    def wrapped(inp):
-        return "".join(list(colors) + [inp, colorama.Style.RESET_ALL])
-    return wrapped
-
-
-class ColorizedStreamHandler(logging.StreamHandler):
-
-    # Don't build up a list of colors if we don't have colorama
-    if colorama:
-        COLORS = [
-            # This needs to be in order from highest logging level to lowest.
-            (logging.ERROR, _color_wrap(colorama.Fore.RED)),
-            (logging.WARNING, _color_wrap(colorama.Fore.YELLOW)),
-        ]
-    else:
-        COLORS = []
-
-    def __init__(self, stream=None, no_color=None):
-        logging.StreamHandler.__init__(self, stream)
-        self._no_color = no_color
-
-        if WINDOWS and colorama:
-            self.stream = colorama.AnsiToWin32(self.stream)
-
-    def _using_stdout(self):
-        """
-        Return whether the handler is using sys.stdout.
-        """
-        if WINDOWS and colorama:
-            # Then self.stream is an AnsiToWin32 object.
-            return self.stream.wrapped is sys.stdout
-
-        return self.stream is sys.stdout
-
-    def should_color(self):
-        # Don't colorize things if we do not have colorama or if told not to
-        if not colorama or self._no_color:
-            return False
-
-        real_stream = (
-            self.stream if not isinstance(self.stream, colorama.AnsiToWin32)
-            else self.stream.wrapped
-        )
-
-        # If the stream is a tty we should color it
-        if hasattr(real_stream, "isatty") and real_stream.isatty():
-            return True
-
-        # If we have an ANSI term we should color it
-        if os.environ.get("TERM") == "ANSI":
-            return True
-
-        # If anything else we should not color it
-        return False
-
-    def format(self, record):
-        msg = logging.StreamHandler.format(self, record)
-
-        if self.should_color():
-            for level, color in self.COLORS:
-                if record.levelno >= level:
-                    msg = color(msg)
-                    break
-
-        return msg
-
-    # The logging module says handleError() can be customized.
-    def handleError(self, record):
-        exc_class, exc = sys.exc_info()[:2]
-        # If a broken pipe occurred while calling write() or flush() on the
-        # stdout stream in logging's Handler.emit(), then raise our special
-        # exception so we can handle it in main() instead of logging the
-        # broken pipe error and continuing.
-        if (exc_class and self._using_stdout() and
-                _is_broken_pipe_error(exc_class, exc)):
-            raise BrokenStdoutLoggingError()
-
-        return super(ColorizedStreamHandler, self).handleError(record)
-
-
-class BetterRotatingFileHandler(logging.handlers.RotatingFileHandler):
-
-    def _open(self):
-        ensure_dir(os.path.dirname(self.baseFilename))
-        return logging.handlers.RotatingFileHandler._open(self)
-
-
-class MaxLevelFilter(logging.Filter):
-
-    def __init__(self, level):
-        self.level = level
-
-    def filter(self, record):
-        return record.levelno < self.level
-
-
-def setup_logging(verbosity, no_color, user_log_file):
-    """Configures and sets up all of the logging
-
-    Returns the requested logging level, as its integer value.
-    """
-
-    # Determine the level to be logging at.
-    if verbosity >= 1:
-        level = "DEBUG"
-    elif verbosity == -1:
-        level = "WARNING"
-    elif verbosity == -2:
-        level = "ERROR"
-    elif verbosity <= -3:
-        level = "CRITICAL"
-    else:
-        level = "INFO"
-
-    level_number = getattr(logging, level)
-
-    # The "root" logger should match the "console" level *unless* we also need
-    # to log to a user log file.
-    include_user_log = user_log_file is not None
-    if include_user_log:
-        additional_log_file = user_log_file
-        root_level = "DEBUG"
-    else:
-        additional_log_file = "/dev/null"
-        root_level = level
-
-    # Disable any logging besides WARNING unless we have DEBUG level logging
-    # enabled for vendored libraries.
-    vendored_log_level = "WARNING" if level in ["INFO", "ERROR"] else "DEBUG"
-
-    # Shorthands for clarity
-    log_streams = {
-        "stdout": "ext://sys.stdout",
-        "stderr": "ext://sys.stderr",
-    }
-    handler_classes = {
-        "stream": "pip._internal.utils.logging.ColorizedStreamHandler",
-        "file": "pip._internal.utils.logging.BetterRotatingFileHandler",
-    }
-
-    logging.config.dictConfig({
-        "version": 1,
-        "disable_existing_loggers": False,
-        "filters": {
-            "exclude_warnings": {
-                "()": "pip._internal.utils.logging.MaxLevelFilter",
-                "level": logging.WARNING,
-            },
-        },
-        "formatters": {
-            "indent": {
-                "()": IndentingFormatter,
-                "format": "%(message)s",
-            },
-            "indent_with_timestamp": {
-                "()": IndentingFormatter,
-                "format": "%(message)s",
-                "add_timestamp": True,
-            },
-        },
-        "handlers": {
-            "console": {
-                "level": level,
-                "class": handler_classes["stream"],
-                "no_color": no_color,
-                "stream": log_streams["stdout"],
-                "filters": ["exclude_warnings"],
-                "formatter": "indent",
-            },
-            "console_errors": {
-                "level": "WARNING",
-                "class": handler_classes["stream"],
-                "no_color": no_color,
-                "stream": log_streams["stderr"],
-                "formatter": "indent",
-            },
-            "user_log": {
-                "level": "DEBUG",
-                "class": handler_classes["file"],
-                "filename": additional_log_file,
-                "delay": True,
-                "formatter": "indent_with_timestamp",
-            },
-        },
-        "root": {
-            "level": root_level,
-            "handlers": ["console", "console_errors"] + (
-                ["user_log"] if include_user_log else []
-            ),
-        },
-        "loggers": {
-            "pip._vendor": {
-                "level": vendored_log_level
-            }
-        },
-    })
-
-    return level_number
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/misc.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/misc.py
deleted file mode 100644
index 84605ee..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/misc.py
+++ /dev/null
@@ -1,1040 +0,0 @@
-from __future__ import absolute_import
-
-import contextlib
-import errno
-import io
-import locale
-# we have a submodule named 'logging' which would shadow this if we used the
-# regular name:
-import logging as std_logging
-import os
-import posixpath
-import re
-import shutil
-import stat
-import subprocess
-import sys
-import tarfile
-import zipfile
-from collections import deque
-
-from pip._vendor import pkg_resources
-# NOTE: retrying is not annotated in typeshed as on 2017-07-17, which is
-#       why we ignore the type on this import.
-from pip._vendor.retrying import retry  # type: ignore
-from pip._vendor.six import PY2
-from pip._vendor.six.moves import input
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-from pip._vendor.six.moves.urllib.parse import unquote as urllib_unquote
-
-from pip._internal.exceptions import CommandError, InstallationError
-from pip._internal.locations import (
-    running_under_virtualenv, site_packages, user_site, virtualenv_no_global,
-    write_delete_marker_file,
-)
-from pip._internal.utils.compat import (
-    WINDOWS, console_to_str, expanduser, stdlib_pkgs,
-)
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if PY2:
-    from io import BytesIO as StringIO
-else:
-    from io import StringIO
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Optional, Tuple, Iterable, List, Match, Union, Any, Mapping, Text,
-        AnyStr, Container
-    )
-    from pip._vendor.pkg_resources import Distribution  # noqa: F401
-    from pip._internal.models.link import Link  # noqa: F401
-    from pip._internal.utils.ui import SpinnerInterface  # noqa: F401
-
-
-__all__ = ['rmtree', 'display_path', 'backup_dir',
-           'ask', 'splitext',
-           'format_size', 'is_installable_dir',
-           'is_svn_page', 'file_contents',
-           'split_leading_dir', 'has_leading_dir',
-           'normalize_path',
-           'renames', 'get_prog',
-           'unzip_file', 'untar_file', 'unpack_file', 'call_subprocess',
-           'captured_stdout', 'ensure_dir',
-           'ARCHIVE_EXTENSIONS', 'SUPPORTED_EXTENSIONS', 'WHEEL_EXTENSION',
-           'get_installed_version', 'remove_auth_from_url']
-
-
-logger = std_logging.getLogger(__name__)
-
-WHEEL_EXTENSION = '.whl'
-BZ2_EXTENSIONS = ('.tar.bz2', '.tbz')
-XZ_EXTENSIONS = ('.tar.xz', '.txz', '.tlz', '.tar.lz', '.tar.lzma')
-ZIP_EXTENSIONS = ('.zip', WHEEL_EXTENSION)
-TAR_EXTENSIONS = ('.tar.gz', '.tgz', '.tar')
-ARCHIVE_EXTENSIONS = (
-    ZIP_EXTENSIONS + BZ2_EXTENSIONS + TAR_EXTENSIONS + XZ_EXTENSIONS)
-SUPPORTED_EXTENSIONS = ZIP_EXTENSIONS + TAR_EXTENSIONS
-
-try:
-    import bz2  # noqa
-    SUPPORTED_EXTENSIONS += BZ2_EXTENSIONS
-except ImportError:
-    logger.debug('bz2 module is not available')
-
-try:
-    # Only for Python 3.3+
-    import lzma  # noqa
-    SUPPORTED_EXTENSIONS += XZ_EXTENSIONS
-except ImportError:
-    logger.debug('lzma module is not available')
-
-
-def ensure_dir(path):
-    # type: (AnyStr) -> None
-    """os.path.makedirs without EEXIST."""
-    try:
-        os.makedirs(path)
-    except OSError as e:
-        if e.errno != errno.EEXIST:
-            raise
-
-
-def get_prog():
-    # type: () -> str
-    try:
-        prog = os.path.basename(sys.argv[0])
-        if prog in ('__main__.py', '-c'):
-            return "%s -m pip" % sys.executable
-        else:
-            return prog
-    except (AttributeError, TypeError, IndexError):
-        pass
-    return 'pip'
-
-
-# Retry every half second for up to 3 seconds
-@retry(stop_max_delay=3000, wait_fixed=500)
-def rmtree(dir, ignore_errors=False):
-    # type: (str, bool) -> None
-    shutil.rmtree(dir, ignore_errors=ignore_errors,
-                  onerror=rmtree_errorhandler)
-
-
-def rmtree_errorhandler(func, path, exc_info):
-    """On Windows, the files in .svn are read-only, so when rmtree() tries to
-    remove them, an exception is thrown.  We catch that here, remove the
-    read-only attribute, and hopefully continue without problems."""
-    # if file type currently read only
-    if os.stat(path).st_mode & stat.S_IREAD:
-        # convert to read/write
-        os.chmod(path, stat.S_IWRITE)
-        # use the original function to repeat the operation
-        func(path)
-        return
-    else:
-        raise
-
-
-def display_path(path):
-    # type: (Union[str, Text]) -> str
-    """Gives the display value for a given path, making it relative to cwd
-    if possible."""
-    path = os.path.normcase(os.path.abspath(path))
-    if sys.version_info[0] == 2:
-        path = path.decode(sys.getfilesystemencoding(), 'replace')
-        path = path.encode(sys.getdefaultencoding(), 'replace')
-    if path.startswith(os.getcwd() + os.path.sep):
-        path = '.' + path[len(os.getcwd()):]
-    return path
-
-
-def backup_dir(dir, ext='.bak'):
-    # type: (str, str) -> str
-    """Figure out the name of a directory to back up the given dir to
-    (adding .bak, .bak2, etc)"""
-    n = 1
-    extension = ext
-    while os.path.exists(dir + extension):
-        n += 1
-        extension = ext + str(n)
-    return dir + extension
-
-
-def ask_path_exists(message, options):
-    # type: (str, Iterable[str]) -> str
-    for action in os.environ.get('PIP_EXISTS_ACTION', '').split():
-        if action in options:
-            return action
-    return ask(message, options)
-
-
-def ask(message, options):
-    # type: (str, Iterable[str]) -> str
-    """Ask the message interactively, with the given possible responses"""
-    while 1:
-        if os.environ.get('PIP_NO_INPUT'):
-            raise Exception(
-                'No input was expected ($PIP_NO_INPUT set); question: %s' %
-                message
-            )
-        response = input(message)
-        response = response.strip().lower()
-        if response not in options:
-            print(
-                'Your response (%r) was not one of the expected responses: '
-                '%s' % (response, ', '.join(options))
-            )
-        else:
-            return response
-
-
-def format_size(bytes):
-    # type: (float) -> str
-    if bytes > 1000 * 1000:
-        return '%.1fMB' % (bytes / 1000.0 / 1000)
-    elif bytes > 10 * 1000:
-        return '%ikB' % (bytes / 1000)
-    elif bytes > 1000:
-        return '%.1fkB' % (bytes / 1000.0)
-    else:
-        return '%ibytes' % bytes
-
-
-def is_installable_dir(path):
-    # type: (str) -> bool
-    """Is path is a directory containing setup.py or pyproject.toml?
-    """
-    if not os.path.isdir(path):
-        return False
-    setup_py = os.path.join(path, 'setup.py')
-    if os.path.isfile(setup_py):
-        return True
-    pyproject_toml = os.path.join(path, 'pyproject.toml')
-    if os.path.isfile(pyproject_toml):
-        return True
-    return False
-
-
-def is_svn_page(html):
-    # type: (Union[str, Text]) -> Optional[Match[Union[str, Text]]]
-    """
-    Returns true if the page appears to be the index page of an svn repository
-    """
-    return (re.search(r'<title>[^<]*Revision \d+:', html) and
-            re.search(r'Powered by (?:<a[^>]*?>)?Subversion', html, re.I))
-
-
-def file_contents(filename):
-    # type: (str) -> Text
-    with open(filename, 'rb') as fp:
-        return fp.read().decode('utf-8')
-
-
-def read_chunks(file, size=io.DEFAULT_BUFFER_SIZE):
-    """Yield pieces of data from a file-like object until EOF."""
-    while True:
-        chunk = file.read(size)
-        if not chunk:
-            break
-        yield chunk
-
-
-def split_leading_dir(path):
-    # type: (Union[str, Text]) -> List[Union[str, Text]]
-    path = path.lstrip('/').lstrip('\\')
-    if '/' in path and (('\\' in path and path.find('/') < path.find('\\')) or
-                        '\\' not in path):
-        return path.split('/', 1)
-    elif '\\' in path:
-        return path.split('\\', 1)
-    else:
-        return [path, '']
-
-
-def has_leading_dir(paths):
-    # type: (Iterable[Union[str, Text]]) -> bool
-    """Returns true if all the paths have the same leading path name
-    (i.e., everything is in one subdirectory in an archive)"""
-    common_prefix = None
-    for path in paths:
-        prefix, rest = split_leading_dir(path)
-        if not prefix:
-            return False
-        elif common_prefix is None:
-            common_prefix = prefix
-        elif prefix != common_prefix:
-            return False
-    return True
-
-
-def normalize_path(path, resolve_symlinks=True):
-    # type: (str, bool) -> str
-    """
-    Convert a path to its canonical, case-normalized, absolute version.
-
-    """
-    path = expanduser(path)
-    if resolve_symlinks:
-        path = os.path.realpath(path)
-    else:
-        path = os.path.abspath(path)
-    return os.path.normcase(path)
-
-
-def splitext(path):
-    # type: (str) -> Tuple[str, str]
-    """Like os.path.splitext, but take off .tar too"""
-    base, ext = posixpath.splitext(path)
-    if base.lower().endswith('.tar'):
-        ext = base[-4:] + ext
-        base = base[:-4]
-    return base, ext
-
-
-def renames(old, new):
-    # type: (str, str) -> None
-    """Like os.renames(), but handles renaming across devices."""
-    # Implementation borrowed from os.renames().
-    head, tail = os.path.split(new)
-    if head and tail and not os.path.exists(head):
-        os.makedirs(head)
-
-    shutil.move(old, new)
-
-    head, tail = os.path.split(old)
-    if head and tail:
-        try:
-            os.removedirs(head)
-        except OSError:
-            pass
-
-
-def is_local(path):
-    # type: (str) -> bool
-    """
-    Return True if path is within sys.prefix, if we're running in a virtualenv.
-
-    If we're not in a virtualenv, all paths are considered "local."
-
-    """
-    if not running_under_virtualenv():
-        return True
-    return normalize_path(path).startswith(normalize_path(sys.prefix))
-
-
-def dist_is_local(dist):
-    # type: (Distribution) -> bool
-    """
-    Return True if given Distribution object is installed locally
-    (i.e. within current virtualenv).
-
-    Always True if we're not in a virtualenv.
-
-    """
-    return is_local(dist_location(dist))
-
-
-def dist_in_usersite(dist):
-    # type: (Distribution) -> bool
-    """
-    Return True if given Distribution is installed in user site.
-    """
-    norm_path = normalize_path(dist_location(dist))
-    return norm_path.startswith(normalize_path(user_site))
-
-
-def dist_in_site_packages(dist):
-    # type: (Distribution) -> bool
-    """
-    Return True if given Distribution is installed in
-    sysconfig.get_python_lib().
-    """
-    return normalize_path(
-        dist_location(dist)
-    ).startswith(normalize_path(site_packages))
-
-
-def dist_is_editable(dist):
-    # type: (Distribution) -> bool
-    """
-    Return True if given Distribution is an editable install.
-    """
-    for path_item in sys.path:
-        egg_link = os.path.join(path_item, dist.project_name + '.egg-link')
-        if os.path.isfile(egg_link):
-            return True
-    return False
-
-
-def get_installed_distributions(local_only=True,
-                                skip=stdlib_pkgs,
-                                include_editables=True,
-                                editables_only=False,
-                                user_only=False):
-    # type: (bool, Container[str], bool, bool, bool) -> List[Distribution]
-    """
-    Return a list of installed Distribution objects.
-
-    If ``local_only`` is True (default), only return installations
-    local to the current virtualenv, if in a virtualenv.
-
-    ``skip`` argument is an iterable of lower-case project names to
-    ignore; defaults to stdlib_pkgs
-
-    If ``include_editables`` is False, don't report editables.
-
-    If ``editables_only`` is True , only report editables.
-
-    If ``user_only`` is True , only report installations in the user
-    site directory.
-
-    """
-    if local_only:
-        local_test = dist_is_local
-    else:
-        def local_test(d):
-            return True
-
-    if include_editables:
-        def editable_test(d):
-            return True
-    else:
-        def editable_test(d):
-            return not dist_is_editable(d)
-
-    if editables_only:
-        def editables_only_test(d):
-            return dist_is_editable(d)
-    else:
-        def editables_only_test(d):
-            return True
-
-    if user_only:
-        user_test = dist_in_usersite
-    else:
-        def user_test(d):
-            return True
-
-    # because of pkg_resources vendoring, mypy cannot find stub in typeshed
-    return [d for d in pkg_resources.working_set  # type: ignore
-            if local_test(d) and
-            d.key not in skip and
-            editable_test(d) and
-            editables_only_test(d) and
-            user_test(d)
-            ]
-
-
-def egg_link_path(dist):
-    # type: (Distribution) -> Optional[str]
-    """
-    Return the path for the .egg-link file if it exists, otherwise, None.
-
-    There's 3 scenarios:
-    1) not in a virtualenv
-       try to find in site.USER_SITE, then site_packages
-    2) in a no-global virtualenv
-       try to find in site_packages
-    3) in a yes-global virtualenv
-       try to find in site_packages, then site.USER_SITE
-       (don't look in global location)
-
-    For #1 and #3, there could be odd cases, where there's an egg-link in 2
-    locations.
-
-    This method will just return the first one found.
-    """
-    sites = []
-    if running_under_virtualenv():
-        if virtualenv_no_global():
-            sites.append(site_packages)
-        else:
-            sites.append(site_packages)
-            if user_site:
-                sites.append(user_site)
-    else:
-        if user_site:
-            sites.append(user_site)
-        sites.append(site_packages)
-
-    for site in sites:
-        egglink = os.path.join(site, dist.project_name) + '.egg-link'
-        if os.path.isfile(egglink):
-            return egglink
-    return None
-
-
-def dist_location(dist):
-    # type: (Distribution) -> str
-    """
-    Get the site-packages location of this distribution. Generally
-    this is dist.location, except in the case of develop-installed
-    packages, where dist.location is the source code location, and we
-    want to know where the egg-link file is.
-
-    """
-    egg_link = egg_link_path(dist)
-    if egg_link:
-        return egg_link
-    return dist.location
-
-
-def current_umask():
-    """Get the current umask which involves having to set it temporarily."""
-    mask = os.umask(0)
-    os.umask(mask)
-    return mask
-
-
-def unzip_file(filename, location, flatten=True):
-    # type: (str, str, bool) -> None
-    """
-    Unzip the file (with path `filename`) to the destination `location`.  All
-    files are written based on system defaults and umask (i.e. permissions are
-    not preserved), except that regular file members with any execute
-    permissions (user, group, or world) have "chmod +x" applied after being
-    written. Note that for windows, any execute changes using os.chmod are
-    no-ops per the python docs.
-    """
-    ensure_dir(location)
-    zipfp = open(filename, 'rb')
-    try:
-        zip = zipfile.ZipFile(zipfp, allowZip64=True)
-        leading = has_leading_dir(zip.namelist()) and flatten
-        for info in zip.infolist():
-            name = info.filename
-            fn = name
-            if leading:
-                fn = split_leading_dir(name)[1]
-            fn = os.path.join(location, fn)
-            dir = os.path.dirname(fn)
-            if fn.endswith('/') or fn.endswith('\\'):
-                # A directory
-                ensure_dir(fn)
-            else:
-                ensure_dir(dir)
-                # Don't use read() to avoid allocating an arbitrarily large
-                # chunk of memory for the file's content
-                fp = zip.open(name)
-                try:
-                    with open(fn, 'wb') as destfp:
-                        shutil.copyfileobj(fp, destfp)
-                finally:
-                    fp.close()
-                    mode = info.external_attr >> 16
-                    # if mode and regular file and any execute permissions for
-                    # user/group/world?
-                    if mode and stat.S_ISREG(mode) and mode & 0o111:
-                        # make dest file have execute for user/group/world
-                        # (chmod +x) no-op on windows per python docs
-                        os.chmod(fn, (0o777 - current_umask() | 0o111))
-    finally:
-        zipfp.close()
-
-
-def untar_file(filename, location):
-    # type: (str, str) -> None
-    """
-    Untar the file (with path `filename`) to the destination `location`.
-    All files are written based on system defaults and umask (i.e. permissions
-    are not preserved), except that regular file members with any execute
-    permissions (user, group, or world) have "chmod +x" applied after being
-    written.  Note that for windows, any execute changes using os.chmod are
-    no-ops per the python docs.
-    """
-    ensure_dir(location)
-    if filename.lower().endswith('.gz') or filename.lower().endswith('.tgz'):
-        mode = 'r:gz'
-    elif filename.lower().endswith(BZ2_EXTENSIONS):
-        mode = 'r:bz2'
-    elif filename.lower().endswith(XZ_EXTENSIONS):
-        mode = 'r:xz'
-    elif filename.lower().endswith('.tar'):
-        mode = 'r'
-    else:
-        logger.warning(
-            'Cannot determine compression type for file %s', filename,
-        )
-        mode = 'r:*'
-    tar = tarfile.open(filename, mode)
-    try:
-        leading = has_leading_dir([
-            member.name for member in tar.getmembers()
-        ])
-        for member in tar.getmembers():
-            fn = member.name
-            if leading:
-                # https://github.com/python/mypy/issues/1174
-                fn = split_leading_dir(fn)[1]  # type: ignore
-            path = os.path.join(location, fn)
-            if member.isdir():
-                ensure_dir(path)
-            elif member.issym():
-                try:
-                    # https://github.com/python/typeshed/issues/2673
-                    tar._extract_member(member, path)  # type: ignore
-                except Exception as exc:
-                    # Some corrupt tar files seem to produce this
-                    # (specifically bad symlinks)
-                    logger.warning(
-                        'In the tar file %s the member %s is invalid: %s',
-                        filename, member.name, exc,
-                    )
-                    continue
-            else:
-                try:
-                    fp = tar.extractfile(member)
-                except (KeyError, AttributeError) as exc:
-                    # Some corrupt tar files seem to produce this
-                    # (specifically bad symlinks)
-                    logger.warning(
-                        'In the tar file %s the member %s is invalid: %s',
-                        filename, member.name, exc,
-                    )
-                    continue
-                ensure_dir(os.path.dirname(path))
-                with open(path, 'wb') as destfp:
-                    shutil.copyfileobj(fp, destfp)
-                fp.close()
-                # Update the timestamp (useful for cython compiled files)
-                # https://github.com/python/typeshed/issues/2673
-                tar.utime(member, path)  # type: ignore
-                # member have any execute permissions for user/group/world?
-                if member.mode & 0o111:
-                    # make dest file have execute for user/group/world
-                    # no-op on windows per python docs
-                    os.chmod(path, (0o777 - current_umask() | 0o111))
-    finally:
-        tar.close()
-
-
-def unpack_file(
-    filename,  # type: str
-    location,  # type: str
-    content_type,  # type: Optional[str]
-    link  # type: Optional[Link]
-):
-    # type: (...) -> None
-    filename = os.path.realpath(filename)
-    if (content_type == 'application/zip' or
-            filename.lower().endswith(ZIP_EXTENSIONS) or
-            zipfile.is_zipfile(filename)):
-        unzip_file(
-            filename,
-            location,
-            flatten=not filename.endswith('.whl')
-        )
-    elif (content_type == 'application/x-gzip' or
-            tarfile.is_tarfile(filename) or
-            filename.lower().endswith(
-                TAR_EXTENSIONS + BZ2_EXTENSIONS + XZ_EXTENSIONS)):
-        untar_file(filename, location)
-    elif (content_type and content_type.startswith('text/html') and
-            is_svn_page(file_contents(filename))):
-        # We don't really care about this
-        from pip._internal.vcs.subversion import Subversion
-        Subversion('svn+' + link.url).unpack(location)
-    else:
-        # FIXME: handle?
-        # FIXME: magic signatures?
-        logger.critical(
-            'Cannot unpack file %s (downloaded from %s, content-type: %s); '
-            'cannot detect archive format',
-            filename, location, content_type,
-        )
-        raise InstallationError(
-            'Cannot determine archive format of %s' % location
-        )
-
-
-def call_subprocess(
-    cmd,  # type: List[str]
-    show_stdout=True,  # type: bool
-    cwd=None,  # type: Optional[str]
-    on_returncode='raise',  # type: str
-    extra_ok_returncodes=None,  # type: Optional[Iterable[int]]
-    command_desc=None,  # type: Optional[str]
-    extra_environ=None,  # type: Optional[Mapping[str, Any]]
-    unset_environ=None,  # type: Optional[Iterable[str]]
-    spinner=None  # type: Optional[SpinnerInterface]
-):
-    # type: (...) -> Optional[Text]
-    """
-    Args:
-      extra_ok_returncodes: an iterable of integer return codes that are
-        acceptable, in addition to 0. Defaults to None, which means [].
-      unset_environ: an iterable of environment variable names to unset
-        prior to calling subprocess.Popen().
-    """
-    if extra_ok_returncodes is None:
-        extra_ok_returncodes = []
-    if unset_environ is None:
-        unset_environ = []
-    # This function's handling of subprocess output is confusing and I
-    # previously broke it terribly, so as penance I will write a long comment
-    # explaining things.
-    #
-    # The obvious thing that affects output is the show_stdout=
-    # kwarg. show_stdout=True means, let the subprocess write directly to our
-    # stdout. Even though it is nominally the default, it is almost never used
-    # inside pip (and should not be used in new code without a very good
-    # reason); as of 2016-02-22 it is only used in a few places inside the VCS
-    # wrapper code. Ideally we should get rid of it entirely, because it
-    # creates a lot of complexity here for a rarely used feature.
-    #
-    # Most places in pip set show_stdout=False. What this means is:
-    # - We connect the child stdout to a pipe, which we read.
-    # - By default, we hide the output but show a spinner -- unless the
-    #   subprocess exits with an error, in which case we show the output.
-    # - If the --verbose option was passed (= loglevel is DEBUG), then we show
-    #   the output unconditionally. (But in this case we don't want to show
-    #   the output a second time if it turns out that there was an error.)
-    #
-    # stderr is always merged with stdout (even if show_stdout=True).
-    if show_stdout:
-        stdout = None
-    else:
-        stdout = subprocess.PIPE
-    if command_desc is None:
-        cmd_parts = []
-        for part in cmd:
-            if ' ' in part or '\n' in part or '"' in part or "'" in part:
-                part = '"%s"' % part.replace('"', '\\"')
-            cmd_parts.append(part)
-        command_desc = ' '.join(cmd_parts)
-    logger.debug("Running command %s", command_desc)
-    env = os.environ.copy()
-    if extra_environ:
-        env.update(extra_environ)
-    for name in unset_environ:
-        env.pop(name, None)
-    try:
-        proc = subprocess.Popen(
-            cmd, stderr=subprocess.STDOUT, stdin=subprocess.PIPE,
-            stdout=stdout, cwd=cwd, env=env,
-        )
-        proc.stdin.close()
-    except Exception as exc:
-        logger.critical(
-            "Error %s while executing command %s", exc, command_desc,
-        )
-        raise
-    all_output = []
-    if stdout is not None:
-        while True:
-            line = console_to_str(proc.stdout.readline())
-            if not line:
-                break
-            line = line.rstrip()
-            all_output.append(line + '\n')
-            if logger.getEffectiveLevel() <= std_logging.DEBUG:
-                # Show the line immediately
-                logger.debug(line)
-            else:
-                # Update the spinner
-                if spinner is not None:
-                    spinner.spin()
-    try:
-        proc.wait()
-    finally:
-        if proc.stdout:
-            proc.stdout.close()
-    if spinner is not None:
-        if proc.returncode:
-            spinner.finish("error")
-        else:
-            spinner.finish("done")
-    if proc.returncode and proc.returncode not in extra_ok_returncodes:
-        if on_returncode == 'raise':
-            if (logger.getEffectiveLevel() > std_logging.DEBUG and
-                    not show_stdout):
-                logger.info(
-                    'Complete output from command %s:', command_desc,
-                )
-                logger.info(
-                    ''.join(all_output) +
-                    '\n----------------------------------------'
-                )
-            raise InstallationError(
-                'Command "%s" failed with error code %s in %s'
-                % (command_desc, proc.returncode, cwd))
-        elif on_returncode == 'warn':
-            logger.warning(
-                'Command "%s" had error code %s in %s',
-                command_desc, proc.returncode, cwd,
-            )
-        elif on_returncode == 'ignore':
-            pass
-        else:
-            raise ValueError('Invalid value: on_returncode=%s' %
-                             repr(on_returncode))
-    if not show_stdout:
-        return ''.join(all_output)
-    return None
-
-
-def read_text_file(filename):
-    # type: (str) -> str
-    """Return the contents of *filename*.
-
-    Try to decode the file contents with utf-8, the preferred system encoding
-    (e.g., cp1252 on some Windows machines), and latin1, in that order.
-    Decoding a byte string with latin1 will never raise an error. In the worst
-    case, the returned string will contain some garbage characters.
-
-    """
-    with open(filename, 'rb') as fp:
-        data = fp.read()
-
-    encodings = ['utf-8', locale.getpreferredencoding(False), 'latin1']
-    for enc in encodings:
-        try:
-            # https://github.com/python/mypy/issues/1174
-            data = data.decode(enc)  # type: ignore
-        except UnicodeDecodeError:
-            continue
-        break
-
-    assert not isinstance(data, bytes)  # Latin1 should have worked.
-    return data
-
-
-def _make_build_dir(build_dir):
-    os.makedirs(build_dir)
-    write_delete_marker_file(build_dir)
-
-
-class FakeFile(object):
-    """Wrap a list of lines in an object with readline() to make
-    ConfigParser happy."""
-    def __init__(self, lines):
-        self._gen = (l for l in lines)
-
-    def readline(self):
-        try:
-            try:
-                return next(self._gen)
-            except NameError:
-                return self._gen.next()
-        except StopIteration:
-            return ''
-
-    def __iter__(self):
-        return self._gen
-
-
-class StreamWrapper(StringIO):
-
-    @classmethod
-    def from_stream(cls, orig_stream):
-        cls.orig_stream = orig_stream
-        return cls()
-
-    # compileall.compile_dir() needs stdout.encoding to print to stdout
-    @property
-    def encoding(self):
-        return self.orig_stream.encoding
-
-
-@contextlib.contextmanager
-def captured_output(stream_name):
-    """Return a context manager used by captured_stdout/stdin/stderr
-    that temporarily replaces the sys stream *stream_name* with a StringIO.
-
-    Taken from Lib/support/__init__.py in the CPython repo.
-    """
-    orig_stdout = getattr(sys, stream_name)
-    setattr(sys, stream_name, StreamWrapper.from_stream(orig_stdout))
-    try:
-        yield getattr(sys, stream_name)
-    finally:
-        setattr(sys, stream_name, orig_stdout)
-
-
-def captured_stdout():
-    """Capture the output of sys.stdout:
-
-       with captured_stdout() as stdout:
-           print('hello')
-       self.assertEqual(stdout.getvalue(), 'hello\n')
-
-    Taken from Lib/support/__init__.py in the CPython repo.
-    """
-    return captured_output('stdout')
-
-
-def captured_stderr():
-    """
-    See captured_stdout().
-    """
-    return captured_output('stderr')
-
-
-class cached_property(object):
-    """A property that is only computed once per instance and then replaces
-       itself with an ordinary attribute. Deleting the attribute resets the
-       property.
-
-       Source: https://github.com/bottlepy/bottle/blob/0.11.5/bottle.py#L175
-    """
-
-    def __init__(self, func):
-        self.__doc__ = getattr(func, '__doc__')
-        self.func = func
-
-    def __get__(self, obj, cls):
-        if obj is None:
-            # We're being accessed from the class itself, not from an object
-            return self
-        value = obj.__dict__[self.func.__name__] = self.func(obj)
-        return value
-
-
-def get_installed_version(dist_name, working_set=None):
-    """Get the installed version of dist_name avoiding pkg_resources cache"""
-    # Create a requirement that we'll look for inside of setuptools.
-    req = pkg_resources.Requirement.parse(dist_name)
-
-    if working_set is None:
-        # We want to avoid having this cached, so we need to construct a new
-        # working set each time.
-        working_set = pkg_resources.WorkingSet()
-
-    # Get the installed distribution from our working set
-    dist = working_set.find(req)
-
-    # Check to see if we got an installed distribution or not, if we did
-    # we want to return it's version.
-    return dist.version if dist else None
-
-
-def consume(iterator):
-    """Consume an iterable at C speed."""
-    deque(iterator, maxlen=0)
-
-
-# Simulates an enum
-def enum(*sequential, **named):
-    enums = dict(zip(sequential, range(len(sequential))), **named)
-    reverse = {value: key for key, value in enums.items()}
-    enums['reverse_mapping'] = reverse
-    return type('Enum', (), enums)
-
-
-def make_vcs_requirement_url(repo_url, rev, project_name, subdir=None):
-    """
-    Return the URL for a VCS requirement.
-
-    Args:
-      repo_url: the remote VCS url, with any needed VCS prefix (e.g. "git+").
-      project_name: the (unescaped) project name.
-    """
-    egg_project_name = pkg_resources.to_filename(project_name)
-    req = '{}@{}#egg={}'.format(repo_url, rev, egg_project_name)
-    if subdir:
-        req += '&subdirectory={}'.format(subdir)
-
-    return req
-
-
-def split_auth_from_netloc(netloc):
-    """
-    Parse out and remove the auth information from a netloc.
-
-    Returns: (netloc, (username, password)).
-    """
-    if '@' not in netloc:
-        return netloc, (None, None)
-
-    # Split from the right because that's how urllib.parse.urlsplit()
-    # behaves if more than one @ is present (which can be checked using
-    # the password attribute of urlsplit()'s return value).
-    auth, netloc = netloc.rsplit('@', 1)
-    if ':' in auth:
-        # Split from the left because that's how urllib.parse.urlsplit()
-        # behaves if more than one : is present (which again can be checked
-        # using the password attribute of the return value)
-        user_pass = auth.split(':', 1)
-    else:
-        user_pass = auth, None
-
-    user_pass = tuple(
-        None if x is None else urllib_unquote(x) for x in user_pass
-    )
-
-    return netloc, user_pass
-
-
-def redact_netloc(netloc):
-    # type: (str) -> str
-    """
-    Replace the password in a netloc with "****", if it exists.
-
-    For example, "user:pass@example.com" returns "user:****@example.com".
-    """
-    netloc, (user, password) = split_auth_from_netloc(netloc)
-    if user is None:
-        return netloc
-    password = '' if password is None else ':****'
-    return '{user}{password}@{netloc}'.format(user=urllib_parse.quote(user),
-                                              password=password,
-                                              netloc=netloc)
-
-
-def _transform_url(url, transform_netloc):
-    purl = urllib_parse.urlsplit(url)
-    netloc = transform_netloc(purl.netloc)
-    # stripped url
-    url_pieces = (
-        purl.scheme, netloc, purl.path, purl.query, purl.fragment
-    )
-    surl = urllib_parse.urlunsplit(url_pieces)
-    return surl
-
-
-def _get_netloc(netloc):
-    return split_auth_from_netloc(netloc)[0]
-
-
-def remove_auth_from_url(url):
-    # type: (str) -> str
-    # Return a copy of url with 'username:password@' removed.
-    # username/pass params are passed to subversion through flags
-    # and are not recognized in the url.
-    return _transform_url(url, _get_netloc)
-
-
-def redact_password_from_url(url):
-    # type: (str) -> str
-    """Replace the password in a given url with ****."""
-    return _transform_url(url, redact_netloc)
-
-
-def protect_pip_from_modification_on_windows(modifying_pip):
-    """Protection of pip.exe from modification on Windows
-
-    On Windows, any operation modifying pip should be run as:
-        python -m pip ...
-    """
-    pip_names = [
-        "pip.exe",
-        "pip{}.exe".format(sys.version_info[0]),
-        "pip{}.{}.exe".format(*sys.version_info[:2])
-    ]
-
-    # See https://github.com/pypa/pip/issues/1299 for more discussion
-    should_show_use_python_msg = (
-        modifying_pip and
-        WINDOWS and
-        os.path.basename(sys.argv[0]) in pip_names
-    )
-
-    if should_show_use_python_msg:
-        new_command = [
-            sys.executable, "-m", "pip"
-        ] + sys.argv[1:]
-        raise CommandError(
-            'To modify pip, please run the following command:\n{}'
-            .format(" ".join(new_command))
-        )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/models.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/models.py
deleted file mode 100644
index d5cb80a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/models.py
+++ /dev/null
@@ -1,40 +0,0 @@
-"""Utilities for defining models
-"""
-
-import operator
-
-
-class KeyBasedCompareMixin(object):
-    """Provides comparision capabilities that is based on a key
-    """
-
-    def __init__(self, key, defining_class):
-        self._compare_key = key
-        self._defining_class = defining_class
-
-    def __hash__(self):
-        return hash(self._compare_key)
-
-    def __lt__(self, other):
-        return self._compare(other, operator.__lt__)
-
-    def __le__(self, other):
-        return self._compare(other, operator.__le__)
-
-    def __gt__(self, other):
-        return self._compare(other, operator.__gt__)
-
-    def __ge__(self, other):
-        return self._compare(other, operator.__ge__)
-
-    def __eq__(self, other):
-        return self._compare(other, operator.__eq__)
-
-    def __ne__(self, other):
-        return self._compare(other, operator.__ne__)
-
-    def _compare(self, other, method):
-        if not isinstance(other, self._defining_class):
-            return NotImplemented
-
-        return method(self._compare_key, other._compare_key)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/outdated.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/outdated.py
deleted file mode 100644
index 37c47a4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/outdated.py
+++ /dev/null
@@ -1,164 +0,0 @@
-from __future__ import absolute_import
-
-import datetime
-import json
-import logging
-import os.path
-import sys
-
-from pip._vendor import lockfile, pkg_resources
-from pip._vendor.packaging import version as packaging_version
-
-from pip._internal.index import PackageFinder
-from pip._internal.utils.compat import WINDOWS
-from pip._internal.utils.filesystem import check_path_owner
-from pip._internal.utils.misc import ensure_dir, get_installed_version
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    import optparse  # noqa: F401
-    from typing import Any, Dict  # noqa: F401
-    from pip._internal.download import PipSession  # noqa: F401
-
-
-SELFCHECK_DATE_FMT = "%Y-%m-%dT%H:%M:%SZ"
-
-
-logger = logging.getLogger(__name__)
-
-
-class SelfCheckState(object):
-    def __init__(self, cache_dir):
-        # type: (str) -> None
-        self.state = {}  # type: Dict[str, Any]
-        self.statefile_path = None
-
-        # Try to load the existing state
-        if cache_dir:
-            self.statefile_path = os.path.join(cache_dir, "selfcheck.json")
-            try:
-                with open(self.statefile_path) as statefile:
-                    self.state = json.load(statefile)[sys.prefix]
-            except (IOError, ValueError, KeyError):
-                # Explicitly suppressing exceptions, since we don't want to
-                # error out if the cache file is invalid.
-                pass
-
-    def save(self, pypi_version, current_time):
-        # type: (str, datetime.datetime) -> None
-        # If we do not have a path to cache in, don't bother saving.
-        if not self.statefile_path:
-            return
-
-        # Check to make sure that we own the directory
-        if not check_path_owner(os.path.dirname(self.statefile_path)):
-            return
-
-        # Now that we've ensured the directory is owned by this user, we'll go
-        # ahead and make sure that all our directories are created.
-        ensure_dir(os.path.dirname(self.statefile_path))
-
-        # Attempt to write out our version check file
-        with lockfile.LockFile(self.statefile_path):
-            if os.path.exists(self.statefile_path):
-                with open(self.statefile_path) as statefile:
-                    state = json.load(statefile)
-            else:
-                state = {}
-
-            state[sys.prefix] = {
-                "last_check": current_time.strftime(SELFCHECK_DATE_FMT),
-                "pypi_version": pypi_version,
-            }
-
-            with open(self.statefile_path, "w") as statefile:
-                json.dump(state, statefile, sort_keys=True,
-                          separators=(",", ":"))
-
-
-def was_installed_by_pip(pkg):
-    # type: (str) -> bool
-    """Checks whether pkg was installed by pip
-
-    This is used not to display the upgrade message when pip is in fact
-    installed by system package manager, such as dnf on Fedora.
-    """
-    try:
-        dist = pkg_resources.get_distribution(pkg)
-        return (dist.has_metadata('INSTALLER') and
-                'pip' in dist.get_metadata_lines('INSTALLER'))
-    except pkg_resources.DistributionNotFound:
-        return False
-
-
-def pip_version_check(session, options):
-    # type: (PipSession, optparse.Values) -> None
-    """Check for an update for pip.
-
-    Limit the frequency of checks to once per week. State is stored either in
-    the active virtualenv or in the user's USER_CACHE_DIR keyed off the prefix
-    of the pip script path.
-    """
-    installed_version = get_installed_version("pip")
-    if not installed_version:
-        return
-
-    pip_version = packaging_version.parse(installed_version)
-    pypi_version = None
-
-    try:
-        state = SelfCheckState(cache_dir=options.cache_dir)
-
-        current_time = datetime.datetime.utcnow()
-        # Determine if we need to refresh the state
-        if "last_check" in state.state and "pypi_version" in state.state:
-            last_check = datetime.datetime.strptime(
-                state.state["last_check"],
-                SELFCHECK_DATE_FMT
-            )
-            if (current_time - last_check).total_seconds() < 7 * 24 * 60 * 60:
-                pypi_version = state.state["pypi_version"]
-
-        # Refresh the version if we need to or just see if we need to warn
-        if pypi_version is None:
-            # Lets use PackageFinder to see what the latest pip version is
-            finder = PackageFinder(
-                find_links=options.find_links,
-                index_urls=[options.index_url] + options.extra_index_urls,
-                allow_all_prereleases=False,  # Explicitly set to False
-                trusted_hosts=options.trusted_hosts,
-                session=session,
-            )
-            all_candidates = finder.find_all_candidates("pip")
-            if not all_candidates:
-                return
-            pypi_version = str(
-                max(all_candidates, key=lambda c: c.version).version
-            )
-
-            # save that we've performed a check
-            state.save(pypi_version, current_time)
-
-        remote_version = packaging_version.parse(pypi_version)
-
-        # Determine if our pypi_version is older
-        if (pip_version < remote_version and
-                pip_version.base_version != remote_version.base_version and
-                was_installed_by_pip('pip')):
-            # Advise "python -m pip" on Windows to avoid issues
-            # with overwriting pip.exe.
-            if WINDOWS:
-                pip_cmd = "python -m pip"
-            else:
-                pip_cmd = "pip"
-            logger.warning(
-                "You are using pip version %s, however version %s is "
-                "available.\nYou should consider upgrading via the "
-                "'%s install --upgrade pip' command.",
-                pip_version, pypi_version, pip_cmd
-            )
-    except Exception:
-        logger.debug(
-            "There was an error checking the latest version of pip",
-            exc_info=True,
-        )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/packaging.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/packaging.py
deleted file mode 100644
index 7aaf7b5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/packaging.py
+++ /dev/null
@@ -1,85 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import sys
-from email.parser import FeedParser
-
-from pip._vendor import pkg_resources
-from pip._vendor.packaging import specifiers, version
-
-from pip._internal import exceptions
-from pip._internal.utils.misc import display_path
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Optional  # noqa: F401
-    from email.message import Message  # noqa: F401
-    from pip._vendor.pkg_resources import Distribution  # noqa: F401
-
-
-logger = logging.getLogger(__name__)
-
-
-def check_requires_python(requires_python):
-    # type: (Optional[str]) -> bool
-    """
-    Check if the python version in use match the `requires_python` specifier.
-
-    Returns `True` if the version of python in use matches the requirement.
-    Returns `False` if the version of python in use does not matches the
-    requirement.
-
-    Raises an InvalidSpecifier if `requires_python` have an invalid format.
-    """
-    if requires_python is None:
-        # The package provides no information
-        return True
-    requires_python_specifier = specifiers.SpecifierSet(requires_python)
-
-    # We only use major.minor.micro
-    python_version = version.parse('.'.join(map(str, sys.version_info[:3])))
-    return python_version in requires_python_specifier
-
-
-def get_metadata(dist):
-    # type: (Distribution) -> Message
-    if (isinstance(dist, pkg_resources.DistInfoDistribution) and
-            dist.has_metadata('METADATA')):
-        metadata = dist.get_metadata('METADATA')
-    elif dist.has_metadata('PKG-INFO'):
-        metadata = dist.get_metadata('PKG-INFO')
-    else:
-        logger.warning("No metadata found in %s", display_path(dist.location))
-        metadata = ''
-
-    feed_parser = FeedParser()
-    feed_parser.feed(metadata)
-    return feed_parser.close()
-
-
-def check_dist_requires_python(dist):
-    pkg_info_dict = get_metadata(dist)
-    requires_python = pkg_info_dict.get('Requires-Python')
-    try:
-        if not check_requires_python(requires_python):
-            raise exceptions.UnsupportedPythonVersion(
-                "%s requires Python '%s' but the running Python is %s" % (
-                    dist.project_name,
-                    requires_python,
-                    '.'.join(map(str, sys.version_info[:3])),)
-            )
-    except specifiers.InvalidSpecifier as e:
-        logger.warning(
-            "Package %s has an invalid Requires-Python entry %s - %s",
-            dist.project_name, requires_python, e,
-        )
-        return
-
-
-def get_installer(dist):
-    # type: (Distribution) -> str
-    if dist.has_metadata('INSTALLER'):
-        for line in dist.get_metadata_lines('INSTALLER'):
-            if line.strip():
-                return line.strip()
-    return ''
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/setuptools_build.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/setuptools_build.py
deleted file mode 100644
index 03973e9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/setuptools_build.py
+++ /dev/null
@@ -1,8 +0,0 @@
-# Shim to wrap setup.py invocation with setuptools
-SETUPTOOLS_SHIM = (
-    "import setuptools, tokenize;__file__=%r;"
-    "f=getattr(tokenize, 'open', open)(__file__);"
-    "code=f.read().replace('\\r\\n', '\\n');"
-    "f.close();"
-    "exec(compile(code, __file__, 'exec'))"
-)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/temp_dir.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/temp_dir.py
deleted file mode 100644
index 2c81ad5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/temp_dir.py
+++ /dev/null
@@ -1,155 +0,0 @@
-from __future__ import absolute_import
-
-import errno
-import itertools
-import logging
-import os.path
-import tempfile
-
-from pip._internal.utils.misc import rmtree
-
-logger = logging.getLogger(__name__)
-
-
-class TempDirectory(object):
-    """Helper class that owns and cleans up a temporary directory.
-
-    This class can be used as a context manager or as an OO representation of a
-    temporary directory.
-
-    Attributes:
-        path
-            Location to the created temporary directory or None
-        delete
-            Whether the directory should be deleted when exiting
-            (when used as a contextmanager)
-
-    Methods:
-        create()
-            Creates a temporary directory and stores its path in the path
-            attribute.
-        cleanup()
-            Deletes the temporary directory and sets path attribute to None
-
-    When used as a context manager, a temporary directory is created on
-    entering the context and, if the delete attribute is True, on exiting the
-    context the created directory is deleted.
-    """
-
-    def __init__(self, path=None, delete=None, kind="temp"):
-        super(TempDirectory, self).__init__()
-
-        if path is None and delete is None:
-            # If we were not given an explicit directory, and we were not given
-            # an explicit delete option, then we'll default to deleting.
-            delete = True
-
-        self.path = path
-        self.delete = delete
-        self.kind = kind
-
-    def __repr__(self):
-        return "<{} {!r}>".format(self.__class__.__name__, self.path)
-
-    def __enter__(self):
-        self.create()
-        return self
-
-    def __exit__(self, exc, value, tb):
-        if self.delete:
-            self.cleanup()
-
-    def create(self):
-        """Create a temporary directory and store its path in self.path
-        """
-        if self.path is not None:
-            logger.debug(
-                "Skipped creation of temporary directory: {}".format(self.path)
-            )
-            return
-        # We realpath here because some systems have their default tmpdir
-        # symlinked to another directory.  This tends to confuse build
-        # scripts, so we canonicalize the path by traversing potential
-        # symlinks here.
-        self.path = os.path.realpath(
-            tempfile.mkdtemp(prefix="pip-{}-".format(self.kind))
-        )
-        logger.debug("Created temporary directory: {}".format(self.path))
-
-    def cleanup(self):
-        """Remove the temporary directory created and reset state
-        """
-        if self.path is not None and os.path.exists(self.path):
-            rmtree(self.path)
-        self.path = None
-
-
-class AdjacentTempDirectory(TempDirectory):
-    """Helper class that creates a temporary directory adjacent to a real one.
-
-    Attributes:
-        original
-            The original directory to create a temp directory for.
-        path
-            After calling create() or entering, contains the full
-            path to the temporary directory.
-        delete
-            Whether the directory should be deleted when exiting
-            (when used as a contextmanager)
-
-    """
-    # The characters that may be used to name the temp directory
-    # We always prepend a ~ and then rotate through these until
-    # a usable name is found.
-    # pkg_resources raises a different error for .dist-info folder
-    # with leading '-' and invalid metadata
-    LEADING_CHARS = "-~.=%0123456789"
-
-    def __init__(self, original, delete=None):
-        super(AdjacentTempDirectory, self).__init__(delete=delete)
-        self.original = original.rstrip('/\\')
-
-    @classmethod
-    def _generate_names(cls, name):
-        """Generates a series of temporary names.
-
-        The algorithm replaces the leading characters in the name
-        with ones that are valid filesystem characters, but are not
-        valid package names (for both Python and pip definitions of
-        package).
-        """
-        for i in range(1, len(name)):
-            for candidate in itertools.combinations_with_replacement(
-                    cls.LEADING_CHARS, i - 1):
-                new_name = '~' + ''.join(candidate) + name[i:]
-                if new_name != name:
-                    yield new_name
-
-        # If we make it this far, we will have to make a longer name
-        for i in range(len(cls.LEADING_CHARS)):
-            for candidate in itertools.combinations_with_replacement(
-                    cls.LEADING_CHARS, i):
-                new_name = '~' + ''.join(candidate) + name
-                if new_name != name:
-                    yield new_name
-
-    def create(self):
-        root, name = os.path.split(self.original)
-        for candidate in self._generate_names(name):
-            path = os.path.join(root, candidate)
-            try:
-                os.mkdir(path)
-            except OSError as ex:
-                # Continue if the name exists already
-                if ex.errno != errno.EEXIST:
-                    raise
-            else:
-                self.path = os.path.realpath(path)
-                break
-
-        if not self.path:
-            # Final fallback on the default behavior.
-            self.path = os.path.realpath(
-                tempfile.mkdtemp(prefix="pip-{}-".format(self.kind))
-            )
-        logger.debug("Created temporary directory: {}".format(self.path))
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/typing.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/typing.py
deleted file mode 100644
index e085cdf..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/typing.py
+++ /dev/null
@@ -1,29 +0,0 @@
-"""For neatly implementing static typing in pip.
-
-`mypy` - the static type analysis tool we use - uses the `typing` module, which
-provides core functionality fundamental to mypy's functioning.
-
-Generally, `typing` would be imported at runtime and used in that fashion -
-it acts as a no-op at runtime and does not have any run-time overhead by
-design.
-
-As it turns out, `typing` is not vendorable - it uses separate sources for
-Python 2/Python 3. Thus, this codebase can not expect it to be present.
-To work around this, mypy allows the typing import to be behind a False-y
-optional to prevent it from running at runtime and type-comments can be used
-to remove the need for the types to be accessible directly during runtime.
-
-This module provides the False-y guard in a nicely named fashion so that a
-curious maintainer can reach here to read this.
-
-In pip, all static-typing related imports should be guarded as follows:
-
-    from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-    if MYPY_CHECK_RUNNING:
-        from typing import ...  # noqa: F401
-
-Ref: https://github.com/python/mypy/issues/3216
-"""
-
-MYPY_CHECK_RUNNING = False
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/ui.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/ui.py
deleted file mode 100644
index 433675d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/utils/ui.py
+++ /dev/null
@@ -1,441 +0,0 @@
-from __future__ import absolute_import, division
-
-import contextlib
-import itertools
-import logging
-import sys
-import time
-from signal import SIGINT, default_int_handler, signal
-
-from pip._vendor import six
-from pip._vendor.progress.bar import (
-    Bar, ChargingBar, FillingCirclesBar, FillingSquaresBar, IncrementalBar,
-    ShadyBar,
-)
-from pip._vendor.progress.helpers import HIDE_CURSOR, SHOW_CURSOR, WritelnMixin
-from pip._vendor.progress.spinner import Spinner
-
-from pip._internal.utils.compat import WINDOWS
-from pip._internal.utils.logging import get_indentation
-from pip._internal.utils.misc import format_size
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import Any, Iterator, IO  # noqa: F401
-
-try:
-    from pip._vendor import colorama
-# Lots of different errors can come from this, including SystemError and
-# ImportError.
-except Exception:
-    colorama = None
-
-logger = logging.getLogger(__name__)
-
-
-def _select_progress_class(preferred, fallback):
-    encoding = getattr(preferred.file, "encoding", None)
-
-    # If we don't know what encoding this file is in, then we'll just assume
-    # that it doesn't support unicode and use the ASCII bar.
-    if not encoding:
-        return fallback
-
-    # Collect all of the possible characters we want to use with the preferred
-    # bar.
-    characters = [
-        getattr(preferred, "empty_fill", six.text_type()),
-        getattr(preferred, "fill", six.text_type()),
-    ]
-    characters += list(getattr(preferred, "phases", []))
-
-    # Try to decode the characters we're using for the bar using the encoding
-    # of the given file, if this works then we'll assume that we can use the
-    # fancier bar and if not we'll fall back to the plaintext bar.
-    try:
-        six.text_type().join(characters).encode(encoding)
-    except UnicodeEncodeError:
-        return fallback
-    else:
-        return preferred
-
-
-_BaseBar = _select_progress_class(IncrementalBar, Bar)  # type: Any
-
-
-class InterruptibleMixin(object):
-    """
-    Helper to ensure that self.finish() gets called on keyboard interrupt.
-
-    This allows downloads to be interrupted without leaving temporary state
-    (like hidden cursors) behind.
-
-    This class is similar to the progress library's existing SigIntMixin
-    helper, but as of version 1.2, that helper has the following problems:
-
-    1. It calls sys.exit().
-    2. It discards the existing SIGINT handler completely.
-    3. It leaves its own handler in place even after an uninterrupted finish,
-       which will have unexpected delayed effects if the user triggers an
-       unrelated keyboard interrupt some time after a progress-displaying
-       download has already completed, for example.
-    """
-
-    def __init__(self, *args, **kwargs):
-        """
-        Save the original SIGINT handler for later.
-        """
-        super(InterruptibleMixin, self).__init__(*args, **kwargs)
-
-        self.original_handler = signal(SIGINT, self.handle_sigint)
-
-        # If signal() returns None, the previous handler was not installed from
-        # Python, and we cannot restore it. This probably should not happen,
-        # but if it does, we must restore something sensible instead, at least.
-        # The least bad option should be Python's default SIGINT handler, which
-        # just raises KeyboardInterrupt.
-        if self.original_handler is None:
-            self.original_handler = default_int_handler
-
-    def finish(self):
-        """
-        Restore the original SIGINT handler after finishing.
-
-        This should happen regardless of whether the progress display finishes
-        normally, or gets interrupted.
-        """
-        super(InterruptibleMixin, self).finish()
-        signal(SIGINT, self.original_handler)
-
-    def handle_sigint(self, signum, frame):
-        """
-        Call self.finish() before delegating to the original SIGINT handler.
-
-        This handler should only be in place while the progress display is
-        active.
-        """
-        self.finish()
-        self.original_handler(signum, frame)
-
-
-class SilentBar(Bar):
-
-    def update(self):
-        pass
-
-
-class BlueEmojiBar(IncrementalBar):
-
-    suffix = "%(percent)d%%"
-    bar_prefix = " "
-    bar_suffix = " "
-    phases = (u"\U0001F539", u"\U0001F537", u"\U0001F535")  # type: Any
-
-
-class DownloadProgressMixin(object):
-
-    def __init__(self, *args, **kwargs):
-        super(DownloadProgressMixin, self).__init__(*args, **kwargs)
-        self.message = (" " * (get_indentation() + 2)) + self.message
-
-    @property
-    def downloaded(self):
-        return format_size(self.index)
-
-    @property
-    def download_speed(self):
-        # Avoid zero division errors...
-        if self.avg == 0.0:
-            return "..."
-        return format_size(1 / self.avg) + "/s"
-
-    @property
-    def pretty_eta(self):
-        if self.eta:
-            return "eta %s" % self.eta_td
-        return ""
-
-    def iter(self, it, n=1):
-        for x in it:
-            yield x
-            self.next(n)
-        self.finish()
-
-
-class WindowsMixin(object):
-
-    def __init__(self, *args, **kwargs):
-        # The Windows terminal does not support the hide/show cursor ANSI codes
-        # even with colorama. So we'll ensure that hide_cursor is False on
-        # Windows.
-        # This call neds to go before the super() call, so that hide_cursor
-        # is set in time. The base progress bar class writes the "hide cursor"
-        # code to the terminal in its init, so if we don't set this soon
-        # enough, we get a "hide" with no corresponding "show"...
-        if WINDOWS and self.hide_cursor:
-            self.hide_cursor = False
-
-        super(WindowsMixin, self).__init__(*args, **kwargs)
-
-        # Check if we are running on Windows and we have the colorama module,
-        # if we do then wrap our file with it.
-        if WINDOWS and colorama:
-            self.file = colorama.AnsiToWin32(self.file)
-            # The progress code expects to be able to call self.file.isatty()
-            # but the colorama.AnsiToWin32() object doesn't have that, so we'll
-            # add it.
-            self.file.isatty = lambda: self.file.wrapped.isatty()
-            # The progress code expects to be able to call self.file.flush()
-            # but the colorama.AnsiToWin32() object doesn't have that, so we'll
-            # add it.
-            self.file.flush = lambda: self.file.wrapped.flush()
-
-
-class BaseDownloadProgressBar(WindowsMixin, InterruptibleMixin,
-                              DownloadProgressMixin):
-
-    file = sys.stdout
-    message = "%(percent)d%%"
-    suffix = "%(downloaded)s %(download_speed)s %(pretty_eta)s"
-
-# NOTE: The "type: ignore" comments on the following classes are there to
-#       work around https://github.com/python/typing/issues/241
-
-
-class DefaultDownloadProgressBar(BaseDownloadProgressBar,
-                                 _BaseBar):
-    pass
-
-
-class DownloadSilentBar(BaseDownloadProgressBar, SilentBar):  # type: ignore
-    pass
-
-
-class DownloadIncrementalBar(BaseDownloadProgressBar,  # type: ignore
-                             IncrementalBar):
-    pass
-
-
-class DownloadChargingBar(BaseDownloadProgressBar,  # type: ignore
-                          ChargingBar):
-    pass
-
-
-class DownloadShadyBar(BaseDownloadProgressBar, ShadyBar):  # type: ignore
-    pass
-
-
-class DownloadFillingSquaresBar(BaseDownloadProgressBar,  # type: ignore
-                                FillingSquaresBar):
-    pass
-
-
-class DownloadFillingCirclesBar(BaseDownloadProgressBar,  # type: ignore
-                                FillingCirclesBar):
-    pass
-
-
-class DownloadBlueEmojiProgressBar(BaseDownloadProgressBar,  # type: ignore
-                                   BlueEmojiBar):
-    pass
-
-
-class DownloadProgressSpinner(WindowsMixin, InterruptibleMixin,
-                              DownloadProgressMixin, WritelnMixin, Spinner):
-
-    file = sys.stdout
-    suffix = "%(downloaded)s %(download_speed)s"
-
-    def next_phase(self):
-        if not hasattr(self, "_phaser"):
-            self._phaser = itertools.cycle(self.phases)
-        return next(self._phaser)
-
-    def update(self):
-        message = self.message % self
-        phase = self.next_phase()
-        suffix = self.suffix % self
-        line = ''.join([
-            message,
-            " " if message else "",
-            phase,
-            " " if suffix else "",
-            suffix,
-        ])
-
-        self.writeln(line)
-
-
-BAR_TYPES = {
-    "off": (DownloadSilentBar, DownloadSilentBar),
-    "on": (DefaultDownloadProgressBar, DownloadProgressSpinner),
-    "ascii": (DownloadIncrementalBar, DownloadProgressSpinner),
-    "pretty": (DownloadFillingCirclesBar, DownloadProgressSpinner),
-    "emoji": (DownloadBlueEmojiProgressBar, DownloadProgressSpinner)
-}
-
-
-def DownloadProgressProvider(progress_bar, max=None):
-    if max is None or max == 0:
-        return BAR_TYPES[progress_bar][1]().iter
-    else:
-        return BAR_TYPES[progress_bar][0](max=max).iter
-
-
-################################################################
-# Generic "something is happening" spinners
-#
-# We don't even try using progress.spinner.Spinner here because it's actually
-# simpler to reimplement from scratch than to coerce their code into doing
-# what we need.
-################################################################
-
-@contextlib.contextmanager
-def hidden_cursor(file):
-    # type: (IO) -> Iterator[None]
-    # The Windows terminal does not support the hide/show cursor ANSI codes,
-    # even via colorama. So don't even try.
-    if WINDOWS:
-        yield
-    # We don't want to clutter the output with control characters if we're
-    # writing to a file, or if the user is running with --quiet.
-    # See https://github.com/pypa/pip/issues/3418
-    elif not file.isatty() or logger.getEffectiveLevel() > logging.INFO:
-        yield
-    else:
-        file.write(HIDE_CURSOR)
-        try:
-            yield
-        finally:
-            file.write(SHOW_CURSOR)
-
-
-class RateLimiter(object):
-    def __init__(self, min_update_interval_seconds):
-        # type: (float) -> None
-        self._min_update_interval_seconds = min_update_interval_seconds
-        self._last_update = 0  # type: float
-
-    def ready(self):
-        # type: () -> bool
-        now = time.time()
-        delta = now - self._last_update
-        return delta >= self._min_update_interval_seconds
-
-    def reset(self):
-        # type: () -> None
-        self._last_update = time.time()
-
-
-class SpinnerInterface(object):
-    def spin(self):
-        # type: () -> None
-        raise NotImplementedError()
-
-    def finish(self, final_status):
-        # type: (str) -> None
-        raise NotImplementedError()
-
-
-class InteractiveSpinner(SpinnerInterface):
-    def __init__(self, message, file=None, spin_chars="-\\|/",
-                 # Empirically, 8 updates/second looks nice
-                 min_update_interval_seconds=0.125):
-        self._message = message
-        if file is None:
-            file = sys.stdout
-        self._file = file
-        self._rate_limiter = RateLimiter(min_update_interval_seconds)
-        self._finished = False
-
-        self._spin_cycle = itertools.cycle(spin_chars)
-
-        self._file.write(" " * get_indentation() + self._message + " ... ")
-        self._width = 0
-
-    def _write(self, status):
-        assert not self._finished
-        # Erase what we wrote before by backspacing to the beginning, writing
-        # spaces to overwrite the old text, and then backspacing again
-        backup = "\b" * self._width
-        self._file.write(backup + " " * self._width + backup)
-        # Now we have a blank slate to add our status
-        self._file.write(status)
-        self._width = len(status)
-        self._file.flush()
-        self._rate_limiter.reset()
-
-    def spin(self):
-        # type: () -> None
-        if self._finished:
-            return
-        if not self._rate_limiter.ready():
-            return
-        self._write(next(self._spin_cycle))
-
-    def finish(self, final_status):
-        # type: (str) -> None
-        if self._finished:
-            return
-        self._write(final_status)
-        self._file.write("\n")
-        self._file.flush()
-        self._finished = True
-
-
-# Used for dumb terminals, non-interactive installs (no tty), etc.
-# We still print updates occasionally (once every 60 seconds by default) to
-# act as a keep-alive for systems like Travis-CI that take lack-of-output as
-# an indication that a task has frozen.
-class NonInteractiveSpinner(SpinnerInterface):
-    def __init__(self, message, min_update_interval_seconds=60):
-        # type: (str, float) -> None
-        self._message = message
-        self._finished = False
-        self._rate_limiter = RateLimiter(min_update_interval_seconds)
-        self._update("started")
-
-    def _update(self, status):
-        assert not self._finished
-        self._rate_limiter.reset()
-        logger.info("%s: %s", self._message, status)
-
-    def spin(self):
-        # type: () -> None
-        if self._finished:
-            return
-        if not self._rate_limiter.ready():
-            return
-        self._update("still running...")
-
-    def finish(self, final_status):
-        # type: (str) -> None
-        if self._finished:
-            return
-        self._update("finished with status '%s'" % (final_status,))
-        self._finished = True
-
-
-@contextlib.contextmanager
-def open_spinner(message):
-    # type: (str) -> Iterator[SpinnerInterface]
-    # Interactive spinner goes directly to sys.stdout rather than being routed
-    # through the logging system, but it acts like it has level INFO,
-    # i.e. it's only displayed if we're at level INFO or better.
-    # Non-interactive spinner goes through the logging system, so it is always
-    # in sync with logging configuration.
-    if sys.stdout.isatty() and logger.getEffectiveLevel() <= logging.INFO:
-        spinner = InteractiveSpinner(message)  # type: SpinnerInterface
-    else:
-        spinner = NonInteractiveSpinner(message)
-    try:
-        with hidden_cursor(sys.stdout):
-            yield spinner
-    except KeyboardInterrupt:
-        spinner.finish("canceled")
-        raise
-    except Exception:
-        spinner.finish("error")
-        raise
-    else:
-        spinner.finish("done")
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__init__.py
deleted file mode 100644
index 9cba764..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__init__.py
+++ /dev/null
@@ -1,534 +0,0 @@
-"""Handles all VCS (version control) support"""
-from __future__ import absolute_import
-
-import errno
-import logging
-import os
-import shutil
-import sys
-
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-
-from pip._internal.exceptions import BadCommand
-from pip._internal.utils.misc import (
-    display_path, backup_dir, call_subprocess, rmtree, ask_path_exists,
-)
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Any, Dict, Iterable, List, Mapping, Optional, Text, Tuple, Type
-    )
-    from pip._internal.utils.ui import SpinnerInterface  # noqa: F401
-
-    AuthInfo = Tuple[Optional[str], Optional[str]]
-
-__all__ = ['vcs']
-
-
-logger = logging.getLogger(__name__)
-
-
-class RemoteNotFoundError(Exception):
-    pass
-
-
-class RevOptions(object):
-
-    """
-    Encapsulates a VCS-specific revision to install, along with any VCS
-    install options.
-
-    Instances of this class should be treated as if immutable.
-    """
-
-    def __init__(self, vcs, rev=None, extra_args=None):
-        # type: (VersionControl, Optional[str], Optional[List[str]]) -> None
-        """
-        Args:
-          vcs: a VersionControl object.
-          rev: the name of the revision to install.
-          extra_args: a list of extra options.
-        """
-        if extra_args is None:
-            extra_args = []
-
-        self.extra_args = extra_args
-        self.rev = rev
-        self.vcs = vcs
-
-    def __repr__(self):
-        return '<RevOptions {}: rev={!r}>'.format(self.vcs.name, self.rev)
-
-    @property
-    def arg_rev(self):
-        # type: () -> Optional[str]
-        if self.rev is None:
-            return self.vcs.default_arg_rev
-
-        return self.rev
-
-    def to_args(self):
-        # type: () -> List[str]
-        """
-        Return the VCS-specific command arguments.
-        """
-        args = []  # type: List[str]
-        rev = self.arg_rev
-        if rev is not None:
-            args += self.vcs.get_base_rev_args(rev)
-        args += self.extra_args
-
-        return args
-
-    def to_display(self):
-        # type: () -> str
-        if not self.rev:
-            return ''
-
-        return ' (to revision {})'.format(self.rev)
-
-    def make_new(self, rev):
-        # type: (str) -> RevOptions
-        """
-        Make a copy of the current instance, but with a new rev.
-
-        Args:
-          rev: the name of the revision for the new object.
-        """
-        return self.vcs.make_rev_options(rev, extra_args=self.extra_args)
-
-
-class VcsSupport(object):
-    _registry = {}  # type: Dict[str, Type[VersionControl]]
-    schemes = ['ssh', 'git', 'hg', 'bzr', 'sftp', 'svn']
-
-    def __init__(self):
-        # type: () -> None
-        # Register more schemes with urlparse for various version control
-        # systems
-        urllib_parse.uses_netloc.extend(self.schemes)
-        # Python >= 2.7.4, 3.3 doesn't have uses_fragment
-        if getattr(urllib_parse, 'uses_fragment', None):
-            urllib_parse.uses_fragment.extend(self.schemes)
-        super(VcsSupport, self).__init__()
-
-    def __iter__(self):
-        return self._registry.__iter__()
-
-    @property
-    def backends(self):
-        # type: () -> List[Type[VersionControl]]
-        return list(self._registry.values())
-
-    @property
-    def dirnames(self):
-        # type: () -> List[str]
-        return [backend.dirname for backend in self.backends]
-
-    @property
-    def all_schemes(self):
-        # type: () -> List[str]
-        schemes = []  # type: List[str]
-        for backend in self.backends:
-            schemes.extend(backend.schemes)
-        return schemes
-
-    def register(self, cls):
-        # type: (Type[VersionControl]) -> None
-        if not hasattr(cls, 'name'):
-            logger.warning('Cannot register VCS %s', cls.__name__)
-            return
-        if cls.name not in self._registry:
-            self._registry[cls.name] = cls
-            logger.debug('Registered VCS backend: %s', cls.name)
-
-    def unregister(self, cls=None, name=None):
-        # type: (Optional[Type[VersionControl]], Optional[str]) -> None
-        if name in self._registry:
-            del self._registry[name]
-        elif cls in self._registry.values():
-            del self._registry[cls.name]
-        else:
-            logger.warning('Cannot unregister because no class or name given')
-
-    def get_backend_type(self, location):
-        # type: (str) -> Optional[Type[VersionControl]]
-        """
-        Return the type of the version control backend if found at given
-        location, e.g. vcs.get_backend_type('/path/to/vcs/checkout')
-        """
-        for vc_type in self._registry.values():
-            if vc_type.controls_location(location):
-                logger.debug('Determine that %s uses VCS: %s',
-                             location, vc_type.name)
-                return vc_type
-        return None
-
-    def get_backend(self, name):
-        # type: (str) -> Optional[Type[VersionControl]]
-        name = name.lower()
-        if name in self._registry:
-            return self._registry[name]
-        return None
-
-
-vcs = VcsSupport()
-
-
-class VersionControl(object):
-    name = ''
-    dirname = ''
-    repo_name = ''
-    # List of supported schemes for this Version Control
-    schemes = ()  # type: Tuple[str, ...]
-    # Iterable of environment variable names to pass to call_subprocess().
-    unset_environ = ()  # type: Tuple[str, ...]
-    default_arg_rev = None  # type: Optional[str]
-
-    def __init__(self, url=None, *args, **kwargs):
-        self.url = url
-        super(VersionControl, self).__init__(*args, **kwargs)
-
-    def get_base_rev_args(self, rev):
-        """
-        Return the base revision arguments for a vcs command.
-
-        Args:
-          rev: the name of a revision to install.  Cannot be None.
-        """
-        raise NotImplementedError
-
-    def make_rev_options(self, rev=None, extra_args=None):
-        # type: (Optional[str], Optional[List[str]]) -> RevOptions
-        """
-        Return a RevOptions object.
-
-        Args:
-          rev: the name of a revision to install.
-          extra_args: a list of extra options.
-        """
-        return RevOptions(self, rev, extra_args=extra_args)
-
-    @classmethod
-    def _is_local_repository(cls, repo):
-        # type: (str) -> bool
-        """
-           posix absolute paths start with os.path.sep,
-           win32 ones start with drive (like c:\\folder)
-        """
-        drive, tail = os.path.splitdrive(repo)
-        return repo.startswith(os.path.sep) or bool(drive)
-
-    def export(self, location):
-        """
-        Export the repository at the url to the destination location
-        i.e. only download the files, without vcs informations
-        """
-        raise NotImplementedError
-
-    def get_netloc_and_auth(self, netloc, scheme):
-        """
-        Parse the repository URL's netloc, and return the new netloc to use
-        along with auth information.
-
-        Args:
-          netloc: the original repository URL netloc.
-          scheme: the repository URL's scheme without the vcs prefix.
-
-        This is mainly for the Subversion class to override, so that auth
-        information can be provided via the --username and --password options
-        instead of through the URL.  For other subclasses like Git without
-        such an option, auth information must stay in the URL.
-
-        Returns: (netloc, (username, password)).
-        """
-        return netloc, (None, None)
-
-    def get_url_rev_and_auth(self, url):
-        # type: (str) -> Tuple[str, Optional[str], AuthInfo]
-        """
-        Parse the repository URL to use, and return the URL, revision,
-        and auth info to use.
-
-        Returns: (url, rev, (username, password)).
-        """
-        scheme, netloc, path, query, frag = urllib_parse.urlsplit(url)
-        if '+' not in scheme:
-            raise ValueError(
-                "Sorry, {!r} is a malformed VCS url. "
-                "The format is <vcs>+<protocol>://<url>, "
-                "e.g. svn+http://myrepo/svn/MyApp#egg=MyApp".format(url)
-            )
-        # Remove the vcs prefix.
-        scheme = scheme.split('+', 1)[1]
-        netloc, user_pass = self.get_netloc_and_auth(netloc, scheme)
-        rev = None
-        if '@' in path:
-            path, rev = path.rsplit('@', 1)
-        url = urllib_parse.urlunsplit((scheme, netloc, path, query, ''))
-        return url, rev, user_pass
-
-    def make_rev_args(self, username, password):
-        """
-        Return the RevOptions "extra arguments" to use in obtain().
-        """
-        return []
-
-    def get_url_rev_options(self, url):
-        # type: (str) -> Tuple[str, RevOptions]
-        """
-        Return the URL and RevOptions object to use in obtain() and in
-        some cases export(), as a tuple (url, rev_options).
-        """
-        url, rev, user_pass = self.get_url_rev_and_auth(url)
-        username, password = user_pass
-        extra_args = self.make_rev_args(username, password)
-        rev_options = self.make_rev_options(rev, extra_args=extra_args)
-
-        return url, rev_options
-
-    def normalize_url(self, url):
-        # type: (str) -> str
-        """
-        Normalize a URL for comparison by unquoting it and removing any
-        trailing slash.
-        """
-        return urllib_parse.unquote(url).rstrip('/')
-
-    def compare_urls(self, url1, url2):
-        # type: (str, str) -> bool
-        """
-        Compare two repo URLs for identity, ignoring incidental differences.
-        """
-        return (self.normalize_url(url1) == self.normalize_url(url2))
-
-    def fetch_new(self, dest, url, rev_options):
-        """
-        Fetch a revision from a repository, in the case that this is the
-        first fetch from the repository.
-
-        Args:
-          dest: the directory to fetch the repository to.
-          rev_options: a RevOptions object.
-        """
-        raise NotImplementedError
-
-    def switch(self, dest, url, rev_options):
-        """
-        Switch the repo at ``dest`` to point to ``URL``.
-
-        Args:
-          rev_options: a RevOptions object.
-        """
-        raise NotImplementedError
-
-    def update(self, dest, url, rev_options):
-        """
-        Update an already-existing repo to the given ``rev_options``.
-
-        Args:
-          rev_options: a RevOptions object.
-        """
-        raise NotImplementedError
-
-    def is_commit_id_equal(self, dest, name):
-        """
-        Return whether the id of the current commit equals the given name.
-
-        Args:
-          dest: the repository directory.
-          name: a string name.
-        """
-        raise NotImplementedError
-
-    def obtain(self, dest):
-        # type: (str) -> None
-        """
-        Install or update in editable mode the package represented by this
-        VersionControl object.
-
-        Args:
-          dest: the repository directory in which to install or update.
-        """
-        url, rev_options = self.get_url_rev_options(self.url)
-
-        if not os.path.exists(dest):
-            self.fetch_new(dest, url, rev_options)
-            return
-
-        rev_display = rev_options.to_display()
-        if self.is_repository_directory(dest):
-            existing_url = self.get_remote_url(dest)
-            if self.compare_urls(existing_url, url):
-                logger.debug(
-                    '%s in %s exists, and has correct URL (%s)',
-                    self.repo_name.title(),
-                    display_path(dest),
-                    url,
-                )
-                if not self.is_commit_id_equal(dest, rev_options.rev):
-                    logger.info(
-                        'Updating %s %s%s',
-                        display_path(dest),
-                        self.repo_name,
-                        rev_display,
-                    )
-                    self.update(dest, url, rev_options)
-                else:
-                    logger.info('Skipping because already up-to-date.')
-                return
-
-            logger.warning(
-                '%s %s in %s exists with URL %s',
-                self.name,
-                self.repo_name,
-                display_path(dest),
-                existing_url,
-            )
-            prompt = ('(s)witch, (i)gnore, (w)ipe, (b)ackup ',
-                      ('s', 'i', 'w', 'b'))
-        else:
-            logger.warning(
-                'Directory %s already exists, and is not a %s %s.',
-                dest,
-                self.name,
-                self.repo_name,
-            )
-            # https://github.com/python/mypy/issues/1174
-            prompt = ('(i)gnore, (w)ipe, (b)ackup ',  # type: ignore
-                      ('i', 'w', 'b'))
-
-        logger.warning(
-            'The plan is to install the %s repository %s',
-            self.name,
-            url,
-        )
-        response = ask_path_exists('What to do?  %s' % prompt[0], prompt[1])
-
-        if response == 'a':
-            sys.exit(-1)
-
-        if response == 'w':
-            logger.warning('Deleting %s', display_path(dest))
-            rmtree(dest)
-            self.fetch_new(dest, url, rev_options)
-            return
-
-        if response == 'b':
-            dest_dir = backup_dir(dest)
-            logger.warning(
-                'Backing up %s to %s', display_path(dest), dest_dir,
-            )
-            shutil.move(dest, dest_dir)
-            self.fetch_new(dest, url, rev_options)
-            return
-
-        # Do nothing if the response is "i".
-        if response == 's':
-            logger.info(
-                'Switching %s %s to %s%s',
-                self.repo_name,
-                display_path(dest),
-                url,
-                rev_display,
-            )
-            self.switch(dest, url, rev_options)
-
-    def unpack(self, location):
-        # type: (str) -> None
-        """
-        Clean up current location and download the url repository
-        (and vcs infos) into location
-        """
-        if os.path.exists(location):
-            rmtree(location)
-        self.obtain(location)
-
-    @classmethod
-    def get_src_requirement(cls, location, project_name):
-        """
-        Return a string representing the requirement needed to
-        redownload the files currently present in location, something
-        like:
-          {repository_url}@{revision}#egg={project_name}-{version_identifier}
-        """
-        raise NotImplementedError
-
-    @classmethod
-    def get_remote_url(cls, location):
-        """
-        Return the url used at location
-
-        Raises RemoteNotFoundError if the repository does not have a remote
-        url configured.
-        """
-        raise NotImplementedError
-
-    @classmethod
-    def get_revision(cls, location):
-        """
-        Return the current commit id of the files at the given location.
-        """
-        raise NotImplementedError
-
-    @classmethod
-    def run_command(
-        cls,
-        cmd,  # type: List[str]
-        show_stdout=True,  # type: bool
-        cwd=None,  # type: Optional[str]
-        on_returncode='raise',  # type: str
-        extra_ok_returncodes=None,  # type: Optional[Iterable[int]]
-        command_desc=None,  # type: Optional[str]
-        extra_environ=None,  # type: Optional[Mapping[str, Any]]
-        spinner=None  # type: Optional[SpinnerInterface]
-    ):
-        # type: (...) -> Optional[Text]
-        """
-        Run a VCS subcommand
-        This is simply a wrapper around call_subprocess that adds the VCS
-        command name, and checks that the VCS is available
-        """
-        cmd = [cls.name] + cmd
-        try:
-            return call_subprocess(cmd, show_stdout, cwd,
-                                   on_returncode=on_returncode,
-                                   extra_ok_returncodes=extra_ok_returncodes,
-                                   command_desc=command_desc,
-                                   extra_environ=extra_environ,
-                                   unset_environ=cls.unset_environ,
-                                   spinner=spinner)
-        except OSError as e:
-            # errno.ENOENT = no such file or directory
-            # In other words, the VCS executable isn't available
-            if e.errno == errno.ENOENT:
-                raise BadCommand(
-                    'Cannot find command %r - do you have '
-                    '%r installed and in your '
-                    'PATH?' % (cls.name, cls.name))
-            else:
-                raise  # re-raise exception if a different error occurred
-
-    @classmethod
-    def is_repository_directory(cls, path):
-        # type: (str) -> bool
-        """
-        Return whether a directory path is a repository directory.
-        """
-        logger.debug('Checking in %s for %s (%s)...',
-                     path, cls.dirname, cls.name)
-        return os.path.exists(os.path.join(path, cls.dirname))
-
-    @classmethod
-    def controls_location(cls, location):
-        # type: (str) -> bool
-        """
-        Check if a location is controlled by the vcs.
-        It is meant to be overridden to implement smarter detection
-        mechanisms for specific vcs.
-
-        This can do more than is_repository_directory() alone.  For example,
-        the Git override checks that Git is actually available.
-        """
-        return cls.is_repository_directory(location)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 96e1d11..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/bazaar.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/bazaar.cpython-37.pyc
deleted file mode 100644
index 1b9c28f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/bazaar.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/git.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/git.cpython-37.pyc
deleted file mode 100644
index ce34c91..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/git.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/mercurial.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/mercurial.cpython-37.pyc
deleted file mode 100644
index 929ae09..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/mercurial.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/subversion.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/subversion.cpython-37.pyc
deleted file mode 100644
index 80e464e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/__pycache__/subversion.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/bazaar.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/bazaar.py
deleted file mode 100644
index 4c6ac79..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/bazaar.py
+++ /dev/null
@@ -1,114 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import os
-
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-
-from pip._internal.download import path_to_url
-from pip._internal.utils.misc import (
-    display_path, make_vcs_requirement_url, rmtree,
-)
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.vcs import VersionControl, vcs
-
-logger = logging.getLogger(__name__)
-
-
-class Bazaar(VersionControl):
-    name = 'bzr'
-    dirname = '.bzr'
-    repo_name = 'branch'
-    schemes = (
-        'bzr', 'bzr+http', 'bzr+https', 'bzr+ssh', 'bzr+sftp', 'bzr+ftp',
-        'bzr+lp',
-    )
-
-    def __init__(self, url=None, *args, **kwargs):
-        super(Bazaar, self).__init__(url, *args, **kwargs)
-        # This is only needed for python <2.7.5
-        # Register lp but do not expose as a scheme to support bzr+lp.
-        if getattr(urllib_parse, 'uses_fragment', None):
-            urllib_parse.uses_fragment.extend(['lp'])
-
-    def get_base_rev_args(self, rev):
-        return ['-r', rev]
-
-    def export(self, location):
-        """
-        Export the Bazaar repository at the url to the destination location
-        """
-        # Remove the location to make sure Bazaar can export it correctly
-        if os.path.exists(location):
-            rmtree(location)
-
-        with TempDirectory(kind="export") as temp_dir:
-            self.unpack(temp_dir.path)
-
-            self.run_command(
-                ['export', location],
-                cwd=temp_dir.path, show_stdout=False,
-            )
-
-    def fetch_new(self, dest, url, rev_options):
-        rev_display = rev_options.to_display()
-        logger.info(
-            'Checking out %s%s to %s',
-            url,
-            rev_display,
-            display_path(dest),
-        )
-        cmd_args = ['branch', '-q'] + rev_options.to_args() + [url, dest]
-        self.run_command(cmd_args)
-
-    def switch(self, dest, url, rev_options):
-        self.run_command(['switch', url], cwd=dest)
-
-    def update(self, dest, url, rev_options):
-        cmd_args = ['pull', '-q'] + rev_options.to_args()
-        self.run_command(cmd_args, cwd=dest)
-
-    def get_url_rev_and_auth(self, url):
-        # hotfix the URL scheme after removing bzr+ from bzr+ssh:// readd it
-        url, rev, user_pass = super(Bazaar, self).get_url_rev_and_auth(url)
-        if url.startswith('ssh://'):
-            url = 'bzr+' + url
-        return url, rev, user_pass
-
-    @classmethod
-    def get_remote_url(cls, location):
-        urls = cls.run_command(['info'], show_stdout=False, cwd=location)
-        for line in urls.splitlines():
-            line = line.strip()
-            for x in ('checkout of branch: ',
-                      'parent branch: '):
-                if line.startswith(x):
-                    repo = line.split(x)[1]
-                    if cls._is_local_repository(repo):
-                        return path_to_url(repo)
-                    return repo
-        return None
-
-    @classmethod
-    def get_revision(cls, location):
-        revision = cls.run_command(
-            ['revno'], show_stdout=False, cwd=location,
-        )
-        return revision.splitlines()[-1]
-
-    @classmethod
-    def get_src_requirement(cls, location, project_name):
-        repo = cls.get_remote_url(location)
-        if not repo:
-            return None
-        if not repo.lower().startswith('bzr:'):
-            repo = 'bzr+' + repo
-        current_rev = cls.get_revision(location)
-        return make_vcs_requirement_url(repo, current_rev, project_name)
-
-    def is_commit_id_equal(self, dest, name):
-        """Always assume the versions don't match"""
-        return False
-
-
-vcs.register(Bazaar)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/git.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/git.py
deleted file mode 100644
index dd2bd61..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/git.py
+++ /dev/null
@@ -1,369 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import os.path
-import re
-
-from pip._vendor.packaging.version import parse as parse_version
-from pip._vendor.six.moves.urllib import parse as urllib_parse
-from pip._vendor.six.moves.urllib import request as urllib_request
-
-from pip._internal.exceptions import BadCommand
-from pip._internal.utils.compat import samefile
-from pip._internal.utils.misc import (
-    display_path, make_vcs_requirement_url, redact_password_from_url,
-)
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.vcs import RemoteNotFoundError, VersionControl, vcs
-
-urlsplit = urllib_parse.urlsplit
-urlunsplit = urllib_parse.urlunsplit
-
-
-logger = logging.getLogger(__name__)
-
-
-HASH_REGEX = re.compile('[a-fA-F0-9]{40}')
-
-
-def looks_like_hash(sha):
-    return bool(HASH_REGEX.match(sha))
-
-
-class Git(VersionControl):
-    name = 'git'
-    dirname = '.git'
-    repo_name = 'clone'
-    schemes = (
-        'git', 'git+http', 'git+https', 'git+ssh', 'git+git', 'git+file',
-    )
-    # Prevent the user's environment variables from interfering with pip:
-    # https://github.com/pypa/pip/issues/1130
-    unset_environ = ('GIT_DIR', 'GIT_WORK_TREE')
-    default_arg_rev = 'HEAD'
-
-    def __init__(self, url=None, *args, **kwargs):
-
-        # Works around an apparent Git bug
-        # (see https://article.gmane.org/gmane.comp.version-control.git/146500)
-        if url:
-            scheme, netloc, path, query, fragment = urlsplit(url)
-            if scheme.endswith('file'):
-                initial_slashes = path[:-len(path.lstrip('/'))]
-                newpath = (
-                    initial_slashes +
-                    urllib_request.url2pathname(path)
-                    .replace('\\', '/').lstrip('/')
-                )
-                url = urlunsplit((scheme, netloc, newpath, query, fragment))
-                after_plus = scheme.find('+') + 1
-                url = scheme[:after_plus] + urlunsplit(
-                    (scheme[after_plus:], netloc, newpath, query, fragment),
-                )
-
-        super(Git, self).__init__(url, *args, **kwargs)
-
-    def get_base_rev_args(self, rev):
-        return [rev]
-
-    def get_git_version(self):
-        VERSION_PFX = 'git version '
-        version = self.run_command(['version'], show_stdout=False)
-        if version.startswith(VERSION_PFX):
-            version = version[len(VERSION_PFX):].split()[0]
-        else:
-            version = ''
-        # get first 3 positions of the git version becasue
-        # on windows it is x.y.z.windows.t, and this parses as
-        # LegacyVersion which always smaller than a Version.
-        version = '.'.join(version.split('.')[:3])
-        return parse_version(version)
-
-    def get_current_branch(self, location):
-        """
-        Return the current branch, or None if HEAD isn't at a branch
-        (e.g. detached HEAD).
-        """
-        # git-symbolic-ref exits with empty stdout if "HEAD" is a detached
-        # HEAD rather than a symbolic ref.  In addition, the -q causes the
-        # command to exit with status code 1 instead of 128 in this case
-        # and to suppress the message to stderr.
-        args = ['symbolic-ref', '-q', 'HEAD']
-        output = self.run_command(
-            args, extra_ok_returncodes=(1, ), show_stdout=False, cwd=location,
-        )
-        ref = output.strip()
-
-        if ref.startswith('refs/heads/'):
-            return ref[len('refs/heads/'):]
-
-        return None
-
-    def export(self, location):
-        """Export the Git repository at the url to the destination location"""
-        if not location.endswith('/'):
-            location = location + '/'
-
-        with TempDirectory(kind="export") as temp_dir:
-            self.unpack(temp_dir.path)
-            self.run_command(
-                ['checkout-index', '-a', '-f', '--prefix', location],
-                show_stdout=False, cwd=temp_dir.path
-            )
-
-    def get_revision_sha(self, dest, rev):
-        """
-        Return (sha_or_none, is_branch), where sha_or_none is a commit hash
-        if the revision names a remote branch or tag, otherwise None.
-
-        Args:
-          dest: the repository directory.
-          rev: the revision name.
-        """
-        # Pass rev to pre-filter the list.
-        output = self.run_command(['show-ref', rev], cwd=dest,
-                                  show_stdout=False, on_returncode='ignore')
-        refs = {}
-        for line in output.strip().splitlines():
-            try:
-                sha, ref = line.split()
-            except ValueError:
-                # Include the offending line to simplify troubleshooting if
-                # this error ever occurs.
-                raise ValueError('unexpected show-ref line: {!r}'.format(line))
-
-            refs[ref] = sha
-
-        branch_ref = 'refs/remotes/origin/{}'.format(rev)
-        tag_ref = 'refs/tags/{}'.format(rev)
-
-        sha = refs.get(branch_ref)
-        if sha is not None:
-            return (sha, True)
-
-        sha = refs.get(tag_ref)
-
-        return (sha, False)
-
-    def resolve_revision(self, dest, url, rev_options):
-        """
-        Resolve a revision to a new RevOptions object with the SHA1 of the
-        branch, tag, or ref if found.
-
-        Args:
-          rev_options: a RevOptions object.
-        """
-        rev = rev_options.arg_rev
-        sha, is_branch = self.get_revision_sha(dest, rev)
-
-        if sha is not None:
-            rev_options = rev_options.make_new(sha)
-            rev_options.branch_name = rev if is_branch else None
-
-            return rev_options
-
-        # Do not show a warning for the common case of something that has
-        # the form of a Git commit hash.
-        if not looks_like_hash(rev):
-            logger.warning(
-                "Did not find branch or tag '%s', assuming revision or ref.",
-                rev,
-            )
-
-        if not rev.startswith('refs/'):
-            return rev_options
-
-        # If it looks like a ref, we have to fetch it explicitly.
-        self.run_command(
-            ['fetch', '-q', url] + rev_options.to_args(),
-            cwd=dest,
-        )
-        # Change the revision to the SHA of the ref we fetched
-        sha = self.get_revision(dest, rev='FETCH_HEAD')
-        rev_options = rev_options.make_new(sha)
-
-        return rev_options
-
-    def is_commit_id_equal(self, dest, name):
-        """
-        Return whether the current commit hash equals the given name.
-
-        Args:
-          dest: the repository directory.
-          name: a string name.
-        """
-        if not name:
-            # Then avoid an unnecessary subprocess call.
-            return False
-
-        return self.get_revision(dest) == name
-
-    def fetch_new(self, dest, url, rev_options):
-        rev_display = rev_options.to_display()
-        logger.info(
-            'Cloning %s%s to %s', redact_password_from_url(url),
-            rev_display, display_path(dest),
-        )
-        self.run_command(['clone', '-q', url, dest])
-
-        if rev_options.rev:
-            # Then a specific revision was requested.
-            rev_options = self.resolve_revision(dest, url, rev_options)
-            branch_name = getattr(rev_options, 'branch_name', None)
-            if branch_name is None:
-                # Only do a checkout if the current commit id doesn't match
-                # the requested revision.
-                if not self.is_commit_id_equal(dest, rev_options.rev):
-                    cmd_args = ['checkout', '-q'] + rev_options.to_args()
-                    self.run_command(cmd_args, cwd=dest)
-            elif self.get_current_branch(dest) != branch_name:
-                # Then a specific branch was requested, and that branch
-                # is not yet checked out.
-                track_branch = 'origin/{}'.format(branch_name)
-                cmd_args = [
-                    'checkout', '-b', branch_name, '--track', track_branch,
-                ]
-                self.run_command(cmd_args, cwd=dest)
-
-        #: repo may contain submodules
-        self.update_submodules(dest)
-
-    def switch(self, dest, url, rev_options):
-        self.run_command(['config', 'remote.origin.url', url], cwd=dest)
-        cmd_args = ['checkout', '-q'] + rev_options.to_args()
-        self.run_command(cmd_args, cwd=dest)
-
-        self.update_submodules(dest)
-
-    def update(self, dest, url, rev_options):
-        # First fetch changes from the default remote
-        if self.get_git_version() >= parse_version('1.9.0'):
-            # fetch tags in addition to everything else
-            self.run_command(['fetch', '-q', '--tags'], cwd=dest)
-        else:
-            self.run_command(['fetch', '-q'], cwd=dest)
-        # Then reset to wanted revision (maybe even origin/master)
-        rev_options = self.resolve_revision(dest, url, rev_options)
-        cmd_args = ['reset', '--hard', '-q'] + rev_options.to_args()
-        self.run_command(cmd_args, cwd=dest)
-        #: update submodules
-        self.update_submodules(dest)
-
-    @classmethod
-    def get_remote_url(cls, location):
-        """
-        Return URL of the first remote encountered.
-
-        Raises RemoteNotFoundError if the repository does not have a remote
-        url configured.
-        """
-        # We need to pass 1 for extra_ok_returncodes since the command
-        # exits with return code 1 if there are no matching lines.
-        stdout = cls.run_command(
-            ['config', '--get-regexp', r'remote\..*\.url'],
-            extra_ok_returncodes=(1, ), show_stdout=False, cwd=location,
-        )
-        remotes = stdout.splitlines()
-        try:
-            found_remote = remotes[0]
-        except IndexError:
-            raise RemoteNotFoundError
-
-        for remote in remotes:
-            if remote.startswith('remote.origin.url '):
-                found_remote = remote
-                break
-        url = found_remote.split(' ')[1]
-        return url.strip()
-
-    @classmethod
-    def get_revision(cls, location, rev=None):
-        if rev is None:
-            rev = 'HEAD'
-        current_rev = cls.run_command(
-            ['rev-parse', rev], show_stdout=False, cwd=location,
-        )
-        return current_rev.strip()
-
-    @classmethod
-    def _get_subdirectory(cls, location):
-        """Return the relative path of setup.py to the git repo root."""
-        # find the repo root
-        git_dir = cls.run_command(['rev-parse', '--git-dir'],
-                                  show_stdout=False, cwd=location).strip()
-        if not os.path.isabs(git_dir):
-            git_dir = os.path.join(location, git_dir)
-        root_dir = os.path.join(git_dir, '..')
-        # find setup.py
-        orig_location = location
-        while not os.path.exists(os.path.join(location, 'setup.py')):
-            last_location = location
-            location = os.path.dirname(location)
-            if location == last_location:
-                # We've traversed up to the root of the filesystem without
-                # finding setup.py
-                logger.warning(
-                    "Could not find setup.py for directory %s (tried all "
-                    "parent directories)",
-                    orig_location,
-                )
-                return None
-        # relative path of setup.py to repo root
-        if samefile(root_dir, location):
-            return None
-        return os.path.relpath(location, root_dir)
-
-    @classmethod
-    def get_src_requirement(cls, location, project_name):
-        repo = cls.get_remote_url(location)
-        if not repo.lower().startswith('git:'):
-            repo = 'git+' + repo
-        current_rev = cls.get_revision(location)
-        subdir = cls._get_subdirectory(location)
-        req = make_vcs_requirement_url(repo, current_rev, project_name,
-                                       subdir=subdir)
-
-        return req
-
-    def get_url_rev_and_auth(self, url):
-        """
-        Prefixes stub URLs like 'user@hostname:user/repo.git' with 'ssh://'.
-        That's required because although they use SSH they sometimes don't
-        work with a ssh:// scheme (e.g. GitHub). But we need a scheme for
-        parsing. Hence we remove it again afterwards and return it as a stub.
-        """
-        if '://' not in url:
-            assert 'file:' not in url
-            url = url.replace('git+', 'git+ssh://')
-            url, rev, user_pass = super(Git, self).get_url_rev_and_auth(url)
-            url = url.replace('ssh://', '')
-        else:
-            url, rev, user_pass = super(Git, self).get_url_rev_and_auth(url)
-
-        return url, rev, user_pass
-
-    def update_submodules(self, location):
-        if not os.path.exists(os.path.join(location, '.gitmodules')):
-            return
-        self.run_command(
-            ['submodule', 'update', '--init', '--recursive', '-q'],
-            cwd=location,
-        )
-
-    @classmethod
-    def controls_location(cls, location):
-        if super(Git, cls).controls_location(location):
-            return True
-        try:
-            r = cls.run_command(['rev-parse'],
-                                cwd=location,
-                                show_stdout=False,
-                                on_returncode='ignore')
-            return not r
-        except BadCommand:
-            logger.debug("could not determine if %s is under git control "
-                         "because git is not available", location)
-            return False
-
-
-vcs.register(Git)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/mercurial.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/mercurial.py
deleted file mode 100644
index 26e75de..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/mercurial.py
+++ /dev/null
@@ -1,103 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import os
-
-from pip._vendor.six.moves import configparser
-
-from pip._internal.download import path_to_url
-from pip._internal.utils.misc import display_path, make_vcs_requirement_url
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.vcs import VersionControl, vcs
-
-logger = logging.getLogger(__name__)
-
-
-class Mercurial(VersionControl):
-    name = 'hg'
-    dirname = '.hg'
-    repo_name = 'clone'
-    schemes = ('hg', 'hg+http', 'hg+https', 'hg+ssh', 'hg+static-http')
-
-    def get_base_rev_args(self, rev):
-        return [rev]
-
-    def export(self, location):
-        """Export the Hg repository at the url to the destination location"""
-        with TempDirectory(kind="export") as temp_dir:
-            self.unpack(temp_dir.path)
-
-            self.run_command(
-                ['archive', location], show_stdout=False, cwd=temp_dir.path
-            )
-
-    def fetch_new(self, dest, url, rev_options):
-        rev_display = rev_options.to_display()
-        logger.info(
-            'Cloning hg %s%s to %s',
-            url,
-            rev_display,
-            display_path(dest),
-        )
-        self.run_command(['clone', '--noupdate', '-q', url, dest])
-        cmd_args = ['update', '-q'] + rev_options.to_args()
-        self.run_command(cmd_args, cwd=dest)
-
-    def switch(self, dest, url, rev_options):
-        repo_config = os.path.join(dest, self.dirname, 'hgrc')
-        config = configparser.SafeConfigParser()
-        try:
-            config.read(repo_config)
-            config.set('paths', 'default', url)
-            with open(repo_config, 'w') as config_file:
-                config.write(config_file)
-        except (OSError, configparser.NoSectionError) as exc:
-            logger.warning(
-                'Could not switch Mercurial repository to %s: %s', url, exc,
-            )
-        else:
-            cmd_args = ['update', '-q'] + rev_options.to_args()
-            self.run_command(cmd_args, cwd=dest)
-
-    def update(self, dest, url, rev_options):
-        self.run_command(['pull', '-q'], cwd=dest)
-        cmd_args = ['update', '-q'] + rev_options.to_args()
-        self.run_command(cmd_args, cwd=dest)
-
-    @classmethod
-    def get_remote_url(cls, location):
-        url = cls.run_command(
-            ['showconfig', 'paths.default'],
-            show_stdout=False, cwd=location).strip()
-        if cls._is_local_repository(url):
-            url = path_to_url(url)
-        return url.strip()
-
-    @classmethod
-    def get_revision(cls, location):
-        current_revision = cls.run_command(
-            ['parents', '--template={rev}'],
-            show_stdout=False, cwd=location).strip()
-        return current_revision
-
-    @classmethod
-    def get_revision_hash(cls, location):
-        current_rev_hash = cls.run_command(
-            ['parents', '--template={node}'],
-            show_stdout=False, cwd=location).strip()
-        return current_rev_hash
-
-    @classmethod
-    def get_src_requirement(cls, location, project_name):
-        repo = cls.get_remote_url(location)
-        if not repo.lower().startswith('hg:'):
-            repo = 'hg+' + repo
-        current_rev_hash = cls.get_revision_hash(location)
-        return make_vcs_requirement_url(repo, current_rev_hash, project_name)
-
-    def is_commit_id_equal(self, dest, name):
-        """Always assume the versions don't match"""
-        return False
-
-
-vcs.register(Mercurial)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/subversion.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/subversion.py
deleted file mode 100644
index 42ac5ac..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/vcs/subversion.py
+++ /dev/null
@@ -1,200 +0,0 @@
-from __future__ import absolute_import
-
-import logging
-import os
-import re
-
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import (
-    display_path, make_vcs_requirement_url, rmtree, split_auth_from_netloc,
-)
-from pip._internal.vcs import VersionControl, vcs
-
-_svn_xml_url_re = re.compile('url="([^"]+)"')
-_svn_rev_re = re.compile(r'committed-rev="(\d+)"')
-_svn_info_xml_rev_re = re.compile(r'\s*revision="(\d+)"')
-_svn_info_xml_url_re = re.compile(r'<url>(.*)</url>')
-
-
-logger = logging.getLogger(__name__)
-
-
-class Subversion(VersionControl):
-    name = 'svn'
-    dirname = '.svn'
-    repo_name = 'checkout'
-    schemes = ('svn', 'svn+ssh', 'svn+http', 'svn+https', 'svn+svn')
-
-    def get_base_rev_args(self, rev):
-        return ['-r', rev]
-
-    def export(self, location):
-        """Export the svn repository at the url to the destination location"""
-        url, rev_options = self.get_url_rev_options(self.url)
-
-        logger.info('Exporting svn repository %s to %s', url, location)
-        with indent_log():
-            if os.path.exists(location):
-                # Subversion doesn't like to check out over an existing
-                # directory --force fixes this, but was only added in svn 1.5
-                rmtree(location)
-            cmd_args = ['export'] + rev_options.to_args() + [url, location]
-            self.run_command(cmd_args, show_stdout=False)
-
-    def fetch_new(self, dest, url, rev_options):
-        rev_display = rev_options.to_display()
-        logger.info(
-            'Checking out %s%s to %s',
-            url,
-            rev_display,
-            display_path(dest),
-        )
-        cmd_args = ['checkout', '-q'] + rev_options.to_args() + [url, dest]
-        self.run_command(cmd_args)
-
-    def switch(self, dest, url, rev_options):
-        cmd_args = ['switch'] + rev_options.to_args() + [url, dest]
-        self.run_command(cmd_args)
-
-    def update(self, dest, url, rev_options):
-        cmd_args = ['update'] + rev_options.to_args() + [dest]
-        self.run_command(cmd_args)
-
-    @classmethod
-    def get_revision(cls, location):
-        """
-        Return the maximum revision for all files under a given location
-        """
-        # Note: taken from setuptools.command.egg_info
-        revision = 0
-
-        for base, dirs, files in os.walk(location):
-            if cls.dirname not in dirs:
-                dirs[:] = []
-                continue    # no sense walking uncontrolled subdirs
-            dirs.remove(cls.dirname)
-            entries_fn = os.path.join(base, cls.dirname, 'entries')
-            if not os.path.exists(entries_fn):
-                # FIXME: should we warn?
-                continue
-
-            dirurl, localrev = cls._get_svn_url_rev(base)
-
-            if base == location:
-                base = dirurl + '/'   # save the root url
-            elif not dirurl or not dirurl.startswith(base):
-                dirs[:] = []
-                continue    # not part of the same svn tree, skip it
-            revision = max(revision, localrev)
-        return revision
-
-    def get_netloc_and_auth(self, netloc, scheme):
-        """
-        This override allows the auth information to be passed to svn via the
-        --username and --password options instead of via the URL.
-        """
-        if scheme == 'ssh':
-            # The --username and --password options can't be used for
-            # svn+ssh URLs, so keep the auth information in the URL.
-            return super(Subversion, self).get_netloc_and_auth(
-                netloc, scheme)
-
-        return split_auth_from_netloc(netloc)
-
-    def get_url_rev_and_auth(self, url):
-        # hotfix the URL scheme after removing svn+ from svn+ssh:// readd it
-        url, rev, user_pass = super(Subversion, self).get_url_rev_and_auth(url)
-        if url.startswith('ssh://'):
-            url = 'svn+' + url
-        return url, rev, user_pass
-
-    def make_rev_args(self, username, password):
-        extra_args = []
-        if username:
-            extra_args += ['--username', username]
-        if password:
-            extra_args += ['--password', password]
-
-        return extra_args
-
-    @classmethod
-    def get_remote_url(cls, location):
-        # In cases where the source is in a subdirectory, not alongside
-        # setup.py we have to look up in the location until we find a real
-        # setup.py
-        orig_location = location
-        while not os.path.exists(os.path.join(location, 'setup.py')):
-            last_location = location
-            location = os.path.dirname(location)
-            if location == last_location:
-                # We've traversed up to the root of the filesystem without
-                # finding setup.py
-                logger.warning(
-                    "Could not find setup.py for directory %s (tried all "
-                    "parent directories)",
-                    orig_location,
-                )
-                return None
-
-        return cls._get_svn_url_rev(location)[0]
-
-    @classmethod
-    def _get_svn_url_rev(cls, location):
-        from pip._internal.exceptions import InstallationError
-
-        entries_path = os.path.join(location, cls.dirname, 'entries')
-        if os.path.exists(entries_path):
-            with open(entries_path) as f:
-                data = f.read()
-        else:  # subversion >= 1.7 does not have the 'entries' file
-            data = ''
-
-        if (data.startswith('8') or
-                data.startswith('9') or
-                data.startswith('10')):
-            data = list(map(str.splitlines, data.split('\n\x0c\n')))
-            del data[0][0]  # get rid of the '8'
-            url = data[0][3]
-            revs = [int(d[9]) for d in data if len(d) > 9 and d[9]] + [0]
-        elif data.startswith('<?xml'):
-            match = _svn_xml_url_re.search(data)
-            if not match:
-                raise ValueError('Badly formatted data: %r' % data)
-            url = match.group(1)    # get repository URL
-            revs = [int(m.group(1)) for m in _svn_rev_re.finditer(data)] + [0]
-        else:
-            try:
-                # subversion >= 1.7
-                xml = cls.run_command(
-                    ['info', '--xml', location],
-                    show_stdout=False,
-                )
-                url = _svn_info_xml_url_re.search(xml).group(1)
-                revs = [
-                    int(m.group(1)) for m in _svn_info_xml_rev_re.finditer(xml)
-                ]
-            except InstallationError:
-                url, revs = None, []
-
-        if revs:
-            rev = max(revs)
-        else:
-            rev = 0
-
-        return url, rev
-
-    @classmethod
-    def get_src_requirement(cls, location, project_name):
-        repo = cls.get_remote_url(location)
-        if repo is None:
-            return None
-        repo = 'svn+' + repo
-        rev = cls.get_revision(location)
-        return make_vcs_requirement_url(repo, rev, project_name)
-
-    def is_commit_id_equal(self, dest, name):
-        """Always assume the versions don't match"""
-        return False
-
-
-vcs.register(Subversion)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/wheel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/wheel.py
deleted file mode 100644
index 67bcc7f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_internal/wheel.py
+++ /dev/null
@@ -1,1095 +0,0 @@
-"""
-Support for installing and building the "wheel" binary package format.
-"""
-from __future__ import absolute_import
-
-import collections
-import compileall
-import csv
-import hashlib
-import logging
-import os.path
-import re
-import shutil
-import stat
-import sys
-import warnings
-from base64 import urlsafe_b64encode
-from email.parser import Parser
-
-from pip._vendor import pkg_resources
-from pip._vendor.distlib.scripts import ScriptMaker
-from pip._vendor.packaging.utils import canonicalize_name
-from pip._vendor.six import StringIO
-
-from pip._internal import pep425tags
-from pip._internal.download import path_to_url, unpack_url
-from pip._internal.exceptions import (
-    InstallationError, InvalidWheelFilename, UnsupportedWheel,
-)
-from pip._internal.locations import (
-    PIP_DELETE_MARKER_FILENAME, distutils_scheme,
-)
-from pip._internal.models.link import Link
-from pip._internal.utils.logging import indent_log
-from pip._internal.utils.misc import (
-    call_subprocess, captured_stdout, ensure_dir, read_chunks,
-)
-from pip._internal.utils.setuptools_build import SETUPTOOLS_SHIM
-from pip._internal.utils.temp_dir import TempDirectory
-from pip._internal.utils.typing import MYPY_CHECK_RUNNING
-from pip._internal.utils.ui import open_spinner
-
-if MYPY_CHECK_RUNNING:
-    from typing import (  # noqa: F401
-        Dict, List, Optional, Sequence, Mapping, Tuple, IO, Text, Any,
-        Union, Iterable
-    )
-    from pip._vendor.packaging.requirements import Requirement  # noqa: F401
-    from pip._internal.req.req_install import InstallRequirement  # noqa: F401
-    from pip._internal.download import PipSession  # noqa: F401
-    from pip._internal.index import FormatControl, PackageFinder  # noqa: F401
-    from pip._internal.operations.prepare import (  # noqa: F401
-        RequirementPreparer
-    )
-    from pip._internal.cache import WheelCache  # noqa: F401
-    from pip._internal.pep425tags import Pep425Tag  # noqa: F401
-
-    InstalledCSVRow = Tuple[str, ...]
-
-
-VERSION_COMPATIBLE = (1, 0)
-
-
-logger = logging.getLogger(__name__)
-
-
-def normpath(src, p):
-    return os.path.relpath(src, p).replace(os.path.sep, '/')
-
-
-def rehash(path, blocksize=1 << 20):
-    # type: (str, int) -> Tuple[str, str]
-    """Return (hash, length) for path using hashlib.sha256()"""
-    h = hashlib.sha256()
-    length = 0
-    with open(path, 'rb') as f:
-        for block in read_chunks(f, size=blocksize):
-            length += len(block)
-            h.update(block)
-    digest = 'sha256=' + urlsafe_b64encode(
-        h.digest()
-    ).decode('latin1').rstrip('=')
-    # unicode/str python2 issues
-    return (digest, str(length))  # type: ignore
-
-
-def open_for_csv(name, mode):
-    # type: (str, Text) -> IO
-    if sys.version_info[0] < 3:
-        nl = {}  # type: Dict[str, Any]
-        bin = 'b'
-    else:
-        nl = {'newline': ''}  # type: Dict[str, Any]
-        bin = ''
-    return open(name, mode + bin, **nl)
-
-
-def replace_python_tag(wheelname, new_tag):
-    # type: (str, str) -> str
-    """Replace the Python tag in a wheel file name with a new value.
-    """
-    parts = wheelname.split('-')
-    parts[-3] = new_tag
-    return '-'.join(parts)
-
-
-def fix_script(path):
-    # type: (str) -> Optional[bool]
-    """Replace #!python with #!/path/to/python
-    Return True if file was changed."""
-    # XXX RECORD hashes will need to be updated
-    if os.path.isfile(path):
-        with open(path, 'rb') as script:
-            firstline = script.readline()
-            if not firstline.startswith(b'#!python'):
-                return False
-            exename = sys.executable.encode(sys.getfilesystemencoding())
-            firstline = b'#!' + exename + os.linesep.encode("ascii")
-            rest = script.read()
-        with open(path, 'wb') as script:
-            script.write(firstline)
-            script.write(rest)
-        return True
-    return None
-
-
-dist_info_re = re.compile(r"""^(?P<namever>(?P<name>.+?)(-(?P<ver>.+?))?)
-                                \.dist-info$""", re.VERBOSE)
-
-
-def root_is_purelib(name, wheeldir):
-    # type: (str, str) -> bool
-    """
-    Return True if the extracted wheel in wheeldir should go into purelib.
-    """
-    name_folded = name.replace("-", "_")
-    for item in os.listdir(wheeldir):
-        match = dist_info_re.match(item)
-        if match and match.group('name') == name_folded:
-            with open(os.path.join(wheeldir, item, 'WHEEL')) as wheel:
-                for line in wheel:
-                    line = line.lower().rstrip()
-                    if line == "root-is-purelib: true":
-                        return True
-    return False
-
-
-def get_entrypoints(filename):
-    # type: (str) -> Tuple[Dict[str, str], Dict[str, str]]
-    if not os.path.exists(filename):
-        return {}, {}
-
-    # This is done because you can pass a string to entry_points wrappers which
-    # means that they may or may not be valid INI files. The attempt here is to
-    # strip leading and trailing whitespace in order to make them valid INI
-    # files.
-    with open(filename) as fp:
-        data = StringIO()
-        for line in fp:
-            data.write(line.strip())
-            data.write("\n")
-        data.seek(0)
-
-    # get the entry points and then the script names
-    entry_points = pkg_resources.EntryPoint.parse_map(data)
-    console = entry_points.get('console_scripts', {})
-    gui = entry_points.get('gui_scripts', {})
-
-    def _split_ep(s):
-        """get the string representation of EntryPoint, remove space and split
-        on '='"""
-        return str(s).replace(" ", "").split("=")
-
-    # convert the EntryPoint objects into strings with module:function
-    console = dict(_split_ep(v) for v in console.values())
-    gui = dict(_split_ep(v) for v in gui.values())
-    return console, gui
-
-
-def message_about_scripts_not_on_PATH(scripts):
-    # type: (Sequence[str]) -> Optional[str]
-    """Determine if any scripts are not on PATH and format a warning.
-
-    Returns a warning message if one or more scripts are not on PATH,
-    otherwise None.
-    """
-    if not scripts:
-        return None
-
-    # Group scripts by the path they were installed in
-    grouped_by_dir = collections.defaultdict(set)  # type: Dict[str, set]
-    for destfile in scripts:
-        parent_dir = os.path.dirname(destfile)
-        script_name = os.path.basename(destfile)
-        grouped_by_dir[parent_dir].add(script_name)
-
-    # We don't want to warn for directories that are on PATH.
-    not_warn_dirs = [
-        os.path.normcase(i).rstrip(os.sep) for i in
-        os.environ.get("PATH", "").split(os.pathsep)
-    ]
-    # If an executable sits with sys.executable, we don't warn for it.
-    #     This covers the case of venv invocations without activating the venv.
-    not_warn_dirs.append(os.path.normcase(os.path.dirname(sys.executable)))
-    warn_for = {
-        parent_dir: scripts for parent_dir, scripts in grouped_by_dir.items()
-        if os.path.normcase(parent_dir) not in not_warn_dirs
-    }
-    if not warn_for:
-        return None
-
-    # Format a message
-    msg_lines = []
-    for parent_dir, scripts in warn_for.items():
-        scripts = sorted(scripts)
-        if len(scripts) == 1:
-            start_text = "script {} is".format(scripts[0])
-        else:
-            start_text = "scripts {} are".format(
-                ", ".join(scripts[:-1]) + " and " + scripts[-1]
-            )
-
-        msg_lines.append(
-            "The {} installed in '{}' which is not on PATH."
-            .format(start_text, parent_dir)
-        )
-
-    last_line_fmt = (
-        "Consider adding {} to PATH or, if you prefer "
-        "to suppress this warning, use --no-warn-script-location."
-    )
-    if len(msg_lines) == 1:
-        msg_lines.append(last_line_fmt.format("this directory"))
-    else:
-        msg_lines.append(last_line_fmt.format("these directories"))
-
-    # Returns the formatted multiline message
-    return "\n".join(msg_lines)
-
-
-def sorted_outrows(outrows):
-    # type: (Iterable[InstalledCSVRow]) -> List[InstalledCSVRow]
-    """
-    Return the given rows of a RECORD file in sorted order.
-
-    Each row is a 3-tuple (path, hash, size) and corresponds to a record of
-    a RECORD file (see PEP 376 and PEP 427 for details).  For the rows
-    passed to this function, the size can be an integer as an int or string,
-    or the empty string.
-    """
-    # Normally, there should only be one row per path, in which case the
-    # second and third elements don't come into play when sorting.
-    # However, in cases in the wild where a path might happen to occur twice,
-    # we don't want the sort operation to trigger an error (but still want
-    # determinism).  Since the third element can be an int or string, we
-    # coerce each element to a string to avoid a TypeError in this case.
-    # For additional background, see--
-    # https://github.com/pypa/pip/issues/5868
-    return sorted(outrows, key=lambda row: tuple(str(x) for x in row))
-
-
-def get_csv_rows_for_installed(
-    old_csv_rows,  # type: Iterable[List[str]]
-    installed,  # type: Dict[str, str]
-    changed,  # type: set
-    generated,  # type: List[str]
-    lib_dir,  # type: str
-):
-    # type: (...) -> List[InstalledCSVRow]
-    """
-    :param installed: A map from archive RECORD path to installation RECORD
-        path.
-    """
-    installed_rows = []  # type: List[InstalledCSVRow]
-    for row in old_csv_rows:
-        if len(row) > 3:
-            logger.warning(
-                'RECORD line has more than three elements: {}'.format(row)
-            )
-        # Make a copy because we are mutating the row.
-        row = list(row)
-        old_path = row[0]
-        new_path = installed.pop(old_path, old_path)
-        row[0] = new_path
-        if new_path in changed:
-            digest, length = rehash(new_path)
-            row[1] = digest
-            row[2] = length
-        installed_rows.append(tuple(row))
-    for f in generated:
-        digest, length = rehash(f)
-        installed_rows.append((normpath(f, lib_dir), digest, str(length)))
-    for f in installed:
-        installed_rows.append((installed[f], '', ''))
-    return installed_rows
-
-
-def move_wheel_files(
-    name,  # type: str
-    req,  # type: Requirement
-    wheeldir,  # type: str
-    user=False,  # type: bool
-    home=None,  # type: Optional[str]
-    root=None,  # type: Optional[str]
-    pycompile=True,  # type: bool
-    scheme=None,  # type: Optional[Mapping[str, str]]
-    isolated=False,  # type: bool
-    prefix=None,  # type: Optional[str]
-    warn_script_location=True  # type: bool
-):
-    # type: (...) -> None
-    """Install a wheel"""
-    # TODO: Investigate and break this up.
-    # TODO: Look into moving this into a dedicated class for representing an
-    #       installation.
-
-    if not scheme:
-        scheme = distutils_scheme(
-            name, user=user, home=home, root=root, isolated=isolated,
-            prefix=prefix,
-        )
-
-    if root_is_purelib(name, wheeldir):
-        lib_dir = scheme['purelib']
-    else:
-        lib_dir = scheme['platlib']
-
-    info_dir = []  # type: List[str]
-    data_dirs = []
-    source = wheeldir.rstrip(os.path.sep) + os.path.sep
-
-    # Record details of the files moved
-    #   installed = files copied from the wheel to the destination
-    #   changed = files changed while installing (scripts #! line typically)
-    #   generated = files newly generated during the install (script wrappers)
-    installed = {}  # type: Dict[str, str]
-    changed = set()
-    generated = []  # type: List[str]
-
-    # Compile all of the pyc files that we're going to be installing
-    if pycompile:
-        with captured_stdout() as stdout:
-            with warnings.catch_warnings():
-                warnings.filterwarnings('ignore')
-                compileall.compile_dir(source, force=True, quiet=True)
-        logger.debug(stdout.getvalue())
-
-    def record_installed(srcfile, destfile, modified=False):
-        """Map archive RECORD paths to installation RECORD paths."""
-        oldpath = normpath(srcfile, wheeldir)
-        newpath = normpath(destfile, lib_dir)
-        installed[oldpath] = newpath
-        if modified:
-            changed.add(destfile)
-
-    def clobber(source, dest, is_base, fixer=None, filter=None):
-        ensure_dir(dest)  # common for the 'include' path
-
-        for dir, subdirs, files in os.walk(source):
-            basedir = dir[len(source):].lstrip(os.path.sep)
-            destdir = os.path.join(dest, basedir)
-            if is_base and basedir.split(os.path.sep, 1)[0].endswith('.data'):
-                continue
-            for s in subdirs:
-                destsubdir = os.path.join(dest, basedir, s)
-                if is_base and basedir == '' and destsubdir.endswith('.data'):
-                    data_dirs.append(s)
-                    continue
-                elif (is_base and
-                        s.endswith('.dist-info') and
-                        canonicalize_name(s).startswith(
-                            canonicalize_name(req.name))):
-                    assert not info_dir, ('Multiple .dist-info directories: ' +
-                                          destsubdir + ', ' +
-                                          ', '.join(info_dir))
-                    info_dir.append(destsubdir)
-            for f in files:
-                # Skip unwanted files
-                if filter and filter(f):
-                    continue
-                srcfile = os.path.join(dir, f)
-                destfile = os.path.join(dest, basedir, f)
-                # directory creation is lazy and after the file filtering above
-                # to ensure we don't install empty dirs; empty dirs can't be
-                # uninstalled.
-                ensure_dir(destdir)
-
-                # copyfile (called below) truncates the destination if it
-                # exists and then writes the new contents. This is fine in most
-                # cases, but can cause a segfault if pip has loaded a shared
-                # object (e.g. from pyopenssl through its vendored urllib3)
-                # Since the shared object is mmap'd an attempt to call a
-                # symbol in it will then cause a segfault. Unlinking the file
-                # allows writing of new contents while allowing the process to
-                # continue to use the old copy.
-                if os.path.exists(destfile):
-                    os.unlink(destfile)
-
-                # We use copyfile (not move, copy, or copy2) to be extra sure
-                # that we are not moving directories over (copyfile fails for
-                # directories) as well as to ensure that we are not copying
-                # over any metadata because we want more control over what
-                # metadata we actually copy over.
-                shutil.copyfile(srcfile, destfile)
-
-                # Copy over the metadata for the file, currently this only
-                # includes the atime and mtime.
-                st = os.stat(srcfile)
-                if hasattr(os, "utime"):
-                    os.utime(destfile, (st.st_atime, st.st_mtime))
-
-                # If our file is executable, then make our destination file
-                # executable.
-                if os.access(srcfile, os.X_OK):
-                    st = os.stat(srcfile)
-                    permissions = (
-                        st.st_mode | stat.S_IXUSR | stat.S_IXGRP | stat.S_IXOTH
-                    )
-                    os.chmod(destfile, permissions)
-
-                changed = False
-                if fixer:
-                    changed = fixer(destfile)
-                record_installed(srcfile, destfile, changed)
-
-    clobber(source, lib_dir, True)
-
-    assert info_dir, "%s .dist-info directory not found" % req
-
-    # Get the defined entry points
-    ep_file = os.path.join(info_dir[0], 'entry_points.txt')
-    console, gui = get_entrypoints(ep_file)
-
-    def is_entrypoint_wrapper(name):
-        # EP, EP.exe and EP-script.py are scripts generated for
-        # entry point EP by setuptools
-        if name.lower().endswith('.exe'):
-            matchname = name[:-4]
-        elif name.lower().endswith('-script.py'):
-            matchname = name[:-10]
-        elif name.lower().endswith(".pya"):
-            matchname = name[:-4]
-        else:
-            matchname = name
-        # Ignore setuptools-generated scripts
-        return (matchname in console or matchname in gui)
-
-    for datadir in data_dirs:
-        fixer = None
-        filter = None
-        for subdir in os.listdir(os.path.join(wheeldir, datadir)):
-            fixer = None
-            if subdir == 'scripts':
-                fixer = fix_script
-                filter = is_entrypoint_wrapper
-            source = os.path.join(wheeldir, datadir, subdir)
-            dest = scheme[subdir]
-            clobber(source, dest, False, fixer=fixer, filter=filter)
-
-    maker = ScriptMaker(None, scheme['scripts'])
-
-    # Ensure old scripts are overwritten.
-    # See https://github.com/pypa/pip/issues/1800
-    maker.clobber = True
-
-    # Ensure we don't generate any variants for scripts because this is almost
-    # never what somebody wants.
-    # See https://bitbucket.org/pypa/distlib/issue/35/
-    maker.variants = {''}
-
-    # This is required because otherwise distlib creates scripts that are not
-    # executable.
-    # See https://bitbucket.org/pypa/distlib/issue/32/
-    maker.set_mode = True
-
-    # Simplify the script and fix the fact that the default script swallows
-    # every single stack trace.
-    # See https://bitbucket.org/pypa/distlib/issue/34/
-    # See https://bitbucket.org/pypa/distlib/issue/33/
-    def _get_script_text(entry):
-        if entry.suffix is None:
-            raise InstallationError(
-                "Invalid script entry point: %s for req: %s - A callable "
-                "suffix is required. Cf https://packaging.python.org/en/"
-                "latest/distributing.html#console-scripts for more "
-                "information." % (entry, req)
-            )
-        return maker.script_template % {
-            "module": entry.prefix,
-            "import_name": entry.suffix.split(".")[0],
-            "func": entry.suffix,
-        }
-    # ignore type, because mypy disallows assigning to a method,
-    # see https://github.com/python/mypy/issues/2427
-    maker._get_script_text = _get_script_text  # type: ignore
-    maker.script_template = r"""# -*- coding: utf-8 -*-
-import re
-import sys
-
-from %(module)s import %(import_name)s
-
-if __name__ == '__main__':
-    sys.argv[0] = re.sub(r'(-script\.pyw?|\.exe)?$', '', sys.argv[0])
-    sys.exit(%(func)s())
-"""
-
-    # Special case pip and setuptools to generate versioned wrappers
-    #
-    # The issue is that some projects (specifically, pip and setuptools) use
-    # code in setup.py to create "versioned" entry points - pip2.7 on Python
-    # 2.7, pip3.3 on Python 3.3, etc. But these entry points are baked into
-    # the wheel metadata at build time, and so if the wheel is installed with
-    # a *different* version of Python the entry points will be wrong. The
-    # correct fix for this is to enhance the metadata to be able to describe
-    # such versioned entry points, but that won't happen till Metadata 2.0 is
-    # available.
-    # In the meantime, projects using versioned entry points will either have
-    # incorrect versioned entry points, or they will not be able to distribute
-    # "universal" wheels (i.e., they will need a wheel per Python version).
-    #
-    # Because setuptools and pip are bundled with _ensurepip and virtualenv,
-    # we need to use universal wheels. So, as a stopgap until Metadata 2.0, we
-    # override the versioned entry points in the wheel and generate the
-    # correct ones. This code is purely a short-term measure until Metadata 2.0
-    # is available.
-    #
-    # To add the level of hack in this section of code, in order to support
-    # ensurepip this code will look for an ``ENSUREPIP_OPTIONS`` environment
-    # variable which will control which version scripts get installed.
-    #
-    # ENSUREPIP_OPTIONS=altinstall
-    #   - Only pipX.Y and easy_install-X.Y will be generated and installed
-    # ENSUREPIP_OPTIONS=install
-    #   - pipX.Y, pipX, easy_install-X.Y will be generated and installed. Note
-    #     that this option is technically if ENSUREPIP_OPTIONS is set and is
-    #     not altinstall
-    # DEFAULT
-    #   - The default behavior is to install pip, pipX, pipX.Y, easy_install
-    #     and easy_install-X.Y.
-    pip_script = console.pop('pip', None)
-    if pip_script:
-        if "ENSUREPIP_OPTIONS" not in os.environ:
-            spec = 'pip = ' + pip_script
-            generated.extend(maker.make(spec))
-
-        if os.environ.get("ENSUREPIP_OPTIONS", "") != "altinstall":
-            spec = 'pip%s = %s' % (sys.version[:1], pip_script)
-            generated.extend(maker.make(spec))
-
-        spec = 'pip%s = %s' % (sys.version[:3], pip_script)
-        generated.extend(maker.make(spec))
-        # Delete any other versioned pip entry points
-        pip_ep = [k for k in console if re.match(r'pip(\d(\.\d)?)?$', k)]
-        for k in pip_ep:
-            del console[k]
-    easy_install_script = console.pop('easy_install', None)
-    if easy_install_script:
-        if "ENSUREPIP_OPTIONS" not in os.environ:
-            spec = 'easy_install = ' + easy_install_script
-            generated.extend(maker.make(spec))
-
-        spec = 'easy_install-%s = %s' % (sys.version[:3], easy_install_script)
-        generated.extend(maker.make(spec))
-        # Delete any other versioned easy_install entry points
-        easy_install_ep = [
-            k for k in console if re.match(r'easy_install(-\d\.\d)?$', k)
-        ]
-        for k in easy_install_ep:
-            del console[k]
-
-    # Generate the console and GUI entry points specified in the wheel
-    if len(console) > 0:
-        generated_console_scripts = maker.make_multiple(
-            ['%s = %s' % kv for kv in console.items()]
-        )
-        generated.extend(generated_console_scripts)
-
-        if warn_script_location:
-            msg = message_about_scripts_not_on_PATH(generated_console_scripts)
-            if msg is not None:
-                logger.warning(msg)
-
-    if len(gui) > 0:
-        generated.extend(
-            maker.make_multiple(
-                ['%s = %s' % kv for kv in gui.items()],
-                {'gui': True}
-            )
-        )
-
-    # Record pip as the installer
-    installer = os.path.join(info_dir[0], 'INSTALLER')
-    temp_installer = os.path.join(info_dir[0], 'INSTALLER.pip')
-    with open(temp_installer, 'wb') as installer_file:
-        installer_file.write(b'pip\n')
-    shutil.move(temp_installer, installer)
-    generated.append(installer)
-
-    # Record details of all files installed
-    record = os.path.join(info_dir[0], 'RECORD')
-    temp_record = os.path.join(info_dir[0], 'RECORD.pip')
-    with open_for_csv(record, 'r') as record_in:
-        with open_for_csv(temp_record, 'w+') as record_out:
-            reader = csv.reader(record_in)
-            outrows = get_csv_rows_for_installed(
-                reader, installed=installed, changed=changed,
-                generated=generated, lib_dir=lib_dir,
-            )
-            writer = csv.writer(record_out)
-            # Sort to simplify testing.
-            for row in sorted_outrows(outrows):
-                writer.writerow(row)
-    shutil.move(temp_record, record)
-
-
-def wheel_version(source_dir):
-    # type: (Optional[str]) -> Optional[Tuple[int, ...]]
-    """
-    Return the Wheel-Version of an extracted wheel, if possible.
-
-    Otherwise, return None if we couldn't parse / extract it.
-    """
-    try:
-        dist = [d for d in pkg_resources.find_on_path(None, source_dir)][0]
-
-        wheel_data = dist.get_metadata('WHEEL')
-        wheel_data = Parser().parsestr(wheel_data)
-
-        version = wheel_data['Wheel-Version'].strip()
-        version = tuple(map(int, version.split('.')))
-        return version
-    except Exception:
-        return None
-
-
-def check_compatibility(version, name):
-    # type: (Optional[Tuple[int, ...]], str) -> None
-    """
-    Raises errors or warns if called with an incompatible Wheel-Version.
-
-    Pip should refuse to install a Wheel-Version that's a major series
-    ahead of what it's compatible with (e.g 2.0 > 1.1); and warn when
-    installing a version only minor version ahead (e.g 1.2 > 1.1).
-
-    version: a 2-tuple representing a Wheel-Version (Major, Minor)
-    name: name of wheel or package to raise exception about
-
-    :raises UnsupportedWheel: when an incompatible Wheel-Version is given
-    """
-    if not version:
-        raise UnsupportedWheel(
-            "%s is in an unsupported or invalid wheel" % name
-        )
-    if version[0] > VERSION_COMPATIBLE[0]:
-        raise UnsupportedWheel(
-            "%s's Wheel-Version (%s) is not compatible with this version "
-            "of pip" % (name, '.'.join(map(str, version)))
-        )
-    elif version > VERSION_COMPATIBLE:
-        logger.warning(
-            'Installing from a newer Wheel-Version (%s)',
-            '.'.join(map(str, version)),
-        )
-
-
-class Wheel(object):
-    """A wheel file"""
-
-    # TODO: Maybe move the class into the models sub-package
-    # TODO: Maybe move the install code into this class
-
-    wheel_file_re = re.compile(
-        r"""^(?P<namever>(?P<name>.+?)-(?P<ver>.*?))
-        ((-(?P<build>\d[^-]*?))?-(?P<pyver>.+?)-(?P<abi>.+?)-(?P<plat>.+?)
-        \.whl|\.dist-info)$""",
-        re.VERBOSE
-    )
-
-    def __init__(self, filename):
-        # type: (str) -> None
-        """
-        :raises InvalidWheelFilename: when the filename is invalid for a wheel
-        """
-        wheel_info = self.wheel_file_re.match(filename)
-        if not wheel_info:
-            raise InvalidWheelFilename(
-                "%s is not a valid wheel filename." % filename
-            )
-        self.filename = filename
-        self.name = wheel_info.group('name').replace('_', '-')
-        # we'll assume "_" means "-" due to wheel naming scheme
-        # (https://github.com/pypa/pip/issues/1150)
-        self.version = wheel_info.group('ver').replace('_', '-')
-        self.build_tag = wheel_info.group('build')
-        self.pyversions = wheel_info.group('pyver').split('.')
-        self.abis = wheel_info.group('abi').split('.')
-        self.plats = wheel_info.group('plat').split('.')
-
-        # All the tag combinations from this file
-        self.file_tags = {
-            (x, y, z) for x in self.pyversions
-            for y in self.abis for z in self.plats
-        }
-
-    def support_index_min(self, tags=None):
-        # type: (Optional[List[Pep425Tag]]) -> Optional[int]
-        """
-        Return the lowest index that one of the wheel's file_tag combinations
-        achieves in the supported_tags list e.g. if there are 8 supported tags,
-        and one of the file tags is first in the list, then return 0.  Returns
-        None is the wheel is not supported.
-        """
-        if tags is None:  # for mock
-            tags = pep425tags.get_supported()
-        indexes = [tags.index(c) for c in self.file_tags if c in tags]
-        return min(indexes) if indexes else None
-
-    def supported(self, tags=None):
-        # type: (Optional[List[Pep425Tag]]) -> bool
-        """Is this wheel supported on this system?"""
-        if tags is None:  # for mock
-            tags = pep425tags.get_supported()
-        return bool(set(tags).intersection(self.file_tags))
-
-
-def _contains_egg_info(
-        s, _egg_info_re=re.compile(r'([a-z0-9_.]+)-([a-z0-9_.!+-]+)', re.I)):
-    """Determine whether the string looks like an egg_info.
-
-    :param s: The string to parse. E.g. foo-2.1
-    """
-    return bool(_egg_info_re.search(s))
-
-
-def should_use_ephemeral_cache(
-    req,  # type: InstallRequirement
-    format_control,  # type: FormatControl
-    autobuilding,  # type: bool
-    cache_available  # type: bool
-):
-    # type: (...) -> Optional[bool]
-    """
-    Return whether to build an InstallRequirement object using the
-    ephemeral cache.
-
-    :param cache_available: whether a cache directory is available for the
-        autobuilding=True case.
-
-    :return: True or False to build the requirement with ephem_cache=True
-        or False, respectively; or None not to build the requirement.
-    """
-    if req.constraint:
-        return None
-    if req.is_wheel:
-        if not autobuilding:
-            logger.info(
-                'Skipping %s, due to already being wheel.', req.name,
-            )
-        return None
-    if not autobuilding:
-        return False
-
-    if req.editable or not req.source_dir:
-        return None
-
-    if req.link and not req.link.is_artifact:
-        # VCS checkout. Build wheel just for this run.
-        return True
-
-    if "binary" not in format_control.get_allowed_formats(
-            canonicalize_name(req.name)):
-        logger.info(
-            "Skipping bdist_wheel for %s, due to binaries "
-            "being disabled for it.", req.name,
-        )
-        return None
-
-    link = req.link
-    base, ext = link.splitext()
-    if cache_available and _contains_egg_info(base):
-        return False
-
-    # Otherwise, build the wheel just for this run using the ephemeral
-    # cache since we are either in the case of e.g. a local directory, or
-    # no cache directory is available to use.
-    return True
-
-
-def format_command(
-    command_args,  # type: List[str]
-    command_output,  # type: str
-):
-    # type: (...) -> str
-    """
-    Format command information for logging.
-    """
-    text = 'Command arguments: {}\n'.format(command_args)
-
-    if not command_output:
-        text += 'Command output: None'
-    elif logger.getEffectiveLevel() > logging.DEBUG:
-        text += 'Command output: [use --verbose to show]'
-    else:
-        if not command_output.endswith('\n'):
-            command_output += '\n'
-        text += (
-            'Command output:\n{}'
-            '-----------------------------------------'
-        ).format(command_output)
-
-    return text
-
-
-def get_legacy_build_wheel_path(
-    names,  # type: List[str]
-    temp_dir,  # type: str
-    req,  # type: InstallRequirement
-    command_args,  # type: List[str]
-    command_output,  # type: str
-):
-    # type: (...) -> Optional[str]
-    """
-    Return the path to the wheel in the temporary build directory.
-    """
-    # Sort for determinism.
-    names = sorted(names)
-    if not names:
-        msg = (
-            'Legacy build of wheel for {!r} created no files.\n'
-        ).format(req.name)
-        msg += format_command(command_args, command_output)
-        logger.warning(msg)
-        return None
-
-    if len(names) > 1:
-        msg = (
-            'Legacy build of wheel for {!r} created more than one file.\n'
-            'Filenames (choosing first): {}\n'
-        ).format(req.name, names)
-        msg += format_command(command_args, command_output)
-        logger.warning(msg)
-
-    return os.path.join(temp_dir, names[0])
-
-
-class WheelBuilder(object):
-    """Build wheels from a RequirementSet."""
-
-    def __init__(
-        self,
-        finder,  # type: PackageFinder
-        preparer,  # type: RequirementPreparer
-        wheel_cache,  # type: WheelCache
-        build_options=None,  # type: Optional[List[str]]
-        global_options=None,  # type: Optional[List[str]]
-        no_clean=False  # type: bool
-    ):
-        # type: (...) -> None
-        self.finder = finder
-        self.preparer = preparer
-        self.wheel_cache = wheel_cache
-
-        self._wheel_dir = preparer.wheel_download_dir
-
-        self.build_options = build_options or []
-        self.global_options = global_options or []
-        self.no_clean = no_clean
-
-    def _build_one(self, req, output_dir, python_tag=None):
-        """Build one wheel.
-
-        :return: The filename of the built wheel, or None if the build failed.
-        """
-        # Install build deps into temporary directory (PEP 518)
-        with req.build_env:
-            return self._build_one_inside_env(req, output_dir,
-                                              python_tag=python_tag)
-
-    def _build_one_inside_env(self, req, output_dir, python_tag=None):
-        with TempDirectory(kind="wheel") as temp_dir:
-            if req.use_pep517:
-                builder = self._build_one_pep517
-            else:
-                builder = self._build_one_legacy
-            wheel_path = builder(req, temp_dir.path, python_tag=python_tag)
-            if wheel_path is not None:
-                wheel_name = os.path.basename(wheel_path)
-                dest_path = os.path.join(output_dir, wheel_name)
-                try:
-                    shutil.move(wheel_path, dest_path)
-                    logger.info('Stored in directory: %s', output_dir)
-                    return dest_path
-                except Exception:
-                    pass
-            # Ignore return, we can't do anything else useful.
-            self._clean_one(req)
-            return None
-
-    def _base_setup_args(self, req):
-        # NOTE: Eventually, we'd want to also -S to the flags here, when we're
-        # isolating. Currently, it breaks Python in virtualenvs, because it
-        # relies on site.py to find parts of the standard library outside the
-        # virtualenv.
-        return [
-            sys.executable, '-u', '-c',
-            SETUPTOOLS_SHIM % req.setup_py
-        ] + list(self.global_options)
-
-    def _build_one_pep517(self, req, tempd, python_tag=None):
-        """Build one InstallRequirement using the PEP 517 build process.
-
-        Returns path to wheel if successfully built. Otherwise, returns None.
-        """
-        assert req.metadata_directory is not None
-        try:
-            req.spin_message = 'Building wheel for %s (PEP 517)' % (req.name,)
-            logger.debug('Destination directory: %s', tempd)
-            wheel_name = req.pep517_backend.build_wheel(
-                tempd,
-                metadata_directory=req.metadata_directory
-            )
-            if python_tag:
-                # General PEP 517 backends don't necessarily support
-                # a "--python-tag" option, so we rename the wheel
-                # file directly.
-                new_name = replace_python_tag(wheel_name, python_tag)
-                os.rename(
-                    os.path.join(tempd, wheel_name),
-                    os.path.join(tempd, new_name)
-                )
-                # Reassign to simplify the return at the end of function
-                wheel_name = new_name
-        except Exception:
-            logger.error('Failed building wheel for %s', req.name)
-            return None
-        return os.path.join(tempd, wheel_name)
-
-    def _build_one_legacy(self, req, tempd, python_tag=None):
-        """Build one InstallRequirement using the "legacy" build process.
-
-        Returns path to wheel if successfully built. Otherwise, returns None.
-        """
-        base_args = self._base_setup_args(req)
-
-        spin_message = 'Building wheel for %s (setup.py)' % (req.name,)
-        with open_spinner(spin_message) as spinner:
-            logger.debug('Destination directory: %s', tempd)
-            wheel_args = base_args + ['bdist_wheel', '-d', tempd] \
-                + self.build_options
-
-            if python_tag is not None:
-                wheel_args += ["--python-tag", python_tag]
-
-            try:
-                output = call_subprocess(wheel_args, cwd=req.setup_py_dir,
-                                         show_stdout=False, spinner=spinner)
-            except Exception:
-                spinner.finish("error")
-                logger.error('Failed building wheel for %s', req.name)
-                return None
-            names = os.listdir(tempd)
-            wheel_path = get_legacy_build_wheel_path(
-                names=names,
-                temp_dir=tempd,
-                req=req,
-                command_args=wheel_args,
-                command_output=output,
-            )
-            return wheel_path
-
-    def _clean_one(self, req):
-        base_args = self._base_setup_args(req)
-
-        logger.info('Running setup.py clean for %s', req.name)
-        clean_args = base_args + ['clean', '--all']
-        try:
-            call_subprocess(clean_args, cwd=req.source_dir, show_stdout=False)
-            return True
-        except Exception:
-            logger.error('Failed cleaning build dir for %s', req.name)
-            return False
-
-    def build(
-        self,
-        requirements,  # type: Iterable[InstallRequirement]
-        session,  # type: PipSession
-        autobuilding=False  # type: bool
-    ):
-        # type: (...) -> List[InstallRequirement]
-        """Build wheels.
-
-        :param unpack: If True, replace the sdist we built from with the
-            newly built wheel, in preparation for installation.
-        :return: True if all the wheels built correctly.
-        """
-        buildset = []
-        format_control = self.finder.format_control
-        # Whether a cache directory is available for autobuilding=True.
-        cache_available = bool(self._wheel_dir or self.wheel_cache.cache_dir)
-
-        for req in requirements:
-            ephem_cache = should_use_ephemeral_cache(
-                req, format_control=format_control, autobuilding=autobuilding,
-                cache_available=cache_available,
-            )
-            if ephem_cache is None:
-                continue
-
-            buildset.append((req, ephem_cache))
-
-        if not buildset:
-            return []
-
-        # Is any wheel build not using the ephemeral cache?
-        if any(not ephem_cache for _, ephem_cache in buildset):
-            have_directory_for_build = self._wheel_dir or (
-                autobuilding and self.wheel_cache.cache_dir
-            )
-            assert have_directory_for_build
-
-        # TODO by @pradyunsg
-        # Should break up this method into 2 separate methods.
-
-        # Build the wheels.
-        logger.info(
-            'Building wheels for collected packages: %s',
-            ', '.join([req.name for (req, _) in buildset]),
-        )
-        _cache = self.wheel_cache  # shorter name
-        with indent_log():
-            build_success, build_failure = [], []
-            for req, ephem in buildset:
-                python_tag = None
-                if autobuilding:
-                    python_tag = pep425tags.implementation_tag
-                    if ephem:
-                        output_dir = _cache.get_ephem_path_for_link(req.link)
-                    else:
-                        output_dir = _cache.get_path_for_link(req.link)
-                    try:
-                        ensure_dir(output_dir)
-                    except OSError as e:
-                        logger.warning("Building wheel for %s failed: %s",
-                                       req.name, e)
-                        build_failure.append(req)
-                        continue
-                else:
-                    output_dir = self._wheel_dir
-                wheel_file = self._build_one(
-                    req, output_dir,
-                    python_tag=python_tag,
-                )
-                if wheel_file:
-                    build_success.append(req)
-                    if autobuilding:
-                        # XXX: This is mildly duplicative with prepare_files,
-                        # but not close enough to pull out to a single common
-                        # method.
-                        # The code below assumes temporary source dirs -
-                        # prevent it doing bad things.
-                        if req.source_dir and not os.path.exists(os.path.join(
-                                req.source_dir, PIP_DELETE_MARKER_FILENAME)):
-                            raise AssertionError(
-                                "bad source dir - missing marker")
-                        # Delete the source we built the wheel from
-                        req.remove_temporary_source()
-                        # set the build directory again - name is known from
-                        # the work prepare_files did.
-                        req.source_dir = req.build_location(
-                            self.preparer.build_dir
-                        )
-                        # Update the link for this.
-                        req.link = Link(path_to_url(wheel_file))
-                        assert req.link.is_wheel
-                        # extract the wheel into the dir
-                        unpack_url(
-                            req.link, req.source_dir, None, False,
-                            session=session,
-                        )
-                else:
-                    build_failure.append(req)
-
-        # notify success/failure
-        if build_success:
-            logger.info(
-                'Successfully built %s',
-                ' '.join([req.name for req in build_success]),
-            )
-        if build_failure:
-            logger.info(
-                'Failed to build %s',
-                ' '.join([req.name for req in build_failure]),
-            )
-        # Return a list of requirements that failed to build
-        return build_failure
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__init__.py
deleted file mode 100644
index b919b54..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__init__.py
+++ /dev/null
@@ -1,111 +0,0 @@
-"""
-pip._vendor is for vendoring dependencies of pip to prevent needing pip to
-depend on something external.
-
-Files inside of pip._vendor should be considered immutable and should only be
-updated to versions from upstream.
-"""
-from __future__ import absolute_import
-
-import glob
-import os.path
-import sys
-
-# Downstream redistributors which have debundled our dependencies should also
-# patch this value to be true. This will trigger the additional patching
-# to cause things like "six" to be available as pip.
-DEBUNDLED = False
-
-# By default, look in this directory for a bunch of .whl files which we will
-# add to the beginning of sys.path before attempting to import anything. This
-# is done to support downstream re-distributors like Debian and Fedora who
-# wish to create their own Wheels for our dependencies to aid in debundling.
-WHEEL_DIR = os.path.abspath(os.path.dirname(__file__))
-
-
-# Define a small helper function to alias our vendored modules to the real ones
-# if the vendored ones do not exist. This idea of this was taken from
-# https://github.com/kennethreitz/requests/pull/2567.
-def vendored(modulename):
-    vendored_name = "{0}.{1}".format(__name__, modulename)
-
-    try:
-        __import__(vendored_name, globals(), locals(), level=0)
-    except ImportError:
-        try:
-            __import__(modulename, globals(), locals(), level=0)
-        except ImportError:
-            # We can just silently allow import failures to pass here. If we
-            # got to this point it means that ``import pip._vendor.whatever``
-            # failed and so did ``import whatever``. Since we're importing this
-            # upfront in an attempt to alias imports, not erroring here will
-            # just mean we get a regular import error whenever pip *actually*
-            # tries to import one of these modules to use it, which actually
-            # gives us a better error message than we would have otherwise
-            # gotten.
-            pass
-        else:
-            sys.modules[vendored_name] = sys.modules[modulename]
-            base, head = vendored_name.rsplit(".", 1)
-            setattr(sys.modules[base], head, sys.modules[modulename])
-
-
-# If we're operating in a debundled setup, then we want to go ahead and trigger
-# the aliasing of our vendored libraries as well as looking for wheels to add
-# to our sys.path. This will cause all of this code to be a no-op typically
-# however downstream redistributors can enable it in a consistent way across
-# all platforms.
-if DEBUNDLED:
-    # Actually look inside of WHEEL_DIR to find .whl files and add them to the
-    # front of our sys.path.
-    sys.path[:] = glob.glob(os.path.join(WHEEL_DIR, "*.whl")) + sys.path
-
-    # Actually alias all of our vendored dependencies.
-    vendored("cachecontrol")
-    vendored("colorama")
-    vendored("distlib")
-    vendored("distro")
-    vendored("html5lib")
-    vendored("lockfile")
-    vendored("six")
-    vendored("six.moves")
-    vendored("six.moves.urllib")
-    vendored("six.moves.urllib.parse")
-    vendored("packaging")
-    vendored("packaging.version")
-    vendored("packaging.specifiers")
-    vendored("pep517")
-    vendored("pkg_resources")
-    vendored("progress")
-    vendored("pytoml")
-    vendored("retrying")
-    vendored("requests")
-    vendored("requests.packages")
-    vendored("requests.packages.urllib3")
-    vendored("requests.packages.urllib3._collections")
-    vendored("requests.packages.urllib3.connection")
-    vendored("requests.packages.urllib3.connectionpool")
-    vendored("requests.packages.urllib3.contrib")
-    vendored("requests.packages.urllib3.contrib.ntlmpool")
-    vendored("requests.packages.urllib3.contrib.pyopenssl")
-    vendored("requests.packages.urllib3.exceptions")
-    vendored("requests.packages.urllib3.fields")
-    vendored("requests.packages.urllib3.filepost")
-    vendored("requests.packages.urllib3.packages")
-    vendored("requests.packages.urllib3.packages.ordered_dict")
-    vendored("requests.packages.urllib3.packages.six")
-    vendored("requests.packages.urllib3.packages.ssl_match_hostname")
-    vendored("requests.packages.urllib3.packages.ssl_match_hostname."
-             "_implementation")
-    vendored("requests.packages.urllib3.poolmanager")
-    vendored("requests.packages.urllib3.request")
-    vendored("requests.packages.urllib3.response")
-    vendored("requests.packages.urllib3.util")
-    vendored("requests.packages.urllib3.util.connection")
-    vendored("requests.packages.urllib3.util.request")
-    vendored("requests.packages.urllib3.util.response")
-    vendored("requests.packages.urllib3.util.retry")
-    vendored("requests.packages.urllib3.util.ssl_")
-    vendored("requests.packages.urllib3.util.timeout")
-    vendored("requests.packages.urllib3.util.url")
-    vendored("urllib3")
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 85c198f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/appdirs.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/appdirs.cpython-37.pyc
deleted file mode 100644
index 82a5e45..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/appdirs.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/pyparsing.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/pyparsing.cpython-37.pyc
deleted file mode 100644
index 0060b54..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/pyparsing.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/retrying.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/retrying.cpython-37.pyc
deleted file mode 100644
index 44d7fec..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/retrying.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/six.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/six.cpython-37.pyc
deleted file mode 100644
index 09f881b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/__pycache__/six.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/appdirs.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/appdirs.py
deleted file mode 100644
index 2bd3911..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/appdirs.py
+++ /dev/null
@@ -1,604 +0,0 @@
-#!/usr/bin/env python
-# -*- coding: utf-8 -*-
-# Copyright (c) 2005-2010 ActiveState Software Inc.
-# Copyright (c) 2013 Eddy Petrișor
-
-"""Utilities for determining application-specific dirs.
-
-See <http://github.com/ActiveState/appdirs> for details and usage.
-"""
-# Dev Notes:
-# - MSDN on where to store app data files:
-#   http://support.microsoft.com/default.aspx?scid=kb;en-us;310294#XSLTH3194121123120121120120
-# - Mac OS X: http://developer.apple.com/documentation/MacOSX/Conceptual/BPFileSystem/index.html
-# - XDG spec for Un*x: http://standards.freedesktop.org/basedir-spec/basedir-spec-latest.html
-
-__version_info__ = (1, 4, 3)
-__version__ = '.'.join(map(str, __version_info__))
-
-
-import sys
-import os
-
-PY3 = sys.version_info[0] == 3
-
-if PY3:
-    unicode = str
-
-if sys.platform.startswith('java'):
-    import platform
-    os_name = platform.java_ver()[3][0]
-    if os_name.startswith('Windows'): # "Windows XP", "Windows 7", etc.
-        system = 'win32'
-    elif os_name.startswith('Mac'): # "Mac OS X", etc.
-        system = 'darwin'
-    else: # "Linux", "SunOS", "FreeBSD", etc.
-        # Setting this to "linux2" is not ideal, but only Windows or Mac
-        # are actually checked for and the rest of the module expects
-        # *sys.platform* style strings.
-        system = 'linux2'
-else:
-    system = sys.platform
-
-
-
-def user_data_dir(appname=None, appauthor=None, version=None, roaming=False):
-    r"""Return full path to the user-specific data dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "appauthor" (only used on Windows) is the name of the
-            appauthor or distributing body for this application. Typically
-            it is the owning company name. This falls back to appname. You may
-            pass False to disable it.
-        "version" is an optional version path element to append to the
-            path. You might want to use this if you want multiple versions
-            of your app to be able to run independently. If used, this
-            would typically be "<major>.<minor>".
-            Only applied when appname is present.
-        "roaming" (boolean, default False) can be set True to use the Windows
-            roaming appdata directory. That means that for users on a Windows
-            network setup for roaming profiles, this user data will be
-            sync'd on login. See
-            <http://technet.microsoft.com/en-us/library/cc766489(WS.10).aspx>
-            for a discussion of issues.
-
-    Typical user data directories are:
-        Mac OS X:               ~/Library/Application Support/<AppName>
-        Unix:                   ~/.local/share/<AppName>    # or in $XDG_DATA_HOME, if defined
-        Win XP (not roaming):   C:\Documents and Settings\<username>\Application Data\<AppAuthor>\<AppName>
-        Win XP (roaming):       C:\Documents and Settings\<username>\Local Settings\Application Data\<AppAuthor>\<AppName>
-        Win 7  (not roaming):   C:\Users\<username>\AppData\Local\<AppAuthor>\<AppName>
-        Win 7  (roaming):       C:\Users\<username>\AppData\Roaming\<AppAuthor>\<AppName>
-
-    For Unix, we follow the XDG spec and support $XDG_DATA_HOME.
-    That means, by default "~/.local/share/<AppName>".
-    """
-    if system == "win32":
-        if appauthor is None:
-            appauthor = appname
-        const = roaming and "CSIDL_APPDATA" or "CSIDL_LOCAL_APPDATA"
-        path = os.path.normpath(_get_win_folder(const))
-        if appname:
-            if appauthor is not False:
-                path = os.path.join(path, appauthor, appname)
-            else:
-                path = os.path.join(path, appname)
-    elif system == 'darwin':
-        path = os.path.expanduser('~/Library/Application Support/')
-        if appname:
-            path = os.path.join(path, appname)
-    else:
-        path = os.getenv('XDG_DATA_HOME', os.path.expanduser("~/.local/share"))
-        if appname:
-            path = os.path.join(path, appname)
-    if appname and version:
-        path = os.path.join(path, version)
-    return path
-
-
-def site_data_dir(appname=None, appauthor=None, version=None, multipath=False):
-    r"""Return full path to the user-shared data dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "appauthor" (only used on Windows) is the name of the
-            appauthor or distributing body for this application. Typically
-            it is the owning company name. This falls back to appname. You may
-            pass False to disable it.
-        "version" is an optional version path element to append to the
-            path. You might want to use this if you want multiple versions
-            of your app to be able to run independently. If used, this
-            would typically be "<major>.<minor>".
-            Only applied when appname is present.
-        "multipath" is an optional parameter only applicable to *nix
-            which indicates that the entire list of data dirs should be
-            returned. By default, the first item from XDG_DATA_DIRS is
-            returned, or '/usr/local/share/<AppName>',
-            if XDG_DATA_DIRS is not set
-
-    Typical site data directories are:
-        Mac OS X:   /Library/Application Support/<AppName>
-        Unix:       /usr/local/share/<AppName> or /usr/share/<AppName>
-        Win XP:     C:\Documents and Settings\All Users\Application Data\<AppAuthor>\<AppName>
-        Vista:      (Fail! "C:\ProgramData" is a hidden *system* directory on Vista.)
-        Win 7:      C:\ProgramData\<AppAuthor>\<AppName>   # Hidden, but writeable on Win 7.
-
-    For Unix, this is using the $XDG_DATA_DIRS[0] default.
-
-    WARNING: Do not use this on Windows. See the Vista-Fail note above for why.
-    """
-    if system == "win32":
-        if appauthor is None:
-            appauthor = appname
-        path = os.path.normpath(_get_win_folder("CSIDL_COMMON_APPDATA"))
-        if appname:
-            if appauthor is not False:
-                path = os.path.join(path, appauthor, appname)
-            else:
-                path = os.path.join(path, appname)
-    elif system == 'darwin':
-        path = os.path.expanduser('/Library/Application Support')
-        if appname:
-            path = os.path.join(path, appname)
-    else:
-        # XDG default for $XDG_DATA_DIRS
-        # only first, if multipath is False
-        path = os.getenv('XDG_DATA_DIRS',
-                         os.pathsep.join(['/usr/local/share', '/usr/share']))
-        pathlist = [os.path.expanduser(x.rstrip(os.sep)) for x in path.split(os.pathsep)]
-        if appname:
-            if version:
-                appname = os.path.join(appname, version)
-            pathlist = [os.sep.join([x, appname]) for x in pathlist]
-
-        if multipath:
-            path = os.pathsep.join(pathlist)
-        else:
-            path = pathlist[0]
-        return path
-
-    if appname and version:
-        path = os.path.join(path, version)
-    return path
-
-
-def user_config_dir(appname=None, appauthor=None, version=None, roaming=False):
-    r"""Return full path to the user-specific config dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "appauthor" (only used on Windows) is the name of the
-            appauthor or distributing body for this application. Typically
-            it is the owning company name. This falls back to appname. You may
-            pass False to disable it.
-        "version" is an optional version path element to append to the
-            path. You might want to use this if you want multiple versions
-            of your app to be able to run independently. If used, this
-            would typically be "<major>.<minor>".
-            Only applied when appname is present.
-        "roaming" (boolean, default False) can be set True to use the Windows
-            roaming appdata directory. That means that for users on a Windows
-            network setup for roaming profiles, this user data will be
-            sync'd on login. See
-            <http://technet.microsoft.com/en-us/library/cc766489(WS.10).aspx>
-            for a discussion of issues.
-
-    Typical user config directories are:
-        Mac OS X:               same as user_data_dir
-        Unix:                   ~/.config/<AppName>     # or in $XDG_CONFIG_HOME, if defined
-        Win *:                  same as user_data_dir
-
-    For Unix, we follow the XDG spec and support $XDG_CONFIG_HOME.
-    That means, by default "~/.config/<AppName>".
-    """
-    if system in ["win32", "darwin"]:
-        path = user_data_dir(appname, appauthor, None, roaming)
-    else:
-        path = os.getenv('XDG_CONFIG_HOME', os.path.expanduser("~/.config"))
-        if appname:
-            path = os.path.join(path, appname)
-    if appname and version:
-        path = os.path.join(path, version)
-    return path
-
-
-def site_config_dir(appname=None, appauthor=None, version=None, multipath=False):
-    r"""Return full path to the user-shared data dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "appauthor" (only used on Windows) is the name of the
-            appauthor or distributing body for this application. Typically
-            it is the owning company name. This falls back to appname. You may
-            pass False to disable it.
-        "version" is an optional version path element to append to the
-            path. You might want to use this if you want multiple versions
-            of your app to be able to run independently. If used, this
-            would typically be "<major>.<minor>".
-            Only applied when appname is present.
-        "multipath" is an optional parameter only applicable to *nix
-            which indicates that the entire list of config dirs should be
-            returned. By default, the first item from XDG_CONFIG_DIRS is
-            returned, or '/etc/xdg/<AppName>', if XDG_CONFIG_DIRS is not set
-
-    Typical site config directories are:
-        Mac OS X:   same as site_data_dir
-        Unix:       /etc/xdg/<AppName> or $XDG_CONFIG_DIRS[i]/<AppName> for each value in
-                    $XDG_CONFIG_DIRS
-        Win *:      same as site_data_dir
-        Vista:      (Fail! "C:\ProgramData" is a hidden *system* directory on Vista.)
-
-    For Unix, this is using the $XDG_CONFIG_DIRS[0] default, if multipath=False
-
-    WARNING: Do not use this on Windows. See the Vista-Fail note above for why.
-    """
-    if system in ["win32", "darwin"]:
-        path = site_data_dir(appname, appauthor)
-        if appname and version:
-            path = os.path.join(path, version)
-    else:
-        # XDG default for $XDG_CONFIG_DIRS
-        # only first, if multipath is False
-        path = os.getenv('XDG_CONFIG_DIRS', '/etc/xdg')
-        pathlist = [os.path.expanduser(x.rstrip(os.sep)) for x in path.split(os.pathsep)]
-        if appname:
-            if version:
-                appname = os.path.join(appname, version)
-            pathlist = [os.sep.join([x, appname]) for x in pathlist]
-
-        if multipath:
-            path = os.pathsep.join(pathlist)
-        else:
-            path = pathlist[0]
-    return path
-
-
-def user_cache_dir(appname=None, appauthor=None, version=None, opinion=True):
-    r"""Return full path to the user-specific cache dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "appauthor" (only used on Windows) is the name of the
-            appauthor or distributing body for this application. Typically
-            it is the owning company name. This falls back to appname. You may
-            pass False to disable it.
-        "version" is an optional version path element to append to the
-            path. You might want to use this if you want multiple versions
-            of your app to be able to run independently. If used, this
-            would typically be "<major>.<minor>".
-            Only applied when appname is present.
-        "opinion" (boolean) can be False to disable the appending of
-            "Cache" to the base app data dir for Windows. See
-            discussion below.
-
-    Typical user cache directories are:
-        Mac OS X:   ~/Library/Caches/<AppName>
-        Unix:       ~/.cache/<AppName> (XDG default)
-        Win XP:     C:\Documents and Settings\<username>\Local Settings\Application Data\<AppAuthor>\<AppName>\Cache
-        Vista:      C:\Users\<username>\AppData\Local\<AppAuthor>\<AppName>\Cache
-
-    On Windows the only suggestion in the MSDN docs is that local settings go in
-    the `CSIDL_LOCAL_APPDATA` directory. This is identical to the non-roaming
-    app data dir (the default returned by `user_data_dir` above). Apps typically
-    put cache data somewhere *under* the given dir here. Some examples:
-        ...\Mozilla\Firefox\Profiles\<ProfileName>\Cache
-        ...\Acme\SuperApp\Cache\1.0
-    OPINION: This function appends "Cache" to the `CSIDL_LOCAL_APPDATA` value.
-    This can be disabled with the `opinion=False` option.
-    """
-    if system == "win32":
-        if appauthor is None:
-            appauthor = appname
-        path = os.path.normpath(_get_win_folder("CSIDL_LOCAL_APPDATA"))
-        if appname:
-            if appauthor is not False:
-                path = os.path.join(path, appauthor, appname)
-            else:
-                path = os.path.join(path, appname)
-            if opinion:
-                path = os.path.join(path, "Cache")
-    elif system == 'darwin':
-        path = os.path.expanduser('~/Library/Caches')
-        if appname:
-            path = os.path.join(path, appname)
-    else:
-        path = os.getenv('XDG_CACHE_HOME', os.path.expanduser('~/.cache'))
-        if appname:
-            path = os.path.join(path, appname)
-    if appname and version:
-        path = os.path.join(path, version)
-    return path
-
-
-def user_state_dir(appname=None, appauthor=None, version=None, roaming=False):
-    r"""Return full path to the user-specific state dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "appauthor" (only used on Windows) is the name of the
-            appauthor or distributing body for this application. Typically
-            it is the owning company name. This falls back to appname. You may
-            pass False to disable it.
-        "version" is an optional version path element to append to the
-            path. You might want to use this if you want multiple versions
-            of your app to be able to run independently. If used, this
-            would typically be "<major>.<minor>".
-            Only applied when appname is present.
-        "roaming" (boolean, default False) can be set True to use the Windows
-            roaming appdata directory. That means that for users on a Windows
-            network setup for roaming profiles, this user data will be
-            sync'd on login. See
-            <http://technet.microsoft.com/en-us/library/cc766489(WS.10).aspx>
-            for a discussion of issues.
-
-    Typical user state directories are:
-        Mac OS X:  same as user_data_dir
-        Unix:      ~/.local/state/<AppName>   # or in $XDG_STATE_HOME, if defined
-        Win *:     same as user_data_dir
-
-    For Unix, we follow this Debian proposal <https://wiki.debian.org/XDGBaseDirectorySpecification#state>
-    to extend the XDG spec and support $XDG_STATE_HOME.
-
-    That means, by default "~/.local/state/<AppName>".
-    """
-    if system in ["win32", "darwin"]:
-        path = user_data_dir(appname, appauthor, None, roaming)
-    else:
-        path = os.getenv('XDG_STATE_HOME', os.path.expanduser("~/.local/state"))
-        if appname:
-            path = os.path.join(path, appname)
-    if appname and version:
-        path = os.path.join(path, version)
-    return path
-
-
-def user_log_dir(appname=None, appauthor=None, version=None, opinion=True):
-    r"""Return full path to the user-specific log dir for this application.
-
-        "appname" is the name of application.
-            If None, just the system directory is returned.
-        "appauthor" (only used on Windows) is the name of the
-            appauthor or distributing body for this application. Typically
-            it is the owning company name. This falls back to appname. You may
-            pass False to disable it.
-        "version" is an optional version path element to append to the
-            path. You might want to use this if you want multiple versions
-            of your app to be able to run independently. If used, this
-            would typically be "<major>.<minor>".
-            Only applied when appname is present.
-        "opinion" (boolean) can be False to disable the appending of
-            "Logs" to the base app data dir for Windows, and "log" to the
-            base cache dir for Unix. See discussion below.
-
-    Typical user log directories are:
-        Mac OS X:   ~/Library/Logs/<AppName>
-        Unix:       ~/.cache/<AppName>/log  # or under $XDG_CACHE_HOME if defined
-        Win XP:     C:\Documents and Settings\<username>\Local Settings\Application Data\<AppAuthor>\<AppName>\Logs
-        Vista:      C:\Users\<username>\AppData\Local\<AppAuthor>\<AppName>\Logs
-
-    On Windows the only suggestion in the MSDN docs is that local settings
-    go in the `CSIDL_LOCAL_APPDATA` directory. (Note: I'm interested in
-    examples of what some windows apps use for a logs dir.)
-
-    OPINION: This function appends "Logs" to the `CSIDL_LOCAL_APPDATA`
-    value for Windows and appends "log" to the user cache dir for Unix.
-    This can be disabled with the `opinion=False` option.
-    """
-    if system == "darwin":
-        path = os.path.join(
-            os.path.expanduser('~/Library/Logs'),
-            appname)
-    elif system == "win32":
-        path = user_data_dir(appname, appauthor, version)
-        version = False
-        if opinion:
-            path = os.path.join(path, "Logs")
-    else:
-        path = user_cache_dir(appname, appauthor, version)
-        version = False
-        if opinion:
-            path = os.path.join(path, "log")
-    if appname and version:
-        path = os.path.join(path, version)
-    return path
-
-
-class AppDirs(object):
-    """Convenience wrapper for getting application dirs."""
-    def __init__(self, appname=None, appauthor=None, version=None,
-            roaming=False, multipath=False):
-        self.appname = appname
-        self.appauthor = appauthor
-        self.version = version
-        self.roaming = roaming
-        self.multipath = multipath
-
-    @property
-    def user_data_dir(self):
-        return user_data_dir(self.appname, self.appauthor,
-                             version=self.version, roaming=self.roaming)
-
-    @property
-    def site_data_dir(self):
-        return site_data_dir(self.appname, self.appauthor,
-                             version=self.version, multipath=self.multipath)
-
-    @property
-    def user_config_dir(self):
-        return user_config_dir(self.appname, self.appauthor,
-                               version=self.version, roaming=self.roaming)
-
-    @property
-    def site_config_dir(self):
-        return site_config_dir(self.appname, self.appauthor,
-                             version=self.version, multipath=self.multipath)
-
-    @property
-    def user_cache_dir(self):
-        return user_cache_dir(self.appname, self.appauthor,
-                              version=self.version)
-
-    @property
-    def user_state_dir(self):
-        return user_state_dir(self.appname, self.appauthor,
-                              version=self.version)
-
-    @property
-    def user_log_dir(self):
-        return user_log_dir(self.appname, self.appauthor,
-                            version=self.version)
-
-
-#---- internal support stuff
-
-def _get_win_folder_from_registry(csidl_name):
-    """This is a fallback technique at best. I'm not sure if using the
-    registry for this guarantees us the correct answer for all CSIDL_*
-    names.
-    """
-    if PY3:
-      import winreg as _winreg
-    else:
-      import _winreg
-
-    shell_folder_name = {
-        "CSIDL_APPDATA": "AppData",
-        "CSIDL_COMMON_APPDATA": "Common AppData",
-        "CSIDL_LOCAL_APPDATA": "Local AppData",
-    }[csidl_name]
-
-    key = _winreg.OpenKey(
-        _winreg.HKEY_CURRENT_USER,
-        r"Software\Microsoft\Windows\CurrentVersion\Explorer\Shell Folders"
-    )
-    dir, type = _winreg.QueryValueEx(key, shell_folder_name)
-    return dir
-
-
-def _get_win_folder_with_pywin32(csidl_name):
-    from win32com.shell import shellcon, shell
-    dir = shell.SHGetFolderPath(0, getattr(shellcon, csidl_name), 0, 0)
-    # Try to make this a unicode path because SHGetFolderPath does
-    # not return unicode strings when there is unicode data in the
-    # path.
-    try:
-        dir = unicode(dir)
-
-        # Downgrade to short path name if have highbit chars. See
-        # <http://bugs.activestate.com/show_bug.cgi?id=85099>.
-        has_high_char = False
-        for c in dir:
-            if ord(c) > 255:
-                has_high_char = True
-                break
-        if has_high_char:
-            try:
-                import win32api
-                dir = win32api.GetShortPathName(dir)
-            except ImportError:
-                pass
-    except UnicodeError:
-        pass
-    return dir
-
-
-def _get_win_folder_with_ctypes(csidl_name):
-    import ctypes
-
-    csidl_const = {
-        "CSIDL_APPDATA": 26,
-        "CSIDL_COMMON_APPDATA": 35,
-        "CSIDL_LOCAL_APPDATA": 28,
-    }[csidl_name]
-
-    buf = ctypes.create_unicode_buffer(1024)
-    ctypes.windll.shell32.SHGetFolderPathW(None, csidl_const, None, 0, buf)
-
-    # Downgrade to short path name if have highbit chars. See
-    # <http://bugs.activestate.com/show_bug.cgi?id=85099>.
-    has_high_char = False
-    for c in buf:
-        if ord(c) > 255:
-            has_high_char = True
-            break
-    if has_high_char:
-        buf2 = ctypes.create_unicode_buffer(1024)
-        if ctypes.windll.kernel32.GetShortPathNameW(buf.value, buf2, 1024):
-            buf = buf2
-
-    return buf.value
-
-def _get_win_folder_with_jna(csidl_name):
-    import array
-    from com.sun import jna
-    from com.sun.jna.platform import win32
-
-    buf_size = win32.WinDef.MAX_PATH * 2
-    buf = array.zeros('c', buf_size)
-    shell = win32.Shell32.INSTANCE
-    shell.SHGetFolderPath(None, getattr(win32.ShlObj, csidl_name), None, win32.ShlObj.SHGFP_TYPE_CURRENT, buf)
-    dir = jna.Native.toString(buf.tostring()).rstrip("\0")
-
-    # Downgrade to short path name if have highbit chars. See
-    # <http://bugs.activestate.com/show_bug.cgi?id=85099>.
-    has_high_char = False
-    for c in dir:
-        if ord(c) > 255:
-            has_high_char = True
-            break
-    if has_high_char:
-        buf = array.zeros('c', buf_size)
-        kernel = win32.Kernel32.INSTANCE
-        if kernel.GetShortPathName(dir, buf, buf_size):
-            dir = jna.Native.toString(buf.tostring()).rstrip("\0")
-
-    return dir
-
-if system == "win32":
-    try:
-        from ctypes import windll
-        _get_win_folder = _get_win_folder_with_ctypes
-    except ImportError:
-        try:
-            import com.sun.jna
-            _get_win_folder = _get_win_folder_with_jna
-        except ImportError:
-            _get_win_folder = _get_win_folder_from_registry
-
-
-#---- self test code
-
-if __name__ == "__main__":
-    appname = "MyApp"
-    appauthor = "MyCompany"
-
-    props = ("user_data_dir",
-             "user_config_dir",
-             "user_cache_dir",
-             "user_state_dir",
-             "user_log_dir",
-             "site_data_dir",
-             "site_config_dir")
-
-    print("-- app dirs %s --" % __version__)
-
-    print("-- app dirs (with optional 'version')")
-    dirs = AppDirs(appname, appauthor, version="1.0")
-    for prop in props:
-        print("%s: %s" % (prop, getattr(dirs, prop)))
-
-    print("\n-- app dirs (without optional 'version')")
-    dirs = AppDirs(appname, appauthor)
-    for prop in props:
-        print("%s: %s" % (prop, getattr(dirs, prop)))
-
-    print("\n-- app dirs (without optional 'appauthor')")
-    dirs = AppDirs(appname)
-    for prop in props:
-        print("%s: %s" % (prop, getattr(dirs, prop)))
-
-    print("\n-- app dirs (with disabled 'appauthor')")
-    dirs = AppDirs(appname, appauthor=False)
-    for prop in props:
-        print("%s: %s" % (prop, getattr(dirs, prop)))
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__init__.py
deleted file mode 100644
index 8fdee66..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__init__.py
+++ /dev/null
@@ -1,11 +0,0 @@
-"""CacheControl import Interface.
-
-Make it easy to import from cachecontrol without long namespaces.
-"""
-__author__ = "Eric Larson"
-__email__ = "eric@ionrock.org"
-__version__ = "0.12.5"
-
-from .wrapper import CacheControl
-from .adapter import CacheControlAdapter
-from .controller import CacheController
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 32f3e2c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/adapter.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/adapter.cpython-37.pyc
deleted file mode 100644
index 8ec155b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/adapter.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/cache.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/cache.cpython-37.pyc
deleted file mode 100644
index 3b39486..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/cache.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/compat.cpython-37.pyc
deleted file mode 100644
index 0cd12fb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/controller.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/controller.cpython-37.pyc
deleted file mode 100644
index 07de623..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/controller.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/filewrapper.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/filewrapper.cpython-37.pyc
deleted file mode 100644
index 50fda96..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/filewrapper.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/serialize.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/serialize.cpython-37.pyc
deleted file mode 100644
index ec38444..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/serialize.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/wrapper.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/wrapper.cpython-37.pyc
deleted file mode 100644
index c7db3b0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/__pycache__/wrapper.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/_cmd.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/_cmd.py
deleted file mode 100644
index f1e0ad9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/_cmd.py
+++ /dev/null
@@ -1,57 +0,0 @@
-import logging
-
-from pip._vendor import requests
-
-from pip._vendor.cachecontrol.adapter import CacheControlAdapter
-from pip._vendor.cachecontrol.cache import DictCache
-from pip._vendor.cachecontrol.controller import logger
-
-from argparse import ArgumentParser
-
-
-def setup_logging():
-    logger.setLevel(logging.DEBUG)
-    handler = logging.StreamHandler()
-    logger.addHandler(handler)
-
-
-def get_session():
-    adapter = CacheControlAdapter(
-        DictCache(), cache_etags=True, serializer=None, heuristic=None
-    )
-    sess = requests.Session()
-    sess.mount("http://", adapter)
-    sess.mount("https://", adapter)
-
-    sess.cache_controller = adapter.controller
-    return sess
-
-
-def get_args():
-    parser = ArgumentParser()
-    parser.add_argument("url", help="The URL to try and cache")
-    return parser.parse_args()
-
-
-def main(args=None):
-    args = get_args()
-    sess = get_session()
-
-    # Make a request to get a response
-    resp = sess.get(args.url)
-
-    # Turn on logging
-    setup_logging()
-
-    # try setting the cache
-    sess.cache_controller.cache_response(resp.request, resp.raw)
-
-    # Now try to get it
-    if sess.cache_controller.cached_request(resp.request):
-        print("Cached!")
-    else:
-        print("Not cached :(")
-
-
-if __name__ == "__main__":
-    main()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/adapter.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/adapter.py
deleted file mode 100644
index 780eb28..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/adapter.py
+++ /dev/null
@@ -1,133 +0,0 @@
-import types
-import functools
-import zlib
-
-from pip._vendor.requests.adapters import HTTPAdapter
-
-from .controller import CacheController
-from .cache import DictCache
-from .filewrapper import CallbackFileWrapper
-
-
-class CacheControlAdapter(HTTPAdapter):
-    invalidating_methods = {"PUT", "DELETE"}
-
-    def __init__(
-        self,
-        cache=None,
-        cache_etags=True,
-        controller_class=None,
-        serializer=None,
-        heuristic=None,
-        cacheable_methods=None,
-        *args,
-        **kw
-    ):
-        super(CacheControlAdapter, self).__init__(*args, **kw)
-        self.cache = cache or DictCache()
-        self.heuristic = heuristic
-        self.cacheable_methods = cacheable_methods or ("GET",)
-
-        controller_factory = controller_class or CacheController
-        self.controller = controller_factory(
-            self.cache, cache_etags=cache_etags, serializer=serializer
-        )
-
-    def send(self, request, cacheable_methods=None, **kw):
-        """
-        Send a request. Use the request information to see if it
-        exists in the cache and cache the response if we need to and can.
-        """
-        cacheable = cacheable_methods or self.cacheable_methods
-        if request.method in cacheable:
-            try:
-                cached_response = self.controller.cached_request(request)
-            except zlib.error:
-                cached_response = None
-            if cached_response:
-                return self.build_response(request, cached_response, from_cache=True)
-
-            # check for etags and add headers if appropriate
-            request.headers.update(self.controller.conditional_headers(request))
-
-        resp = super(CacheControlAdapter, self).send(request, **kw)
-
-        return resp
-
-    def build_response(
-        self, request, response, from_cache=False, cacheable_methods=None
-    ):
-        """
-        Build a response by making a request or using the cache.
-
-        This will end up calling send and returning a potentially
-        cached response
-        """
-        cacheable = cacheable_methods or self.cacheable_methods
-        if not from_cache and request.method in cacheable:
-            # Check for any heuristics that might update headers
-            # before trying to cache.
-            if self.heuristic:
-                response = self.heuristic.apply(response)
-
-            # apply any expiration heuristics
-            if response.status == 304:
-                # We must have sent an ETag request. This could mean
-                # that we've been expired already or that we simply
-                # have an etag. In either case, we want to try and
-                # update the cache if that is the case.
-                cached_response = self.controller.update_cached_response(
-                    request, response
-                )
-
-                if cached_response is not response:
-                    from_cache = True
-
-                # We are done with the server response, read a
-                # possible response body (compliant servers will
-                # not return one, but we cannot be 100% sure) and
-                # release the connection back to the pool.
-                response.read(decode_content=False)
-                response.release_conn()
-
-                response = cached_response
-
-            # We always cache the 301 responses
-            elif response.status == 301:
-                self.controller.cache_response(request, response)
-            else:
-                # Wrap the response file with a wrapper that will cache the
-                #   response when the stream has been consumed.
-                response._fp = CallbackFileWrapper(
-                    response._fp,
-                    functools.partial(
-                        self.controller.cache_response, request, response
-                    ),
-                )
-                if response.chunked:
-                    super_update_chunk_length = response._update_chunk_length
-
-                    def _update_chunk_length(self):
-                        super_update_chunk_length()
-                        if self.chunk_left == 0:
-                            self._fp._close()
-
-                    response._update_chunk_length = types.MethodType(
-                        _update_chunk_length, response
-                    )
-
-        resp = super(CacheControlAdapter, self).build_response(request, response)
-
-        # See if we should invalidate the cache.
-        if request.method in self.invalidating_methods and resp.ok:
-            cache_url = self.controller.cache_url(request.url)
-            self.cache.delete(cache_url)
-
-        # Give the request a from_cache attr to let people use it
-        resp.from_cache = from_cache
-
-        return resp
-
-    def close(self):
-        self.cache.close()
-        super(CacheControlAdapter, self).close()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/cache.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/cache.py
deleted file mode 100644
index 94e0773..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/cache.py
+++ /dev/null
@@ -1,39 +0,0 @@
-"""
-The cache object API for implementing caches. The default is a thread
-safe in-memory dictionary.
-"""
-from threading import Lock
-
-
-class BaseCache(object):
-
-    def get(self, key):
-        raise NotImplementedError()
-
-    def set(self, key, value):
-        raise NotImplementedError()
-
-    def delete(self, key):
-        raise NotImplementedError()
-
-    def close(self):
-        pass
-
-
-class DictCache(BaseCache):
-
-    def __init__(self, init_dict=None):
-        self.lock = Lock()
-        self.data = init_dict or {}
-
-    def get(self, key):
-        return self.data.get(key, None)
-
-    def set(self, key, value):
-        with self.lock:
-            self.data.update({key: value})
-
-    def delete(self, key):
-        with self.lock:
-            if key in self.data:
-                self.data.pop(key)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__init__.py
deleted file mode 100644
index 0e1658f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__init__.py
+++ /dev/null
@@ -1,2 +0,0 @@
-from .file_cache import FileCache  # noqa
-from .redis_cache import RedisCache  # noqa
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 204f42d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/file_cache.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/file_cache.cpython-37.pyc
deleted file mode 100644
index 3015df0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/file_cache.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/redis_cache.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/redis_cache.cpython-37.pyc
deleted file mode 100644
index 4ae5794..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/__pycache__/redis_cache.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/file_cache.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/file_cache.py
deleted file mode 100644
index 1ba0080..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/file_cache.py
+++ /dev/null
@@ -1,146 +0,0 @@
-import hashlib
-import os
-from textwrap import dedent
-
-from ..cache import BaseCache
-from ..controller import CacheController
-
-try:
-    FileNotFoundError
-except NameError:
-    # py2.X
-    FileNotFoundError = (IOError, OSError)
-
-
-def _secure_open_write(filename, fmode):
-    # We only want to write to this file, so open it in write only mode
-    flags = os.O_WRONLY
-
-    # os.O_CREAT | os.O_EXCL will fail if the file already exists, so we only
-    #  will open *new* files.
-    # We specify this because we want to ensure that the mode we pass is the
-    # mode of the file.
-    flags |= os.O_CREAT | os.O_EXCL
-
-    # Do not follow symlinks to prevent someone from making a symlink that
-    # we follow and insecurely open a cache file.
-    if hasattr(os, "O_NOFOLLOW"):
-        flags |= os.O_NOFOLLOW
-
-    # On Windows we'll mark this file as binary
-    if hasattr(os, "O_BINARY"):
-        flags |= os.O_BINARY
-
-    # Before we open our file, we want to delete any existing file that is
-    # there
-    try:
-        os.remove(filename)
-    except (IOError, OSError):
-        # The file must not exist already, so we can just skip ahead to opening
-        pass
-
-    # Open our file, the use of os.O_CREAT | os.O_EXCL will ensure that if a
-    # race condition happens between the os.remove and this line, that an
-    # error will be raised. Because we utilize a lockfile this should only
-    # happen if someone is attempting to attack us.
-    fd = os.open(filename, flags, fmode)
-    try:
-        return os.fdopen(fd, "wb")
-
-    except:
-        # An error occurred wrapping our FD in a file object
-        os.close(fd)
-        raise
-
-
-class FileCache(BaseCache):
-
-    def __init__(
-        self,
-        directory,
-        forever=False,
-        filemode=0o0600,
-        dirmode=0o0700,
-        use_dir_lock=None,
-        lock_class=None,
-    ):
-
-        if use_dir_lock is not None and lock_class is not None:
-            raise ValueError("Cannot use use_dir_lock and lock_class together")
-
-        try:
-            from pip._vendor.lockfile import LockFile
-            from pip._vendor.lockfile.mkdirlockfile import MkdirLockFile
-        except ImportError:
-            notice = dedent(
-                """
-            NOTE: In order to use the FileCache you must have
-            lockfile installed. You can install it via pip:
-              pip install lockfile
-            """
-            )
-            raise ImportError(notice)
-
-        else:
-            if use_dir_lock:
-                lock_class = MkdirLockFile
-
-            elif lock_class is None:
-                lock_class = LockFile
-
-        self.directory = directory
-        self.forever = forever
-        self.filemode = filemode
-        self.dirmode = dirmode
-        self.lock_class = lock_class
-
-    @staticmethod
-    def encode(x):
-        return hashlib.sha224(x.encode()).hexdigest()
-
-    def _fn(self, name):
-        # NOTE: This method should not change as some may depend on it.
-        #       See: https://github.com/ionrock/cachecontrol/issues/63
-        hashed = self.encode(name)
-        parts = list(hashed[:5]) + [hashed]
-        return os.path.join(self.directory, *parts)
-
-    def get(self, key):
-        name = self._fn(key)
-        try:
-            with open(name, "rb") as fh:
-                return fh.read()
-
-        except FileNotFoundError:
-            return None
-
-    def set(self, key, value):
-        name = self._fn(key)
-
-        # Make sure the directory exists
-        try:
-            os.makedirs(os.path.dirname(name), self.dirmode)
-        except (IOError, OSError):
-            pass
-
-        with self.lock_class(name) as lock:
-            # Write our actual file
-            with _secure_open_write(lock.path, self.filemode) as fh:
-                fh.write(value)
-
-    def delete(self, key):
-        name = self._fn(key)
-        if not self.forever:
-            try:
-                os.remove(name)
-            except FileNotFoundError:
-                pass
-
-
-def url_to_file_path(url, filecache):
-    """Return the file cache path based on the URL.
-
-    This does not ensure the file exists!
-    """
-    key = CacheController.cache_url(url)
-    return filecache._fn(key)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/redis_cache.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/redis_cache.py
deleted file mode 100644
index ed705ce..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/caches/redis_cache.py
+++ /dev/null
@@ -1,33 +0,0 @@
-from __future__ import division
-
-from datetime import datetime
-from pip._vendor.cachecontrol.cache import BaseCache
-
-
-class RedisCache(BaseCache):
-
-    def __init__(self, conn):
-        self.conn = conn
-
-    def get(self, key):
-        return self.conn.get(key)
-
-    def set(self, key, value, expires=None):
-        if not expires:
-            self.conn.set(key, value)
-        else:
-            expires = expires - datetime.utcnow()
-            self.conn.setex(key, int(expires.total_seconds()), value)
-
-    def delete(self, key):
-        self.conn.delete(key)
-
-    def clear(self):
-        """Helper for clearing all the keys in a database. Use with
-        caution!"""
-        for key in self.conn.keys():
-            self.conn.delete(key)
-
-    def close(self):
-        """Redis uses connection pooling, no need to close the connection."""
-        pass
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/compat.py
deleted file mode 100644
index 33b5aed..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/compat.py
+++ /dev/null
@@ -1,29 +0,0 @@
-try:
-    from urllib.parse import urljoin
-except ImportError:
-    from urlparse import urljoin
-
-
-try:
-    import cPickle as pickle
-except ImportError:
-    import pickle
-
-
-# Handle the case where the requests module has been patched to not have
-# urllib3 bundled as part of its source.
-try:
-    from pip._vendor.requests.packages.urllib3.response import HTTPResponse
-except ImportError:
-    from pip._vendor.urllib3.response import HTTPResponse
-
-try:
-    from pip._vendor.requests.packages.urllib3.util import is_fp_closed
-except ImportError:
-    from pip._vendor.urllib3.util import is_fp_closed
-
-# Replicate some six behaviour
-try:
-    text_type = unicode
-except NameError:
-    text_type = str
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/controller.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/controller.py
deleted file mode 100644
index 1b2b943..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/controller.py
+++ /dev/null
@@ -1,367 +0,0 @@
-"""
-The httplib2 algorithms ported for use with requests.
-"""
-import logging
-import re
-import calendar
-import time
-from email.utils import parsedate_tz
-
-from pip._vendor.requests.structures import CaseInsensitiveDict
-
-from .cache import DictCache
-from .serialize import Serializer
-
-
-logger = logging.getLogger(__name__)
-
-URI = re.compile(r"^(([^:/?#]+):)?(//([^/?#]*))?([^?#]*)(\?([^#]*))?(#(.*))?")
-
-
-def parse_uri(uri):
-    """Parses a URI using the regex given in Appendix B of RFC 3986.
-
-        (scheme, authority, path, query, fragment) = parse_uri(uri)
-    """
-    groups = URI.match(uri).groups()
-    return (groups[1], groups[3], groups[4], groups[6], groups[8])
-
-
-class CacheController(object):
-    """An interface to see if request should cached or not.
-    """
-
-    def __init__(
-        self, cache=None, cache_etags=True, serializer=None, status_codes=None
-    ):
-        self.cache = cache or DictCache()
-        self.cache_etags = cache_etags
-        self.serializer = serializer or Serializer()
-        self.cacheable_status_codes = status_codes or (200, 203, 300, 301)
-
-    @classmethod
-    def _urlnorm(cls, uri):
-        """Normalize the URL to create a safe key for the cache"""
-        (scheme, authority, path, query, fragment) = parse_uri(uri)
-        if not scheme or not authority:
-            raise Exception("Only absolute URIs are allowed. uri = %s" % uri)
-
-        scheme = scheme.lower()
-        authority = authority.lower()
-
-        if not path:
-            path = "/"
-
-        # Could do syntax based normalization of the URI before
-        # computing the digest. See Section 6.2.2 of Std 66.
-        request_uri = query and "?".join([path, query]) or path
-        defrag_uri = scheme + "://" + authority + request_uri
-
-        return defrag_uri
-
-    @classmethod
-    def cache_url(cls, uri):
-        return cls._urlnorm(uri)
-
-    def parse_cache_control(self, headers):
-        known_directives = {
-            # https://tools.ietf.org/html/rfc7234#section-5.2
-            "max-age": (int, True),
-            "max-stale": (int, False),
-            "min-fresh": (int, True),
-            "no-cache": (None, False),
-            "no-store": (None, False),
-            "no-transform": (None, False),
-            "only-if-cached": (None, False),
-            "must-revalidate": (None, False),
-            "public": (None, False),
-            "private": (None, False),
-            "proxy-revalidate": (None, False),
-            "s-maxage": (int, True),
-        }
-
-        cc_headers = headers.get("cache-control", headers.get("Cache-Control", ""))
-
-        retval = {}
-
-        for cc_directive in cc_headers.split(","):
-            if not cc_directive.strip():
-                continue
-
-            parts = cc_directive.split("=", 1)
-            directive = parts[0].strip()
-
-            try:
-                typ, required = known_directives[directive]
-            except KeyError:
-                logger.debug("Ignoring unknown cache-control directive: %s", directive)
-                continue
-
-            if not typ or not required:
-                retval[directive] = None
-            if typ:
-                try:
-                    retval[directive] = typ(parts[1].strip())
-                except IndexError:
-                    if required:
-                        logger.debug(
-                            "Missing value for cache-control " "directive: %s",
-                            directive,
-                        )
-                except ValueError:
-                    logger.debug(
-                        "Invalid value for cache-control directive " "%s, must be %s",
-                        directive,
-                        typ.__name__,
-                    )
-
-        return retval
-
-    def cached_request(self, request):
-        """
-        Return a cached response if it exists in the cache, otherwise
-        return False.
-        """
-        cache_url = self.cache_url(request.url)
-        logger.debug('Looking up "%s" in the cache', cache_url)
-        cc = self.parse_cache_control(request.headers)
-
-        # Bail out if the request insists on fresh data
-        if "no-cache" in cc:
-            logger.debug('Request header has "no-cache", cache bypassed')
-            return False
-
-        if "max-age" in cc and cc["max-age"] == 0:
-            logger.debug('Request header has "max_age" as 0, cache bypassed')
-            return False
-
-        # Request allows serving from the cache, let's see if we find something
-        cache_data = self.cache.get(cache_url)
-        if cache_data is None:
-            logger.debug("No cache entry available")
-            return False
-
-        # Check whether it can be deserialized
-        resp = self.serializer.loads(request, cache_data)
-        if not resp:
-            logger.warning("Cache entry deserialization failed, entry ignored")
-            return False
-
-        # If we have a cached 301, return it immediately. We don't
-        # need to test our response for other headers b/c it is
-        # intrinsically "cacheable" as it is Permanent.
-        # See:
-        #   https://tools.ietf.org/html/rfc7231#section-6.4.2
-        #
-        # Client can try to refresh the value by repeating the request
-        # with cache busting headers as usual (ie no-cache).
-        if resp.status == 301:
-            msg = (
-                'Returning cached "301 Moved Permanently" response '
-                "(ignoring date and etag information)"
-            )
-            logger.debug(msg)
-            return resp
-
-        headers = CaseInsensitiveDict(resp.headers)
-        if not headers or "date" not in headers:
-            if "etag" not in headers:
-                # Without date or etag, the cached response can never be used
-                # and should be deleted.
-                logger.debug("Purging cached response: no date or etag")
-                self.cache.delete(cache_url)
-            logger.debug("Ignoring cached response: no date")
-            return False
-
-        now = time.time()
-        date = calendar.timegm(parsedate_tz(headers["date"]))
-        current_age = max(0, now - date)
-        logger.debug("Current age based on date: %i", current_age)
-
-        # TODO: There is an assumption that the result will be a
-        #       urllib3 response object. This may not be best since we
-        #       could probably avoid instantiating or constructing the
-        #       response until we know we need it.
-        resp_cc = self.parse_cache_control(headers)
-
-        # determine freshness
-        freshness_lifetime = 0
-
-        # Check the max-age pragma in the cache control header
-        if "max-age" in resp_cc:
-            freshness_lifetime = resp_cc["max-age"]
-            logger.debug("Freshness lifetime from max-age: %i", freshness_lifetime)
-
-        # If there isn't a max-age, check for an expires header
-        elif "expires" in headers:
-            expires = parsedate_tz(headers["expires"])
-            if expires is not None:
-                expire_time = calendar.timegm(expires) - date
-                freshness_lifetime = max(0, expire_time)
-                logger.debug("Freshness lifetime from expires: %i", freshness_lifetime)
-
-        # Determine if we are setting freshness limit in the
-        # request. Note, this overrides what was in the response.
-        if "max-age" in cc:
-            freshness_lifetime = cc["max-age"]
-            logger.debug(
-                "Freshness lifetime from request max-age: %i", freshness_lifetime
-            )
-
-        if "min-fresh" in cc:
-            min_fresh = cc["min-fresh"]
-            # adjust our current age by our min fresh
-            current_age += min_fresh
-            logger.debug("Adjusted current age from min-fresh: %i", current_age)
-
-        # Return entry if it is fresh enough
-        if freshness_lifetime > current_age:
-            logger.debug('The response is "fresh", returning cached response')
-            logger.debug("%i > %i", freshness_lifetime, current_age)
-            return resp
-
-        # we're not fresh. If we don't have an Etag, clear it out
-        if "etag" not in headers:
-            logger.debug('The cached response is "stale" with no etag, purging')
-            self.cache.delete(cache_url)
-
-        # return the original handler
-        return False
-
-    def conditional_headers(self, request):
-        cache_url = self.cache_url(request.url)
-        resp = self.serializer.loads(request, self.cache.get(cache_url))
-        new_headers = {}
-
-        if resp:
-            headers = CaseInsensitiveDict(resp.headers)
-
-            if "etag" in headers:
-                new_headers["If-None-Match"] = headers["ETag"]
-
-            if "last-modified" in headers:
-                new_headers["If-Modified-Since"] = headers["Last-Modified"]
-
-        return new_headers
-
-    def cache_response(self, request, response, body=None, status_codes=None):
-        """
-        Algorithm for caching requests.
-
-        This assumes a requests Response object.
-        """
-        # From httplib2: Don't cache 206's since we aren't going to
-        #                handle byte range requests
-        cacheable_status_codes = status_codes or self.cacheable_status_codes
-        if response.status not in cacheable_status_codes:
-            logger.debug(
-                "Status code %s not in %s", response.status, cacheable_status_codes
-            )
-            return
-
-        response_headers = CaseInsensitiveDict(response.headers)
-
-        # If we've been given a body, our response has a Content-Length, that
-        # Content-Length is valid then we can check to see if the body we've
-        # been given matches the expected size, and if it doesn't we'll just
-        # skip trying to cache it.
-        if (
-            body is not None
-            and "content-length" in response_headers
-            and response_headers["content-length"].isdigit()
-            and int(response_headers["content-length"]) != len(body)
-        ):
-            return
-
-        cc_req = self.parse_cache_control(request.headers)
-        cc = self.parse_cache_control(response_headers)
-
-        cache_url = self.cache_url(request.url)
-        logger.debug('Updating cache with response from "%s"', cache_url)
-
-        # Delete it from the cache if we happen to have it stored there
-        no_store = False
-        if "no-store" in cc:
-            no_store = True
-            logger.debug('Response header has "no-store"')
-        if "no-store" in cc_req:
-            no_store = True
-            logger.debug('Request header has "no-store"')
-        if no_store and self.cache.get(cache_url):
-            logger.debug('Purging existing cache entry to honor "no-store"')
-            self.cache.delete(cache_url)
-        if no_store:
-            return
-
-        # If we've been given an etag, then keep the response
-        if self.cache_etags and "etag" in response_headers:
-            logger.debug("Caching due to etag")
-            self.cache.set(
-                cache_url, self.serializer.dumps(request, response, body=body)
-            )
-
-        # Add to the cache any 301s. We do this before looking that
-        # the Date headers.
-        elif response.status == 301:
-            logger.debug("Caching permanant redirect")
-            self.cache.set(cache_url, self.serializer.dumps(request, response))
-
-        # Add to the cache if the response headers demand it. If there
-        # is no date header then we can't do anything about expiring
-        # the cache.
-        elif "date" in response_headers:
-            # cache when there is a max-age > 0
-            if "max-age" in cc and cc["max-age"] > 0:
-                logger.debug("Caching b/c date exists and max-age > 0")
-                self.cache.set(
-                    cache_url, self.serializer.dumps(request, response, body=body)
-                )
-
-            # If the request can expire, it means we should cache it
-            # in the meantime.
-            elif "expires" in response_headers:
-                if response_headers["expires"]:
-                    logger.debug("Caching b/c of expires header")
-                    self.cache.set(
-                        cache_url, self.serializer.dumps(request, response, body=body)
-                    )
-
-    def update_cached_response(self, request, response):
-        """On a 304 we will get a new set of headers that we want to
-        update our cached value with, assuming we have one.
-
-        This should only ever be called when we've sent an ETag and
-        gotten a 304 as the response.
-        """
-        cache_url = self.cache_url(request.url)
-
-        cached_response = self.serializer.loads(request, self.cache.get(cache_url))
-
-        if not cached_response:
-            # we didn't have a cached response
-            return response
-
-        # Lets update our headers with the headers from the new request:
-        # http://tools.ietf.org/html/draft-ietf-httpbis-p4-conditional-26#section-4.1
-        #
-        # The server isn't supposed to send headers that would make
-        # the cached body invalid. But... just in case, we'll be sure
-        # to strip out ones we know that might be problmatic due to
-        # typical assumptions.
-        excluded_headers = ["content-length"]
-
-        cached_response.headers.update(
-            dict(
-                (k, v)
-                for k, v in response.headers.items()
-                if k.lower() not in excluded_headers
-            )
-        )
-
-        # we want a 200 b/c we have content via the cache
-        cached_response.status = 200
-
-        # update our cache
-        self.cache.set(cache_url, self.serializer.dumps(request, cached_response))
-
-        return cached_response
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/filewrapper.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/filewrapper.py
deleted file mode 100644
index 30ed4c5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/filewrapper.py
+++ /dev/null
@@ -1,80 +0,0 @@
-from io import BytesIO
-
-
-class CallbackFileWrapper(object):
-    """
-    Small wrapper around a fp object which will tee everything read into a
-    buffer, and when that file is closed it will execute a callback with the
-    contents of that buffer.
-
-    All attributes are proxied to the underlying file object.
-
-    This class uses members with a double underscore (__) leading prefix so as
-    not to accidentally shadow an attribute.
-    """
-
-    def __init__(self, fp, callback):
-        self.__buf = BytesIO()
-        self.__fp = fp
-        self.__callback = callback
-
-    def __getattr__(self, name):
-        # The vaguaries of garbage collection means that self.__fp is
-        # not always set.  By using __getattribute__ and the private
-        # name[0] allows looking up the attribute value and raising an
-        # AttributeError when it doesn't exist. This stop thigns from
-        # infinitely recursing calls to getattr in the case where
-        # self.__fp hasn't been set.
-        #
-        # [0] https://docs.python.org/2/reference/expressions.html#atom-identifiers
-        fp = self.__getattribute__("_CallbackFileWrapper__fp")
-        return getattr(fp, name)
-
-    def __is_fp_closed(self):
-        try:
-            return self.__fp.fp is None
-
-        except AttributeError:
-            pass
-
-        try:
-            return self.__fp.closed
-
-        except AttributeError:
-            pass
-
-        # We just don't cache it then.
-        # TODO: Add some logging here...
-        return False
-
-    def _close(self):
-        if self.__callback:
-            self.__callback(self.__buf.getvalue())
-
-        # We assign this to None here, because otherwise we can get into
-        # really tricky problems where the CPython interpreter dead locks
-        # because the callback is holding a reference to something which
-        # has a __del__ method. Setting this to None breaks the cycle
-        # and allows the garbage collector to do it's thing normally.
-        self.__callback = None
-
-    def read(self, amt=None):
-        data = self.__fp.read(amt)
-        self.__buf.write(data)
-        if self.__is_fp_closed():
-            self._close()
-
-        return data
-
-    def _safe_read(self, amt):
-        data = self.__fp._safe_read(amt)
-        if amt == 2 and data == b"\r\n":
-            # urllib executes this read to toss the CRLF at the end
-            # of the chunk.
-            return data
-
-        self.__buf.write(data)
-        if self.__is_fp_closed():
-            self._close()
-
-        return data
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/heuristics.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/heuristics.py
deleted file mode 100644
index 6c0e979..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/heuristics.py
+++ /dev/null
@@ -1,135 +0,0 @@
-import calendar
-import time
-
-from email.utils import formatdate, parsedate, parsedate_tz
-
-from datetime import datetime, timedelta
-
-TIME_FMT = "%a, %d %b %Y %H:%M:%S GMT"
-
-
-def expire_after(delta, date=None):
-    date = date or datetime.utcnow()
-    return date + delta
-
-
-def datetime_to_header(dt):
-    return formatdate(calendar.timegm(dt.timetuple()))
-
-
-class BaseHeuristic(object):
-
-    def warning(self, response):
-        """
-        Return a valid 1xx warning header value describing the cache
-        adjustments.
-
-        The response is provided too allow warnings like 113
-        http://tools.ietf.org/html/rfc7234#section-5.5.4 where we need
-        to explicitly say response is over 24 hours old.
-        """
-        return '110 - "Response is Stale"'
-
-    def update_headers(self, response):
-        """Update the response headers with any new headers.
-
-        NOTE: This SHOULD always include some Warning header to
-              signify that the response was cached by the client, not
-              by way of the provided headers.
-        """
-        return {}
-
-    def apply(self, response):
-        updated_headers = self.update_headers(response)
-
-        if updated_headers:
-            response.headers.update(updated_headers)
-            warning_header_value = self.warning(response)
-            if warning_header_value is not None:
-                response.headers.update({"Warning": warning_header_value})
-
-        return response
-
-
-class OneDayCache(BaseHeuristic):
-    """
-    Cache the response by providing an expires 1 day in the
-    future.
-    """
-
-    def update_headers(self, response):
-        headers = {}
-
-        if "expires" not in response.headers:
-            date = parsedate(response.headers["date"])
-            expires = expire_after(timedelta(days=1), date=datetime(*date[:6]))
-            headers["expires"] = datetime_to_header(expires)
-            headers["cache-control"] = "public"
-        return headers
-
-
-class ExpiresAfter(BaseHeuristic):
-    """
-    Cache **all** requests for a defined time period.
-    """
-
-    def __init__(self, **kw):
-        self.delta = timedelta(**kw)
-
-    def update_headers(self, response):
-        expires = expire_after(self.delta)
-        return {"expires": datetime_to_header(expires), "cache-control": "public"}
-
-    def warning(self, response):
-        tmpl = "110 - Automatically cached for %s. Response might be stale"
-        return tmpl % self.delta
-
-
-class LastModified(BaseHeuristic):
-    """
-    If there is no Expires header already, fall back on Last-Modified
-    using the heuristic from
-    http://tools.ietf.org/html/rfc7234#section-4.2.2
-    to calculate a reasonable value.
-
-    Firefox also does something like this per
-    https://developer.mozilla.org/en-US/docs/Web/HTTP/Caching_FAQ
-    http://lxr.mozilla.org/mozilla-release/source/netwerk/protocol/http/nsHttpResponseHead.cpp#397
-    Unlike mozilla we limit this to 24-hr.
-    """
-    cacheable_by_default_statuses = {
-        200, 203, 204, 206, 300, 301, 404, 405, 410, 414, 501
-    }
-
-    def update_headers(self, resp):
-        headers = resp.headers
-
-        if "expires" in headers:
-            return {}
-
-        if "cache-control" in headers and headers["cache-control"] != "public":
-            return {}
-
-        if resp.status not in self.cacheable_by_default_statuses:
-            return {}
-
-        if "date" not in headers or "last-modified" not in headers:
-            return {}
-
-        date = calendar.timegm(parsedate_tz(headers["date"]))
-        last_modified = parsedate(headers["last-modified"])
-        if date is None or last_modified is None:
-            return {}
-
-        now = time.time()
-        current_age = max(0, now - date)
-        delta = date - calendar.timegm(last_modified)
-        freshness_lifetime = max(0, min(delta / 10, 24 * 3600))
-        if freshness_lifetime <= current_age:
-            return {}
-
-        expires = date + freshness_lifetime
-        return {"expires": time.strftime(TIME_FMT, time.gmtime(expires))}
-
-    def warning(self, resp):
-        return None
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/serialize.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/serialize.py
deleted file mode 100644
index ec43ff2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/serialize.py
+++ /dev/null
@@ -1,186 +0,0 @@
-import base64
-import io
-import json
-import zlib
-
-from pip._vendor import msgpack
-from pip._vendor.requests.structures import CaseInsensitiveDict
-
-from .compat import HTTPResponse, pickle, text_type
-
-
-def _b64_decode_bytes(b):
-    return base64.b64decode(b.encode("ascii"))
-
-
-def _b64_decode_str(s):
-    return _b64_decode_bytes(s).decode("utf8")
-
-
-class Serializer(object):
-
-    def dumps(self, request, response, body=None):
-        response_headers = CaseInsensitiveDict(response.headers)
-
-        if body is None:
-            body = response.read(decode_content=False)
-
-            # NOTE: 99% sure this is dead code. I'm only leaving it
-            #       here b/c I don't have a test yet to prove
-            #       it. Basically, before using
-            #       `cachecontrol.filewrapper.CallbackFileWrapper`,
-            #       this made an effort to reset the file handle. The
-            #       `CallbackFileWrapper` short circuits this code by
-            #       setting the body as the content is consumed, the
-            #       result being a `body` argument is *always* passed
-            #       into cache_response, and in turn,
-            #       `Serializer.dump`.
-            response._fp = io.BytesIO(body)
-
-        # NOTE: This is all a bit weird, but it's really important that on
-        #       Python 2.x these objects are unicode and not str, even when
-        #       they contain only ascii. The problem here is that msgpack
-        #       understands the difference between unicode and bytes and we
-        #       have it set to differentiate between them, however Python 2
-        #       doesn't know the difference. Forcing these to unicode will be
-        #       enough to have msgpack know the difference.
-        data = {
-            u"response": {
-                u"body": body,
-                u"headers": dict(
-                    (text_type(k), text_type(v)) for k, v in response.headers.items()
-                ),
-                u"status": response.status,
-                u"version": response.version,
-                u"reason": text_type(response.reason),
-                u"strict": response.strict,
-                u"decode_content": response.decode_content,
-            }
-        }
-
-        # Construct our vary headers
-        data[u"vary"] = {}
-        if u"vary" in response_headers:
-            varied_headers = response_headers[u"vary"].split(",")
-            for header in varied_headers:
-                header = text_type(header).strip()
-                header_value = request.headers.get(header, None)
-                if header_value is not None:
-                    header_value = text_type(header_value)
-                data[u"vary"][header] = header_value
-
-        return b",".join([b"cc=4", msgpack.dumps(data, use_bin_type=True)])
-
-    def loads(self, request, data):
-        # Short circuit if we've been given an empty set of data
-        if not data:
-            return
-
-        # Determine what version of the serializer the data was serialized
-        # with
-        try:
-            ver, data = data.split(b",", 1)
-        except ValueError:
-            ver = b"cc=0"
-
-        # Make sure that our "ver" is actually a version and isn't a false
-        # positive from a , being in the data stream.
-        if ver[:3] != b"cc=":
-            data = ver + data
-            ver = b"cc=0"
-
-        # Get the version number out of the cc=N
-        ver = ver.split(b"=", 1)[-1].decode("ascii")
-
-        # Dispatch to the actual load method for the given version
-        try:
-            return getattr(self, "_loads_v{}".format(ver))(request, data)
-
-        except AttributeError:
-            # This is a version we don't have a loads function for, so we'll
-            # just treat it as a miss and return None
-            return
-
-    def prepare_response(self, request, cached):
-        """Verify our vary headers match and construct a real urllib3
-        HTTPResponse object.
-        """
-        # Special case the '*' Vary value as it means we cannot actually
-        # determine if the cached response is suitable for this request.
-        if "*" in cached.get("vary", {}):
-            return
-
-        # Ensure that the Vary headers for the cached response match our
-        # request
-        for header, value in cached.get("vary", {}).items():
-            if request.headers.get(header, None) != value:
-                return
-
-        body_raw = cached["response"].pop("body")
-
-        headers = CaseInsensitiveDict(data=cached["response"]["headers"])
-        if headers.get("transfer-encoding", "") == "chunked":
-            headers.pop("transfer-encoding")
-
-        cached["response"]["headers"] = headers
-
-        try:
-            body = io.BytesIO(body_raw)
-        except TypeError:
-            # This can happen if cachecontrol serialized to v1 format (pickle)
-            # using Python 2. A Python 2 str(byte string) will be unpickled as
-            # a Python 3 str (unicode string), which will cause the above to
-            # fail with:
-            #
-            #     TypeError: 'str' does not support the buffer interface
-            body = io.BytesIO(body_raw.encode("utf8"))
-
-        return HTTPResponse(body=body, preload_content=False, **cached["response"])
-
-    def _loads_v0(self, request, data):
-        # The original legacy cache data. This doesn't contain enough
-        # information to construct everything we need, so we'll treat this as
-        # a miss.
-        return
-
-    def _loads_v1(self, request, data):
-        try:
-            cached = pickle.loads(data)
-        except ValueError:
-            return
-
-        return self.prepare_response(request, cached)
-
-    def _loads_v2(self, request, data):
-        try:
-            cached = json.loads(zlib.decompress(data).decode("utf8"))
-        except (ValueError, zlib.error):
-            return
-
-        # We need to decode the items that we've base64 encoded
-        cached["response"]["body"] = _b64_decode_bytes(cached["response"]["body"])
-        cached["response"]["headers"] = dict(
-            (_b64_decode_str(k), _b64_decode_str(v))
-            for k, v in cached["response"]["headers"].items()
-        )
-        cached["response"]["reason"] = _b64_decode_str(cached["response"]["reason"])
-        cached["vary"] = dict(
-            (_b64_decode_str(k), _b64_decode_str(v) if v is not None else v)
-            for k, v in cached["vary"].items()
-        )
-
-        return self.prepare_response(request, cached)
-
-    def _loads_v3(self, request, data):
-        # Due to Python 2 encoding issues, it's impossible to know for sure
-        # exactly how to load v3 entries, thus we'll treat these as a miss so
-        # that they get rewritten out as v4 entries.
-        return
-
-    def _loads_v4(self, request, data):
-        try:
-            cached = msgpack.loads(data, encoding="utf-8")
-        except ValueError:
-            return
-
-        return self.prepare_response(request, cached)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/wrapper.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/wrapper.py
deleted file mode 100644
index 265bfc8..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/cachecontrol/wrapper.py
+++ /dev/null
@@ -1,29 +0,0 @@
-from .adapter import CacheControlAdapter
-from .cache import DictCache
-
-
-def CacheControl(
-    sess,
-    cache=None,
-    cache_etags=True,
-    serializer=None,
-    heuristic=None,
-    controller_class=None,
-    adapter_class=None,
-    cacheable_methods=None,
-):
-
-    cache = cache or DictCache()
-    adapter_class = adapter_class or CacheControlAdapter
-    adapter = adapter_class(
-        cache,
-        cache_etags=cache_etags,
-        serializer=serializer,
-        heuristic=heuristic,
-        controller_class=controller_class,
-        cacheable_methods=cacheable_methods,
-    )
-    sess.mount("http://", adapter)
-    sess.mount("https://", adapter)
-
-    return sess
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__init__.py
deleted file mode 100644
index ef71f3a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__init__.py
+++ /dev/null
@@ -1,3 +0,0 @@
-from .core import where
-
-__version__ = "2018.11.29"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__main__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__main__.py
deleted file mode 100644
index ae2aff5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__main__.py
+++ /dev/null
@@ -1,2 +0,0 @@
-from pip._vendor.certifi import where
-print(where())
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 0a7b8cb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__pycache__/core.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__pycache__/core.cpython-37.pyc
deleted file mode 100644
index 8a3c613..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/__pycache__/core.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/cacert.pem b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/cacert.pem
deleted file mode 100644
index db68797..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/cacert.pem
+++ /dev/null
@@ -1,4512 +0,0 @@
-
-# Issuer: CN=GlobalSign Root CA O=GlobalSign nv-sa OU=Root CA
-# Subject: CN=GlobalSign Root CA O=GlobalSign nv-sa OU=Root CA
-# Label: "GlobalSign Root CA"
-# Serial: 4835703278459707669005204
-# MD5 Fingerprint: 3e:45:52:15:09:51:92:e1:b7:5d:37:9f:b1:87:29:8a
-# SHA1 Fingerprint: b1:bc:96:8b:d4:f4:9d:62:2a:a8:9a:81:f2:15:01:52:a4:1d:82:9c
-# SHA256 Fingerprint: eb:d4:10:40:e4:bb:3e:c7:42:c9:e3:81:d3:1e:f2:a4:1a:48:b6:68:5c:96:e7:ce:f3:c1:df:6c:d4:33:1c:99
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=GlobalSign O=GlobalSign OU=GlobalSign Root CA - R2
-# Subject: CN=GlobalSign O=GlobalSign OU=GlobalSign Root CA - R2
-# Label: "GlobalSign Root CA - R2"
-# Serial: 4835703278459682885658125
-# MD5 Fingerprint: 94:14:77:7e:3e:5e:fd:8f:30:bd:41:b0:cf:e7:d0:30
-# SHA1 Fingerprint: 75:e0:ab:b6:13:85:12:27:1c:04:f8:5f:dd:de:38:e4:b7:24:2e:fe
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=VeriSign Class 3 Public Primary Certification Authority - G3 O=VeriSign, Inc. OU=VeriSign Trust Network/(c) 1999 VeriSign, Inc. - For authorized use only
-# Subject: CN=VeriSign Class 3 Public Primary Certification Authority - G3 O=VeriSign, Inc. OU=VeriSign Trust Network/(c) 1999 VeriSign, Inc. - For authorized use only
-# Label: "Verisign Class 3 Public Primary Certification Authority - G3"
-# Serial: 206684696279472310254277870180966723415
-# MD5 Fingerprint: cd:68:b6:a7:c7:c4:ce:75:e0:1d:4f:57:44:61:92:09
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Entrust.net Certification Authority (2048) O=Entrust.net OU=www.entrust.net/CPS_2048 incorp. by ref. (limits liab.)/(c) 1999 Entrust.net Limited
-# Subject: CN=Entrust.net Certification Authority (2048) O=Entrust.net OU=www.entrust.net/CPS_2048 incorp. by ref. (limits liab.)/(c) 1999 Entrust.net Limited
-# Label: "Entrust.net Premium 2048 Secure Server CA"
-# Serial: 946069240
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Baltimore CyberTrust Root O=Baltimore OU=CyberTrust
-# Subject: CN=Baltimore CyberTrust Root O=Baltimore OU=CyberTrust
-# Label: "Baltimore CyberTrust Root"
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-# Issuer: CN=Entrust Root Certification Authority O=Entrust, Inc. OU=www.entrust.net/CPS is incorporated by reference/(c) 2006 Entrust, Inc.
-# Subject: CN=Entrust Root Certification Authority O=Entrust, Inc. OU=www.entrust.net/CPS is incorporated by reference/(c) 2006 Entrust, Inc.
-# Label: "Entrust Root Certification Authority"
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=GeoTrust Global CA O=GeoTrust Inc.
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-# Issuer: CN=AAA Certificate Services O=Comodo CA Limited
-# Subject: CN=AAA Certificate Services O=Comodo CA Limited
-# Label: "Comodo AAA Services root"
-# Serial: 1
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------END CERTIFICATE-----
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-# Issuer: CN=QuoVadis Root Certification Authority O=QuoVadis Limited OU=Root Certification Authority
-# Subject: CN=QuoVadis Root Certification Authority O=QuoVadis Limited OU=Root Certification Authority
-# Label: "QuoVadis Root CA"
-# Serial: 985026699
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=QuoVadis Root CA 2 O=QuoVadis Limited
-# Subject: CN=QuoVadis Root CA 2 O=QuoVadis Limited
-# Label: "QuoVadis Root CA 2"
-# Serial: 1289
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=QuoVadis Root CA 3 O=QuoVadis Limited
-# Subject: CN=QuoVadis Root CA 3 O=QuoVadis Limited
-# Label: "QuoVadis Root CA 3"
-# Serial: 1478
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: O=SECOM Trust.net OU=Security Communication RootCA1
-# Subject: O=SECOM Trust.net OU=Security Communication RootCA1
-# Label: "Security Communication Root CA"
-# Serial: 0
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------BEGIN CERTIFICATE-----
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-# Subject: CN=Sonera Class2 CA O=Sonera
-# Label: "Sonera Class 2 Root CA"
-# Serial: 29
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-# Issuer: O=The Go Daddy Group, Inc. OU=Go Daddy Class 2 Certification Authority
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-# Issuer: O=Government Root Certification Authority
-# Subject: O=Government Root Certification Authority
-# Label: "Taiwan GRCA"
-# Serial: 42023070807708724159991140556527066870
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-# Issuer: CN=DigiCert Assured ID Root CA O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert Assured ID Root CA O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert Assured ID Root CA"
-# Serial: 17154717934120587862167794914071425081
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=DigiCert Global Root CA O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert Global Root CA O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert Global Root CA"
-# Serial: 10944719598952040374951832963794454346
-# MD5 Fingerprint: 79:e4:a9:84:0d:7d:3a:96:d7:c0:4f:e2:43:4c:89:2e
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=DigiCert High Assurance EV Root CA O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert High Assurance EV Root CA O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert High Assurance EV Root CA"
-# Serial: 3553400076410547919724730734378100087
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Class 2 Primary CA O=Certplus
-# Subject: CN=Class 2 Primary CA O=Certplus
-# Label: "Certplus Class 2 Primary CA"
-# Serial: 177770208045934040241468760488327595043
-# MD5 Fingerprint: 88:2c:8c:52:b8:a2:3c:f3:f7:bb:03:ea:ae:ac:42:0b
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=DST Root CA X3 O=Digital Signature Trust Co.
-# Subject: CN=DST Root CA X3 O=Digital Signature Trust Co.
-# Label: "DST Root CA X3"
-# Serial: 91299735575339953335919266965803778155
-# MD5 Fingerprint: 41:03:52:dc:0f:f7:50:1b:16:f0:02:8e:ba:6f:45:c5
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=SwissSign Gold CA - G2 O=SwissSign AG
-# Subject: CN=SwissSign Gold CA - G2 O=SwissSign AG
-# Label: "SwissSign Gold CA - G2"
-# Serial: 13492815561806991280
-# MD5 Fingerprint: 24:77:d9:a8:91:d1:3b:fa:88:2d:c2:ff:f8:cd:33:93
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=SwissSign Silver CA - G2 O=SwissSign AG
-# Subject: CN=SwissSign Silver CA - G2 O=SwissSign AG
-# Label: "SwissSign Silver CA - G2"
-# Serial: 5700383053117599563
-# MD5 Fingerprint: e0:06:a1:c9:7d:cf:c9:fc:0d:c0:56:75:96:d8:62:13
-# SHA1 Fingerprint: 9b:aa:e5:9f:56:ee:21:cb:43:5a:be:25:93:df:a7:f0:40:d1:1d:cb
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------BEGIN CERTIFICATE-----
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-# Subject: CN=thawte Primary Root CA O=thawte, Inc. OU=Certification Services Division/(c) 2006 thawte, Inc. - For authorized use only
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-# Subject: CN=VeriSign Class 3 Public Primary Certification Authority - G5 O=VeriSign, Inc. OU=VeriSign Trust Network/(c) 2006 VeriSign, Inc. - For authorized use only
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-# Issuer: CN=SecureTrust CA O=SecureTrust Corporation
-# Subject: CN=SecureTrust CA O=SecureTrust Corporation
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=Secure Global CA O=SecureTrust Corporation
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-# Label: "Secure Global CA"
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=Cybertrust Global Root O=Cybertrust, Inc
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-# Serial: 4835703278459682877484360
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------BEGIN CERTIFICATE-----
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-# Subject: O=Chunghwa Telecom Co., Ltd. OU=ePKI Root Certification Authority
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-# Label: "certSIGN ROOT CA"
-# Serial: 35210227249154
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-# Issuer: CN=GeoTrust Primary Certification Authority - G3 O=GeoTrust Inc. OU=(c) 2008 GeoTrust Inc. - For authorized use only
-# Subject: CN=GeoTrust Primary Certification Authority - G3 O=GeoTrust Inc. OU=(c) 2008 GeoTrust Inc. - For authorized use only
-# Label: "GeoTrust Primary Certification Authority - G3"
-# Serial: 28809105769928564313984085209975885599
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=thawte Primary Root CA - G2 O=thawte, Inc. OU=(c) 2007 thawte, Inc. - For authorized use only
-# Subject: CN=thawte Primary Root CA - G2 O=thawte, Inc. OU=(c) 2007 thawte, Inc. - For authorized use only
-# Label: "thawte Primary Root CA - G2"
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=thawte Primary Root CA - G3 O=thawte, Inc. OU=Certification Services Division/(c) 2008 thawte, Inc. - For authorized use only
-# Subject: CN=thawte Primary Root CA - G3 O=thawte, Inc. OU=Certification Services Division/(c) 2008 thawte, Inc. - For authorized use only
-# Label: "thawte Primary Root CA - G3"
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=GeoTrust Primary Certification Authority - G2 O=GeoTrust Inc. OU=(c) 2007 GeoTrust Inc. - For authorized use only
-# Subject: CN=GeoTrust Primary Certification Authority - G2 O=GeoTrust Inc. OU=(c) 2007 GeoTrust Inc. - For authorized use only
-# Label: "GeoTrust Primary Certification Authority - G2"
-# Serial: 80682863203381065782177908751794619243
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------BEGIN CERTIFICATE-----
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-
-# Issuer: CN=VeriSign Universal Root Certification Authority O=VeriSign, Inc. OU=VeriSign Trust Network/(c) 2008 VeriSign, Inc. - For authorized use only
-# Subject: CN=VeriSign Universal Root Certification Authority O=VeriSign, Inc. OU=VeriSign Trust Network/(c) 2008 VeriSign, Inc. - For authorized use only
-# Label: "VeriSign Universal Root Certification Authority"
-# Serial: 85209574734084581917763752644031726877
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=VeriSign Class 3 Public Primary Certification Authority - G4 O=VeriSign, Inc. OU=VeriSign Trust Network/(c) 2007 VeriSign, Inc. - For authorized use only
-# Subject: CN=VeriSign Class 3 Public Primary Certification Authority - G4 O=VeriSign, Inc. OU=VeriSign Trust Network/(c) 2007 VeriSign, Inc. - For authorized use only
-# Label: "VeriSign Class 3 Public Primary Certification Authority - G4"
-# Serial: 63143484348153506665311985501458640051
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=NetLock Arany (Class Gold) F\u0151tan\xfas\xedtv\xe1ny O=NetLock Kft. OU=Tan\xfas\xedtv\xe1nykiad\xf3k (Certification Services)
-# Subject: CN=NetLock Arany (Class Gold) F\u0151tan\xfas\xedtv\xe1ny O=NetLock Kft. OU=Tan\xfas\xedtv\xe1nykiad\xf3k (Certification Services)
-# Label: "NetLock Arany (Class Gold) F\u0151tan\xfas\xedtv\xe1ny"
-# Serial: 80544274841616
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Staat der Nederlanden Root CA - G2 O=Staat der Nederlanden
-# Subject: CN=Staat der Nederlanden Root CA - G2 O=Staat der Nederlanden
-# Label: "Staat der Nederlanden Root CA - G2"
-# Serial: 10000012
-# MD5 Fingerprint: 7c:a5:0f:f8:5b:9a:7d:6d:30:ae:54:5a:e3:42:a2:8a
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Hongkong Post Root CA 1 O=Hongkong Post
-# Subject: CN=Hongkong Post Root CA 1 O=Hongkong Post
-# Label: "Hongkong Post Root CA 1"
-# Serial: 1000
-# MD5 Fingerprint: a8:0d:6f:39:78:b9:43:6d:77:42:6d:98:5a:cc:23:ca
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=SecureSign RootCA11 O=Japan Certification Services, Inc.
-# Subject: CN=SecureSign RootCA11 O=Japan Certification Services, Inc.
-# Label: "SecureSign RootCA11"
-# Serial: 1
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=Microsec e-Szigno Root CA 2009 O=Microsec Ltd.
-# Subject: CN=Microsec e-Szigno Root CA 2009 O=Microsec Ltd.
-# Label: "Microsec e-Szigno Root CA 2009"
-# Serial: 14014712776195784473
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=GlobalSign O=GlobalSign OU=GlobalSign Root CA - R3
-# Subject: CN=GlobalSign O=GlobalSign OU=GlobalSign Root CA - R3
-# Label: "GlobalSign Root CA - R3"
-# Serial: 4835703278459759426209954
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=Autoridad de Certificacion Firmaprofesional CIF A62634068
-# Subject: CN=Autoridad de Certificacion Firmaprofesional CIF A62634068
-# Label: "Autoridad de Certificacion Firmaprofesional CIF A62634068"
-# Serial: 6047274297262753887
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Izenpe.com O=IZENPE S.A.
-# Subject: CN=Izenpe.com O=IZENPE S.A.
-# Label: "Izenpe.com"
-# Serial: 917563065490389241595536686991402621
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=Chambers of Commerce Root - 2008 O=AC Camerfirma S.A.
-# Subject: CN=Chambers of Commerce Root - 2008 O=AC Camerfirma S.A.
-# Label: "Chambers of Commerce Root - 2008"
-# Serial: 11806822484801597146
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=Buypass Class 3 Root CA O=Buypass AS-983163327
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=T-TeleSec GlobalRoot Class 3 O=T-Systems Enterprise Services GmbH OU=T-Systems Trust Center
-# Subject: CN=T-TeleSec GlobalRoot Class 3 O=T-Systems Enterprise Services GmbH OU=T-Systems Trust Center
-# Label: "T-TeleSec GlobalRoot Class 3"
-# Serial: 1
-# MD5 Fingerprint: ca:fb:40:a8:4e:39:92:8a:1d:fe:8e:2f:c4:27:ea:ef
-# SHA1 Fingerprint: 55:a6:72:3e:cb:f2:ec:cd:c3:23:74:70:19:9d:2a:be:11:e3:81:d1
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=EE Certification Centre Root CA O=AS Sertifitseerimiskeskus
-# Subject: CN=EE Certification Centre Root CA O=AS Sertifitseerimiskeskus
-# Label: "EE Certification Centre Root CA"
-# Serial: 112324828676200291871926431888494945866
-# MD5 Fingerprint: 43:5e:88:d4:7d:1a:4a:7e:fd:84:2e:52:eb:01:d4:6f
-# SHA1 Fingerprint: c9:a8:b9:e7:55:80:5e:58:e3:53:77:a7:25:eb:af:c3:7b:27:cc:d7
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=D-TRUST Root Class 3 CA 2 2009 O=D-Trust GmbH
-# Subject: CN=D-TRUST Root Class 3 CA 2 2009 O=D-Trust GmbH
-# Label: "D-TRUST Root Class 3 CA 2 2009"
-# Serial: 623603
-# MD5 Fingerprint: cd:e0:25:69:8d:47:ac:9c:89:35:90:f7:fd:51:3d:2f
-# SHA1 Fingerprint: 58:e8:ab:b0:36:15:33:fb:80:f7:9b:1b:6d:29:d3:ff:8d:5f:00:f0
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=D-TRUST Root Class 3 CA 2 EV 2009 O=D-Trust GmbH
-# Subject: CN=D-TRUST Root Class 3 CA 2 EV 2009 O=D-Trust GmbH
-# Label: "D-TRUST Root Class 3 CA 2 EV 2009"
-# Serial: 623604
-# MD5 Fingerprint: aa:c6:43:2c:5e:2d:cd:c4:34:c0:50:4f:11:02:4f:b6
-# SHA1 Fingerprint: 96:c9:1b:0b:95:b4:10:98:42:fa:d0:d8:22:79:fe:60:fa:b9:16:83
-# SHA256 Fingerprint: ee:c5:49:6b:98:8c:e9:86:25:b9:34:09:2e:ec:29:08:be:d0:b0:f3:16:c2:d4:73:0c:84:ea:f1:f3:d3:48:81
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=CA Disig Root R2 O=Disig a.s.
-# Subject: CN=CA Disig Root R2 O=Disig a.s.
-# Label: "CA Disig Root R2"
-# Serial: 10572350602393338211
-# MD5 Fingerprint: 26:01:fb:d8:27:a7:17:9a:45:54:38:1a:43:01:3b:03
-# SHA1 Fingerprint: b5:61:eb:ea:a4:de:e4:25:4b:69:1a:98:a5:57:47:c2:34:c7:d9:71
-# SHA256 Fingerprint: e2:3d:4a:03:6d:7b:70:e9:f5:95:b1:42:20:79:d2:b9:1e:df:bb:1f:b6:51:a0:63:3e:aa:8a:9d:c5:f8:07:03
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=ACCVRAIZ1 O=ACCV OU=PKIACCV
-# Subject: CN=ACCVRAIZ1 O=ACCV OU=PKIACCV
-# Label: "ACCVRAIZ1"
-# Serial: 6828503384748696800
-# MD5 Fingerprint: d0:a0:5a:ee:05:b6:09:94:21:a1:7d:f1:b2:29:82:02
-# SHA1 Fingerprint: 93:05:7a:88:15:c6:4f:ce:88:2f:fa:91:16:52:28:78:bc:53:64:17
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=TWCA Global Root CA O=TAIWAN-CA OU=Root CA
-# Subject: CN=TWCA Global Root CA O=TAIWAN-CA OU=Root CA
-# Label: "TWCA Global Root CA"
-# Serial: 3262
-# MD5 Fingerprint: f9:03:7e:cf:e6:9e:3c:73:7a:2a:90:07:69:ff:2b:96
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=TeliaSonera Root CA v1 O=TeliaSonera
-# Subject: CN=TeliaSonera Root CA v1 O=TeliaSonera
-# Label: "TeliaSonera Root CA v1"
-# Serial: 199041966741090107964904287217786801558
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=E-Tugra Certification Authority O=E-Tu\u011fra EBG Bili\u015fim Teknolojileri ve Hizmetleri A.\u015e. OU=E-Tugra Sertifikasyon Merkezi
-# Subject: CN=E-Tugra Certification Authority O=E-Tu\u011fra EBG Bili\u015fim Teknolojileri ve Hizmetleri A.\u015e. OU=E-Tugra Sertifikasyon Merkezi
-# Label: "E-Tugra Certification Authority"
-# Serial: 7667447206703254355
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=T-TeleSec GlobalRoot Class 2 O=T-Systems Enterprise Services GmbH OU=T-Systems Trust Center
-# Subject: CN=T-TeleSec GlobalRoot Class 2 O=T-Systems Enterprise Services GmbH OU=T-Systems Trust Center
-# Label: "T-TeleSec GlobalRoot Class 2"
-# Serial: 1
-# MD5 Fingerprint: 2b:9b:9e:e4:7b:6c:1f:00:72:1a:cc:c1:77:79:df:6a
-# SHA1 Fingerprint: 59:0d:2d:7d:88:4f:40:2e:61:7e:a5:62:32:17:65:cf:17:d8:94:e9
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=Atos TrustedRoot 2011 O=Atos
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-# Label: "Atos TrustedRoot 2011"
-# Serial: 6643877497813316402
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=QuoVadis Root CA 1 G3 O=QuoVadis Limited
-# Subject: CN=QuoVadis Root CA 1 G3 O=QuoVadis Limited
-# Label: "QuoVadis Root CA 1 G3"
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=QuoVadis Root CA 2 G3 O=QuoVadis Limited
-# Subject: CN=QuoVadis Root CA 2 G3 O=QuoVadis Limited
-# Label: "QuoVadis Root CA 2 G3"
-# Serial: 390156079458959257446133169266079962026824725800
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=QuoVadis Root CA 3 G3 O=QuoVadis Limited
-# Subject: CN=QuoVadis Root CA 3 G3 O=QuoVadis Limited
-# Label: "QuoVadis Root CA 3 G3"
-# Serial: 268090761170461462463995952157327242137089239581
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=DigiCert Assured ID Root G2 O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert Assured ID Root G2 O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert Assured ID Root G2"
-# Serial: 15385348160840213938643033620894905419
-# MD5 Fingerprint: 92:38:b9:f8:63:24:82:65:2c:57:33:e6:fe:81:8f:9d
-# SHA1 Fingerprint: a1:4b:48:d9:43:ee:0a:0e:40:90:4f:3c:e0:a4:c0:91:93:51:5d:3f
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=DigiCert Assured ID Root G3 O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert Assured ID Root G3 O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert Assured ID Root G3"
-# Serial: 15459312981008553731928384953135426796
-# MD5 Fingerprint: 7c:7f:65:31:0c:81:df:8d:ba:3e:99:e2:5c:ad:6e:fb
-# SHA1 Fingerprint: f5:17:a2:4f:9a:48:c6:c9:f8:a2:00:26:9f:dc:0f:48:2c:ab:30:89
-# SHA256 Fingerprint: 7e:37:cb:8b:4c:47:09:0c:ab:36:55:1b:a6:f4:5d:b8:40:68:0f:ba:16:6a:95:2d:b1:00:71:7f:43:05:3f:c2
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=DigiCert Global Root G2 O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert Global Root G2 O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert Global Root G2"
-# Serial: 4293743540046975378534879503202253541
-# MD5 Fingerprint: e4:a6:8a:c8:54:ac:52:42:46:0a:fd:72:48:1b:2a:44
-# SHA1 Fingerprint: df:3c:24:f9:bf:d6:66:76:1b:26:80:73:fe:06:d1:cc:8d:4f:82:a4
-# SHA256 Fingerprint: cb:3c:cb:b7:60:31:e5:e0:13:8f:8d:d3:9a:23:f9:de:47:ff:c3:5e:43:c1:14:4c:ea:27:d4:6a:5a:b1:cb:5f
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=DigiCert Global Root G3 O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert Global Root G3 O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert Global Root G3"
-# Serial: 7089244469030293291760083333884364146
-# MD5 Fingerprint: f5:5d:a4:50:a5:fb:28:7e:1e:0f:0d:cc:96:57:56:ca
-# SHA1 Fingerprint: 7e:04:de:89:6a:3e:66:6d:00:e6:87:d3:3f:fa:d9:3b:e8:3d:34:9e
-# SHA256 Fingerprint: 31:ad:66:48:f8:10:41:38:c7:38:f3:9e:a4:32:01:33:39:3e:3a:18:cc:02:29:6e:f9:7c:2a:c9:ef:67:31:d0
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=DigiCert Trusted Root G4 O=DigiCert Inc OU=www.digicert.com
-# Subject: CN=DigiCert Trusted Root G4 O=DigiCert Inc OU=www.digicert.com
-# Label: "DigiCert Trusted Root G4"
-# Serial: 7451500558977370777930084869016614236
-# MD5 Fingerprint: 78:f2:fc:aa:60:1f:2f:b4:eb:c9:37:ba:53:2e:75:49
-# SHA1 Fingerprint: dd:fb:16:cd:49:31:c9:73:a2:03:7d:3f:c8:3a:4d:7d:77:5d:05:e4
-# SHA256 Fingerprint: 55:2f:7b:dc:f1:a7:af:9e:6c:e6:72:01:7f:4f:12:ab:f7:72:40:c7:8e:76:1a:c2:03:d1:d9:d2:0a:c8:99:88
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=COMODO RSA Certification Authority O=COMODO CA Limited
-# Subject: CN=COMODO RSA Certification Authority O=COMODO CA Limited
-# Label: "COMODO RSA Certification Authority"
-# Serial: 101909084537582093308941363524873193117
-# MD5 Fingerprint: 1b:31:b0:71:40:36:cc:14:36:91:ad:c4:3e:fd:ec:18
-# SHA1 Fingerprint: af:e5:d2:44:a8:d1:19:42:30:ff:47:9f:e2:f8:97:bb:cd:7a:8c:b4
-# SHA256 Fingerprint: 52:f0:e1:c4:e5:8e:c6:29:29:1b:60:31:7f:07:46:71:b8:5d:7e:a8:0d:5b:07:27:34:63:53:4b:32:b4:02:34
------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=USERTrust RSA Certification Authority O=The USERTRUST Network
-# Subject: CN=USERTrust RSA Certification Authority O=The USERTRUST Network
-# Label: "USERTrust RSA Certification Authority"
-# Serial: 2645093764781058787591871645665788717
-# MD5 Fingerprint: 1b:fe:69:d1:91:b7:19:33:a3:72:a8:0f:e1:55:e5:b5
-# SHA1 Fingerprint: 2b:8f:1b:57:33:0d:bb:a2:d0:7a:6c:51:f7:0e:e9:0d:da:b9:ad:8e
-# SHA256 Fingerprint: e7:93:c9:b0:2f:d8:aa:13:e2:1c:31:22:8a:cc:b0:81:19:64:3b:74:9c:89:89:64:b1:74:6d:46:c3:d4:cb:d2
------BEGIN CERTIFICATE-----
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-# Issuer: CN=USERTrust ECC Certification Authority O=The USERTRUST Network
-# Subject: CN=USERTrust ECC Certification Authority O=The USERTRUST Network
-# Label: "USERTrust ECC Certification Authority"
-# Serial: 123013823720199481456569720443997572134
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=GlobalSign O=GlobalSign OU=GlobalSign ECC Root CA - R4
-# Subject: CN=GlobalSign O=GlobalSign OU=GlobalSign ECC Root CA - R4
-# Label: "GlobalSign ECC Root CA - R4"
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=GlobalSign O=GlobalSign OU=GlobalSign ECC Root CA - R5
-# Subject: CN=GlobalSign O=GlobalSign OU=GlobalSign ECC Root CA - R5
-# Label: "GlobalSign ECC Root CA - R5"
-# Serial: 32785792099990507226680698011560947931244
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=Staat der Nederlanden Root CA - G3 O=Staat der Nederlanden
-# Subject: CN=Staat der Nederlanden Root CA - G3 O=Staat der Nederlanden
-# Label: "Staat der Nederlanden Root CA - G3"
-# Serial: 10003001
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=Staat der Nederlanden EV Root CA O=Staat der Nederlanden
-# Subject: CN=Staat der Nederlanden EV Root CA O=Staat der Nederlanden
-# Label: "Staat der Nederlanden EV Root CA"
-# Serial: 10000013
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=IdenTrust Commercial Root CA 1 O=IdenTrust
-# Subject: CN=IdenTrust Commercial Root CA 1 O=IdenTrust
-# Label: "IdenTrust Commercial Root CA 1"
-# Serial: 13298821034946342390520003877796839426
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=Entrust Root Certification Authority - G2 O=Entrust, Inc. OU=See www.entrust.net/legal-terms/(c) 2009 Entrust, Inc. - for authorized use only
-# Subject: CN=Entrust Root Certification Authority - G2 O=Entrust, Inc. OU=See www.entrust.net/legal-terms/(c) 2009 Entrust, Inc. - for authorized use only
-# Label: "Entrust Root Certification Authority - G2"
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-# Issuer: CN=CFCA EV ROOT O=China Financial Certification Authority
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------END CERTIFICATE-----
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-# Label: "AC RAIZ FNMT-RCM"
-# Serial: 485876308206448804701554682760554759
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=Amazon Root CA 1 O=Amazon
-# Subject: CN=Amazon Root CA 1 O=Amazon
-# Label: "Amazon Root CA 1"
-# Serial: 143266978916655856878034712317230054538369994
-# MD5 Fingerprint: 43:c6:bf:ae:ec:fe:ad:2f:18:c6:88:68:30:fc:c8:e6
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=Amazon Root CA 2 O=Amazon
-# Subject: CN=Amazon Root CA 2 O=Amazon
-# Label: "Amazon Root CA 2"
-# Serial: 143266982885963551818349160658925006970653239
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Amazon Root CA 3 O=Amazon
-# Subject: CN=Amazon Root CA 3 O=Amazon
-# Label: "Amazon Root CA 3"
-# Serial: 143266986699090766294700635381230934788665930
-# MD5 Fingerprint: a0:d4:ef:0b:f7:b5:d8:49:95:2a:ec:f5:c4:fc:81:87
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Amazon Root CA 4 O=Amazon
-# Subject: CN=Amazon Root CA 4 O=Amazon
-# Label: "Amazon Root CA 4"
-# Serial: 143266989758080763974105200630763877849284878
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=LuxTrust Global Root 2 O=LuxTrust S.A.
-# Subject: CN=LuxTrust Global Root 2 O=LuxTrust S.A.
-# Label: "LuxTrust Global Root 2"
-# Serial: 59914338225734147123941058376788110305822489521
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------BEGIN CERTIFICATE-----
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-# Subject: CN=TUBITAK Kamu SM SSL Kok Sertifikasi - Surum 1 O=Turkiye Bilimsel ve Teknolojik Arastirma Kurumu - TUBITAK OU=Kamu Sertifikasyon Merkezi - Kamu SM
-# Label: "TUBITAK Kamu SM SSL Kok Sertifikasi - Surum 1"
-# Serial: 1
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=GDCA TrustAUTH R5 ROOT O=GUANG DONG CERTIFICATE AUTHORITY CO.,LTD.
-# Subject: CN=GDCA TrustAUTH R5 ROOT O=GUANG DONG CERTIFICATE AUTHORITY CO.,LTD.
-# Label: "GDCA TrustAUTH R5 ROOT"
-# Serial: 9009899650740120186
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-# Issuer: CN=TrustCor RootCert CA-1 O=TrustCor Systems S. de R.L. OU=TrustCor Certificate Authority
-# Subject: CN=TrustCor RootCert CA-1 O=TrustCor Systems S. de R.L. OU=TrustCor Certificate Authority
-# Label: "TrustCor RootCert CA-1"
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------BEGIN CERTIFICATE-----
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-# Issuer: CN=TrustCor RootCert CA-2 O=TrustCor Systems S. de R.L. OU=TrustCor Certificate Authority
-# Subject: CN=TrustCor RootCert CA-2 O=TrustCor Systems S. de R.L. OU=TrustCor Certificate Authority
-# Label: "TrustCor RootCert CA-2"
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=TrustCor ECA-1 O=TrustCor Systems S. de R.L. OU=TrustCor Certificate Authority
-# Subject: CN=TrustCor ECA-1 O=TrustCor Systems S. de R.L. OU=TrustCor Certificate Authority
-# Label: "TrustCor ECA-1"
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=SSL.com Root Certification Authority RSA O=SSL Corporation
-# Subject: CN=SSL.com Root Certification Authority RSA O=SSL Corporation
-# Label: "SSL.com Root Certification Authority RSA"
-# Serial: 8875640296558310041
-# MD5 Fingerprint: 86:69:12:c0:70:f1:ec:ac:ac:c2:d5:bc:a5:5b:a1:29
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=SSL.com Root Certification Authority ECC O=SSL Corporation
-# Subject: CN=SSL.com Root Certification Authority ECC O=SSL Corporation
-# Label: "SSL.com Root Certification Authority ECC"
-# Serial: 8495723813297216424
-# MD5 Fingerprint: 2e:da:e4:39:7f:9c:8f:37:d1:70:9f:26:17:51:3a:8e
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
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-# Issuer: CN=SSL.com EV Root Certification Authority RSA R2 O=SSL Corporation
-# Subject: CN=SSL.com EV Root Certification Authority RSA R2 O=SSL Corporation
-# Label: "SSL.com EV Root Certification Authority RSA R2"
-# Serial: 6248227494352943350
-# MD5 Fingerprint: e1:1e:31:58:1a:ae:54:53:02:f6:17:6a:11:7b:4d:95
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=SSL.com EV Root Certification Authority ECC O=SSL Corporation
-# Subject: CN=SSL.com EV Root Certification Authority ECC O=SSL Corporation
-# Label: "SSL.com EV Root Certification Authority ECC"
-# Serial: 3182246526754555285
-# MD5 Fingerprint: 59:53:22:65:83:42:01:54:c0:ce:42:b9:5a:7c:f2:90
-# SHA1 Fingerprint: 4c:dd:51:a3:d1:f5:20:32:14:b0:c6:c5:32:23:03:91:c7:46:42:6d
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=GlobalSign O=GlobalSign OU=GlobalSign Root CA - R6
-# Subject: CN=GlobalSign O=GlobalSign OU=GlobalSign Root CA - R6
-# Label: "GlobalSign Root CA - R6"
-# Serial: 1417766617973444989252670301619537
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------BEGIN CERTIFICATE-----
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-# Serial: 146587175971765017618439757810265552097
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-# Issuer: CN=GTS Root R2 O=Google Trust Services LLC
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-# Label: "GTS Root R2"
-# Serial: 146587176055767053814479386953112547951
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-# Issuer: CN=GTS Root R3 O=Google Trust Services LLC
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-# Label: "GTS Root R3"
-# Serial: 146587176140553309517047991083707763997
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=UCA Extended Validation Root O=UniTrust
-# Subject: CN=UCA Extended Validation Root O=UniTrust
-# Label: "UCA Extended Validation Root"
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
-
-# Issuer: CN=Certigna Root CA O=Dhimyotis OU=0002 48146308100036
-# Subject: CN=Certigna Root CA O=Dhimyotis OU=0002 48146308100036
-# Label: "Certigna Root CA"
-# Serial: 269714418870597844693661054334862075617
-# MD5 Fingerprint: 0e:5c:30:62:27:eb:5b:bc:d7:ae:62:ba:e9:d5:df:77
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------BEGIN CERTIFICATE-----
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------END CERTIFICATE-----
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/core.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/core.py
deleted file mode 100644
index 2d02ea4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/certifi/core.py
+++ /dev/null
@@ -1,20 +0,0 @@
-#!/usr/bin/env python
-# -*- coding: utf-8 -*-
-
-"""
-certifi.py
-~~~~~~~~~~
-
-This module returns the installation location of cacert.pem.
-"""
-import os
-
-
-def where():
-    f = os.path.dirname(__file__)
-
-    return os.path.join(f, 'cacert.pem')
-
-
-if __name__ == '__main__':
-    print(where())
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__init__.py
deleted file mode 100644
index 0f9f820..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__init__.py
+++ /dev/null
@@ -1,39 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-
-from .compat import PY2, PY3
-from .universaldetector import UniversalDetector
-from .version import __version__, VERSION
-
-
-def detect(byte_str):
-    """
-    Detect the encoding of the given byte string.
-
-    :param byte_str:     The byte sequence to examine.
-    :type byte_str:      ``bytes`` or ``bytearray``
-    """
-    if not isinstance(byte_str, bytearray):
-        if not isinstance(byte_str, bytes):
-            raise TypeError('Expected object of type bytes or bytearray, got: '
-                            '{0}'.format(type(byte_str)))
-        else:
-            byte_str = bytearray(byte_str)
-    detector = UniversalDetector()
-    detector.feed(byte_str)
-    return detector.close()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index ae5b615..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/big5freq.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/big5freq.cpython-37.pyc
deleted file mode 100644
index d09c3b9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/big5freq.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/big5prober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/big5prober.cpython-37.pyc
deleted file mode 100644
index 79fd058..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/big5prober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/chardistribution.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/chardistribution.cpython-37.pyc
deleted file mode 100644
index 245b4ca..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/chardistribution.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/charsetgroupprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/charsetgroupprober.cpython-37.pyc
deleted file mode 100644
index e4ba863..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/charsetgroupprober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/charsetprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/charsetprober.cpython-37.pyc
deleted file mode 100644
index db34adc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/charsetprober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/codingstatemachine.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/codingstatemachine.cpython-37.pyc
deleted file mode 100644
index e73da8d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/codingstatemachine.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/compat.cpython-37.pyc
deleted file mode 100644
index f3cd010..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/cp949prober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/cp949prober.cpython-37.pyc
deleted file mode 100644
index 9a8ba33..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/cp949prober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/enums.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/enums.cpython-37.pyc
deleted file mode 100644
index ca0ef53..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/enums.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/escprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/escprober.cpython-37.pyc
deleted file mode 100644
index f13269c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/escprober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/escsm.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/escsm.cpython-37.pyc
deleted file mode 100644
index 1df7589..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/escsm.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/eucjpprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/eucjpprober.cpython-37.pyc
deleted file mode 100644
index b24802b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/eucjpprober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euckrfreq.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euckrfreq.cpython-37.pyc
deleted file mode 100644
index bd8df2f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euckrfreq.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euckrprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euckrprober.cpython-37.pyc
deleted file mode 100644
index 7f5a090..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euckrprober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euctwfreq.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euctwfreq.cpython-37.pyc
deleted file mode 100644
index 2e4e530..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euctwfreq.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euctwprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euctwprober.cpython-37.pyc
deleted file mode 100644
index 76147f8..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/euctwprober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/gb2312freq.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/gb2312freq.cpython-37.pyc
deleted file mode 100644
index cbc7ce7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/gb2312freq.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/gb2312prober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/gb2312prober.cpython-37.pyc
deleted file mode 100644
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--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/gb2312prober.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/hebrewprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/hebrewprober.cpython-37.pyc
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+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/jisfreq.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/jisfreq.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/jpcntx.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/jpcntx.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/langcyrillicmodel.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/langcyrillicmodel.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/sjisprober.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/__pycache__/sjisprober.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/big5freq.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/big5freq.py
deleted file mode 100644
index 38f3251..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/big5freq.py
+++ /dev/null
@@ -1,386 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# Big5 frequency table
-# by Taiwan's Mandarin Promotion Council
-# <http://www.edu.tw:81/mandr/>
-#
-# 128  --> 0.42261
-# 256  --> 0.57851
-# 512  --> 0.74851
-# 1024 --> 0.89384
-# 2048 --> 0.97583
-#
-# Ideal Distribution Ratio = 0.74851/(1-0.74851) =2.98
-# Random Distribution Ration = 512/(5401-512)=0.105
-#
-# Typical Distribution Ratio about 25% of Ideal one, still much higher than RDR
-
-BIG5_TYPICAL_DISTRIBUTION_RATIO = 0.75
-
-#Char to FreqOrder table
-BIG5_TABLE_SIZE = 5376
-
-BIG5_CHAR_TO_FREQ_ORDER = (
-   1,1801,1506, 255,1431, 198,   9,  82,   6,5008, 177, 202,3681,1256,2821, 110, #   16
-3814,  33,3274, 261,  76,  44,2114,  16,2946,2187,1176, 659,3971,  26,3451,2653, #   32
-1198,3972,3350,4202, 410,2215, 302, 590, 361,1964,   8, 204,  58,4510,5009,1932, #   48
-  63,5010,5011, 317,1614,  75, 222, 159,4203,2417,1480,5012,3555,3091, 224,2822, #   64
-3682,   3,  10,3973,1471,  29,2787,1135,2866,1940, 873, 130,3275,1123, 312,5013, #   80
-4511,2052, 507, 252, 682,5014, 142,1915, 124, 206,2947,  34,3556,3204,  64, 604, #   96
-5015,2501,1977,1978, 155,1991, 645, 641,1606,5016,3452, 337,  72, 406,5017,  80, #  112
- 630, 238,3205,1509, 263, 939,1092,2654, 756,1440,1094,3453, 449,  69,2987, 591, #  128
- 179,2096, 471, 115,2035,1844,  60,  50,2988, 134, 806,1869, 734,2036,3454, 180, #  144
- 995,1607, 156, 537,2907, 688,5018, 319,1305, 779,2145, 514,2379, 298,4512, 359, #  160
-2502,  90,2716,1338, 663,  11, 906,1099,2553,  20,2441, 182, 532,1716,5019, 732, #  176
-1376,4204,1311,1420,3206,  25,2317,1056, 113, 399, 382,1950, 242,3455,2474, 529, #  192
-3276, 475,1447,3683,5020, 117,  21, 656, 810,1297,2300,2334,3557,5021, 126,4205, #  208
- 706, 456, 150, 613,4513,  71,1118,2037,4206, 145,3092,  85, 835, 486,2115,1246, #  224
-1426, 428, 727,1285,1015, 800, 106, 623, 303,1281,5022,2128,2359, 347,3815, 221, #  240
-3558,3135,5023,1956,1153,4207,  83, 296,1199,3093, 192, 624,  93,5024, 822,1898, #  256
-2823,3136, 795,2065, 991,1554,1542,1592,  27,  43,2867, 859, 139,1456, 860,4514, #  272
- 437, 712,3974, 164,2397,3137, 695, 211,3037,2097, 195,3975,1608,3559,3560,3684, #  288
-3976, 234, 811,2989,2098,3977,2233,1441,3561,1615,2380, 668,2077,1638, 305, 228, #  304
-1664,4515, 467, 415,5025, 262,2099,1593, 239, 108, 300, 200,1033, 512,1247,2078, #  320
-5026,5027,2176,3207,3685,2682, 593, 845,1062,3277,  88,1723,2038,3978,1951, 212, #  336
- 266, 152, 149, 468,1899,4208,4516,  77, 187,5028,3038,  37,   5,2990,5029,3979, #  352
-5030,5031,  39,2524,4517,2908,3208,2079,  55, 148,  74,4518, 545, 483,1474,1029, #  368
-1665, 217,1870,1531,3138,1104,2655,4209,  24, 172,3562, 900,3980,3563,3564,4519, #  384
-  32,1408,2824,1312, 329, 487,2360,2251,2717, 784,2683,   4,3039,3351,1427,1789, #  400
- 188, 109, 499,5032,3686,1717,1790, 888,1217,3040,4520,5033,3565,5034,3352,1520, #  416
-3687,3981, 196,1034, 775,5035,5036, 929,1816, 249, 439,  38,5037,1063,5038, 794, #  432
-3982,1435,2301,  46, 178,3278,2066,5039,2381,5040, 214,1709,4521, 804,  35, 707, #  448
- 324,3688,1601,2554, 140, 459,4210,5041,5042,1365, 839, 272, 978,2262,2580,3456, #  464
-2129,1363,3689,1423, 697, 100,3094,  48,  70,1231, 495,3139,2196,5043,1294,5044, #  480
-2080, 462, 586,1042,3279, 853, 256, 988, 185,2382,3457,1698, 434,1084,5045,3458, #  496
- 314,2625,2788,4522,2335,2336, 569,2285, 637,1817,2525, 757,1162,1879,1616,3459, #  512
- 287,1577,2116, 768,4523,1671,2868,3566,2526,1321,3816, 909,2418,5046,4211, 933, #  528
-3817,4212,2053,2361,1222,4524, 765,2419,1322, 786,4525,5047,1920,1462,1677,2909, #  544
-1699,5048,4526,1424,2442,3140,3690,2600,3353,1775,1941,3460,3983,4213, 309,1369, #  560
-1130,2825, 364,2234,1653,1299,3984,3567,3985,3986,2656, 525,1085,3041, 902,2001, #  576
-1475, 964,4527, 421,1845,1415,1057,2286, 940,1364,3141, 376,4528,4529,1381,   7, #  592
-2527, 983,2383, 336,1710,2684,1846, 321,3461, 559,1131,3042,2752,1809,1132,1313, #  608
- 265,1481,1858,5049, 352,1203,2826,3280, 167,1089, 420,2827, 776, 792,1724,3568, #  624
-4214,2443,3281,5050,4215,5051, 446, 229, 333,2753, 901,3818,1200,1557,4530,2657, #  640
-1921, 395,2754,2685,3819,4216,1836, 125, 916,3209,2626,4531,5052,5053,3820,5054, #  656
-5055,5056,4532,3142,3691,1133,2555,1757,3462,1510,2318,1409,3569,5057,2146, 438, #  672
-2601,2910,2384,3354,1068, 958,3043, 461, 311,2869,2686,4217,1916,3210,4218,1979, #  688
- 383, 750,2755,2627,4219, 274, 539, 385,1278,1442,5058,1154,1965, 384, 561, 210, #  704
-  98,1295,2556,3570,5059,1711,2420,1482,3463,3987,2911,1257, 129,5060,3821, 642, #  720
- 523,2789,2790,2658,5061, 141,2235,1333,  68, 176, 441, 876, 907,4220, 603,2602, #  736
- 710, 171,3464, 404, 549,  18,3143,2398,1410,3692,1666,5062,3571,4533,2912,4534, #  752
-5063,2991, 368,5064, 146, 366,  99, 871,3693,1543, 748, 807,1586,1185,  22,2263, #  768
- 379,3822,3211,5065,3212, 505,1942,2628,1992,1382,2319,5066, 380,2362, 218, 702, #  784
-1818,1248,3465,3044,3572,3355,3282,5067,2992,3694, 930,3283,3823,5068,  59,5069, #  800
- 585, 601,4221, 497,3466,1112,1314,4535,1802,5070,1223,1472,2177,5071, 749,1837, #  816
- 690,1900,3824,1773,3988,1476, 429,1043,1791,2236,2117, 917,4222, 447,1086,1629, #  832
-5072, 556,5073,5074,2021,1654, 844,1090, 105, 550, 966,1758,2828,1008,1783, 686, #  848
-1095,5075,2287, 793,1602,5076,3573,2603,4536,4223,2948,2302,4537,3825, 980,2503, #  864
- 544, 353, 527,4538, 908,2687,2913,5077, 381,2629,1943,1348,5078,1341,1252, 560, #  880
-3095,5079,3467,2870,5080,2054, 973, 886,2081, 143,4539,5081,5082, 157,3989, 496, #  896
-4224,  57, 840, 540,2039,4540,4541,3468,2118,1445, 970,2264,1748,1966,2082,4225, #  912
-3144,1234,1776,3284,2829,3695, 773,1206,2130,1066,2040,1326,3990,1738,1725,4226, #  928
- 279,3145,  51,1544,2604, 423,1578,2131,2067, 173,4542,1880,5083,5084,1583, 264, #  944
- 610,3696,4543,2444, 280, 154,5085,5086,5087,1739, 338,1282,3096, 693,2871,1411, #  960
-1074,3826,2445,5088,4544,5089,5090,1240, 952,2399,5091,2914,1538,2688, 685,1483, #  976
-4227,2475,1436, 953,4228,2055,4545, 671,2400,  79,4229,2446,3285, 608, 567,2689, #  992
-3469,4230,4231,1691, 393,1261,1792,2401,5092,4546,5093,5094,5095,5096,1383,1672, # 1008
-3827,3213,1464, 522,1119, 661,1150, 216, 675,4547,3991,1432,3574, 609,4548,2690, # 1024
-2402,5097,5098,5099,4232,3045,   0,5100,2476, 315, 231,2447, 301,3356,4549,2385, # 1040
-5101, 233,4233,3697,1819,4550,4551,5102,  96,1777,1315,2083,5103, 257,5104,1810, # 1056
-3698,2718,1139,1820,4234,2022,1124,2164,2791,1778,2659,5105,3097, 363,1655,3214, # 1072
-5106,2993,5107,5108,5109,3992,1567,3993, 718, 103,3215, 849,1443, 341,3357,2949, # 1088
-1484,5110,1712, 127,  67, 339,4235,2403, 679,1412, 821,5111,5112, 834, 738, 351, # 1104
-2994,2147, 846, 235,1497,1881, 418,1993,3828,2719, 186,1100,2148,2756,3575,1545, # 1120
-1355,2950,2872,1377, 583,3994,4236,2581,2995,5113,1298,3699,1078,2557,3700,2363, # 1136
-  78,3829,3830, 267,1289,2100,2002,1594,4237, 348, 369,1274,2197,2178,1838,4552, # 1152
-1821,2830,3701,2757,2288,2003,4553,2951,2758, 144,3358, 882,4554,3995,2759,3470, # 1168
-4555,2915,5114,4238,1726, 320,5115,3996,3046, 788,2996,5116,2831,1774,1327,2873, # 1184
-3997,2832,5117,1306,4556,2004,1700,3831,3576,2364,2660, 787,2023, 506, 824,3702, # 1200
- 534, 323,4557,1044,3359,2024,1901, 946,3471,5118,1779,1500,1678,5119,1882,4558, # 1216
- 165, 243,4559,3703,2528, 123, 683,4239, 764,4560,  36,3998,1793, 589,2916, 816, # 1232
- 626,1667,3047,2237,1639,1555,1622,3832,3999,5120,4000,2874,1370,1228,1933, 891, # 1248
-2084,2917, 304,4240,5121, 292,2997,2720,3577, 691,2101,4241,1115,4561, 118, 662, # 1264
-5122, 611,1156, 854,2386,1316,2875,   2, 386, 515,2918,5123,5124,3286, 868,2238, # 1280
-1486, 855,2661, 785,2216,3048,5125,1040,3216,3578,5126,3146, 448,5127,1525,5128, # 1296
-2165,4562,5129,3833,5130,4242,2833,3579,3147, 503, 818,4001,3148,1568, 814, 676, # 1312
-1444, 306,1749,5131,3834,1416,1030, 197,1428, 805,2834,1501,4563,5132,5133,5134, # 1328
-1994,5135,4564,5136,5137,2198,  13,2792,3704,2998,3149,1229,1917,5138,3835,2132, # 1344
-5139,4243,4565,2404,3580,5140,2217,1511,1727,1120,5141,5142, 646,3836,2448, 307, # 1360
-5143,5144,1595,3217,5145,5146,5147,3705,1113,1356,4002,1465,2529,2530,5148, 519, # 1376
-5149, 128,2133,  92,2289,1980,5150,4003,1512, 342,3150,2199,5151,2793,2218,1981, # 1392
-3360,4244, 290,1656,1317, 789, 827,2365,5152,3837,4566, 562, 581,4004,5153, 401, # 1408
-4567,2252,  94,4568,5154,1399,2794,5155,1463,2025,4569,3218,1944,5156, 828,1105, # 1424
-4245,1262,1394,5157,4246, 605,4570,5158,1784,2876,5159,2835, 819,2102, 578,2200, # 1440
-2952,5160,1502, 436,3287,4247,3288,2836,4005,2919,3472,3473,5161,2721,2320,5162, # 1456
-5163,2337,2068,  23,4571, 193, 826,3838,2103, 699,1630,4248,3098, 390,1794,1064, # 1472
-3581,5164,1579,3099,3100,1400,5165,4249,1839,1640,2877,5166,4572,4573, 137,4250, # 1488
- 598,3101,1967, 780, 104, 974,2953,5167, 278, 899, 253, 402, 572, 504, 493,1339, # 1504
-5168,4006,1275,4574,2582,2558,5169,3706,3049,3102,2253, 565,1334,2722, 863,  41, # 1520
-5170,5171,4575,5172,1657,2338,  19, 463,2760,4251, 606,5173,2999,3289,1087,2085, # 1536
-1323,2662,3000,5174,1631,1623,1750,4252,2691,5175,2878, 791,2723,2663,2339, 232, # 1552
-2421,5176,3001,1498,5177,2664,2630, 755,1366,3707,3290,3151,2026,1609, 119,1918, # 1568
-3474, 862,1026,4253,5178,4007,3839,4576,4008,4577,2265,1952,2477,5179,1125, 817, # 1584
-4254,4255,4009,1513,1766,2041,1487,4256,3050,3291,2837,3840,3152,5180,5181,1507, # 1600
-5182,2692, 733,  40,1632,1106,2879, 345,4257, 841,2531, 230,4578,3002,1847,3292, # 1616
-3475,5183,1263, 986,3476,5184, 735, 879, 254,1137, 857, 622,1300,1180,1388,1562, # 1632
-4010,4011,2954, 967,2761,2665,1349, 592,2134,1692,3361,3003,1995,4258,1679,4012, # 1648
-1902,2188,5185, 739,3708,2724,1296,1290,5186,4259,2201,2202,1922,1563,2605,2559, # 1664
-1871,2762,3004,5187, 435,5188, 343,1108, 596,  17,1751,4579,2239,3477,3709,5189, # 1680
-4580, 294,3582,2955,1693, 477, 979, 281,2042,3583, 643,2043,3710,2631,2795,2266, # 1696
-1031,2340,2135,2303,3584,4581, 367,1249,2560,5190,3585,5191,4582,1283,3362,2005, # 1712
- 240,1762,3363,4583,4584, 836,1069,3153, 474,5192,2149,2532, 268,3586,5193,3219, # 1728
-1521,1284,5194,1658,1546,4260,5195,3587,3588,5196,4261,3364,2693,1685,4262, 961, # 1744
-1673,2632, 190,2006,2203,3841,4585,4586,5197, 570,2504,3711,1490,5198,4587,2633, # 1760
-3293,1957,4588, 584,1514, 396,1045,1945,5199,4589,1968,2449,5200,5201,4590,4013, # 1776
- 619,5202,3154,3294, 215,2007,2796,2561,3220,4591,3221,4592, 763,4263,3842,4593, # 1792
-5203,5204,1958,1767,2956,3365,3712,1174, 452,1477,4594,3366,3155,5205,2838,1253, # 1808
-2387,2189,1091,2290,4264, 492,5206, 638,1169,1825,2136,1752,4014, 648, 926,1021, # 1824
-1324,4595, 520,4596, 997, 847,1007, 892,4597,3843,2267,1872,3713,2405,1785,4598, # 1840
-1953,2957,3103,3222,1728,4265,2044,3714,4599,2008,1701,3156,1551,  30,2268,4266, # 1856
-5207,2027,4600,3589,5208, 501,5209,4267, 594,3478,2166,1822,3590,3479,3591,3223, # 1872
- 829,2839,4268,5210,1680,3157,1225,4269,5211,3295,4601,4270,3158,2341,5212,4602, # 1888
-4271,5213,4015,4016,5214,1848,2388,2606,3367,5215,4603, 374,4017, 652,4272,4273, # 1904
- 375,1140, 798,5216,5217,5218,2366,4604,2269, 546,1659, 138,3051,2450,4605,5219, # 1920
-2254, 612,1849, 910, 796,3844,1740,1371, 825,3845,3846,5220,2920,2562,5221, 692, # 1936
- 444,3052,2634, 801,4606,4274,5222,1491, 244,1053,3053,4275,4276, 340,5223,4018, # 1952
-1041,3005, 293,1168,  87,1357,5224,1539, 959,5225,2240, 721, 694,4277,3847, 219, # 1968
-1478, 644,1417,3368,2666,1413,1401,1335,1389,4019,5226,5227,3006,2367,3159,1826, # 1984
- 730,1515, 184,2840,  66,4607,5228,1660,2958, 246,3369, 378,1457, 226,3480, 975, # 2000
-4020,2959,1264,3592, 674, 696,5229, 163,5230,1141,2422,2167, 713,3593,3370,4608, # 2016
-4021,5231,5232,1186,  15,5233,1079,1070,5234,1522,3224,3594, 276,1050,2725, 758, # 2032
-1126, 653,2960,3296,5235,2342, 889,3595,4022,3104,3007, 903,1250,4609,4023,3481, # 2048
-3596,1342,1681,1718, 766,3297, 286,  89,2961,3715,5236,1713,5237,2607,3371,3008, # 2064
-5238,2962,2219,3225,2880,5239,4610,2505,2533, 181, 387,1075,4024, 731,2190,3372, # 2080
-5240,3298, 310, 313,3482,2304, 770,4278,  54,3054, 189,4611,3105,3848,4025,5241, # 2096
-1230,1617,1850, 355,3597,4279,4612,3373, 111,4280,3716,1350,3160,3483,3055,4281, # 2112
-2150,3299,3598,5242,2797,4026,4027,3009, 722,2009,5243,1071, 247,1207,2343,2478, # 2128
-1378,4613,2010, 864,1437,1214,4614, 373,3849,1142,2220, 667,4615, 442,2763,2563, # 2144
-3850,4028,1969,4282,3300,1840, 837, 170,1107, 934,1336,1883,5244,5245,2119,4283, # 2160
-2841, 743,1569,5246,4616,4284, 582,2389,1418,3484,5247,1803,5248, 357,1395,1729, # 2176
-3717,3301,2423,1564,2241,5249,3106,3851,1633,4617,1114,2086,4285,1532,5250, 482, # 2192
-2451,4618,5251,5252,1492, 833,1466,5253,2726,3599,1641,2842,5254,1526,1272,3718, # 2208
-4286,1686,1795, 416,2564,1903,1954,1804,5255,3852,2798,3853,1159,2321,5256,2881, # 2224
-4619,1610,1584,3056,2424,2764, 443,3302,1163,3161,5257,5258,4029,5259,4287,2506, # 2240
-3057,4620,4030,3162,2104,1647,3600,2011,1873,4288,5260,4289, 431,3485,5261, 250, # 2256
-  97,  81,4290,5262,1648,1851,1558, 160, 848,5263, 866, 740,1694,5264,2204,2843, # 2272
-3226,4291,4621,3719,1687, 950,2479, 426, 469,3227,3720,3721,4031,5265,5266,1188, # 2288
- 424,1996, 861,3601,4292,3854,2205,2694, 168,1235,3602,4293,5267,2087,1674,4622, # 2304
-3374,3303, 220,2565,1009,5268,3855, 670,3010, 332,1208, 717,5269,5270,3603,2452, # 2320
-4032,3375,5271, 513,5272,1209,2882,3376,3163,4623,1080,5273,5274,5275,5276,2534, # 2336
-3722,3604, 815,1587,4033,4034,5277,3605,3486,3856,1254,4624,1328,3058,1390,4035, # 2352
-1741,4036,3857,4037,5278, 236,3858,2453,3304,5279,5280,3723,3859,1273,3860,4625, # 2368
-5281, 308,5282,4626, 245,4627,1852,2480,1307,2583, 430, 715,2137,2454,5283, 270, # 2384
- 199,2883,4038,5284,3606,2727,1753, 761,1754, 725,1661,1841,4628,3487,3724,5285, # 2400
-5286, 587,  14,3305, 227,2608, 326, 480,2270, 943,2765,3607, 291, 650,1884,5287, # 2416
-1702,1226, 102,1547,  62,3488, 904,4629,3489,1164,4294,5288,5289,1224,1548,2766, # 2432
- 391, 498,1493,5290,1386,1419,5291,2056,1177,4630, 813, 880,1081,2368, 566,1145, # 2448
-4631,2291,1001,1035,2566,2609,2242, 394,1286,5292,5293,2069,5294,  86,1494,1730, # 2464
-4039, 491,1588, 745, 897,2963, 843,3377,4040,2767,2884,3306,1768, 998,2221,2070, # 2480
- 397,1827,1195,1970,3725,3011,3378, 284,5295,3861,2507,2138,2120,1904,5296,4041, # 2496
-2151,4042,4295,1036,3490,1905, 114,2567,4296, 209,1527,5297,5298,2964,2844,2635, # 2512
-2390,2728,3164, 812,2568,5299,3307,5300,1559, 737,1885,3726,1210, 885,  28,2695, # 2528
-3608,3862,5301,4297,1004,1780,4632,5302, 346,1982,2222,2696,4633,3863,1742, 797, # 2544
-1642,4043,1934,1072,1384,2152, 896,4044,3308,3727,3228,2885,3609,5303,2569,1959, # 2560
-4634,2455,1786,5304,5305,5306,4045,4298,1005,1308,3728,4299,2729,4635,4636,1528, # 2576
-2610, 161,1178,4300,1983, 987,4637,1101,4301, 631,4046,1157,3229,2425,1343,1241, # 2592
-1016,2243,2570, 372, 877,2344,2508,1160, 555,1935, 911,4047,5307, 466,1170, 169, # 2608
-1051,2921,2697,3729,2481,3012,1182,2012,2571,1251,2636,5308, 992,2345,3491,1540, # 2624
-2730,1201,2071,2406,1997,2482,5309,4638, 528,1923,2191,1503,1874,1570,2369,3379, # 2640
-3309,5310, 557,1073,5311,1828,3492,2088,2271,3165,3059,3107, 767,3108,2799,4639, # 2656
-1006,4302,4640,2346,1267,2179,3730,3230, 778,4048,3231,2731,1597,2667,5312,4641, # 2672
-5313,3493,5314,5315,5316,3310,2698,1433,3311, 131,  95,1504,4049, 723,4303,3166, # 2688
-1842,3610,2768,2192,4050,2028,2105,3731,5317,3013,4051,1218,5318,3380,3232,4052, # 2704
-4304,2584, 248,1634,3864, 912,5319,2845,3732,3060,3865, 654,  53,5320,3014,5321, # 2720
-1688,4642, 777,3494,1032,4053,1425,5322, 191, 820,2121,2846, 971,4643, 931,3233, # 2736
- 135, 664, 783,3866,1998, 772,2922,1936,4054,3867,4644,2923,3234, 282,2732, 640, # 2752
-1372,3495,1127, 922, 325,3381,5323,5324, 711,2045,5325,5326,4055,2223,2800,1937, # 2768
-4056,3382,2224,2255,3868,2305,5327,4645,3869,1258,3312,4057,3235,2139,2965,4058, # 2784
-4059,5328,2225, 258,3236,4646, 101,1227,5329,3313,1755,5330,1391,3314,5331,2924, # 2800
-2057, 893,5332,5333,5334,1402,4305,2347,5335,5336,3237,3611,5337,5338, 878,1325, # 2816
-1781,2801,4647, 259,1385,2585, 744,1183,2272,4648,5339,4060,2509,5340, 684,1024, # 2832
-4306,5341, 472,3612,3496,1165,3315,4061,4062, 322,2153, 881, 455,1695,1152,1340, # 2848
- 660, 554,2154,4649,1058,4650,4307, 830,1065,3383,4063,4651,1924,5342,1703,1919, # 2864
-5343, 932,2273, 122,5344,4652, 947, 677,5345,3870,2637, 297,1906,1925,2274,4653, # 2880
-2322,3316,5346,5347,4308,5348,4309,  84,4310, 112, 989,5349, 547,1059,4064, 701, # 2896
-3613,1019,5350,4311,5351,3497, 942, 639, 457,2306,2456, 993,2966, 407, 851, 494, # 2912
-4654,3384, 927,5352,1237,5353,2426,3385, 573,4312, 680, 921,2925,1279,1875, 285, # 2928
- 790,1448,1984, 719,2168,5354,5355,4655,4065,4066,1649,5356,1541, 563,5357,1077, # 2944
-5358,3386,3061,3498, 511,3015,4067,4068,3733,4069,1268,2572,3387,3238,4656,4657, # 2960
-5359, 535,1048,1276,1189,2926,2029,3167,1438,1373,2847,2967,1134,2013,5360,4313, # 2976
-1238,2586,3109,1259,5361, 700,5362,2968,3168,3734,4314,5363,4315,1146,1876,1907, # 2992
-4658,2611,4070, 781,2427, 132,1589, 203, 147, 273,2802,2407, 898,1787,2155,4071, # 3008
-4072,5364,3871,2803,5365,5366,4659,4660,5367,3239,5368,1635,3872, 965,5369,1805, # 3024
-2699,1516,3614,1121,1082,1329,3317,4073,1449,3873,  65,1128,2848,2927,2769,1590, # 3040
-3874,5370,5371,  12,2668,  45, 976,2587,3169,4661, 517,2535,1013,1037,3240,5372, # 3056
-3875,2849,5373,3876,5374,3499,5375,2612, 614,1999,2323,3877,3110,2733,2638,5376, # 3072
-2588,4316, 599,1269,5377,1811,3735,5378,2700,3111, 759,1060, 489,1806,3388,3318, # 3088
-1358,5379,5380,2391,1387,1215,2639,2256, 490,5381,5382,4317,1759,2392,2348,5383, # 3104
-4662,3878,1908,4074,2640,1807,3241,4663,3500,3319,2770,2349, 874,5384,5385,3501, # 3120
-3736,1859,  91,2928,3737,3062,3879,4664,5386,3170,4075,2669,5387,3502,1202,1403, # 3136
-3880,2969,2536,1517,2510,4665,3503,2511,5388,4666,5389,2701,1886,1495,1731,4076, # 3152
-2370,4667,5390,2030,5391,5392,4077,2702,1216, 237,2589,4318,2324,4078,3881,4668, # 3168
-4669,2703,3615,3504, 445,4670,5393,5394,5395,5396,2771,  61,4079,3738,1823,4080, # 3184
-5397, 687,2046, 935, 925, 405,2670, 703,1096,1860,2734,4671,4081,1877,1367,2704, # 3200
-3389, 918,2106,1782,2483, 334,3320,1611,1093,4672, 564,3171,3505,3739,3390, 945, # 3216
-2641,2058,4673,5398,1926, 872,4319,5399,3506,2705,3112, 349,4320,3740,4082,4674, # 3232
-3882,4321,3741,2156,4083,4675,4676,4322,4677,2408,2047, 782,4084, 400, 251,4323, # 3248
-1624,5400,5401, 277,3742, 299,1265, 476,1191,3883,2122,4324,4325,1109, 205,5402, # 3264
-2590,1000,2157,3616,1861,5403,5404,5405,4678,5406,4679,2573, 107,2484,2158,4085, # 3280
-3507,3172,5407,1533, 541,1301, 158, 753,4326,2886,3617,5408,1696, 370,1088,4327, # 3296
-4680,3618, 579, 327, 440, 162,2244, 269,1938,1374,3508, 968,3063,  56,1396,3113, # 3312
-2107,3321,3391,5409,1927,2159,4681,3016,5410,3619,5411,5412,3743,4682,2485,5413, # 3328
-2804,5414,1650,4683,5415,2613,5416,5417,4086,2671,3392,1149,3393,4087,3884,4088, # 3344
-5418,1076,  49,5419, 951,3242,3322,3323, 450,2850, 920,5420,1812,2805,2371,4328, # 3360
-1909,1138,2372,3885,3509,5421,3243,4684,1910,1147,1518,2428,4685,3886,5422,4686, # 3376
-2393,2614, 260,1796,3244,5423,5424,3887,3324, 708,5425,3620,1704,5426,3621,1351, # 3392
-1618,3394,3017,1887, 944,4329,3395,4330,3064,3396,4331,5427,3744, 422, 413,1714, # 3408
-3325, 500,2059,2350,4332,2486,5428,1344,1911, 954,5429,1668,5430,5431,4089,2409, # 3424
-4333,3622,3888,4334,5432,2307,1318,2512,3114, 133,3115,2887,4687, 629,  31,2851, # 3440
-2706,3889,4688, 850, 949,4689,4090,2970,1732,2089,4335,1496,1853,5433,4091, 620, # 3456
-3245, 981,1242,3745,3397,1619,3746,1643,3326,2140,2457,1971,1719,3510,2169,5434, # 3472
-3246,5435,5436,3398,1829,5437,1277,4690,1565,2048,5438,1636,3623,3116,5439, 869, # 3488
-2852, 655,3890,3891,3117,4092,3018,3892,1310,3624,4691,5440,5441,5442,1733, 558, # 3504
-4692,3747, 335,1549,3065,1756,4336,3748,1946,3511,1830,1291,1192, 470,2735,2108, # 3520
-2806, 913,1054,4093,5443,1027,5444,3066,4094,4693, 982,2672,3399,3173,3512,3247, # 3536
-3248,1947,2807,5445, 571,4694,5446,1831,5447,3625,2591,1523,2429,5448,2090, 984, # 3552
-4695,3749,1960,5449,3750, 852, 923,2808,3513,3751, 969,1519, 999,2049,2325,1705, # 3568
-5450,3118, 615,1662, 151, 597,4095,2410,2326,1049, 275,4696,3752,4337, 568,3753, # 3584
-3626,2487,4338,3754,5451,2430,2275, 409,3249,5452,1566,2888,3514,1002, 769,2853, # 3600
- 194,2091,3174,3755,2226,3327,4339, 628,1505,5453,5454,1763,2180,3019,4096, 521, # 3616
-1161,2592,1788,2206,2411,4697,4097,1625,4340,4341, 412,  42,3119, 464,5455,2642, # 3632
-4698,3400,1760,1571,2889,3515,2537,1219,2207,3893,2643,2141,2373,4699,4700,3328, # 3648
-1651,3401,3627,5456,5457,3628,2488,3516,5458,3756,5459,5460,2276,2092, 460,5461, # 3664
-4701,5462,3020, 962, 588,3629, 289,3250,2644,1116,  52,5463,3067,1797,5464,5465, # 3680
-5466,1467,5467,1598,1143,3757,4342,1985,1734,1067,4702,1280,3402, 465,4703,1572, # 3696
- 510,5468,1928,2245,1813,1644,3630,5469,4704,3758,5470,5471,2673,1573,1534,5472, # 3712
-5473, 536,1808,1761,3517,3894,3175,2645,5474,5475,5476,4705,3518,2929,1912,2809, # 3728
-5477,3329,1122, 377,3251,5478, 360,5479,5480,4343,1529, 551,5481,2060,3759,1769, # 3744
-2431,5482,2930,4344,3330,3120,2327,2109,2031,4706,1404, 136,1468,1479, 672,1171, # 3760
-3252,2308, 271,3176,5483,2772,5484,2050, 678,2736, 865,1948,4707,5485,2014,4098, # 3776
-2971,5486,2737,2227,1397,3068,3760,4708,4709,1735,2931,3403,3631,5487,3895, 509, # 3792
-2854,2458,2890,3896,5488,5489,3177,3178,4710,4345,2538,4711,2309,1166,1010, 552, # 3808
- 681,1888,5490,5491,2972,2973,4099,1287,1596,1862,3179, 358, 453, 736, 175, 478, # 3824
-1117, 905,1167,1097,5492,1854,1530,5493,1706,5494,2181,3519,2292,3761,3520,3632, # 3840
-4346,2093,4347,5495,3404,1193,2489,4348,1458,2193,2208,1863,1889,1421,3331,2932, # 3856
-3069,2182,3521, 595,2123,5496,4100,5497,5498,4349,1707,2646, 223,3762,1359, 751, # 3872
-3121, 183,3522,5499,2810,3021, 419,2374, 633, 704,3897,2394, 241,5500,5501,5502, # 3888
- 838,3022,3763,2277,2773,2459,3898,1939,2051,4101,1309,3122,2246,1181,5503,1136, # 3904
-2209,3899,2375,1446,4350,2310,4712,5504,5505,4351,1055,2615, 484,3764,5506,4102, # 3920
- 625,4352,2278,3405,1499,4353,4103,5507,4104,4354,3253,2279,2280,3523,5508,5509, # 3936
-2774, 808,2616,3765,3406,4105,4355,3123,2539, 526,3407,3900,4356, 955,5510,1620, # 3952
-4357,2647,2432,5511,1429,3766,1669,1832, 994, 928,5512,3633,1260,5513,5514,5515, # 3968
-1949,2293, 741,2933,1626,4358,2738,2460, 867,1184, 362,3408,1392,5516,5517,4106, # 3984
-4359,1770,1736,3254,2934,4713,4714,1929,2707,1459,1158,5518,3070,3409,2891,1292, # 4000
-1930,2513,2855,3767,1986,1187,2072,2015,2617,4360,5519,2574,2514,2170,3768,2490, # 4016
-3332,5520,3769,4715,5521,5522, 666,1003,3023,1022,3634,4361,5523,4716,1814,2257, # 4032
- 574,3901,1603, 295,1535, 705,3902,4362, 283, 858, 417,5524,5525,3255,4717,4718, # 4048
-3071,1220,1890,1046,2281,2461,4107,1393,1599, 689,2575, 388,4363,5526,2491, 802, # 4064
-5527,2811,3903,2061,1405,2258,5528,4719,3904,2110,1052,1345,3256,1585,5529, 809, # 4080
-5530,5531,5532, 575,2739,3524, 956,1552,1469,1144,2328,5533,2329,1560,2462,3635, # 4096
-3257,4108, 616,2210,4364,3180,2183,2294,5534,1833,5535,3525,4720,5536,1319,3770, # 4112
-3771,1211,3636,1023,3258,1293,2812,5537,5538,5539,3905, 607,2311,3906, 762,2892, # 4128
-1439,4365,1360,4721,1485,3072,5540,4722,1038,4366,1450,2062,2648,4367,1379,4723, # 4144
-2593,5541,5542,4368,1352,1414,2330,2935,1172,5543,5544,3907,3908,4724,1798,1451, # 4160
-5545,5546,5547,5548,2936,4109,4110,2492,2351, 411,4111,4112,3637,3333,3124,4725, # 4176
-1561,2674,1452,4113,1375,5549,5550,  47,2974, 316,5551,1406,1591,2937,3181,5552, # 4192
-1025,2142,3125,3182, 354,2740, 884,2228,4369,2412, 508,3772, 726,3638, 996,2433, # 4208
-3639, 729,5553, 392,2194,1453,4114,4726,3773,5554,5555,2463,3640,2618,1675,2813, # 4224
- 919,2352,2975,2353,1270,4727,4115,  73,5556,5557, 647,5558,3259,2856,2259,1550, # 4240
-1346,3024,5559,1332, 883,3526,5560,5561,5562,5563,3334,2775,5564,1212, 831,1347, # 4256
-4370,4728,2331,3909,1864,3073, 720,3910,4729,4730,3911,5565,4371,5566,5567,4731, # 4272
-5568,5569,1799,4732,3774,2619,4733,3641,1645,2376,4734,5570,2938, 669,2211,2675, # 4288
-2434,5571,2893,5572,5573,1028,3260,5574,4372,2413,5575,2260,1353,5576,5577,4735, # 4304
-3183, 518,5578,4116,5579,4373,1961,5580,2143,4374,5581,5582,3025,2354,2355,3912, # 4320
- 516,1834,1454,4117,2708,4375,4736,2229,2620,1972,1129,3642,5583,2776,5584,2976, # 4336
-1422, 577,1470,3026,1524,3410,5585,5586, 432,4376,3074,3527,5587,2594,1455,2515, # 4352
-2230,1973,1175,5588,1020,2741,4118,3528,4737,5589,2742,5590,1743,1361,3075,3529, # 4368
-2649,4119,4377,4738,2295, 895, 924,4378,2171, 331,2247,3076, 166,1627,3077,1098, # 4384
-5591,1232,2894,2231,3411,4739, 657, 403,1196,2377, 542,3775,3412,1600,4379,3530, # 4400
-5592,4740,2777,3261, 576, 530,1362,4741,4742,2540,2676,3776,4120,5593, 842,3913, # 4416
-5594,2814,2032,1014,4121, 213,2709,3413, 665, 621,4380,5595,3777,2939,2435,5596, # 4432
-2436,3335,3643,3414,4743,4381,2541,4382,4744,3644,1682,4383,3531,1380,5597, 724, # 4448
-2282, 600,1670,5598,1337,1233,4745,3126,2248,5599,1621,4746,5600, 651,4384,5601, # 4464
-1612,4385,2621,5602,2857,5603,2743,2312,3078,5604, 716,2464,3079, 174,1255,2710, # 4480
-4122,3645, 548,1320,1398, 728,4123,1574,5605,1891,1197,3080,4124,5606,3081,3082, # 4496
-3778,3646,3779, 747,5607, 635,4386,4747,5608,5609,5610,4387,5611,5612,4748,5613, # 4512
-3415,4749,2437, 451,5614,3780,2542,2073,4388,2744,4389,4125,5615,1764,4750,5616, # 4528
-4390, 350,4751,2283,2395,2493,5617,4391,4126,2249,1434,4127, 488,4752, 458,4392, # 4544
-4128,3781, 771,1330,2396,3914,2576,3184,2160,2414,1553,2677,3185,4393,5618,2494, # 4560
-2895,2622,1720,2711,4394,3416,4753,5619,2543,4395,5620,3262,4396,2778,5621,2016, # 4576
-2745,5622,1155,1017,3782,3915,5623,3336,2313, 201,1865,4397,1430,5624,4129,5625, # 4592
-5626,5627,5628,5629,4398,1604,5630, 414,1866, 371,2595,4754,4755,3532,2017,3127, # 4608
-4756,1708, 960,4399, 887, 389,2172,1536,1663,1721,5631,2232,4130,2356,2940,1580, # 4624
-5632,5633,1744,4757,2544,4758,4759,5634,4760,5635,2074,5636,4761,3647,3417,2896, # 4640
-4400,5637,4401,2650,3418,2815, 673,2712,2465, 709,3533,4131,3648,4402,5638,1148, # 4656
- 502, 634,5639,5640,1204,4762,3649,1575,4763,2623,3783,5641,3784,3128, 948,3263, # 4672
- 121,1745,3916,1110,5642,4403,3083,2516,3027,4132,3785,1151,1771,3917,1488,4133, # 4688
-1987,5643,2438,3534,5644,5645,2094,5646,4404,3918,1213,1407,2816, 531,2746,2545, # 4704
-3264,1011,1537,4764,2779,4405,3129,1061,5647,3786,3787,1867,2897,5648,2018, 120, # 4720
-4406,4407,2063,3650,3265,2314,3919,2678,3419,1955,4765,4134,5649,3535,1047,2713, # 4736
-1266,5650,1368,4766,2858, 649,3420,3920,2546,2747,1102,2859,2679,5651,5652,2000, # 4752
-5653,1111,3651,2977,5654,2495,3921,3652,2817,1855,3421,3788,5655,5656,3422,2415, # 4768
-2898,3337,3266,3653,5657,2577,5658,3654,2818,4135,1460, 856,5659,3655,5660,2899, # 4784
-2978,5661,2900,3922,5662,4408, 632,2517, 875,3923,1697,3924,2296,5663,5664,4767, # 4800
-3028,1239, 580,4768,4409,5665, 914, 936,2075,1190,4136,1039,2124,5666,5667,5668, # 4816
-5669,3423,1473,5670,1354,4410,3925,4769,2173,3084,4137, 915,3338,4411,4412,3339, # 4832
-1605,1835,5671,2748, 398,3656,4413,3926,4138, 328,1913,2860,4139,3927,1331,4414, # 4848
-3029, 937,4415,5672,3657,4140,4141,3424,2161,4770,3425, 524, 742, 538,3085,1012, # 4864
-5673,5674,3928,2466,5675, 658,1103, 225,3929,5676,5677,4771,5678,4772,5679,3267, # 4880
-1243,5680,4142, 963,2250,4773,5681,2714,3658,3186,5682,5683,2596,2332,5684,4774, # 4896
-5685,5686,5687,3536, 957,3426,2547,2033,1931,2941,2467, 870,2019,3659,1746,2780, # 4912
-2781,2439,2468,5688,3930,5689,3789,3130,3790,3537,3427,3791,5690,1179,3086,5691, # 4928
-3187,2378,4416,3792,2548,3188,3131,2749,4143,5692,3428,1556,2549,2297, 977,2901, # 4944
-2034,4144,1205,3429,5693,1765,3430,3189,2125,1271, 714,1689,4775,3538,5694,2333, # 4960
-3931, 533,4417,3660,2184, 617,5695,2469,3340,3539,2315,5696,5697,3190,5698,5699, # 4976
-3932,1988, 618, 427,2651,3540,3431,5700,5701,1244,1690,5702,2819,4418,4776,5703, # 4992
-3541,4777,5704,2284,1576, 473,3661,4419,3432, 972,5705,3662,5706,3087,5707,5708, # 5008
-4778,4779,5709,3793,4145,4146,5710, 153,4780, 356,5711,1892,2902,4420,2144, 408, # 5024
- 803,2357,5712,3933,5713,4421,1646,2578,2518,4781,4782,3934,5714,3935,4422,5715, # 5040
-2416,3433, 752,5716,5717,1962,3341,2979,5718, 746,3030,2470,4783,4423,3794, 698, # 5056
-4784,1893,4424,3663,2550,4785,3664,3936,5719,3191,3434,5720,1824,1302,4147,2715, # 5072
-3937,1974,4425,5721,4426,3192, 823,1303,1288,1236,2861,3542,4148,3435, 774,3938, # 5088
-5722,1581,4786,1304,2862,3939,4787,5723,2440,2162,1083,3268,4427,4149,4428, 344, # 5104
-1173, 288,2316, 454,1683,5724,5725,1461,4788,4150,2597,5726,5727,4789, 985, 894, # 5120
-5728,3436,3193,5729,1914,2942,3795,1989,5730,2111,1975,5731,4151,5732,2579,1194, # 5136
- 425,5733,4790,3194,1245,3796,4429,5734,5735,2863,5736, 636,4791,1856,3940, 760, # 5152
-1800,5737,4430,2212,1508,4792,4152,1894,1684,2298,5738,5739,4793,4431,4432,2213, # 5168
- 479,5740,5741, 832,5742,4153,2496,5743,2980,2497,3797, 990,3132, 627,1815,2652, # 5184
-4433,1582,4434,2126,2112,3543,4794,5744, 799,4435,3195,5745,4795,2113,1737,3031, # 5200
-1018, 543, 754,4436,3342,1676,4796,4797,4154,4798,1489,5746,3544,5747,2624,2903, # 5216
-4155,5748,5749,2981,5750,5751,5752,5753,3196,4799,4800,2185,1722,5754,3269,3270, # 5232
-1843,3665,1715, 481, 365,1976,1857,5755,5756,1963,2498,4801,5757,2127,3666,3271, # 5248
- 433,1895,2064,2076,5758, 602,2750,5759,5760,5761,5762,5763,3032,1628,3437,5764, # 5264
-3197,4802,4156,2904,4803,2519,5765,2551,2782,5766,5767,5768,3343,4804,2905,5769, # 5280
-4805,5770,2864,4806,4807,1221,2982,4157,2520,5771,5772,5773,1868,1990,5774,5775, # 5296
-5776,1896,5777,5778,4808,1897,4158, 318,5779,2095,4159,4437,5780,5781, 485,5782, # 5312
- 938,3941, 553,2680, 116,5783,3942,3667,5784,3545,2681,2783,3438,3344,2820,5785, # 5328
-3668,2943,4160,1747,2944,2983,5786,5787, 207,5788,4809,5789,4810,2521,5790,3033, # 5344
- 890,3669,3943,5791,1878,3798,3439,5792,2186,2358,3440,1652,5793,5794,5795, 941, # 5360
-2299, 208,3546,4161,2020, 330,4438,3944,2906,2499,3799,4439,4811,5796,5797,5798, # 5376
-)
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/big5prober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/big5prober.py
deleted file mode 100644
index 98f9970..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/big5prober.py
+++ /dev/null
@@ -1,47 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .mbcharsetprober import MultiByteCharSetProber
-from .codingstatemachine import CodingStateMachine
-from .chardistribution import Big5DistributionAnalysis
-from .mbcssm import BIG5_SM_MODEL
-
-
-class Big5Prober(MultiByteCharSetProber):
-    def __init__(self):
-        super(Big5Prober, self).__init__()
-        self.coding_sm = CodingStateMachine(BIG5_SM_MODEL)
-        self.distribution_analyzer = Big5DistributionAnalysis()
-        self.reset()
-
-    @property
-    def charset_name(self):
-        return "Big5"
-
-    @property
-    def language(self):
-        return "Chinese"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/chardistribution.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/chardistribution.py
deleted file mode 100644
index c0395f4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/chardistribution.py
+++ /dev/null
@@ -1,233 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .euctwfreq import (EUCTW_CHAR_TO_FREQ_ORDER, EUCTW_TABLE_SIZE,
-                        EUCTW_TYPICAL_DISTRIBUTION_RATIO)
-from .euckrfreq import (EUCKR_CHAR_TO_FREQ_ORDER, EUCKR_TABLE_SIZE,
-                        EUCKR_TYPICAL_DISTRIBUTION_RATIO)
-from .gb2312freq import (GB2312_CHAR_TO_FREQ_ORDER, GB2312_TABLE_SIZE,
-                         GB2312_TYPICAL_DISTRIBUTION_RATIO)
-from .big5freq import (BIG5_CHAR_TO_FREQ_ORDER, BIG5_TABLE_SIZE,
-                       BIG5_TYPICAL_DISTRIBUTION_RATIO)
-from .jisfreq import (JIS_CHAR_TO_FREQ_ORDER, JIS_TABLE_SIZE,
-                      JIS_TYPICAL_DISTRIBUTION_RATIO)
-
-
-class CharDistributionAnalysis(object):
-    ENOUGH_DATA_THRESHOLD = 1024
-    SURE_YES = 0.99
-    SURE_NO = 0.01
-    MINIMUM_DATA_THRESHOLD = 3
-
-    def __init__(self):
-        # Mapping table to get frequency order from char order (get from
-        # GetOrder())
-        self._char_to_freq_order = None
-        self._table_size = None  # Size of above table
-        # This is a constant value which varies from language to language,
-        # used in calculating confidence.  See
-        # http://www.mozilla.org/projects/intl/UniversalCharsetDetection.html
-        # for further detail.
-        self.typical_distribution_ratio = None
-        self._done = None
-        self._total_chars = None
-        self._freq_chars = None
-        self.reset()
-
-    def reset(self):
-        """reset analyser, clear any state"""
-        # If this flag is set to True, detection is done and conclusion has
-        # been made
-        self._done = False
-        self._total_chars = 0  # Total characters encountered
-        # The number of characters whose frequency order is less than 512
-        self._freq_chars = 0
-
-    def feed(self, char, char_len):
-        """feed a character with known length"""
-        if char_len == 2:
-            # we only care about 2-bytes character in our distribution analysis
-            order = self.get_order(char)
-        else:
-            order = -1
-        if order >= 0:
-            self._total_chars += 1
-            # order is valid
-            if order < self._table_size:
-                if 512 > self._char_to_freq_order[order]:
-                    self._freq_chars += 1
-
-    def get_confidence(self):
-        """return confidence based on existing data"""
-        # if we didn't receive any character in our consideration range,
-        # return negative answer
-        if self._total_chars <= 0 or self._freq_chars <= self.MINIMUM_DATA_THRESHOLD:
-            return self.SURE_NO
-
-        if self._total_chars != self._freq_chars:
-            r = (self._freq_chars / ((self._total_chars - self._freq_chars)
-                 * self.typical_distribution_ratio))
-            if r < self.SURE_YES:
-                return r
-
-        # normalize confidence (we don't want to be 100% sure)
-        return self.SURE_YES
-
-    def got_enough_data(self):
-        # It is not necessary to receive all data to draw conclusion.
-        # For charset detection, certain amount of data is enough
-        return self._total_chars > self.ENOUGH_DATA_THRESHOLD
-
-    def get_order(self, byte_str):
-        # We do not handle characters based on the original encoding string,
-        # but convert this encoding string to a number, here called order.
-        # This allows multiple encodings of a language to share one frequency
-        # table.
-        return -1
-
-
-class EUCTWDistributionAnalysis(CharDistributionAnalysis):
-    def __init__(self):
-        super(EUCTWDistributionAnalysis, self).__init__()
-        self._char_to_freq_order = EUCTW_CHAR_TO_FREQ_ORDER
-        self._table_size = EUCTW_TABLE_SIZE
-        self.typical_distribution_ratio = EUCTW_TYPICAL_DISTRIBUTION_RATIO
-
-    def get_order(self, byte_str):
-        # for euc-TW encoding, we are interested
-        #   first  byte range: 0xc4 -- 0xfe
-        #   second byte range: 0xa1 -- 0xfe
-        # no validation needed here. State machine has done that
-        first_char = byte_str[0]
-        if first_char >= 0xC4:
-            return 94 * (first_char - 0xC4) + byte_str[1] - 0xA1
-        else:
-            return -1
-
-
-class EUCKRDistributionAnalysis(CharDistributionAnalysis):
-    def __init__(self):
-        super(EUCKRDistributionAnalysis, self).__init__()
-        self._char_to_freq_order = EUCKR_CHAR_TO_FREQ_ORDER
-        self._table_size = EUCKR_TABLE_SIZE
-        self.typical_distribution_ratio = EUCKR_TYPICAL_DISTRIBUTION_RATIO
-
-    def get_order(self, byte_str):
-        # for euc-KR encoding, we are interested
-        #   first  byte range: 0xb0 -- 0xfe
-        #   second byte range: 0xa1 -- 0xfe
-        # no validation needed here. State machine has done that
-        first_char = byte_str[0]
-        if first_char >= 0xB0:
-            return 94 * (first_char - 0xB0) + byte_str[1] - 0xA1
-        else:
-            return -1
-
-
-class GB2312DistributionAnalysis(CharDistributionAnalysis):
-    def __init__(self):
-        super(GB2312DistributionAnalysis, self).__init__()
-        self._char_to_freq_order = GB2312_CHAR_TO_FREQ_ORDER
-        self._table_size = GB2312_TABLE_SIZE
-        self.typical_distribution_ratio = GB2312_TYPICAL_DISTRIBUTION_RATIO
-
-    def get_order(self, byte_str):
-        # for GB2312 encoding, we are interested
-        #  first  byte range: 0xb0 -- 0xfe
-        #  second byte range: 0xa1 -- 0xfe
-        # no validation needed here. State machine has done that
-        first_char, second_char = byte_str[0], byte_str[1]
-        if (first_char >= 0xB0) and (second_char >= 0xA1):
-            return 94 * (first_char - 0xB0) + second_char - 0xA1
-        else:
-            return -1
-
-
-class Big5DistributionAnalysis(CharDistributionAnalysis):
-    def __init__(self):
-        super(Big5DistributionAnalysis, self).__init__()
-        self._char_to_freq_order = BIG5_CHAR_TO_FREQ_ORDER
-        self._table_size = BIG5_TABLE_SIZE
-        self.typical_distribution_ratio = BIG5_TYPICAL_DISTRIBUTION_RATIO
-
-    def get_order(self, byte_str):
-        # for big5 encoding, we are interested
-        #   first  byte range: 0xa4 -- 0xfe
-        #   second byte range: 0x40 -- 0x7e , 0xa1 -- 0xfe
-        # no validation needed here. State machine has done that
-        first_char, second_char = byte_str[0], byte_str[1]
-        if first_char >= 0xA4:
-            if second_char >= 0xA1:
-                return 157 * (first_char - 0xA4) + second_char - 0xA1 + 63
-            else:
-                return 157 * (first_char - 0xA4) + second_char - 0x40
-        else:
-            return -1
-
-
-class SJISDistributionAnalysis(CharDistributionAnalysis):
-    def __init__(self):
-        super(SJISDistributionAnalysis, self).__init__()
-        self._char_to_freq_order = JIS_CHAR_TO_FREQ_ORDER
-        self._table_size = JIS_TABLE_SIZE
-        self.typical_distribution_ratio = JIS_TYPICAL_DISTRIBUTION_RATIO
-
-    def get_order(self, byte_str):
-        # for sjis encoding, we are interested
-        #   first  byte range: 0x81 -- 0x9f , 0xe0 -- 0xfe
-        #   second byte range: 0x40 -- 0x7e,  0x81 -- oxfe
-        # no validation needed here. State machine has done that
-        first_char, second_char = byte_str[0], byte_str[1]
-        if (first_char >= 0x81) and (first_char <= 0x9F):
-            order = 188 * (first_char - 0x81)
-        elif (first_char >= 0xE0) and (first_char <= 0xEF):
-            order = 188 * (first_char - 0xE0 + 31)
-        else:
-            return -1
-        order = order + second_char - 0x40
-        if second_char > 0x7F:
-            order = -1
-        return order
-
-
-class EUCJPDistributionAnalysis(CharDistributionAnalysis):
-    def __init__(self):
-        super(EUCJPDistributionAnalysis, self).__init__()
-        self._char_to_freq_order = JIS_CHAR_TO_FREQ_ORDER
-        self._table_size = JIS_TABLE_SIZE
-        self.typical_distribution_ratio = JIS_TYPICAL_DISTRIBUTION_RATIO
-
-    def get_order(self, byte_str):
-        # for euc-JP encoding, we are interested
-        #   first  byte range: 0xa0 -- 0xfe
-        #   second byte range: 0xa1 -- 0xfe
-        # no validation needed here. State machine has done that
-        char = byte_str[0]
-        if char >= 0xA0:
-            return 94 * (char - 0xA1) + byte_str[1] - 0xa1
-        else:
-            return -1
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/charsetgroupprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/charsetgroupprober.py
deleted file mode 100644
index 8b3738e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/charsetgroupprober.py
+++ /dev/null
@@ -1,106 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .enums import ProbingState
-from .charsetprober import CharSetProber
-
-
-class CharSetGroupProber(CharSetProber):
-    def __init__(self, lang_filter=None):
-        super(CharSetGroupProber, self).__init__(lang_filter=lang_filter)
-        self._active_num = 0
-        self.probers = []
-        self._best_guess_prober = None
-
-    def reset(self):
-        super(CharSetGroupProber, self).reset()
-        self._active_num = 0
-        for prober in self.probers:
-            if prober:
-                prober.reset()
-                prober.active = True
-                self._active_num += 1
-        self._best_guess_prober = None
-
-    @property
-    def charset_name(self):
-        if not self._best_guess_prober:
-            self.get_confidence()
-            if not self._best_guess_prober:
-                return None
-        return self._best_guess_prober.charset_name
-
-    @property
-    def language(self):
-        if not self._best_guess_prober:
-            self.get_confidence()
-            if not self._best_guess_prober:
-                return None
-        return self._best_guess_prober.language
-
-    def feed(self, byte_str):
-        for prober in self.probers:
-            if not prober:
-                continue
-            if not prober.active:
-                continue
-            state = prober.feed(byte_str)
-            if not state:
-                continue
-            if state == ProbingState.FOUND_IT:
-                self._best_guess_prober = prober
-                return self.state
-            elif state == ProbingState.NOT_ME:
-                prober.active = False
-                self._active_num -= 1
-                if self._active_num <= 0:
-                    self._state = ProbingState.NOT_ME
-                    return self.state
-        return self.state
-
-    def get_confidence(self):
-        state = self.state
-        if state == ProbingState.FOUND_IT:
-            return 0.99
-        elif state == ProbingState.NOT_ME:
-            return 0.01
-        best_conf = 0.0
-        self._best_guess_prober = None
-        for prober in self.probers:
-            if not prober:
-                continue
-            if not prober.active:
-                self.logger.debug('%s not active', prober.charset_name)
-                continue
-            conf = prober.get_confidence()
-            self.logger.debug('%s %s confidence = %s', prober.charset_name, prober.language, conf)
-            if best_conf < conf:
-                best_conf = conf
-                self._best_guess_prober = prober
-        if not self._best_guess_prober:
-            return 0.0
-        return best_conf
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/charsetprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/charsetprober.py
deleted file mode 100644
index eac4e59..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/charsetprober.py
+++ /dev/null
@@ -1,145 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 2001
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-import logging
-import re
-
-from .enums import ProbingState
-
-
-class CharSetProber(object):
-
-    SHORTCUT_THRESHOLD = 0.95
-
-    def __init__(self, lang_filter=None):
-        self._state = None
-        self.lang_filter = lang_filter
-        self.logger = logging.getLogger(__name__)
-
-    def reset(self):
-        self._state = ProbingState.DETECTING
-
-    @property
-    def charset_name(self):
-        return None
-
-    def feed(self, buf):
-        pass
-
-    @property
-    def state(self):
-        return self._state
-
-    def get_confidence(self):
-        return 0.0
-
-    @staticmethod
-    def filter_high_byte_only(buf):
-        buf = re.sub(b'([\x00-\x7F])+', b' ', buf)
-        return buf
-
-    @staticmethod
-    def filter_international_words(buf):
-        """
-        We define three types of bytes:
-        alphabet: english alphabets [a-zA-Z]
-        international: international characters [\x80-\xFF]
-        marker: everything else [^a-zA-Z\x80-\xFF]
-
-        The input buffer can be thought to contain a series of words delimited
-        by markers. This function works to filter all words that contain at
-        least one international character. All contiguous sequences of markers
-        are replaced by a single space ascii character.
-
-        This filter applies to all scripts which do not use English characters.
-        """
-        filtered = bytearray()
-
-        # This regex expression filters out only words that have at-least one
-        # international character. The word may include one marker character at
-        # the end.
-        words = re.findall(b'[a-zA-Z]*[\x80-\xFF]+[a-zA-Z]*[^a-zA-Z\x80-\xFF]?',
-                           buf)
-
-        for word in words:
-            filtered.extend(word[:-1])
-
-            # If the last character in the word is a marker, replace it with a
-            # space as markers shouldn't affect our analysis (they are used
-            # similarly across all languages and may thus have similar
-            # frequencies).
-            last_char = word[-1:]
-            if not last_char.isalpha() and last_char < b'\x80':
-                last_char = b' '
-            filtered.extend(last_char)
-
-        return filtered
-
-    @staticmethod
-    def filter_with_english_letters(buf):
-        """
-        Returns a copy of ``buf`` that retains only the sequences of English
-        alphabet and high byte characters that are not between <> characters.
-        Also retains English alphabet and high byte characters immediately
-        before occurrences of >.
-
-        This filter can be applied to all scripts which contain both English
-        characters and extended ASCII characters, but is currently only used by
-        ``Latin1Prober``.
-        """
-        filtered = bytearray()
-        in_tag = False
-        prev = 0
-
-        for curr in range(len(buf)):
-            # Slice here to get bytes instead of an int with Python 3
-            buf_char = buf[curr:curr + 1]
-            # Check if we're coming out of or entering an HTML tag
-            if buf_char == b'>':
-                in_tag = False
-            elif buf_char == b'<':
-                in_tag = True
-
-            # If current character is not extended-ASCII and not alphabetic...
-            if buf_char < b'\x80' and not buf_char.isalpha():
-                # ...and we're not in a tag
-                if curr > prev and not in_tag:
-                    # Keep everything after last non-extended-ASCII,
-                    # non-alphabetic character
-                    filtered.extend(buf[prev:curr])
-                    # Output a space to delimit stretch we kept
-                    filtered.extend(b' ')
-                prev = curr + 1
-
-        # If we're not in a tag...
-        if not in_tag:
-            # Keep everything after last non-extended-ASCII, non-alphabetic
-            # character
-            filtered.extend(buf[prev:])
-
-        return filtered
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cli/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cli/__init__.py
deleted file mode 100644
index 8b13789..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cli/__init__.py
+++ /dev/null
@@ -1 +0,0 @@
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cli/chardetect.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cli/chardetect.py
deleted file mode 100644
index c61136b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cli/chardetect.py
+++ /dev/null
@@ -1,85 +0,0 @@
-#!/usr/bin/env python
-"""
-Script which takes one or more file paths and reports on their detected
-encodings
-
-Example::
-
-    % chardetect somefile someotherfile
-    somefile: windows-1252 with confidence 0.5
-    someotherfile: ascii with confidence 1.0
-
-If no paths are provided, it takes its input from stdin.
-
-"""
-
-from __future__ import absolute_import, print_function, unicode_literals
-
-import argparse
-import sys
-
-from pip._vendor.chardet import __version__
-from pip._vendor.chardet.compat import PY2
-from pip._vendor.chardet.universaldetector import UniversalDetector
-
-
-def description_of(lines, name='stdin'):
-    """
-    Return a string describing the probable encoding of a file or
-    list of strings.
-
-    :param lines: The lines to get the encoding of.
-    :type lines: Iterable of bytes
-    :param name: Name of file or collection of lines
-    :type name: str
-    """
-    u = UniversalDetector()
-    for line in lines:
-        line = bytearray(line)
-        u.feed(line)
-        # shortcut out of the loop to save reading further - particularly useful if we read a BOM.
-        if u.done:
-            break
-    u.close()
-    result = u.result
-    if PY2:
-        name = name.decode(sys.getfilesystemencoding(), 'ignore')
-    if result['encoding']:
-        return '{0}: {1} with confidence {2}'.format(name, result['encoding'],
-                                                     result['confidence'])
-    else:
-        return '{0}: no result'.format(name)
-
-
-def main(argv=None):
-    """
-    Handles command line arguments and gets things started.
-
-    :param argv: List of arguments, as if specified on the command-line.
-                 If None, ``sys.argv[1:]`` is used instead.
-    :type argv: list of str
-    """
-    # Get command line arguments
-    parser = argparse.ArgumentParser(
-        description="Takes one or more file paths and reports their detected \
-                     encodings")
-    parser.add_argument('input',
-                        help='File whose encoding we would like to determine. \
-                              (default: stdin)',
-                        type=argparse.FileType('rb'), nargs='*',
-                        default=[sys.stdin if PY2 else sys.stdin.buffer])
-    parser.add_argument('--version', action='version',
-                        version='%(prog)s {0}'.format(__version__))
-    args = parser.parse_args(argv)
-
-    for f in args.input:
-        if f.isatty():
-            print("You are running chardetect interactively. Press " +
-                  "CTRL-D twice at the start of a blank line to signal the " +
-                  "end of your input. If you want help, run chardetect " +
-                  "--help\n", file=sys.stderr)
-        print(description_of(f, f.name))
-
-
-if __name__ == '__main__':
-    main()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/codingstatemachine.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/codingstatemachine.py
deleted file mode 100644
index 68fba44..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/codingstatemachine.py
+++ /dev/null
@@ -1,88 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-import logging
-
-from .enums import MachineState
-
-
-class CodingStateMachine(object):
-    """
-    A state machine to verify a byte sequence for a particular encoding. For
-    each byte the detector receives, it will feed that byte to every active
-    state machine available, one byte at a time. The state machine changes its
-    state based on its previous state and the byte it receives. There are 3
-    states in a state machine that are of interest to an auto-detector:
-
-    START state: This is the state to start with, or a legal byte sequence
-                 (i.e. a valid code point) for character has been identified.
-
-    ME state:  This indicates that the state machine identified a byte sequence
-               that is specific to the charset it is designed for and that
-               there is no other possible encoding which can contain this byte
-               sequence. This will to lead to an immediate positive answer for
-               the detector.
-
-    ERROR state: This indicates the state machine identified an illegal byte
-                 sequence for that encoding. This will lead to an immediate
-                 negative answer for this encoding. Detector will exclude this
-                 encoding from consideration from here on.
-    """
-    def __init__(self, sm):
-        self._model = sm
-        self._curr_byte_pos = 0
-        self._curr_char_len = 0
-        self._curr_state = None
-        self.logger = logging.getLogger(__name__)
-        self.reset()
-
-    def reset(self):
-        self._curr_state = MachineState.START
-
-    def next_state(self, c):
-        # for each byte we get its class
-        # if it is first byte, we also get byte length
-        byte_class = self._model['class_table'][c]
-        if self._curr_state == MachineState.START:
-            self._curr_byte_pos = 0
-            self._curr_char_len = self._model['char_len_table'][byte_class]
-        # from byte's class and state_table, we get its next state
-        curr_state = (self._curr_state * self._model['class_factor']
-                      + byte_class)
-        self._curr_state = self._model['state_table'][curr_state]
-        self._curr_byte_pos += 1
-        return self._curr_state
-
-    def get_current_charlen(self):
-        return self._curr_char_len
-
-    def get_coding_state_machine(self):
-        return self._model['name']
-
-    @property
-    def language(self):
-        return self._model['language']
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/compat.py
deleted file mode 100644
index ddd7468..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/compat.py
+++ /dev/null
@@ -1,34 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# Contributor(s):
-#   Dan Blanchard
-#   Ian Cordasco
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-import sys
-
-
-if sys.version_info < (3, 0):
-    PY2 = True
-    PY3 = False
-    base_str = (str, unicode)
-    text_type = unicode
-else:
-    PY2 = False
-    PY3 = True
-    base_str = (bytes, str)
-    text_type = str
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cp949prober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cp949prober.py
deleted file mode 100644
index efd793a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/cp949prober.py
+++ /dev/null
@@ -1,49 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .chardistribution import EUCKRDistributionAnalysis
-from .codingstatemachine import CodingStateMachine
-from .mbcharsetprober import MultiByteCharSetProber
-from .mbcssm import CP949_SM_MODEL
-
-
-class CP949Prober(MultiByteCharSetProber):
-    def __init__(self):
-        super(CP949Prober, self).__init__()
-        self.coding_sm = CodingStateMachine(CP949_SM_MODEL)
-        # NOTE: CP949 is a superset of EUC-KR, so the distribution should be
-        #       not different.
-        self.distribution_analyzer = EUCKRDistributionAnalysis()
-        self.reset()
-
-    @property
-    def charset_name(self):
-        return "CP949"
-
-    @property
-    def language(self):
-        return "Korean"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/enums.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/enums.py
deleted file mode 100644
index 0451207..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/enums.py
+++ /dev/null
@@ -1,76 +0,0 @@
-"""
-All of the Enums that are used throughout the chardet package.
-
-:author: Dan Blanchard (dan.blanchard@gmail.com)
-"""
-
-
-class InputState(object):
-    """
-    This enum represents the different states a universal detector can be in.
-    """
-    PURE_ASCII = 0
-    ESC_ASCII = 1
-    HIGH_BYTE = 2
-
-
-class LanguageFilter(object):
-    """
-    This enum represents the different language filters we can apply to a
-    ``UniversalDetector``.
-    """
-    CHINESE_SIMPLIFIED = 0x01
-    CHINESE_TRADITIONAL = 0x02
-    JAPANESE = 0x04
-    KOREAN = 0x08
-    NON_CJK = 0x10
-    ALL = 0x1F
-    CHINESE = CHINESE_SIMPLIFIED | CHINESE_TRADITIONAL
-    CJK = CHINESE | JAPANESE | KOREAN
-
-
-class ProbingState(object):
-    """
-    This enum represents the different states a prober can be in.
-    """
-    DETECTING = 0
-    FOUND_IT = 1
-    NOT_ME = 2
-
-
-class MachineState(object):
-    """
-    This enum represents the different states a state machine can be in.
-    """
-    START = 0
-    ERROR = 1
-    ITS_ME = 2
-
-
-class SequenceLikelihood(object):
-    """
-    This enum represents the likelihood of a character following the previous one.
-    """
-    NEGATIVE = 0
-    UNLIKELY = 1
-    LIKELY = 2
-    POSITIVE = 3
-
-    @classmethod
-    def get_num_categories(cls):
-        """:returns: The number of likelihood categories in the enum."""
-        return 4
-
-
-class CharacterCategory(object):
-    """
-    This enum represents the different categories language models for
-    ``SingleByteCharsetProber`` put characters into.
-
-    Anything less than CONTROL is considered a letter.
-    """
-    UNDEFINED = 255
-    LINE_BREAK = 254
-    SYMBOL = 253
-    DIGIT = 252
-    CONTROL = 251
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/escprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/escprober.py
deleted file mode 100644
index c70493f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/escprober.py
+++ /dev/null
@@ -1,101 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetprober import CharSetProber
-from .codingstatemachine import CodingStateMachine
-from .enums import LanguageFilter, ProbingState, MachineState
-from .escsm import (HZ_SM_MODEL, ISO2022CN_SM_MODEL, ISO2022JP_SM_MODEL,
-                    ISO2022KR_SM_MODEL)
-
-
-class EscCharSetProber(CharSetProber):
-    """
-    This CharSetProber uses a "code scheme" approach for detecting encodings,
-    whereby easily recognizable escape or shift sequences are relied on to
-    identify these encodings.
-    """
-
-    def __init__(self, lang_filter=None):
-        super(EscCharSetProber, self).__init__(lang_filter=lang_filter)
-        self.coding_sm = []
-        if self.lang_filter & LanguageFilter.CHINESE_SIMPLIFIED:
-            self.coding_sm.append(CodingStateMachine(HZ_SM_MODEL))
-            self.coding_sm.append(CodingStateMachine(ISO2022CN_SM_MODEL))
-        if self.lang_filter & LanguageFilter.JAPANESE:
-            self.coding_sm.append(CodingStateMachine(ISO2022JP_SM_MODEL))
-        if self.lang_filter & LanguageFilter.KOREAN:
-            self.coding_sm.append(CodingStateMachine(ISO2022KR_SM_MODEL))
-        self.active_sm_count = None
-        self._detected_charset = None
-        self._detected_language = None
-        self._state = None
-        self.reset()
-
-    def reset(self):
-        super(EscCharSetProber, self).reset()
-        for coding_sm in self.coding_sm:
-            if not coding_sm:
-                continue
-            coding_sm.active = True
-            coding_sm.reset()
-        self.active_sm_count = len(self.coding_sm)
-        self._detected_charset = None
-        self._detected_language = None
-
-    @property
-    def charset_name(self):
-        return self._detected_charset
-
-    @property
-    def language(self):
-        return self._detected_language
-
-    def get_confidence(self):
-        if self._detected_charset:
-            return 0.99
-        else:
-            return 0.00
-
-    def feed(self, byte_str):
-        for c in byte_str:
-            for coding_sm in self.coding_sm:
-                if not coding_sm or not coding_sm.active:
-                    continue
-                coding_state = coding_sm.next_state(c)
-                if coding_state == MachineState.ERROR:
-                    coding_sm.active = False
-                    self.active_sm_count -= 1
-                    if self.active_sm_count <= 0:
-                        self._state = ProbingState.NOT_ME
-                        return self.state
-                elif coding_state == MachineState.ITS_ME:
-                    self._state = ProbingState.FOUND_IT
-                    self._detected_charset = coding_sm.get_coding_state_machine()
-                    self._detected_language = coding_sm.language
-                    return self.state
-
-        return self.state
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/escsm.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/escsm.py
deleted file mode 100644
index 0069523..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/escsm.py
+++ /dev/null
@@ -1,246 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .enums import MachineState
-
-HZ_CLS = (
-1,0,0,0,0,0,0,0,  # 00 - 07
-0,0,0,0,0,0,0,0,  # 08 - 0f
-0,0,0,0,0,0,0,0,  # 10 - 17
-0,0,0,1,0,0,0,0,  # 18 - 1f
-0,0,0,0,0,0,0,0,  # 20 - 27
-0,0,0,0,0,0,0,0,  # 28 - 2f
-0,0,0,0,0,0,0,0,  # 30 - 37
-0,0,0,0,0,0,0,0,  # 38 - 3f
-0,0,0,0,0,0,0,0,  # 40 - 47
-0,0,0,0,0,0,0,0,  # 48 - 4f
-0,0,0,0,0,0,0,0,  # 50 - 57
-0,0,0,0,0,0,0,0,  # 58 - 5f
-0,0,0,0,0,0,0,0,  # 60 - 67
-0,0,0,0,0,0,0,0,  # 68 - 6f
-0,0,0,0,0,0,0,0,  # 70 - 77
-0,0,0,4,0,5,2,0,  # 78 - 7f
-1,1,1,1,1,1,1,1,  # 80 - 87
-1,1,1,1,1,1,1,1,  # 88 - 8f
-1,1,1,1,1,1,1,1,  # 90 - 97
-1,1,1,1,1,1,1,1,  # 98 - 9f
-1,1,1,1,1,1,1,1,  # a0 - a7
-1,1,1,1,1,1,1,1,  # a8 - af
-1,1,1,1,1,1,1,1,  # b0 - b7
-1,1,1,1,1,1,1,1,  # b8 - bf
-1,1,1,1,1,1,1,1,  # c0 - c7
-1,1,1,1,1,1,1,1,  # c8 - cf
-1,1,1,1,1,1,1,1,  # d0 - d7
-1,1,1,1,1,1,1,1,  # d8 - df
-1,1,1,1,1,1,1,1,  # e0 - e7
-1,1,1,1,1,1,1,1,  # e8 - ef
-1,1,1,1,1,1,1,1,  # f0 - f7
-1,1,1,1,1,1,1,1,  # f8 - ff
-)
-
-HZ_ST = (
-MachineState.START,MachineState.ERROR,     3,MachineState.START,MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,# 00-07
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,# 08-0f
-MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,     4,MachineState.ERROR,# 10-17
-     5,MachineState.ERROR,     6,MachineState.ERROR,     5,     5,     4,MachineState.ERROR,# 18-1f
-     4,MachineState.ERROR,     4,     4,     4,MachineState.ERROR,     4,MachineState.ERROR,# 20-27
-     4,MachineState.ITS_ME,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,# 28-2f
-)
-
-HZ_CHAR_LEN_TABLE = (0, 0, 0, 0, 0, 0)
-
-HZ_SM_MODEL = {'class_table': HZ_CLS,
-               'class_factor': 6,
-               'state_table': HZ_ST,
-               'char_len_table': HZ_CHAR_LEN_TABLE,
-               'name': "HZ-GB-2312",
-               'language': 'Chinese'}
-
-ISO2022CN_CLS = (
-2,0,0,0,0,0,0,0,  # 00 - 07
-0,0,0,0,0,0,0,0,  # 08 - 0f
-0,0,0,0,0,0,0,0,  # 10 - 17
-0,0,0,1,0,0,0,0,  # 18 - 1f
-0,0,0,0,0,0,0,0,  # 20 - 27
-0,3,0,0,0,0,0,0,  # 28 - 2f
-0,0,0,0,0,0,0,0,  # 30 - 37
-0,0,0,0,0,0,0,0,  # 38 - 3f
-0,0,0,4,0,0,0,0,  # 40 - 47
-0,0,0,0,0,0,0,0,  # 48 - 4f
-0,0,0,0,0,0,0,0,  # 50 - 57
-0,0,0,0,0,0,0,0,  # 58 - 5f
-0,0,0,0,0,0,0,0,  # 60 - 67
-0,0,0,0,0,0,0,0,  # 68 - 6f
-0,0,0,0,0,0,0,0,  # 70 - 77
-0,0,0,0,0,0,0,0,  # 78 - 7f
-2,2,2,2,2,2,2,2,  # 80 - 87
-2,2,2,2,2,2,2,2,  # 88 - 8f
-2,2,2,2,2,2,2,2,  # 90 - 97
-2,2,2,2,2,2,2,2,  # 98 - 9f
-2,2,2,2,2,2,2,2,  # a0 - a7
-2,2,2,2,2,2,2,2,  # a8 - af
-2,2,2,2,2,2,2,2,  # b0 - b7
-2,2,2,2,2,2,2,2,  # b8 - bf
-2,2,2,2,2,2,2,2,  # c0 - c7
-2,2,2,2,2,2,2,2,  # c8 - cf
-2,2,2,2,2,2,2,2,  # d0 - d7
-2,2,2,2,2,2,2,2,  # d8 - df
-2,2,2,2,2,2,2,2,  # e0 - e7
-2,2,2,2,2,2,2,2,  # e8 - ef
-2,2,2,2,2,2,2,2,  # f0 - f7
-2,2,2,2,2,2,2,2,  # f8 - ff
-)
-
-ISO2022CN_ST = (
-MachineState.START,     3,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,# 00-07
-MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,# 08-0f
-MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,# 10-17
-MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     4,MachineState.ERROR,# 18-1f
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,# 20-27
-     5,     6,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,# 28-2f
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,# 30-37
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,MachineState.START,# 38-3f
-)
-
-ISO2022CN_CHAR_LEN_TABLE = (0, 0, 0, 0, 0, 0, 0, 0, 0)
-
-ISO2022CN_SM_MODEL = {'class_table': ISO2022CN_CLS,
-                      'class_factor': 9,
-                      'state_table': ISO2022CN_ST,
-                      'char_len_table': ISO2022CN_CHAR_LEN_TABLE,
-                      'name': "ISO-2022-CN",
-                      'language': 'Chinese'}
-
-ISO2022JP_CLS = (
-2,0,0,0,0,0,0,0,  # 00 - 07
-0,0,0,0,0,0,2,2,  # 08 - 0f
-0,0,0,0,0,0,0,0,  # 10 - 17
-0,0,0,1,0,0,0,0,  # 18 - 1f
-0,0,0,0,7,0,0,0,  # 20 - 27
-3,0,0,0,0,0,0,0,  # 28 - 2f
-0,0,0,0,0,0,0,0,  # 30 - 37
-0,0,0,0,0,0,0,0,  # 38 - 3f
-6,0,4,0,8,0,0,0,  # 40 - 47
-0,9,5,0,0,0,0,0,  # 48 - 4f
-0,0,0,0,0,0,0,0,  # 50 - 57
-0,0,0,0,0,0,0,0,  # 58 - 5f
-0,0,0,0,0,0,0,0,  # 60 - 67
-0,0,0,0,0,0,0,0,  # 68 - 6f
-0,0,0,0,0,0,0,0,  # 70 - 77
-0,0,0,0,0,0,0,0,  # 78 - 7f
-2,2,2,2,2,2,2,2,  # 80 - 87
-2,2,2,2,2,2,2,2,  # 88 - 8f
-2,2,2,2,2,2,2,2,  # 90 - 97
-2,2,2,2,2,2,2,2,  # 98 - 9f
-2,2,2,2,2,2,2,2,  # a0 - a7
-2,2,2,2,2,2,2,2,  # a8 - af
-2,2,2,2,2,2,2,2,  # b0 - b7
-2,2,2,2,2,2,2,2,  # b8 - bf
-2,2,2,2,2,2,2,2,  # c0 - c7
-2,2,2,2,2,2,2,2,  # c8 - cf
-2,2,2,2,2,2,2,2,  # d0 - d7
-2,2,2,2,2,2,2,2,  # d8 - df
-2,2,2,2,2,2,2,2,  # e0 - e7
-2,2,2,2,2,2,2,2,  # e8 - ef
-2,2,2,2,2,2,2,2,  # f0 - f7
-2,2,2,2,2,2,2,2,  # f8 - ff
-)
-
-ISO2022JP_ST = (
-MachineState.START,     3,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,# 00-07
-MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,# 08-0f
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,# 10-17
-MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,# 18-1f
-MachineState.ERROR,     5,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     4,MachineState.ERROR,MachineState.ERROR,# 20-27
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     6,MachineState.ITS_ME,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,# 28-2f
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,# 30-37
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,# 38-3f
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,MachineState.START,MachineState.START,# 40-47
-)
-
-ISO2022JP_CHAR_LEN_TABLE = (0, 0, 0, 0, 0, 0, 0, 0, 0, 0)
-
-ISO2022JP_SM_MODEL = {'class_table': ISO2022JP_CLS,
-                      'class_factor': 10,
-                      'state_table': ISO2022JP_ST,
-                      'char_len_table': ISO2022JP_CHAR_LEN_TABLE,
-                      'name': "ISO-2022-JP",
-                      'language': 'Japanese'}
-
-ISO2022KR_CLS = (
-2,0,0,0,0,0,0,0,  # 00 - 07
-0,0,0,0,0,0,0,0,  # 08 - 0f
-0,0,0,0,0,0,0,0,  # 10 - 17
-0,0,0,1,0,0,0,0,  # 18 - 1f
-0,0,0,0,3,0,0,0,  # 20 - 27
-0,4,0,0,0,0,0,0,  # 28 - 2f
-0,0,0,0,0,0,0,0,  # 30 - 37
-0,0,0,0,0,0,0,0,  # 38 - 3f
-0,0,0,5,0,0,0,0,  # 40 - 47
-0,0,0,0,0,0,0,0,  # 48 - 4f
-0,0,0,0,0,0,0,0,  # 50 - 57
-0,0,0,0,0,0,0,0,  # 58 - 5f
-0,0,0,0,0,0,0,0,  # 60 - 67
-0,0,0,0,0,0,0,0,  # 68 - 6f
-0,0,0,0,0,0,0,0,  # 70 - 77
-0,0,0,0,0,0,0,0,  # 78 - 7f
-2,2,2,2,2,2,2,2,  # 80 - 87
-2,2,2,2,2,2,2,2,  # 88 - 8f
-2,2,2,2,2,2,2,2,  # 90 - 97
-2,2,2,2,2,2,2,2,  # 98 - 9f
-2,2,2,2,2,2,2,2,  # a0 - a7
-2,2,2,2,2,2,2,2,  # a8 - af
-2,2,2,2,2,2,2,2,  # b0 - b7
-2,2,2,2,2,2,2,2,  # b8 - bf
-2,2,2,2,2,2,2,2,  # c0 - c7
-2,2,2,2,2,2,2,2,  # c8 - cf
-2,2,2,2,2,2,2,2,  # d0 - d7
-2,2,2,2,2,2,2,2,  # d8 - df
-2,2,2,2,2,2,2,2,  # e0 - e7
-2,2,2,2,2,2,2,2,  # e8 - ef
-2,2,2,2,2,2,2,2,  # f0 - f7
-2,2,2,2,2,2,2,2,  # f8 - ff
-)
-
-ISO2022KR_ST = (
-MachineState.START,     3,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,# 00-07
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,# 08-0f
-MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     4,MachineState.ERROR,MachineState.ERROR,# 10-17
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     5,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,# 18-1f
-MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.START,MachineState.START,MachineState.START,MachineState.START,# 20-27
-)
-
-ISO2022KR_CHAR_LEN_TABLE = (0, 0, 0, 0, 0, 0)
-
-ISO2022KR_SM_MODEL = {'class_table': ISO2022KR_CLS,
-                      'class_factor': 6,
-                      'state_table': ISO2022KR_ST,
-                      'char_len_table': ISO2022KR_CHAR_LEN_TABLE,
-                      'name': "ISO-2022-KR",
-                      'language': 'Korean'}
-
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/eucjpprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/eucjpprober.py
deleted file mode 100644
index 20ce8f7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/eucjpprober.py
+++ /dev/null
@@ -1,92 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .enums import ProbingState, MachineState
-from .mbcharsetprober import MultiByteCharSetProber
-from .codingstatemachine import CodingStateMachine
-from .chardistribution import EUCJPDistributionAnalysis
-from .jpcntx import EUCJPContextAnalysis
-from .mbcssm import EUCJP_SM_MODEL
-
-
-class EUCJPProber(MultiByteCharSetProber):
-    def __init__(self):
-        super(EUCJPProber, self).__init__()
-        self.coding_sm = CodingStateMachine(EUCJP_SM_MODEL)
-        self.distribution_analyzer = EUCJPDistributionAnalysis()
-        self.context_analyzer = EUCJPContextAnalysis()
-        self.reset()
-
-    def reset(self):
-        super(EUCJPProber, self).reset()
-        self.context_analyzer.reset()
-
-    @property
-    def charset_name(self):
-        return "EUC-JP"
-
-    @property
-    def language(self):
-        return "Japanese"
-
-    def feed(self, byte_str):
-        for i in range(len(byte_str)):
-            # PY3K: byte_str is a byte array, so byte_str[i] is an int, not a byte
-            coding_state = self.coding_sm.next_state(byte_str[i])
-            if coding_state == MachineState.ERROR:
-                self.logger.debug('%s %s prober hit error at byte %s',
-                                  self.charset_name, self.language, i)
-                self._state = ProbingState.NOT_ME
-                break
-            elif coding_state == MachineState.ITS_ME:
-                self._state = ProbingState.FOUND_IT
-                break
-            elif coding_state == MachineState.START:
-                char_len = self.coding_sm.get_current_charlen()
-                if i == 0:
-                    self._last_char[1] = byte_str[0]
-                    self.context_analyzer.feed(self._last_char, char_len)
-                    self.distribution_analyzer.feed(self._last_char, char_len)
-                else:
-                    self.context_analyzer.feed(byte_str[i - 1:i + 1],
-                                                char_len)
-                    self.distribution_analyzer.feed(byte_str[i - 1:i + 1],
-                                                     char_len)
-
-        self._last_char[0] = byte_str[-1]
-
-        if self.state == ProbingState.DETECTING:
-            if (self.context_analyzer.got_enough_data() and
-               (self.get_confidence() > self.SHORTCUT_THRESHOLD)):
-                self._state = ProbingState.FOUND_IT
-
-        return self.state
-
-    def get_confidence(self):
-        context_conf = self.context_analyzer.get_confidence()
-        distrib_conf = self.distribution_analyzer.get_confidence()
-        return max(context_conf, distrib_conf)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euckrfreq.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euckrfreq.py
deleted file mode 100644
index b68078c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euckrfreq.py
+++ /dev/null
@@ -1,195 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# Sampling from about 20M text materials include literature and computer technology
-
-# 128  --> 0.79
-# 256  --> 0.92
-# 512  --> 0.986
-# 1024 --> 0.99944
-# 2048 --> 0.99999
-#
-# Idea Distribution Ratio = 0.98653 / (1-0.98653) = 73.24
-# Random Distribution Ration = 512 / (2350-512) = 0.279.
-#
-# Typical Distribution Ratio
-
-EUCKR_TYPICAL_DISTRIBUTION_RATIO = 6.0
-
-EUCKR_TABLE_SIZE = 2352
-
-# Char to FreqOrder table ,
-EUCKR_CHAR_TO_FREQ_ORDER = (
-  13, 130, 120,1396, 481,1719,1720, 328, 609, 212,1721, 707, 400, 299,1722,  87,
-1397,1723, 104, 536,1117,1203,1724,1267, 685,1268, 508,1725,1726,1727,1728,1398,
-1399,1729,1730,1731, 141, 621, 326,1057, 368,1732, 267, 488,  20,1733,1269,1734,
- 945,1400,1735,  47, 904,1270,1736,1737, 773, 248,1738, 409, 313, 786, 429,1739,
- 116, 987, 813,1401, 683,  75,1204, 145,1740,1741,1742,1743,  16, 847, 667, 622,
- 708,1744,1745,1746, 966, 787, 304, 129,1747,  60, 820, 123, 676,1748,1749,1750,
-1751, 617,1752, 626,1753,1754,1755,1756, 653,1757,1758,1759,1760,1761,1762, 856,
- 344,1763,1764,1765,1766,  89, 401, 418, 806, 905, 848,1767,1768,1769, 946,1205,
- 709,1770,1118,1771, 241,1772,1773,1774,1271,1775, 569,1776, 999,1777,1778,1779,
-1780, 337, 751,1058,  28, 628, 254,1781, 177, 906, 270, 349, 891,1079,1782,  19,
-1783, 379,1784, 315,1785, 629, 754,1402, 559,1786, 636, 203,1206,1787, 710, 567,
-1788, 935, 814,1789,1790,1207, 766, 528,1791,1792,1208,1793,1794,1795,1796,1797,
-1403,1798,1799, 533,1059,1404,1405,1156,1406, 936, 884,1080,1800, 351,1801,1802,
-1803,1804,1805, 801,1806,1807,1808,1119,1809,1157, 714, 474,1407,1810, 298, 899,
- 885,1811,1120, 802,1158,1812, 892,1813,1814,1408, 659,1815,1816,1121,1817,1818,
-1819,1820,1821,1822, 319,1823, 594, 545,1824, 815, 937,1209,1825,1826, 573,1409,
-1022,1827,1210,1828,1829,1830,1831,1832,1833, 556, 722, 807,1122,1060,1834, 697,
-1835, 900, 557, 715,1836,1410, 540,1411, 752,1159, 294, 597,1211, 976, 803, 770,
-1412,1837,1838,  39, 794,1413, 358,1839, 371, 925,1840, 453, 661, 788, 531, 723,
- 544,1023,1081, 869,  91,1841, 392, 430, 790, 602,1414, 677,1082, 457,1415,1416,
-1842,1843, 475, 327,1024,1417, 795, 121,1844, 733, 403,1418,1845,1846,1847, 300,
- 119, 711,1212, 627,1848,1272, 207,1849,1850, 796,1213, 382,1851, 519,1852,1083,
- 893,1853,1854,1855, 367, 809, 487, 671,1856, 663,1857,1858, 956, 471, 306, 857,
-1859,1860,1160,1084,1861,1862,1863,1864,1865,1061,1866,1867,1868,1869,1870,1871,
- 282,  96, 574,1872, 502,1085,1873,1214,1874, 907,1875,1876, 827, 977,1419,1420,
-1421, 268,1877,1422,1878,1879,1880, 308,1881,   2, 537,1882,1883,1215,1884,1885,
- 127, 791,1886,1273,1423,1887,  34, 336, 404, 643,1888, 571, 654, 894, 840,1889,
-   0, 886,1274, 122, 575, 260, 908, 938,1890,1275, 410, 316,1891,1892, 100,1893,
-1894,1123,  48,1161,1124,1025,1895, 633, 901,1276,1896,1897, 115, 816,1898, 317,
-1899, 694,1900, 909, 734,1424, 572, 866,1425, 691,  85, 524,1010, 543, 394, 841,
-1901,1902,1903,1026,1904,1905,1906,1907,1908,1909,  30, 451, 651, 988, 310,1910,
-1911,1426, 810,1216,  93,1912,1913,1277,1217,1914, 858, 759,  45,  58, 181, 610,
- 269,1915,1916, 131,1062, 551, 443,1000, 821,1427, 957, 895,1086,1917,1918, 375,
-1919, 359,1920, 687,1921, 822,1922, 293,1923,1924,  40, 662, 118, 692,  29, 939,
- 887, 640, 482, 174,1925,  69,1162, 728,1428, 910,1926,1278,1218,1279, 386, 870,
- 217, 854,1163, 823,1927,1928,1929,1930, 834,1931,  78,1932, 859,1933,1063,1934,
-1935,1936,1937, 438,1164, 208, 595,1938,1939,1940,1941,1219,1125,1942, 280, 888,
-1429,1430,1220,1431,1943,1944,1945,1946,1947,1280, 150, 510,1432,1948,1949,1950,
-1951,1952,1953,1954,1011,1087,1955,1433,1043,1956, 881,1957, 614, 958,1064,1065,
-1221,1958, 638,1001, 860, 967, 896,1434, 989, 492, 553,1281,1165,1959,1282,1002,
-1283,1222,1960,1961,1962,1963,  36, 383, 228, 753, 247, 454,1964, 876, 678,1965,
-1966,1284, 126, 464, 490, 835, 136, 672, 529, 940,1088,1435, 473,1967,1968, 467,
-  50, 390, 227, 587, 279, 378, 598, 792, 968, 240, 151, 160, 849, 882,1126,1285,
- 639,1044, 133, 140, 288, 360, 811, 563,1027, 561, 142, 523,1969,1970,1971,   7,
- 103, 296, 439, 407, 506, 634, 990,1972,1973,1974,1975, 645,1976,1977,1978,1979,
-1980,1981, 236,1982,1436,1983,1984,1089, 192, 828, 618, 518,1166, 333,1127,1985,
- 818,1223,1986,1987,1988,1989,1990,1991,1992,1993, 342,1128,1286, 746, 842,1994,
-1995, 560, 223,1287,  98,   8, 189, 650, 978,1288,1996,1437,1997,  17, 345, 250,
- 423, 277, 234, 512, 226,  97, 289,  42, 167,1998, 201,1999,2000, 843, 836, 824,
- 532, 338, 783,1090, 182, 576, 436,1438,1439, 527, 500,2001, 947, 889,2002,2003,
-2004,2005, 262, 600, 314, 447,2006, 547,2007, 693, 738,1129,2008,  71,1440, 745,
- 619, 688,2009, 829,2010,2011, 147,2012,  33, 948,2013,2014,  74, 224,2015,  61,
- 191, 918, 399, 637,2016,1028,1130, 257, 902,2017,2018,2019,2020,2021,2022,2023,
-2024,2025,2026, 837,2027,2028,2029,2030, 179, 874, 591,  52, 724, 246,2031,2032,
-2033,2034,1167, 969,2035,1289, 630, 605, 911,1091,1168,2036,2037,2038,1441, 912,
-2039, 623,2040,2041, 253,1169,1290,2042,1442, 146, 620, 611, 577, 433,2043,1224,
- 719,1170, 959, 440, 437, 534,  84, 388, 480,1131, 159, 220, 198, 679,2044,1012,
- 819,1066,1443, 113,1225, 194, 318,1003,1029,2045,2046,2047,2048,1067,2049,2050,
-2051,2052,2053,  59, 913, 112,2054, 632,2055, 455, 144, 739,1291,2056, 273, 681,
- 499,2057, 448,2058,2059, 760,2060,2061, 970, 384, 169, 245,1132,2062,2063, 414,
-1444,2064,2065,  41, 235,2066, 157, 252, 877, 568, 919, 789, 580,2067, 725,2068,
-2069,1292,2070,2071,1445,2072,1446,2073,2074,  55, 588,  66,1447, 271,1092,2075,
-1226,2076, 960,1013, 372,2077,2078,2079,2080,2081,1293,2082,2083,2084,2085, 850,
-2086,2087,2088,2089,2090, 186,2091,1068, 180,2092,2093,2094, 109,1227, 522, 606,
-2095, 867,1448,1093, 991,1171, 926, 353,1133,2096, 581,2097,2098,2099,1294,1449,
-1450,2100, 596,1172,1014,1228,2101,1451,1295,1173,1229,2102,2103,1296,1134,1452,
- 949,1135,2104,2105,1094,1453,1454,1455,2106,1095,2107,2108,2109,2110,2111,2112,
-2113,2114,2115,2116,2117, 804,2118,2119,1230,1231, 805,1456, 405,1136,2120,2121,
-2122,2123,2124, 720, 701,1297, 992,1457, 927,1004,2125,2126,2127,2128,2129,2130,
-  22, 417,2131, 303,2132, 385,2133, 971, 520, 513,2134,1174,  73,1096, 231, 274,
- 962,1458, 673,2135,1459,2136, 152,1137,2137,2138,2139,2140,1005,1138,1460,1139,
-2141,2142,2143,2144,  11, 374, 844,2145, 154,1232,  46,1461,2146, 838, 830, 721,
-1233, 106,2147,  90, 428, 462, 578, 566,1175, 352,2148,2149, 538,1234, 124,1298,
-2150,1462, 761, 565,2151, 686,2152, 649,2153,  72, 173,2154, 460, 415,2155,1463,
-2156,1235, 305,2157,2158,2159,2160,2161,2162, 579,2163,2164,2165,2166,2167, 747,
-2168,2169,2170,2171,1464, 669,2172,2173,2174,2175,2176,1465,2177,  23, 530, 285,
-2178, 335, 729,2179, 397,2180,2181,2182,1030,2183,2184, 698,2185,2186, 325,2187,
-2188, 369,2189, 799,1097,1015, 348,2190,1069, 680,2191, 851,1466,2192,2193,  10,
-2194, 613, 424,2195, 979, 108, 449, 589,  27, 172,  81,1031,  80, 774, 281, 350,
-1032, 525, 301, 582,1176,2196, 674,1045,2197,2198,1467, 730, 762,2199,2200,2201,
-2202,1468,2203, 993,2204,2205, 266,1070, 963,1140,2206,2207,2208, 664,1098, 972,
-2209,2210,2211,1177,1469,1470, 871,2212,2213,2214,2215,2216,1471,2217,2218,2219,
-2220,2221,2222,2223,2224,2225,2226,2227,1472,1236,2228,2229,2230,2231,2232,2233,
-2234,2235,1299,2236,2237, 200,2238, 477, 373,2239,2240, 731, 825, 777,2241,2242,
-2243, 521, 486, 548,2244,2245,2246,1473,1300,  53, 549, 137, 875,  76, 158,2247,
-1301,1474, 469, 396,1016, 278, 712,2248, 321, 442, 503, 767, 744, 941,1237,1178,
-1475,2249,  82, 178,1141,1179, 973,2250,1302,2251, 297,2252,2253, 570,2254,2255,
-2256,  18, 450, 206,2257, 290, 292,1142,2258, 511, 162,  99, 346, 164, 735,2259,
-1476,1477,   4, 554, 343, 798,1099,2260,1100,2261,  43, 171,1303, 139, 215,2262,
-2263, 717, 775,2264,1033, 322, 216,2265, 831,2266, 149,2267,1304,2268,2269, 702,
-1238, 135, 845, 347, 309,2270, 484,2271, 878, 655, 238,1006,1478,2272,  67,2273,
- 295,2274,2275, 461,2276, 478, 942, 412,2277,1034,2278,2279,2280, 265,2281, 541,
-2282,2283,2284,2285,2286,  70, 852,1071,2287,2288,2289,2290,  21,  56, 509, 117,
- 432,2291,2292, 331, 980, 552,1101, 148, 284, 105, 393,1180,1239, 755,2293, 187,
-2294,1046,1479,2295, 340,2296,  63,1047, 230,2297,2298,1305, 763,1306, 101, 800,
- 808, 494,2299,2300,2301, 903,2302,  37,1072,  14,   5,2303,  79, 675,2304, 312,
-2305,2306,2307,2308,2309,1480,   6,1307,2310,2311,2312,   1, 470,  35,  24, 229,
-2313, 695, 210,  86, 778,  15, 784, 592, 779,  32,  77, 855, 964,2314, 259,2315,
- 501, 380,2316,2317,  83, 981, 153, 689,1308,1481,1482,1483,2318,2319, 716,1484,
-2320,2321,2322,2323,2324,2325,1485,2326,2327, 128,  57,  68, 261,1048, 211, 170,
-1240,  31,2328,  51, 435, 742,2329,2330,2331, 635,2332, 264, 456,2333,2334,2335,
- 425,2336,1486, 143, 507, 263, 943,2337, 363, 920,1487, 256,1488,1102, 243, 601,
-1489,2338,2339,2340,2341,2342,2343,2344, 861,2345,2346,2347,2348,2349,2350, 395,
-2351,1490,1491,  62, 535, 166, 225,2352,2353, 668, 419,1241, 138, 604, 928,2354,
-1181,2355,1492,1493,2356,2357,2358,1143,2359, 696,2360, 387, 307,1309, 682, 476,
-2361,2362, 332,  12, 222, 156,2363, 232,2364, 641, 276, 656, 517,1494,1495,1035,
- 416, 736,1496,2365,1017, 586,2366,2367,2368,1497,2369, 242,2370,2371,2372,1498,
-2373, 965, 713,2374,2375,2376,2377, 740, 982,1499, 944,1500,1007,2378,2379,1310,
-1501,2380,2381,2382, 785, 329,2383,2384,1502,2385,2386,2387, 932,2388,1503,2389,
-2390,2391,2392,1242,2393,2394,2395,2396,2397, 994, 950,2398,2399,2400,2401,1504,
-1311,2402,2403,2404,2405,1049, 749,2406,2407, 853, 718,1144,1312,2408,1182,1505,
-2409,2410, 255, 516, 479, 564, 550, 214,1506,1507,1313, 413, 239, 444, 339,1145,
-1036,1508,1509,1314,1037,1510,1315,2411,1511,2412,2413,2414, 176, 703, 497, 624,
- 593, 921, 302,2415, 341, 165,1103,1512,2416,1513,2417,2418,2419, 376,2420, 700,
-2421,2422,2423, 258, 768,1316,2424,1183,2425, 995, 608,2426,2427,2428,2429, 221,
-2430,2431,2432,2433,2434,2435,2436,2437, 195, 323, 726, 188, 897, 983,1317, 377,
- 644,1050, 879,2438, 452,2439,2440,2441,2442,2443,2444, 914,2445,2446,2447,2448,
- 915, 489,2449,1514,1184,2450,2451, 515,  64, 427, 495,2452, 583,2453, 483, 485,
-1038, 562, 213,1515, 748, 666,2454,2455,2456,2457, 334,2458, 780, 996,1008, 705,
-1243,2459,2460,2461,2462,2463, 114,2464, 493,1146, 366, 163,1516, 961,1104,2465,
- 291,2466,1318,1105,2467,1517, 365,2468, 355, 951,1244,2469,1319,2470, 631,2471,
-2472, 218,1320, 364, 320, 756,1518,1519,1321,1520,1322,2473,2474,2475,2476, 997,
-2477,2478,2479,2480, 665,1185,2481, 916,1521,2482,2483,2484, 584, 684,2485,2486,
- 797,2487,1051,1186,2488,2489,2490,1522,2491,2492, 370,2493,1039,1187,  65,2494,
- 434, 205, 463,1188,2495, 125, 812, 391, 402, 826, 699, 286, 398, 155, 781, 771,
- 585,2496, 590, 505,1073,2497, 599, 244, 219, 917,1018, 952, 646,1523,2498,1323,
-2499,2500,  49, 984, 354, 741,2501, 625,2502,1324,2503,1019, 190, 357, 757, 491,
-  95, 782, 868,2504,2505,2506,2507,2508,2509, 134,1524,1074, 422,1525, 898,2510,
- 161,2511,2512,2513,2514, 769,2515,1526,2516,2517, 411,1325,2518, 472,1527,2519,
-2520,2521,2522,2523,2524, 985,2525,2526,2527,2528,2529,2530, 764,2531,1245,2532,
-2533,  25, 204, 311,2534, 496,2535,1052,2536,2537,2538,2539,2540,2541,2542, 199,
- 704, 504, 468, 758, 657,1528, 196,  44, 839,1246, 272, 750,2543, 765, 862,2544,
-2545,1326,2546, 132, 615, 933,2547, 732,2548,2549,2550,1189,1529,2551, 283,1247,
-1053, 607, 929,2552,2553,2554, 930, 183, 872, 616,1040,1147,2555,1148,1020, 441,
- 249,1075,2556,2557,2558, 466, 743,2559,2560,2561,  92, 514, 426, 420, 526,2562,
-2563,2564,2565,2566,2567,2568, 185,2569,2570,2571,2572, 776,1530, 658,2573, 362,
-2574, 361, 922,1076, 793,2575,2576,2577,2578,2579,2580,1531, 251,2581,2582,2583,
-2584,1532,  54, 612, 237,1327,2585,2586, 275, 408, 647, 111,2587,1533,1106, 465,
-   3, 458,   9,  38,2588, 107, 110, 890, 209,  26, 737, 498,2589,1534,2590, 431,
- 202,  88,1535, 356, 287,1107, 660,1149,2591, 381,1536, 986,1150, 445,1248,1151,
- 974,2592,2593, 846,2594, 446, 953, 184,1249,1250, 727,2595, 923, 193, 883,2596,
-2597,2598, 102, 324, 539, 817,2599, 421,1041,2600, 832,2601,  94, 175, 197, 406,
-2602, 459,2603,2604,2605,2606,2607, 330, 555,2608,2609,2610, 706,1108, 389,2611,
-2612,2613,2614, 233,2615, 833, 558, 931, 954,1251,2616,2617,1537, 546,2618,2619,
-1009,2620,2621,2622,1538, 690,1328,2623, 955,2624,1539,2625,2626, 772,2627,2628,
-2629,2630,2631, 924, 648, 863, 603,2632,2633, 934,1540, 864, 865,2634, 642,1042,
- 670,1190,2635,2636,2637,2638, 168,2639, 652, 873, 542,1054,1541,2640,2641,2642,  # 512, 256
-)
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euckrprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euckrprober.py
deleted file mode 100644
index 345a060..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euckrprober.py
+++ /dev/null
@@ -1,47 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .mbcharsetprober import MultiByteCharSetProber
-from .codingstatemachine import CodingStateMachine
-from .chardistribution import EUCKRDistributionAnalysis
-from .mbcssm import EUCKR_SM_MODEL
-
-
-class EUCKRProber(MultiByteCharSetProber):
-    def __init__(self):
-        super(EUCKRProber, self).__init__()
-        self.coding_sm = CodingStateMachine(EUCKR_SM_MODEL)
-        self.distribution_analyzer = EUCKRDistributionAnalysis()
-        self.reset()
-
-    @property
-    def charset_name(self):
-        return "EUC-KR"
-
-    @property
-    def language(self):
-        return "Korean"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euctwfreq.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euctwfreq.py
deleted file mode 100644
index ed7a995..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euctwfreq.py
+++ /dev/null
@@ -1,387 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# EUCTW frequency table
-# Converted from big5 work
-# by Taiwan's Mandarin Promotion Council
-# <http:#www.edu.tw:81/mandr/>
-
-# 128  --> 0.42261
-# 256  --> 0.57851
-# 512  --> 0.74851
-# 1024 --> 0.89384
-# 2048 --> 0.97583
-#
-# Idea Distribution Ratio = 0.74851/(1-0.74851) =2.98
-# Random Distribution Ration = 512/(5401-512)=0.105
-#
-# Typical Distribution Ratio about 25% of Ideal one, still much higher than RDR
-
-EUCTW_TYPICAL_DISTRIBUTION_RATIO = 0.75
-
-# Char to FreqOrder table ,
-EUCTW_TABLE_SIZE = 5376
-
-EUCTW_CHAR_TO_FREQ_ORDER = (
-   1,1800,1506, 255,1431, 198,   9,  82,   6,7310, 177, 202,3615,1256,2808, 110,  # 2742
-3735,  33,3241, 261,  76,  44,2113,  16,2931,2184,1176, 659,3868,  26,3404,2643,  # 2758
-1198,3869,3313,4060, 410,2211, 302, 590, 361,1963,   8, 204,  58,4296,7311,1931,  # 2774
-  63,7312,7313, 317,1614,  75, 222, 159,4061,2412,1480,7314,3500,3068, 224,2809,  # 2790
-3616,   3,  10,3870,1471,  29,2774,1135,2852,1939, 873, 130,3242,1123, 312,7315,  # 2806
-4297,2051, 507, 252, 682,7316, 142,1914, 124, 206,2932,  34,3501,3173,  64, 604,  # 2822
-7317,2494,1976,1977, 155,1990, 645, 641,1606,7318,3405, 337,  72, 406,7319,  80,  # 2838
- 630, 238,3174,1509, 263, 939,1092,2644, 756,1440,1094,3406, 449,  69,2969, 591,  # 2854
- 179,2095, 471, 115,2034,1843,  60,  50,2970, 134, 806,1868, 734,2035,3407, 180,  # 2870
- 995,1607, 156, 537,2893, 688,7320, 319,1305, 779,2144, 514,2374, 298,4298, 359,  # 2886
-2495,  90,2707,1338, 663,  11, 906,1099,2545,  20,2436, 182, 532,1716,7321, 732,  # 2902
-1376,4062,1311,1420,3175,  25,2312,1056, 113, 399, 382,1949, 242,3408,2467, 529,  # 2918
-3243, 475,1447,3617,7322, 117,  21, 656, 810,1297,2295,2329,3502,7323, 126,4063,  # 2934
- 706, 456, 150, 613,4299,  71,1118,2036,4064, 145,3069,  85, 835, 486,2114,1246,  # 2950
-1426, 428, 727,1285,1015, 800, 106, 623, 303,1281,7324,2127,2354, 347,3736, 221,  # 2966
-3503,3110,7325,1955,1153,4065,  83, 296,1199,3070, 192, 624,  93,7326, 822,1897,  # 2982
-2810,3111, 795,2064, 991,1554,1542,1592,  27,  43,2853, 859, 139,1456, 860,4300,  # 2998
- 437, 712,3871, 164,2392,3112, 695, 211,3017,2096, 195,3872,1608,3504,3505,3618,  # 3014
-3873, 234, 811,2971,2097,3874,2229,1441,3506,1615,2375, 668,2076,1638, 305, 228,  # 3030
-1664,4301, 467, 415,7327, 262,2098,1593, 239, 108, 300, 200,1033, 512,1247,2077,  # 3046
-7328,7329,2173,3176,3619,2673, 593, 845,1062,3244,  88,1723,2037,3875,1950, 212,  # 3062
- 266, 152, 149, 468,1898,4066,4302,  77, 187,7330,3018,  37,   5,2972,7331,3876,  # 3078
-7332,7333,  39,2517,4303,2894,3177,2078,  55, 148,  74,4304, 545, 483,1474,1029,  # 3094
-1665, 217,1869,1531,3113,1104,2645,4067,  24, 172,3507, 900,3877,3508,3509,4305,  # 3110
-  32,1408,2811,1312, 329, 487,2355,2247,2708, 784,2674,   4,3019,3314,1427,1788,  # 3126
- 188, 109, 499,7334,3620,1717,1789, 888,1217,3020,4306,7335,3510,7336,3315,1520,  # 3142
-3621,3878, 196,1034, 775,7337,7338, 929,1815, 249, 439,  38,7339,1063,7340, 794,  # 3158
-3879,1435,2296,  46, 178,3245,2065,7341,2376,7342, 214,1709,4307, 804,  35, 707,  # 3174
- 324,3622,1601,2546, 140, 459,4068,7343,7344,1365, 839, 272, 978,2257,2572,3409,  # 3190
-2128,1363,3623,1423, 697, 100,3071,  48,  70,1231, 495,3114,2193,7345,1294,7346,  # 3206
-2079, 462, 586,1042,3246, 853, 256, 988, 185,2377,3410,1698, 434,1084,7347,3411,  # 3222
- 314,2615,2775,4308,2330,2331, 569,2280, 637,1816,2518, 757,1162,1878,1616,3412,  # 3238
- 287,1577,2115, 768,4309,1671,2854,3511,2519,1321,3737, 909,2413,7348,4069, 933,  # 3254
-3738,7349,2052,2356,1222,4310, 765,2414,1322, 786,4311,7350,1919,1462,1677,2895,  # 3270
-1699,7351,4312,1424,2437,3115,3624,2590,3316,1774,1940,3413,3880,4070, 309,1369,  # 3286
-1130,2812, 364,2230,1653,1299,3881,3512,3882,3883,2646, 525,1085,3021, 902,2000,  # 3302
-1475, 964,4313, 421,1844,1415,1057,2281, 940,1364,3116, 376,4314,4315,1381,   7,  # 3318
-2520, 983,2378, 336,1710,2675,1845, 321,3414, 559,1131,3022,2742,1808,1132,1313,  # 3334
- 265,1481,1857,7352, 352,1203,2813,3247, 167,1089, 420,2814, 776, 792,1724,3513,  # 3350
-4071,2438,3248,7353,4072,7354, 446, 229, 333,2743, 901,3739,1200,1557,4316,2647,  # 3366
-1920, 395,2744,2676,3740,4073,1835, 125, 916,3178,2616,4317,7355,7356,3741,7357,  # 3382
-7358,7359,4318,3117,3625,1133,2547,1757,3415,1510,2313,1409,3514,7360,2145, 438,  # 3398
-2591,2896,2379,3317,1068, 958,3023, 461, 311,2855,2677,4074,1915,3179,4075,1978,  # 3414
- 383, 750,2745,2617,4076, 274, 539, 385,1278,1442,7361,1154,1964, 384, 561, 210,  # 3430
-  98,1295,2548,3515,7362,1711,2415,1482,3416,3884,2897,1257, 129,7363,3742, 642,  # 3446
- 523,2776,2777,2648,7364, 141,2231,1333,  68, 176, 441, 876, 907,4077, 603,2592,  # 3462
- 710, 171,3417, 404, 549,  18,3118,2393,1410,3626,1666,7365,3516,4319,2898,4320,  # 3478
-7366,2973, 368,7367, 146, 366,  99, 871,3627,1543, 748, 807,1586,1185,  22,2258,  # 3494
- 379,3743,3180,7368,3181, 505,1941,2618,1991,1382,2314,7369, 380,2357, 218, 702,  # 3510
-1817,1248,3418,3024,3517,3318,3249,7370,2974,3628, 930,3250,3744,7371,  59,7372,  # 3526
- 585, 601,4078, 497,3419,1112,1314,4321,1801,7373,1223,1472,2174,7374, 749,1836,  # 3542
- 690,1899,3745,1772,3885,1476, 429,1043,1790,2232,2116, 917,4079, 447,1086,1629,  # 3558
-7375, 556,7376,7377,2020,1654, 844,1090, 105, 550, 966,1758,2815,1008,1782, 686,  # 3574
-1095,7378,2282, 793,1602,7379,3518,2593,4322,4080,2933,2297,4323,3746, 980,2496,  # 3590
- 544, 353, 527,4324, 908,2678,2899,7380, 381,2619,1942,1348,7381,1341,1252, 560,  # 3606
-3072,7382,3420,2856,7383,2053, 973, 886,2080, 143,4325,7384,7385, 157,3886, 496,  # 3622
-4081,  57, 840, 540,2038,4326,4327,3421,2117,1445, 970,2259,1748,1965,2081,4082,  # 3638
-3119,1234,1775,3251,2816,3629, 773,1206,2129,1066,2039,1326,3887,1738,1725,4083,  # 3654
- 279,3120,  51,1544,2594, 423,1578,2130,2066, 173,4328,1879,7386,7387,1583, 264,  # 3670
- 610,3630,4329,2439, 280, 154,7388,7389,7390,1739, 338,1282,3073, 693,2857,1411,  # 3686
-1074,3747,2440,7391,4330,7392,7393,1240, 952,2394,7394,2900,1538,2679, 685,1483,  # 3702
-4084,2468,1436, 953,4085,2054,4331, 671,2395,  79,4086,2441,3252, 608, 567,2680,  # 3718
-3422,4087,4088,1691, 393,1261,1791,2396,7395,4332,7396,7397,7398,7399,1383,1672,  # 3734
-3748,3182,1464, 522,1119, 661,1150, 216, 675,4333,3888,1432,3519, 609,4334,2681,  # 3750
-2397,7400,7401,7402,4089,3025,   0,7403,2469, 315, 231,2442, 301,3319,4335,2380,  # 3766
-7404, 233,4090,3631,1818,4336,4337,7405,  96,1776,1315,2082,7406, 257,7407,1809,  # 3782
-3632,2709,1139,1819,4091,2021,1124,2163,2778,1777,2649,7408,3074, 363,1655,3183,  # 3798
-7409,2975,7410,7411,7412,3889,1567,3890, 718, 103,3184, 849,1443, 341,3320,2934,  # 3814
-1484,7413,1712, 127,  67, 339,4092,2398, 679,1412, 821,7414,7415, 834, 738, 351,  # 3830
-2976,2146, 846, 235,1497,1880, 418,1992,3749,2710, 186,1100,2147,2746,3520,1545,  # 3846
-1355,2935,2858,1377, 583,3891,4093,2573,2977,7416,1298,3633,1078,2549,3634,2358,  # 3862
-  78,3750,3751, 267,1289,2099,2001,1594,4094, 348, 369,1274,2194,2175,1837,4338,  # 3878
-1820,2817,3635,2747,2283,2002,4339,2936,2748, 144,3321, 882,4340,3892,2749,3423,  # 3894
-4341,2901,7417,4095,1726, 320,7418,3893,3026, 788,2978,7419,2818,1773,1327,2859,  # 3910
-3894,2819,7420,1306,4342,2003,1700,3752,3521,2359,2650, 787,2022, 506, 824,3636,  # 3926
- 534, 323,4343,1044,3322,2023,1900, 946,3424,7421,1778,1500,1678,7422,1881,4344,  # 3942
- 165, 243,4345,3637,2521, 123, 683,4096, 764,4346,  36,3895,1792, 589,2902, 816,  # 3958
- 626,1667,3027,2233,1639,1555,1622,3753,3896,7423,3897,2860,1370,1228,1932, 891,  # 3974
-2083,2903, 304,4097,7424, 292,2979,2711,3522, 691,2100,4098,1115,4347, 118, 662,  # 3990
-7425, 611,1156, 854,2381,1316,2861,   2, 386, 515,2904,7426,7427,3253, 868,2234,  # 4006
-1486, 855,2651, 785,2212,3028,7428,1040,3185,3523,7429,3121, 448,7430,1525,7431,  # 4022
-2164,4348,7432,3754,7433,4099,2820,3524,3122, 503, 818,3898,3123,1568, 814, 676,  # 4038
-1444, 306,1749,7434,3755,1416,1030, 197,1428, 805,2821,1501,4349,7435,7436,7437,  # 4054
-1993,7438,4350,7439,7440,2195,  13,2779,3638,2980,3124,1229,1916,7441,3756,2131,  # 4070
-7442,4100,4351,2399,3525,7443,2213,1511,1727,1120,7444,7445, 646,3757,2443, 307,  # 4086
-7446,7447,1595,3186,7448,7449,7450,3639,1113,1356,3899,1465,2522,2523,7451, 519,  # 4102
-7452, 128,2132,  92,2284,1979,7453,3900,1512, 342,3125,2196,7454,2780,2214,1980,  # 4118
-3323,7455, 290,1656,1317, 789, 827,2360,7456,3758,4352, 562, 581,3901,7457, 401,  # 4134
-4353,2248,  94,4354,1399,2781,7458,1463,2024,4355,3187,1943,7459, 828,1105,4101,  # 4150
-1262,1394,7460,4102, 605,4356,7461,1783,2862,7462,2822, 819,2101, 578,2197,2937,  # 4166
-7463,1502, 436,3254,4103,3255,2823,3902,2905,3425,3426,7464,2712,2315,7465,7466,  # 4182
-2332,2067,  23,4357, 193, 826,3759,2102, 699,1630,4104,3075, 390,1793,1064,3526,  # 4198
-7467,1579,3076,3077,1400,7468,4105,1838,1640,2863,7469,4358,4359, 137,4106, 598,  # 4214
-3078,1966, 780, 104, 974,2938,7470, 278, 899, 253, 402, 572, 504, 493,1339,7471,  # 4230
-3903,1275,4360,2574,2550,7472,3640,3029,3079,2249, 565,1334,2713, 863,  41,7473,  # 4246
-7474,4361,7475,1657,2333,  19, 463,2750,4107, 606,7476,2981,3256,1087,2084,1323,  # 4262
-2652,2982,7477,1631,1623,1750,4108,2682,7478,2864, 791,2714,2653,2334, 232,2416,  # 4278
-7479,2983,1498,7480,2654,2620, 755,1366,3641,3257,3126,2025,1609, 119,1917,3427,  # 4294
- 862,1026,4109,7481,3904,3760,4362,3905,4363,2260,1951,2470,7482,1125, 817,4110,  # 4310
-4111,3906,1513,1766,2040,1487,4112,3030,3258,2824,3761,3127,7483,7484,1507,7485,  # 4326
-2683, 733,  40,1632,1106,2865, 345,4113, 841,2524, 230,4364,2984,1846,3259,3428,  # 4342
-7486,1263, 986,3429,7487, 735, 879, 254,1137, 857, 622,1300,1180,1388,1562,3907,  # 4358
-3908,2939, 967,2751,2655,1349, 592,2133,1692,3324,2985,1994,4114,1679,3909,1901,  # 4374
-2185,7488, 739,3642,2715,1296,1290,7489,4115,2198,2199,1921,1563,2595,2551,1870,  # 4390
-2752,2986,7490, 435,7491, 343,1108, 596,  17,1751,4365,2235,3430,3643,7492,4366,  # 4406
- 294,3527,2940,1693, 477, 979, 281,2041,3528, 643,2042,3644,2621,2782,2261,1031,  # 4422
-2335,2134,2298,3529,4367, 367,1249,2552,7493,3530,7494,4368,1283,3325,2004, 240,  # 4438
-1762,3326,4369,4370, 836,1069,3128, 474,7495,2148,2525, 268,3531,7496,3188,1521,  # 4454
-1284,7497,1658,1546,4116,7498,3532,3533,7499,4117,3327,2684,1685,4118, 961,1673,  # 4470
-2622, 190,2005,2200,3762,4371,4372,7500, 570,2497,3645,1490,7501,4373,2623,3260,  # 4486
-1956,4374, 584,1514, 396,1045,1944,7502,4375,1967,2444,7503,7504,4376,3910, 619,  # 4502
-7505,3129,3261, 215,2006,2783,2553,3189,4377,3190,4378, 763,4119,3763,4379,7506,  # 4518
-7507,1957,1767,2941,3328,3646,1174, 452,1477,4380,3329,3130,7508,2825,1253,2382,  # 4534
-2186,1091,2285,4120, 492,7509, 638,1169,1824,2135,1752,3911, 648, 926,1021,1324,  # 4550
-4381, 520,4382, 997, 847,1007, 892,4383,3764,2262,1871,3647,7510,2400,1784,4384,  # 4566
-1952,2942,3080,3191,1728,4121,2043,3648,4385,2007,1701,3131,1551,  30,2263,4122,  # 4582
-7511,2026,4386,3534,7512, 501,7513,4123, 594,3431,2165,1821,3535,3432,3536,3192,  # 4598
- 829,2826,4124,7514,1680,3132,1225,4125,7515,3262,4387,4126,3133,2336,7516,4388,  # 4614
-4127,7517,3912,3913,7518,1847,2383,2596,3330,7519,4389, 374,3914, 652,4128,4129,  # 4630
- 375,1140, 798,7520,7521,7522,2361,4390,2264, 546,1659, 138,3031,2445,4391,7523,  # 4646
-2250, 612,1848, 910, 796,3765,1740,1371, 825,3766,3767,7524,2906,2554,7525, 692,  # 4662
- 444,3032,2624, 801,4392,4130,7526,1491, 244,1053,3033,4131,4132, 340,7527,3915,  # 4678
-1041,2987, 293,1168,  87,1357,7528,1539, 959,7529,2236, 721, 694,4133,3768, 219,  # 4694
-1478, 644,1417,3331,2656,1413,1401,1335,1389,3916,7530,7531,2988,2362,3134,1825,  # 4710
- 730,1515, 184,2827,  66,4393,7532,1660,2943, 246,3332, 378,1457, 226,3433, 975,  # 4726
-3917,2944,1264,3537, 674, 696,7533, 163,7534,1141,2417,2166, 713,3538,3333,4394,  # 4742
-3918,7535,7536,1186,  15,7537,1079,1070,7538,1522,3193,3539, 276,1050,2716, 758,  # 4758
-1126, 653,2945,3263,7539,2337, 889,3540,3919,3081,2989, 903,1250,4395,3920,3434,  # 4774
-3541,1342,1681,1718, 766,3264, 286,  89,2946,3649,7540,1713,7541,2597,3334,2990,  # 4790
-7542,2947,2215,3194,2866,7543,4396,2498,2526, 181, 387,1075,3921, 731,2187,3335,  # 4806
-7544,3265, 310, 313,3435,2299, 770,4134,  54,3034, 189,4397,3082,3769,3922,7545,  # 4822
-1230,1617,1849, 355,3542,4135,4398,3336, 111,4136,3650,1350,3135,3436,3035,4137,  # 4838
-2149,3266,3543,7546,2784,3923,3924,2991, 722,2008,7547,1071, 247,1207,2338,2471,  # 4854
-1378,4399,2009, 864,1437,1214,4400, 373,3770,1142,2216, 667,4401, 442,2753,2555,  # 4870
-3771,3925,1968,4138,3267,1839, 837, 170,1107, 934,1336,1882,7548,7549,2118,4139,  # 4886
-2828, 743,1569,7550,4402,4140, 582,2384,1418,3437,7551,1802,7552, 357,1395,1729,  # 4902
-3651,3268,2418,1564,2237,7553,3083,3772,1633,4403,1114,2085,4141,1532,7554, 482,  # 4918
-2446,4404,7555,7556,1492, 833,1466,7557,2717,3544,1641,2829,7558,1526,1272,3652,  # 4934
-4142,1686,1794, 416,2556,1902,1953,1803,7559,3773,2785,3774,1159,2316,7560,2867,  # 4950
-4405,1610,1584,3036,2419,2754, 443,3269,1163,3136,7561,7562,3926,7563,4143,2499,  # 4966
-3037,4406,3927,3137,2103,1647,3545,2010,1872,4144,7564,4145, 431,3438,7565, 250,  # 4982
-  97,  81,4146,7566,1648,1850,1558, 160, 848,7567, 866, 740,1694,7568,2201,2830,  # 4998
-3195,4147,4407,3653,1687, 950,2472, 426, 469,3196,3654,3655,3928,7569,7570,1188,  # 5014
- 424,1995, 861,3546,4148,3775,2202,2685, 168,1235,3547,4149,7571,2086,1674,4408,  # 5030
-3337,3270, 220,2557,1009,7572,3776, 670,2992, 332,1208, 717,7573,7574,3548,2447,  # 5046
-3929,3338,7575, 513,7576,1209,2868,3339,3138,4409,1080,7577,7578,7579,7580,2527,  # 5062
-3656,3549, 815,1587,3930,3931,7581,3550,3439,3777,1254,4410,1328,3038,1390,3932,  # 5078
-1741,3933,3778,3934,7582, 236,3779,2448,3271,7583,7584,3657,3780,1273,3781,4411,  # 5094
-7585, 308,7586,4412, 245,4413,1851,2473,1307,2575, 430, 715,2136,2449,7587, 270,  # 5110
- 199,2869,3935,7588,3551,2718,1753, 761,1754, 725,1661,1840,4414,3440,3658,7589,  # 5126
-7590, 587,  14,3272, 227,2598, 326, 480,2265, 943,2755,3552, 291, 650,1883,7591,  # 5142
-1702,1226, 102,1547,  62,3441, 904,4415,3442,1164,4150,7592,7593,1224,1548,2756,  # 5158
- 391, 498,1493,7594,1386,1419,7595,2055,1177,4416, 813, 880,1081,2363, 566,1145,  # 5174
-4417,2286,1001,1035,2558,2599,2238, 394,1286,7596,7597,2068,7598,  86,1494,1730,  # 5190
-3936, 491,1588, 745, 897,2948, 843,3340,3937,2757,2870,3273,1768, 998,2217,2069,  # 5206
- 397,1826,1195,1969,3659,2993,3341, 284,7599,3782,2500,2137,2119,1903,7600,3938,  # 5222
-2150,3939,4151,1036,3443,1904, 114,2559,4152, 209,1527,7601,7602,2949,2831,2625,  # 5238
-2385,2719,3139, 812,2560,7603,3274,7604,1559, 737,1884,3660,1210, 885,  28,2686,  # 5254
-3553,3783,7605,4153,1004,1779,4418,7606, 346,1981,2218,2687,4419,3784,1742, 797,  # 5270
-1642,3940,1933,1072,1384,2151, 896,3941,3275,3661,3197,2871,3554,7607,2561,1958,  # 5286
-4420,2450,1785,7608,7609,7610,3942,4154,1005,1308,3662,4155,2720,4421,4422,1528,  # 5302
-2600, 161,1178,4156,1982, 987,4423,1101,4157, 631,3943,1157,3198,2420,1343,1241,  # 5318
-1016,2239,2562, 372, 877,2339,2501,1160, 555,1934, 911,3944,7611, 466,1170, 169,  # 5334
-1051,2907,2688,3663,2474,2994,1182,2011,2563,1251,2626,7612, 992,2340,3444,1540,  # 5350
-2721,1201,2070,2401,1996,2475,7613,4424, 528,1922,2188,1503,1873,1570,2364,3342,  # 5366
-3276,7614, 557,1073,7615,1827,3445,2087,2266,3140,3039,3084, 767,3085,2786,4425,  # 5382
-1006,4158,4426,2341,1267,2176,3664,3199, 778,3945,3200,2722,1597,2657,7616,4427,  # 5398
-7617,3446,7618,7619,7620,3277,2689,1433,3278, 131,  95,1504,3946, 723,4159,3141,  # 5414
-1841,3555,2758,2189,3947,2027,2104,3665,7621,2995,3948,1218,7622,3343,3201,3949,  # 5430
-4160,2576, 248,1634,3785, 912,7623,2832,3666,3040,3786, 654,  53,7624,2996,7625,  # 5446
-1688,4428, 777,3447,1032,3950,1425,7626, 191, 820,2120,2833, 971,4429, 931,3202,  # 5462
- 135, 664, 783,3787,1997, 772,2908,1935,3951,3788,4430,2909,3203, 282,2723, 640,  # 5478
-1372,3448,1127, 922, 325,3344,7627,7628, 711,2044,7629,7630,3952,2219,2787,1936,  # 5494
-3953,3345,2220,2251,3789,2300,7631,4431,3790,1258,3279,3954,3204,2138,2950,3955,  # 5510
-3956,7632,2221, 258,3205,4432, 101,1227,7633,3280,1755,7634,1391,3281,7635,2910,  # 5526
-2056, 893,7636,7637,7638,1402,4161,2342,7639,7640,3206,3556,7641,7642, 878,1325,  # 5542
-1780,2788,4433, 259,1385,2577, 744,1183,2267,4434,7643,3957,2502,7644, 684,1024,  # 5558
-4162,7645, 472,3557,3449,1165,3282,3958,3959, 322,2152, 881, 455,1695,1152,1340,  # 5574
- 660, 554,2153,4435,1058,4436,4163, 830,1065,3346,3960,4437,1923,7646,1703,1918,  # 5590
-7647, 932,2268, 122,7648,4438, 947, 677,7649,3791,2627, 297,1905,1924,2269,4439,  # 5606
-2317,3283,7650,7651,4164,7652,4165,  84,4166, 112, 989,7653, 547,1059,3961, 701,  # 5622
-3558,1019,7654,4167,7655,3450, 942, 639, 457,2301,2451, 993,2951, 407, 851, 494,  # 5638
-4440,3347, 927,7656,1237,7657,2421,3348, 573,4168, 680, 921,2911,1279,1874, 285,  # 5654
- 790,1448,1983, 719,2167,7658,7659,4441,3962,3963,1649,7660,1541, 563,7661,1077,  # 5670
-7662,3349,3041,3451, 511,2997,3964,3965,3667,3966,1268,2564,3350,3207,4442,4443,  # 5686
-7663, 535,1048,1276,1189,2912,2028,3142,1438,1373,2834,2952,1134,2012,7664,4169,  # 5702
-1238,2578,3086,1259,7665, 700,7666,2953,3143,3668,4170,7667,4171,1146,1875,1906,  # 5718
-4444,2601,3967, 781,2422, 132,1589, 203, 147, 273,2789,2402, 898,1786,2154,3968,  # 5734
-3969,7668,3792,2790,7669,7670,4445,4446,7671,3208,7672,1635,3793, 965,7673,1804,  # 5750
-2690,1516,3559,1121,1082,1329,3284,3970,1449,3794,  65,1128,2835,2913,2759,1590,  # 5766
-3795,7674,7675,  12,2658,  45, 976,2579,3144,4447, 517,2528,1013,1037,3209,7676,  # 5782
-3796,2836,7677,3797,7678,3452,7679,2602, 614,1998,2318,3798,3087,2724,2628,7680,  # 5798
-2580,4172, 599,1269,7681,1810,3669,7682,2691,3088, 759,1060, 489,1805,3351,3285,  # 5814
-1358,7683,7684,2386,1387,1215,2629,2252, 490,7685,7686,4173,1759,2387,2343,7687,  # 5830
-4448,3799,1907,3971,2630,1806,3210,4449,3453,3286,2760,2344, 874,7688,7689,3454,  # 5846
-3670,1858,  91,2914,3671,3042,3800,4450,7690,3145,3972,2659,7691,3455,1202,1403,  # 5862
-3801,2954,2529,1517,2503,4451,3456,2504,7692,4452,7693,2692,1885,1495,1731,3973,  # 5878
-2365,4453,7694,2029,7695,7696,3974,2693,1216, 237,2581,4174,2319,3975,3802,4454,  # 5894
-4455,2694,3560,3457, 445,4456,7697,7698,7699,7700,2761,  61,3976,3672,1822,3977,  # 5910
-7701, 687,2045, 935, 925, 405,2660, 703,1096,1859,2725,4457,3978,1876,1367,2695,  # 5926
-3352, 918,2105,1781,2476, 334,3287,1611,1093,4458, 564,3146,3458,3673,3353, 945,  # 5942
-2631,2057,4459,7702,1925, 872,4175,7703,3459,2696,3089, 349,4176,3674,3979,4460,  # 5958
-3803,4177,3675,2155,3980,4461,4462,4178,4463,2403,2046, 782,3981, 400, 251,4179,  # 5974
-1624,7704,7705, 277,3676, 299,1265, 476,1191,3804,2121,4180,4181,1109, 205,7706,  # 5990
-2582,1000,2156,3561,1860,7707,7708,7709,4464,7710,4465,2565, 107,2477,2157,3982,  # 6006
-3460,3147,7711,1533, 541,1301, 158, 753,4182,2872,3562,7712,1696, 370,1088,4183,  # 6022
-4466,3563, 579, 327, 440, 162,2240, 269,1937,1374,3461, 968,3043,  56,1396,3090,  # 6038
-2106,3288,3354,7713,1926,2158,4467,2998,7714,3564,7715,7716,3677,4468,2478,7717,  # 6054
-2791,7718,1650,4469,7719,2603,7720,7721,3983,2661,3355,1149,3356,3984,3805,3985,  # 6070
-7722,1076,  49,7723, 951,3211,3289,3290, 450,2837, 920,7724,1811,2792,2366,4184,  # 6086
-1908,1138,2367,3806,3462,7725,3212,4470,1909,1147,1518,2423,4471,3807,7726,4472,  # 6102
-2388,2604, 260,1795,3213,7727,7728,3808,3291, 708,7729,3565,1704,7730,3566,1351,  # 6118
-1618,3357,2999,1886, 944,4185,3358,4186,3044,3359,4187,7731,3678, 422, 413,1714,  # 6134
-3292, 500,2058,2345,4188,2479,7732,1344,1910, 954,7733,1668,7734,7735,3986,2404,  # 6150
-4189,3567,3809,4190,7736,2302,1318,2505,3091, 133,3092,2873,4473, 629,  31,2838,  # 6166
-2697,3810,4474, 850, 949,4475,3987,2955,1732,2088,4191,1496,1852,7737,3988, 620,  # 6182
-3214, 981,1242,3679,3360,1619,3680,1643,3293,2139,2452,1970,1719,3463,2168,7738,  # 6198
-3215,7739,7740,3361,1828,7741,1277,4476,1565,2047,7742,1636,3568,3093,7743, 869,  # 6214
-2839, 655,3811,3812,3094,3989,3000,3813,1310,3569,4477,7744,7745,7746,1733, 558,  # 6230
-4478,3681, 335,1549,3045,1756,4192,3682,1945,3464,1829,1291,1192, 470,2726,2107,  # 6246
-2793, 913,1054,3990,7747,1027,7748,3046,3991,4479, 982,2662,3362,3148,3465,3216,  # 6262
-3217,1946,2794,7749, 571,4480,7750,1830,7751,3570,2583,1523,2424,7752,2089, 984,  # 6278
-4481,3683,1959,7753,3684, 852, 923,2795,3466,3685, 969,1519, 999,2048,2320,1705,  # 6294
-7754,3095, 615,1662, 151, 597,3992,2405,2321,1049, 275,4482,3686,4193, 568,3687,  # 6310
-3571,2480,4194,3688,7755,2425,2270, 409,3218,7756,1566,2874,3467,1002, 769,2840,  # 6326
- 194,2090,3149,3689,2222,3294,4195, 628,1505,7757,7758,1763,2177,3001,3993, 521,  # 6342
-1161,2584,1787,2203,2406,4483,3994,1625,4196,4197, 412,  42,3096, 464,7759,2632,  # 6358
-4484,3363,1760,1571,2875,3468,2530,1219,2204,3814,2633,2140,2368,4485,4486,3295,  # 6374
-1651,3364,3572,7760,7761,3573,2481,3469,7762,3690,7763,7764,2271,2091, 460,7765,  # 6390
-4487,7766,3002, 962, 588,3574, 289,3219,2634,1116,  52,7767,3047,1796,7768,7769,  # 6406
-7770,1467,7771,1598,1143,3691,4198,1984,1734,1067,4488,1280,3365, 465,4489,1572,  # 6422
- 510,7772,1927,2241,1812,1644,3575,7773,4490,3692,7774,7775,2663,1573,1534,7776,  # 6438
-7777,4199, 536,1807,1761,3470,3815,3150,2635,7778,7779,7780,4491,3471,2915,1911,  # 6454
-2796,7781,3296,1122, 377,3220,7782, 360,7783,7784,4200,1529, 551,7785,2059,3693,  # 6470
-1769,2426,7786,2916,4201,3297,3097,2322,2108,2030,4492,1404, 136,1468,1479, 672,  # 6486
-1171,3221,2303, 271,3151,7787,2762,7788,2049, 678,2727, 865,1947,4493,7789,2013,  # 6502
-3995,2956,7790,2728,2223,1397,3048,3694,4494,4495,1735,2917,3366,3576,7791,3816,  # 6518
- 509,2841,2453,2876,3817,7792,7793,3152,3153,4496,4202,2531,4497,2304,1166,1010,  # 6534
- 552, 681,1887,7794,7795,2957,2958,3996,1287,1596,1861,3154, 358, 453, 736, 175,  # 6550
- 478,1117, 905,1167,1097,7796,1853,1530,7797,1706,7798,2178,3472,2287,3695,3473,  # 6566
-3577,4203,2092,4204,7799,3367,1193,2482,4205,1458,2190,2205,1862,1888,1421,3298,  # 6582
-2918,3049,2179,3474, 595,2122,7800,3997,7801,7802,4206,1707,2636, 223,3696,1359,  # 6598
- 751,3098, 183,3475,7803,2797,3003, 419,2369, 633, 704,3818,2389, 241,7804,7805,  # 6614
-7806, 838,3004,3697,2272,2763,2454,3819,1938,2050,3998,1309,3099,2242,1181,7807,  # 6630
-1136,2206,3820,2370,1446,4207,2305,4498,7808,7809,4208,1055,2605, 484,3698,7810,  # 6646
-3999, 625,4209,2273,3368,1499,4210,4000,7811,4001,4211,3222,2274,2275,3476,7812,  # 6662
-7813,2764, 808,2606,3699,3369,4002,4212,3100,2532, 526,3370,3821,4213, 955,7814,  # 6678
-1620,4214,2637,2427,7815,1429,3700,1669,1831, 994, 928,7816,3578,1260,7817,7818,  # 6694
-7819,1948,2288, 741,2919,1626,4215,2729,2455, 867,1184, 362,3371,1392,7820,7821,  # 6710
-4003,4216,1770,1736,3223,2920,4499,4500,1928,2698,1459,1158,7822,3050,3372,2877,  # 6726
-1292,1929,2506,2842,3701,1985,1187,2071,2014,2607,4217,7823,2566,2507,2169,3702,  # 6742
-2483,3299,7824,3703,4501,7825,7826, 666,1003,3005,1022,3579,4218,7827,4502,1813,  # 6758
-2253, 574,3822,1603, 295,1535, 705,3823,4219, 283, 858, 417,7828,7829,3224,4503,  # 6774
-4504,3051,1220,1889,1046,2276,2456,4004,1393,1599, 689,2567, 388,4220,7830,2484,  # 6790
- 802,7831,2798,3824,2060,1405,2254,7832,4505,3825,2109,1052,1345,3225,1585,7833,  # 6806
- 809,7834,7835,7836, 575,2730,3477, 956,1552,1469,1144,2323,7837,2324,1560,2457,  # 6822
-3580,3226,4005, 616,2207,3155,2180,2289,7838,1832,7839,3478,4506,7840,1319,3704,  # 6838
-3705,1211,3581,1023,3227,1293,2799,7841,7842,7843,3826, 607,2306,3827, 762,2878,  # 6854
-1439,4221,1360,7844,1485,3052,7845,4507,1038,4222,1450,2061,2638,4223,1379,4508,  # 6870
-2585,7846,7847,4224,1352,1414,2325,2921,1172,7848,7849,3828,3829,7850,1797,1451,  # 6886
-7851,7852,7853,7854,2922,4006,4007,2485,2346, 411,4008,4009,3582,3300,3101,4509,  # 6902
-1561,2664,1452,4010,1375,7855,7856,  47,2959, 316,7857,1406,1591,2923,3156,7858,  # 6918
-1025,2141,3102,3157, 354,2731, 884,2224,4225,2407, 508,3706, 726,3583, 996,2428,  # 6934
-3584, 729,7859, 392,2191,1453,4011,4510,3707,7860,7861,2458,3585,2608,1675,2800,  # 6950
- 919,2347,2960,2348,1270,4511,4012,  73,7862,7863, 647,7864,3228,2843,2255,1550,  # 6966
-1346,3006,7865,1332, 883,3479,7866,7867,7868,7869,3301,2765,7870,1212, 831,1347,  # 6982
-4226,4512,2326,3830,1863,3053, 720,3831,4513,4514,3832,7871,4227,7872,7873,4515,  # 6998
-7874,7875,1798,4516,3708,2609,4517,3586,1645,2371,7876,7877,2924, 669,2208,2665,  # 7014
-2429,7878,2879,7879,7880,1028,3229,7881,4228,2408,7882,2256,1353,7883,7884,4518,  # 7030
-3158, 518,7885,4013,7886,4229,1960,7887,2142,4230,7888,7889,3007,2349,2350,3833,  # 7046
- 516,1833,1454,4014,2699,4231,4519,2225,2610,1971,1129,3587,7890,2766,7891,2961,  # 7062
-1422, 577,1470,3008,1524,3373,7892,7893, 432,4232,3054,3480,7894,2586,1455,2508,  # 7078
-2226,1972,1175,7895,1020,2732,4015,3481,4520,7896,2733,7897,1743,1361,3055,3482,  # 7094
-2639,4016,4233,4521,2290, 895, 924,4234,2170, 331,2243,3056, 166,1627,3057,1098,  # 7110
-7898,1232,2880,2227,3374,4522, 657, 403,1196,2372, 542,3709,3375,1600,4235,3483,  # 7126
-7899,4523,2767,3230, 576, 530,1362,7900,4524,2533,2666,3710,4017,7901, 842,3834,  # 7142
-7902,2801,2031,1014,4018, 213,2700,3376, 665, 621,4236,7903,3711,2925,2430,7904,  # 7158
-2431,3302,3588,3377,7905,4237,2534,4238,4525,3589,1682,4239,3484,1380,7906, 724,  # 7174
-2277, 600,1670,7907,1337,1233,4526,3103,2244,7908,1621,4527,7909, 651,4240,7910,  # 7190
-1612,4241,2611,7911,2844,7912,2734,2307,3058,7913, 716,2459,3059, 174,1255,2701,  # 7206
-4019,3590, 548,1320,1398, 728,4020,1574,7914,1890,1197,3060,4021,7915,3061,3062,  # 7222
-3712,3591,3713, 747,7916, 635,4242,4528,7917,7918,7919,4243,7920,7921,4529,7922,  # 7238
-3378,4530,2432, 451,7923,3714,2535,2072,4244,2735,4245,4022,7924,1764,4531,7925,  # 7254
-4246, 350,7926,2278,2390,2486,7927,4247,4023,2245,1434,4024, 488,4532, 458,4248,  # 7270
-4025,3715, 771,1330,2391,3835,2568,3159,2159,2409,1553,2667,3160,4249,7928,2487,  # 7286
-2881,2612,1720,2702,4250,3379,4533,7929,2536,4251,7930,3231,4252,2768,7931,2015,  # 7302
-2736,7932,1155,1017,3716,3836,7933,3303,2308, 201,1864,4253,1430,7934,4026,7935,  # 7318
-7936,7937,7938,7939,4254,1604,7940, 414,1865, 371,2587,4534,4535,3485,2016,3104,  # 7334
-4536,1708, 960,4255, 887, 389,2171,1536,1663,1721,7941,2228,4027,2351,2926,1580,  # 7350
-7942,7943,7944,1744,7945,2537,4537,4538,7946,4539,7947,2073,7948,7949,3592,3380,  # 7366
-2882,4256,7950,4257,2640,3381,2802, 673,2703,2460, 709,3486,4028,3593,4258,7951,  # 7382
-1148, 502, 634,7952,7953,1204,4540,3594,1575,4541,2613,3717,7954,3718,3105, 948,  # 7398
-3232, 121,1745,3837,1110,7955,4259,3063,2509,3009,4029,3719,1151,1771,3838,1488,  # 7414
-4030,1986,7956,2433,3487,7957,7958,2093,7959,4260,3839,1213,1407,2803, 531,2737,  # 7430
-2538,3233,1011,1537,7960,2769,4261,3106,1061,7961,3720,3721,1866,2883,7962,2017,  # 7446
- 120,4262,4263,2062,3595,3234,2309,3840,2668,3382,1954,4542,7963,7964,3488,1047,  # 7462
-2704,1266,7965,1368,4543,2845, 649,3383,3841,2539,2738,1102,2846,2669,7966,7967,  # 7478
-1999,7968,1111,3596,2962,7969,2488,3842,3597,2804,1854,3384,3722,7970,7971,3385,  # 7494
-2410,2884,3304,3235,3598,7972,2569,7973,3599,2805,4031,1460, 856,7974,3600,7975,  # 7510
-2885,2963,7976,2886,3843,7977,4264, 632,2510, 875,3844,1697,3845,2291,7978,7979,  # 7526
-4544,3010,1239, 580,4545,4265,7980, 914, 936,2074,1190,4032,1039,2123,7981,7982,  # 7542
-7983,3386,1473,7984,1354,4266,3846,7985,2172,3064,4033, 915,3305,4267,4268,3306,  # 7558
-1605,1834,7986,2739, 398,3601,4269,3847,4034, 328,1912,2847,4035,3848,1331,4270,  # 7574
-3011, 937,4271,7987,3602,4036,4037,3387,2160,4546,3388, 524, 742, 538,3065,1012,  # 7590
-7988,7989,3849,2461,7990, 658,1103, 225,3850,7991,7992,4547,7993,4548,7994,3236,  # 7606
-1243,7995,4038, 963,2246,4549,7996,2705,3603,3161,7997,7998,2588,2327,7999,4550,  # 7622
-8000,8001,8002,3489,3307, 957,3389,2540,2032,1930,2927,2462, 870,2018,3604,1746,  # 7638
-2770,2771,2434,2463,8003,3851,8004,3723,3107,3724,3490,3390,3725,8005,1179,3066,  # 7654
-8006,3162,2373,4272,3726,2541,3163,3108,2740,4039,8007,3391,1556,2542,2292, 977,  # 7670
-2887,2033,4040,1205,3392,8008,1765,3393,3164,2124,1271,1689, 714,4551,3491,8009,  # 7686
-2328,3852, 533,4273,3605,2181, 617,8010,2464,3308,3492,2310,8011,8012,3165,8013,  # 7702
-8014,3853,1987, 618, 427,2641,3493,3394,8015,8016,1244,1690,8017,2806,4274,4552,  # 7718
-8018,3494,8019,8020,2279,1576, 473,3606,4275,3395, 972,8021,3607,8022,3067,8023,  # 7734
-8024,4553,4554,8025,3727,4041,4042,8026, 153,4555, 356,8027,1891,2888,4276,2143,  # 7750
- 408, 803,2352,8028,3854,8029,4277,1646,2570,2511,4556,4557,3855,8030,3856,4278,  # 7766
-8031,2411,3396, 752,8032,8033,1961,2964,8034, 746,3012,2465,8035,4279,3728, 698,  # 7782
-4558,1892,4280,3608,2543,4559,3609,3857,8036,3166,3397,8037,1823,1302,4043,2706,  # 7798
-3858,1973,4281,8038,4282,3167, 823,1303,1288,1236,2848,3495,4044,3398, 774,3859,  # 7814
-8039,1581,4560,1304,2849,3860,4561,8040,2435,2161,1083,3237,4283,4045,4284, 344,  # 7830
-1173, 288,2311, 454,1683,8041,8042,1461,4562,4046,2589,8043,8044,4563, 985, 894,  # 7846
-8045,3399,3168,8046,1913,2928,3729,1988,8047,2110,1974,8048,4047,8049,2571,1194,  # 7862
- 425,8050,4564,3169,1245,3730,4285,8051,8052,2850,8053, 636,4565,1855,3861, 760,  # 7878
-1799,8054,4286,2209,1508,4566,4048,1893,1684,2293,8055,8056,8057,4287,4288,2210,  # 7894
- 479,8058,8059, 832,8060,4049,2489,8061,2965,2490,3731, 990,3109, 627,1814,2642,  # 7910
-4289,1582,4290,2125,2111,3496,4567,8062, 799,4291,3170,8063,4568,2112,1737,3013,  # 7926
-1018, 543, 754,4292,3309,1676,4569,4570,4050,8064,1489,8065,3497,8066,2614,2889,  # 7942
-4051,8067,8068,2966,8069,8070,8071,8072,3171,4571,4572,2182,1722,8073,3238,3239,  # 7958
-1842,3610,1715, 481, 365,1975,1856,8074,8075,1962,2491,4573,8076,2126,3611,3240,  # 7974
- 433,1894,2063,2075,8077, 602,2741,8078,8079,8080,8081,8082,3014,1628,3400,8083,  # 7990
-3172,4574,4052,2890,4575,2512,8084,2544,2772,8085,8086,8087,3310,4576,2891,8088,  # 8006
-4577,8089,2851,4578,4579,1221,2967,4053,2513,8090,8091,8092,1867,1989,8093,8094,  # 8022
-8095,1895,8096,8097,4580,1896,4054, 318,8098,2094,4055,4293,8099,8100, 485,8101,  # 8038
- 938,3862, 553,2670, 116,8102,3863,3612,8103,3498,2671,2773,3401,3311,2807,8104,  # 8054
-3613,2929,4056,1747,2930,2968,8105,8106, 207,8107,8108,2672,4581,2514,8109,3015,  # 8070
- 890,3614,3864,8110,1877,3732,3402,8111,2183,2353,3403,1652,8112,8113,8114, 941,  # 8086
-2294, 208,3499,4057,2019, 330,4294,3865,2892,2492,3733,4295,8115,8116,8117,8118,  # 8102
-)
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euctwprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euctwprober.py
deleted file mode 100644
index 35669cc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/euctwprober.py
+++ /dev/null
@@ -1,46 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .mbcharsetprober import MultiByteCharSetProber
-from .codingstatemachine import CodingStateMachine
-from .chardistribution import EUCTWDistributionAnalysis
-from .mbcssm import EUCTW_SM_MODEL
-
-class EUCTWProber(MultiByteCharSetProber):
-    def __init__(self):
-        super(EUCTWProber, self).__init__()
-        self.coding_sm = CodingStateMachine(EUCTW_SM_MODEL)
-        self.distribution_analyzer = EUCTWDistributionAnalysis()
-        self.reset()
-
-    @property
-    def charset_name(self):
-        return "EUC-TW"
-
-    @property
-    def language(self):
-        return "Taiwan"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/gb2312freq.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/gb2312freq.py
deleted file mode 100644
index 697837b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/gb2312freq.py
+++ /dev/null
@@ -1,283 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# GB2312 most frequently used character table
-#
-# Char to FreqOrder table , from hz6763
-
-# 512  --> 0.79  -- 0.79
-# 1024 --> 0.92  -- 0.13
-# 2048 --> 0.98  -- 0.06
-# 6768 --> 1.00  -- 0.02
-#
-# Ideal Distribution Ratio = 0.79135/(1-0.79135) = 3.79
-# Random Distribution Ration = 512 / (3755 - 512) = 0.157
-#
-# Typical Distribution Ratio about 25% of Ideal one, still much higher that RDR
-
-GB2312_TYPICAL_DISTRIBUTION_RATIO = 0.9
-
-GB2312_TABLE_SIZE = 3760
-
-GB2312_CHAR_TO_FREQ_ORDER = (
-1671, 749,1443,2364,3924,3807,2330,3921,1704,3463,2691,1511,1515, 572,3191,2205,
-2361, 224,2558, 479,1711, 963,3162, 440,4060,1905,2966,2947,3580,2647,3961,3842,
-2204, 869,4207, 970,2678,5626,2944,2956,1479,4048, 514,3595, 588,1346,2820,3409,
- 249,4088,1746,1873,2047,1774, 581,1813, 358,1174,3590,1014,1561,4844,2245, 670,
-1636,3112, 889,1286, 953, 556,2327,3060,1290,3141, 613, 185,3477,1367, 850,3820,
-1715,2428,2642,2303,2732,3041,2562,2648,3566,3946,1349, 388,3098,2091,1360,3585,
- 152,1687,1539, 738,1559,  59,1232,2925,2267,1388,1249,1741,1679,2960, 151,1566,
-1125,1352,4271, 924,4296, 385,3166,4459, 310,1245,2850,  70,3285,2729,3534,3575,
-2398,3298,3466,1960,2265, 217,3647, 864,1909,2084,4401,2773,1010,3269,5152, 853,
-3051,3121,1244,4251,1895, 364,1499,1540,2313,1180,3655,2268, 562, 715,2417,3061,
- 544, 336,3768,2380,1752,4075, 950, 280,2425,4382, 183,2759,3272, 333,4297,2155,
-1688,2356,1444,1039,4540, 736,1177,3349,2443,2368,2144,2225, 565, 196,1482,3406,
- 927,1335,4147, 692, 878,1311,1653,3911,3622,1378,4200,1840,2969,3149,2126,1816,
-2534,1546,2393,2760, 737,2494,  13, 447, 245,2747,  38,2765,2129,2589,1079, 606,
- 360, 471,3755,2890, 404, 848, 699,1785,1236, 370,2221,1023,3746,2074,2026,2023,
-2388,1581,2119, 812,1141,3091,2536,1519, 804,2053, 406,1596,1090, 784, 548,4414,
-1806,2264,2936,1100, 343,4114,5096, 622,3358, 743,3668,1510,1626,5020,3567,2513,
-3195,4115,5627,2489,2991,  24,2065,2697,1087,2719,  48,1634, 315,  68, 985,2052,
- 198,2239,1347,1107,1439, 597,2366,2172, 871,3307, 919,2487,2790,1867, 236,2570,
-1413,3794, 906,3365,3381,1701,1982,1818,1524,2924,1205, 616,2586,2072,2004, 575,
- 253,3099,  32,1365,1182, 197,1714,2454,1201, 554,3388,3224,2748, 756,2587, 250,
-2567,1507,1517,3529,1922,2761,2337,3416,1961,1677,2452,2238,3153, 615, 911,1506,
-1474,2495,1265,1906,2749,3756,3280,2161, 898,2714,1759,3450,2243,2444, 563,  26,
-3286,2266,3769,3344,2707,3677, 611,1402, 531,1028,2871,4548,1375, 261,2948, 835,
-1190,4134, 353, 840,2684,1900,3082,1435,2109,1207,1674, 329,1872,2781,4055,2686,
-2104, 608,3318,2423,2957,2768,1108,3739,3512,3271,3985,2203,1771,3520,1418,2054,
-1681,1153, 225,1627,2929, 162,2050,2511,3687,1954, 124,1859,2431,1684,3032,2894,
- 585,4805,3969,2869,2704,2088,2032,2095,3656,2635,4362,2209, 256, 518,2042,2105,
-3777,3657, 643,2298,1148,1779, 190, 989,3544, 414,  11,2135,2063,2979,1471, 403,
-3678, 126, 770,1563, 671,2499,3216,2877, 600,1179, 307,2805,4937,1268,1297,2694,
- 252,4032,1448,1494,1331,1394, 127,2256, 222,1647,1035,1481,3056,1915,1048, 873,
-3651, 210,  33,1608,2516, 200,1520, 415, 102,   0,3389,1287, 817,  91,3299,2940,
- 836,1814, 549,2197,1396,1669,2987,3582,2297,2848,4528,1070, 687,  20,1819, 121,
-1552,1364,1461,1968,2617,3540,2824,2083, 177, 948,4938,2291, 110,4549,2066, 648,
-3359,1755,2110,2114,4642,4845,1693,3937,3308,1257,1869,2123, 208,1804,3159,2992,
-2531,2549,3361,2418,1350,2347,2800,2568,1291,2036,2680,  72, 842,1990, 212,1233,
-1154,1586,  75,2027,3410,4900,1823,1337,2710,2676, 728,2810,1522,3026,4995, 157,
- 755,1050,4022, 710, 785,1936,2194,2085,1406,2777,2400, 150,1250,4049,1206, 807,
-1910, 534, 529,3309,1721,1660, 274,  39,2827, 661,2670,1578, 925,3248,3815,1094,
-4278,4901,4252,  41,1150,3747,2572,2227,4501,3658,4902,3813,3357,3617,2884,2258,
- 887, 538,4187,3199,1294,2439,3042,2329,2343,2497,1255, 107, 543,1527, 521,3478,
-3568, 194,5062,  15, 961,3870,1241,1192,2664,  66,5215,3260,2111,1295,1127,2152,
-3805,4135, 901,1164,1976, 398,1278, 530,1460, 748, 904,1054,1966,1426,  53,2909,
- 509, 523,2279,1534, 536,1019, 239,1685, 460,2353, 673,1065,2401,3600,4298,2272,
-1272,2363, 284,1753,3679,4064,1695,  81, 815,2677,2757,2731,1386, 859, 500,4221,
-2190,2566, 757,1006,2519,2068,1166,1455, 337,2654,3203,1863,1682,1914,3025,1252,
-1409,1366, 847, 714,2834,2038,3209, 964,2970,1901, 885,2553,1078,1756,3049, 301,
-1572,3326, 688,2130,1996,2429,1805,1648,2930,3421,2750,3652,3088, 262,1158,1254,
- 389,1641,1812, 526,1719, 923,2073,1073,1902, 468, 489,4625,1140, 857,2375,3070,
-3319,2863, 380, 116,1328,2693,1161,2244, 273,1212,1884,2769,3011,1775,1142, 461,
-3066,1200,2147,2212, 790, 702,2695,4222,1601,1058, 434,2338,5153,3640,  67,2360,
-4099,2502, 618,3472,1329, 416,1132, 830,2782,1807,2653,3211,3510,1662, 192,2124,
- 296,3979,1739,1611,3684,  23, 118, 324, 446,1239,1225, 293,2520,3814,3795,2535,
-3116,  17,1074, 467,2692,2201, 387,2922,  45,1326,3055,1645,3659,2817, 958, 243,
-1903,2320,1339,2825,1784,3289, 356, 576, 865,2315,2381,3377,3916,1088,3122,1713,
-1655, 935, 628,4689,1034,1327, 441, 800, 720, 894,1979,2183,1528,5289,2702,1071,
-4046,3572,2399,1571,3281,  79, 761,1103, 327, 134, 758,1899,1371,1615, 879, 442,
- 215,2605,2579, 173,2048,2485,1057,2975,3317,1097,2253,3801,4263,1403,1650,2946,
- 814,4968,3487,1548,2644,1567,1285,   2, 295,2636,  97, 946,3576, 832, 141,4257,
-3273, 760,3821,3521,3156,2607, 949,1024,1733,1516,1803,1920,2125,2283,2665,3180,
-1501,2064,3560,2171,1592, 803,3518,1416, 732,3897,4258,1363,1362,2458, 119,1427,
- 602,1525,2608,1605,1639,3175, 694,3064,  10, 465,  76,2000,4846,4208, 444,3781,
-1619,3353,2206,1273,3796, 740,2483, 320,1723,2377,3660,2619,1359,1137,1762,1724,
-2345,2842,1850,1862, 912, 821,1866, 612,2625,1735,2573,3369,1093, 844,  89, 937,
- 930,1424,3564,2413,2972,1004,3046,3019,2011, 711,3171,1452,4178, 428, 801,1943,
- 432, 445,2811, 206,4136,1472, 730, 349,  73, 397,2802,2547, 998,1637,1167, 789,
- 396,3217, 154,1218, 716,1120,1780,2819,4826,1931,3334,3762,2139,1215,2627, 552,
-3664,3628,3232,1405,2383,3111,1356,2652,3577,3320,3101,1703, 640,1045,1370,1246,
-4996, 371,1575,2436,1621,2210, 984,4033,1734,2638,  16,4529, 663,2755,3255,1451,
-3917,2257,1253,1955,2234,1263,2951, 214,1229, 617, 485, 359,1831,1969, 473,2310,
- 750,2058, 165,  80,2864,2419, 361,4344,2416,2479,1134, 796,3726,1266,2943, 860,
-2715, 938, 390,2734,1313,1384, 248, 202, 877,1064,2854, 522,3907, 279,1602, 297,
-2357, 395,3740, 137,2075, 944,4089,2584,1267,3802,  62,1533,2285, 178, 176, 780,
-2440, 201,3707, 590, 478,1560,4354,2117,1075,  30,  74,4643,4004,1635,1441,2745,
- 776,2596, 238,1077,1692,1912,2844, 605, 499,1742,3947, 241,3053, 980,1749, 936,
-2640,4511,2582, 515,1543,2162,5322,2892,2993, 890,2148,1924, 665,1827,3581,1032,
- 968,3163, 339,1044,1896, 270, 583,1791,1720,4367,1194,3488,3669,  43,2523,1657,
- 163,2167, 290,1209,1622,3378, 550, 634,2508,2510, 695,2634,2384,2512,1476,1414,
- 220,1469,2341,2138,2852,3183,2900,4939,2865,3502,1211,3680, 854,3227,1299,2976,
-3172, 186,2998,1459, 443,1067,3251,1495, 321,1932,3054, 909, 753,1410,1828, 436,
-2441,1119,1587,3164,2186,1258, 227, 231,1425,1890,3200,3942, 247, 959, 725,5254,
-2741, 577,2158,2079, 929, 120, 174, 838,2813, 591,1115, 417,2024,  40,3240,1536,
-1037, 291,4151,2354, 632,1298,2406,2500,3535,1825,1846,3451, 205,1171, 345,4238,
-  18,1163, 811, 685,2208,1217, 425,1312,1508,1175,4308,2552,1033, 587,1381,3059,
-2984,3482, 340,1316,4023,3972, 792,3176, 519, 777,4690, 918, 933,4130,2981,3741,
-  90,3360,2911,2200,5184,4550, 609,3079,2030, 272,3379,2736, 363,3881,1130,1447,
- 286, 779, 357,1169,3350,3137,1630,1220,2687,2391, 747,1277,3688,2618,2682,2601,
-1156,3196,5290,4034,3102,1689,3596,3128, 874, 219,2783, 798, 508,1843,2461, 269,
-1658,1776,1392,1913,2983,3287,2866,2159,2372, 829,4076,  46,4253,2873,1889,1894,
- 915,1834,1631,2181,2318, 298, 664,2818,3555,2735, 954,3228,3117, 527,3511,2173,
- 681,2712,3033,2247,2346,3467,1652, 155,2164,3382, 113,1994, 450, 899, 494, 994,
-1237,2958,1875,2336,1926,3727, 545,1577,1550, 633,3473, 204,1305,3072,2410,1956,
-2471, 707,2134, 841,2195,2196,2663,3843,1026,4940, 990,3252,4997, 368,1092, 437,
-3212,3258,1933,1829, 675,2977,2893, 412, 943,3723,4644,3294,3283,2230,2373,5154,
-2389,2241,2661,2323,1404,2524, 593, 787, 677,3008,1275,2059, 438,2709,2609,2240,
-2269,2246,1446,  36,1568,1373,3892,1574,2301,1456,3962, 693,2276,5216,2035,1143,
-2720,1919,1797,1811,2763,4137,2597,1830,1699,1488,1198,2090, 424,1694, 312,3634,
-3390,4179,3335,2252,1214, 561,1059,3243,2295,2561, 975,5155,2321,2751,3772, 472,
-1537,3282,3398,1047,2077,2348,2878,1323,3340,3076, 690,2906,  51, 369, 170,3541,
-1060,2187,2688,3670,2541,1083,1683, 928,3918, 459, 109,4427, 599,3744,4286, 143,
-2101,2730,2490,  82,1588,3036,2121, 281,1860, 477,4035,1238,2812,3020,2716,3312,
-1530,2188,2055,1317, 843, 636,1808,1173,3495, 649, 181,1002, 147,3641,1159,2414,
-3750,2289,2795, 813,3123,2610,1136,4368,   5,3391,4541,2174, 420, 429,1728, 754,
-1228,2115,2219, 347,2223,2733, 735,1518,3003,2355,3134,1764,3948,3329,1888,2424,
-1001,1234,1972,3321,3363,1672,1021,1450,1584, 226, 765, 655,2526,3404,3244,2302,
-3665, 731, 594,2184, 319,1576, 621, 658,2656,4299,2099,3864,1279,2071,2598,2739,
- 795,3086,3699,3908,1707,2352,2402,1382,3136,2475,1465,4847,3496,3865,1085,3004,
-2591,1084, 213,2287,1963,3565,2250, 822, 793,4574,3187,1772,1789,3050, 595,1484,
-1959,2770,1080,2650, 456, 422,2996, 940,3322,4328,4345,3092,2742, 965,2784, 739,
-4124, 952,1358,2498,2949,2565, 332,2698,2378, 660,2260,2473,4194,3856,2919, 535,
-1260,2651,1208,1428,1300,1949,1303,2942, 433,2455,2450,1251,1946, 614,1269, 641,
-1306,1810,2737,3078,2912, 564,2365,1419,1415,1497,4460,2367,2185,1379,3005,1307,
-3218,2175,1897,3063, 682,1157,4040,4005,1712,1160,1941,1399, 394, 402,2952,1573,
-1151,2986,2404, 862, 299,2033,1489,3006, 346, 171,2886,3401,1726,2932, 168,2533,
-  47,2507,1030,3735,1145,3370,1395,1318,1579,3609,4560,2857,4116,1457,2529,1965,
- 504,1036,2690,2988,2405, 745,5871, 849,2397,2056,3081, 863,2359,3857,2096,  99,
-1397,1769,2300,4428,1643,3455,1978,1757,3718,1440,  35,4879,3742,1296,4228,2280,
- 160,5063,1599,2013, 166, 520,3479,1646,3345,3012, 490,1937,1545,1264,2182,2505,
-1096,1188,1369,1436,2421,1667,2792,2460,1270,2122, 727,3167,2143, 806,1706,1012,
-1800,3037, 960,2218,1882, 805, 139,2456,1139,1521, 851,1052,3093,3089, 342,2039,
- 744,5097,1468,1502,1585,2087, 223, 939, 326,2140,2577, 892,2481,1623,4077, 982,
-3708, 135,2131,  87,2503,3114,2326,1106, 876,1616, 547,2997,2831,2093,3441,4530,
-4314,   9,3256,4229,4148, 659,1462,1986,1710,2046,2913,2231,4090,4880,5255,3392,
-3274,1368,3689,4645,1477, 705,3384,3635,1068,1529,2941,1458,3782,1509, 100,1656,
-2548, 718,2339, 408,1590,2780,3548,1838,4117,3719,1345,3530, 717,3442,2778,3220,
-2898,1892,4590,3614,3371,2043,1998,1224,3483, 891, 635, 584,2559,3355, 733,1766,
-1729,1172,3789,1891,2307, 781,2982,2271,1957,1580,5773,2633,2005,4195,3097,1535,
-3213,1189,1934,5693,3262, 586,3118,1324,1598, 517,1564,2217,1868,1893,4445,3728,
-2703,3139,1526,1787,1992,3882,2875,1549,1199,1056,2224,1904,2711,5098,4287, 338,
-1993,3129,3489,2689,1809,2815,1997, 957,1855,3898,2550,3275,3057,1105,1319, 627,
-1505,1911,1883,3526, 698,3629,3456,1833,1431, 746,  77,1261,2017,2296,1977,1885,
- 125,1334,1600, 525,1798,1109,2222,1470,1945, 559,2236,1186,3443,2476,1929,1411,
-2411,3135,1777,3372,2621,1841,1613,3229, 668,1430,1839,2643,2916, 195,1989,2671,
-2358,1387, 629,3205,2293,5256,4439, 123,1310, 888,1879,4300,3021,3605,1003,1162,
-3192,2910,2010, 140,2395,2859,  55,1082,2012,2901, 662, 419,2081,1438, 680,2774,
-4654,3912,1620,1731,1625,5035,4065,2328, 512,1344, 802,5443,2163,2311,2537, 524,
-3399,  98,1155,2103,1918,2606,3925,2816,1393,2465,1504,3773,2177,3963,1478,4346,
- 180,1113,4655,3461,2028,1698, 833,2696,1235,1322,1594,4408,3623,3013,3225,2040,
-3022, 541,2881, 607,3632,2029,1665,1219, 639,1385,1686,1099,2803,3231,1938,3188,
-2858, 427, 676,2772,1168,2025, 454,3253,2486,3556, 230,1950, 580, 791,1991,1280,
-1086,1974,2034, 630, 257,3338,2788,4903,1017,  86,4790, 966,2789,1995,1696,1131,
- 259,3095,4188,1308, 179,1463,5257, 289,4107,1248,  42,3413,1725,2288, 896,1947,
- 774,4474,4254, 604,3430,4264, 392,2514,2588, 452, 237,1408,3018, 988,4531,1970,
-3034,3310, 540,2370,1562,1288,2990, 502,4765,1147,   4,1853,2708, 207, 294,2814,
-4078,2902,2509, 684,  34,3105,3532,2551, 644, 709,2801,2344, 573,1727,3573,3557,
-2021,1081,3100,4315,2100,3681, 199,2263,1837,2385, 146,3484,1195,2776,3949, 997,
-1939,3973,1008,1091,1202,1962,1847,1149,4209,5444,1076, 493, 117,5400,2521, 972,
-1490,2934,1796,4542,2374,1512,2933,2657, 413,2888,1135,2762,2314,2156,1355,2369,
- 766,2007,2527,2170,3124,2491,2593,2632,4757,2437, 234,3125,3591,1898,1750,1376,
-1942,3468,3138, 570,2127,2145,3276,4131, 962, 132,1445,4196,  19, 941,3624,3480,
-3366,1973,1374,4461,3431,2629, 283,2415,2275, 808,2887,3620,2112,2563,1353,3610,
- 955,1089,3103,1053,  96,  88,4097, 823,3808,1583, 399, 292,4091,3313, 421,1128,
- 642,4006, 903,2539,1877,2082, 596,  29,4066,1790, 722,2157, 130, 995,1569, 769,
-1485, 464, 513,2213, 288,1923,1101,2453,4316, 133, 486,2445,  50, 625, 487,2207,
-  57, 423, 481,2962, 159,3729,1558, 491, 303, 482, 501, 240,2837, 112,3648,2392,
-1783, 362,   8,3433,3422, 610,2793,3277,1390,1284,1654,  21,3823, 734, 367, 623,
- 193, 287, 374,1009,1483, 816, 476, 313,2255,2340,1262,2150,2899,1146,2581, 782,
-2116,1659,2018,1880, 255,3586,3314,1110,2867,2137,2564, 986,2767,5185,2006, 650,
- 158, 926, 762, 881,3157,2717,2362,3587, 306,3690,3245,1542,3077,2427,1691,2478,
-2118,2985,3490,2438, 539,2305, 983, 129,1754, 355,4201,2386, 827,2923, 104,1773,
-2838,2771, 411,2905,3919, 376, 767, 122,1114, 828,2422,1817,3506, 266,3460,1007,
-1609,4998, 945,2612,4429,2274, 726,1247,1964,2914,2199,2070,4002,4108, 657,3323,
-1422, 579, 455,2764,4737,1222,2895,1670, 824,1223,1487,2525, 558, 861,3080, 598,
-2659,2515,1967, 752,2583,2376,2214,4180, 977, 704,2464,4999,2622,4109,1210,2961,
- 819,1541, 142,2284,  44, 418, 457,1126,3730,4347,4626,1644,1876,3671,1864, 302,
-1063,5694, 624, 723,1984,3745,1314,1676,2488,1610,1449,3558,3569,2166,2098, 409,
-1011,2325,3704,2306, 818,1732,1383,1824,1844,3757, 999,2705,3497,1216,1423,2683,
-2426,2954,2501,2726,2229,1475,2554,5064,1971,1794,1666,2014,1343, 783, 724, 191,
-2434,1354,2220,5065,1763,2752,2472,4152, 131, 175,2885,3434,  92,1466,4920,2616,
-3871,3872,3866, 128,1551,1632, 669,1854,3682,4691,4125,1230, 188,2973,3290,1302,
-1213, 560,3266, 917, 763,3909,3249,1760, 868,1958, 764,1782,2097, 145,2277,3774,
-4462,  64,1491,3062, 971,2132,3606,2442, 221,1226,1617, 218, 323,1185,3207,3147,
- 571, 619,1473,1005,1744,2281, 449,1887,2396,3685, 275, 375,3816,1743,3844,3731,
- 845,1983,2350,4210,1377, 773, 967,3499,3052,3743,2725,4007,1697,1022,3943,1464,
-3264,2855,2722,1952,1029,2839,2467,  84,4383,2215, 820,1391,2015,2448,3672, 377,
-1948,2168, 797,2545,3536,2578,2645,  94,2874,1678, 405,1259,3071, 771, 546,1315,
- 470,1243,3083, 895,2468, 981, 969,2037, 846,4181, 653,1276,2928,  14,2594, 557,
-3007,2474, 156, 902,1338,1740,2574, 537,2518, 973,2282,2216,2433,1928, 138,2903,
-1293,2631,1612, 646,3457, 839,2935, 111, 496,2191,2847, 589,3186, 149,3994,2060,
-4031,2641,4067,3145,1870,  37,3597,2136,1025,2051,3009,3383,3549,1121,1016,3261,
-1301, 251,2446,2599,2153, 872,3246, 637, 334,3705, 831, 884, 921,3065,3140,4092,
-2198,1944, 246,2964, 108,2045,1152,1921,2308,1031, 203,3173,4170,1907,3890, 810,
-1401,2003,1690, 506, 647,1242,2828,1761,1649,3208,2249,1589,3709,2931,5156,1708,
- 498, 666,2613, 834,3817,1231, 184,2851,1124, 883,3197,2261,3710,1765,1553,2658,
-1178,2639,2351,  93,1193, 942,2538,2141,4402, 235,1821, 870,1591,2192,1709,1871,
-3341,1618,4126,2595,2334, 603, 651,  69, 701, 268,2662,3411,2555,1380,1606, 503,
- 448, 254,2371,2646, 574,1187,2309,1770, 322,2235,1292,1801, 305, 566,1133, 229,
-2067,2057, 706, 167, 483,2002,2672,3295,1820,3561,3067, 316, 378,2746,3452,1112,
- 136,1981, 507,1651,2917,1117, 285,4591, 182,2580,3522,1304, 335,3303,1835,2504,
-1795,1792,2248, 674,1018,2106,2449,1857,2292,2845, 976,3047,1781,2600,2727,1389,
-1281,  52,3152, 153, 265,3950, 672,3485,3951,4463, 430,1183, 365, 278,2169,  27,
-1407,1336,2304, 209,1340,1730,2202,1852,2403,2883, 979,1737,1062, 631,2829,2542,
-3876,2592, 825,2086,2226,3048,3625, 352,1417,3724, 542, 991, 431,1351,3938,1861,
-2294, 826,1361,2927,3142,3503,1738, 463,2462,2723, 582,1916,1595,2808, 400,3845,
-3891,2868,3621,2254,  58,2492,1123, 910,2160,2614,1372,1603,1196,1072,3385,1700,
-3267,1980, 696, 480,2430, 920, 799,1570,2920,1951,2041,4047,2540,1321,4223,2469,
-3562,2228,1271,2602, 401,2833,3351,2575,5157, 907,2312,1256, 410, 263,3507,1582,
- 996, 678,1849,2316,1480, 908,3545,2237, 703,2322, 667,1826,2849,1531,2604,2999,
-2407,3146,2151,2630,1786,3711, 469,3542, 497,3899,2409, 858, 837,4446,3393,1274,
- 786, 620,1845,2001,3311, 484, 308,3367,1204,1815,3691,2332,1532,2557,1842,2020,
-2724,1927,2333,4440, 567,  22,1673,2728,4475,1987,1858,1144,1597, 101,1832,3601,
-  12, 974,3783,4391, 951,1412,   1,3720, 453,4608,4041, 528,1041,1027,3230,2628,
-1129, 875,1051,3291,1203,2262,1069,2860,2799,2149,2615,3278, 144,1758,3040,  31,
- 475,1680, 366,2685,3184, 311,1642,4008,2466,5036,1593,1493,2809, 216,1420,1668,
- 233, 304,2128,3284, 232,1429,1768,1040,2008,3407,2740,2967,2543, 242,2133, 778,
-1565,2022,2620, 505,2189,2756,1098,2273, 372,1614, 708, 553,2846,2094,2278, 169,
-3626,2835,4161, 228,2674,3165, 809,1454,1309, 466,1705,1095, 900,3423, 880,2667,
-3751,5258,2317,3109,2571,4317,2766,1503,1342, 866,4447,1118,  63,2076, 314,1881,
-1348,1061, 172, 978,3515,1747, 532, 511,3970,   6, 601, 905,2699,3300,1751, 276,
-1467,3725,2668,  65,4239,2544,2779,2556,1604, 578,2451,1802, 992,2331,2624,1320,
-3446, 713,1513,1013, 103,2786,2447,1661, 886,1702, 916, 654,3574,2031,1556, 751,
-2178,2821,2179,1498,1538,2176, 271, 914,2251,2080,1325, 638,1953,2937,3877,2432,
-2754,  95,3265,1716, 260,1227,4083, 775, 106,1357,3254, 426,1607, 555,2480, 772,
-1985, 244,2546, 474, 495,1046,2611,1851,2061,  71,2089,1675,2590, 742,3758,2843,
-3222,1433, 267,2180,2576,2826,2233,2092,3913,2435, 956,1745,3075, 856,2113,1116,
- 451,   3,1988,2896,1398, 993,2463,1878,2049,1341,2718,2721,2870,2108, 712,2904,
-4363,2753,2324, 277,2872,2349,2649, 384, 987, 435, 691,3000, 922, 164,3939, 652,
-1500,1184,4153,2482,3373,2165,4848,2335,3775,3508,3154,2806,2830,1554,2102,1664,
-2530,1434,2408, 893,1547,2623,3447,2832,2242,2532,3169,2856,3223,2078,  49,3770,
-3469, 462, 318, 656,2259,3250,3069, 679,1629,2758, 344,1138,1104,3120,1836,1283,
-3115,2154,1437,4448, 934, 759,1999, 794,2862,1038, 533,2560,1722,2342, 855,2626,
-1197,1663,4476,3127,  85,4240,2528,  25,1111,1181,3673, 407,3470,4561,2679,2713,
- 768,1925,2841,3986,1544,1165, 932, 373,1240,2146,1930,2673, 721,4766, 354,4333,
- 391,2963, 187,  61,3364,1442,1102, 330,1940,1767, 341,3809,4118, 393,2496,2062,
-2211, 105, 331, 300, 439, 913,1332, 626, 379,3304,1557, 328, 689,3952, 309,1555,
- 931, 317,2517,3027, 325, 569, 686,2107,3084,  60,1042,1333,2794, 264,3177,4014,
-1628, 258,3712,   7,4464,1176,1043,1778, 683, 114,1975,  78,1492, 383,1886, 510,
- 386, 645,5291,2891,2069,3305,4138,3867,2939,2603,2493,1935,1066,1848,3588,1015,
-1282,1289,4609, 697,1453,3044,2666,3611,1856,2412,  54, 719,1330, 568,3778,2459,
-1748, 788, 492, 551,1191,1000, 488,3394,3763, 282,1799, 348,2016,1523,3155,2390,
-1049, 382,2019,1788,1170, 729,2968,3523, 897,3926,2785,2938,3292, 350,2319,3238,
-1718,1717,2655,3453,3143,4465, 161,2889,2980,2009,1421,  56,1908,1640,2387,2232,
-1917,1874,2477,4921, 148,  83,3438, 592,4245,2882,1822,1055, 741, 115,1496,1624,
- 381,1638,4592,1020, 516,3214, 458, 947,4575,1432, 211,1514,2926,1865,2142, 189,
- 852,1221,1400,1486, 882,2299,4036, 351,  28,1122, 700,6479,6480,6481,6482,6483,  #last 512
-)
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/gb2312prober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/gb2312prober.py
deleted file mode 100644
index 8446d2d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/gb2312prober.py
+++ /dev/null
@@ -1,46 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .mbcharsetprober import MultiByteCharSetProber
-from .codingstatemachine import CodingStateMachine
-from .chardistribution import GB2312DistributionAnalysis
-from .mbcssm import GB2312_SM_MODEL
-
-class GB2312Prober(MultiByteCharSetProber):
-    def __init__(self):
-        super(GB2312Prober, self).__init__()
-        self.coding_sm = CodingStateMachine(GB2312_SM_MODEL)
-        self.distribution_analyzer = GB2312DistributionAnalysis()
-        self.reset()
-
-    @property
-    def charset_name(self):
-        return "GB2312"
-
-    @property
-    def language(self):
-        return "Chinese"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/hebrewprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/hebrewprober.py
deleted file mode 100644
index b0e1bf4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/hebrewprober.py
+++ /dev/null
@@ -1,292 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-#          Shy Shalom
-# Portions created by the Initial Developer are Copyright (C) 2005
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetprober import CharSetProber
-from .enums import ProbingState
-
-# This prober doesn't actually recognize a language or a charset.
-# It is a helper prober for the use of the Hebrew model probers
-
-### General ideas of the Hebrew charset recognition ###
-#
-# Four main charsets exist in Hebrew:
-# "ISO-8859-8" - Visual Hebrew
-# "windows-1255" - Logical Hebrew
-# "ISO-8859-8-I" - Logical Hebrew
-# "x-mac-hebrew" - ?? Logical Hebrew ??
-#
-# Both "ISO" charsets use a completely identical set of code points, whereas
-# "windows-1255" and "x-mac-hebrew" are two different proper supersets of
-# these code points. windows-1255 defines additional characters in the range
-# 0x80-0x9F as some misc punctuation marks as well as some Hebrew-specific
-# diacritics and additional 'Yiddish' ligature letters in the range 0xc0-0xd6.
-# x-mac-hebrew defines similar additional code points but with a different
-# mapping.
-#
-# As far as an average Hebrew text with no diacritics is concerned, all four
-# charsets are identical with respect to code points. Meaning that for the
-# main Hebrew alphabet, all four map the same values to all 27 Hebrew letters
-# (including final letters).
-#
-# The dominant difference between these charsets is their directionality.
-# "Visual" directionality means that the text is ordered as if the renderer is
-# not aware of a BIDI rendering algorithm. The renderer sees the text and
-# draws it from left to right. The text itself when ordered naturally is read
-# backwards. A buffer of Visual Hebrew generally looks like so:
-# "[last word of first line spelled backwards] [whole line ordered backwards
-# and spelled backwards] [first word of first line spelled backwards]
-# [end of line] [last word of second line] ... etc' "
-# adding punctuation marks, numbers and English text to visual text is
-# naturally also "visual" and from left to right.
-#
-# "Logical" directionality means the text is ordered "naturally" according to
-# the order it is read. It is the responsibility of the renderer to display
-# the text from right to left. A BIDI algorithm is used to place general
-# punctuation marks, numbers and English text in the text.
-#
-# Texts in x-mac-hebrew are almost impossible to find on the Internet. From
-# what little evidence I could find, it seems that its general directionality
-# is Logical.
-#
-# To sum up all of the above, the Hebrew probing mechanism knows about two
-# charsets:
-# Visual Hebrew - "ISO-8859-8" - backwards text - Words and sentences are
-#    backwards while line order is natural. For charset recognition purposes
-#    the line order is unimportant (In fact, for this implementation, even
-#    word order is unimportant).
-# Logical Hebrew - "windows-1255" - normal, naturally ordered text.
-#
-# "ISO-8859-8-I" is a subset of windows-1255 and doesn't need to be
-#    specifically identified.
-# "x-mac-hebrew" is also identified as windows-1255. A text in x-mac-hebrew
-#    that contain special punctuation marks or diacritics is displayed with
-#    some unconverted characters showing as question marks. This problem might
-#    be corrected using another model prober for x-mac-hebrew. Due to the fact
-#    that x-mac-hebrew texts are so rare, writing another model prober isn't
-#    worth the effort and performance hit.
-#
-#### The Prober ####
-#
-# The prober is divided between two SBCharSetProbers and a HebrewProber,
-# all of which are managed, created, fed data, inquired and deleted by the
-# SBCSGroupProber. The two SBCharSetProbers identify that the text is in
-# fact some kind of Hebrew, Logical or Visual. The final decision about which
-# one is it is made by the HebrewProber by combining final-letter scores
-# with the scores of the two SBCharSetProbers to produce a final answer.
-#
-# The SBCSGroupProber is responsible for stripping the original text of HTML
-# tags, English characters, numbers, low-ASCII punctuation characters, spaces
-# and new lines. It reduces any sequence of such characters to a single space.
-# The buffer fed to each prober in the SBCS group prober is pure text in
-# high-ASCII.
-# The two SBCharSetProbers (model probers) share the same language model:
-# Win1255Model.
-# The first SBCharSetProber uses the model normally as any other
-# SBCharSetProber does, to recognize windows-1255, upon which this model was
-# built. The second SBCharSetProber is told to make the pair-of-letter
-# lookup in the language model backwards. This in practice exactly simulates
-# a visual Hebrew model using the windows-1255 logical Hebrew model.
-#
-# The HebrewProber is not using any language model. All it does is look for
-# final-letter evidence suggesting the text is either logical Hebrew or visual
-# Hebrew. Disjointed from the model probers, the results of the HebrewProber
-# alone are meaningless. HebrewProber always returns 0.00 as confidence
-# since it never identifies a charset by itself. Instead, the pointer to the
-# HebrewProber is passed to the model probers as a helper "Name Prober".
-# When the Group prober receives a positive identification from any prober,
-# it asks for the name of the charset identified. If the prober queried is a
-# Hebrew model prober, the model prober forwards the call to the
-# HebrewProber to make the final decision. In the HebrewProber, the
-# decision is made according to the final-letters scores maintained and Both
-# model probers scores. The answer is returned in the form of the name of the
-# charset identified, either "windows-1255" or "ISO-8859-8".
-
-class HebrewProber(CharSetProber):
-    # windows-1255 / ISO-8859-8 code points of interest
-    FINAL_KAF = 0xea
-    NORMAL_KAF = 0xeb
-    FINAL_MEM = 0xed
-    NORMAL_MEM = 0xee
-    FINAL_NUN = 0xef
-    NORMAL_NUN = 0xf0
-    FINAL_PE = 0xf3
-    NORMAL_PE = 0xf4
-    FINAL_TSADI = 0xf5
-    NORMAL_TSADI = 0xf6
-
-    # Minimum Visual vs Logical final letter score difference.
-    # If the difference is below this, don't rely solely on the final letter score
-    # distance.
-    MIN_FINAL_CHAR_DISTANCE = 5
-
-    # Minimum Visual vs Logical model score difference.
-    # If the difference is below this, don't rely at all on the model score
-    # distance.
-    MIN_MODEL_DISTANCE = 0.01
-
-    VISUAL_HEBREW_NAME = "ISO-8859-8"
-    LOGICAL_HEBREW_NAME = "windows-1255"
-
-    def __init__(self):
-        super(HebrewProber, self).__init__()
-        self._final_char_logical_score = None
-        self._final_char_visual_score = None
-        self._prev = None
-        self._before_prev = None
-        self._logical_prober = None
-        self._visual_prober = None
-        self.reset()
-
-    def reset(self):
-        self._final_char_logical_score = 0
-        self._final_char_visual_score = 0
-        # The two last characters seen in the previous buffer,
-        # mPrev and mBeforePrev are initialized to space in order to simulate
-        # a word delimiter at the beginning of the data
-        self._prev = ' '
-        self._before_prev = ' '
-        # These probers are owned by the group prober.
-
-    def set_model_probers(self, logicalProber, visualProber):
-        self._logical_prober = logicalProber
-        self._visual_prober = visualProber
-
-    def is_final(self, c):
-        return c in [self.FINAL_KAF, self.FINAL_MEM, self.FINAL_NUN,
-                     self.FINAL_PE, self.FINAL_TSADI]
-
-    def is_non_final(self, c):
-        # The normal Tsadi is not a good Non-Final letter due to words like
-        # 'lechotet' (to chat) containing an apostrophe after the tsadi. This
-        # apostrophe is converted to a space in FilterWithoutEnglishLetters
-        # causing the Non-Final tsadi to appear at an end of a word even
-        # though this is not the case in the original text.
-        # The letters Pe and Kaf rarely display a related behavior of not being
-        # a good Non-Final letter. Words like 'Pop', 'Winamp' and 'Mubarak'
-        # for example legally end with a Non-Final Pe or Kaf. However, the
-        # benefit of these letters as Non-Final letters outweighs the damage
-        # since these words are quite rare.
-        return c in [self.NORMAL_KAF, self.NORMAL_MEM,
-                     self.NORMAL_NUN, self.NORMAL_PE]
-
-    def feed(self, byte_str):
-        # Final letter analysis for logical-visual decision.
-        # Look for evidence that the received buffer is either logical Hebrew
-        # or visual Hebrew.
-        # The following cases are checked:
-        # 1) A word longer than 1 letter, ending with a final letter. This is
-        #    an indication that the text is laid out "naturally" since the
-        #    final letter really appears at the end. +1 for logical score.
-        # 2) A word longer than 1 letter, ending with a Non-Final letter. In
-        #    normal Hebrew, words ending with Kaf, Mem, Nun, Pe or Tsadi,
-        #    should not end with the Non-Final form of that letter. Exceptions
-        #    to this rule are mentioned above in isNonFinal(). This is an
-        #    indication that the text is laid out backwards. +1 for visual
-        #    score
-        # 3) A word longer than 1 letter, starting with a final letter. Final
-        #    letters should not appear at the beginning of a word. This is an
-        #    indication that the text is laid out backwards. +1 for visual
-        #    score.
-        #
-        # The visual score and logical score are accumulated throughout the
-        # text and are finally checked against each other in GetCharSetName().
-        # No checking for final letters in the middle of words is done since
-        # that case is not an indication for either Logical or Visual text.
-        #
-        # We automatically filter out all 7-bit characters (replace them with
-        # spaces) so the word boundary detection works properly. [MAP]
-
-        if self.state == ProbingState.NOT_ME:
-            # Both model probers say it's not them. No reason to continue.
-            return ProbingState.NOT_ME
-
-        byte_str = self.filter_high_byte_only(byte_str)
-
-        for cur in byte_str:
-            if cur == ' ':
-                # We stand on a space - a word just ended
-                if self._before_prev != ' ':
-                    # next-to-last char was not a space so self._prev is not a
-                    # 1 letter word
-                    if self.is_final(self._prev):
-                        # case (1) [-2:not space][-1:final letter][cur:space]
-                        self._final_char_logical_score += 1
-                    elif self.is_non_final(self._prev):
-                        # case (2) [-2:not space][-1:Non-Final letter][
-                        #  cur:space]
-                        self._final_char_visual_score += 1
-            else:
-                # Not standing on a space
-                if ((self._before_prev == ' ') and
-                        (self.is_final(self._prev)) and (cur != ' ')):
-                    # case (3) [-2:space][-1:final letter][cur:not space]
-                    self._final_char_visual_score += 1
-            self._before_prev = self._prev
-            self._prev = cur
-
-        # Forever detecting, till the end or until both model probers return
-        # ProbingState.NOT_ME (handled above)
-        return ProbingState.DETECTING
-
-    @property
-    def charset_name(self):
-        # Make the decision: is it Logical or Visual?
-        # If the final letter score distance is dominant enough, rely on it.
-        finalsub = self._final_char_logical_score - self._final_char_visual_score
-        if finalsub >= self.MIN_FINAL_CHAR_DISTANCE:
-            return self.LOGICAL_HEBREW_NAME
-        if finalsub <= -self.MIN_FINAL_CHAR_DISTANCE:
-            return self.VISUAL_HEBREW_NAME
-
-        # It's not dominant enough, try to rely on the model scores instead.
-        modelsub = (self._logical_prober.get_confidence()
-                    - self._visual_prober.get_confidence())
-        if modelsub > self.MIN_MODEL_DISTANCE:
-            return self.LOGICAL_HEBREW_NAME
-        if modelsub < -self.MIN_MODEL_DISTANCE:
-            return self.VISUAL_HEBREW_NAME
-
-        # Still no good, back to final letter distance, maybe it'll save the
-        # day.
-        if finalsub < 0.0:
-            return self.VISUAL_HEBREW_NAME
-
-        # (finalsub > 0 - Logical) or (don't know what to do) default to
-        # Logical.
-        return self.LOGICAL_HEBREW_NAME
-
-    @property
-    def language(self):
-        return 'Hebrew'
-
-    @property
-    def state(self):
-        # Remain active as long as any of the model probers are active.
-        if (self._logical_prober.state == ProbingState.NOT_ME) and \
-           (self._visual_prober.state == ProbingState.NOT_ME):
-            return ProbingState.NOT_ME
-        return ProbingState.DETECTING
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/jisfreq.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/jisfreq.py
deleted file mode 100644
index 83fc082..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/jisfreq.py
+++ /dev/null
@@ -1,325 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# Sampling from about 20M text materials include literature and computer technology
-#
-# Japanese frequency table, applied to both S-JIS and EUC-JP
-# They are sorted in order.
-
-# 128  --> 0.77094
-# 256  --> 0.85710
-# 512  --> 0.92635
-# 1024 --> 0.97130
-# 2048 --> 0.99431
-#
-# Ideal Distribution Ratio = 0.92635 / (1-0.92635) = 12.58
-# Random Distribution Ration = 512 / (2965+62+83+86-512) = 0.191
-#
-# Typical Distribution Ratio, 25% of IDR
-
-JIS_TYPICAL_DISTRIBUTION_RATIO = 3.0
-
-# Char to FreqOrder table ,
-JIS_TABLE_SIZE = 4368
-
-JIS_CHAR_TO_FREQ_ORDER = (
-  40,   1,   6, 182, 152, 180, 295,2127, 285, 381,3295,4304,3068,4606,3165,3510, #   16
-3511,1822,2785,4607,1193,2226,5070,4608, 171,2996,1247,  18, 179,5071, 856,1661, #   32
-1262,5072, 619, 127,3431,3512,3230,1899,1700, 232, 228,1294,1298, 284, 283,2041, #   48
-2042,1061,1062,  48,  49,  44,  45, 433, 434,1040,1041, 996, 787,2997,1255,4305, #   64
-2108,4609,1684,1648,5073,5074,5075,5076,5077,5078,3687,5079,4610,5080,3927,3928, #   80
-5081,3296,3432, 290,2285,1471,2187,5082,2580,2825,1303,2140,1739,1445,2691,3375, #   96
-1691,3297,4306,4307,4611, 452,3376,1182,2713,3688,3069,4308,5083,5084,5085,5086, #  112
-5087,5088,5089,5090,5091,5092,5093,5094,5095,5096,5097,5098,5099,5100,5101,5102, #  128
-5103,5104,5105,5106,5107,5108,5109,5110,5111,5112,4097,5113,5114,5115,5116,5117, #  144
-5118,5119,5120,5121,5122,5123,5124,5125,5126,5127,5128,5129,5130,5131,5132,5133, #  160
-5134,5135,5136,5137,5138,5139,5140,5141,5142,5143,5144,5145,5146,5147,5148,5149, #  176
-5150,5151,5152,4612,5153,5154,5155,5156,5157,5158,5159,5160,5161,5162,5163,5164, #  192
-5165,5166,5167,5168,5169,5170,5171,5172,5173,5174,5175,1472, 598, 618, 820,1205, #  208
-1309,1412,1858,1307,1692,5176,5177,5178,5179,5180,5181,5182,1142,1452,1234,1172, #  224
-1875,2043,2149,1793,1382,2973, 925,2404,1067,1241, 960,1377,2935,1491, 919,1217, #  240
-1865,2030,1406,1499,2749,4098,5183,5184,5185,5186,5187,5188,2561,4099,3117,1804, #  256
-2049,3689,4309,3513,1663,5189,3166,3118,3298,1587,1561,3433,5190,3119,1625,2998, #  272
-3299,4613,1766,3690,2786,4614,5191,5192,5193,5194,2161,  26,3377,   2,3929,  20, #  288
-3691,  47,4100,  50,  17,  16,  35, 268,  27, 243,  42, 155,  24, 154,  29, 184, #  304
-   4,  91,  14,  92,  53, 396,  33, 289,   9,  37,  64, 620,  21,  39, 321,   5, #  320
-  12,  11,  52,  13,   3, 208, 138,   0,   7,  60, 526, 141, 151,1069, 181, 275, #  336
-1591,  83, 132,1475, 126, 331, 829,  15,  69, 160,  59,  22, 157,  55,1079, 312, #  352
- 109,  38,  23,  25,  10,  19,  79,5195,  61, 382,1124,   8,  30,5196,5197,5198, #  368
-5199,5200,5201,5202,5203,5204,5205,5206,  89,  62,  74,  34,2416, 112, 139, 196, #  384
- 271, 149,  84, 607, 131, 765,  46,  88, 153, 683,  76, 874, 101, 258,  57,  80, #  400
-  32, 364, 121,1508, 169,1547,  68, 235, 145,2999,  41, 360,3027,  70,  63,  31, #  416
-  43, 259, 262,1383,  99, 533, 194,  66,  93, 846, 217, 192,  56, 106,  58, 565, #  432
- 280, 272, 311, 256, 146,  82, 308,  71, 100, 128, 214, 655, 110, 261, 104,1140, #  448
-  54,  51,  36,  87,  67,3070, 185,2618,2936,2020,  28,1066,2390,2059,5207,5208, #  464
-5209,5210,5211,5212,5213,5214,5215,5216,4615,5217,5218,5219,5220,5221,5222,5223, #  480
-5224,5225,5226,5227,5228,5229,5230,5231,5232,5233,5234,5235,5236,3514,5237,5238, #  496
-5239,5240,5241,5242,5243,5244,2297,2031,4616,4310,3692,5245,3071,5246,3598,5247, #  512
-4617,3231,3515,5248,4101,4311,4618,3808,4312,4102,5249,4103,4104,3599,5250,5251, #  528
-5252,5253,5254,5255,5256,5257,5258,5259,5260,5261,5262,5263,5264,5265,5266,5267, #  544
-5268,5269,5270,5271,5272,5273,5274,5275,5276,5277,5278,5279,5280,5281,5282,5283, #  560
-5284,5285,5286,5287,5288,5289,5290,5291,5292,5293,5294,5295,5296,5297,5298,5299, #  576
-5300,5301,5302,5303,5304,5305,5306,5307,5308,5309,5310,5311,5312,5313,5314,5315, #  592
-5316,5317,5318,5319,5320,5321,5322,5323,5324,5325,5326,5327,5328,5329,5330,5331, #  608
-5332,5333,5334,5335,5336,5337,5338,5339,5340,5341,5342,5343,5344,5345,5346,5347, #  624
-5348,5349,5350,5351,5352,5353,5354,5355,5356,5357,5358,5359,5360,5361,5362,5363, #  640
-5364,5365,5366,5367,5368,5369,5370,5371,5372,5373,5374,5375,5376,5377,5378,5379, #  656
-5380,5381, 363, 642,2787,2878,2788,2789,2316,3232,2317,3434,2011, 165,1942,3930, #  672
-3931,3932,3933,5382,4619,5383,4620,5384,5385,5386,5387,5388,5389,5390,5391,5392, #  688
-5393,5394,5395,5396,5397,5398,5399,5400,5401,5402,5403,5404,5405,5406,5407,5408, #  704
-5409,5410,5411,5412,5413,5414,5415,5416,5417,5418,5419,5420,5421,5422,5423,5424, #  720
-5425,5426,5427,5428,5429,5430,5431,5432,5433,5434,5435,5436,5437,5438,5439,5440, #  736
-5441,5442,5443,5444,5445,5446,5447,5448,5449,5450,5451,5452,5453,5454,5455,5456, #  752
-5457,5458,5459,5460,5461,5462,5463,5464,5465,5466,5467,5468,5469,5470,5471,5472, #  768
-5473,5474,5475,5476,5477,5478,5479,5480,5481,5482,5483,5484,5485,5486,5487,5488, #  784
-5489,5490,5491,5492,5493,5494,5495,5496,5497,5498,5499,5500,5501,5502,5503,5504, #  800
-5505,5506,5507,5508,5509,5510,5511,5512,5513,5514,5515,5516,5517,5518,5519,5520, #  816
-5521,5522,5523,5524,5525,5526,5527,5528,5529,5530,5531,5532,5533,5534,5535,5536, #  832
-5537,5538,5539,5540,5541,5542,5543,5544,5545,5546,5547,5548,5549,5550,5551,5552, #  848
-5553,5554,5555,5556,5557,5558,5559,5560,5561,5562,5563,5564,5565,5566,5567,5568, #  864
-5569,5570,5571,5572,5573,5574,5575,5576,5577,5578,5579,5580,5581,5582,5583,5584, #  880
-5585,5586,5587,5588,5589,5590,5591,5592,5593,5594,5595,5596,5597,5598,5599,5600, #  896
-5601,5602,5603,5604,5605,5606,5607,5608,5609,5610,5611,5612,5613,5614,5615,5616, #  912
-5617,5618,5619,5620,5621,5622,5623,5624,5625,5626,5627,5628,5629,5630,5631,5632, #  928
-5633,5634,5635,5636,5637,5638,5639,5640,5641,5642,5643,5644,5645,5646,5647,5648, #  944
-5649,5650,5651,5652,5653,5654,5655,5656,5657,5658,5659,5660,5661,5662,5663,5664, #  960
-5665,5666,5667,5668,5669,5670,5671,5672,5673,5674,5675,5676,5677,5678,5679,5680, #  976
-5681,5682,5683,5684,5685,5686,5687,5688,5689,5690,5691,5692,5693,5694,5695,5696, #  992
-5697,5698,5699,5700,5701,5702,5703,5704,5705,5706,5707,5708,5709,5710,5711,5712, # 1008
-5713,5714,5715,5716,5717,5718,5719,5720,5721,5722,5723,5724,5725,5726,5727,5728, # 1024
-5729,5730,5731,5732,5733,5734,5735,5736,5737,5738,5739,5740,5741,5742,5743,5744, # 1040
-5745,5746,5747,5748,5749,5750,5751,5752,5753,5754,5755,5756,5757,5758,5759,5760, # 1056
-5761,5762,5763,5764,5765,5766,5767,5768,5769,5770,5771,5772,5773,5774,5775,5776, # 1072
-5777,5778,5779,5780,5781,5782,5783,5784,5785,5786,5787,5788,5789,5790,5791,5792, # 1088
-5793,5794,5795,5796,5797,5798,5799,5800,5801,5802,5803,5804,5805,5806,5807,5808, # 1104
-5809,5810,5811,5812,5813,5814,5815,5816,5817,5818,5819,5820,5821,5822,5823,5824, # 1120
-5825,5826,5827,5828,5829,5830,5831,5832,5833,5834,5835,5836,5837,5838,5839,5840, # 1136
-5841,5842,5843,5844,5845,5846,5847,5848,5849,5850,5851,5852,5853,5854,5855,5856, # 1152
-5857,5858,5859,5860,5861,5862,5863,5864,5865,5866,5867,5868,5869,5870,5871,5872, # 1168
-5873,5874,5875,5876,5877,5878,5879,5880,5881,5882,5883,5884,5885,5886,5887,5888, # 1184
-5889,5890,5891,5892,5893,5894,5895,5896,5897,5898,5899,5900,5901,5902,5903,5904, # 1200
-5905,5906,5907,5908,5909,5910,5911,5912,5913,5914,5915,5916,5917,5918,5919,5920, # 1216
-5921,5922,5923,5924,5925,5926,5927,5928,5929,5930,5931,5932,5933,5934,5935,5936, # 1232
-5937,5938,5939,5940,5941,5942,5943,5944,5945,5946,5947,5948,5949,5950,5951,5952, # 1248
-5953,5954,5955,5956,5957,5958,5959,5960,5961,5962,5963,5964,5965,5966,5967,5968, # 1264
-5969,5970,5971,5972,5973,5974,5975,5976,5977,5978,5979,5980,5981,5982,5983,5984, # 1280
-5985,5986,5987,5988,5989,5990,5991,5992,5993,5994,5995,5996,5997,5998,5999,6000, # 1296
-6001,6002,6003,6004,6005,6006,6007,6008,6009,6010,6011,6012,6013,6014,6015,6016, # 1312
-6017,6018,6019,6020,6021,6022,6023,6024,6025,6026,6027,6028,6029,6030,6031,6032, # 1328
-6033,6034,6035,6036,6037,6038,6039,6040,6041,6042,6043,6044,6045,6046,6047,6048, # 1344
-6049,6050,6051,6052,6053,6054,6055,6056,6057,6058,6059,6060,6061,6062,6063,6064, # 1360
-6065,6066,6067,6068,6069,6070,6071,6072,6073,6074,6075,6076,6077,6078,6079,6080, # 1376
-6081,6082,6083,6084,6085,6086,6087,6088,6089,6090,6091,6092,6093,6094,6095,6096, # 1392
-6097,6098,6099,6100,6101,6102,6103,6104,6105,6106,6107,6108,6109,6110,6111,6112, # 1408
-6113,6114,2044,2060,4621, 997,1235, 473,1186,4622, 920,3378,6115,6116, 379,1108, # 1424
-4313,2657,2735,3934,6117,3809, 636,3233, 573,1026,3693,3435,2974,3300,2298,4105, # 1440
- 854,2937,2463, 393,2581,2417, 539, 752,1280,2750,2480, 140,1161, 440, 708,1569, # 1456
- 665,2497,1746,1291,1523,3000, 164,1603, 847,1331, 537,1997, 486, 508,1693,2418, # 1472
-1970,2227, 878,1220, 299,1030, 969, 652,2751, 624,1137,3301,2619,  65,3302,2045, # 1488
-1761,1859,3120,1930,3694,3516, 663,1767, 852, 835,3695, 269, 767,2826,2339,1305, # 1504
- 896,1150, 770,1616,6118, 506,1502,2075,1012,2519, 775,2520,2975,2340,2938,4314, # 1520
-3028,2086,1224,1943,2286,6119,3072,4315,2240,1273,1987,3935,1557, 175, 597, 985, # 1536
-3517,2419,2521,1416,3029, 585, 938,1931,1007,1052,1932,1685,6120,3379,4316,4623, # 1552
- 804, 599,3121,1333,2128,2539,1159,1554,2032,3810, 687,2033,2904, 952, 675,1467, # 1568
-3436,6121,2241,1096,1786,2440,1543,1924, 980,1813,2228, 781,2692,1879, 728,1918, # 1584
-3696,4624, 548,1950,4625,1809,1088,1356,3303,2522,1944, 502, 972, 373, 513,2827, # 1600
- 586,2377,2391,1003,1976,1631,6122,2464,1084, 648,1776,4626,2141, 324, 962,2012, # 1616
-2177,2076,1384, 742,2178,1448,1173,1810, 222, 102, 301, 445, 125,2420, 662,2498, # 1632
- 277, 200,1476,1165,1068, 224,2562,1378,1446, 450,1880, 659, 791, 582,4627,2939, # 1648
-3936,1516,1274, 555,2099,3697,1020,1389,1526,3380,1762,1723,1787,2229, 412,2114, # 1664
-1900,2392,3518, 512,2597, 427,1925,2341,3122,1653,1686,2465,2499, 697, 330, 273, # 1680
- 380,2162, 951, 832, 780, 991,1301,3073, 965,2270,3519, 668,2523,2636,1286, 535, # 1696
-1407, 518, 671, 957,2658,2378, 267, 611,2197,3030,6123, 248,2299, 967,1799,2356, # 1712
- 850,1418,3437,1876,1256,1480,2828,1718,6124,6125,1755,1664,2405,6126,4628,2879, # 1728
-2829, 499,2179, 676,4629, 557,2329,2214,2090, 325,3234, 464, 811,3001, 992,2342, # 1744
-2481,1232,1469, 303,2242, 466,1070,2163, 603,1777,2091,4630,2752,4631,2714, 322, # 1760
-2659,1964,1768, 481,2188,1463,2330,2857,3600,2092,3031,2421,4632,2318,2070,1849, # 1776
-2598,4633,1302,2254,1668,1701,2422,3811,2905,3032,3123,2046,4106,1763,1694,4634, # 1792
-1604, 943,1724,1454, 917, 868,2215,1169,2940, 552,1145,1800,1228,1823,1955, 316, # 1808
-1080,2510, 361,1807,2830,4107,2660,3381,1346,1423,1134,4108,6127, 541,1263,1229, # 1824
-1148,2540, 545, 465,1833,2880,3438,1901,3074,2482, 816,3937, 713,1788,2500, 122, # 1840
-1575, 195,1451,2501,1111,6128, 859, 374,1225,2243,2483,4317, 390,1033,3439,3075, # 1856
-2524,1687, 266, 793,1440,2599, 946, 779, 802, 507, 897,1081, 528,2189,1292, 711, # 1872
-1866,1725,1167,1640, 753, 398,2661,1053, 246, 348,4318, 137,1024,3440,1600,2077, # 1888
-2129, 825,4319, 698, 238, 521, 187,2300,1157,2423,1641,1605,1464,1610,1097,2541, # 1904
-1260,1436, 759,2255,1814,2150, 705,3235, 409,2563,3304, 561,3033,2005,2564, 726, # 1920
-1956,2343,3698,4109, 949,3812,3813,3520,1669, 653,1379,2525, 881,2198, 632,2256, # 1936
-1027, 778,1074, 733,1957, 514,1481,2466, 554,2180, 702,3938,1606,1017,1398,6129, # 1952
-1380,3521, 921, 993,1313, 594, 449,1489,1617,1166, 768,1426,1360, 495,1794,3601, # 1968
-1177,3602,1170,4320,2344, 476, 425,3167,4635,3168,1424, 401,2662,1171,3382,1998, # 1984
-1089,4110, 477,3169, 474,6130,1909, 596,2831,1842, 494, 693,1051,1028,1207,3076, # 2000
- 606,2115, 727,2790,1473,1115, 743,3522, 630, 805,1532,4321,2021, 366,1057, 838, # 2016
- 684,1114,2142,4322,2050,1492,1892,1808,2271,3814,2424,1971,1447,1373,3305,1090, # 2032
-1536,3939,3523,3306,1455,2199, 336, 369,2331,1035, 584,2393, 902, 718,2600,6131, # 2048
-2753, 463,2151,1149,1611,2467, 715,1308,3124,1268, 343,1413,3236,1517,1347,2663, # 2064
-2093,3940,2022,1131,1553,2100,2941,1427,3441,2942,1323,2484,6132,1980, 872,2368, # 2080
-2441,2943, 320,2369,2116,1082, 679,1933,3941,2791,3815, 625,1143,2023, 422,2200, # 2096
-3816,6133, 730,1695, 356,2257,1626,2301,2858,2637,1627,1778, 937, 883,2906,2693, # 2112
-3002,1769,1086, 400,1063,1325,3307,2792,4111,3077, 456,2345,1046, 747,6134,1524, # 2128
- 884,1094,3383,1474,2164,1059, 974,1688,2181,2258,1047, 345,1665,1187, 358, 875, # 2144
-3170, 305, 660,3524,2190,1334,1135,3171,1540,1649,2542,1527, 927, 968,2793, 885, # 2160
-1972,1850, 482, 500,2638,1218,1109,1085,2543,1654,2034, 876,  78,2287,1482,1277, # 2176
- 861,1675,1083,1779, 724,2754, 454, 397,1132,1612,2332, 893, 672,1237, 257,2259, # 2192
-2370, 135,3384, 337,2244, 547, 352, 340, 709,2485,1400, 788,1138,2511, 540, 772, # 2208
-1682,2260,2272,2544,2013,1843,1902,4636,1999,1562,2288,4637,2201,1403,1533, 407, # 2224
- 576,3308,1254,2071, 978,3385, 170, 136,1201,3125,2664,3172,2394, 213, 912, 873, # 2240
-3603,1713,2202, 699,3604,3699, 813,3442, 493, 531,1054, 468,2907,1483, 304, 281, # 2256
-4112,1726,1252,2094, 339,2319,2130,2639, 756,1563,2944, 748, 571,2976,1588,2425, # 2272
-2715,1851,1460,2426,1528,1392,1973,3237, 288,3309, 685,3386, 296, 892,2716,2216, # 2288
-1570,2245, 722,1747,2217, 905,3238,1103,6135,1893,1441,1965, 251,1805,2371,3700, # 2304
-2601,1919,1078,  75,2182,1509,1592,1270,2640,4638,2152,6136,3310,3817, 524, 706, # 2320
-1075, 292,3818,1756,2602, 317,  98,3173,3605,3525,1844,2218,3819,2502, 814, 567, # 2336
- 385,2908,1534,6137, 534,1642,3239, 797,6138,1670,1529, 953,4323, 188,1071, 538, # 2352
- 178, 729,3240,2109,1226,1374,2000,2357,2977, 731,2468,1116,2014,2051,6139,1261, # 2368
-1593, 803,2859,2736,3443, 556, 682, 823,1541,6140,1369,2289,1706,2794, 845, 462, # 2384
-2603,2665,1361, 387, 162,2358,1740, 739,1770,1720,1304,1401,3241,1049, 627,1571, # 2400
-2427,3526,1877,3942,1852,1500, 431,1910,1503, 677, 297,2795, 286,1433,1038,1198, # 2416
-2290,1133,1596,4113,4639,2469,1510,1484,3943,6141,2442, 108, 712,4640,2372, 866, # 2432
-3701,2755,3242,1348, 834,1945,1408,3527,2395,3243,1811, 824, 994,1179,2110,1548, # 2448
-1453, 790,3003, 690,4324,4325,2832,2909,3820,1860,3821, 225,1748, 310, 346,1780, # 2464
-2470, 821,1993,2717,2796, 828, 877,3528,2860,2471,1702,2165,2910,2486,1789, 453, # 2480
- 359,2291,1676,  73,1164,1461,1127,3311, 421, 604, 314,1037, 589, 116,2487, 737, # 2496
- 837,1180, 111, 244, 735,6142,2261,1861,1362, 986, 523, 418, 581,2666,3822, 103, # 2512
- 855, 503,1414,1867,2488,1091, 657,1597, 979, 605,1316,4641,1021,2443,2078,2001, # 2528
-1209,  96, 587,2166,1032, 260,1072,2153, 173,  94, 226,3244, 819,2006,4642,4114, # 2544
-2203, 231,1744, 782,  97,2667, 786,3387, 887, 391, 442,2219,4326,1425,6143,2694, # 2560
- 633,1544,1202, 483,2015, 592,2052,1958,2472,1655, 419, 129,4327,3444,3312,1714, # 2576
-1257,3078,4328,1518,1098, 865,1310,1019,1885,1512,1734, 469,2444, 148, 773, 436, # 2592
-1815,1868,1128,1055,4329,1245,2756,3445,2154,1934,1039,4643, 579,1238, 932,2320, # 2608
- 353, 205, 801, 115,2428, 944,2321,1881, 399,2565,1211, 678, 766,3944, 335,2101, # 2624
-1459,1781,1402,3945,2737,2131,1010, 844, 981,1326,1013, 550,1816,1545,2620,1335, # 2640
-1008, 371,2881, 936,1419,1613,3529,1456,1395,2273,1834,2604,1317,2738,2503, 416, # 2656
-1643,4330, 806,1126, 229, 591,3946,1314,1981,1576,1837,1666, 347,1790, 977,3313, # 2672
- 764,2861,1853, 688,2429,1920,1462,  77, 595, 415,2002,3034, 798,1192,4115,6144, # 2688
-2978,4331,3035,2695,2582,2072,2566, 430,2430,1727, 842,1396,3947,3702, 613, 377, # 2704
- 278, 236,1417,3388,3314,3174, 757,1869, 107,3530,6145,1194, 623,2262, 207,1253, # 2720
-2167,3446,3948, 492,1117,1935, 536,1838,2757,1246,4332, 696,2095,2406,1393,1572, # 2736
-3175,1782, 583, 190, 253,1390,2230, 830,3126,3389, 934,3245,1703,1749,2979,1870, # 2752
-2545,1656,2204, 869,2346,4116,3176,1817, 496,1764,4644, 942,1504, 404,1903,1122, # 2768
-1580,3606,2945,1022, 515, 372,1735, 955,2431,3036,6146,2797,1110,2302,2798, 617, # 2784
-6147, 441, 762,1771,3447,3607,3608,1904, 840,3037,  86, 939,1385, 572,1370,2445, # 2800
-1336, 114,3703, 898, 294, 203,3315, 703,1583,2274, 429, 961,4333,1854,1951,3390, # 2816
-2373,3704,4334,1318,1381, 966,1911,2322,1006,1155, 309, 989, 458,2718,1795,1372, # 2832
-1203, 252,1689,1363,3177, 517,1936, 168,1490, 562, 193,3823,1042,4117,1835, 551, # 2848
- 470,4645, 395, 489,3448,1871,1465,2583,2641, 417,1493, 279,1295, 511,1236,1119, # 2864
-  72,1231,1982,1812,3004, 871,1564, 984,3449,1667,2696,2096,4646,2347,2833,1673, # 2880
-3609, 695,3246,2668, 807,1183,4647, 890, 388,2333,1801,1457,2911,1765,1477,1031, # 2896
-3316,3317,1278,3391,2799,2292,2526, 163,3450,4335,2669,1404,1802,6148,2323,2407, # 2912
-1584,1728,1494,1824,1269, 298, 909,3318,1034,1632, 375, 776,1683,2061, 291, 210, # 2928
-1123, 809,1249,1002,2642,3038, 206,1011,2132, 144, 975, 882,1565, 342, 667, 754, # 2944
-1442,2143,1299,2303,2062, 447, 626,2205,1221,2739,2912,1144,1214,2206,2584, 760, # 2960
-1715, 614, 950,1281,2670,2621, 810, 577,1287,2546,4648, 242,2168, 250,2643, 691, # 2976
- 123,2644, 647, 313,1029, 689,1357,2946,1650, 216, 771,1339,1306, 808,2063, 549, # 2992
- 913,1371,2913,2914,6149,1466,1092,1174,1196,1311,2605,2396,1783,1796,3079, 406, # 3008
-2671,2117,3949,4649, 487,1825,2220,6150,2915, 448,2348,1073,6151,2397,1707, 130, # 3024
- 900,1598, 329, 176,1959,2527,1620,6152,2275,4336,3319,1983,2191,3705,3610,2155, # 3040
-3706,1912,1513,1614,6153,1988, 646, 392,2304,1589,3320,3039,1826,1239,1352,1340, # 3056
-2916, 505,2567,1709,1437,2408,2547, 906,6154,2672, 384,1458,1594,1100,1329, 710, # 3072
- 423,3531,2064,2231,2622,1989,2673,1087,1882, 333, 841,3005,1296,2882,2379, 580, # 3088
-1937,1827,1293,2585, 601, 574, 249,1772,4118,2079,1120, 645, 901,1176,1690, 795, # 3104
-2207, 478,1434, 516,1190,1530, 761,2080, 930,1264, 355, 435,1552, 644,1791, 987, # 3120
- 220,1364,1163,1121,1538, 306,2169,1327,1222, 546,2645, 218, 241, 610,1704,3321, # 3136
-1984,1839,1966,2528, 451,6155,2586,3707,2568, 907,3178, 254,2947, 186,1845,4650, # 3152
- 745, 432,1757, 428,1633, 888,2246,2221,2489,3611,2118,1258,1265, 956,3127,1784, # 3168
-4337,2490, 319, 510, 119, 457,3612, 274,2035,2007,4651,1409,3128, 970,2758, 590, # 3184
-2800, 661,2247,4652,2008,3950,1420,1549,3080,3322,3951,1651,1375,2111, 485,2491, # 3200
-1429,1156,6156,2548,2183,1495, 831,1840,2529,2446, 501,1657, 307,1894,3247,1341, # 3216
- 666, 899,2156,1539,2549,1559, 886, 349,2208,3081,2305,1736,3824,2170,2759,1014, # 3232
-1913,1386, 542,1397,2948, 490, 368, 716, 362, 159, 282,2569,1129,1658,1288,1750, # 3248
-2674, 276, 649,2016, 751,1496, 658,1818,1284,1862,2209,2087,2512,3451, 622,2834, # 3264
- 376, 117,1060,2053,1208,1721,1101,1443, 247,1250,3179,1792,3952,2760,2398,3953, # 3280
-6157,2144,3708, 446,2432,1151,2570,3452,2447,2761,2835,1210,2448,3082, 424,2222, # 3296
-1251,2449,2119,2836, 504,1581,4338, 602, 817, 857,3825,2349,2306, 357,3826,1470, # 3312
-1883,2883, 255, 958, 929,2917,3248, 302,4653,1050,1271,1751,2307,1952,1430,2697, # 3328
-2719,2359, 354,3180, 777, 158,2036,4339,1659,4340,4654,2308,2949,2248,1146,2232, # 3344
-3532,2720,1696,2623,3827,6158,3129,1550,2698,1485,1297,1428, 637, 931,2721,2145, # 3360
- 914,2550,2587,  81,2450, 612, 827,2646,1242,4655,1118,2884, 472,1855,3181,3533, # 3376
-3534, 569,1353,2699,1244,1758,2588,4119,2009,2762,2171,3709,1312,1531,6159,1152, # 3392
-1938, 134,1830, 471,3710,2276,1112,1535,3323,3453,3535, 982,1337,2950, 488, 826, # 3408
- 674,1058,1628,4120,2017, 522,2399, 211, 568,1367,3454, 350, 293,1872,1139,3249, # 3424
-1399,1946,3006,1300,2360,3324, 588, 736,6160,2606, 744, 669,3536,3828,6161,1358, # 3440
- 199, 723, 848, 933, 851,1939,1505,1514,1338,1618,1831,4656,1634,3613, 443,2740, # 3456
-3829, 717,1947, 491,1914,6162,2551,1542,4121,1025,6163,1099,1223, 198,3040,2722, # 3472
- 370, 410,1905,2589, 998,1248,3182,2380, 519,1449,4122,1710, 947, 928,1153,4341, # 3488
-2277, 344,2624,1511, 615, 105, 161,1212,1076,1960,3130,2054,1926,1175,1906,2473, # 3504
- 414,1873,2801,6164,2309, 315,1319,3325, 318,2018,2146,2157, 963, 631, 223,4342, # 3520
-4343,2675, 479,3711,1197,2625,3712,2676,2361,6165,4344,4123,6166,2451,3183,1886, # 3536
-2184,1674,1330,1711,1635,1506, 799, 219,3250,3083,3954,1677,3713,3326,2081,3614, # 3552
-1652,2073,4657,1147,3041,1752, 643,1961, 147,1974,3955,6167,1716,2037, 918,3007, # 3568
-1994, 120,1537, 118, 609,3184,4345, 740,3455,1219, 332,1615,3830,6168,1621,2980, # 3584
-1582, 783, 212, 553,2350,3714,1349,2433,2082,4124, 889,6169,2310,1275,1410, 973, # 3600
- 166,1320,3456,1797,1215,3185,2885,1846,2590,2763,4658, 629, 822,3008, 763, 940, # 3616
-1990,2862, 439,2409,1566,1240,1622, 926,1282,1907,2764, 654,2210,1607, 327,1130, # 3632
-3956,1678,1623,6170,2434,2192, 686, 608,3831,3715, 903,3957,3042,6171,2741,1522, # 3648
-1915,1105,1555,2552,1359, 323,3251,4346,3457, 738,1354,2553,2311,2334,1828,2003, # 3664
-3832,1753,2351,1227,6172,1887,4125,1478,6173,2410,1874,1712,1847, 520,1204,2607, # 3680
- 264,4659, 836,2677,2102, 600,4660,3833,2278,3084,6174,4347,3615,1342, 640, 532, # 3696
- 543,2608,1888,2400,2591,1009,4348,1497, 341,1737,3616,2723,1394, 529,3252,1321, # 3712
- 983,4661,1515,2120, 971,2592, 924, 287,1662,3186,4349,2700,4350,1519, 908,1948, # 3728
-2452, 156, 796,1629,1486,2223,2055, 694,4126,1259,1036,3392,1213,2249,2742,1889, # 3744
-1230,3958,1015, 910, 408, 559,3617,4662, 746, 725, 935,4663,3959,3009,1289, 563, # 3760
- 867,4664,3960,1567,2981,2038,2626, 988,2263,2381,4351, 143,2374, 704,1895,6175, # 3776
-1188,3716,2088, 673,3085,2362,4352, 484,1608,1921,2765,2918, 215, 904,3618,3537, # 3792
- 894, 509, 976,3043,2701,3961,4353,2837,2982, 498,6176,6177,1102,3538,1332,3393, # 3808
-1487,1636,1637, 233, 245,3962, 383, 650, 995,3044, 460,1520,1206,2352, 749,3327, # 3824
- 530, 700, 389,1438,1560,1773,3963,2264, 719,2951,2724,3834, 870,1832,1644,1000, # 3840
- 839,2474,3717, 197,1630,3394, 365,2886,3964,1285,2133, 734, 922, 818,1106, 732, # 3856
- 480,2083,1774,3458, 923,2279,1350, 221,3086,  85,2233,2234,3835,1585,3010,2147, # 3872
-1387,1705,2382,1619,2475, 133, 239,2802,1991,1016,2084,2383, 411,2838,1113, 651, # 3888
-1985,1160,3328, 990,1863,3087,1048,1276,2647, 265,2627,1599,3253,2056, 150, 638, # 3904
-2019, 656, 853, 326,1479, 680,1439,4354,1001,1759, 413,3459,3395,2492,1431, 459, # 3920
-4355,1125,3329,2265,1953,1450,2065,2863, 849, 351,2678,3131,3254,3255,1104,1577, # 3936
- 227,1351,1645,2453,2193,1421,2887, 812,2121, 634,  95,2435, 201,2312,4665,1646, # 3952
-1671,2743,1601,2554,2702,2648,2280,1315,1366,2089,3132,1573,3718,3965,1729,1189, # 3968
- 328,2679,1077,1940,1136, 558,1283, 964,1195, 621,2074,1199,1743,3460,3619,1896, # 3984
-1916,1890,3836,2952,1154,2112,1064, 862, 378,3011,2066,2113,2803,1568,2839,6178, # 4000
-3088,2919,1941,1660,2004,1992,2194, 142, 707,1590,1708,1624,1922,1023,1836,1233, # 4016
-1004,2313, 789, 741,3620,6179,1609,2411,1200,4127,3719,3720,4666,2057,3721, 593, # 4032
-2840, 367,2920,1878,6180,3461,1521, 628,1168, 692,2211,2649, 300, 720,2067,2571, # 4048
-2953,3396, 959,2504,3966,3539,3462,1977, 701,6181, 954,1043, 800, 681, 183,3722, # 4064
-1803,1730,3540,4128,2103, 815,2314, 174, 467, 230,2454,1093,2134, 755,3541,3397, # 4080
-1141,1162,6182,1738,2039, 270,3256,2513,1005,1647,2185,3837, 858,1679,1897,1719, # 4096
-2954,2324,1806, 402, 670, 167,4129,1498,2158,2104, 750,6183, 915, 189,1680,1551, # 4112
- 455,4356,1501,2455, 405,1095,2955, 338,1586,1266,1819, 570, 641,1324, 237,1556, # 4128
-2650,1388,3723,6184,1368,2384,1343,1978,3089,2436, 879,3724, 792,1191, 758,3012, # 4144
-1411,2135,1322,4357, 240,4667,1848,3725,1574,6185, 420,3045,1546,1391, 714,4358, # 4160
-1967, 941,1864, 863, 664, 426, 560,1731,2680,1785,2864,1949,2363, 403,3330,1415, # 4176
-1279,2136,1697,2335, 204, 721,2097,3838,  90,6186,2085,2505, 191,3967, 124,2148, # 4192
-1376,1798,1178,1107,1898,1405, 860,4359,1243,1272,2375,2983,1558,2456,1638, 113, # 4208
-3621, 578,1923,2609, 880, 386,4130, 784,2186,2266,1422,2956,2172,1722, 497, 263, # 4224
-2514,1267,2412,2610, 177,2703,3542, 774,1927,1344, 616,1432,1595,1018, 172,4360, # 4240
-2325, 911,4361, 438,1468,3622, 794,3968,2024,2173,1681,1829,2957, 945, 895,3090, # 4256
- 575,2212,2476, 475,2401,2681, 785,2744,1745,2293,2555,1975,3133,2865, 394,4668, # 4272
-3839, 635,4131, 639, 202,1507,2195,2766,1345,1435,2572,3726,1908,1184,1181,2457, # 4288
-3727,3134,4362, 843,2611, 437, 916,4669, 234, 769,1884,3046,3047,3623, 833,6187, # 4304
-1639,2250,2402,1355,1185,2010,2047, 999, 525,1732,1290,1488,2612, 948,1578,3728, # 4320
-2413,2477,1216,2725,2159, 334,3840,1328,3624,2921,1525,4132, 564,1056, 891,4363, # 4336
-1444,1698,2385,2251,3729,1365,2281,2235,1717,6188, 864,3841,2515, 444, 527,2767, # 4352
-2922,3625, 544, 461,6189, 566, 209,2437,3398,2098,1065,2068,3331,3626,3257,2137, # 4368  #last 512
-)
-
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/jpcntx.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/jpcntx.py
deleted file mode 100644
index 20044e4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/jpcntx.py
+++ /dev/null
@@ -1,233 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-
-# This is hiragana 2-char sequence table, the number in each cell represents its frequency category
-jp2CharContext = (
-(0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1),
-(2,4,0,4,0,3,0,4,0,3,4,4,4,2,4,3,3,4,3,2,3,3,4,2,3,3,3,2,4,1,4,3,3,1,5,4,3,4,3,4,3,5,3,0,3,5,4,2,0,3,1,0,3,3,0,3,3,0,1,1,0,4,3,0,3,3,0,4,0,2,0,3,5,5,5,5,4,0,4,1,0,3,4),
-(0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2),
-(0,4,0,5,0,5,0,4,0,4,5,4,4,3,5,3,5,1,5,3,4,3,4,4,3,4,3,3,4,3,5,4,4,3,5,5,3,5,5,5,3,5,5,3,4,5,5,3,1,3,2,0,3,4,0,4,2,0,4,2,1,5,3,2,3,5,0,4,0,2,0,5,4,4,5,4,5,0,4,0,0,4,4),
-(0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0),
-(0,3,0,4,0,3,0,3,0,4,5,4,3,3,3,3,4,3,5,4,4,3,5,4,4,3,4,3,4,4,4,4,5,3,4,4,3,4,5,5,4,5,5,1,4,5,4,3,0,3,3,1,3,3,0,4,4,0,3,3,1,5,3,3,3,5,0,4,0,3,0,4,4,3,4,3,3,0,4,1,1,3,4),
-(0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0),
-(0,4,0,3,0,3,0,4,0,3,4,4,3,2,2,1,2,1,3,1,3,3,3,3,3,4,3,1,3,3,5,3,3,0,4,3,0,5,4,3,3,5,4,4,3,4,4,5,0,1,2,0,1,2,0,2,2,0,1,0,0,5,2,2,1,4,0,3,0,1,0,4,4,3,5,4,3,0,2,1,0,4,3),
-(0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0),
-(0,3,0,5,0,4,0,2,1,4,4,2,4,1,4,2,4,2,4,3,3,3,4,3,3,3,3,1,4,2,3,3,3,1,4,4,1,1,1,4,3,3,2,0,2,4,3,2,0,3,3,0,3,1,1,0,0,0,3,3,0,4,2,2,3,4,0,4,0,3,0,4,4,5,3,4,4,0,3,0,0,1,4),
-(1,4,0,4,0,4,0,4,0,3,5,4,4,3,4,3,5,4,3,3,4,3,5,4,4,4,4,3,4,2,4,3,3,1,5,4,3,2,4,5,4,5,5,4,4,5,4,4,0,3,2,2,3,3,0,4,3,1,3,2,1,4,3,3,4,5,0,3,0,2,0,4,5,5,4,5,4,0,4,0,0,5,4),
-(0,5,0,5,0,4,0,3,0,4,4,3,4,3,3,3,4,0,4,4,4,3,4,3,4,3,3,1,4,2,4,3,4,0,5,4,1,4,5,4,4,5,3,2,4,3,4,3,2,4,1,3,3,3,2,3,2,0,4,3,3,4,3,3,3,4,0,4,0,3,0,4,5,4,4,4,3,0,4,1,0,1,3),
-(0,3,1,4,0,3,0,2,0,3,4,4,3,1,4,2,3,3,4,3,4,3,4,3,4,4,3,2,3,1,5,4,4,1,4,4,3,5,4,4,3,5,5,4,3,4,4,3,1,2,3,1,2,2,0,3,2,0,3,1,0,5,3,3,3,4,3,3,3,3,4,4,4,4,5,4,2,0,3,3,2,4,3),
-(0,2,0,3,0,1,0,1,0,0,3,2,0,0,2,0,1,0,2,1,3,3,3,1,2,3,1,0,1,0,4,2,1,1,3,3,0,4,3,3,1,4,3,3,0,3,3,2,0,0,0,0,1,0,0,2,0,0,0,0,0,4,1,0,2,3,2,2,2,1,3,3,3,4,4,3,2,0,3,1,0,3,3),
-(0,4,0,4,0,3,0,3,0,4,4,4,3,3,3,3,3,3,4,3,4,2,4,3,4,3,3,2,4,3,4,5,4,1,4,5,3,5,4,5,3,5,4,0,3,5,5,3,1,3,3,2,2,3,0,3,4,1,3,3,2,4,3,3,3,4,0,4,0,3,0,4,5,4,4,5,3,0,4,1,0,3,4),
-(0,2,0,3,0,3,0,0,0,2,2,2,1,0,1,0,0,0,3,0,3,0,3,0,1,3,1,0,3,1,3,3,3,1,3,3,3,0,1,3,1,3,4,0,0,3,1,1,0,3,2,0,0,0,0,1,3,0,1,0,0,3,3,2,0,3,0,0,0,0,0,3,4,3,4,3,3,0,3,0,0,2,3),
-(2,3,0,3,0,2,0,1,0,3,3,4,3,1,3,1,1,1,3,1,4,3,4,3,3,3,0,0,3,1,5,4,3,1,4,3,2,5,5,4,4,4,4,3,3,4,4,4,0,2,1,1,3,2,0,1,2,0,0,1,0,4,1,3,3,3,0,3,0,1,0,4,4,4,5,5,3,0,2,0,0,4,4),
-(0,2,0,1,0,3,1,3,0,2,3,3,3,0,3,1,0,0,3,0,3,2,3,1,3,2,1,1,0,0,4,2,1,0,2,3,1,4,3,2,0,4,4,3,1,3,1,3,0,1,0,0,1,0,0,0,1,0,0,0,0,4,1,1,1,2,0,3,0,0,0,3,4,2,4,3,2,0,1,0,0,3,3),
-(0,1,0,4,0,5,0,4,0,2,4,4,2,3,3,2,3,3,5,3,3,3,4,3,4,2,3,0,4,3,3,3,4,1,4,3,2,1,5,5,3,4,5,1,3,5,4,2,0,3,3,0,1,3,0,4,2,0,1,3,1,4,3,3,3,3,0,3,0,1,0,3,4,4,4,5,5,0,3,0,1,4,5),
-(0,2,0,3,0,3,0,0,0,2,3,1,3,0,4,0,1,1,3,0,3,4,3,2,3,1,0,3,3,2,3,1,3,0,2,3,0,2,1,4,1,2,2,0,0,3,3,0,0,2,0,0,0,1,0,0,0,0,2,2,0,3,2,1,3,3,0,2,0,2,0,0,3,3,1,2,4,0,3,0,2,2,3),
-(2,4,0,5,0,4,0,4,0,2,4,4,4,3,4,3,3,3,1,2,4,3,4,3,4,4,5,0,3,3,3,3,2,0,4,3,1,4,3,4,1,4,4,3,3,4,4,3,1,2,3,0,4,2,0,4,1,0,3,3,0,4,3,3,3,4,0,4,0,2,0,3,5,3,4,5,2,0,3,0,0,4,5),
-(0,3,0,4,0,1,0,1,0,1,3,2,2,1,3,0,3,0,2,0,2,0,3,0,2,0,0,0,1,0,1,1,0,0,3,1,0,0,0,4,0,3,1,0,2,1,3,0,0,0,0,0,0,3,0,0,0,0,0,0,0,4,2,2,3,1,0,3,0,0,0,1,4,4,4,3,0,0,4,0,0,1,4),
-(1,4,1,5,0,3,0,3,0,4,5,4,4,3,5,3,3,4,4,3,4,1,3,3,3,3,2,1,4,1,5,4,3,1,4,4,3,5,4,4,3,5,4,3,3,4,4,4,0,3,3,1,2,3,0,3,1,0,3,3,0,5,4,4,4,4,4,4,3,3,5,4,4,3,3,5,4,0,3,2,0,4,4),
-(0,2,0,3,0,1,0,0,0,1,3,3,3,2,4,1,3,0,3,1,3,0,2,2,1,1,0,0,2,0,4,3,1,0,4,3,0,4,4,4,1,4,3,1,1,3,3,1,0,2,0,0,1,3,0,0,0,0,2,0,0,4,3,2,4,3,5,4,3,3,3,4,3,3,4,3,3,0,2,1,0,3,3),
-(0,2,0,4,0,3,0,2,0,2,5,5,3,4,4,4,4,1,4,3,3,0,4,3,4,3,1,3,3,2,4,3,0,3,4,3,0,3,4,4,2,4,4,0,4,5,3,3,2,2,1,1,1,2,0,1,5,0,3,3,2,4,3,3,3,4,0,3,0,2,0,4,4,3,5,5,0,0,3,0,2,3,3),
-(0,3,0,4,0,3,0,1,0,3,4,3,3,1,3,3,3,0,3,1,3,0,4,3,3,1,1,0,3,0,3,3,0,0,4,4,0,1,5,4,3,3,5,0,3,3,4,3,0,2,0,1,1,1,0,1,3,0,1,2,1,3,3,2,3,3,0,3,0,1,0,1,3,3,4,4,1,0,1,2,2,1,3),
-(0,1,0,4,0,4,0,3,0,1,3,3,3,2,3,1,1,0,3,0,3,3,4,3,2,4,2,0,1,0,4,3,2,0,4,3,0,5,3,3,2,4,4,4,3,3,3,4,0,1,3,0,0,1,0,0,1,0,0,0,0,4,2,3,3,3,0,3,0,0,0,4,4,4,5,3,2,0,3,3,0,3,5),
-(0,2,0,3,0,0,0,3,0,1,3,0,2,0,0,0,1,0,3,1,1,3,3,0,0,3,0,0,3,0,2,3,1,0,3,1,0,3,3,2,0,4,2,2,0,2,0,0,0,4,0,0,0,0,0,0,0,0,0,0,0,2,1,2,0,1,0,1,0,0,0,1,3,1,2,0,0,0,1,0,0,1,4),
-(0,3,0,3,0,5,0,1,0,2,4,3,1,3,3,2,1,1,5,2,1,0,5,1,2,0,0,0,3,3,2,2,3,2,4,3,0,0,3,3,1,3,3,0,2,5,3,4,0,3,3,0,1,2,0,2,2,0,3,2,0,2,2,3,3,3,0,2,0,1,0,3,4,4,2,5,4,0,3,0,0,3,5),
-(0,3,0,3,0,3,0,1,0,3,3,3,3,0,3,0,2,0,2,1,1,0,2,0,1,0,0,0,2,1,0,0,1,0,3,2,0,0,3,3,1,2,3,1,0,3,3,0,0,1,0,0,0,0,0,2,0,0,0,0,0,2,3,1,2,3,0,3,0,1,0,3,2,1,0,4,3,0,1,1,0,3,3),
-(0,4,0,5,0,3,0,3,0,4,5,5,4,3,5,3,4,3,5,3,3,2,5,3,4,4,4,3,4,3,4,5,5,3,4,4,3,4,4,5,4,4,4,3,4,5,5,4,2,3,4,2,3,4,0,3,3,1,4,3,2,4,3,3,5,5,0,3,0,3,0,5,5,5,5,4,4,0,4,0,1,4,4),
-(0,4,0,4,0,3,0,3,0,3,5,4,4,2,3,2,5,1,3,2,5,1,4,2,3,2,3,3,4,3,3,3,3,2,5,4,1,3,3,5,3,4,4,0,4,4,3,1,1,3,1,0,2,3,0,2,3,0,3,0,0,4,3,1,3,4,0,3,0,2,0,4,4,4,3,4,5,0,4,0,0,3,4),
-(0,3,0,3,0,3,1,2,0,3,4,4,3,3,3,0,2,2,4,3,3,1,3,3,3,1,1,0,3,1,4,3,2,3,4,4,2,4,4,4,3,4,4,3,2,4,4,3,1,3,3,1,3,3,0,4,1,0,2,2,1,4,3,2,3,3,5,4,3,3,5,4,4,3,3,0,4,0,3,2,2,4,4),
-(0,2,0,1,0,0,0,0,0,1,2,1,3,0,0,0,0,0,2,0,1,2,1,0,0,1,0,0,0,0,3,0,0,1,0,1,1,3,1,0,0,0,1,1,0,1,1,0,0,0,0,0,2,0,0,0,0,0,0,0,0,1,1,2,2,0,3,4,0,0,0,1,1,0,0,1,0,0,0,0,0,1,1),
-(0,1,0,0,0,1,0,0,0,0,4,0,4,1,4,0,3,0,4,0,3,0,4,0,3,0,3,0,4,1,5,1,4,0,0,3,0,5,0,5,2,0,1,0,0,0,2,1,4,0,1,3,0,0,3,0,0,3,1,1,4,1,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0),
-(1,4,0,5,0,3,0,2,0,3,5,4,4,3,4,3,5,3,4,3,3,0,4,3,3,3,3,3,3,2,4,4,3,1,3,4,4,5,4,4,3,4,4,1,3,5,4,3,3,3,1,2,2,3,3,1,3,1,3,3,3,5,3,3,4,5,0,3,0,3,0,3,4,3,4,4,3,0,3,0,2,4,3),
-(0,1,0,4,0,0,0,0,0,1,4,0,4,1,4,2,4,0,3,0,1,0,1,0,0,0,0,0,2,0,3,1,1,1,0,3,0,0,0,1,2,1,0,0,1,1,1,1,0,1,0,0,0,1,0,0,3,0,0,0,0,3,2,0,2,2,0,1,0,0,0,2,3,2,3,3,0,0,0,0,2,1,0),
-(0,5,1,5,0,3,0,3,0,5,4,4,5,1,5,3,3,0,4,3,4,3,5,3,4,3,3,2,4,3,4,3,3,0,3,3,1,4,4,3,4,4,4,3,4,5,5,3,2,3,1,1,3,3,1,3,1,1,3,3,2,4,5,3,3,5,0,4,0,3,0,4,4,3,5,3,3,0,3,4,0,4,3),
-(0,5,0,5,0,3,0,2,0,4,4,3,5,2,4,3,3,3,4,4,4,3,5,3,5,3,3,1,4,0,4,3,3,0,3,3,0,4,4,4,4,5,4,3,3,5,5,3,2,3,1,2,3,2,0,1,0,0,3,2,2,4,4,3,1,5,0,4,0,3,0,4,3,1,3,2,1,0,3,3,0,3,3),
-(0,4,0,5,0,5,0,4,0,4,5,5,5,3,4,3,3,2,5,4,4,3,5,3,5,3,4,0,4,3,4,4,3,2,4,4,3,4,5,4,4,5,5,0,3,5,5,4,1,3,3,2,3,3,1,3,1,0,4,3,1,4,4,3,4,5,0,4,0,2,0,4,3,4,4,3,3,0,4,0,0,5,5),
-(0,4,0,4,0,5,0,1,1,3,3,4,4,3,4,1,3,0,5,1,3,0,3,1,3,1,1,0,3,0,3,3,4,0,4,3,0,4,4,4,3,4,4,0,3,5,4,1,0,3,0,0,2,3,0,3,1,0,3,1,0,3,2,1,3,5,0,3,0,1,0,3,2,3,3,4,4,0,2,2,0,4,4),
-(2,4,0,5,0,4,0,3,0,4,5,5,4,3,5,3,5,3,5,3,5,2,5,3,4,3,3,4,3,4,5,3,2,1,5,4,3,2,3,4,5,3,4,1,2,5,4,3,0,3,3,0,3,2,0,2,3,0,4,1,0,3,4,3,3,5,0,3,0,1,0,4,5,5,5,4,3,0,4,2,0,3,5),
-(0,5,0,4,0,4,0,2,0,5,4,3,4,3,4,3,3,3,4,3,4,2,5,3,5,3,4,1,4,3,4,4,4,0,3,5,0,4,4,4,4,5,3,1,3,4,5,3,3,3,3,3,3,3,0,2,2,0,3,3,2,4,3,3,3,5,3,4,1,3,3,5,3,2,0,0,0,0,4,3,1,3,3),
-(0,1,0,3,0,3,0,1,0,1,3,3,3,2,3,3,3,0,3,0,0,0,3,1,3,0,0,0,2,2,2,3,0,0,3,2,0,1,2,4,1,3,3,0,0,3,3,3,0,1,0,0,2,1,0,0,3,0,3,1,0,3,0,0,1,3,0,2,0,1,0,3,3,1,3,3,0,0,1,1,0,3,3),
-(0,2,0,3,0,2,1,4,0,2,2,3,1,1,3,1,1,0,2,0,3,1,2,3,1,3,0,0,1,0,4,3,2,3,3,3,1,4,2,3,3,3,3,1,0,3,1,4,0,1,1,0,1,2,0,1,1,0,1,1,0,3,1,3,2,2,0,1,0,0,0,2,3,3,3,1,0,0,0,0,0,2,3),
-(0,5,0,4,0,5,0,2,0,4,5,5,3,3,4,3,3,1,5,4,4,2,4,4,4,3,4,2,4,3,5,5,4,3,3,4,3,3,5,5,4,5,5,1,3,4,5,3,1,4,3,1,3,3,0,3,3,1,4,3,1,4,5,3,3,5,0,4,0,3,0,5,3,3,1,4,3,0,4,0,1,5,3),
-(0,5,0,5,0,4,0,2,0,4,4,3,4,3,3,3,3,3,5,4,4,4,4,4,4,5,3,3,5,2,4,4,4,3,4,4,3,3,4,4,5,5,3,3,4,3,4,3,3,4,3,3,3,3,1,2,2,1,4,3,3,5,4,4,3,4,0,4,0,3,0,4,4,4,4,4,1,0,4,2,0,2,4),
-(0,4,0,4,0,3,0,1,0,3,5,2,3,0,3,0,2,1,4,2,3,3,4,1,4,3,3,2,4,1,3,3,3,0,3,3,0,0,3,3,3,5,3,3,3,3,3,2,0,2,0,0,2,0,0,2,0,0,1,0,0,3,1,2,2,3,0,3,0,2,0,4,4,3,3,4,1,0,3,0,0,2,4),
-(0,0,0,4,0,0,0,0,0,0,1,0,1,0,2,0,0,0,0,0,1,0,2,0,1,0,0,0,0,0,3,1,3,0,3,2,0,0,0,1,0,3,2,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,3,4,0,2,0,0,0,0,0,0,2),
-(0,2,1,3,0,2,0,2,0,3,3,3,3,1,3,1,3,3,3,3,3,3,4,2,2,1,2,1,4,0,4,3,1,3,3,3,2,4,3,5,4,3,3,3,3,3,3,3,0,1,3,0,2,0,0,1,0,0,1,0,0,4,2,0,2,3,0,3,3,0,3,3,4,2,3,1,4,0,1,2,0,2,3),
-(0,3,0,3,0,1,0,3,0,2,3,3,3,0,3,1,2,0,3,3,2,3,3,2,3,2,3,1,3,0,4,3,2,0,3,3,1,4,3,3,2,3,4,3,1,3,3,1,1,0,1,1,0,1,0,1,0,1,0,0,0,4,1,1,0,3,0,3,1,0,2,3,3,3,3,3,1,0,0,2,0,3,3),
-(0,0,0,0,0,0,0,0,0,0,3,0,2,0,3,0,0,0,0,0,0,0,3,0,0,0,0,0,0,0,3,0,3,0,3,1,0,1,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,3,0,2,0,2,3,0,0,0,0,0,0,0,0,3),
-(0,2,0,3,1,3,0,3,0,2,3,3,3,1,3,1,3,1,3,1,3,3,3,1,3,0,2,3,1,1,4,3,3,2,3,3,1,2,2,4,1,3,3,0,1,4,2,3,0,1,3,0,3,0,0,1,3,0,2,0,0,3,3,2,1,3,0,3,0,2,0,3,4,4,4,3,1,0,3,0,0,3,3),
-(0,2,0,1,0,2,0,0,0,1,3,2,2,1,3,0,1,1,3,0,3,2,3,1,2,0,2,0,1,1,3,3,3,0,3,3,1,1,2,3,2,3,3,1,2,3,2,0,0,1,0,0,0,0,0,0,3,0,1,0,0,2,1,2,1,3,0,3,0,0,0,3,4,4,4,3,2,0,2,0,0,2,4),
-(0,0,0,1,0,1,0,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,1,1,1,0,0,0,0,0,0,0,0,0,2,2,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,1,3,1,0,0,0,0,0,0,0,3),
-(0,3,0,3,0,2,0,3,0,3,3,3,2,3,2,2,2,0,3,1,3,3,3,2,3,3,0,0,3,0,3,2,2,0,2,3,1,4,3,4,3,3,2,3,1,5,4,4,0,3,1,2,1,3,0,3,1,1,2,0,2,3,1,3,1,3,0,3,0,1,0,3,3,4,4,2,1,0,2,1,0,2,4),
-(0,1,0,3,0,1,0,2,0,1,4,2,5,1,4,0,2,0,2,1,3,1,4,0,2,1,0,0,2,1,4,1,1,0,3,3,0,5,1,3,2,3,3,1,0,3,2,3,0,1,0,0,0,0,0,0,1,0,0,0,0,4,0,1,0,3,0,2,0,1,0,3,3,3,4,3,3,0,0,0,0,2,3),
-(0,0,0,1,0,0,0,0,0,0,2,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,3,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,1,0,0,1,0,0,0,0,0,3),
-(0,1,0,3,0,4,0,3,0,2,4,3,1,0,3,2,2,1,3,1,2,2,3,1,1,1,2,1,3,0,1,2,0,1,3,2,1,3,0,5,5,1,0,0,1,3,2,1,0,3,0,0,1,0,0,0,0,0,3,4,0,1,1,1,3,2,0,2,0,1,0,2,3,3,1,2,3,0,1,0,1,0,4),
-(0,0,0,1,0,3,0,3,0,2,2,1,0,0,4,0,3,0,3,1,3,0,3,0,3,0,1,0,3,0,3,1,3,0,3,3,0,0,1,2,1,1,1,0,1,2,0,0,0,1,0,0,1,0,0,0,0,0,0,0,0,2,2,1,2,0,0,2,0,0,0,0,2,3,3,3,3,0,0,0,0,1,4),
-(0,0,0,3,0,3,0,0,0,0,3,1,1,0,3,0,1,0,2,0,1,0,0,0,0,0,0,0,1,0,3,0,2,0,2,3,0,0,2,2,3,1,2,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,3,0,0,2,0,0,0,0,2,3),
-(2,4,0,5,0,5,0,4,0,3,4,3,3,3,4,3,3,3,4,3,4,4,5,4,5,5,5,2,3,0,5,5,4,1,5,4,3,1,5,4,3,4,4,3,3,4,3,3,0,3,2,0,2,3,0,3,0,0,3,3,0,5,3,2,3,3,0,3,0,3,0,3,4,5,4,5,3,0,4,3,0,3,4),
-(0,3,0,3,0,3,0,3,0,3,3,4,3,2,3,2,3,0,4,3,3,3,3,3,3,3,3,0,3,2,4,3,3,1,3,4,3,4,4,4,3,4,4,3,2,4,4,1,0,2,0,0,1,1,0,2,0,0,3,1,0,5,3,2,1,3,0,3,0,1,2,4,3,2,4,3,3,0,3,2,0,4,4),
-(0,3,0,3,0,1,0,0,0,1,4,3,3,2,3,1,3,1,4,2,3,2,4,2,3,4,3,0,2,2,3,3,3,0,3,3,3,0,3,4,1,3,3,0,3,4,3,3,0,1,1,0,1,0,0,0,4,0,3,0,0,3,1,2,1,3,0,4,0,1,0,4,3,3,4,3,3,0,2,0,0,3,3),
-(0,3,0,4,0,1,0,3,0,3,4,3,3,0,3,3,3,1,3,1,3,3,4,3,3,3,0,0,3,1,5,3,3,1,3,3,2,5,4,3,3,4,5,3,2,5,3,4,0,1,0,0,0,0,0,2,0,0,1,1,0,4,2,2,1,3,0,3,0,2,0,4,4,3,5,3,2,0,1,1,0,3,4),
-(0,5,0,4,0,5,0,2,0,4,4,3,3,2,3,3,3,1,4,3,4,1,5,3,4,3,4,0,4,2,4,3,4,1,5,4,0,4,4,4,4,5,4,1,3,5,4,2,1,4,1,1,3,2,0,3,1,0,3,2,1,4,3,3,3,4,0,4,0,3,0,4,4,4,3,3,3,0,4,2,0,3,4),
-(1,4,0,4,0,3,0,1,0,3,3,3,1,1,3,3,2,2,3,3,1,0,3,2,2,1,2,0,3,1,2,1,2,0,3,2,0,2,2,3,3,4,3,0,3,3,1,2,0,1,1,3,1,2,0,0,3,0,1,1,0,3,2,2,3,3,0,3,0,0,0,2,3,3,4,3,3,0,1,0,0,1,4),
-(0,4,0,4,0,4,0,0,0,3,4,4,3,1,4,2,3,2,3,3,3,1,4,3,4,0,3,0,4,2,3,3,2,2,5,4,2,1,3,4,3,4,3,1,3,3,4,2,0,2,1,0,3,3,0,0,2,0,3,1,0,4,4,3,4,3,0,4,0,1,0,2,4,4,4,4,4,0,3,2,0,3,3),
-(0,0,0,1,0,4,0,0,0,0,0,0,1,1,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,1,0,3,2,0,0,1,0,0,0,1,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,2),
-(0,2,0,3,0,4,0,4,0,1,3,3,3,0,4,0,2,1,2,1,1,1,2,0,3,1,1,0,1,0,3,1,0,0,3,3,2,0,1,1,0,0,0,0,0,1,0,2,0,2,2,0,3,1,0,0,1,0,1,1,0,1,2,0,3,0,0,0,0,1,0,0,3,3,4,3,1,0,1,0,3,0,2),
-(0,0,0,3,0,5,0,0,0,0,1,0,2,0,3,1,0,1,3,0,0,0,2,0,0,0,1,0,0,0,1,1,0,0,4,0,0,0,2,3,0,1,4,1,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,3,0,0,0,0,0,1,0,0,0,0,0,0,0,2,0,0,3,0,0,0,0,0,3),
-(0,2,0,5,0,5,0,1,0,2,4,3,3,2,5,1,3,2,3,3,3,0,4,1,2,0,3,0,4,0,2,2,1,1,5,3,0,0,1,4,2,3,2,0,3,3,3,2,0,2,4,1,1,2,0,1,1,0,3,1,0,1,3,1,2,3,0,2,0,0,0,1,3,5,4,4,4,0,3,0,0,1,3),
-(0,4,0,5,0,4,0,4,0,4,5,4,3,3,4,3,3,3,4,3,4,4,5,3,4,5,4,2,4,2,3,4,3,1,4,4,1,3,5,4,4,5,5,4,4,5,5,5,2,3,3,1,4,3,1,3,3,0,3,3,1,4,3,4,4,4,0,3,0,4,0,3,3,4,4,5,0,0,4,3,0,4,5),
-(0,4,0,4,0,3,0,3,0,3,4,4,4,3,3,2,4,3,4,3,4,3,5,3,4,3,2,1,4,2,4,4,3,1,3,4,2,4,5,5,3,4,5,4,1,5,4,3,0,3,2,2,3,2,1,3,1,0,3,3,3,5,3,3,3,5,4,4,2,3,3,4,3,3,3,2,1,0,3,2,1,4,3),
-(0,4,0,5,0,4,0,3,0,3,5,5,3,2,4,3,4,0,5,4,4,1,4,4,4,3,3,3,4,3,5,5,2,3,3,4,1,2,5,5,3,5,5,2,3,5,5,4,0,3,2,0,3,3,1,1,5,1,4,1,0,4,3,2,3,5,0,4,0,3,0,5,4,3,4,3,0,0,4,1,0,4,4),
-(1,3,0,4,0,2,0,2,0,2,5,5,3,3,3,3,3,0,4,2,3,4,4,4,3,4,0,0,3,4,5,4,3,3,3,3,2,5,5,4,5,5,5,4,3,5,5,5,1,3,1,0,1,0,0,3,2,0,4,2,0,5,2,3,2,4,1,3,0,3,0,4,5,4,5,4,3,0,4,2,0,5,4),
-(0,3,0,4,0,5,0,3,0,3,4,4,3,2,3,2,3,3,3,3,3,2,4,3,3,2,2,0,3,3,3,3,3,1,3,3,3,0,4,4,3,4,4,1,1,4,4,2,0,3,1,0,1,1,0,4,1,0,2,3,1,3,3,1,3,4,0,3,0,1,0,3,1,3,0,0,1,0,2,0,0,4,4),
-(0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0),
-(0,3,0,3,0,2,0,3,0,1,5,4,3,3,3,1,4,2,1,2,3,4,4,2,4,4,5,0,3,1,4,3,4,0,4,3,3,3,2,3,2,5,3,4,3,2,2,3,0,0,3,0,2,1,0,1,2,0,0,0,0,2,1,1,3,1,0,2,0,4,0,3,4,4,4,5,2,0,2,0,0,1,3),
-(0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,1,1,1,0,0,1,1,0,0,0,4,2,1,1,0,1,0,3,2,0,0,3,1,1,1,2,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,3,0,1,0,0,0,2,0,0,0,1,4,0,4,2,1,0,0,0,0,0,1),
-(0,0,0,0,0,0,0,0,0,1,0,1,0,0,0,0,1,0,0,0,0,0,0,1,0,1,0,0,0,0,3,1,0,0,0,2,0,2,1,0,0,1,2,1,0,1,1,0,0,3,0,0,0,0,0,0,0,0,0,0,0,1,3,1,0,0,0,0,0,1,0,0,2,1,0,0,0,0,0,0,0,0,2),
-(0,4,0,4,0,4,0,3,0,4,4,3,4,2,4,3,2,0,4,4,4,3,5,3,5,3,3,2,4,2,4,3,4,3,1,4,0,2,3,4,4,4,3,3,3,4,4,4,3,4,1,3,4,3,2,1,2,1,3,3,3,4,4,3,3,5,0,4,0,3,0,4,3,3,3,2,1,0,3,0,0,3,3),
-(0,4,0,3,0,3,0,3,0,3,5,5,3,3,3,3,4,3,4,3,3,3,4,4,4,3,3,3,3,4,3,5,3,3,1,3,2,4,5,5,5,5,4,3,4,5,5,3,2,2,3,3,3,3,2,3,3,1,2,3,2,4,3,3,3,4,0,4,0,2,0,4,3,2,2,1,2,0,3,0,0,4,1),
-)
-
-class JapaneseContextAnalysis(object):
-    NUM_OF_CATEGORY = 6
-    DONT_KNOW = -1
-    ENOUGH_REL_THRESHOLD = 100
-    MAX_REL_THRESHOLD = 1000
-    MINIMUM_DATA_THRESHOLD = 4
-
-    def __init__(self):
-        self._total_rel = None
-        self._rel_sample = None
-        self._need_to_skip_char_num = None
-        self._last_char_order = None
-        self._done = None
-        self.reset()
-
-    def reset(self):
-        self._total_rel = 0  # total sequence received
-        # category counters, each integer counts sequence in its category
-        self._rel_sample = [0] * self.NUM_OF_CATEGORY
-        # if last byte in current buffer is not the last byte of a character,
-        # we need to know how many bytes to skip in next buffer
-        self._need_to_skip_char_num = 0
-        self._last_char_order = -1  # The order of previous char
-        # If this flag is set to True, detection is done and conclusion has
-        # been made
-        self._done = False
-
-    def feed(self, byte_str, num_bytes):
-        if self._done:
-            return
-
-        # The buffer we got is byte oriented, and a character may span in more than one
-        # buffers. In case the last one or two byte in last buffer is not
-        # complete, we record how many byte needed to complete that character
-        # and skip these bytes here.  We can choose to record those bytes as
-        # well and analyse the character once it is complete, but since a
-        # character will not make much difference, by simply skipping
-        # this character will simply our logic and improve performance.
-        i = self._need_to_skip_char_num
-        while i < num_bytes:
-            order, char_len = self.get_order(byte_str[i:i + 2])
-            i += char_len
-            if i > num_bytes:
-                self._need_to_skip_char_num = i - num_bytes
-                self._last_char_order = -1
-            else:
-                if (order != -1) and (self._last_char_order != -1):
-                    self._total_rel += 1
-                    if self._total_rel > self.MAX_REL_THRESHOLD:
-                        self._done = True
-                        break
-                    self._rel_sample[jp2CharContext[self._last_char_order][order]] += 1
-                self._last_char_order = order
-
-    def got_enough_data(self):
-        return self._total_rel > self.ENOUGH_REL_THRESHOLD
-
-    def get_confidence(self):
-        # This is just one way to calculate confidence. It works well for me.
-        if self._total_rel > self.MINIMUM_DATA_THRESHOLD:
-            return (self._total_rel - self._rel_sample[0]) / self._total_rel
-        else:
-            return self.DONT_KNOW
-
-    def get_order(self, byte_str):
-        return -1, 1
-
-class SJISContextAnalysis(JapaneseContextAnalysis):
-    def __init__(self):
-        super(SJISContextAnalysis, self).__init__()
-        self._charset_name = "SHIFT_JIS"
-
-    @property
-    def charset_name(self):
-        return self._charset_name
-
-    def get_order(self, byte_str):
-        if not byte_str:
-            return -1, 1
-        # find out current char's byte length
-        first_char = byte_str[0]
-        if (0x81 <= first_char <= 0x9F) or (0xE0 <= first_char <= 0xFC):
-            char_len = 2
-            if (first_char == 0x87) or (0xFA <= first_char <= 0xFC):
-                self._charset_name = "CP932"
-        else:
-            char_len = 1
-
-        # return its order if it is hiragana
-        if len(byte_str) > 1:
-            second_char = byte_str[1]
-            if (first_char == 202) and (0x9F <= second_char <= 0xF1):
-                return second_char - 0x9F, char_len
-
-        return -1, char_len
-
-class EUCJPContextAnalysis(JapaneseContextAnalysis):
-    def get_order(self, byte_str):
-        if not byte_str:
-            return -1, 1
-        # find out current char's byte length
-        first_char = byte_str[0]
-        if (first_char == 0x8E) or (0xA1 <= first_char <= 0xFE):
-            char_len = 2
-        elif first_char == 0x8F:
-            char_len = 3
-        else:
-            char_len = 1
-
-        # return its order if it is hiragana
-        if len(byte_str) > 1:
-            second_char = byte_str[1]
-            if (first_char == 0xA4) and (0xA1 <= second_char <= 0xF3):
-                return second_char - 0xA1, char_len
-
-        return -1, char_len
-
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langbulgarianmodel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langbulgarianmodel.py
deleted file mode 100644
index 2aa4fb2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langbulgarianmodel.py
+++ /dev/null
@@ -1,228 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# 255: Control characters that usually does not exist in any text
-# 254: Carriage/Return
-# 253: symbol (punctuation) that does not belong to word
-# 252: 0 - 9
-
-# Character Mapping Table:
-# this table is modified base on win1251BulgarianCharToOrderMap, so
-# only number <64 is sure valid
-
-Latin5_BulgarianCharToOrderMap = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253, 77, 90, 99,100, 72,109,107,101, 79,185, 81,102, 76, 94, 82,  # 40
-110,186,108, 91, 74,119, 84, 96,111,187,115,253,253,253,253,253,  # 50
-253, 65, 69, 70, 66, 63, 68,112,103, 92,194,104, 95, 86, 87, 71,  # 60
-116,195, 85, 93, 97,113,196,197,198,199,200,253,253,253,253,253,  # 70
-194,195,196,197,198,199,200,201,202,203,204,205,206,207,208,209,  # 80
-210,211,212,213,214,215,216,217,218,219,220,221,222,223,224,225,  # 90
- 81,226,227,228,229,230,105,231,232,233,234,235,236, 45,237,238,  # a0
- 31, 32, 35, 43, 37, 44, 55, 47, 40, 59, 33, 46, 38, 36, 41, 30,  # b0
- 39, 28, 34, 51, 48, 49, 53, 50, 54, 57, 61,239, 67,240, 60, 56,  # c0
-  1, 18,  9, 20, 11,  3, 23, 15,  2, 26, 12, 10, 14,  6,  4, 13,  # d0
-  7,  8,  5, 19, 29, 25, 22, 21, 27, 24, 17, 75, 52,241, 42, 16,  # e0
- 62,242,243,244, 58,245, 98,246,247,248,249,250,251, 91,252,253,  # f0
-)
-
-win1251BulgarianCharToOrderMap = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253, 77, 90, 99,100, 72,109,107,101, 79,185, 81,102, 76, 94, 82,  # 40
-110,186,108, 91, 74,119, 84, 96,111,187,115,253,253,253,253,253,  # 50
-253, 65, 69, 70, 66, 63, 68,112,103, 92,194,104, 95, 86, 87, 71,  # 60
-116,195, 85, 93, 97,113,196,197,198,199,200,253,253,253,253,253,  # 70
-206,207,208,209,210,211,212,213,120,214,215,216,217,218,219,220,  # 80
-221, 78, 64, 83,121, 98,117,105,222,223,224,225,226,227,228,229,  # 90
- 88,230,231,232,233,122, 89,106,234,235,236,237,238, 45,239,240,  # a0
- 73, 80,118,114,241,242,243,244,245, 62, 58,246,247,248,249,250,  # b0
- 31, 32, 35, 43, 37, 44, 55, 47, 40, 59, 33, 46, 38, 36, 41, 30,  # c0
- 39, 28, 34, 51, 48, 49, 53, 50, 54, 57, 61,251, 67,252, 60, 56,  # d0
-  1, 18,  9, 20, 11,  3, 23, 15,  2, 26, 12, 10, 14,  6,  4, 13,  # e0
-  7,  8,  5, 19, 29, 25, 22, 21, 27, 24, 17, 75, 52,253, 42, 16,  # f0
-)
-
-# Model Table:
-# total sequences: 100%
-# first 512 sequences: 96.9392%
-# first 1024 sequences:3.0618%
-# rest  sequences:     0.2992%
-# negative sequences:  0.0020%
-BulgarianLangModel = (
-0,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,3,3,3,3,3,3,3,2,3,3,3,3,3,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,0,3,3,3,2,2,3,2,2,1,2,2,
-3,1,3,3,2,3,3,3,3,3,3,3,3,3,3,3,3,0,3,3,3,3,3,3,3,3,3,3,0,3,0,1,
-0,0,0,0,0,0,0,0,0,0,1,0,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,2,3,3,3,3,3,3,3,3,0,3,1,0,
-0,1,0,0,0,0,0,0,0,0,1,1,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-3,2,2,2,3,3,3,3,3,3,3,3,3,3,3,3,3,1,3,2,3,3,3,3,3,3,3,3,0,3,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,2,3,3,2,3,3,3,3,3,3,3,3,3,3,3,3,1,3,2,3,3,3,3,3,3,3,3,0,3,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,2,3,2,2,1,3,3,3,3,2,2,2,1,1,2,0,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,2,3,2,2,3,3,1,1,2,3,3,2,3,3,3,3,2,1,2,0,2,0,3,0,0,
-0,0,0,0,0,0,0,1,0,0,2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,1,3,3,3,3,3,2,3,2,3,3,3,3,3,2,3,3,1,3,0,3,0,2,0,0,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,3,1,3,3,2,3,3,3,1,3,3,2,3,2,2,2,0,0,2,0,2,0,2,0,0,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,3,3,0,3,3,3,2,2,3,3,3,1,2,2,3,2,1,1,2,0,2,0,0,0,0,
-1,0,0,0,0,0,0,0,0,0,2,0,0,1,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,2,3,3,1,2,3,2,2,2,3,3,3,3,3,2,2,3,1,2,0,2,1,2,0,0,
-0,0,0,0,0,0,0,0,0,0,3,0,0,1,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,1,3,3,3,3,3,2,3,3,3,2,3,3,2,3,2,2,2,3,1,2,0,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,3,3,3,3,1,1,1,2,2,1,3,1,3,2,2,3,0,0,1,0,1,0,1,0,0,
-0,0,0,1,0,0,0,0,1,0,2,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,2,2,3,2,2,3,1,2,1,1,1,2,3,1,3,1,2,2,0,1,1,1,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,1,3,2,2,3,3,1,2,3,1,1,3,3,3,3,1,2,2,1,1,1,0,2,0,2,0,1,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,1,2,2,3,3,3,2,2,1,1,2,0,2,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,0,1,2,1,3,3,2,3,3,3,3,3,2,3,2,1,0,3,1,2,1,2,1,2,3,2,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,1,1,2,3,3,3,3,3,3,3,3,3,3,3,3,0,0,3,1,3,3,2,3,3,2,2,2,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,3,3,3,3,0,3,3,3,3,3,2,1,1,2,1,3,3,0,3,1,1,1,1,3,2,0,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,2,2,2,3,3,3,3,3,3,3,3,3,3,3,1,1,3,1,3,3,2,3,2,2,2,3,0,2,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,2,3,3,2,2,3,2,1,1,1,1,1,3,1,3,1,1,0,0,0,1,0,0,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,2,3,2,0,3,2,0,3,0,2,0,0,2,1,3,1,0,0,1,0,0,0,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,2,1,1,1,1,2,1,1,2,1,1,1,2,2,1,2,1,1,1,0,1,1,0,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,2,1,3,1,1,2,1,3,2,1,1,0,1,2,3,2,1,1,1,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,3,3,3,3,2,2,1,0,1,0,0,1,0,0,0,2,1,0,3,0,0,1,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,2,3,2,3,3,1,3,2,1,1,1,2,1,1,2,1,3,0,1,0,0,0,1,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,1,2,2,3,3,2,3,2,2,2,3,1,2,2,1,1,2,1,1,2,2,0,1,1,0,1,0,2,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,2,1,3,1,0,2,2,1,3,2,1,0,0,2,0,2,0,1,0,0,0,0,0,0,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,3,1,2,0,2,3,1,2,3,2,0,1,3,1,2,1,1,1,0,0,1,0,0,2,2,2,3,
-2,2,2,2,1,2,1,1,2,2,1,1,2,0,1,1,1,0,0,1,1,0,0,1,1,0,0,0,1,1,0,1,
-3,3,3,3,3,2,1,2,2,1,2,0,2,0,1,0,1,2,1,2,1,1,0,0,0,1,0,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,1,
-3,3,2,3,3,1,1,3,1,0,3,2,1,0,0,0,1,2,0,2,0,1,0,0,0,1,0,1,2,1,2,2,
-1,1,1,1,1,1,1,2,2,2,1,1,1,1,1,1,1,0,1,2,1,1,1,0,0,0,0,0,1,1,0,0,
-3,1,0,1,0,2,3,2,2,2,3,2,2,2,2,2,1,0,2,1,2,1,1,1,0,1,2,1,2,2,2,1,
-1,1,2,2,2,2,1,2,1,1,0,1,2,1,2,2,2,1,1,1,0,1,1,1,1,2,0,1,0,0,0,0,
-2,3,2,3,3,0,0,2,1,0,2,1,0,0,0,0,2,3,0,2,0,0,0,0,0,1,0,0,2,0,1,2,
-2,1,2,1,2,2,1,1,1,2,1,1,1,0,1,2,2,1,1,1,1,1,0,1,1,1,0,0,1,2,0,0,
-3,3,2,2,3,0,2,3,1,1,2,0,0,0,1,0,0,2,0,2,0,0,0,1,0,1,0,1,2,0,2,2,
-1,1,1,1,2,1,0,1,2,2,2,1,1,1,1,1,1,1,0,1,1,1,0,0,0,0,0,0,1,1,0,0,
-2,3,2,3,3,0,0,3,0,1,1,0,1,0,0,0,2,2,1,2,0,0,0,0,0,0,0,0,2,0,1,2,
-2,2,1,1,1,1,1,2,2,2,1,0,2,0,1,0,1,0,0,1,0,1,0,0,1,0,0,0,0,1,0,0,
-3,3,3,3,2,2,2,2,2,0,2,1,1,1,1,2,1,2,1,1,0,2,0,1,0,1,0,0,2,0,1,2,
-1,1,1,1,1,1,1,2,2,1,1,0,2,0,1,0,2,0,0,1,1,1,0,0,2,0,0,0,1,1,0,0,
-2,3,3,3,3,1,0,0,0,0,0,0,0,0,0,0,2,0,0,1,1,0,0,0,0,0,0,1,2,0,1,2,
-2,2,2,1,1,2,1,1,2,2,2,1,2,0,1,1,1,1,1,1,0,1,1,1,1,0,0,1,1,1,0,0,
-2,3,3,3,3,0,2,2,0,2,1,0,0,0,1,1,1,2,0,2,0,0,0,3,0,0,0,0,2,0,2,2,
-1,1,1,2,1,2,1,1,2,2,2,1,2,0,1,1,1,0,1,1,1,1,0,2,1,0,0,0,1,1,0,0,
-2,3,3,3,3,0,2,1,0,0,2,0,0,0,0,0,1,2,0,2,0,0,0,0,0,0,0,0,2,0,1,2,
-1,1,1,2,1,1,1,1,2,2,2,0,1,0,1,1,1,0,0,1,1,1,0,0,1,0,0,0,0,1,0,0,
-3,3,2,2,3,0,1,0,1,0,0,0,0,0,0,0,1,1,0,3,0,0,0,0,0,0,0,0,1,0,2,2,
-1,1,1,1,1,2,1,1,2,2,1,2,2,1,0,1,1,1,1,1,0,1,0,0,1,0,0,0,1,1,0,0,
-3,1,0,1,0,2,2,2,2,3,2,1,1,1,2,3,0,0,1,0,2,1,1,0,1,1,1,1,2,1,1,1,
-1,2,2,1,2,1,2,2,1,1,0,1,2,1,2,2,1,1,1,0,0,1,1,1,2,1,0,1,0,0,0,0,
-2,1,0,1,0,3,1,2,2,2,2,1,2,2,1,1,1,0,2,1,2,2,1,1,2,1,1,0,2,1,1,1,
-1,2,2,2,2,2,2,2,1,2,0,1,1,0,2,1,1,1,1,1,0,0,1,1,1,1,0,1,0,0,0,0,
-2,1,1,1,1,2,2,2,2,1,2,2,2,1,2,2,1,1,2,1,2,3,2,2,1,1,1,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,2,2,3,2,0,1,2,0,1,2,1,1,0,1,0,1,2,1,2,0,0,0,1,1,0,0,0,1,0,0,2,
-1,1,0,0,1,1,0,1,1,1,1,0,2,0,1,1,1,0,0,1,1,0,0,0,0,1,0,0,0,1,0,0,
-2,0,0,0,0,1,2,2,2,2,2,2,2,1,2,1,1,1,1,1,1,1,0,1,1,1,1,1,2,1,1,1,
-1,2,2,2,2,1,1,2,1,2,1,1,1,0,2,1,2,1,1,1,0,2,1,1,1,1,0,1,0,0,0,0,
-3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,1,0,
-1,1,0,1,0,1,1,1,1,1,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,2,2,3,2,0,0,0,0,1,0,0,0,0,0,0,1,1,0,2,0,0,0,0,0,0,0,0,1,0,1,2,
-1,1,1,1,1,1,0,0,2,2,2,2,2,0,1,1,0,1,1,1,1,1,0,0,1,0,0,0,1,1,0,1,
-2,3,1,2,1,0,1,1,0,2,2,2,0,0,1,0,0,1,1,1,1,0,0,0,0,0,0,0,1,0,1,2,
-1,1,1,1,2,1,1,1,1,1,1,1,1,0,1,1,0,1,0,1,0,1,0,0,1,0,0,0,0,1,0,0,
-2,2,2,2,2,0,0,2,0,0,2,0,0,0,0,0,0,1,0,1,0,0,0,0,0,0,0,0,2,0,2,2,
-1,1,1,1,1,0,0,1,2,1,1,0,1,0,1,0,0,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,
-1,2,2,2,2,0,0,2,0,1,1,0,0,0,1,0,0,2,0,2,0,0,0,0,0,0,0,0,0,0,1,1,
-0,0,0,1,1,1,1,1,1,1,1,1,1,0,1,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,
-1,2,2,3,2,0,0,1,0,0,1,0,0,0,0,0,0,1,0,2,0,0,0,1,0,0,0,0,0,0,0,2,
-1,1,0,0,1,0,0,0,1,1,0,0,1,0,1,1,0,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,
-2,1,2,2,2,1,2,1,2,2,1,1,2,1,1,1,0,1,1,1,1,2,0,1,0,1,1,1,1,0,1,1,
-1,1,2,1,1,1,1,1,1,0,0,1,2,1,1,1,1,1,1,0,0,1,1,1,0,0,0,0,0,0,0,0,
-1,0,0,1,3,1,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,2,2,2,1,0,0,1,0,2,0,0,0,0,0,1,1,1,0,1,0,0,0,0,0,0,0,0,2,0,0,1,
-0,2,0,1,0,0,1,1,2,0,1,0,1,0,1,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,
-1,2,2,2,2,0,1,1,0,2,1,0,1,1,1,0,0,1,0,2,0,1,0,0,0,0,0,0,0,0,0,1,
-0,1,0,0,1,0,0,0,1,1,0,0,1,0,0,1,0,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,
-2,2,2,2,2,0,0,1,0,0,0,1,0,1,0,0,0,1,0,1,0,0,0,0,0,0,0,0,0,0,0,1,
-0,1,0,1,1,1,0,0,1,1,1,0,1,0,0,0,0,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,
-2,0,1,0,0,1,2,1,1,1,1,1,1,2,2,1,0,0,1,0,1,0,0,0,0,1,1,1,1,0,0,0,
-1,1,2,1,1,1,1,0,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,2,1,2,1,0,0,1,0,0,0,0,0,0,0,0,1,1,0,1,0,0,0,0,0,0,0,0,0,0,0,1,
-0,0,0,0,0,0,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,1,2,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,0,0,0,
-0,1,1,0,1,1,1,0,0,1,0,0,1,0,1,0,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,
-1,0,1,0,0,1,1,1,1,1,1,1,1,1,1,1,0,0,1,0,2,0,0,2,0,1,0,0,1,0,0,1,
-1,1,0,0,1,1,0,1,0,0,0,1,0,0,1,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,1,0,
-1,1,1,1,1,1,1,2,0,0,0,0,0,0,2,1,0,1,1,0,0,1,1,1,0,1,0,0,0,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,1,1,1,1,1,1,1,1,1,1,1,1,1,1,0,1,0,1,1,0,1,1,1,1,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-)
-
-Latin5BulgarianModel = {
-  'char_to_order_map': Latin5_BulgarianCharToOrderMap,
-  'precedence_matrix': BulgarianLangModel,
-  'typical_positive_ratio': 0.969392,
-  'keep_english_letter': False,
-  'charset_name': "ISO-8859-5",
-  'language': 'Bulgairan',
-}
-
-Win1251BulgarianModel = {
-  'char_to_order_map': win1251BulgarianCharToOrderMap,
-  'precedence_matrix': BulgarianLangModel,
-  'typical_positive_ratio': 0.969392,
-  'keep_english_letter': False,
-  'charset_name': "windows-1251",
-  'language': 'Bulgarian',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langcyrillicmodel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langcyrillicmodel.py
deleted file mode 100644
index e5f9a1f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langcyrillicmodel.py
+++ /dev/null
@@ -1,333 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# KOI8-R language model
-# Character Mapping Table:
-KOI8R_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253,142,143,144,145,146,147,148,149,150,151,152, 74,153, 75,154,  # 40
-155,156,157,158,159,160,161,162,163,164,165,253,253,253,253,253,  # 50
-253, 71,172, 66,173, 65,174, 76,175, 64,176,177, 77, 72,178, 69,  # 60
- 67,179, 78, 73,180,181, 79,182,183,184,185,253,253,253,253,253,  # 70
-191,192,193,194,195,196,197,198,199,200,201,202,203,204,205,206,  # 80
-207,208,209,210,211,212,213,214,215,216,217,218,219,220,221,222,  # 90
-223,224,225, 68,226,227,228,229,230,231,232,233,234,235,236,237,  # a0
-238,239,240,241,242,243,244,245,246,247,248,249,250,251,252,253,  # b0
- 27,  3, 21, 28, 13,  2, 39, 19, 26,  4, 23, 11,  8, 12,  5,  1,  # c0
- 15, 16,  9,  7,  6, 14, 24, 10, 17, 18, 20, 25, 30, 29, 22, 54,  # d0
- 59, 37, 44, 58, 41, 48, 53, 46, 55, 42, 60, 36, 49, 38, 31, 34,  # e0
- 35, 43, 45, 32, 40, 52, 56, 33, 61, 62, 51, 57, 47, 63, 50, 70,  # f0
-)
-
-win1251_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253,142,143,144,145,146,147,148,149,150,151,152, 74,153, 75,154,  # 40
-155,156,157,158,159,160,161,162,163,164,165,253,253,253,253,253,  # 50
-253, 71,172, 66,173, 65,174, 76,175, 64,176,177, 77, 72,178, 69,  # 60
- 67,179, 78, 73,180,181, 79,182,183,184,185,253,253,253,253,253,  # 70
-191,192,193,194,195,196,197,198,199,200,201,202,203,204,205,206,
-207,208,209,210,211,212,213,214,215,216,217,218,219,220,221,222,
-223,224,225,226,227,228,229,230,231,232,233,234,235,236,237,238,
-239,240,241,242,243,244,245,246, 68,247,248,249,250,251,252,253,
- 37, 44, 33, 46, 41, 48, 56, 51, 42, 60, 36, 49, 38, 31, 34, 35,
- 45, 32, 40, 52, 53, 55, 58, 50, 57, 63, 70, 62, 61, 47, 59, 43,
-  3, 21, 10, 19, 13,  2, 24, 20,  4, 23, 11,  8, 12,  5,  1, 15,
-  9,  7,  6, 14, 39, 26, 28, 22, 25, 29, 54, 18, 17, 30, 27, 16,
-)
-
-latin5_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253,142,143,144,145,146,147,148,149,150,151,152, 74,153, 75,154,  # 40
-155,156,157,158,159,160,161,162,163,164,165,253,253,253,253,253,  # 50
-253, 71,172, 66,173, 65,174, 76,175, 64,176,177, 77, 72,178, 69,  # 60
- 67,179, 78, 73,180,181, 79,182,183,184,185,253,253,253,253,253,  # 70
-191,192,193,194,195,196,197,198,199,200,201,202,203,204,205,206,
-207,208,209,210,211,212,213,214,215,216,217,218,219,220,221,222,
-223,224,225,226,227,228,229,230,231,232,233,234,235,236,237,238,
- 37, 44, 33, 46, 41, 48, 56, 51, 42, 60, 36, 49, 38, 31, 34, 35,
- 45, 32, 40, 52, 53, 55, 58, 50, 57, 63, 70, 62, 61, 47, 59, 43,
-  3, 21, 10, 19, 13,  2, 24, 20,  4, 23, 11,  8, 12,  5,  1, 15,
-  9,  7,  6, 14, 39, 26, 28, 22, 25, 29, 54, 18, 17, 30, 27, 16,
-239, 68,240,241,242,243,244,245,246,247,248,249,250,251,252,255,
-)
-
-macCyrillic_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253,142,143,144,145,146,147,148,149,150,151,152, 74,153, 75,154,  # 40
-155,156,157,158,159,160,161,162,163,164,165,253,253,253,253,253,  # 50
-253, 71,172, 66,173, 65,174, 76,175, 64,176,177, 77, 72,178, 69,  # 60
- 67,179, 78, 73,180,181, 79,182,183,184,185,253,253,253,253,253,  # 70
- 37, 44, 33, 46, 41, 48, 56, 51, 42, 60, 36, 49, 38, 31, 34, 35,
- 45, 32, 40, 52, 53, 55, 58, 50, 57, 63, 70, 62, 61, 47, 59, 43,
-191,192,193,194,195,196,197,198,199,200,201,202,203,204,205,206,
-207,208,209,210,211,212,213,214,215,216,217,218,219,220,221,222,
-223,224,225,226,227,228,229,230,231,232,233,234,235,236,237,238,
-239,240,241,242,243,244,245,246,247,248,249,250,251,252, 68, 16,
-  3, 21, 10, 19, 13,  2, 24, 20,  4, 23, 11,  8, 12,  5,  1, 15,
-  9,  7,  6, 14, 39, 26, 28, 22, 25, 29, 54, 18, 17, 30, 27,255,
-)
-
-IBM855_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253,142,143,144,145,146,147,148,149,150,151,152, 74,153, 75,154,  # 40
-155,156,157,158,159,160,161,162,163,164,165,253,253,253,253,253,  # 50
-253, 71,172, 66,173, 65,174, 76,175, 64,176,177, 77, 72,178, 69,  # 60
- 67,179, 78, 73,180,181, 79,182,183,184,185,253,253,253,253,253,  # 70
-191,192,193,194, 68,195,196,197,198,199,200,201,202,203,204,205,
-206,207,208,209,210,211,212,213,214,215,216,217, 27, 59, 54, 70,
-  3, 37, 21, 44, 28, 58, 13, 41,  2, 48, 39, 53, 19, 46,218,219,
-220,221,222,223,224, 26, 55,  4, 42,225,226,227,228, 23, 60,229,
-230,231,232,233,234,235, 11, 36,236,237,238,239,240,241,242,243,
-  8, 49, 12, 38,  5, 31,  1, 34, 15,244,245,246,247, 35, 16,248,
- 43,  9, 45,  7, 32,  6, 40, 14, 52, 24, 56, 10, 33, 17, 61,249,
-250, 18, 62, 20, 51, 25, 57, 30, 47, 29, 63, 22, 50,251,252,255,
-)
-
-IBM866_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253,142,143,144,145,146,147,148,149,150,151,152, 74,153, 75,154,  # 40
-155,156,157,158,159,160,161,162,163,164,165,253,253,253,253,253,  # 50
-253, 71,172, 66,173, 65,174, 76,175, 64,176,177, 77, 72,178, 69,  # 60
- 67,179, 78, 73,180,181, 79,182,183,184,185,253,253,253,253,253,  # 70
- 37, 44, 33, 46, 41, 48, 56, 51, 42, 60, 36, 49, 38, 31, 34, 35,
- 45, 32, 40, 52, 53, 55, 58, 50, 57, 63, 70, 62, 61, 47, 59, 43,
-  3, 21, 10, 19, 13,  2, 24, 20,  4, 23, 11,  8, 12,  5,  1, 15,
-191,192,193,194,195,196,197,198,199,200,201,202,203,204,205,206,
-207,208,209,210,211,212,213,214,215,216,217,218,219,220,221,222,
-223,224,225,226,227,228,229,230,231,232,233,234,235,236,237,238,
-  9,  7,  6, 14, 39, 26, 28, 22, 25, 29, 54, 18, 17, 30, 27, 16,
-239, 68,240,241,242,243,244,245,246,247,248,249,250,251,252,255,
-)
-
-# Model Table:
-# total sequences: 100%
-# first 512 sequences: 97.6601%
-# first 1024 sequences: 2.3389%
-# rest  sequences:      0.1237%
-# negative sequences:   0.0009%
-RussianLangModel = (
-0,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,1,1,3,3,3,3,1,3,3,3,2,3,2,3,3,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,0,3,2,2,2,2,2,0,0,2,
-3,3,3,2,3,3,3,3,3,3,3,3,3,3,2,3,3,0,0,3,3,3,3,3,3,3,3,3,2,3,2,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,2,2,3,3,3,3,3,3,3,3,3,2,3,3,0,0,3,3,3,3,3,3,3,3,2,3,3,1,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,2,3,2,3,3,3,3,3,3,3,3,3,3,3,3,3,0,0,3,3,3,3,3,3,3,3,3,3,3,2,1,
-0,0,0,0,0,0,0,2,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,3,0,0,3,3,3,3,3,3,3,3,3,3,3,2,1,
-0,0,0,0,0,1,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,2,2,2,3,1,3,3,1,3,3,3,3,2,2,3,0,2,2,2,3,3,2,1,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,3,3,3,3,3,2,2,3,2,3,3,3,2,1,2,2,0,1,2,2,2,2,2,2,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,2,2,3,0,2,2,3,3,2,1,2,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,1,0,0,2,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,3,3,1,2,3,2,2,3,2,3,3,3,3,2,2,3,0,3,2,2,3,1,1,1,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,2,2,3,3,3,3,3,2,3,3,3,3,2,2,2,0,3,3,3,2,2,2,2,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,2,3,2,3,3,3,3,3,3,2,3,2,2,0,1,3,2,1,2,2,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,2,1,1,3,0,1,1,1,1,2,1,1,0,2,2,2,1,2,0,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,3,3,2,2,2,2,1,3,2,3,2,3,2,1,2,2,0,1,1,2,1,2,1,2,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,3,2,2,3,2,3,3,3,2,2,2,2,0,2,2,2,2,3,1,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-3,2,3,2,2,3,3,3,3,3,3,3,3,3,1,3,2,0,0,3,3,3,3,2,3,3,3,3,2,3,2,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,3,3,3,3,3,2,2,3,3,0,2,1,0,3,2,3,2,3,0,0,1,2,0,0,1,0,1,2,1,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,3,0,2,3,3,3,3,2,3,3,3,3,1,2,2,0,0,2,3,2,2,2,3,2,3,2,2,3,0,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,2,3,0,2,3,2,3,0,1,2,3,3,2,0,2,3,0,0,2,3,2,2,0,1,3,1,3,2,2,1,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,3,0,2,3,3,3,3,3,3,3,3,2,1,3,2,0,0,2,2,3,3,3,2,3,3,0,2,2,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,2,3,3,2,2,2,3,3,0,0,1,1,1,1,1,2,0,0,1,1,1,1,0,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,2,3,3,3,3,3,3,3,0,3,2,3,3,2,3,2,0,2,1,0,1,1,0,1,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,3,3,3,2,2,2,2,3,1,3,2,3,1,1,2,1,0,2,2,2,2,1,3,1,0,
-0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-2,2,3,3,3,3,3,1,2,2,1,3,1,0,3,0,0,3,0,0,0,1,1,0,1,2,1,0,0,0,0,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,2,2,1,1,3,3,3,2,2,1,2,2,3,1,1,2,0,0,2,2,1,3,0,0,2,1,1,2,1,1,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,2,3,3,3,3,1,2,2,2,1,2,1,3,3,1,1,2,1,2,1,2,2,0,2,0,0,1,1,0,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,3,3,3,3,3,2,1,3,2,2,3,2,0,3,2,0,3,0,1,0,1,1,0,0,1,1,1,1,0,1,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,2,3,3,3,2,2,2,3,3,1,2,1,2,1,0,1,0,1,1,0,1,0,0,2,1,1,1,0,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,
-3,1,1,2,1,2,3,3,2,2,1,2,2,3,0,2,1,0,0,2,2,3,2,1,2,2,2,2,2,3,1,0,
-0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,1,1,0,1,1,2,2,1,1,3,0,0,1,3,1,1,1,0,0,0,1,0,1,1,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,1,3,3,3,2,0,0,0,2,1,0,1,0,2,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,0,1,0,0,2,3,2,2,2,1,2,2,2,1,2,1,0,0,1,1,1,0,2,0,1,1,1,0,0,1,1,
-1,0,0,0,0,0,1,2,0,0,0,0,0,1,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,
-2,3,3,3,3,0,0,0,0,1,0,0,0,0,3,0,1,2,1,0,0,0,0,0,0,0,1,1,0,0,1,1,
-1,0,1,0,1,2,0,0,1,1,2,1,0,1,1,1,1,0,1,1,1,1,0,1,0,0,1,0,0,1,1,0,
-2,2,3,2,2,2,3,1,2,2,2,2,2,2,2,2,1,1,1,1,1,1,1,0,1,0,1,1,1,0,2,1,
-1,1,1,1,1,1,1,1,2,1,1,1,1,1,1,1,1,1,1,0,1,0,1,1,0,1,1,1,0,1,1,0,
-3,3,3,2,2,2,2,3,2,2,1,1,2,2,2,2,1,1,3,1,2,1,2,0,0,1,1,0,1,0,2,1,
-1,1,1,1,1,2,1,0,1,1,1,1,0,1,0,0,1,1,0,0,1,0,1,0,0,1,0,0,0,1,1,0,
-2,0,0,1,0,3,2,2,2,2,1,2,1,2,1,2,0,0,0,2,1,2,2,1,1,2,2,0,1,1,0,2,
-1,1,1,1,1,0,1,1,1,2,1,1,1,2,1,0,1,2,1,1,1,1,0,1,1,1,0,0,1,0,0,1,
-1,3,2,2,2,1,1,1,2,3,0,0,0,0,2,0,2,2,1,0,0,0,0,0,0,1,0,0,0,0,1,1,
-1,0,1,1,0,1,0,1,1,0,1,1,0,2,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,1,1,0,
-2,3,2,3,2,1,2,2,2,2,1,0,0,0,2,0,0,1,1,0,0,0,0,0,0,0,1,1,0,0,2,1,
-1,1,2,1,0,2,0,0,1,0,1,0,0,1,0,0,1,1,0,1,1,0,0,0,0,0,1,0,0,0,0,0,
-3,0,0,1,0,2,2,2,3,2,2,2,2,2,2,2,0,0,0,2,1,2,1,1,1,2,2,0,0,0,1,2,
-1,1,1,1,1,0,1,2,1,1,1,1,1,1,1,0,1,1,1,1,1,1,0,1,1,1,1,1,1,0,0,1,
-2,3,2,3,3,2,0,1,1,1,0,0,1,0,2,0,1,1,3,1,0,0,0,0,0,0,0,1,0,0,2,1,
-1,1,1,1,1,1,1,0,1,0,1,1,1,1,0,1,1,1,0,0,1,1,0,1,0,0,0,0,0,0,1,0,
-2,3,3,3,3,1,2,2,2,2,0,1,1,0,2,1,1,1,2,1,0,1,1,0,0,1,0,1,0,0,2,0,
-0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,3,3,3,2,0,0,1,1,2,2,1,0,0,2,0,1,1,3,0,0,1,0,0,0,0,0,1,0,1,2,1,
-1,1,2,0,1,1,1,0,1,0,1,1,0,1,0,1,1,1,1,0,1,0,0,0,0,0,0,1,0,1,1,0,
-1,3,2,3,2,1,0,0,2,2,2,0,1,0,2,0,1,1,1,0,1,0,0,0,3,0,1,1,0,0,2,1,
-1,1,1,0,1,1,0,0,0,0,1,1,0,1,0,0,2,1,1,0,1,0,0,0,1,0,1,0,0,1,1,0,
-3,1,2,1,1,2,2,2,2,2,2,1,2,2,1,1,0,0,0,2,2,2,0,0,0,1,2,1,0,1,0,1,
-2,1,1,1,1,1,1,1,1,1,1,1,1,1,1,0,2,1,1,1,0,1,0,1,1,0,1,1,1,0,0,1,
-3,0,0,0,0,2,0,1,1,1,1,1,1,1,0,1,0,0,0,1,1,1,0,1,0,1,1,0,0,1,0,1,
-1,1,0,0,1,0,0,0,1,0,1,1,0,0,1,0,1,0,1,0,0,0,0,1,0,0,0,1,0,0,0,1,
-1,3,3,2,2,0,0,0,2,2,0,0,0,1,2,0,1,1,2,0,0,0,0,0,0,0,0,1,0,0,2,1,
-0,1,1,0,0,1,1,0,0,0,1,1,0,1,1,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,1,0,
-2,3,2,3,2,0,0,0,0,1,1,0,0,0,2,0,2,0,2,0,0,0,0,0,1,0,0,1,0,0,1,1,
-1,1,2,0,1,2,1,0,1,1,2,1,1,1,1,1,2,1,1,0,1,0,0,1,1,1,1,1,0,1,1,0,
-1,3,2,2,2,1,0,0,2,2,1,0,1,2,2,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,1,1,
-0,0,1,1,0,1,1,0,0,1,1,0,1,1,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,1,0,2,3,1,2,2,2,2,2,2,1,1,0,0,0,1,0,1,0,2,1,1,1,0,0,0,0,1,
-1,1,0,1,1,0,1,1,1,1,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,0,0,0,
-2,0,2,0,0,1,0,3,2,1,2,1,2,2,0,1,0,0,0,2,1,0,0,2,1,1,1,1,0,2,0,2,
-2,1,1,1,1,1,1,1,1,1,1,1,1,2,1,0,1,1,1,1,0,0,0,1,1,1,1,0,1,0,0,1,
-1,2,2,2,2,1,0,0,1,0,0,0,0,0,2,0,1,1,1,1,0,0,0,0,1,0,1,2,0,0,2,0,
-1,0,1,1,1,2,1,0,1,0,1,1,0,0,1,0,1,1,1,0,1,0,0,0,1,0,0,1,0,1,1,0,
-2,1,2,2,2,0,3,0,1,1,0,0,0,0,2,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-0,0,0,1,1,1,0,0,1,0,1,0,0,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,1,0,0,
-1,2,2,3,2,2,0,0,1,1,2,0,1,2,1,0,1,0,1,0,0,1,0,0,0,0,0,0,0,0,0,1,
-0,1,1,0,0,1,1,0,0,1,1,0,0,1,1,0,1,1,0,0,1,0,0,0,0,0,0,0,0,1,1,0,
-2,2,1,1,2,1,2,2,2,2,2,1,2,2,0,1,0,0,0,1,2,2,2,1,2,1,1,1,1,1,2,1,
-1,1,1,1,1,1,1,1,1,1,0,0,1,1,1,0,1,1,1,0,0,0,0,1,1,1,0,1,1,0,0,1,
-1,2,2,2,2,0,1,0,2,2,0,0,0,0,2,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,2,0,
-0,0,1,0,0,1,0,0,0,0,1,0,1,1,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,
-0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,2,2,2,2,0,0,0,2,2,2,0,1,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,1,1,
-0,1,1,0,0,1,1,0,0,0,1,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,2,2,2,2,0,0,0,0,1,0,0,1,1,2,0,0,0,0,1,0,1,0,0,1,0,0,2,0,0,0,1,
-0,0,1,0,0,1,0,0,0,1,1,0,0,0,0,0,1,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,
-1,2,2,2,1,1,2,0,2,1,1,1,1,0,2,2,0,0,0,0,0,0,0,0,0,1,1,0,0,0,1,1,
-0,0,1,0,1,1,0,0,0,0,1,0,0,0,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,
-1,0,2,1,2,0,0,0,0,0,1,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,1,0,0,0,0,
-0,0,1,0,1,1,0,0,0,0,1,0,0,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,1,0,
-1,0,0,0,0,2,0,1,2,1,0,1,1,1,0,1,0,0,0,1,0,1,0,0,1,0,1,0,0,0,0,1,
-0,0,0,0,0,1,0,0,1,1,0,0,1,1,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,1,
-2,2,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-1,0,0,0,1,0,0,0,1,1,0,0,0,0,0,0,0,1,0,0,0,0,0,1,0,0,1,0,0,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-1,1,1,0,1,0,1,0,0,1,1,1,1,0,0,0,1,0,0,0,0,1,0,0,0,1,0,1,0,0,0,0,
-1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-1,1,0,1,1,0,1,0,1,0,0,0,0,1,1,0,1,1,0,0,0,0,0,1,0,1,1,0,1,0,0,0,
-0,1,1,1,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,1,0,0,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,
-)
-
-Koi8rModel = {
-  'char_to_order_map': KOI8R_char_to_order_map,
-  'precedence_matrix': RussianLangModel,
-  'typical_positive_ratio': 0.976601,
-  'keep_english_letter': False,
-  'charset_name': "KOI8-R",
-  'language': 'Russian',
-}
-
-Win1251CyrillicModel = {
-  'char_to_order_map': win1251_char_to_order_map,
-  'precedence_matrix': RussianLangModel,
-  'typical_positive_ratio': 0.976601,
-  'keep_english_letter': False,
-  'charset_name': "windows-1251",
-  'language': 'Russian',
-}
-
-Latin5CyrillicModel = {
-  'char_to_order_map': latin5_char_to_order_map,
-  'precedence_matrix': RussianLangModel,
-  'typical_positive_ratio': 0.976601,
-  'keep_english_letter': False,
-  'charset_name': "ISO-8859-5",
-  'language': 'Russian',
-}
-
-MacCyrillicModel = {
-  'char_to_order_map': macCyrillic_char_to_order_map,
-  'precedence_matrix': RussianLangModel,
-  'typical_positive_ratio': 0.976601,
-  'keep_english_letter': False,
-  'charset_name': "MacCyrillic",
-  'language': 'Russian',
-}
-
-Ibm866Model = {
-  'char_to_order_map': IBM866_char_to_order_map,
-  'precedence_matrix': RussianLangModel,
-  'typical_positive_ratio': 0.976601,
-  'keep_english_letter': False,
-  'charset_name': "IBM866",
-  'language': 'Russian',
-}
-
-Ibm855Model = {
-  'char_to_order_map': IBM855_char_to_order_map,
-  'precedence_matrix': RussianLangModel,
-  'typical_positive_ratio': 0.976601,
-  'keep_english_letter': False,
-  'charset_name': "IBM855",
-  'language': 'Russian',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langgreekmodel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langgreekmodel.py
deleted file mode 100644
index 5332221..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langgreekmodel.py
+++ /dev/null
@@ -1,225 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# 255: Control characters that usually does not exist in any text
-# 254: Carriage/Return
-# 253: symbol (punctuation) that does not belong to word
-# 252: 0 - 9
-
-# Character Mapping Table:
-Latin7_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253, 82,100,104, 94, 98,101,116,102,111,187,117, 92, 88,113, 85,  # 40
- 79,118,105, 83, 67,114,119, 95, 99,109,188,253,253,253,253,253,  # 50
-253, 72, 70, 80, 81, 60, 96, 93, 89, 68,120, 97, 77, 86, 69, 55,  # 60
- 78,115, 65, 66, 58, 76,106,103, 87,107,112,253,253,253,253,253,  # 70
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 80
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 90
-253,233, 90,253,253,253,253,253,253,253,253,253,253, 74,253,253,  # a0
-253,253,253,253,247,248, 61, 36, 46, 71, 73,253, 54,253,108,123,  # b0
-110, 31, 51, 43, 41, 34, 91, 40, 52, 47, 44, 53, 38, 49, 59, 39,  # c0
- 35, 48,250, 37, 33, 45, 56, 50, 84, 57,120,121, 17, 18, 22, 15,  # d0
-124,  1, 29, 20, 21,  3, 32, 13, 25,  5, 11, 16, 10,  6, 30,  4,  # e0
-  9,  8, 14,  7,  2, 12, 28, 23, 42, 24, 64, 75, 19, 26, 27,253,  # f0
-)
-
-win1253_char_to_order_map = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253, 82,100,104, 94, 98,101,116,102,111,187,117, 92, 88,113, 85,  # 40
- 79,118,105, 83, 67,114,119, 95, 99,109,188,253,253,253,253,253,  # 50
-253, 72, 70, 80, 81, 60, 96, 93, 89, 68,120, 97, 77, 86, 69, 55,  # 60
- 78,115, 65, 66, 58, 76,106,103, 87,107,112,253,253,253,253,253,  # 70
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 80
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 90
-253,233, 61,253,253,253,253,253,253,253,253,253,253, 74,253,253,  # a0
-253,253,253,253,247,253,253, 36, 46, 71, 73,253, 54,253,108,123,  # b0
-110, 31, 51, 43, 41, 34, 91, 40, 52, 47, 44, 53, 38, 49, 59, 39,  # c0
- 35, 48,250, 37, 33, 45, 56, 50, 84, 57,120,121, 17, 18, 22, 15,  # d0
-124,  1, 29, 20, 21,  3, 32, 13, 25,  5, 11, 16, 10,  6, 30,  4,  # e0
-  9,  8, 14,  7,  2, 12, 28, 23, 42, 24, 64, 75, 19, 26, 27,253,  # f0
-)
-
-# Model Table:
-# total sequences: 100%
-# first 512 sequences: 98.2851%
-# first 1024 sequences:1.7001%
-# rest  sequences:     0.0359%
-# negative sequences:  0.0148%
-GreekLangModel = (
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,3,2,2,3,3,3,3,3,3,3,3,1,3,3,3,0,2,2,3,3,0,3,0,3,2,0,3,3,3,0,
-3,0,0,0,2,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,0,3,3,0,3,2,3,3,0,3,2,3,3,3,0,0,3,0,3,0,3,3,2,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,
-0,2,3,2,2,3,3,3,3,3,3,3,3,0,3,3,3,3,0,2,3,3,0,3,3,3,3,2,3,3,3,0,
-2,0,0,0,2,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,2,3,3,2,3,3,3,3,3,3,3,3,3,3,3,3,0,2,1,3,3,3,3,2,3,3,2,3,3,2,0,
-0,0,0,0,2,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,0,3,3,3,3,3,3,0,3,3,0,3,3,3,3,3,3,3,3,3,3,0,3,2,3,3,0,
-2,0,1,0,2,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,2,3,0,0,0,0,3,3,0,3,1,3,3,3,0,3,3,0,3,3,3,3,0,0,0,0,
-2,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,0,3,0,3,3,3,3,3,0,3,2,2,2,3,0,2,3,3,3,3,3,2,3,3,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,3,2,2,2,3,3,3,3,0,3,1,3,3,3,3,2,3,3,3,3,3,3,3,2,2,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,2,0,3,0,0,0,3,3,2,3,3,3,3,3,0,0,3,2,3,0,2,3,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,0,3,3,3,3,0,0,3,3,0,2,3,0,3,0,3,3,3,0,0,3,0,3,0,2,2,3,3,0,0,
-0,0,1,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,2,0,3,2,3,3,3,3,0,3,3,3,3,3,0,3,3,2,3,2,3,3,2,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,2,3,2,3,3,3,3,3,3,0,2,3,2,3,2,2,2,3,2,3,3,2,3,0,2,2,2,3,0,
-2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,3,0,0,0,3,3,3,2,3,3,0,0,3,0,3,0,0,0,3,2,0,3,0,3,0,0,2,0,2,0,
-0,0,0,0,2,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,0,3,3,3,3,3,3,0,3,3,0,3,0,0,0,3,3,0,3,3,3,0,0,1,2,3,0,
-3,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,2,0,0,3,2,2,3,3,0,3,3,3,3,3,2,1,3,0,3,2,3,3,2,1,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,3,3,0,2,3,3,3,3,3,3,0,0,3,0,3,0,0,0,3,3,0,3,2,3,0,0,3,3,3,0,
-3,0,0,0,2,0,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,0,3,3,3,3,3,3,0,0,3,0,3,0,0,0,3,2,0,3,2,3,0,0,3,2,3,0,
-2,0,0,0,0,0,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,3,1,2,2,3,3,3,3,3,3,0,2,3,0,3,0,0,0,3,3,0,3,0,2,0,0,2,3,1,0,
-2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,0,3,3,3,3,0,3,0,3,3,2,3,0,3,3,3,3,3,3,0,3,3,3,0,2,3,0,0,3,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,0,3,3,3,0,0,3,0,0,0,3,3,0,3,0,2,3,3,0,0,3,0,3,0,3,3,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,3,0,0,0,3,3,3,3,3,3,0,0,3,0,2,0,0,0,3,3,0,3,0,3,0,0,2,0,2,0,
-0,0,0,0,1,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,3,0,3,0,2,0,3,2,0,3,2,3,2,3,0,0,3,2,3,2,3,3,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,3,0,0,2,3,3,3,3,3,0,0,0,3,0,2,1,0,0,3,2,2,2,0,3,0,0,2,2,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,0,3,3,3,2,0,3,0,3,0,3,3,0,2,1,2,3,3,0,0,3,0,3,0,3,3,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,2,3,3,3,0,3,3,3,3,3,3,0,2,3,0,3,0,0,0,2,1,0,2,2,3,0,0,2,2,2,0,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,3,0,0,2,3,3,3,2,3,0,0,1,3,0,2,0,0,0,0,3,0,1,0,2,0,0,1,1,1,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,3,1,0,3,0,0,0,3,2,0,3,2,3,3,3,0,0,3,0,3,2,2,2,1,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,0,3,3,3,0,0,3,0,0,0,0,2,0,2,3,3,2,2,2,2,3,0,2,0,2,2,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,3,3,3,2,0,0,0,0,0,0,2,3,0,2,0,2,3,2,0,0,3,0,3,0,3,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,3,2,3,3,2,2,3,0,2,0,3,0,0,0,2,0,0,0,0,1,2,0,2,0,2,0,
-0,2,0,2,0,2,2,0,0,1,0,2,2,2,0,2,2,2,0,2,2,2,0,0,2,0,0,1,0,0,0,0,
-0,2,0,3,3,2,0,0,0,0,0,0,1,3,0,2,0,2,2,2,0,0,2,0,3,0,0,2,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,0,2,3,2,0,2,2,0,2,0,2,2,0,2,0,2,2,2,0,0,0,0,0,0,2,3,0,0,0,2,
-0,1,2,0,0,0,0,2,2,0,0,0,2,1,0,2,2,0,0,0,0,0,0,1,0,2,0,0,0,0,0,0,
-0,0,2,1,0,2,3,2,2,3,2,3,2,0,0,3,3,3,0,0,3,2,0,0,0,1,1,0,2,0,2,2,
-0,2,0,2,0,2,2,0,0,2,0,2,2,2,0,2,2,2,2,0,0,2,0,0,0,2,0,1,0,0,0,0,
-0,3,0,3,3,2,2,0,3,0,0,0,2,2,0,2,2,2,1,2,0,0,1,2,2,0,0,3,0,0,0,2,
-0,1,2,0,0,0,1,2,0,0,0,0,0,0,0,2,2,0,1,0,0,2,0,0,0,2,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,2,3,3,2,2,0,0,0,2,0,2,3,3,0,2,0,0,0,0,0,0,2,2,2,0,2,2,0,2,0,2,
-0,2,2,0,0,2,2,2,2,1,0,0,2,2,0,2,0,0,2,0,0,0,0,0,0,2,0,0,0,0,0,0,
-0,2,0,3,2,3,0,0,0,3,0,0,2,2,0,2,0,2,2,2,0,0,2,0,0,0,0,0,0,0,0,2,
-0,0,2,2,0,0,2,2,2,0,0,0,0,0,0,2,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,2,0,0,3,2,0,2,2,2,2,2,0,0,0,2,0,0,0,0,2,0,1,0,0,2,0,1,0,0,0,
-0,2,2,2,0,2,2,0,1,2,0,2,2,2,0,2,2,2,2,1,2,2,0,0,2,0,0,0,0,0,0,0,
-0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,
-0,2,0,2,0,2,2,0,0,0,0,1,2,1,0,0,2,2,0,0,2,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,3,2,3,0,0,2,0,0,0,2,2,0,2,0,0,0,1,0,0,2,0,2,0,2,2,0,0,0,0,
-0,0,2,0,0,0,0,2,2,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,
-0,2,2,3,2,2,0,0,0,0,0,0,1,3,0,2,0,2,2,0,0,0,1,0,2,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,2,0,2,0,3,2,0,2,0,0,0,0,0,0,2,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-0,0,2,0,0,0,0,1,1,0,0,2,1,2,0,2,2,0,1,0,0,1,0,0,0,2,0,0,0,0,0,0,
-0,3,0,2,2,2,0,0,2,0,0,0,2,0,0,0,2,3,0,2,0,0,0,0,0,0,2,2,0,0,0,2,
-0,1,2,0,0,0,1,2,2,1,0,0,0,2,0,0,2,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,3,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,2,1,2,0,2,2,0,2,0,0,2,0,0,0,0,1,2,1,0,2,1,0,0,0,0,0,0,0,0,0,0,
-0,0,2,0,0,0,3,1,2,2,0,2,0,0,0,0,2,0,0,0,2,0,0,3,0,0,0,0,2,2,2,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,2,1,0,2,0,1,2,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,1,0,0,0,0,0,0,2,
-0,2,2,0,0,2,2,2,2,2,0,1,2,0,0,0,2,2,0,1,0,2,0,0,2,2,0,0,0,0,0,0,
-0,0,0,0,1,0,0,0,0,0,0,0,3,0,0,2,0,0,0,0,0,0,0,0,2,0,2,0,0,0,0,2,
-0,1,2,0,0,0,0,2,2,1,0,1,0,1,0,2,2,2,1,0,0,0,0,0,0,1,0,0,0,0,0,0,
-0,2,0,1,2,0,0,0,0,0,0,0,0,0,0,2,0,0,2,2,0,0,0,0,1,0,0,0,0,0,0,2,
-0,2,2,0,0,0,0,2,2,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,2,0,0,2,0,0,0,
-0,2,2,2,2,0,0,0,3,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,2,0,0,0,0,0,0,1,
-0,0,2,0,0,0,0,1,2,0,0,0,0,0,0,2,2,1,1,0,0,0,0,0,0,1,0,0,0,0,0,0,
-0,2,0,2,2,2,0,0,2,0,0,0,0,0,0,0,2,2,2,0,0,0,2,0,0,0,0,0,0,0,0,2,
-0,0,1,0,0,0,0,2,1,0,0,0,0,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,
-0,3,0,2,0,0,0,0,0,0,0,0,2,0,0,0,0,0,2,0,0,0,0,0,0,0,2,0,0,0,0,2,
-0,0,2,0,0,0,0,2,2,0,0,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,2,0,2,2,1,0,0,0,0,0,0,2,0,0,2,0,2,2,2,0,0,0,0,0,0,2,0,0,0,0,2,
-0,0,2,0,0,2,0,2,2,0,0,0,0,2,0,2,0,0,0,0,0,2,0,0,0,2,0,0,0,0,0,0,
-0,0,3,0,0,0,2,2,0,2,2,0,0,0,0,0,2,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,2,0,0,0,0,0,
-0,2,2,2,2,2,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,1,1,0,0,0,1,
-0,0,0,0,0,0,0,2,1,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,2,2,0,0,0,0,0,2,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,
-0,2,0,0,0,2,0,0,0,0,0,1,0,0,0,0,2,2,0,0,0,1,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,1,0,2,0,0,0,
-0,2,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,1,0,0,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,1,0,0,2,0,2,0,0,0,
-0,0,0,0,0,0,0,0,2,1,0,0,0,0,0,0,2,0,0,0,1,2,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-)
-
-Latin7GreekModel = {
-  'char_to_order_map': Latin7_char_to_order_map,
-  'precedence_matrix': GreekLangModel,
-  'typical_positive_ratio': 0.982851,
-  'keep_english_letter': False,
-  'charset_name': "ISO-8859-7",
-  'language': 'Greek',
-}
-
-Win1253GreekModel = {
-  'char_to_order_map': win1253_char_to_order_map,
-  'precedence_matrix': GreekLangModel,
-  'typical_positive_ratio': 0.982851,
-  'keep_english_letter': False,
-  'charset_name': "windows-1253",
-  'language': 'Greek',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langhebrewmodel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langhebrewmodel.py
deleted file mode 100644
index 58f4c87..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langhebrewmodel.py
+++ /dev/null
@@ -1,200 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-#          Simon Montagu
-# Portions created by the Initial Developer are Copyright (C) 2005
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#   Shoshannah Forbes - original C code (?)
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# 255: Control characters that usually does not exist in any text
-# 254: Carriage/Return
-# 253: symbol (punctuation) that does not belong to word
-# 252: 0 - 9
-
-# Windows-1255 language model
-# Character Mapping Table:
-WIN1255_CHAR_TO_ORDER_MAP = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253, 69, 91, 79, 80, 92, 89, 97, 90, 68,111,112, 82, 73, 95, 85,  # 40
- 78,121, 86, 71, 67,102,107, 84,114,103,115,253,253,253,253,253,  # 50
-253, 50, 74, 60, 61, 42, 76, 70, 64, 53,105, 93, 56, 65, 54, 49,  # 60
- 66,110, 51, 43, 44, 63, 81, 77, 98, 75,108,253,253,253,253,253,  # 70
-124,202,203,204,205, 40, 58,206,207,208,209,210,211,212,213,214,
-215, 83, 52, 47, 46, 72, 32, 94,216,113,217,109,218,219,220,221,
- 34,116,222,118,100,223,224,117,119,104,125,225,226, 87, 99,227,
-106,122,123,228, 55,229,230,101,231,232,120,233, 48, 39, 57,234,
- 30, 59, 41, 88, 33, 37, 36, 31, 29, 35,235, 62, 28,236,126,237,
-238, 38, 45,239,240,241,242,243,127,244,245,246,247,248,249,250,
-  9,  8, 20, 16,  3,  2, 24, 14, 22,  1, 25, 15,  4, 11,  6, 23,
- 12, 19, 13, 26, 18, 27, 21, 17,  7, 10,  5,251,252,128, 96,253,
-)
-
-# Model Table:
-# total sequences: 100%
-# first 512 sequences: 98.4004%
-# first 1024 sequences: 1.5981%
-# rest  sequences:      0.087%
-# negative sequences:   0.0015%
-HEBREW_LANG_MODEL = (
-0,3,3,3,3,3,3,3,3,3,3,2,3,3,3,3,3,3,3,3,3,3,3,2,3,2,1,2,0,1,0,0,
-3,0,3,1,0,0,1,3,2,0,1,1,2,0,2,2,2,1,1,1,1,2,1,1,1,2,0,0,2,2,0,1,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,2,2,2,
-1,2,1,2,1,2,0,0,2,0,0,0,0,0,1,0,1,0,0,0,0,0,0,1,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,2,2,
-1,2,1,3,1,1,0,0,2,0,0,0,1,0,1,0,1,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,1,0,1,2,2,1,3,
-1,2,1,1,2,2,0,0,2,2,0,0,0,0,1,0,1,0,0,0,1,0,0,0,0,0,0,1,0,1,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,3,2,2,2,2,3,2,
-1,2,1,2,2,2,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,3,2,3,2,2,3,2,2,2,1,2,2,2,2,
-1,2,1,1,2,2,0,1,2,0,0,0,0,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,0,2,2,2,2,2,
-0,2,0,2,2,2,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,0,2,2,2,
-0,2,1,2,2,2,0,0,2,1,0,0,0,0,1,0,1,0,0,0,0,0,0,2,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,2,3,3,3,3,3,3,3,3,3,3,3,3,3,2,1,2,3,2,2,2,
-1,2,1,2,2,2,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,1,0,0,0,0,0,1,1,0,
-3,3,3,3,3,3,3,3,3,2,3,3,3,2,3,3,3,3,3,3,3,3,3,3,3,3,3,1,0,2,0,2,
-0,2,1,2,2,2,0,0,1,2,0,0,0,0,1,0,1,0,0,0,0,0,0,1,0,0,0,2,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,2,3,2,2,3,2,1,2,1,1,1,
-0,1,1,1,1,1,3,0,1,0,0,0,0,2,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,0,1,1,0,1,1,0,0,1,0,0,1,0,0,0,0,
-0,0,1,0,0,0,0,0,2,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,2,2,2,2,2,2,
-0,2,0,1,2,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,2,3,3,3,2,1,2,3,3,2,3,3,3,3,2,3,2,1,2,0,2,1,2,
-0,2,0,2,2,2,0,0,1,2,0,0,0,0,1,0,1,0,0,0,0,0,0,0,0,0,0,1,0,0,1,0,
-3,3,3,3,3,3,3,3,3,2,3,3,3,1,2,2,3,3,2,3,2,3,2,2,3,1,2,2,0,2,2,2,
-0,2,1,2,2,2,0,0,1,2,0,0,0,0,1,0,0,0,0,0,1,0,0,1,0,0,0,1,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,3,3,2,3,3,2,2,2,3,3,3,3,1,3,2,2,2,
-0,2,0,1,2,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,2,3,3,3,2,3,2,2,2,1,2,2,0,2,2,2,2,
-0,2,0,2,2,2,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,2,3,3,3,1,3,2,3,3,2,3,3,2,2,1,2,2,2,2,2,2,
-0,2,1,2,1,2,0,0,1,0,0,0,0,0,1,0,0,0,0,0,1,0,0,1,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,2,3,2,3,3,2,3,3,3,3,2,3,2,3,3,3,3,3,2,2,2,2,2,2,2,1,
-0,2,0,1,2,1,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,2,1,2,3,3,3,3,3,3,3,2,3,2,3,2,1,2,3,0,2,1,2,2,
-0,2,1,1,2,1,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,2,0,
-3,3,3,3,3,3,3,3,3,2,3,3,3,3,2,1,3,1,2,2,2,1,2,3,3,1,2,1,2,2,2,2,
-0,1,1,1,1,1,0,0,0,0,0,0,0,0,1,0,0,0,0,0,1,0,0,2,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,0,2,3,3,3,1,3,3,3,1,2,2,2,2,1,1,2,2,2,2,2,2,
-0,2,0,1,1,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,2,3,3,3,2,2,3,3,3,2,1,2,3,2,3,2,2,2,2,1,2,1,1,1,2,2,
-0,2,1,1,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,0,1,0,0,0,1,0,0,0,0,0,
-1,0,1,0,0,0,0,0,2,0,0,0,0,0,1,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,2,3,3,2,3,1,2,2,2,2,3,2,3,1,1,2,2,1,2,2,1,1,0,2,2,2,2,
-0,1,0,1,2,2,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,1,0,
-3,0,0,1,1,0,1,0,0,1,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,2,2,0,
-0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,1,0,1,0,1,1,0,1,1,0,0,0,1,1,0,1,1,1,0,0,0,0,0,0,1,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,0,0,1,1,0,1,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,
-3,2,2,1,2,2,2,2,2,2,2,1,2,2,1,2,2,1,1,1,1,1,1,1,1,2,1,1,0,3,3,3,
-0,3,0,2,2,2,2,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-2,2,2,3,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,1,2,2,1,2,2,2,1,1,1,2,0,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,2,2,2,2,2,2,2,2,2,2,1,2,2,2,2,2,2,2,2,2,2,2,0,2,2,0,0,0,0,0,0,
-0,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,3,1,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,2,1,2,1,0,2,1,0,
-0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,1,1,1,1,1,1,1,1,1,0,0,1,1,1,1,0,1,1,1,1,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,
-0,3,1,1,2,2,2,2,2,1,2,2,2,1,1,2,2,2,2,2,2,2,1,2,2,1,0,1,1,1,1,0,
-0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,2,1,1,1,1,2,1,1,2,1,0,1,1,1,1,1,1,1,1,1,1,1,0,1,0,0,0,0,0,0,0,
-0,0,2,0,0,0,0,0,0,0,0,1,1,0,0,0,0,1,1,0,0,1,1,0,0,0,0,0,0,1,0,0,
-2,1,1,2,2,2,2,2,2,2,2,2,2,2,1,2,2,2,2,2,1,2,1,2,1,1,1,1,0,0,0,0,
-0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,2,1,2,2,2,2,2,2,2,2,2,2,1,2,1,2,1,1,2,1,1,1,2,1,2,1,2,0,1,0,1,
-0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,3,1,2,2,2,1,2,2,2,2,2,2,2,2,1,2,1,1,1,1,1,1,2,1,2,1,1,0,1,0,1,
-0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,1,2,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,2,2,
-0,2,0,1,2,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,0,0,0,1,0,0,0,0,0,0,0,0,0,0,1,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,1,1,1,1,1,1,1,0,1,1,0,1,0,0,1,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,2,0,1,1,1,0,1,0,0,0,1,1,0,1,1,0,0,0,0,0,1,1,0,0,
-0,1,1,1,2,1,2,2,2,0,2,0,2,0,1,1,2,1,1,1,1,2,1,0,1,1,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,1,0,0,0,0,0,1,0,1,2,2,0,1,0,0,1,1,2,2,1,2,0,2,0,0,0,1,2,0,1,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,2,0,2,1,2,0,2,0,0,1,1,1,1,1,1,0,1,0,0,0,1,0,0,1,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,1,0,0,0,0,0,1,0,2,1,1,0,1,0,0,1,1,1,2,2,0,0,1,0,0,0,1,0,0,1,
-1,1,2,1,0,1,1,1,0,1,0,1,1,1,1,0,0,0,1,0,1,0,0,0,0,0,0,0,0,2,2,1,
-0,2,0,1,2,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,1,0,0,1,0,1,1,1,1,0,0,0,0,0,1,0,0,0,0,1,1,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,1,1,1,1,1,1,1,1,2,1,0,1,1,1,1,1,1,1,1,1,1,1,0,1,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,1,1,0,0,0,0,1,1,1,0,1,1,0,1,0,0,0,1,1,0,1,
-2,0,1,0,1,0,1,0,0,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,1,1,1,0,1,0,0,1,1,2,1,1,2,0,1,0,0,0,1,1,0,1,
-1,0,0,1,0,0,1,0,0,0,1,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,1,1,2,0,1,0,0,0,0,2,1,1,2,0,2,0,0,0,1,1,0,1,
-1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,2,1,1,0,1,0,0,2,2,1,2,1,1,0,1,0,0,0,1,1,0,1,
-2,0,1,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,2,2,0,0,0,0,0,1,1,0,1,0,0,1,0,0,0,0,1,0,1,
-1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,2,2,0,0,0,0,2,1,1,1,0,2,1,1,0,0,0,2,1,0,1,
-1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,1,1,2,0,1,0,0,1,1,0,2,1,1,0,1,0,0,0,1,1,0,1,
-2,2,1,1,1,0,1,1,0,1,1,0,1,0,0,0,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,2,1,1,0,1,0,0,1,1,0,1,2,1,0,2,0,0,0,1,1,0,1,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,
-0,1,0,0,2,0,2,1,1,0,1,0,1,0,0,1,0,0,0,0,1,0,0,0,1,0,0,0,0,0,1,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,1,0,0,1,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,1,0,1,1,2,0,1,0,0,1,1,1,0,1,0,0,1,0,0,0,1,0,0,1,
-1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,0,0,0,0,0,1,0,1,1,0,0,1,0,0,2,1,1,1,1,1,0,1,0,0,0,0,1,0,1,
-0,1,1,1,2,1,1,1,1,0,1,1,1,1,1,1,1,1,1,1,1,1,0,1,1,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,1,2,1,0,0,0,0,0,1,1,1,1,1,0,1,0,0,0,1,1,0,0,
-)
-
-Win1255HebrewModel = {
-  'char_to_order_map': WIN1255_CHAR_TO_ORDER_MAP,
-  'precedence_matrix': HEBREW_LANG_MODEL,
-  'typical_positive_ratio': 0.984004,
-  'keep_english_letter': False,
-  'charset_name': "windows-1255",
-  'language': 'Hebrew',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langhungarianmodel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langhungarianmodel.py
deleted file mode 100644
index bb7c095..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langhungarianmodel.py
+++ /dev/null
@@ -1,225 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# 255: Control characters that usually does not exist in any text
-# 254: Carriage/Return
-# 253: symbol (punctuation) that does not belong to word
-# 252: 0 - 9
-
-# Character Mapping Table:
-Latin2_HungarianCharToOrderMap = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253, 28, 40, 54, 45, 32, 50, 49, 38, 39, 53, 36, 41, 34, 35, 47,
- 46, 71, 43, 33, 37, 57, 48, 64, 68, 55, 52,253,253,253,253,253,
-253,  2, 18, 26, 17,  1, 27, 12, 20,  9, 22,  7,  6, 13,  4,  8,
- 23, 67, 10,  5,  3, 21, 19, 65, 62, 16, 11,253,253,253,253,253,
-159,160,161,162,163,164,165,166,167,168,169,170,171,172,173,174,
-175,176,177,178,179,180,181,182,183,184,185,186,187,188,189,190,
-191,192,193,194,195,196,197, 75,198,199,200,201,202,203,204,205,
- 79,206,207,208,209,210,211,212,213,214,215,216,217,218,219,220,
-221, 51, 81,222, 78,223,224,225,226, 44,227,228,229, 61,230,231,
-232,233,234, 58,235, 66, 59,236,237,238, 60, 69, 63,239,240,241,
- 82, 14, 74,242, 70, 80,243, 72,244, 15, 83, 77, 84, 30, 76, 85,
-245,246,247, 25, 73, 42, 24,248,249,250, 31, 56, 29,251,252,253,
-)
-
-win1250HungarianCharToOrderMap = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253, 28, 40, 54, 45, 32, 50, 49, 38, 39, 53, 36, 41, 34, 35, 47,
- 46, 72, 43, 33, 37, 57, 48, 64, 68, 55, 52,253,253,253,253,253,
-253,  2, 18, 26, 17,  1, 27, 12, 20,  9, 22,  7,  6, 13,  4,  8,
- 23, 67, 10,  5,  3, 21, 19, 65, 62, 16, 11,253,253,253,253,253,
-161,162,163,164,165,166,167,168,169,170,171,172,173,174,175,176,
-177,178,179,180, 78,181, 69,182,183,184,185,186,187,188,189,190,
-191,192,193,194,195,196,197, 76,198,199,200,201,202,203,204,205,
- 81,206,207,208,209,210,211,212,213,214,215,216,217,218,219,220,
-221, 51, 83,222, 80,223,224,225,226, 44,227,228,229, 61,230,231,
-232,233,234, 58,235, 66, 59,236,237,238, 60, 70, 63,239,240,241,
- 84, 14, 75,242, 71, 82,243, 73,244, 15, 85, 79, 86, 30, 77, 87,
-245,246,247, 25, 74, 42, 24,248,249,250, 31, 56, 29,251,252,253,
-)
-
-# Model Table:
-# total sequences: 100%
-# first 512 sequences: 94.7368%
-# first 1024 sequences:5.2623%
-# rest  sequences:     0.8894%
-# negative sequences:  0.0009%
-HungarianLangModel = (
-0,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,1,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,
-3,3,3,3,3,3,3,3,3,3,2,3,3,3,3,3,3,3,3,2,2,3,3,1,1,2,2,2,2,2,1,2,
-3,2,2,3,3,3,3,3,2,3,3,3,3,3,3,1,2,3,3,3,3,2,3,3,1,1,3,3,0,1,1,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,
-3,2,1,3,3,3,3,3,2,3,3,3,3,3,1,1,2,3,3,3,3,3,3,3,1,1,3,2,0,1,1,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,1,1,2,3,3,3,1,3,3,3,3,3,1,3,3,2,2,0,3,2,3,
-0,0,0,0,0,0,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,3,3,3,2,3,3,2,3,3,3,3,3,2,3,3,2,2,3,2,3,2,0,3,2,2,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,1,0,
-3,3,3,3,3,3,2,3,3,3,3,3,2,3,3,3,1,2,3,2,2,3,1,2,3,3,2,2,0,3,3,3,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,2,2,3,3,3,3,3,3,2,3,3,3,3,2,3,3,3,3,0,2,3,2,
-0,0,0,1,1,0,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,3,3,3,1,1,1,3,3,2,1,3,2,2,3,2,1,3,2,2,1,0,3,3,1,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,2,2,3,3,3,3,3,1,2,3,3,3,3,1,2,1,3,3,3,3,2,2,3,1,1,3,2,0,1,1,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,2,2,3,3,3,3,3,2,1,3,3,3,3,3,2,2,1,3,3,3,0,1,1,2,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,1,0,
-3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,3,2,3,3,3,2,3,3,2,3,3,3,2,0,3,2,3,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,1,0,
-3,3,3,3,3,3,2,3,3,3,2,3,2,3,3,3,1,3,2,2,2,3,1,1,3,3,1,1,0,3,3,2,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,2,3,3,3,2,3,2,3,3,3,2,3,3,3,3,3,1,2,3,2,2,0,2,2,2,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,2,2,2,3,1,3,3,2,2,1,3,3,3,1,1,3,1,2,3,2,3,2,2,2,1,0,2,2,2,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,
-3,1,1,3,3,3,3,3,1,2,3,3,3,3,1,2,1,3,3,3,2,2,3,2,1,0,3,2,0,1,1,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,1,3,3,3,3,3,1,2,3,3,3,3,1,1,0,3,3,3,3,0,2,3,0,0,2,1,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,2,2,3,3,2,2,2,2,3,3,0,1,2,3,2,3,2,2,3,2,1,2,0,2,2,2,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,
-3,3,3,3,3,3,1,2,3,3,3,2,1,2,3,3,2,2,2,3,2,3,3,1,3,3,1,1,0,2,3,2,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,1,2,2,2,2,3,3,3,1,1,1,3,3,1,1,3,1,1,3,2,1,2,3,1,1,0,2,2,2,
-0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,2,1,2,1,1,3,3,1,1,1,1,3,3,1,1,2,2,1,2,1,1,2,2,1,1,0,2,2,1,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,1,1,2,1,1,3,3,1,0,1,1,3,3,2,0,1,1,2,3,1,0,2,2,1,0,0,1,3,2,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,2,1,3,3,3,3,3,1,2,3,2,3,3,2,1,1,3,2,3,2,1,2,2,0,1,2,1,0,0,1,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,
-3,3,3,3,2,2,2,2,3,1,2,2,1,1,3,3,0,3,2,1,2,3,2,1,3,3,1,1,0,2,1,3,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,3,3,2,2,2,3,2,3,3,3,2,1,1,3,3,1,1,1,2,2,3,2,3,2,2,2,1,0,2,2,1,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-1,0,0,3,3,3,3,3,0,0,3,3,2,3,0,0,0,2,3,3,1,0,1,2,0,0,1,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,2,3,3,3,3,3,1,2,3,3,2,2,1,1,0,3,3,2,2,1,2,2,1,0,2,2,0,1,1,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,2,2,1,3,1,2,3,3,2,2,1,1,2,2,1,1,1,1,3,2,1,1,1,1,2,1,0,1,2,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,1,0,0,0,0,0,0,0,0,0,
-2,3,3,1,1,1,1,1,3,3,3,0,1,1,3,3,1,1,1,1,1,2,2,0,3,1,1,2,0,2,1,1,
-0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,
-3,1,0,1,2,1,2,2,0,1,2,3,1,2,0,0,0,2,1,1,1,1,1,2,0,0,1,1,0,0,0,0,
-1,2,1,2,2,2,1,2,1,2,0,2,0,2,2,1,1,2,1,1,2,1,1,1,0,1,0,0,0,1,1,0,
-1,1,1,2,3,2,3,3,0,1,2,2,3,1,0,1,0,2,1,2,2,0,1,1,0,0,1,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,3,3,2,2,1,0,0,3,2,3,2,0,0,0,1,1,3,0,0,1,1,0,0,2,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,1,2,2,3,3,1,0,1,3,2,3,1,1,1,0,1,1,1,1,1,3,1,0,0,2,2,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,1,1,2,2,2,1,0,1,2,3,3,2,0,0,0,2,1,1,1,2,1,1,1,0,1,1,1,0,0,0,
-1,2,2,2,2,2,1,1,1,2,0,2,1,1,1,1,1,2,1,1,1,1,1,1,0,1,1,1,0,0,1,1,
-3,2,2,1,0,0,1,1,2,2,0,3,0,1,2,1,1,0,0,1,1,1,0,1,1,1,1,0,2,1,1,1,
-2,2,1,1,1,2,1,2,1,1,1,1,1,1,1,2,1,1,1,2,3,1,1,1,1,1,1,1,1,1,0,1,
-2,3,3,0,1,0,0,0,3,3,1,0,0,1,2,2,1,0,0,0,0,2,0,0,1,1,1,0,2,1,1,1,
-2,1,1,1,1,1,1,2,1,1,0,1,1,0,1,1,1,0,1,2,1,1,0,1,1,1,1,1,1,1,0,1,
-2,3,3,0,1,0,0,0,2,2,0,0,0,0,1,2,2,0,0,0,0,1,0,0,1,1,0,0,2,0,1,0,
-2,1,1,1,1,2,1,1,1,1,1,1,1,2,1,1,1,1,1,1,1,1,1,2,0,1,1,1,1,1,0,1,
-3,2,2,0,1,0,1,0,2,3,2,0,0,1,2,2,1,0,0,1,1,1,0,0,2,1,0,1,2,2,1,1,
-2,1,1,1,1,1,1,2,1,1,1,1,1,1,0,2,1,0,1,1,0,1,1,1,0,1,1,2,1,1,0,1,
-2,2,2,0,0,1,0,0,2,2,1,1,0,0,2,1,1,0,0,0,1,2,0,0,2,1,0,0,2,1,1,1,
-2,1,1,1,1,2,1,2,1,1,1,2,2,1,1,2,1,1,1,2,1,1,1,1,1,1,1,1,1,1,0,1,
-1,2,3,0,0,0,1,0,3,2,1,0,0,1,2,1,1,0,0,0,0,2,1,0,1,1,0,0,2,1,2,1,
-1,1,0,0,0,1,0,1,1,1,1,1,2,0,0,1,0,0,0,2,0,0,1,1,1,1,1,1,1,1,0,1,
-3,0,0,2,1,2,2,1,0,0,2,1,2,2,0,0,0,2,1,1,1,0,1,1,0,0,1,1,2,0,0,0,
-1,2,1,2,2,1,1,2,1,2,0,1,1,1,1,1,1,1,1,1,2,1,1,0,0,1,1,1,1,0,0,1,
-1,3,2,0,0,0,1,0,2,2,2,0,0,0,2,2,1,0,0,0,0,3,1,1,1,1,0,0,2,1,1,1,
-2,1,0,1,1,1,0,1,1,1,1,1,1,1,0,2,1,0,0,1,0,1,1,0,1,1,1,1,1,1,0,1,
-2,3,2,0,0,0,1,0,2,2,0,0,0,0,2,1,1,0,0,0,0,2,1,0,1,1,0,0,2,1,1,0,
-2,1,1,1,1,2,1,2,1,2,0,1,1,1,0,2,1,1,1,2,1,1,1,1,0,1,1,1,1,1,0,1,
-3,1,1,2,2,2,3,2,1,1,2,2,1,1,0,1,0,2,2,1,1,1,1,1,0,0,1,1,0,1,1,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,2,2,0,0,0,0,0,2,2,0,0,0,0,2,2,1,0,0,0,1,1,0,0,1,2,0,0,2,1,1,1,
-2,2,1,1,1,2,1,2,1,1,0,1,1,1,1,2,1,1,1,2,1,1,1,1,0,1,2,1,1,1,0,1,
-1,0,0,1,2,3,2,1,0,0,2,0,1,1,0,0,0,1,1,1,1,0,1,1,0,0,1,0,0,0,0,0,
-1,2,1,2,1,2,1,1,1,2,0,2,1,1,1,0,1,2,0,0,1,1,1,0,0,0,0,0,0,0,0,0,
-2,3,2,0,0,0,0,0,1,1,2,1,0,0,1,1,1,0,0,0,0,2,0,0,1,1,0,0,2,1,1,1,
-2,1,1,1,1,1,1,2,1,0,1,1,1,1,0,2,1,1,1,1,1,1,0,1,0,1,1,1,1,1,0,1,
-1,2,2,0,1,1,1,0,2,2,2,0,0,0,3,2,1,0,0,0,1,1,0,0,1,1,0,1,1,1,0,0,
-1,1,0,1,1,1,1,1,1,1,1,2,1,1,1,1,1,1,1,2,1,1,1,0,0,1,1,1,0,1,0,1,
-2,1,0,2,1,1,2,2,1,1,2,1,1,1,0,0,0,1,1,0,1,1,1,1,0,0,1,1,1,0,0,0,
-1,2,2,2,2,2,1,1,1,2,0,2,1,1,1,1,1,1,1,1,1,1,1,1,0,1,1,0,0,0,1,0,
-1,2,3,0,0,0,1,0,2,2,0,0,0,0,2,2,0,0,0,0,0,1,0,0,1,0,0,0,2,0,1,0,
-2,1,1,1,1,1,0,2,0,0,0,1,2,1,1,1,1,0,1,2,0,1,0,1,0,1,1,1,0,1,0,1,
-2,2,2,0,0,0,1,0,2,1,2,0,0,0,1,1,2,0,0,0,0,1,0,0,1,1,0,0,2,1,0,1,
-2,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,1,2,0,1,1,1,1,1,0,1,
-1,2,2,0,0,0,1,0,2,2,2,0,0,0,1,1,0,0,0,0,0,1,1,0,2,0,0,1,1,1,0,1,
-1,0,1,1,1,1,1,1,0,1,1,1,1,0,0,1,0,0,1,1,0,1,0,1,1,1,1,1,0,0,0,1,
-1,0,0,1,0,1,2,1,0,0,1,1,1,2,0,0,0,1,1,0,1,0,1,1,0,0,1,0,0,0,0,0,
-0,2,1,2,1,1,1,1,1,2,0,2,0,1,1,0,1,2,1,0,1,1,1,0,0,0,0,0,0,1,0,0,
-2,1,1,0,1,2,0,0,1,1,1,0,0,0,1,1,0,0,0,0,0,1,0,0,1,0,0,0,2,1,0,1,
-2,2,1,1,1,1,1,2,1,1,0,1,1,1,1,2,1,1,1,2,1,1,0,1,0,1,1,1,1,1,0,1,
-1,2,2,0,0,0,0,0,1,1,0,0,0,0,2,1,0,0,0,0,0,2,0,0,2,2,0,0,2,0,0,1,
-2,1,1,1,1,1,1,1,0,1,1,0,1,1,0,1,0,0,0,1,1,1,1,0,0,1,1,1,1,0,0,1,
-1,1,2,0,0,3,1,0,2,1,1,1,0,0,1,1,1,0,0,0,1,1,0,0,0,1,0,0,1,0,1,0,
-1,2,1,0,1,1,1,2,1,1,0,1,1,1,1,1,0,0,0,1,1,1,1,1,0,1,0,0,0,1,0,0,
-2,1,1,0,0,0,0,0,1,0,0,0,0,0,0,0,0,1,0,1,0,0,0,1,0,0,0,0,2,0,0,0,
-2,1,1,1,1,1,1,1,1,1,0,1,1,1,1,1,1,1,1,1,2,1,1,0,0,1,1,1,1,1,0,1,
-2,1,1,1,2,1,1,1,0,1,1,2,1,0,0,0,0,1,1,1,1,0,1,0,0,0,0,1,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,1,0,1,1,1,1,1,0,0,1,1,2,1,0,0,0,1,1,0,0,0,1,1,0,0,1,0,1,0,0,0,
-1,2,1,1,1,1,1,1,1,1,0,1,0,1,1,1,1,1,1,0,1,1,1,0,0,0,0,0,0,1,0,0,
-2,0,0,0,1,1,1,1,0,0,1,1,0,0,0,0,0,1,1,1,2,0,0,1,0,0,1,0,1,0,0,0,
-0,1,1,1,1,1,1,1,1,2,0,1,1,1,1,0,1,1,1,0,1,1,1,0,0,0,0,0,0,0,0,0,
-1,0,0,1,1,1,1,1,0,0,2,1,0,1,0,0,0,1,0,1,0,0,0,0,0,0,1,0,0,0,0,0,
-0,1,1,1,1,1,1,0,1,1,0,1,0,1,1,0,1,1,0,0,1,1,1,0,0,0,0,0,0,0,0,0,
-1,0,0,1,1,1,0,0,0,0,1,0,2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-0,1,1,1,1,1,0,0,1,1,0,1,0,1,0,0,1,1,1,0,1,1,1,0,0,0,0,0,0,0,0,0,
-0,0,0,1,0,0,0,0,0,0,1,1,2,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,1,1,1,0,1,0,0,1,1,0,1,0,1,1,0,1,1,1,0,1,1,1,0,0,0,0,0,0,0,0,0,
-2,1,1,1,1,1,1,1,1,1,1,0,0,1,1,1,0,0,1,0,0,1,0,1,0,1,1,1,0,0,1,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,0,1,1,1,1,0,0,0,1,1,1,0,0,0,0,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,
-0,1,1,1,1,1,1,0,1,1,0,1,0,1,0,0,1,1,0,0,1,1,0,0,0,0,0,0,0,0,0,0,
-)
-
-Latin2HungarianModel = {
-  'char_to_order_map': Latin2_HungarianCharToOrderMap,
-  'precedence_matrix': HungarianLangModel,
-  'typical_positive_ratio': 0.947368,
-  'keep_english_letter': True,
-  'charset_name': "ISO-8859-2",
-  'language': 'Hungarian',
-}
-
-Win1250HungarianModel = {
-  'char_to_order_map': win1250HungarianCharToOrderMap,
-  'precedence_matrix': HungarianLangModel,
-  'typical_positive_ratio': 0.947368,
-  'keep_english_letter': True,
-  'charset_name': "windows-1250",
-  'language': 'Hungarian',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langthaimodel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langthaimodel.py
deleted file mode 100644
index 15f94c2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langthaimodel.py
+++ /dev/null
@@ -1,199 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# 255: Control characters that usually does not exist in any text
-# 254: Carriage/Return
-# 253: symbol (punctuation) that does not belong to word
-# 252: 0 - 9
-
-# The following result for thai was collected from a limited sample (1M).
-
-# Character Mapping Table:
-TIS620CharToOrderMap = (
-255,255,255,255,255,255,255,255,255,255,254,255,255,254,255,255,  # 00
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,  # 10
-253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,253,  # 20
-252,252,252,252,252,252,252,252,252,252,253,253,253,253,253,253,  # 30
-253,182,106,107,100,183,184,185,101, 94,186,187,108,109,110,111,  # 40
-188,189,190, 89, 95,112,113,191,192,193,194,253,253,253,253,253,  # 50
-253, 64, 72, 73,114, 74,115,116,102, 81,201,117, 90,103, 78, 82,  # 60
- 96,202, 91, 79, 84,104,105, 97, 98, 92,203,253,253,253,253,253,  # 70
-209,210,211,212,213, 88,214,215,216,217,218,219,220,118,221,222,
-223,224, 99, 85, 83,225,226,227,228,229,230,231,232,233,234,235,
-236,  5, 30,237, 24,238, 75,  8, 26, 52, 34, 51,119, 47, 58, 57,
- 49, 53, 55, 43, 20, 19, 44, 14, 48,  3, 17, 25, 39, 62, 31, 54,
- 45,  9, 16,  2, 61, 15,239, 12, 42, 46, 18, 21, 76,  4, 66, 63,
- 22, 10,  1, 36, 23, 13, 40, 27, 32, 35, 86,240,241,242,243,244,
- 11, 28, 41, 29, 33,245, 50, 37,  6,  7, 67, 77, 38, 93,246,247,
- 68, 56, 59, 65, 69, 60, 70, 80, 71, 87,248,249,250,251,252,253,
-)
-
-# Model Table:
-# total sequences: 100%
-# first 512 sequences: 92.6386%
-# first 1024 sequences:7.3177%
-# rest  sequences:     1.0230%
-# negative sequences:  0.0436%
-ThaiLangModel = (
-0,1,3,3,3,3,0,0,3,3,0,3,3,0,3,3,3,3,3,3,3,3,0,0,3,3,3,0,3,3,3,3,
-0,3,3,0,0,0,1,3,0,3,3,2,3,3,0,1,2,3,3,3,3,0,2,0,2,0,0,3,2,1,2,2,
-3,0,3,3,2,3,0,0,3,3,0,3,3,0,3,3,3,3,3,3,3,3,3,0,3,2,3,0,2,2,2,3,
-0,2,3,0,0,0,0,1,0,1,2,3,1,1,3,2,2,0,1,1,0,0,1,0,0,0,0,0,0,0,1,1,
-3,3,3,2,3,3,3,3,3,3,3,3,3,3,3,2,2,2,2,2,2,2,3,3,2,3,2,3,3,2,2,2,
-3,1,2,3,0,3,3,2,2,1,2,3,3,1,2,0,1,3,0,1,0,0,1,0,0,0,0,0,0,0,1,1,
-3,3,2,2,3,3,3,3,1,2,3,3,3,3,3,2,2,2,2,3,3,2,2,3,3,2,2,3,2,3,2,2,
-3,3,1,2,3,1,2,2,3,3,1,0,2,1,0,0,3,1,2,1,0,0,1,0,0,0,0,0,0,1,0,1,
-3,3,3,3,3,3,2,2,3,3,3,3,2,3,2,2,3,3,2,2,3,2,2,2,2,1,1,3,1,2,1,1,
-3,2,1,0,2,1,0,1,0,1,1,0,1,1,0,0,1,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,
-3,3,3,2,3,2,3,3,2,2,3,2,3,3,2,3,1,1,2,3,2,2,2,3,2,2,2,2,2,1,2,1,
-2,2,1,1,3,3,2,1,0,1,2,2,0,1,3,0,0,0,1,1,0,0,0,0,0,2,3,0,0,2,1,1,
-3,3,2,3,3,2,0,0,3,3,0,3,3,0,2,2,3,1,2,2,1,1,1,0,2,2,2,0,2,2,1,1,
-0,2,1,0,2,0,0,2,0,1,0,0,1,0,0,0,1,1,1,1,0,0,0,0,0,0,0,0,0,0,1,0,
-3,3,2,3,3,2,0,0,3,3,0,2,3,0,2,1,2,2,2,2,1,2,0,0,2,2,2,0,2,2,1,1,
-0,2,1,0,2,0,0,2,0,1,1,0,1,0,0,0,0,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,
-3,3,2,3,2,3,2,0,2,2,1,3,2,1,3,2,1,2,3,2,2,3,0,2,3,2,2,1,2,2,2,2,
-1,2,2,0,0,0,0,2,0,1,2,0,1,1,1,0,1,0,3,1,1,0,0,0,0,0,0,0,0,0,1,0,
-3,3,2,3,3,2,3,2,2,2,3,2,2,3,2,2,1,2,3,2,2,3,1,3,2,2,2,3,2,2,2,3,
-3,2,1,3,0,1,1,1,0,2,1,1,1,1,1,0,1,0,1,1,0,0,0,0,0,0,0,0,0,2,0,0,
-1,0,0,3,0,3,3,3,3,3,0,0,3,0,2,2,3,3,3,3,3,0,0,0,1,1,3,0,0,0,0,2,
-0,0,1,0,0,0,0,0,0,0,2,3,0,0,0,3,0,2,0,0,0,0,0,3,0,0,0,0,0,0,0,0,
-2,0,3,3,3,3,0,0,2,3,0,0,3,0,3,3,2,3,3,3,3,3,0,0,3,3,3,0,0,0,3,3,
-0,0,3,0,0,0,0,2,0,0,2,1,1,3,0,0,1,0,0,2,3,0,1,0,0,0,0,0,0,0,1,0,
-3,3,3,3,2,3,3,3,3,3,3,3,1,2,1,3,3,2,2,1,2,2,2,3,1,1,2,0,2,1,2,1,
-2,2,1,0,0,0,1,1,0,1,0,1,1,0,0,0,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,
-3,0,2,1,2,3,3,3,0,2,0,2,2,0,2,1,3,2,2,1,2,1,0,0,2,2,1,0,2,1,2,2,
-0,1,1,0,0,0,0,1,0,1,1,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,2,1,3,3,1,1,3,0,2,3,1,1,3,2,1,1,2,0,2,2,3,2,1,1,1,1,1,2,
-3,0,0,1,3,1,2,1,2,0,3,0,0,0,1,0,3,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,
-3,3,1,1,3,2,3,3,3,1,3,2,1,3,2,1,3,2,2,2,2,1,3,3,1,2,1,3,1,2,3,0,
-2,1,1,3,2,2,2,1,2,1,0,0,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,
-3,3,2,3,2,3,3,2,3,2,3,2,3,3,2,1,0,3,2,2,2,1,2,2,2,1,2,2,1,2,1,1,
-2,2,2,3,0,1,3,1,1,1,1,0,1,1,0,2,1,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,2,3,2,2,1,1,3,2,3,2,3,2,0,3,2,2,1,2,0,2,2,2,1,2,2,2,2,1,
-3,2,1,2,2,1,0,2,0,1,0,0,1,1,0,0,0,0,0,1,1,0,1,0,0,0,0,0,0,0,0,1,
-3,3,3,3,3,2,3,1,2,3,3,2,2,3,0,1,1,2,0,3,3,2,2,3,0,1,1,3,0,0,0,0,
-3,1,0,3,3,0,2,0,2,1,0,0,3,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,2,3,2,3,3,0,1,3,1,1,2,1,2,1,1,3,1,1,0,2,3,1,1,1,1,1,1,1,1,
-3,1,1,2,2,2,2,1,1,1,0,0,2,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-3,2,2,1,1,2,1,3,3,2,3,2,2,3,2,2,3,1,2,2,1,2,0,3,2,1,2,2,2,2,2,1,
-3,2,1,2,2,2,1,1,1,1,0,0,1,1,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,3,3,3,3,1,3,3,0,2,1,0,3,2,0,0,3,1,0,1,1,0,1,0,0,0,0,0,1,
-1,0,0,1,0,3,2,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,2,2,2,3,0,0,1,3,0,3,2,0,3,2,2,3,3,3,3,3,1,0,2,2,2,0,2,2,1,2,
-0,2,3,0,0,0,0,1,0,1,0,0,1,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,
-3,0,2,3,1,3,3,2,3,3,0,3,3,0,3,2,2,3,2,3,3,3,0,0,2,2,3,0,1,1,1,3,
-0,0,3,0,0,0,2,2,0,1,3,0,1,2,2,2,3,0,0,0,0,0,1,0,0,0,0,0,0,0,0,1,
-3,2,3,3,2,0,3,3,2,2,3,1,3,2,1,3,2,0,1,2,2,0,2,3,2,1,0,3,0,0,0,0,
-3,0,0,2,3,1,3,0,0,3,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,1,3,2,2,2,1,2,0,1,3,1,1,3,1,3,0,0,2,1,1,1,1,2,1,1,1,0,2,1,0,1,
-1,2,0,0,0,3,1,1,0,0,0,0,1,0,1,0,0,1,0,1,0,0,0,0,0,3,1,0,0,0,1,0,
-3,3,3,3,2,2,2,2,2,1,3,1,1,1,2,0,1,1,2,1,2,1,3,2,0,0,3,1,1,1,1,1,
-3,1,0,2,3,0,0,0,3,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,2,3,0,3,3,0,2,0,0,0,0,0,0,0,3,0,0,1,0,0,0,0,0,0,0,0,0,0,0,
-0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,2,3,1,3,0,0,1,2,0,0,2,0,3,3,2,3,3,3,2,3,0,0,2,2,2,0,0,0,2,2,
-0,0,1,0,0,0,0,3,0,0,0,0,2,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-0,0,0,3,0,2,0,0,0,0,0,0,0,0,0,0,1,2,3,1,3,3,0,0,1,0,3,0,0,0,0,0,
-0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,1,2,3,1,2,3,1,0,3,0,2,2,1,0,2,1,1,2,0,1,0,0,1,1,1,1,0,1,0,0,
-1,0,0,0,0,1,1,0,3,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,3,3,2,1,0,1,1,1,3,1,2,2,2,2,2,2,1,1,1,1,0,3,1,0,1,3,1,1,1,1,
-1,1,0,2,0,1,3,1,1,0,0,1,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,2,0,1,
-3,0,2,2,1,3,3,2,3,3,0,1,1,0,2,2,1,2,1,3,3,1,0,0,3,2,0,0,0,0,2,1,
-0,1,0,0,0,0,1,2,0,1,1,3,1,1,2,2,1,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,
-0,0,3,0,0,1,0,0,0,3,0,0,3,0,3,1,0,1,1,1,3,2,0,0,0,3,0,0,0,0,2,0,
-0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,2,0,0,0,0,0,0,0,0,0,
-3,3,1,3,2,1,3,3,1,2,2,0,1,2,1,0,1,2,0,0,0,0,0,3,0,0,0,3,0,0,0,0,
-3,0,0,1,1,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,1,2,0,3,3,3,2,2,0,1,1,0,1,3,0,0,0,2,2,0,0,0,0,3,1,0,1,0,0,0,
-0,0,0,0,0,0,0,0,0,1,0,1,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,2,3,1,2,0,0,2,1,0,3,1,0,1,2,0,1,1,1,1,3,0,0,3,1,1,0,2,2,1,1,
-0,2,0,0,0,0,0,1,0,1,0,0,1,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,0,3,1,2,0,0,2,2,0,1,2,0,1,0,1,3,1,2,1,0,0,0,2,0,3,0,0,0,1,0,
-0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,1,1,2,2,0,0,0,2,0,2,1,0,1,1,0,1,1,1,2,1,0,0,1,1,1,0,2,1,1,1,
-0,1,1,0,0,0,0,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,1,0,1,
-0,0,0,2,0,1,3,1,1,1,1,0,0,0,0,3,2,0,1,0,0,0,1,2,0,0,0,1,0,0,0,0,
-0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,3,3,3,3,1,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,0,2,3,2,2,0,0,0,1,0,0,0,0,2,3,2,1,2,2,3,0,0,0,2,3,1,0,0,0,1,1,
-0,0,1,0,0,0,0,0,0,0,1,0,0,1,0,0,0,0,0,1,1,0,1,0,0,0,0,0,0,0,0,0,
-3,3,2,2,0,1,0,0,0,0,2,0,2,0,1,0,0,0,1,1,0,0,0,2,1,0,1,0,1,1,0,0,
-0,1,0,2,0,0,1,0,3,0,1,0,0,0,2,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,1,0,0,1,0,0,0,0,0,1,1,2,0,0,0,0,1,0,0,1,3,1,0,0,0,0,1,1,0,0,
-0,1,0,0,0,0,3,0,0,0,0,0,0,3,0,0,0,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,
-3,3,1,1,1,1,2,3,0,0,2,1,1,1,1,1,0,2,1,1,0,0,0,2,1,0,1,2,1,1,0,1,
-2,1,0,3,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,3,1,0,0,0,0,0,0,0,3,0,0,0,3,0,0,0,0,0,0,0,0,1,1,0,0,0,0,0,0,1,
-0,0,0,2,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,3,2,0,0,0,0,0,0,1,2,1,0,1,1,0,2,0,0,1,0,0,2,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,2,0,0,0,1,3,0,1,0,0,0,2,0,0,0,0,0,0,0,1,2,0,0,0,0,0,
-3,3,0,0,1,1,2,0,0,1,2,1,0,1,1,1,0,1,1,0,0,2,1,1,0,1,0,0,1,1,1,0,
-0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,3,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,2,2,1,0,0,0,0,1,0,0,0,0,3,0,0,0,0,0,0,0,0,0,3,0,0,0,0,0,0,0,0,
-2,0,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,3,0,0,1,1,0,0,0,2,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,1,0,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-1,1,0,1,2,0,1,2,0,0,1,1,0,2,0,1,0,0,1,0,0,0,0,1,0,0,0,2,0,0,0,0,
-1,0,0,1,0,1,1,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,1,0,0,0,0,0,0,0,1,1,0,1,1,0,2,1,3,0,0,0,0,1,1,0,0,0,0,0,0,0,3,
-1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,0,1,0,1,0,0,2,0,0,2,0,0,1,1,2,0,0,1,1,0,0,0,1,0,0,0,1,1,0,0,0,
-1,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,
-1,0,0,3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,1,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-3,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,1,1,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,0,0,0,0,0,3,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,0,0,0,0,2,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,1,0,1,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,1,3,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,1,0,0,0,0,
-1,0,0,0,0,0,0,0,0,1,0,0,0,0,2,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,1,1,0,0,2,1,0,0,1,0,0,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-)
-
-TIS620ThaiModel = {
-  'char_to_order_map': TIS620CharToOrderMap,
-  'precedence_matrix': ThaiLangModel,
-  'typical_positive_ratio': 0.926386,
-  'keep_english_letter': False,
-  'charset_name': "TIS-620",
-  'language': 'Thai',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langturkishmodel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langturkishmodel.py
deleted file mode 100644
index a427a45..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/langturkishmodel.py
+++ /dev/null
@@ -1,193 +0,0 @@
-# -*- coding: utf-8 -*-
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Communicator client code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Özgür Baskın - Turkish Language Model
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-# 255: Control characters that usually does not exist in any text
-# 254: Carriage/Return
-# 253: symbol (punctuation) that does not belong to word
-# 252: 0 - 9
-
-# Character Mapping Table:
-Latin5_TurkishCharToOrderMap = (
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,
-255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,255,
-255, 23, 37, 47, 39, 29, 52, 36, 45, 53, 60, 16, 49, 20, 46, 42,
- 48, 69, 44, 35, 31, 51, 38, 62, 65, 43, 56,255,255,255,255,255,
-255,  1, 21, 28, 12,  2, 18, 27, 25,  3, 24, 10,  5, 13,  4, 15,
- 26, 64,  7,  8,  9, 14, 32, 57, 58, 11, 22,255,255,255,255,255,
-180,179,178,177,176,175,174,173,172,171,170,169,168,167,166,165,
-164,163,162,161,160,159,101,158,157,156,155,154,153,152,151,106,
-150,149,148,147,146,145,144,100,143,142,141,140,139,138,137,136,
- 94, 80, 93,135,105,134,133, 63,132,131,130,129,128,127,126,125,
-124,104, 73, 99, 79, 85,123, 54,122, 98, 92,121,120, 91,103,119,
- 68,118,117, 97,116,115, 50, 90,114,113,112,111, 55, 41, 40, 86,
- 89, 70, 59, 78, 71, 82, 88, 33, 77, 66, 84, 83,110, 75, 61, 96,
- 30, 67,109, 74, 87,102, 34, 95, 81,108, 76, 72, 17,  6, 19,107,
-)
-
-TurkishLangModel = (
-3,2,3,3,3,1,3,3,3,3,3,3,3,3,2,1,1,3,3,1,3,3,0,3,3,3,3,3,0,3,1,3,
-3,2,1,0,0,1,1,0,0,0,1,0,0,1,1,1,1,0,0,0,0,0,0,0,2,2,0,0,1,0,0,1,
-3,2,2,3,3,0,3,3,3,3,3,3,3,2,3,1,0,3,3,1,3,3,0,3,3,3,3,3,0,3,0,3,
-3,1,1,0,1,0,1,0,0,0,0,0,0,1,1,1,1,0,0,0,0,0,0,0,2,2,0,0,0,1,0,1,
-3,3,2,3,3,0,3,3,3,3,3,3,3,2,3,1,1,3,3,0,3,3,1,2,3,3,3,3,0,3,0,3,
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-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,1,0,0,0,0,1,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,1,0,0,0,0,0,0,0,0,0,0,2,2,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,
-)
-
-Latin5TurkishModel = {
-  'char_to_order_map': Latin5_TurkishCharToOrderMap,
-  'precedence_matrix': TurkishLangModel,
-  'typical_positive_ratio': 0.970290,
-  'keep_english_letter': True,
-  'charset_name': "ISO-8859-9",
-  'language': 'Turkish',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/latin1prober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/latin1prober.py
deleted file mode 100644
index 7d1e8c2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/latin1prober.py
+++ /dev/null
@@ -1,145 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 2001
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetprober import CharSetProber
-from .enums import ProbingState
-
-FREQ_CAT_NUM = 4
-
-UDF = 0  # undefined
-OTH = 1  # other
-ASC = 2  # ascii capital letter
-ASS = 3  # ascii small letter
-ACV = 4  # accent capital vowel
-ACO = 5  # accent capital other
-ASV = 6  # accent small vowel
-ASO = 7  # accent small other
-CLASS_NUM = 8  # total classes
-
-Latin1_CharToClass = (
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 00 - 07
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 08 - 0F
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 10 - 17
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 18 - 1F
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 20 - 27
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 28 - 2F
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 30 - 37
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 38 - 3F
-    OTH, ASC, ASC, ASC, ASC, ASC, ASC, ASC,   # 40 - 47
-    ASC, ASC, ASC, ASC, ASC, ASC, ASC, ASC,   # 48 - 4F
-    ASC, ASC, ASC, ASC, ASC, ASC, ASC, ASC,   # 50 - 57
-    ASC, ASC, ASC, OTH, OTH, OTH, OTH, OTH,   # 58 - 5F
-    OTH, ASS, ASS, ASS, ASS, ASS, ASS, ASS,   # 60 - 67
-    ASS, ASS, ASS, ASS, ASS, ASS, ASS, ASS,   # 68 - 6F
-    ASS, ASS, ASS, ASS, ASS, ASS, ASS, ASS,   # 70 - 77
-    ASS, ASS, ASS, OTH, OTH, OTH, OTH, OTH,   # 78 - 7F
-    OTH, UDF, OTH, ASO, OTH, OTH, OTH, OTH,   # 80 - 87
-    OTH, OTH, ACO, OTH, ACO, UDF, ACO, UDF,   # 88 - 8F
-    UDF, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # 90 - 97
-    OTH, OTH, ASO, OTH, ASO, UDF, ASO, ACO,   # 98 - 9F
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # A0 - A7
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # A8 - AF
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # B0 - B7
-    OTH, OTH, OTH, OTH, OTH, OTH, OTH, OTH,   # B8 - BF
-    ACV, ACV, ACV, ACV, ACV, ACV, ACO, ACO,   # C0 - C7
-    ACV, ACV, ACV, ACV, ACV, ACV, ACV, ACV,   # C8 - CF
-    ACO, ACO, ACV, ACV, ACV, ACV, ACV, OTH,   # D0 - D7
-    ACV, ACV, ACV, ACV, ACV, ACO, ACO, ACO,   # D8 - DF
-    ASV, ASV, ASV, ASV, ASV, ASV, ASO, ASO,   # E0 - E7
-    ASV, ASV, ASV, ASV, ASV, ASV, ASV, ASV,   # E8 - EF
-    ASO, ASO, ASV, ASV, ASV, ASV, ASV, OTH,   # F0 - F7
-    ASV, ASV, ASV, ASV, ASV, ASO, ASO, ASO,   # F8 - FF
-)
-
-# 0 : illegal
-# 1 : very unlikely
-# 2 : normal
-# 3 : very likely
-Latin1ClassModel = (
-# UDF OTH ASC ASS ACV ACO ASV ASO
-    0,  0,  0,  0,  0,  0,  0,  0,  # UDF
-    0,  3,  3,  3,  3,  3,  3,  3,  # OTH
-    0,  3,  3,  3,  3,  3,  3,  3,  # ASC
-    0,  3,  3,  3,  1,  1,  3,  3,  # ASS
-    0,  3,  3,  3,  1,  2,  1,  2,  # ACV
-    0,  3,  3,  3,  3,  3,  3,  3,  # ACO
-    0,  3,  1,  3,  1,  1,  1,  3,  # ASV
-    0,  3,  1,  3,  1,  1,  3,  3,  # ASO
-)
-
-
-class Latin1Prober(CharSetProber):
-    def __init__(self):
-        super(Latin1Prober, self).__init__()
-        self._last_char_class = None
-        self._freq_counter = None
-        self.reset()
-
-    def reset(self):
-        self._last_char_class = OTH
-        self._freq_counter = [0] * FREQ_CAT_NUM
-        CharSetProber.reset(self)
-
-    @property
-    def charset_name(self):
-        return "ISO-8859-1"
-
-    @property
-    def language(self):
-        return ""
-
-    def feed(self, byte_str):
-        byte_str = self.filter_with_english_letters(byte_str)
-        for c in byte_str:
-            char_class = Latin1_CharToClass[c]
-            freq = Latin1ClassModel[(self._last_char_class * CLASS_NUM)
-                                    + char_class]
-            if freq == 0:
-                self._state = ProbingState.NOT_ME
-                break
-            self._freq_counter[freq] += 1
-            self._last_char_class = char_class
-
-        return self.state
-
-    def get_confidence(self):
-        if self.state == ProbingState.NOT_ME:
-            return 0.01
-
-        total = sum(self._freq_counter)
-        if total < 0.01:
-            confidence = 0.0
-        else:
-            confidence = ((self._freq_counter[3] - self._freq_counter[1] * 20.0)
-                          / total)
-        if confidence < 0.0:
-            confidence = 0.0
-        # lower the confidence of latin1 so that other more accurate
-        # detector can take priority.
-        confidence = confidence * 0.73
-        return confidence
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcharsetprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcharsetprober.py
deleted file mode 100644
index 6256ecf..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcharsetprober.py
+++ /dev/null
@@ -1,91 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 2001
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#   Proofpoint, Inc.
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetprober import CharSetProber
-from .enums import ProbingState, MachineState
-
-
-class MultiByteCharSetProber(CharSetProber):
-    """
-    MultiByteCharSetProber
-    """
-
-    def __init__(self, lang_filter=None):
-        super(MultiByteCharSetProber, self).__init__(lang_filter=lang_filter)
-        self.distribution_analyzer = None
-        self.coding_sm = None
-        self._last_char = [0, 0]
-
-    def reset(self):
-        super(MultiByteCharSetProber, self).reset()
-        if self.coding_sm:
-            self.coding_sm.reset()
-        if self.distribution_analyzer:
-            self.distribution_analyzer.reset()
-        self._last_char = [0, 0]
-
-    @property
-    def charset_name(self):
-        raise NotImplementedError
-
-    @property
-    def language(self):
-        raise NotImplementedError
-
-    def feed(self, byte_str):
-        for i in range(len(byte_str)):
-            coding_state = self.coding_sm.next_state(byte_str[i])
-            if coding_state == MachineState.ERROR:
-                self.logger.debug('%s %s prober hit error at byte %s',
-                                  self.charset_name, self.language, i)
-                self._state = ProbingState.NOT_ME
-                break
-            elif coding_state == MachineState.ITS_ME:
-                self._state = ProbingState.FOUND_IT
-                break
-            elif coding_state == MachineState.START:
-                char_len = self.coding_sm.get_current_charlen()
-                if i == 0:
-                    self._last_char[1] = byte_str[0]
-                    self.distribution_analyzer.feed(self._last_char, char_len)
-                else:
-                    self.distribution_analyzer.feed(byte_str[i - 1:i + 1],
-                                                    char_len)
-
-        self._last_char[0] = byte_str[-1]
-
-        if self.state == ProbingState.DETECTING:
-            if (self.distribution_analyzer.got_enough_data() and
-                    (self.get_confidence() > self.SHORTCUT_THRESHOLD)):
-                self._state = ProbingState.FOUND_IT
-
-        return self.state
-
-    def get_confidence(self):
-        return self.distribution_analyzer.get_confidence()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcsgroupprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcsgroupprober.py
deleted file mode 100644
index 530abe7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcsgroupprober.py
+++ /dev/null
@@ -1,54 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 2001
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#   Proofpoint, Inc.
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetgroupprober import CharSetGroupProber
-from .utf8prober import UTF8Prober
-from .sjisprober import SJISProber
-from .eucjpprober import EUCJPProber
-from .gb2312prober import GB2312Prober
-from .euckrprober import EUCKRProber
-from .cp949prober import CP949Prober
-from .big5prober import Big5Prober
-from .euctwprober import EUCTWProber
-
-
-class MBCSGroupProber(CharSetGroupProber):
-    def __init__(self, lang_filter=None):
-        super(MBCSGroupProber, self).__init__(lang_filter=lang_filter)
-        self.probers = [
-            UTF8Prober(),
-            SJISProber(),
-            EUCJPProber(),
-            GB2312Prober(),
-            EUCKRProber(),
-            CP949Prober(),
-            Big5Prober(),
-            EUCTWProber()
-        ]
-        self.reset()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcssm.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcssm.py
deleted file mode 100644
index 8360d0f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/mbcssm.py
+++ /dev/null
@@ -1,572 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .enums import MachineState
-
-# BIG5
-
-BIG5_CLS = (
-    1,1,1,1,1,1,1,1,  # 00 - 07    #allow 0x00 as legal value
-    1,1,1,1,1,1,0,0,  # 08 - 0f
-    1,1,1,1,1,1,1,1,  # 10 - 17
-    1,1,1,0,1,1,1,1,  # 18 - 1f
-    1,1,1,1,1,1,1,1,  # 20 - 27
-    1,1,1,1,1,1,1,1,  # 28 - 2f
-    1,1,1,1,1,1,1,1,  # 30 - 37
-    1,1,1,1,1,1,1,1,  # 38 - 3f
-    2,2,2,2,2,2,2,2,  # 40 - 47
-    2,2,2,2,2,2,2,2,  # 48 - 4f
-    2,2,2,2,2,2,2,2,  # 50 - 57
-    2,2,2,2,2,2,2,2,  # 58 - 5f
-    2,2,2,2,2,2,2,2,  # 60 - 67
-    2,2,2,2,2,2,2,2,  # 68 - 6f
-    2,2,2,2,2,2,2,2,  # 70 - 77
-    2,2,2,2,2,2,2,1,  # 78 - 7f
-    4,4,4,4,4,4,4,4,  # 80 - 87
-    4,4,4,4,4,4,4,4,  # 88 - 8f
-    4,4,4,4,4,4,4,4,  # 90 - 97
-    4,4,4,4,4,4,4,4,  # 98 - 9f
-    4,3,3,3,3,3,3,3,  # a0 - a7
-    3,3,3,3,3,3,3,3,  # a8 - af
-    3,3,3,3,3,3,3,3,  # b0 - b7
-    3,3,3,3,3,3,3,3,  # b8 - bf
-    3,3,3,3,3,3,3,3,  # c0 - c7
-    3,3,3,3,3,3,3,3,  # c8 - cf
-    3,3,3,3,3,3,3,3,  # d0 - d7
-    3,3,3,3,3,3,3,3,  # d8 - df
-    3,3,3,3,3,3,3,3,  # e0 - e7
-    3,3,3,3,3,3,3,3,  # e8 - ef
-    3,3,3,3,3,3,3,3,  # f0 - f7
-    3,3,3,3,3,3,3,0  # f8 - ff
-)
-
-BIG5_ST = (
-    MachineState.ERROR,MachineState.START,MachineState.START,     3,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#00-07
-    MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,#08-0f
-    MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START#10-17
-)
-
-BIG5_CHAR_LEN_TABLE = (0, 1, 1, 2, 0)
-
-BIG5_SM_MODEL = {'class_table': BIG5_CLS,
-                 'class_factor': 5,
-                 'state_table': BIG5_ST,
-                 'char_len_table': BIG5_CHAR_LEN_TABLE,
-                 'name': 'Big5'}
-
-# CP949
-
-CP949_CLS  = (
-    1,1,1,1,1,1,1,1, 1,1,1,1,1,1,0,0,  # 00 - 0f
-    1,1,1,1,1,1,1,1, 1,1,1,0,1,1,1,1,  # 10 - 1f
-    1,1,1,1,1,1,1,1, 1,1,1,1,1,1,1,1,  # 20 - 2f
-    1,1,1,1,1,1,1,1, 1,1,1,1,1,1,1,1,  # 30 - 3f
-    1,4,4,4,4,4,4,4, 4,4,4,4,4,4,4,4,  # 40 - 4f
-    4,4,5,5,5,5,5,5, 5,5,5,1,1,1,1,1,  # 50 - 5f
-    1,5,5,5,5,5,5,5, 5,5,5,5,5,5,5,5,  # 60 - 6f
-    5,5,5,5,5,5,5,5, 5,5,5,1,1,1,1,1,  # 70 - 7f
-    0,6,6,6,6,6,6,6, 6,6,6,6,6,6,6,6,  # 80 - 8f
-    6,6,6,6,6,6,6,6, 6,6,6,6,6,6,6,6,  # 90 - 9f
-    6,7,7,7,7,7,7,7, 7,7,7,7,7,8,8,8,  # a0 - af
-    7,7,7,7,7,7,7,7, 7,7,7,7,7,7,7,7,  # b0 - bf
-    7,7,7,7,7,7,9,2, 2,3,2,2,2,2,2,2,  # c0 - cf
-    2,2,2,2,2,2,2,2, 2,2,2,2,2,2,2,2,  # d0 - df
-    2,2,2,2,2,2,2,2, 2,2,2,2,2,2,2,2,  # e0 - ef
-    2,2,2,2,2,2,2,2, 2,2,2,2,2,2,2,0,  # f0 - ff
-)
-
-CP949_ST = (
-#cls=    0      1      2      3      4      5      6      7      8      9  # previous state =
-    MachineState.ERROR,MachineState.START,     3,MachineState.ERROR,MachineState.START,MachineState.START,     4,     5,MachineState.ERROR,     6, # MachineState.START
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR, # MachineState.ERROR
-    MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME, # MachineState.ITS_ME
-    MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START, # 3
-    MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START, # 4
-    MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START, # 5
-    MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START, # 6
-)
-
-CP949_CHAR_LEN_TABLE = (0, 1, 2, 0, 1, 1, 2, 2, 0, 2)
-
-CP949_SM_MODEL = {'class_table': CP949_CLS,
-                  'class_factor': 10,
-                  'state_table': CP949_ST,
-                  'char_len_table': CP949_CHAR_LEN_TABLE,
-                  'name': 'CP949'}
-
-# EUC-JP
-
-EUCJP_CLS = (
-    4,4,4,4,4,4,4,4,  # 00 - 07
-    4,4,4,4,4,4,5,5,  # 08 - 0f
-    4,4,4,4,4,4,4,4,  # 10 - 17
-    4,4,4,5,4,4,4,4,  # 18 - 1f
-    4,4,4,4,4,4,4,4,  # 20 - 27
-    4,4,4,4,4,4,4,4,  # 28 - 2f
-    4,4,4,4,4,4,4,4,  # 30 - 37
-    4,4,4,4,4,4,4,4,  # 38 - 3f
-    4,4,4,4,4,4,4,4,  # 40 - 47
-    4,4,4,4,4,4,4,4,  # 48 - 4f
-    4,4,4,4,4,4,4,4,  # 50 - 57
-    4,4,4,4,4,4,4,4,  # 58 - 5f
-    4,4,4,4,4,4,4,4,  # 60 - 67
-    4,4,4,4,4,4,4,4,  # 68 - 6f
-    4,4,4,4,4,4,4,4,  # 70 - 77
-    4,4,4,4,4,4,4,4,  # 78 - 7f
-    5,5,5,5,5,5,5,5,  # 80 - 87
-    5,5,5,5,5,5,1,3,  # 88 - 8f
-    5,5,5,5,5,5,5,5,  # 90 - 97
-    5,5,5,5,5,5,5,5,  # 98 - 9f
-    5,2,2,2,2,2,2,2,  # a0 - a7
-    2,2,2,2,2,2,2,2,  # a8 - af
-    2,2,2,2,2,2,2,2,  # b0 - b7
-    2,2,2,2,2,2,2,2,  # b8 - bf
-    2,2,2,2,2,2,2,2,  # c0 - c7
-    2,2,2,2,2,2,2,2,  # c8 - cf
-    2,2,2,2,2,2,2,2,  # d0 - d7
-    2,2,2,2,2,2,2,2,  # d8 - df
-    0,0,0,0,0,0,0,0,  # e0 - e7
-    0,0,0,0,0,0,0,0,  # e8 - ef
-    0,0,0,0,0,0,0,0,  # f0 - f7
-    0,0,0,0,0,0,0,5  # f8 - ff
-)
-
-EUCJP_ST = (
-          3,     4,     3,     5,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#00-07
-     MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,#08-0f
-     MachineState.ITS_ME,MachineState.ITS_ME,MachineState.START,MachineState.ERROR,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#10-17
-     MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     3,MachineState.ERROR,#18-1f
-          3,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START#20-27
-)
-
-EUCJP_CHAR_LEN_TABLE = (2, 2, 2, 3, 1, 0)
-
-EUCJP_SM_MODEL = {'class_table': EUCJP_CLS,
-                  'class_factor': 6,
-                  'state_table': EUCJP_ST,
-                  'char_len_table': EUCJP_CHAR_LEN_TABLE,
-                  'name': 'EUC-JP'}
-
-# EUC-KR
-
-EUCKR_CLS  = (
-    1,1,1,1,1,1,1,1,  # 00 - 07
-    1,1,1,1,1,1,0,0,  # 08 - 0f
-    1,1,1,1,1,1,1,1,  # 10 - 17
-    1,1,1,0,1,1,1,1,  # 18 - 1f
-    1,1,1,1,1,1,1,1,  # 20 - 27
-    1,1,1,1,1,1,1,1,  # 28 - 2f
-    1,1,1,1,1,1,1,1,  # 30 - 37
-    1,1,1,1,1,1,1,1,  # 38 - 3f
-    1,1,1,1,1,1,1,1,  # 40 - 47
-    1,1,1,1,1,1,1,1,  # 48 - 4f
-    1,1,1,1,1,1,1,1,  # 50 - 57
-    1,1,1,1,1,1,1,1,  # 58 - 5f
-    1,1,1,1,1,1,1,1,  # 60 - 67
-    1,1,1,1,1,1,1,1,  # 68 - 6f
-    1,1,1,1,1,1,1,1,  # 70 - 77
-    1,1,1,1,1,1,1,1,  # 78 - 7f
-    0,0,0,0,0,0,0,0,  # 80 - 87
-    0,0,0,0,0,0,0,0,  # 88 - 8f
-    0,0,0,0,0,0,0,0,  # 90 - 97
-    0,0,0,0,0,0,0,0,  # 98 - 9f
-    0,2,2,2,2,2,2,2,  # a0 - a7
-    2,2,2,2,2,3,3,3,  # a8 - af
-    2,2,2,2,2,2,2,2,  # b0 - b7
-    2,2,2,2,2,2,2,2,  # b8 - bf
-    2,2,2,2,2,2,2,2,  # c0 - c7
-    2,3,2,2,2,2,2,2,  # c8 - cf
-    2,2,2,2,2,2,2,2,  # d0 - d7
-    2,2,2,2,2,2,2,2,  # d8 - df
-    2,2,2,2,2,2,2,2,  # e0 - e7
-    2,2,2,2,2,2,2,2,  # e8 - ef
-    2,2,2,2,2,2,2,2,  # f0 - f7
-    2,2,2,2,2,2,2,0   # f8 - ff
-)
-
-EUCKR_ST = (
-    MachineState.ERROR,MachineState.START,     3,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#00-07
-    MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START #08-0f
-)
-
-EUCKR_CHAR_LEN_TABLE = (0, 1, 2, 0)
-
-EUCKR_SM_MODEL = {'class_table': EUCKR_CLS,
-                'class_factor': 4,
-                'state_table': EUCKR_ST,
-                'char_len_table': EUCKR_CHAR_LEN_TABLE,
-                'name': 'EUC-KR'}
-
-# EUC-TW
-
-EUCTW_CLS = (
-    2,2,2,2,2,2,2,2,  # 00 - 07
-    2,2,2,2,2,2,0,0,  # 08 - 0f
-    2,2,2,2,2,2,2,2,  # 10 - 17
-    2,2,2,0,2,2,2,2,  # 18 - 1f
-    2,2,2,2,2,2,2,2,  # 20 - 27
-    2,2,2,2,2,2,2,2,  # 28 - 2f
-    2,2,2,2,2,2,2,2,  # 30 - 37
-    2,2,2,2,2,2,2,2,  # 38 - 3f
-    2,2,2,2,2,2,2,2,  # 40 - 47
-    2,2,2,2,2,2,2,2,  # 48 - 4f
-    2,2,2,2,2,2,2,2,  # 50 - 57
-    2,2,2,2,2,2,2,2,  # 58 - 5f
-    2,2,2,2,2,2,2,2,  # 60 - 67
-    2,2,2,2,2,2,2,2,  # 68 - 6f
-    2,2,2,2,2,2,2,2,  # 70 - 77
-    2,2,2,2,2,2,2,2,  # 78 - 7f
-    0,0,0,0,0,0,0,0,  # 80 - 87
-    0,0,0,0,0,0,6,0,  # 88 - 8f
-    0,0,0,0,0,0,0,0,  # 90 - 97
-    0,0,0,0,0,0,0,0,  # 98 - 9f
-    0,3,4,4,4,4,4,4,  # a0 - a7
-    5,5,1,1,1,1,1,1,  # a8 - af
-    1,1,1,1,1,1,1,1,  # b0 - b7
-    1,1,1,1,1,1,1,1,  # b8 - bf
-    1,1,3,1,3,3,3,3,  # c0 - c7
-    3,3,3,3,3,3,3,3,  # c8 - cf
-    3,3,3,3,3,3,3,3,  # d0 - d7
-    3,3,3,3,3,3,3,3,  # d8 - df
-    3,3,3,3,3,3,3,3,  # e0 - e7
-    3,3,3,3,3,3,3,3,  # e8 - ef
-    3,3,3,3,3,3,3,3,  # f0 - f7
-    3,3,3,3,3,3,3,0   # f8 - ff
-)
-
-EUCTW_ST = (
-    MachineState.ERROR,MachineState.ERROR,MachineState.START,     3,     3,     3,     4,MachineState.ERROR,#00-07
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,#08-0f
-    MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.START,MachineState.ERROR,#10-17
-    MachineState.START,MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#18-1f
-         5,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.ERROR,MachineState.START,MachineState.START,#20-27
-    MachineState.START,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START #28-2f
-)
-
-EUCTW_CHAR_LEN_TABLE = (0, 0, 1, 2, 2, 2, 3)
-
-EUCTW_SM_MODEL = {'class_table': EUCTW_CLS,
-                'class_factor': 7,
-                'state_table': EUCTW_ST,
-                'char_len_table': EUCTW_CHAR_LEN_TABLE,
-                'name': 'x-euc-tw'}
-
-# GB2312
-
-GB2312_CLS = (
-    1,1,1,1,1,1,1,1,  # 00 - 07
-    1,1,1,1,1,1,0,0,  # 08 - 0f
-    1,1,1,1,1,1,1,1,  # 10 - 17
-    1,1,1,0,1,1,1,1,  # 18 - 1f
-    1,1,1,1,1,1,1,1,  # 20 - 27
-    1,1,1,1,1,1,1,1,  # 28 - 2f
-    3,3,3,3,3,3,3,3,  # 30 - 37
-    3,3,1,1,1,1,1,1,  # 38 - 3f
-    2,2,2,2,2,2,2,2,  # 40 - 47
-    2,2,2,2,2,2,2,2,  # 48 - 4f
-    2,2,2,2,2,2,2,2,  # 50 - 57
-    2,2,2,2,2,2,2,2,  # 58 - 5f
-    2,2,2,2,2,2,2,2,  # 60 - 67
-    2,2,2,2,2,2,2,2,  # 68 - 6f
-    2,2,2,2,2,2,2,2,  # 70 - 77
-    2,2,2,2,2,2,2,4,  # 78 - 7f
-    5,6,6,6,6,6,6,6,  # 80 - 87
-    6,6,6,6,6,6,6,6,  # 88 - 8f
-    6,6,6,6,6,6,6,6,  # 90 - 97
-    6,6,6,6,6,6,6,6,  # 98 - 9f
-    6,6,6,6,6,6,6,6,  # a0 - a7
-    6,6,6,6,6,6,6,6,  # a8 - af
-    6,6,6,6,6,6,6,6,  # b0 - b7
-    6,6,6,6,6,6,6,6,  # b8 - bf
-    6,6,6,6,6,6,6,6,  # c0 - c7
-    6,6,6,6,6,6,6,6,  # c8 - cf
-    6,6,6,6,6,6,6,6,  # d0 - d7
-    6,6,6,6,6,6,6,6,  # d8 - df
-    6,6,6,6,6,6,6,6,  # e0 - e7
-    6,6,6,6,6,6,6,6,  # e8 - ef
-    6,6,6,6,6,6,6,6,  # f0 - f7
-    6,6,6,6,6,6,6,0   # f8 - ff
-)
-
-GB2312_ST = (
-    MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,     3,MachineState.ERROR,#00-07
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,#08-0f
-    MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.START,#10-17
-         4,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#18-1f
-    MachineState.ERROR,MachineState.ERROR,     5,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,#20-27
-    MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.START #28-2f
-)
-
-# To be accurate, the length of class 6 can be either 2 or 4.
-# But it is not necessary to discriminate between the two since
-# it is used for frequency analysis only, and we are validating
-# each code range there as well. So it is safe to set it to be
-# 2 here.
-GB2312_CHAR_LEN_TABLE = (0, 1, 1, 1, 1, 1, 2)
-
-GB2312_SM_MODEL = {'class_table': GB2312_CLS,
-                   'class_factor': 7,
-                   'state_table': GB2312_ST,
-                   'char_len_table': GB2312_CHAR_LEN_TABLE,
-                   'name': 'GB2312'}
-
-# Shift_JIS
-
-SJIS_CLS = (
-    1,1,1,1,1,1,1,1,  # 00 - 07
-    1,1,1,1,1,1,0,0,  # 08 - 0f
-    1,1,1,1,1,1,1,1,  # 10 - 17
-    1,1,1,0,1,1,1,1,  # 18 - 1f
-    1,1,1,1,1,1,1,1,  # 20 - 27
-    1,1,1,1,1,1,1,1,  # 28 - 2f
-    1,1,1,1,1,1,1,1,  # 30 - 37
-    1,1,1,1,1,1,1,1,  # 38 - 3f
-    2,2,2,2,2,2,2,2,  # 40 - 47
-    2,2,2,2,2,2,2,2,  # 48 - 4f
-    2,2,2,2,2,2,2,2,  # 50 - 57
-    2,2,2,2,2,2,2,2,  # 58 - 5f
-    2,2,2,2,2,2,2,2,  # 60 - 67
-    2,2,2,2,2,2,2,2,  # 68 - 6f
-    2,2,2,2,2,2,2,2,  # 70 - 77
-    2,2,2,2,2,2,2,1,  # 78 - 7f
-    3,3,3,3,3,2,2,3,  # 80 - 87
-    3,3,3,3,3,3,3,3,  # 88 - 8f
-    3,3,3,3,3,3,3,3,  # 90 - 97
-    3,3,3,3,3,3,3,3,  # 98 - 9f
-    #0xa0 is illegal in sjis encoding, but some pages does
-    #contain such byte. We need to be more error forgiven.
-    2,2,2,2,2,2,2,2,  # a0 - a7
-    2,2,2,2,2,2,2,2,  # a8 - af
-    2,2,2,2,2,2,2,2,  # b0 - b7
-    2,2,2,2,2,2,2,2,  # b8 - bf
-    2,2,2,2,2,2,2,2,  # c0 - c7
-    2,2,2,2,2,2,2,2,  # c8 - cf
-    2,2,2,2,2,2,2,2,  # d0 - d7
-    2,2,2,2,2,2,2,2,  # d8 - df
-    3,3,3,3,3,3,3,3,  # e0 - e7
-    3,3,3,3,3,4,4,4,  # e8 - ef
-    3,3,3,3,3,3,3,3,  # f0 - f7
-    3,3,3,3,3,0,0,0)  # f8 - ff
-
-
-SJIS_ST = (
-    MachineState.ERROR,MachineState.START,MachineState.START,     3,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#00-07
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,#08-0f
-    MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START #10-17
-)
-
-SJIS_CHAR_LEN_TABLE = (0, 1, 1, 2, 0, 0)
-
-SJIS_SM_MODEL = {'class_table': SJIS_CLS,
-               'class_factor': 6,
-               'state_table': SJIS_ST,
-               'char_len_table': SJIS_CHAR_LEN_TABLE,
-               'name': 'Shift_JIS'}
-
-# UCS2-BE
-
-UCS2BE_CLS = (
-    0,0,0,0,0,0,0,0,  # 00 - 07
-    0,0,1,0,0,2,0,0,  # 08 - 0f
-    0,0,0,0,0,0,0,0,  # 10 - 17
-    0,0,0,3,0,0,0,0,  # 18 - 1f
-    0,0,0,0,0,0,0,0,  # 20 - 27
-    0,3,3,3,3,3,0,0,  # 28 - 2f
-    0,0,0,0,0,0,0,0,  # 30 - 37
-    0,0,0,0,0,0,0,0,  # 38 - 3f
-    0,0,0,0,0,0,0,0,  # 40 - 47
-    0,0,0,0,0,0,0,0,  # 48 - 4f
-    0,0,0,0,0,0,0,0,  # 50 - 57
-    0,0,0,0,0,0,0,0,  # 58 - 5f
-    0,0,0,0,0,0,0,0,  # 60 - 67
-    0,0,0,0,0,0,0,0,  # 68 - 6f
-    0,0,0,0,0,0,0,0,  # 70 - 77
-    0,0,0,0,0,0,0,0,  # 78 - 7f
-    0,0,0,0,0,0,0,0,  # 80 - 87
-    0,0,0,0,0,0,0,0,  # 88 - 8f
-    0,0,0,0,0,0,0,0,  # 90 - 97
-    0,0,0,0,0,0,0,0,  # 98 - 9f
-    0,0,0,0,0,0,0,0,  # a0 - a7
-    0,0,0,0,0,0,0,0,  # a8 - af
-    0,0,0,0,0,0,0,0,  # b0 - b7
-    0,0,0,0,0,0,0,0,  # b8 - bf
-    0,0,0,0,0,0,0,0,  # c0 - c7
-    0,0,0,0,0,0,0,0,  # c8 - cf
-    0,0,0,0,0,0,0,0,  # d0 - d7
-    0,0,0,0,0,0,0,0,  # d8 - df
-    0,0,0,0,0,0,0,0,  # e0 - e7
-    0,0,0,0,0,0,0,0,  # e8 - ef
-    0,0,0,0,0,0,0,0,  # f0 - f7
-    0,0,0,0,0,0,4,5   # f8 - ff
-)
-
-UCS2BE_ST  = (
-          5,     7,     7,MachineState.ERROR,     4,     3,MachineState.ERROR,MachineState.ERROR,#00-07
-     MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,#08-0f
-     MachineState.ITS_ME,MachineState.ITS_ME,     6,     6,     6,     6,MachineState.ERROR,MachineState.ERROR,#10-17
-          6,     6,     6,     6,     6,MachineState.ITS_ME,     6,     6,#18-1f
-          6,     6,     6,     6,     5,     7,     7,MachineState.ERROR,#20-27
-          5,     8,     6,     6,MachineState.ERROR,     6,     6,     6,#28-2f
-          6,     6,     6,     6,MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START #30-37
-)
-
-UCS2BE_CHAR_LEN_TABLE = (2, 2, 2, 0, 2, 2)
-
-UCS2BE_SM_MODEL = {'class_table': UCS2BE_CLS,
-                   'class_factor': 6,
-                   'state_table': UCS2BE_ST,
-                   'char_len_table': UCS2BE_CHAR_LEN_TABLE,
-                   'name': 'UTF-16BE'}
-
-# UCS2-LE
-
-UCS2LE_CLS = (
-    0,0,0,0,0,0,0,0,  # 00 - 07
-    0,0,1,0,0,2,0,0,  # 08 - 0f
-    0,0,0,0,0,0,0,0,  # 10 - 17
-    0,0,0,3,0,0,0,0,  # 18 - 1f
-    0,0,0,0,0,0,0,0,  # 20 - 27
-    0,3,3,3,3,3,0,0,  # 28 - 2f
-    0,0,0,0,0,0,0,0,  # 30 - 37
-    0,0,0,0,0,0,0,0,  # 38 - 3f
-    0,0,0,0,0,0,0,0,  # 40 - 47
-    0,0,0,0,0,0,0,0,  # 48 - 4f
-    0,0,0,0,0,0,0,0,  # 50 - 57
-    0,0,0,0,0,0,0,0,  # 58 - 5f
-    0,0,0,0,0,0,0,0,  # 60 - 67
-    0,0,0,0,0,0,0,0,  # 68 - 6f
-    0,0,0,0,0,0,0,0,  # 70 - 77
-    0,0,0,0,0,0,0,0,  # 78 - 7f
-    0,0,0,0,0,0,0,0,  # 80 - 87
-    0,0,0,0,0,0,0,0,  # 88 - 8f
-    0,0,0,0,0,0,0,0,  # 90 - 97
-    0,0,0,0,0,0,0,0,  # 98 - 9f
-    0,0,0,0,0,0,0,0,  # a0 - a7
-    0,0,0,0,0,0,0,0,  # a8 - af
-    0,0,0,0,0,0,0,0,  # b0 - b7
-    0,0,0,0,0,0,0,0,  # b8 - bf
-    0,0,0,0,0,0,0,0,  # c0 - c7
-    0,0,0,0,0,0,0,0,  # c8 - cf
-    0,0,0,0,0,0,0,0,  # d0 - d7
-    0,0,0,0,0,0,0,0,  # d8 - df
-    0,0,0,0,0,0,0,0,  # e0 - e7
-    0,0,0,0,0,0,0,0,  # e8 - ef
-    0,0,0,0,0,0,0,0,  # f0 - f7
-    0,0,0,0,0,0,4,5   # f8 - ff
-)
-
-UCS2LE_ST = (
-          6,     6,     7,     6,     4,     3,MachineState.ERROR,MachineState.ERROR,#00-07
-     MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,#08-0f
-     MachineState.ITS_ME,MachineState.ITS_ME,     5,     5,     5,MachineState.ERROR,MachineState.ITS_ME,MachineState.ERROR,#10-17
-          5,     5,     5,MachineState.ERROR,     5,MachineState.ERROR,     6,     6,#18-1f
-          7,     6,     8,     8,     5,     5,     5,MachineState.ERROR,#20-27
-          5,     5,     5,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     5,     5,#28-2f
-          5,     5,     5,MachineState.ERROR,     5,MachineState.ERROR,MachineState.START,MachineState.START #30-37
-)
-
-UCS2LE_CHAR_LEN_TABLE = (2, 2, 2, 2, 2, 2)
-
-UCS2LE_SM_MODEL = {'class_table': UCS2LE_CLS,
-                 'class_factor': 6,
-                 'state_table': UCS2LE_ST,
-                 'char_len_table': UCS2LE_CHAR_LEN_TABLE,
-                 'name': 'UTF-16LE'}
-
-# UTF-8
-
-UTF8_CLS = (
-    1,1,1,1,1,1,1,1,  # 00 - 07  #allow 0x00 as a legal value
-    1,1,1,1,1,1,0,0,  # 08 - 0f
-    1,1,1,1,1,1,1,1,  # 10 - 17
-    1,1,1,0,1,1,1,1,  # 18 - 1f
-    1,1,1,1,1,1,1,1,  # 20 - 27
-    1,1,1,1,1,1,1,1,  # 28 - 2f
-    1,1,1,1,1,1,1,1,  # 30 - 37
-    1,1,1,1,1,1,1,1,  # 38 - 3f
-    1,1,1,1,1,1,1,1,  # 40 - 47
-    1,1,1,1,1,1,1,1,  # 48 - 4f
-    1,1,1,1,1,1,1,1,  # 50 - 57
-    1,1,1,1,1,1,1,1,  # 58 - 5f
-    1,1,1,1,1,1,1,1,  # 60 - 67
-    1,1,1,1,1,1,1,1,  # 68 - 6f
-    1,1,1,1,1,1,1,1,  # 70 - 77
-    1,1,1,1,1,1,1,1,  # 78 - 7f
-    2,2,2,2,3,3,3,3,  # 80 - 87
-    4,4,4,4,4,4,4,4,  # 88 - 8f
-    4,4,4,4,4,4,4,4,  # 90 - 97
-    4,4,4,4,4,4,4,4,  # 98 - 9f
-    5,5,5,5,5,5,5,5,  # a0 - a7
-    5,5,5,5,5,5,5,5,  # a8 - af
-    5,5,5,5,5,5,5,5,  # b0 - b7
-    5,5,5,5,5,5,5,5,  # b8 - bf
-    0,0,6,6,6,6,6,6,  # c0 - c7
-    6,6,6,6,6,6,6,6,  # c8 - cf
-    6,6,6,6,6,6,6,6,  # d0 - d7
-    6,6,6,6,6,6,6,6,  # d8 - df
-    7,8,8,8,8,8,8,8,  # e0 - e7
-    8,8,8,8,8,9,8,8,  # e8 - ef
-    10,11,11,11,11,11,11,11,  # f0 - f7
-    12,13,13,13,14,15,0,0    # f8 - ff
-)
-
-UTF8_ST = (
-    MachineState.ERROR,MachineState.START,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     12,   10,#00-07
-         9,     11,     8,     7,     6,     5,     4,    3,#08-0f
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#10-17
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#18-1f
-    MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,#20-27
-    MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,MachineState.ITS_ME,#28-2f
-    MachineState.ERROR,MachineState.ERROR,     5,     5,     5,     5,MachineState.ERROR,MachineState.ERROR,#30-37
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#38-3f
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     5,     5,     5,MachineState.ERROR,MachineState.ERROR,#40-47
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#48-4f
-    MachineState.ERROR,MachineState.ERROR,     7,     7,     7,     7,MachineState.ERROR,MachineState.ERROR,#50-57
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#58-5f
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     7,     7,MachineState.ERROR,MachineState.ERROR,#60-67
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#68-6f
-    MachineState.ERROR,MachineState.ERROR,     9,     9,     9,     9,MachineState.ERROR,MachineState.ERROR,#70-77
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#78-7f
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,     9,MachineState.ERROR,MachineState.ERROR,#80-87
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#88-8f
-    MachineState.ERROR,MachineState.ERROR,    12,    12,    12,    12,MachineState.ERROR,MachineState.ERROR,#90-97
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#98-9f
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,    12,MachineState.ERROR,MachineState.ERROR,#a0-a7
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#a8-af
-    MachineState.ERROR,MachineState.ERROR,    12,    12,    12,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#b0-b7
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,#b8-bf
-    MachineState.ERROR,MachineState.ERROR,MachineState.START,MachineState.START,MachineState.START,MachineState.START,MachineState.ERROR,MachineState.ERROR,#c0-c7
-    MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR,MachineState.ERROR #c8-cf
-)
-
-UTF8_CHAR_LEN_TABLE = (0, 1, 0, 0, 0, 0, 2, 3, 3, 3, 4, 4, 5, 5, 6, 6)
-
-UTF8_SM_MODEL = {'class_table': UTF8_CLS,
-                 'class_factor': 16,
-                 'state_table': UTF8_ST,
-                 'char_len_table': UTF8_CHAR_LEN_TABLE,
-                 'name': 'UTF-8'}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sbcharsetprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sbcharsetprober.py
deleted file mode 100644
index 0adb51d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sbcharsetprober.py
+++ /dev/null
@@ -1,132 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 2001
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetprober import CharSetProber
-from .enums import CharacterCategory, ProbingState, SequenceLikelihood
-
-
-class SingleByteCharSetProber(CharSetProber):
-    SAMPLE_SIZE = 64
-    SB_ENOUGH_REL_THRESHOLD = 1024  #  0.25 * SAMPLE_SIZE^2
-    POSITIVE_SHORTCUT_THRESHOLD = 0.95
-    NEGATIVE_SHORTCUT_THRESHOLD = 0.05
-
-    def __init__(self, model, reversed=False, name_prober=None):
-        super(SingleByteCharSetProber, self).__init__()
-        self._model = model
-        # TRUE if we need to reverse every pair in the model lookup
-        self._reversed = reversed
-        # Optional auxiliary prober for name decision
-        self._name_prober = name_prober
-        self._last_order = None
-        self._seq_counters = None
-        self._total_seqs = None
-        self._total_char = None
-        self._freq_char = None
-        self.reset()
-
-    def reset(self):
-        super(SingleByteCharSetProber, self).reset()
-        # char order of last character
-        self._last_order = 255
-        self._seq_counters = [0] * SequenceLikelihood.get_num_categories()
-        self._total_seqs = 0
-        self._total_char = 0
-        # characters that fall in our sampling range
-        self._freq_char = 0
-
-    @property
-    def charset_name(self):
-        if self._name_prober:
-            return self._name_prober.charset_name
-        else:
-            return self._model['charset_name']
-
-    @property
-    def language(self):
-        if self._name_prober:
-            return self._name_prober.language
-        else:
-            return self._model.get('language')
-
-    def feed(self, byte_str):
-        if not self._model['keep_english_letter']:
-            byte_str = self.filter_international_words(byte_str)
-        if not byte_str:
-            return self.state
-        char_to_order_map = self._model['char_to_order_map']
-        for i, c in enumerate(byte_str):
-            # XXX: Order is in range 1-64, so one would think we want 0-63 here,
-            #      but that leads to 27 more test failures than before.
-            order = char_to_order_map[c]
-            # XXX: This was SYMBOL_CAT_ORDER before, with a value of 250, but
-            #      CharacterCategory.SYMBOL is actually 253, so we use CONTROL
-            #      to make it closer to the original intent. The only difference
-            #      is whether or not we count digits and control characters for
-            #      _total_char purposes.
-            if order < CharacterCategory.CONTROL:
-                self._total_char += 1
-            if order < self.SAMPLE_SIZE:
-                self._freq_char += 1
-                if self._last_order < self.SAMPLE_SIZE:
-                    self._total_seqs += 1
-                    if not self._reversed:
-                        i = (self._last_order * self.SAMPLE_SIZE) + order
-                        model = self._model['precedence_matrix'][i]
-                    else:  # reverse the order of the letters in the lookup
-                        i = (order * self.SAMPLE_SIZE) + self._last_order
-                        model = self._model['precedence_matrix'][i]
-                    self._seq_counters[model] += 1
-            self._last_order = order
-
-        charset_name = self._model['charset_name']
-        if self.state == ProbingState.DETECTING:
-            if self._total_seqs > self.SB_ENOUGH_REL_THRESHOLD:
-                confidence = self.get_confidence()
-                if confidence > self.POSITIVE_SHORTCUT_THRESHOLD:
-                    self.logger.debug('%s confidence = %s, we have a winner',
-                                      charset_name, confidence)
-                    self._state = ProbingState.FOUND_IT
-                elif confidence < self.NEGATIVE_SHORTCUT_THRESHOLD:
-                    self.logger.debug('%s confidence = %s, below negative '
-                                      'shortcut threshhold %s', charset_name,
-                                      confidence,
-                                      self.NEGATIVE_SHORTCUT_THRESHOLD)
-                    self._state = ProbingState.NOT_ME
-
-        return self.state
-
-    def get_confidence(self):
-        r = 0.01
-        if self._total_seqs > 0:
-            r = ((1.0 * self._seq_counters[SequenceLikelihood.POSITIVE]) /
-                 self._total_seqs / self._model['typical_positive_ratio'])
-            r = r * self._freq_char / self._total_char
-            if r >= 1.0:
-                r = 0.99
-        return r
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sbcsgroupprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sbcsgroupprober.py
deleted file mode 100644
index 98e95dc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sbcsgroupprober.py
+++ /dev/null
@@ -1,73 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 2001
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetgroupprober import CharSetGroupProber
-from .sbcharsetprober import SingleByteCharSetProber
-from .langcyrillicmodel import (Win1251CyrillicModel, Koi8rModel,
-                                Latin5CyrillicModel, MacCyrillicModel,
-                                Ibm866Model, Ibm855Model)
-from .langgreekmodel import Latin7GreekModel, Win1253GreekModel
-from .langbulgarianmodel import Latin5BulgarianModel, Win1251BulgarianModel
-# from .langhungarianmodel import Latin2HungarianModel, Win1250HungarianModel
-from .langthaimodel import TIS620ThaiModel
-from .langhebrewmodel import Win1255HebrewModel
-from .hebrewprober import HebrewProber
-from .langturkishmodel import Latin5TurkishModel
-
-
-class SBCSGroupProber(CharSetGroupProber):
-    def __init__(self):
-        super(SBCSGroupProber, self).__init__()
-        self.probers = [
-            SingleByteCharSetProber(Win1251CyrillicModel),
-            SingleByteCharSetProber(Koi8rModel),
-            SingleByteCharSetProber(Latin5CyrillicModel),
-            SingleByteCharSetProber(MacCyrillicModel),
-            SingleByteCharSetProber(Ibm866Model),
-            SingleByteCharSetProber(Ibm855Model),
-            SingleByteCharSetProber(Latin7GreekModel),
-            SingleByteCharSetProber(Win1253GreekModel),
-            SingleByteCharSetProber(Latin5BulgarianModel),
-            SingleByteCharSetProber(Win1251BulgarianModel),
-            # TODO: Restore Hungarian encodings (iso-8859-2 and windows-1250)
-            #       after we retrain model.
-            # SingleByteCharSetProber(Latin2HungarianModel),
-            # SingleByteCharSetProber(Win1250HungarianModel),
-            SingleByteCharSetProber(TIS620ThaiModel),
-            SingleByteCharSetProber(Latin5TurkishModel),
-        ]
-        hebrew_prober = HebrewProber()
-        logical_hebrew_prober = SingleByteCharSetProber(Win1255HebrewModel,
-                                                        False, hebrew_prober)
-        visual_hebrew_prober = SingleByteCharSetProber(Win1255HebrewModel, True,
-                                                       hebrew_prober)
-        hebrew_prober.set_model_probers(logical_hebrew_prober, visual_hebrew_prober)
-        self.probers.extend([hebrew_prober, logical_hebrew_prober,
-                             visual_hebrew_prober])
-
-        self.reset()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sjisprober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sjisprober.py
deleted file mode 100644
index 9e29623..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/sjisprober.py
+++ /dev/null
@@ -1,92 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .mbcharsetprober import MultiByteCharSetProber
-from .codingstatemachine import CodingStateMachine
-from .chardistribution import SJISDistributionAnalysis
-from .jpcntx import SJISContextAnalysis
-from .mbcssm import SJIS_SM_MODEL
-from .enums import ProbingState, MachineState
-
-
-class SJISProber(MultiByteCharSetProber):
-    def __init__(self):
-        super(SJISProber, self).__init__()
-        self.coding_sm = CodingStateMachine(SJIS_SM_MODEL)
-        self.distribution_analyzer = SJISDistributionAnalysis()
-        self.context_analyzer = SJISContextAnalysis()
-        self.reset()
-
-    def reset(self):
-        super(SJISProber, self).reset()
-        self.context_analyzer.reset()
-
-    @property
-    def charset_name(self):
-        return self.context_analyzer.charset_name
-
-    @property
-    def language(self):
-        return "Japanese"
-
-    def feed(self, byte_str):
-        for i in range(len(byte_str)):
-            coding_state = self.coding_sm.next_state(byte_str[i])
-            if coding_state == MachineState.ERROR:
-                self.logger.debug('%s %s prober hit error at byte %s',
-                                  self.charset_name, self.language, i)
-                self._state = ProbingState.NOT_ME
-                break
-            elif coding_state == MachineState.ITS_ME:
-                self._state = ProbingState.FOUND_IT
-                break
-            elif coding_state == MachineState.START:
-                char_len = self.coding_sm.get_current_charlen()
-                if i == 0:
-                    self._last_char[1] = byte_str[0]
-                    self.context_analyzer.feed(self._last_char[2 - char_len:],
-                                               char_len)
-                    self.distribution_analyzer.feed(self._last_char, char_len)
-                else:
-                    self.context_analyzer.feed(byte_str[i + 1 - char_len:i + 3
-                                                        - char_len], char_len)
-                    self.distribution_analyzer.feed(byte_str[i - 1:i + 1],
-                                                    char_len)
-
-        self._last_char[0] = byte_str[-1]
-
-        if self.state == ProbingState.DETECTING:
-            if (self.context_analyzer.got_enough_data() and
-               (self.get_confidence() > self.SHORTCUT_THRESHOLD)):
-                self._state = ProbingState.FOUND_IT
-
-        return self.state
-
-    def get_confidence(self):
-        context_conf = self.context_analyzer.get_confidence()
-        distrib_conf = self.distribution_analyzer.get_confidence()
-        return max(context_conf, distrib_conf)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/universaldetector.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/universaldetector.py
deleted file mode 100644
index 7b4e92d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/universaldetector.py
+++ /dev/null
@@ -1,286 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is Mozilla Universal charset detector code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 2001
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#   Shy Shalom - original C code
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-"""
-Module containing the UniversalDetector detector class, which is the primary
-class a user of ``chardet`` should use.
-
-:author: Mark Pilgrim (initial port to Python)
-:author: Shy Shalom (original C code)
-:author: Dan Blanchard (major refactoring for 3.0)
-:author: Ian Cordasco
-"""
-
-
-import codecs
-import logging
-import re
-
-from .charsetgroupprober import CharSetGroupProber
-from .enums import InputState, LanguageFilter, ProbingState
-from .escprober import EscCharSetProber
-from .latin1prober import Latin1Prober
-from .mbcsgroupprober import MBCSGroupProber
-from .sbcsgroupprober import SBCSGroupProber
-
-
-class UniversalDetector(object):
-    """
-    The ``UniversalDetector`` class underlies the ``chardet.detect`` function
-    and coordinates all of the different charset probers.
-
-    To get a ``dict`` containing an encoding and its confidence, you can simply
-    run:
-
-    .. code::
-
-            u = UniversalDetector()
-            u.feed(some_bytes)
-            u.close()
-            detected = u.result
-
-    """
-
-    MINIMUM_THRESHOLD = 0.20
-    HIGH_BYTE_DETECTOR = re.compile(b'[\x80-\xFF]')
-    ESC_DETECTOR = re.compile(b'(\033|~{)')
-    WIN_BYTE_DETECTOR = re.compile(b'[\x80-\x9F]')
-    ISO_WIN_MAP = {'iso-8859-1': 'Windows-1252',
-                   'iso-8859-2': 'Windows-1250',
-                   'iso-8859-5': 'Windows-1251',
-                   'iso-8859-6': 'Windows-1256',
-                   'iso-8859-7': 'Windows-1253',
-                   'iso-8859-8': 'Windows-1255',
-                   'iso-8859-9': 'Windows-1254',
-                   'iso-8859-13': 'Windows-1257'}
-
-    def __init__(self, lang_filter=LanguageFilter.ALL):
-        self._esc_charset_prober = None
-        self._charset_probers = []
-        self.result = None
-        self.done = None
-        self._got_data = None
-        self._input_state = None
-        self._last_char = None
-        self.lang_filter = lang_filter
-        self.logger = logging.getLogger(__name__)
-        self._has_win_bytes = None
-        self.reset()
-
-    def reset(self):
-        """
-        Reset the UniversalDetector and all of its probers back to their
-        initial states.  This is called by ``__init__``, so you only need to
-        call this directly in between analyses of different documents.
-        """
-        self.result = {'encoding': None, 'confidence': 0.0, 'language': None}
-        self.done = False
-        self._got_data = False
-        self._has_win_bytes = False
-        self._input_state = InputState.PURE_ASCII
-        self._last_char = b''
-        if self._esc_charset_prober:
-            self._esc_charset_prober.reset()
-        for prober in self._charset_probers:
-            prober.reset()
-
-    def feed(self, byte_str):
-        """
-        Takes a chunk of a document and feeds it through all of the relevant
-        charset probers.
-
-        After calling ``feed``, you can check the value of the ``done``
-        attribute to see if you need to continue feeding the
-        ``UniversalDetector`` more data, or if it has made a prediction
-        (in the ``result`` attribute).
-
-        .. note::
-           You should always call ``close`` when you're done feeding in your
-           document if ``done`` is not already ``True``.
-        """
-        if self.done:
-            return
-
-        if not len(byte_str):
-            return
-
-        if not isinstance(byte_str, bytearray):
-            byte_str = bytearray(byte_str)
-
-        # First check for known BOMs, since these are guaranteed to be correct
-        if not self._got_data:
-            # If the data starts with BOM, we know it is UTF
-            if byte_str.startswith(codecs.BOM_UTF8):
-                # EF BB BF  UTF-8 with BOM
-                self.result = {'encoding': "UTF-8-SIG",
-                               'confidence': 1.0,
-                               'language': ''}
-            elif byte_str.startswith((codecs.BOM_UTF32_LE,
-                                      codecs.BOM_UTF32_BE)):
-                # FF FE 00 00  UTF-32, little-endian BOM
-                # 00 00 FE FF  UTF-32, big-endian BOM
-                self.result = {'encoding': "UTF-32",
-                               'confidence': 1.0,
-                               'language': ''}
-            elif byte_str.startswith(b'\xFE\xFF\x00\x00'):
-                # FE FF 00 00  UCS-4, unusual octet order BOM (3412)
-                self.result = {'encoding': "X-ISO-10646-UCS-4-3412",
-                               'confidence': 1.0,
-                               'language': ''}
-            elif byte_str.startswith(b'\x00\x00\xFF\xFE'):
-                # 00 00 FF FE  UCS-4, unusual octet order BOM (2143)
-                self.result = {'encoding': "X-ISO-10646-UCS-4-2143",
-                               'confidence': 1.0,
-                               'language': ''}
-            elif byte_str.startswith((codecs.BOM_LE, codecs.BOM_BE)):
-                # FF FE  UTF-16, little endian BOM
-                # FE FF  UTF-16, big endian BOM
-                self.result = {'encoding': "UTF-16",
-                               'confidence': 1.0,
-                               'language': ''}
-
-            self._got_data = True
-            if self.result['encoding'] is not None:
-                self.done = True
-                return
-
-        # If none of those matched and we've only see ASCII so far, check
-        # for high bytes and escape sequences
-        if self._input_state == InputState.PURE_ASCII:
-            if self.HIGH_BYTE_DETECTOR.search(byte_str):
-                self._input_state = InputState.HIGH_BYTE
-            elif self._input_state == InputState.PURE_ASCII and \
-                    self.ESC_DETECTOR.search(self._last_char + byte_str):
-                self._input_state = InputState.ESC_ASCII
-
-        self._last_char = byte_str[-1:]
-
-        # If we've seen escape sequences, use the EscCharSetProber, which
-        # uses a simple state machine to check for known escape sequences in
-        # HZ and ISO-2022 encodings, since those are the only encodings that
-        # use such sequences.
-        if self._input_state == InputState.ESC_ASCII:
-            if not self._esc_charset_prober:
-                self._esc_charset_prober = EscCharSetProber(self.lang_filter)
-            if self._esc_charset_prober.feed(byte_str) == ProbingState.FOUND_IT:
-                self.result = {'encoding':
-                               self._esc_charset_prober.charset_name,
-                               'confidence':
-                               self._esc_charset_prober.get_confidence(),
-                               'language':
-                               self._esc_charset_prober.language}
-                self.done = True
-        # If we've seen high bytes (i.e., those with values greater than 127),
-        # we need to do more complicated checks using all our multi-byte and
-        # single-byte probers that are left.  The single-byte probers
-        # use character bigram distributions to determine the encoding, whereas
-        # the multi-byte probers use a combination of character unigram and
-        # bigram distributions.
-        elif self._input_state == InputState.HIGH_BYTE:
-            if not self._charset_probers:
-                self._charset_probers = [MBCSGroupProber(self.lang_filter)]
-                # If we're checking non-CJK encodings, use single-byte prober
-                if self.lang_filter & LanguageFilter.NON_CJK:
-                    self._charset_probers.append(SBCSGroupProber())
-                self._charset_probers.append(Latin1Prober())
-            for prober in self._charset_probers:
-                if prober.feed(byte_str) == ProbingState.FOUND_IT:
-                    self.result = {'encoding': prober.charset_name,
-                                   'confidence': prober.get_confidence(),
-                                   'language': prober.language}
-                    self.done = True
-                    break
-            if self.WIN_BYTE_DETECTOR.search(byte_str):
-                self._has_win_bytes = True
-
-    def close(self):
-        """
-        Stop analyzing the current document and come up with a final
-        prediction.
-
-        :returns:  The ``result`` attribute, a ``dict`` with the keys
-                   `encoding`, `confidence`, and `language`.
-        """
-        # Don't bother with checks if we're already done
-        if self.done:
-            return self.result
-        self.done = True
-
-        if not self._got_data:
-            self.logger.debug('no data received!')
-
-        # Default to ASCII if it is all we've seen so far
-        elif self._input_state == InputState.PURE_ASCII:
-            self.result = {'encoding': 'ascii',
-                           'confidence': 1.0,
-                           'language': ''}
-
-        # If we have seen non-ASCII, return the best that met MINIMUM_THRESHOLD
-        elif self._input_state == InputState.HIGH_BYTE:
-            prober_confidence = None
-            max_prober_confidence = 0.0
-            max_prober = None
-            for prober in self._charset_probers:
-                if not prober:
-                    continue
-                prober_confidence = prober.get_confidence()
-                if prober_confidence > max_prober_confidence:
-                    max_prober_confidence = prober_confidence
-                    max_prober = prober
-            if max_prober and (max_prober_confidence > self.MINIMUM_THRESHOLD):
-                charset_name = max_prober.charset_name
-                lower_charset_name = max_prober.charset_name.lower()
-                confidence = max_prober.get_confidence()
-                # Use Windows encoding name instead of ISO-8859 if we saw any
-                # extra Windows-specific bytes
-                if lower_charset_name.startswith('iso-8859'):
-                    if self._has_win_bytes:
-                        charset_name = self.ISO_WIN_MAP.get(lower_charset_name,
-                                                            charset_name)
-                self.result = {'encoding': charset_name,
-                               'confidence': confidence,
-                               'language': max_prober.language}
-
-        # Log all prober confidences if none met MINIMUM_THRESHOLD
-        if self.logger.getEffectiveLevel() == logging.DEBUG:
-            if self.result['encoding'] is None:
-                self.logger.debug('no probers hit minimum threshold')
-                for group_prober in self._charset_probers:
-                    if not group_prober:
-                        continue
-                    if isinstance(group_prober, CharSetGroupProber):
-                        for prober in group_prober.probers:
-                            self.logger.debug('%s %s confidence = %s',
-                                              prober.charset_name,
-                                              prober.language,
-                                              prober.get_confidence())
-                    else:
-                        self.logger.debug('%s %s confidence = %s',
-                                          prober.charset_name,
-                                          prober.language,
-                                          prober.get_confidence())
-        return self.result
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/utf8prober.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/utf8prober.py
deleted file mode 100644
index 6c3196c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/utf8prober.py
+++ /dev/null
@@ -1,82 +0,0 @@
-######################## BEGIN LICENSE BLOCK ########################
-# The Original Code is mozilla.org code.
-#
-# The Initial Developer of the Original Code is
-# Netscape Communications Corporation.
-# Portions created by the Initial Developer are Copyright (C) 1998
-# the Initial Developer. All Rights Reserved.
-#
-# Contributor(s):
-#   Mark Pilgrim - port to Python
-#
-# This library is free software; you can redistribute it and/or
-# modify it under the terms of the GNU Lesser General Public
-# License as published by the Free Software Foundation; either
-# version 2.1 of the License, or (at your option) any later version.
-#
-# This library is distributed in the hope that it will be useful,
-# but WITHOUT ANY WARRANTY; without even the implied warranty of
-# MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE.  See the GNU
-# Lesser General Public License for more details.
-#
-# You should have received a copy of the GNU Lesser General Public
-# License along with this library; if not, write to the Free Software
-# Foundation, Inc., 51 Franklin St, Fifth Floor, Boston, MA
-# 02110-1301  USA
-######################### END LICENSE BLOCK #########################
-
-from .charsetprober import CharSetProber
-from .enums import ProbingState, MachineState
-from .codingstatemachine import CodingStateMachine
-from .mbcssm import UTF8_SM_MODEL
-
-
-
-class UTF8Prober(CharSetProber):
-    ONE_CHAR_PROB = 0.5
-
-    def __init__(self):
-        super(UTF8Prober, self).__init__()
-        self.coding_sm = CodingStateMachine(UTF8_SM_MODEL)
-        self._num_mb_chars = None
-        self.reset()
-
-    def reset(self):
-        super(UTF8Prober, self).reset()
-        self.coding_sm.reset()
-        self._num_mb_chars = 0
-
-    @property
-    def charset_name(self):
-        return "utf-8"
-
-    @property
-    def language(self):
-        return ""
-
-    def feed(self, byte_str):
-        for c in byte_str:
-            coding_state = self.coding_sm.next_state(c)
-            if coding_state == MachineState.ERROR:
-                self._state = ProbingState.NOT_ME
-                break
-            elif coding_state == MachineState.ITS_ME:
-                self._state = ProbingState.FOUND_IT
-                break
-            elif coding_state == MachineState.START:
-                if self.coding_sm.get_current_charlen() >= 2:
-                    self._num_mb_chars += 1
-
-        if self.state == ProbingState.DETECTING:
-            if self.get_confidence() > self.SHORTCUT_THRESHOLD:
-                self._state = ProbingState.FOUND_IT
-
-        return self.state
-
-    def get_confidence(self):
-        unlike = 0.99
-        if self._num_mb_chars < 6:
-            unlike *= self.ONE_CHAR_PROB ** self._num_mb_chars
-            return 1.0 - unlike
-        else:
-            return unlike
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/version.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/version.py
deleted file mode 100644
index bb2a34a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/chardet/version.py
+++ /dev/null
@@ -1,9 +0,0 @@
-"""
-This module exists only to simplify retrieving the version number of chardet
-from within setup.py and from chardet subpackages.
-
-:author: Dan Blanchard (dan.blanchard@gmail.com)
-"""
-
-__version__ = "3.0.4"
-VERSION = __version__.split('.')
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__init__.py
deleted file mode 100644
index 2a3bf47..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__init__.py
+++ /dev/null
@@ -1,6 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-from .initialise import init, deinit, reinit, colorama_text
-from .ansi import Fore, Back, Style, Cursor
-from .ansitowin32 import AnsiToWin32
-
-__version__ = '0.4.1'
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 56fd83c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/ansi.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/ansi.cpython-37.pyc
deleted file mode 100644
index bf6f1c5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/ansi.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/ansitowin32.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/ansitowin32.cpython-37.pyc
deleted file mode 100644
index d21905b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/ansitowin32.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/initialise.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/initialise.cpython-37.pyc
deleted file mode 100644
index a79392f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/initialise.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/win32.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/win32.cpython-37.pyc
deleted file mode 100644
index b1b73f9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/win32.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/winterm.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/winterm.cpython-37.pyc
deleted file mode 100644
index a9c9641..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/__pycache__/winterm.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/ansi.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/ansi.py
deleted file mode 100644
index 7877658..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/ansi.py
+++ /dev/null
@@ -1,102 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-'''
-This module generates ANSI character codes to printing colors to terminals.
-See: http://en.wikipedia.org/wiki/ANSI_escape_code
-'''
-
-CSI = '\033['
-OSC = '\033]'
-BEL = '\007'
-
-
-def code_to_chars(code):
-    return CSI + str(code) + 'm'
-
-def set_title(title):
-    return OSC + '2;' + title + BEL
-
-def clear_screen(mode=2):
-    return CSI + str(mode) + 'J'
-
-def clear_line(mode=2):
-    return CSI + str(mode) + 'K'
-
-
-class AnsiCodes(object):
-    def __init__(self):
-        # the subclasses declare class attributes which are numbers.
-        # Upon instantiation we define instance attributes, which are the same
-        # as the class attributes but wrapped with the ANSI escape sequence
-        for name in dir(self):
-            if not name.startswith('_'):
-                value = getattr(self, name)
-                setattr(self, name, code_to_chars(value))
-
-
-class AnsiCursor(object):
-    def UP(self, n=1):
-        return CSI + str(n) + 'A'
-    def DOWN(self, n=1):
-        return CSI + str(n) + 'B'
-    def FORWARD(self, n=1):
-        return CSI + str(n) + 'C'
-    def BACK(self, n=1):
-        return CSI + str(n) + 'D'
-    def POS(self, x=1, y=1):
-        return CSI + str(y) + ';' + str(x) + 'H'
-
-
-class AnsiFore(AnsiCodes):
-    BLACK           = 30
-    RED             = 31
-    GREEN           = 32
-    YELLOW          = 33
-    BLUE            = 34
-    MAGENTA         = 35
-    CYAN            = 36
-    WHITE           = 37
-    RESET           = 39
-
-    # These are fairly well supported, but not part of the standard.
-    LIGHTBLACK_EX   = 90
-    LIGHTRED_EX     = 91
-    LIGHTGREEN_EX   = 92
-    LIGHTYELLOW_EX  = 93
-    LIGHTBLUE_EX    = 94
-    LIGHTMAGENTA_EX = 95
-    LIGHTCYAN_EX    = 96
-    LIGHTWHITE_EX   = 97
-
-
-class AnsiBack(AnsiCodes):
-    BLACK           = 40
-    RED             = 41
-    GREEN           = 42
-    YELLOW          = 43
-    BLUE            = 44
-    MAGENTA         = 45
-    CYAN            = 46
-    WHITE           = 47
-    RESET           = 49
-
-    # These are fairly well supported, but not part of the standard.
-    LIGHTBLACK_EX   = 100
-    LIGHTRED_EX     = 101
-    LIGHTGREEN_EX   = 102
-    LIGHTYELLOW_EX  = 103
-    LIGHTBLUE_EX    = 104
-    LIGHTMAGENTA_EX = 105
-    LIGHTCYAN_EX    = 106
-    LIGHTWHITE_EX   = 107
-
-
-class AnsiStyle(AnsiCodes):
-    BRIGHT    = 1
-    DIM       = 2
-    NORMAL    = 22
-    RESET_ALL = 0
-
-Fore   = AnsiFore()
-Back   = AnsiBack()
-Style  = AnsiStyle()
-Cursor = AnsiCursor()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/ansitowin32.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/ansitowin32.py
deleted file mode 100644
index 359c92b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/ansitowin32.py
+++ /dev/null
@@ -1,257 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-import re
-import sys
-import os
-
-from .ansi import AnsiFore, AnsiBack, AnsiStyle, Style
-from .winterm import WinTerm, WinColor, WinStyle
-from .win32 import windll, winapi_test
-
-
-winterm = None
-if windll is not None:
-    winterm = WinTerm()
-
-
-class StreamWrapper(object):
-    '''
-    Wraps a stream (such as stdout), acting as a transparent proxy for all
-    attribute access apart from method 'write()', which is delegated to our
-    Converter instance.
-    '''
-    def __init__(self, wrapped, converter):
-        # double-underscore everything to prevent clashes with names of
-        # attributes on the wrapped stream object.
-        self.__wrapped = wrapped
-        self.__convertor = converter
-
-    def __getattr__(self, name):
-        return getattr(self.__wrapped, name)
-
-    def __enter__(self, *args, **kwargs):
-        # special method lookup bypasses __getattr__/__getattribute__, see
-        # https://stackoverflow.com/questions/12632894/why-doesnt-getattr-work-with-exit
-        # thus, contextlib magic methods are not proxied via __getattr__
-        return self.__wrapped.__enter__(*args, **kwargs)
-
-    def __exit__(self, *args, **kwargs):
-        return self.__wrapped.__exit__(*args, **kwargs)
-
-    def write(self, text):
-        self.__convertor.write(text)
-
-    def isatty(self):
-        stream = self.__wrapped
-        if 'PYCHARM_HOSTED' in os.environ:
-            if stream is not None and (stream is sys.__stdout__ or stream is sys.__stderr__):
-                return True
-        try:
-            stream_isatty = stream.isatty
-        except AttributeError:
-            return False
-        else:
-            return stream_isatty()
-
-    @property
-    def closed(self):
-        stream = self.__wrapped
-        try:
-            return stream.closed
-        except AttributeError:
-            return True
-
-
-class AnsiToWin32(object):
-    '''
-    Implements a 'write()' method which, on Windows, will strip ANSI character
-    sequences from the text, and if outputting to a tty, will convert them into
-    win32 function calls.
-    '''
-    ANSI_CSI_RE = re.compile('\001?\033\\[((?:\\d|;)*)([a-zA-Z])\002?')   # Control Sequence Introducer
-    ANSI_OSC_RE = re.compile('\001?\033\\]((?:.|;)*?)(\x07)\002?')        # Operating System Command
-
-    def __init__(self, wrapped, convert=None, strip=None, autoreset=False):
-        # The wrapped stream (normally sys.stdout or sys.stderr)
-        self.wrapped = wrapped
-
-        # should we reset colors to defaults after every .write()
-        self.autoreset = autoreset
-
-        # create the proxy wrapping our output stream
-        self.stream = StreamWrapper(wrapped, self)
-
-        on_windows = os.name == 'nt'
-        # We test if the WinAPI works, because even if we are on Windows
-        # we may be using a terminal that doesn't support the WinAPI
-        # (e.g. Cygwin Terminal). In this case it's up to the terminal
-        # to support the ANSI codes.
-        conversion_supported = on_windows and winapi_test()
-
-        # should we strip ANSI sequences from our output?
-        if strip is None:
-            strip = conversion_supported or (not self.stream.closed and not self.stream.isatty())
-        self.strip = strip
-
-        # should we should convert ANSI sequences into win32 calls?
-        if convert is None:
-            convert = conversion_supported and not self.stream.closed and self.stream.isatty()
-        self.convert = convert
-
-        # dict of ansi codes to win32 functions and parameters
-        self.win32_calls = self.get_win32_calls()
-
-        # are we wrapping stderr?
-        self.on_stderr = self.wrapped is sys.stderr
-
-    def should_wrap(self):
-        '''
-        True if this class is actually needed. If false, then the output
-        stream will not be affected, nor will win32 calls be issued, so
-        wrapping stdout is not actually required. This will generally be
-        False on non-Windows platforms, unless optional functionality like
-        autoreset has been requested using kwargs to init()
-        '''
-        return self.convert or self.strip or self.autoreset
-
-    def get_win32_calls(self):
-        if self.convert and winterm:
-            return {
-                AnsiStyle.RESET_ALL: (winterm.reset_all, ),
-                AnsiStyle.BRIGHT: (winterm.style, WinStyle.BRIGHT),
-                AnsiStyle.DIM: (winterm.style, WinStyle.NORMAL),
-                AnsiStyle.NORMAL: (winterm.style, WinStyle.NORMAL),
-                AnsiFore.BLACK: (winterm.fore, WinColor.BLACK),
-                AnsiFore.RED: (winterm.fore, WinColor.RED),
-                AnsiFore.GREEN: (winterm.fore, WinColor.GREEN),
-                AnsiFore.YELLOW: (winterm.fore, WinColor.YELLOW),
-                AnsiFore.BLUE: (winterm.fore, WinColor.BLUE),
-                AnsiFore.MAGENTA: (winterm.fore, WinColor.MAGENTA),
-                AnsiFore.CYAN: (winterm.fore, WinColor.CYAN),
-                AnsiFore.WHITE: (winterm.fore, WinColor.GREY),
-                AnsiFore.RESET: (winterm.fore, ),
-                AnsiFore.LIGHTBLACK_EX: (winterm.fore, WinColor.BLACK, True),
-                AnsiFore.LIGHTRED_EX: (winterm.fore, WinColor.RED, True),
-                AnsiFore.LIGHTGREEN_EX: (winterm.fore, WinColor.GREEN, True),
-                AnsiFore.LIGHTYELLOW_EX: (winterm.fore, WinColor.YELLOW, True),
-                AnsiFore.LIGHTBLUE_EX: (winterm.fore, WinColor.BLUE, True),
-                AnsiFore.LIGHTMAGENTA_EX: (winterm.fore, WinColor.MAGENTA, True),
-                AnsiFore.LIGHTCYAN_EX: (winterm.fore, WinColor.CYAN, True),
-                AnsiFore.LIGHTWHITE_EX: (winterm.fore, WinColor.GREY, True),
-                AnsiBack.BLACK: (winterm.back, WinColor.BLACK),
-                AnsiBack.RED: (winterm.back, WinColor.RED),
-                AnsiBack.GREEN: (winterm.back, WinColor.GREEN),
-                AnsiBack.YELLOW: (winterm.back, WinColor.YELLOW),
-                AnsiBack.BLUE: (winterm.back, WinColor.BLUE),
-                AnsiBack.MAGENTA: (winterm.back, WinColor.MAGENTA),
-                AnsiBack.CYAN: (winterm.back, WinColor.CYAN),
-                AnsiBack.WHITE: (winterm.back, WinColor.GREY),
-                AnsiBack.RESET: (winterm.back, ),
-                AnsiBack.LIGHTBLACK_EX: (winterm.back, WinColor.BLACK, True),
-                AnsiBack.LIGHTRED_EX: (winterm.back, WinColor.RED, True),
-                AnsiBack.LIGHTGREEN_EX: (winterm.back, WinColor.GREEN, True),
-                AnsiBack.LIGHTYELLOW_EX: (winterm.back, WinColor.YELLOW, True),
-                AnsiBack.LIGHTBLUE_EX: (winterm.back, WinColor.BLUE, True),
-                AnsiBack.LIGHTMAGENTA_EX: (winterm.back, WinColor.MAGENTA, True),
-                AnsiBack.LIGHTCYAN_EX: (winterm.back, WinColor.CYAN, True),
-                AnsiBack.LIGHTWHITE_EX: (winterm.back, WinColor.GREY, True),
-            }
-        return dict()
-
-    def write(self, text):
-        if self.strip or self.convert:
-            self.write_and_convert(text)
-        else:
-            self.wrapped.write(text)
-            self.wrapped.flush()
-        if self.autoreset:
-            self.reset_all()
-
-
-    def reset_all(self):
-        if self.convert:
-            self.call_win32('m', (0,))
-        elif not self.strip and not self.stream.closed:
-            self.wrapped.write(Style.RESET_ALL)
-
-
-    def write_and_convert(self, text):
-        '''
-        Write the given text to our wrapped stream, stripping any ANSI
-        sequences from the text, and optionally converting them into win32
-        calls.
-        '''
-        cursor = 0
-        text = self.convert_osc(text)
-        for match in self.ANSI_CSI_RE.finditer(text):
-            start, end = match.span()
-            self.write_plain_text(text, cursor, start)
-            self.convert_ansi(*match.groups())
-            cursor = end
-        self.write_plain_text(text, cursor, len(text))
-
-
-    def write_plain_text(self, text, start, end):
-        if start < end:
-            self.wrapped.write(text[start:end])
-            self.wrapped.flush()
-
-
-    def convert_ansi(self, paramstring, command):
-        if self.convert:
-            params = self.extract_params(command, paramstring)
-            self.call_win32(command, params)
-
-
-    def extract_params(self, command, paramstring):
-        if command in 'Hf':
-            params = tuple(int(p) if len(p) != 0 else 1 for p in paramstring.split(';'))
-            while len(params) < 2:
-                # defaults:
-                params = params + (1,)
-        else:
-            params = tuple(int(p) for p in paramstring.split(';') if len(p) != 0)
-            if len(params) == 0:
-                # defaults:
-                if command in 'JKm':
-                    params = (0,)
-                elif command in 'ABCD':
-                    params = (1,)
-
-        return params
-
-
-    def call_win32(self, command, params):
-        if command == 'm':
-            for param in params:
-                if param in self.win32_calls:
-                    func_args = self.win32_calls[param]
-                    func = func_args[0]
-                    args = func_args[1:]
-                    kwargs = dict(on_stderr=self.on_stderr)
-                    func(*args, **kwargs)
-        elif command in 'J':
-            winterm.erase_screen(params[0], on_stderr=self.on_stderr)
-        elif command in 'K':
-            winterm.erase_line(params[0], on_stderr=self.on_stderr)
-        elif command in 'Hf':     # cursor position - absolute
-            winterm.set_cursor_position(params, on_stderr=self.on_stderr)
-        elif command in 'ABCD':   # cursor position - relative
-            n = params[0]
-            # A - up, B - down, C - forward, D - back
-            x, y = {'A': (0, -n), 'B': (0, n), 'C': (n, 0), 'D': (-n, 0)}[command]
-            winterm.cursor_adjust(x, y, on_stderr=self.on_stderr)
-
-
-    def convert_osc(self, text):
-        for match in self.ANSI_OSC_RE.finditer(text):
-            start, end = match.span()
-            text = text[:start] + text[end:]
-            paramstring, command = match.groups()
-            if command in '\x07':       # \x07 = BEL
-                params = paramstring.split(";")
-                # 0 - change title and icon (we will only change title)
-                # 1 - change icon (we don't support this)
-                # 2 - change title
-                if params[0] in '02':
-                    winterm.set_title(params[1])
-        return text
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/initialise.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/initialise.py
deleted file mode 100644
index 430d066..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/initialise.py
+++ /dev/null
@@ -1,80 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-import atexit
-import contextlib
-import sys
-
-from .ansitowin32 import AnsiToWin32
-
-
-orig_stdout = None
-orig_stderr = None
-
-wrapped_stdout = None
-wrapped_stderr = None
-
-atexit_done = False
-
-
-def reset_all():
-    if AnsiToWin32 is not None:    # Issue #74: objects might become None at exit
-        AnsiToWin32(orig_stdout).reset_all()
-
-
-def init(autoreset=False, convert=None, strip=None, wrap=True):
-
-    if not wrap and any([autoreset, convert, strip]):
-        raise ValueError('wrap=False conflicts with any other arg=True')
-
-    global wrapped_stdout, wrapped_stderr
-    global orig_stdout, orig_stderr
-
-    orig_stdout = sys.stdout
-    orig_stderr = sys.stderr
-
-    if sys.stdout is None:
-        wrapped_stdout = None
-    else:
-        sys.stdout = wrapped_stdout = \
-            wrap_stream(orig_stdout, convert, strip, autoreset, wrap)
-    if sys.stderr is None:
-        wrapped_stderr = None
-    else:
-        sys.stderr = wrapped_stderr = \
-            wrap_stream(orig_stderr, convert, strip, autoreset, wrap)
-
-    global atexit_done
-    if not atexit_done:
-        atexit.register(reset_all)
-        atexit_done = True
-
-
-def deinit():
-    if orig_stdout is not None:
-        sys.stdout = orig_stdout
-    if orig_stderr is not None:
-        sys.stderr = orig_stderr
-
-
-@contextlib.contextmanager
-def colorama_text(*args, **kwargs):
-    init(*args, **kwargs)
-    try:
-        yield
-    finally:
-        deinit()
-
-
-def reinit():
-    if wrapped_stdout is not None:
-        sys.stdout = wrapped_stdout
-    if wrapped_stderr is not None:
-        sys.stderr = wrapped_stderr
-
-
-def wrap_stream(stream, convert, strip, autoreset, wrap):
-    if wrap:
-        wrapper = AnsiToWin32(stream,
-            convert=convert, strip=strip, autoreset=autoreset)
-        if wrapper.should_wrap():
-            stream = wrapper.stream
-    return stream
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/win32.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/win32.py
deleted file mode 100644
index c2d8360..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/win32.py
+++ /dev/null
@@ -1,152 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-
-# from winbase.h
-STDOUT = -11
-STDERR = -12
-
-try:
-    import ctypes
-    from ctypes import LibraryLoader
-    windll = LibraryLoader(ctypes.WinDLL)
-    from ctypes import wintypes
-except (AttributeError, ImportError):
-    windll = None
-    SetConsoleTextAttribute = lambda *_: None
-    winapi_test = lambda *_: None
-else:
-    from ctypes import byref, Structure, c_char, POINTER
-
-    COORD = wintypes._COORD
-
-    class CONSOLE_SCREEN_BUFFER_INFO(Structure):
-        """struct in wincon.h."""
-        _fields_ = [
-            ("dwSize", COORD),
-            ("dwCursorPosition", COORD),
-            ("wAttributes", wintypes.WORD),
-            ("srWindow", wintypes.SMALL_RECT),
-            ("dwMaximumWindowSize", COORD),
-        ]
-        def __str__(self):
-            return '(%d,%d,%d,%d,%d,%d,%d,%d,%d,%d,%d)' % (
-                self.dwSize.Y, self.dwSize.X
-                , self.dwCursorPosition.Y, self.dwCursorPosition.X
-                , self.wAttributes
-                , self.srWindow.Top, self.srWindow.Left, self.srWindow.Bottom, self.srWindow.Right
-                , self.dwMaximumWindowSize.Y, self.dwMaximumWindowSize.X
-            )
-
-    _GetStdHandle = windll.kernel32.GetStdHandle
-    _GetStdHandle.argtypes = [
-        wintypes.DWORD,
-    ]
-    _GetStdHandle.restype = wintypes.HANDLE
-
-    _GetConsoleScreenBufferInfo = windll.kernel32.GetConsoleScreenBufferInfo
-    _GetConsoleScreenBufferInfo.argtypes = [
-        wintypes.HANDLE,
-        POINTER(CONSOLE_SCREEN_BUFFER_INFO),
-    ]
-    _GetConsoleScreenBufferInfo.restype = wintypes.BOOL
-
-    _SetConsoleTextAttribute = windll.kernel32.SetConsoleTextAttribute
-    _SetConsoleTextAttribute.argtypes = [
-        wintypes.HANDLE,
-        wintypes.WORD,
-    ]
-    _SetConsoleTextAttribute.restype = wintypes.BOOL
-
-    _SetConsoleCursorPosition = windll.kernel32.SetConsoleCursorPosition
-    _SetConsoleCursorPosition.argtypes = [
-        wintypes.HANDLE,
-        COORD,
-    ]
-    _SetConsoleCursorPosition.restype = wintypes.BOOL
-
-    _FillConsoleOutputCharacterA = windll.kernel32.FillConsoleOutputCharacterA
-    _FillConsoleOutputCharacterA.argtypes = [
-        wintypes.HANDLE,
-        c_char,
-        wintypes.DWORD,
-        COORD,
-        POINTER(wintypes.DWORD),
-    ]
-    _FillConsoleOutputCharacterA.restype = wintypes.BOOL
-
-    _FillConsoleOutputAttribute = windll.kernel32.FillConsoleOutputAttribute
-    _FillConsoleOutputAttribute.argtypes = [
-        wintypes.HANDLE,
-        wintypes.WORD,
-        wintypes.DWORD,
-        COORD,
-        POINTER(wintypes.DWORD),
-    ]
-    _FillConsoleOutputAttribute.restype = wintypes.BOOL
-
-    _SetConsoleTitleW = windll.kernel32.SetConsoleTitleW
-    _SetConsoleTitleW.argtypes = [
-        wintypes.LPCWSTR
-    ]
-    _SetConsoleTitleW.restype = wintypes.BOOL
-
-    def _winapi_test(handle):
-        csbi = CONSOLE_SCREEN_BUFFER_INFO()
-        success = _GetConsoleScreenBufferInfo(
-            handle, byref(csbi))
-        return bool(success)
-
-    def winapi_test():
-        return any(_winapi_test(h) for h in
-                   (_GetStdHandle(STDOUT), _GetStdHandle(STDERR)))
-
-    def GetConsoleScreenBufferInfo(stream_id=STDOUT):
-        handle = _GetStdHandle(stream_id)
-        csbi = CONSOLE_SCREEN_BUFFER_INFO()
-        success = _GetConsoleScreenBufferInfo(
-            handle, byref(csbi))
-        return csbi
-
-    def SetConsoleTextAttribute(stream_id, attrs):
-        handle = _GetStdHandle(stream_id)
-        return _SetConsoleTextAttribute(handle, attrs)
-
-    def SetConsoleCursorPosition(stream_id, position, adjust=True):
-        position = COORD(*position)
-        # If the position is out of range, do nothing.
-        if position.Y <= 0 or position.X <= 0:
-            return
-        # Adjust for Windows' SetConsoleCursorPosition:
-        #    1. being 0-based, while ANSI is 1-based.
-        #    2. expecting (x,y), while ANSI uses (y,x).
-        adjusted_position = COORD(position.Y - 1, position.X - 1)
-        if adjust:
-            # Adjust for viewport's scroll position
-            sr = GetConsoleScreenBufferInfo(STDOUT).srWindow
-            adjusted_position.Y += sr.Top
-            adjusted_position.X += sr.Left
-        # Resume normal processing
-        handle = _GetStdHandle(stream_id)
-        return _SetConsoleCursorPosition(handle, adjusted_position)
-
-    def FillConsoleOutputCharacter(stream_id, char, length, start):
-        handle = _GetStdHandle(stream_id)
-        char = c_char(char.encode())
-        length = wintypes.DWORD(length)
-        num_written = wintypes.DWORD(0)
-        # Note that this is hard-coded for ANSI (vs wide) bytes.
-        success = _FillConsoleOutputCharacterA(
-            handle, char, length, start, byref(num_written))
-        return num_written.value
-
-    def FillConsoleOutputAttribute(stream_id, attr, length, start):
-        ''' FillConsoleOutputAttribute( hConsole, csbi.wAttributes, dwConSize, coordScreen, &cCharsWritten )'''
-        handle = _GetStdHandle(stream_id)
-        attribute = wintypes.WORD(attr)
-        length = wintypes.DWORD(length)
-        num_written = wintypes.DWORD(0)
-        # Note that this is hard-coded for ANSI (vs wide) bytes.
-        return _FillConsoleOutputAttribute(
-            handle, attribute, length, start, byref(num_written))
-
-    def SetConsoleTitle(title):
-        return _SetConsoleTitleW(title)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/winterm.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/winterm.py
deleted file mode 100644
index 0fdb4ec..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/colorama/winterm.py
+++ /dev/null
@@ -1,169 +0,0 @@
-# Copyright Jonathan Hartley 2013. BSD 3-Clause license, see LICENSE file.
-from . import win32
-
-
-# from wincon.h
-class WinColor(object):
-    BLACK   = 0
-    BLUE    = 1
-    GREEN   = 2
-    CYAN    = 3
-    RED     = 4
-    MAGENTA = 5
-    YELLOW  = 6
-    GREY    = 7
-
-# from wincon.h
-class WinStyle(object):
-    NORMAL              = 0x00 # dim text, dim background
-    BRIGHT              = 0x08 # bright text, dim background
-    BRIGHT_BACKGROUND   = 0x80 # dim text, bright background
-
-class WinTerm(object):
-
-    def __init__(self):
-        self._default = win32.GetConsoleScreenBufferInfo(win32.STDOUT).wAttributes
-        self.set_attrs(self._default)
-        self._default_fore = self._fore
-        self._default_back = self._back
-        self._default_style = self._style
-        # In order to emulate LIGHT_EX in windows, we borrow the BRIGHT style.
-        # So that LIGHT_EX colors and BRIGHT style do not clobber each other,
-        # we track them separately, since LIGHT_EX is overwritten by Fore/Back
-        # and BRIGHT is overwritten by Style codes.
-        self._light = 0
-
-    def get_attrs(self):
-        return self._fore + self._back * 16 + (self._style | self._light)
-
-    def set_attrs(self, value):
-        self._fore = value & 7
-        self._back = (value >> 4) & 7
-        self._style = value & (WinStyle.BRIGHT | WinStyle.BRIGHT_BACKGROUND)
-
-    def reset_all(self, on_stderr=None):
-        self.set_attrs(self._default)
-        self.set_console(attrs=self._default)
-        self._light = 0
-
-    def fore(self, fore=None, light=False, on_stderr=False):
-        if fore is None:
-            fore = self._default_fore
-        self._fore = fore
-        # Emulate LIGHT_EX with BRIGHT Style
-        if light:
-            self._light |= WinStyle.BRIGHT
-        else:
-            self._light &= ~WinStyle.BRIGHT
-        self.set_console(on_stderr=on_stderr)
-
-    def back(self, back=None, light=False, on_stderr=False):
-        if back is None:
-            back = self._default_back
-        self._back = back
-        # Emulate LIGHT_EX with BRIGHT_BACKGROUND Style
-        if light:
-            self._light |= WinStyle.BRIGHT_BACKGROUND
-        else:
-            self._light &= ~WinStyle.BRIGHT_BACKGROUND
-        self.set_console(on_stderr=on_stderr)
-
-    def style(self, style=None, on_stderr=False):
-        if style is None:
-            style = self._default_style
-        self._style = style
-        self.set_console(on_stderr=on_stderr)
-
-    def set_console(self, attrs=None, on_stderr=False):
-        if attrs is None:
-            attrs = self.get_attrs()
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        win32.SetConsoleTextAttribute(handle, attrs)
-
-    def get_position(self, handle):
-        position = win32.GetConsoleScreenBufferInfo(handle).dwCursorPosition
-        # Because Windows coordinates are 0-based,
-        # and win32.SetConsoleCursorPosition expects 1-based.
-        position.X += 1
-        position.Y += 1
-        return position
-
-    def set_cursor_position(self, position=None, on_stderr=False):
-        if position is None:
-            # I'm not currently tracking the position, so there is no default.
-            # position = self.get_position()
-            return
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        win32.SetConsoleCursorPosition(handle, position)
-
-    def cursor_adjust(self, x, y, on_stderr=False):
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        position = self.get_position(handle)
-        adjusted_position = (position.Y + y, position.X + x)
-        win32.SetConsoleCursorPosition(handle, adjusted_position, adjust=False)
-
-    def erase_screen(self, mode=0, on_stderr=False):
-        # 0 should clear from the cursor to the end of the screen.
-        # 1 should clear from the cursor to the beginning of the screen.
-        # 2 should clear the entire screen, and move cursor to (1,1)
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        csbi = win32.GetConsoleScreenBufferInfo(handle)
-        # get the number of character cells in the current buffer
-        cells_in_screen = csbi.dwSize.X * csbi.dwSize.Y
-        # get number of character cells before current cursor position
-        cells_before_cursor = csbi.dwSize.X * csbi.dwCursorPosition.Y + csbi.dwCursorPosition.X
-        if mode == 0:
-            from_coord = csbi.dwCursorPosition
-            cells_to_erase = cells_in_screen - cells_before_cursor
-        elif mode == 1:
-            from_coord = win32.COORD(0, 0)
-            cells_to_erase = cells_before_cursor
-        elif mode == 2:
-            from_coord = win32.COORD(0, 0)
-            cells_to_erase = cells_in_screen
-        else:
-            # invalid mode
-            return
-        # fill the entire screen with blanks
-        win32.FillConsoleOutputCharacter(handle, ' ', cells_to_erase, from_coord)
-        # now set the buffer's attributes accordingly
-        win32.FillConsoleOutputAttribute(handle, self.get_attrs(), cells_to_erase, from_coord)
-        if mode == 2:
-            # put the cursor where needed
-            win32.SetConsoleCursorPosition(handle, (1, 1))
-
-    def erase_line(self, mode=0, on_stderr=False):
-        # 0 should clear from the cursor to the end of the line.
-        # 1 should clear from the cursor to the beginning of the line.
-        # 2 should clear the entire line.
-        handle = win32.STDOUT
-        if on_stderr:
-            handle = win32.STDERR
-        csbi = win32.GetConsoleScreenBufferInfo(handle)
-        if mode == 0:
-            from_coord = csbi.dwCursorPosition
-            cells_to_erase = csbi.dwSize.X - csbi.dwCursorPosition.X
-        elif mode == 1:
-            from_coord = win32.COORD(0, csbi.dwCursorPosition.Y)
-            cells_to_erase = csbi.dwCursorPosition.X
-        elif mode == 2:
-            from_coord = win32.COORD(0, csbi.dwCursorPosition.Y)
-            cells_to_erase = csbi.dwSize.X
-        else:
-            # invalid mode
-            return
-        # fill the entire screen with blanks
-        win32.FillConsoleOutputCharacter(handle, ' ', cells_to_erase, from_coord)
-        # now set the buffer's attributes accordingly
-        win32.FillConsoleOutputAttribute(handle, self.get_attrs(), cells_to_erase, from_coord)
-
-    def set_title(self, title):
-        win32.SetConsoleTitle(title)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__init__.py
deleted file mode 100644
index a786b4d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__init__.py
+++ /dev/null
@@ -1,23 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012-2017 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-import logging
-
-__version__ = '0.2.8'
-
-class DistlibException(Exception):
-    pass
-
-try:
-    from logging import NullHandler
-except ImportError: # pragma: no cover
-    class NullHandler(logging.Handler):
-        def handle(self, record): pass
-        def emit(self, record): pass
-        def createLock(self): self.lock = None
-
-logger = logging.getLogger(__name__)
-logger.addHandler(NullHandler())
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index d988eb4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/compat.cpython-37.pyc
deleted file mode 100644
index 86a7b46..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/resources.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/resources.cpython-37.pyc
deleted file mode 100644
index 736c226..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/resources.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/scripts.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/scripts.cpython-37.pyc
deleted file mode 100644
index 2e01f4a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/scripts.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/util.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/util.cpython-37.pyc
deleted file mode 100644
index 99bedb1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/__pycache__/util.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/__init__.py
deleted file mode 100644
index f7dbf4c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/__init__.py
+++ /dev/null
@@ -1,6 +0,0 @@
-"""Modules copied from Python 3 standard libraries, for internal use only.
-
-Individual classes and functions are found in d2._backport.misc.  Intended
-usage is to always import things missing from 3.1 from that module: the
-built-in/stdlib objects will be used if found.
-"""
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/misc.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/misc.py
deleted file mode 100644
index cfb318d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/misc.py
+++ /dev/null
@@ -1,41 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012 The Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""Backports for individual classes and functions."""
-
-import os
-import sys
-
-__all__ = ['cache_from_source', 'callable', 'fsencode']
-
-
-try:
-    from imp import cache_from_source
-except ImportError:
-    def cache_from_source(py_file, debug=__debug__):
-        ext = debug and 'c' or 'o'
-        return py_file + ext
-
-
-try:
-    callable = callable
-except NameError:
-    from collections import Callable
-
-    def callable(obj):
-        return isinstance(obj, Callable)
-
-
-try:
-    fsencode = os.fsencode
-except AttributeError:
-    def fsencode(filename):
-        if isinstance(filename, bytes):
-            return filename
-        elif isinstance(filename, str):
-            return filename.encode(sys.getfilesystemencoding())
-        else:
-            raise TypeError("expect bytes or str, not %s" %
-                            type(filename).__name__)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/shutil.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/shutil.py
deleted file mode 100644
index 159e49e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/shutil.py
+++ /dev/null
@@ -1,761 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012 The Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""Utility functions for copying and archiving files and directory trees.
-
-XXX The functions here don't copy the resource fork or other metadata on Mac.
-
-"""
-
-import os
-import sys
-import stat
-from os.path import abspath
-import fnmatch
-import collections
-import errno
-from . import tarfile
-
-try:
-    import bz2
-    _BZ2_SUPPORTED = True
-except ImportError:
-    _BZ2_SUPPORTED = False
-
-try:
-    from pwd import getpwnam
-except ImportError:
-    getpwnam = None
-
-try:
-    from grp import getgrnam
-except ImportError:
-    getgrnam = None
-
-__all__ = ["copyfileobj", "copyfile", "copymode", "copystat", "copy", "copy2",
-           "copytree", "move", "rmtree", "Error", "SpecialFileError",
-           "ExecError", "make_archive", "get_archive_formats",
-           "register_archive_format", "unregister_archive_format",
-           "get_unpack_formats", "register_unpack_format",
-           "unregister_unpack_format", "unpack_archive", "ignore_patterns"]
-
-class Error(EnvironmentError):
-    pass
-
-class SpecialFileError(EnvironmentError):
-    """Raised when trying to do a kind of operation (e.g. copying) which is
-    not supported on a special file (e.g. a named pipe)"""
-
-class ExecError(EnvironmentError):
-    """Raised when a command could not be executed"""
-
-class ReadError(EnvironmentError):
-    """Raised when an archive cannot be read"""
-
-class RegistryError(Exception):
-    """Raised when a registry operation with the archiving
-    and unpacking registries fails"""
-
-
-try:
-    WindowsError
-except NameError:
-    WindowsError = None
-
-def copyfileobj(fsrc, fdst, length=16*1024):
-    """copy data from file-like object fsrc to file-like object fdst"""
-    while 1:
-        buf = fsrc.read(length)
-        if not buf:
-            break
-        fdst.write(buf)
-
-def _samefile(src, dst):
-    # Macintosh, Unix.
-    if hasattr(os.path, 'samefile'):
-        try:
-            return os.path.samefile(src, dst)
-        except OSError:
-            return False
-
-    # All other platforms: check for same pathname.
-    return (os.path.normcase(os.path.abspath(src)) ==
-            os.path.normcase(os.path.abspath(dst)))
-
-def copyfile(src, dst):
-    """Copy data from src to dst"""
-    if _samefile(src, dst):
-        raise Error("`%s` and `%s` are the same file" % (src, dst))
-
-    for fn in [src, dst]:
-        try:
-            st = os.stat(fn)
-        except OSError:
-            # File most likely does not exist
-            pass
-        else:
-            # XXX What about other special files? (sockets, devices...)
-            if stat.S_ISFIFO(st.st_mode):
-                raise SpecialFileError("`%s` is a named pipe" % fn)
-
-    with open(src, 'rb') as fsrc:
-        with open(dst, 'wb') as fdst:
-            copyfileobj(fsrc, fdst)
-
-def copymode(src, dst):
-    """Copy mode bits from src to dst"""
-    if hasattr(os, 'chmod'):
-        st = os.stat(src)
-        mode = stat.S_IMODE(st.st_mode)
-        os.chmod(dst, mode)
-
-def copystat(src, dst):
-    """Copy all stat info (mode bits, atime, mtime, flags) from src to dst"""
-    st = os.stat(src)
-    mode = stat.S_IMODE(st.st_mode)
-    if hasattr(os, 'utime'):
-        os.utime(dst, (st.st_atime, st.st_mtime))
-    if hasattr(os, 'chmod'):
-        os.chmod(dst, mode)
-    if hasattr(os, 'chflags') and hasattr(st, 'st_flags'):
-        try:
-            os.chflags(dst, st.st_flags)
-        except OSError as why:
-            if (not hasattr(errno, 'EOPNOTSUPP') or
-                why.errno != errno.EOPNOTSUPP):
-                raise
-
-def copy(src, dst):
-    """Copy data and mode bits ("cp src dst").
-
-    The destination may be a directory.
-
-    """
-    if os.path.isdir(dst):
-        dst = os.path.join(dst, os.path.basename(src))
-    copyfile(src, dst)
-    copymode(src, dst)
-
-def copy2(src, dst):
-    """Copy data and all stat info ("cp -p src dst").
-
-    The destination may be a directory.
-
-    """
-    if os.path.isdir(dst):
-        dst = os.path.join(dst, os.path.basename(src))
-    copyfile(src, dst)
-    copystat(src, dst)
-
-def ignore_patterns(*patterns):
-    """Function that can be used as copytree() ignore parameter.
-
-    Patterns is a sequence of glob-style patterns
-    that are used to exclude files"""
-    def _ignore_patterns(path, names):
-        ignored_names = []
-        for pattern in patterns:
-            ignored_names.extend(fnmatch.filter(names, pattern))
-        return set(ignored_names)
-    return _ignore_patterns
-
-def copytree(src, dst, symlinks=False, ignore=None, copy_function=copy2,
-             ignore_dangling_symlinks=False):
-    """Recursively copy a directory tree.
-
-    The destination directory must not already exist.
-    If exception(s) occur, an Error is raised with a list of reasons.
-
-    If the optional symlinks flag is true, symbolic links in the
-    source tree result in symbolic links in the destination tree; if
-    it is false, the contents of the files pointed to by symbolic
-    links are copied. If the file pointed by the symlink doesn't
-    exist, an exception will be added in the list of errors raised in
-    an Error exception at the end of the copy process.
-
-    You can set the optional ignore_dangling_symlinks flag to true if you
-    want to silence this exception. Notice that this has no effect on
-    platforms that don't support os.symlink.
-
-    The optional ignore argument is a callable. If given, it
-    is called with the `src` parameter, which is the directory
-    being visited by copytree(), and `names` which is the list of
-    `src` contents, as returned by os.listdir():
-
-        callable(src, names) -> ignored_names
-
-    Since copytree() is called recursively, the callable will be
-    called once for each directory that is copied. It returns a
-    list of names relative to the `src` directory that should
-    not be copied.
-
-    The optional copy_function argument is a callable that will be used
-    to copy each file. It will be called with the source path and the
-    destination path as arguments. By default, copy2() is used, but any
-    function that supports the same signature (like copy()) can be used.
-
-    """
-    names = os.listdir(src)
-    if ignore is not None:
-        ignored_names = ignore(src, names)
-    else:
-        ignored_names = set()
-
-    os.makedirs(dst)
-    errors = []
-    for name in names:
-        if name in ignored_names:
-            continue
-        srcname = os.path.join(src, name)
-        dstname = os.path.join(dst, name)
-        try:
-            if os.path.islink(srcname):
-                linkto = os.readlink(srcname)
-                if symlinks:
-                    os.symlink(linkto, dstname)
-                else:
-                    # ignore dangling symlink if the flag is on
-                    if not os.path.exists(linkto) and ignore_dangling_symlinks:
-                        continue
-                    # otherwise let the copy occurs. copy2 will raise an error
-                    copy_function(srcname, dstname)
-            elif os.path.isdir(srcname):
-                copytree(srcname, dstname, symlinks, ignore, copy_function)
-            else:
-                # Will raise a SpecialFileError for unsupported file types
-                copy_function(srcname, dstname)
-        # catch the Error from the recursive copytree so that we can
-        # continue with other files
-        except Error as err:
-            errors.extend(err.args[0])
-        except EnvironmentError as why:
-            errors.append((srcname, dstname, str(why)))
-    try:
-        copystat(src, dst)
-    except OSError as why:
-        if WindowsError is not None and isinstance(why, WindowsError):
-            # Copying file access times may fail on Windows
-            pass
-        else:
-            errors.extend((src, dst, str(why)))
-    if errors:
-        raise Error(errors)
-
-def rmtree(path, ignore_errors=False, onerror=None):
-    """Recursively delete a directory tree.
-
-    If ignore_errors is set, errors are ignored; otherwise, if onerror
-    is set, it is called to handle the error with arguments (func,
-    path, exc_info) where func is os.listdir, os.remove, or os.rmdir;
-    path is the argument to that function that caused it to fail; and
-    exc_info is a tuple returned by sys.exc_info().  If ignore_errors
-    is false and onerror is None, an exception is raised.
-
-    """
-    if ignore_errors:
-        def onerror(*args):
-            pass
-    elif onerror is None:
-        def onerror(*args):
-            raise
-    try:
-        if os.path.islink(path):
-            # symlinks to directories are forbidden, see bug #1669
-            raise OSError("Cannot call rmtree on a symbolic link")
-    except OSError:
-        onerror(os.path.islink, path, sys.exc_info())
-        # can't continue even if onerror hook returns
-        return
-    names = []
-    try:
-        names = os.listdir(path)
-    except os.error:
-        onerror(os.listdir, path, sys.exc_info())
-    for name in names:
-        fullname = os.path.join(path, name)
-        try:
-            mode = os.lstat(fullname).st_mode
-        except os.error:
-            mode = 0
-        if stat.S_ISDIR(mode):
-            rmtree(fullname, ignore_errors, onerror)
-        else:
-            try:
-                os.remove(fullname)
-            except os.error:
-                onerror(os.remove, fullname, sys.exc_info())
-    try:
-        os.rmdir(path)
-    except os.error:
-        onerror(os.rmdir, path, sys.exc_info())
-
-
-def _basename(path):
-    # A basename() variant which first strips the trailing slash, if present.
-    # Thus we always get the last component of the path, even for directories.
-    return os.path.basename(path.rstrip(os.path.sep))
-
-def move(src, dst):
-    """Recursively move a file or directory to another location. This is
-    similar to the Unix "mv" command.
-
-    If the destination is a directory or a symlink to a directory, the source
-    is moved inside the directory. The destination path must not already
-    exist.
-
-    If the destination already exists but is not a directory, it may be
-    overwritten depending on os.rename() semantics.
-
-    If the destination is on our current filesystem, then rename() is used.
-    Otherwise, src is copied to the destination and then removed.
-    A lot more could be done here...  A look at a mv.c shows a lot of
-    the issues this implementation glosses over.
-
-    """
-    real_dst = dst
-    if os.path.isdir(dst):
-        if _samefile(src, dst):
-            # We might be on a case insensitive filesystem,
-            # perform the rename anyway.
-            os.rename(src, dst)
-            return
-
-        real_dst = os.path.join(dst, _basename(src))
-        if os.path.exists(real_dst):
-            raise Error("Destination path '%s' already exists" % real_dst)
-    try:
-        os.rename(src, real_dst)
-    except OSError:
-        if os.path.isdir(src):
-            if _destinsrc(src, dst):
-                raise Error("Cannot move a directory '%s' into itself '%s'." % (src, dst))
-            copytree(src, real_dst, symlinks=True)
-            rmtree(src)
-        else:
-            copy2(src, real_dst)
-            os.unlink(src)
-
-def _destinsrc(src, dst):
-    src = abspath(src)
-    dst = abspath(dst)
-    if not src.endswith(os.path.sep):
-        src += os.path.sep
-    if not dst.endswith(os.path.sep):
-        dst += os.path.sep
-    return dst.startswith(src)
-
-def _get_gid(name):
-    """Returns a gid, given a group name."""
-    if getgrnam is None or name is None:
-        return None
-    try:
-        result = getgrnam(name)
-    except KeyError:
-        result = None
-    if result is not None:
-        return result[2]
-    return None
-
-def _get_uid(name):
-    """Returns an uid, given a user name."""
-    if getpwnam is None or name is None:
-        return None
-    try:
-        result = getpwnam(name)
-    except KeyError:
-        result = None
-    if result is not None:
-        return result[2]
-    return None
-
-def _make_tarball(base_name, base_dir, compress="gzip", verbose=0, dry_run=0,
-                  owner=None, group=None, logger=None):
-    """Create a (possibly compressed) tar file from all the files under
-    'base_dir'.
-
-    'compress' must be "gzip" (the default), "bzip2", or None.
-
-    'owner' and 'group' can be used to define an owner and a group for the
-    archive that is being built. If not provided, the current owner and group
-    will be used.
-
-    The output tar file will be named 'base_name' +  ".tar", possibly plus
-    the appropriate compression extension (".gz", or ".bz2").
-
-    Returns the output filename.
-    """
-    tar_compression = {'gzip': 'gz', None: ''}
-    compress_ext = {'gzip': '.gz'}
-
-    if _BZ2_SUPPORTED:
-        tar_compression['bzip2'] = 'bz2'
-        compress_ext['bzip2'] = '.bz2'
-
-    # flags for compression program, each element of list will be an argument
-    if compress is not None and compress not in compress_ext:
-        raise ValueError("bad value for 'compress', or compression format not "
-                         "supported : {0}".format(compress))
-
-    archive_name = base_name + '.tar' + compress_ext.get(compress, '')
-    archive_dir = os.path.dirname(archive_name)
-
-    if not os.path.exists(archive_dir):
-        if logger is not None:
-            logger.info("creating %s", archive_dir)
-        if not dry_run:
-            os.makedirs(archive_dir)
-
-    # creating the tarball
-    if logger is not None:
-        logger.info('Creating tar archive')
-
-    uid = _get_uid(owner)
-    gid = _get_gid(group)
-
-    def _set_uid_gid(tarinfo):
-        if gid is not None:
-            tarinfo.gid = gid
-            tarinfo.gname = group
-        if uid is not None:
-            tarinfo.uid = uid
-            tarinfo.uname = owner
-        return tarinfo
-
-    if not dry_run:
-        tar = tarfile.open(archive_name, 'w|%s' % tar_compression[compress])
-        try:
-            tar.add(base_dir, filter=_set_uid_gid)
-        finally:
-            tar.close()
-
-    return archive_name
-
-def _call_external_zip(base_dir, zip_filename, verbose=False, dry_run=False):
-    # XXX see if we want to keep an external call here
-    if verbose:
-        zipoptions = "-r"
-    else:
-        zipoptions = "-rq"
-    from distutils.errors import DistutilsExecError
-    from distutils.spawn import spawn
-    try:
-        spawn(["zip", zipoptions, zip_filename, base_dir], dry_run=dry_run)
-    except DistutilsExecError:
-        # XXX really should distinguish between "couldn't find
-        # external 'zip' command" and "zip failed".
-        raise ExecError("unable to create zip file '%s': "
-            "could neither import the 'zipfile' module nor "
-            "find a standalone zip utility") % zip_filename
-
-def _make_zipfile(base_name, base_dir, verbose=0, dry_run=0, logger=None):
-    """Create a zip file from all the files under 'base_dir'.
-
-    The output zip file will be named 'base_name' + ".zip".  Uses either the
-    "zipfile" Python module (if available) or the InfoZIP "zip" utility
-    (if installed and found on the default search path).  If neither tool is
-    available, raises ExecError.  Returns the name of the output zip
-    file.
-    """
-    zip_filename = base_name + ".zip"
-    archive_dir = os.path.dirname(base_name)
-
-    if not os.path.exists(archive_dir):
-        if logger is not None:
-            logger.info("creating %s", archive_dir)
-        if not dry_run:
-            os.makedirs(archive_dir)
-
-    # If zipfile module is not available, try spawning an external 'zip'
-    # command.
-    try:
-        import zipfile
-    except ImportError:
-        zipfile = None
-
-    if zipfile is None:
-        _call_external_zip(base_dir, zip_filename, verbose, dry_run)
-    else:
-        if logger is not None:
-            logger.info("creating '%s' and adding '%s' to it",
-                        zip_filename, base_dir)
-
-        if not dry_run:
-            zip = zipfile.ZipFile(zip_filename, "w",
-                                  compression=zipfile.ZIP_DEFLATED)
-
-            for dirpath, dirnames, filenames in os.walk(base_dir):
-                for name in filenames:
-                    path = os.path.normpath(os.path.join(dirpath, name))
-                    if os.path.isfile(path):
-                        zip.write(path, path)
-                        if logger is not None:
-                            logger.info("adding '%s'", path)
-            zip.close()
-
-    return zip_filename
-
-_ARCHIVE_FORMATS = {
-    'gztar': (_make_tarball, [('compress', 'gzip')], "gzip'ed tar-file"),
-    'bztar': (_make_tarball, [('compress', 'bzip2')], "bzip2'ed tar-file"),
-    'tar':   (_make_tarball, [('compress', None)], "uncompressed tar file"),
-    'zip':   (_make_zipfile, [], "ZIP file"),
-    }
-
-if _BZ2_SUPPORTED:
-    _ARCHIVE_FORMATS['bztar'] = (_make_tarball, [('compress', 'bzip2')],
-                                "bzip2'ed tar-file")
-
-def get_archive_formats():
-    """Returns a list of supported formats for archiving and unarchiving.
-
-    Each element of the returned sequence is a tuple (name, description)
-    """
-    formats = [(name, registry[2]) for name, registry in
-               _ARCHIVE_FORMATS.items()]
-    formats.sort()
-    return formats
-
-def register_archive_format(name, function, extra_args=None, description=''):
-    """Registers an archive format.
-
-    name is the name of the format. function is the callable that will be
-    used to create archives. If provided, extra_args is a sequence of
-    (name, value) tuples that will be passed as arguments to the callable.
-    description can be provided to describe the format, and will be returned
-    by the get_archive_formats() function.
-    """
-    if extra_args is None:
-        extra_args = []
-    if not isinstance(function, collections.Callable):
-        raise TypeError('The %s object is not callable' % function)
-    if not isinstance(extra_args, (tuple, list)):
-        raise TypeError('extra_args needs to be a sequence')
-    for element in extra_args:
-        if not isinstance(element, (tuple, list)) or len(element) !=2:
-            raise TypeError('extra_args elements are : (arg_name, value)')
-
-    _ARCHIVE_FORMATS[name] = (function, extra_args, description)
-
-def unregister_archive_format(name):
-    del _ARCHIVE_FORMATS[name]
-
-def make_archive(base_name, format, root_dir=None, base_dir=None, verbose=0,
-                 dry_run=0, owner=None, group=None, logger=None):
-    """Create an archive file (eg. zip or tar).
-
-    'base_name' is the name of the file to create, minus any format-specific
-    extension; 'format' is the archive format: one of "zip", "tar", "bztar"
-    or "gztar".
-
-    'root_dir' is a directory that will be the root directory of the
-    archive; ie. we typically chdir into 'root_dir' before creating the
-    archive.  'base_dir' is the directory where we start archiving from;
-    ie. 'base_dir' will be the common prefix of all files and
-    directories in the archive.  'root_dir' and 'base_dir' both default
-    to the current directory.  Returns the name of the archive file.
-
-    'owner' and 'group' are used when creating a tar archive. By default,
-    uses the current owner and group.
-    """
-    save_cwd = os.getcwd()
-    if root_dir is not None:
-        if logger is not None:
-            logger.debug("changing into '%s'", root_dir)
-        base_name = os.path.abspath(base_name)
-        if not dry_run:
-            os.chdir(root_dir)
-
-    if base_dir is None:
-        base_dir = os.curdir
-
-    kwargs = {'dry_run': dry_run, 'logger': logger}
-
-    try:
-        format_info = _ARCHIVE_FORMATS[format]
-    except KeyError:
-        raise ValueError("unknown archive format '%s'" % format)
-
-    func = format_info[0]
-    for arg, val in format_info[1]:
-        kwargs[arg] = val
-
-    if format != 'zip':
-        kwargs['owner'] = owner
-        kwargs['group'] = group
-
-    try:
-        filename = func(base_name, base_dir, **kwargs)
-    finally:
-        if root_dir is not None:
-            if logger is not None:
-                logger.debug("changing back to '%s'", save_cwd)
-            os.chdir(save_cwd)
-
-    return filename
-
-
-def get_unpack_formats():
-    """Returns a list of supported formats for unpacking.
-
-    Each element of the returned sequence is a tuple
-    (name, extensions, description)
-    """
-    formats = [(name, info[0], info[3]) for name, info in
-               _UNPACK_FORMATS.items()]
-    formats.sort()
-    return formats
-
-def _check_unpack_options(extensions, function, extra_args):
-    """Checks what gets registered as an unpacker."""
-    # first make sure no other unpacker is registered for this extension
-    existing_extensions = {}
-    for name, info in _UNPACK_FORMATS.items():
-        for ext in info[0]:
-            existing_extensions[ext] = name
-
-    for extension in extensions:
-        if extension in existing_extensions:
-            msg = '%s is already registered for "%s"'
-            raise RegistryError(msg % (extension,
-                                       existing_extensions[extension]))
-
-    if not isinstance(function, collections.Callable):
-        raise TypeError('The registered function must be a callable')
-
-
-def register_unpack_format(name, extensions, function, extra_args=None,
-                           description=''):
-    """Registers an unpack format.
-
-    `name` is the name of the format. `extensions` is a list of extensions
-    corresponding to the format.
-
-    `function` is the callable that will be
-    used to unpack archives. The callable will receive archives to unpack.
-    If it's unable to handle an archive, it needs to raise a ReadError
-    exception.
-
-    If provided, `extra_args` is a sequence of
-    (name, value) tuples that will be passed as arguments to the callable.
-    description can be provided to describe the format, and will be returned
-    by the get_unpack_formats() function.
-    """
-    if extra_args is None:
-        extra_args = []
-    _check_unpack_options(extensions, function, extra_args)
-    _UNPACK_FORMATS[name] = extensions, function, extra_args, description
-
-def unregister_unpack_format(name):
-    """Removes the pack format from the registry."""
-    del _UNPACK_FORMATS[name]
-
-def _ensure_directory(path):
-    """Ensure that the parent directory of `path` exists"""
-    dirname = os.path.dirname(path)
-    if not os.path.isdir(dirname):
-        os.makedirs(dirname)
-
-def _unpack_zipfile(filename, extract_dir):
-    """Unpack zip `filename` to `extract_dir`
-    """
-    try:
-        import zipfile
-    except ImportError:
-        raise ReadError('zlib not supported, cannot unpack this archive.')
-
-    if not zipfile.is_zipfile(filename):
-        raise ReadError("%s is not a zip file" % filename)
-
-    zip = zipfile.ZipFile(filename)
-    try:
-        for info in zip.infolist():
-            name = info.filename
-
-            # don't extract absolute paths or ones with .. in them
-            if name.startswith('/') or '..' in name:
-                continue
-
-            target = os.path.join(extract_dir, *name.split('/'))
-            if not target:
-                continue
-
-            _ensure_directory(target)
-            if not name.endswith('/'):
-                # file
-                data = zip.read(info.filename)
-                f = open(target, 'wb')
-                try:
-                    f.write(data)
-                finally:
-                    f.close()
-                    del data
-    finally:
-        zip.close()
-
-def _unpack_tarfile(filename, extract_dir):
-    """Unpack tar/tar.gz/tar.bz2 `filename` to `extract_dir`
-    """
-    try:
-        tarobj = tarfile.open(filename)
-    except tarfile.TarError:
-        raise ReadError(
-            "%s is not a compressed or uncompressed tar file" % filename)
-    try:
-        tarobj.extractall(extract_dir)
-    finally:
-        tarobj.close()
-
-_UNPACK_FORMATS = {
-    'gztar': (['.tar.gz', '.tgz'], _unpack_tarfile, [], "gzip'ed tar-file"),
-    'tar':   (['.tar'], _unpack_tarfile, [], "uncompressed tar file"),
-    'zip':   (['.zip'], _unpack_zipfile, [], "ZIP file")
-    }
-
-if _BZ2_SUPPORTED:
-    _UNPACK_FORMATS['bztar'] = (['.bz2'], _unpack_tarfile, [],
-                                "bzip2'ed tar-file")
-
-def _find_unpack_format(filename):
-    for name, info in _UNPACK_FORMATS.items():
-        for extension in info[0]:
-            if filename.endswith(extension):
-                return name
-    return None
-
-def unpack_archive(filename, extract_dir=None, format=None):
-    """Unpack an archive.
-
-    `filename` is the name of the archive.
-
-    `extract_dir` is the name of the target directory, where the archive
-    is unpacked. If not provided, the current working directory is used.
-
-    `format` is the archive format: one of "zip", "tar", or "gztar". Or any
-    other registered format. If not provided, unpack_archive will use the
-    filename extension and see if an unpacker was registered for that
-    extension.
-
-    In case none is found, a ValueError is raised.
-    """
-    if extract_dir is None:
-        extract_dir = os.getcwd()
-
-    if format is not None:
-        try:
-            format_info = _UNPACK_FORMATS[format]
-        except KeyError:
-            raise ValueError("Unknown unpack format '{0}'".format(format))
-
-        func = format_info[1]
-        func(filename, extract_dir, **dict(format_info[2]))
-    else:
-        # we need to look at the registered unpackers supported extensions
-        format = _find_unpack_format(filename)
-        if format is None:
-            raise ReadError("Unknown archive format '{0}'".format(filename))
-
-        func = _UNPACK_FORMATS[format][1]
-        kwargs = dict(_UNPACK_FORMATS[format][2])
-        func(filename, extract_dir, **kwargs)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/sysconfig.cfg b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/sysconfig.cfg
deleted file mode 100644
index 1746bd0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/sysconfig.cfg
+++ /dev/null
@@ -1,84 +0,0 @@
-[posix_prefix]
-# Configuration directories.  Some of these come straight out of the
-# configure script.  They are for implementing the other variables, not to
-# be used directly in [resource_locations].
-confdir = /etc
-datadir = /usr/share
-libdir = /usr/lib
-statedir = /var
-# User resource directory
-local = ~/.local/{distribution.name}
-
-stdlib = {base}/lib/python{py_version_short}
-platstdlib = {platbase}/lib/python{py_version_short}
-purelib = {base}/lib/python{py_version_short}/site-packages
-platlib = {platbase}/lib/python{py_version_short}/site-packages
-include = {base}/include/python{py_version_short}{abiflags}
-platinclude = {platbase}/include/python{py_version_short}{abiflags}
-data = {base}
-
-[posix_home]
-stdlib = {base}/lib/python
-platstdlib = {base}/lib/python
-purelib = {base}/lib/python
-platlib = {base}/lib/python
-include = {base}/include/python
-platinclude = {base}/include/python
-scripts = {base}/bin
-data = {base}
-
-[nt]
-stdlib = {base}/Lib
-platstdlib = {base}/Lib
-purelib = {base}/Lib/site-packages
-platlib = {base}/Lib/site-packages
-include = {base}/Include
-platinclude = {base}/Include
-scripts = {base}/Scripts
-data = {base}
-
-[os2]
-stdlib = {base}/Lib
-platstdlib = {base}/Lib
-purelib = {base}/Lib/site-packages
-platlib = {base}/Lib/site-packages
-include = {base}/Include
-platinclude = {base}/Include
-scripts = {base}/Scripts
-data = {base}
-
-[os2_home]
-stdlib = {userbase}/lib/python{py_version_short}
-platstdlib = {userbase}/lib/python{py_version_short}
-purelib = {userbase}/lib/python{py_version_short}/site-packages
-platlib = {userbase}/lib/python{py_version_short}/site-packages
-include = {userbase}/include/python{py_version_short}
-scripts = {userbase}/bin
-data = {userbase}
-
-[nt_user]
-stdlib = {userbase}/Python{py_version_nodot}
-platstdlib = {userbase}/Python{py_version_nodot}
-purelib = {userbase}/Python{py_version_nodot}/site-packages
-platlib = {userbase}/Python{py_version_nodot}/site-packages
-include = {userbase}/Python{py_version_nodot}/Include
-scripts = {userbase}/Scripts
-data = {userbase}
-
-[posix_user]
-stdlib = {userbase}/lib/python{py_version_short}
-platstdlib = {userbase}/lib/python{py_version_short}
-purelib = {userbase}/lib/python{py_version_short}/site-packages
-platlib = {userbase}/lib/python{py_version_short}/site-packages
-include = {userbase}/include/python{py_version_short}
-scripts = {userbase}/bin
-data = {userbase}
-
-[osx_framework_user]
-stdlib = {userbase}/lib/python
-platstdlib = {userbase}/lib/python
-purelib = {userbase}/lib/python/site-packages
-platlib = {userbase}/lib/python/site-packages
-include = {userbase}/include
-scripts = {userbase}/bin
-data = {userbase}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/sysconfig.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/sysconfig.py
deleted file mode 100644
index 1df3aba..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/sysconfig.py
+++ /dev/null
@@ -1,788 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012 The Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""Access to Python's configuration information."""
-
-import codecs
-import os
-import re
-import sys
-from os.path import pardir, realpath
-try:
-    import configparser
-except ImportError:
-    import ConfigParser as configparser
-
-
-__all__ = [
-    'get_config_h_filename',
-    'get_config_var',
-    'get_config_vars',
-    'get_makefile_filename',
-    'get_path',
-    'get_path_names',
-    'get_paths',
-    'get_platform',
-    'get_python_version',
-    'get_scheme_names',
-    'parse_config_h',
-]
-
-
-def _safe_realpath(path):
-    try:
-        return realpath(path)
-    except OSError:
-        return path
-
-
-if sys.executable:
-    _PROJECT_BASE = os.path.dirname(_safe_realpath(sys.executable))
-else:
-    # sys.executable can be empty if argv[0] has been changed and Python is
-    # unable to retrieve the real program name
-    _PROJECT_BASE = _safe_realpath(os.getcwd())
-
-if os.name == "nt" and "pcbuild" in _PROJECT_BASE[-8:].lower():
-    _PROJECT_BASE = _safe_realpath(os.path.join(_PROJECT_BASE, pardir))
-# PC/VS7.1
-if os.name == "nt" and "\\pc\\v" in _PROJECT_BASE[-10:].lower():
-    _PROJECT_BASE = _safe_realpath(os.path.join(_PROJECT_BASE, pardir, pardir))
-# PC/AMD64
-if os.name == "nt" and "\\pcbuild\\amd64" in _PROJECT_BASE[-14:].lower():
-    _PROJECT_BASE = _safe_realpath(os.path.join(_PROJECT_BASE, pardir, pardir))
-
-
-def is_python_build():
-    for fn in ("Setup.dist", "Setup.local"):
-        if os.path.isfile(os.path.join(_PROJECT_BASE, "Modules", fn)):
-            return True
-    return False
-
-_PYTHON_BUILD = is_python_build()
-
-_cfg_read = False
-
-def _ensure_cfg_read():
-    global _cfg_read
-    if not _cfg_read:
-        from ..resources import finder
-        backport_package = __name__.rsplit('.', 1)[0]
-        _finder = finder(backport_package)
-        _cfgfile = _finder.find('sysconfig.cfg')
-        assert _cfgfile, 'sysconfig.cfg exists'
-        with _cfgfile.as_stream() as s:
-            _SCHEMES.readfp(s)
-        if _PYTHON_BUILD:
-            for scheme in ('posix_prefix', 'posix_home'):
-                _SCHEMES.set(scheme, 'include', '{srcdir}/Include')
-                _SCHEMES.set(scheme, 'platinclude', '{projectbase}/.')
-
-        _cfg_read = True
-
-
-_SCHEMES = configparser.RawConfigParser()
-_VAR_REPL = re.compile(r'\{([^{]*?)\}')
-
-def _expand_globals(config):
-    _ensure_cfg_read()
-    if config.has_section('globals'):
-        globals = config.items('globals')
-    else:
-        globals = tuple()
-
-    sections = config.sections()
-    for section in sections:
-        if section == 'globals':
-            continue
-        for option, value in globals:
-            if config.has_option(section, option):
-                continue
-            config.set(section, option, value)
-    config.remove_section('globals')
-
-    # now expanding local variables defined in the cfg file
-    #
-    for section in config.sections():
-        variables = dict(config.items(section))
-
-        def _replacer(matchobj):
-            name = matchobj.group(1)
-            if name in variables:
-                return variables[name]
-            return matchobj.group(0)
-
-        for option, value in config.items(section):
-            config.set(section, option, _VAR_REPL.sub(_replacer, value))
-
-#_expand_globals(_SCHEMES)
-
- # FIXME don't rely on sys.version here, its format is an implementation detail
- # of CPython, use sys.version_info or sys.hexversion
-_PY_VERSION = sys.version.split()[0]
-_PY_VERSION_SHORT = sys.version[:3]
-_PY_VERSION_SHORT_NO_DOT = _PY_VERSION[0] + _PY_VERSION[2]
-_PREFIX = os.path.normpath(sys.prefix)
-_EXEC_PREFIX = os.path.normpath(sys.exec_prefix)
-_CONFIG_VARS = None
-_USER_BASE = None
-
-
-def _subst_vars(path, local_vars):
-    """In the string `path`, replace tokens like {some.thing} with the
-    corresponding value from the map `local_vars`.
-
-    If there is no corresponding value, leave the token unchanged.
-    """
-    def _replacer(matchobj):
-        name = matchobj.group(1)
-        if name in local_vars:
-            return local_vars[name]
-        elif name in os.environ:
-            return os.environ[name]
-        return matchobj.group(0)
-    return _VAR_REPL.sub(_replacer, path)
-
-
-def _extend_dict(target_dict, other_dict):
-    target_keys = target_dict.keys()
-    for key, value in other_dict.items():
-        if key in target_keys:
-            continue
-        target_dict[key] = value
-
-
-def _expand_vars(scheme, vars):
-    res = {}
-    if vars is None:
-        vars = {}
-    _extend_dict(vars, get_config_vars())
-
-    for key, value in _SCHEMES.items(scheme):
-        if os.name in ('posix', 'nt'):
-            value = os.path.expanduser(value)
-        res[key] = os.path.normpath(_subst_vars(value, vars))
-    return res
-
-
-def format_value(value, vars):
-    def _replacer(matchobj):
-        name = matchobj.group(1)
-        if name in vars:
-            return vars[name]
-        return matchobj.group(0)
-    return _VAR_REPL.sub(_replacer, value)
-
-
-def _get_default_scheme():
-    if os.name == 'posix':
-        # the default scheme for posix is posix_prefix
-        return 'posix_prefix'
-    return os.name
-
-
-def _getuserbase():
-    env_base = os.environ.get("PYTHONUSERBASE", None)
-
-    def joinuser(*args):
-        return os.path.expanduser(os.path.join(*args))
-
-    # what about 'os2emx', 'riscos' ?
-    if os.name == "nt":
-        base = os.environ.get("APPDATA") or "~"
-        if env_base:
-            return env_base
-        else:
-            return joinuser(base, "Python")
-
-    if sys.platform == "darwin":
-        framework = get_config_var("PYTHONFRAMEWORK")
-        if framework:
-            if env_base:
-                return env_base
-            else:
-                return joinuser("~", "Library", framework, "%d.%d" %
-                                sys.version_info[:2])
-
-    if env_base:
-        return env_base
-    else:
-        return joinuser("~", ".local")
-
-
-def _parse_makefile(filename, vars=None):
-    """Parse a Makefile-style file.
-
-    A dictionary containing name/value pairs is returned.  If an
-    optional dictionary is passed in as the second argument, it is
-    used instead of a new dictionary.
-    """
-    # Regexes needed for parsing Makefile (and similar syntaxes,
-    # like old-style Setup files).
-    _variable_rx = re.compile(r"([a-zA-Z][a-zA-Z0-9_]+)\s*=\s*(.*)")
-    _findvar1_rx = re.compile(r"\$\(([A-Za-z][A-Za-z0-9_]*)\)")
-    _findvar2_rx = re.compile(r"\${([A-Za-z][A-Za-z0-9_]*)}")
-
-    if vars is None:
-        vars = {}
-    done = {}
-    notdone = {}
-
-    with codecs.open(filename, encoding='utf-8', errors="surrogateescape") as f:
-        lines = f.readlines()
-
-    for line in lines:
-        if line.startswith('#') or line.strip() == '':
-            continue
-        m = _variable_rx.match(line)
-        if m:
-            n, v = m.group(1, 2)
-            v = v.strip()
-            # `$$' is a literal `$' in make
-            tmpv = v.replace('$$', '')
-
-            if "$" in tmpv:
-                notdone[n] = v
-            else:
-                try:
-                    v = int(v)
-                except ValueError:
-                    # insert literal `$'
-                    done[n] = v.replace('$$', '$')
-                else:
-                    done[n] = v
-
-    # do variable interpolation here
-    variables = list(notdone.keys())
-
-    # Variables with a 'PY_' prefix in the makefile. These need to
-    # be made available without that prefix through sysconfig.
-    # Special care is needed to ensure that variable expansion works, even
-    # if the expansion uses the name without a prefix.
-    renamed_variables = ('CFLAGS', 'LDFLAGS', 'CPPFLAGS')
-
-    while len(variables) > 0:
-        for name in tuple(variables):
-            value = notdone[name]
-            m = _findvar1_rx.search(value) or _findvar2_rx.search(value)
-            if m is not None:
-                n = m.group(1)
-                found = True
-                if n in done:
-                    item = str(done[n])
-                elif n in notdone:
-                    # get it on a subsequent round
-                    found = False
-                elif n in os.environ:
-                    # do it like make: fall back to environment
-                    item = os.environ[n]
-
-                elif n in renamed_variables:
-                    if (name.startswith('PY_') and
-                        name[3:] in renamed_variables):
-                        item = ""
-
-                    elif 'PY_' + n in notdone:
-                        found = False
-
-                    else:
-                        item = str(done['PY_' + n])
-
-                else:
-                    done[n] = item = ""
-
-                if found:
-                    after = value[m.end():]
-                    value = value[:m.start()] + item + after
-                    if "$" in after:
-                        notdone[name] = value
-                    else:
-                        try:
-                            value = int(value)
-                        except ValueError:
-                            done[name] = value.strip()
-                        else:
-                            done[name] = value
-                        variables.remove(name)
-
-                        if (name.startswith('PY_') and
-                            name[3:] in renamed_variables):
-
-                            name = name[3:]
-                            if name not in done:
-                                done[name] = value
-
-            else:
-                # bogus variable reference (e.g. "prefix=$/opt/python");
-                # just drop it since we can't deal
-                done[name] = value
-                variables.remove(name)
-
-    # strip spurious spaces
-    for k, v in done.items():
-        if isinstance(v, str):
-            done[k] = v.strip()
-
-    # save the results in the global dictionary
-    vars.update(done)
-    return vars
-
-
-def get_makefile_filename():
-    """Return the path of the Makefile."""
-    if _PYTHON_BUILD:
-        return os.path.join(_PROJECT_BASE, "Makefile")
-    if hasattr(sys, 'abiflags'):
-        config_dir_name = 'config-%s%s' % (_PY_VERSION_SHORT, sys.abiflags)
-    else:
-        config_dir_name = 'config'
-    return os.path.join(get_path('stdlib'), config_dir_name, 'Makefile')
-
-
-def _init_posix(vars):
-    """Initialize the module as appropriate for POSIX systems."""
-    # load the installed Makefile:
-    makefile = get_makefile_filename()
-    try:
-        _parse_makefile(makefile, vars)
-    except IOError as e:
-        msg = "invalid Python installation: unable to open %s" % makefile
-        if hasattr(e, "strerror"):
-            msg = msg + " (%s)" % e.strerror
-        raise IOError(msg)
-    # load the installed pyconfig.h:
-    config_h = get_config_h_filename()
-    try:
-        with open(config_h) as f:
-            parse_config_h(f, vars)
-    except IOError as e:
-        msg = "invalid Python installation: unable to open %s" % config_h
-        if hasattr(e, "strerror"):
-            msg = msg + " (%s)" % e.strerror
-        raise IOError(msg)
-    # On AIX, there are wrong paths to the linker scripts in the Makefile
-    # -- these paths are relative to the Python source, but when installed
-    # the scripts are in another directory.
-    if _PYTHON_BUILD:
-        vars['LDSHARED'] = vars['BLDSHARED']
-
-
-def _init_non_posix(vars):
-    """Initialize the module as appropriate for NT"""
-    # set basic install directories
-    vars['LIBDEST'] = get_path('stdlib')
-    vars['BINLIBDEST'] = get_path('platstdlib')
-    vars['INCLUDEPY'] = get_path('include')
-    vars['SO'] = '.pyd'
-    vars['EXE'] = '.exe'
-    vars['VERSION'] = _PY_VERSION_SHORT_NO_DOT
-    vars['BINDIR'] = os.path.dirname(_safe_realpath(sys.executable))
-
-#
-# public APIs
-#
-
-
-def parse_config_h(fp, vars=None):
-    """Parse a config.h-style file.
-
-    A dictionary containing name/value pairs is returned.  If an
-    optional dictionary is passed in as the second argument, it is
-    used instead of a new dictionary.
-    """
-    if vars is None:
-        vars = {}
-    define_rx = re.compile("#define ([A-Z][A-Za-z0-9_]+) (.*)\n")
-    undef_rx = re.compile("/[*] #undef ([A-Z][A-Za-z0-9_]+) [*]/\n")
-
-    while True:
-        line = fp.readline()
-        if not line:
-            break
-        m = define_rx.match(line)
-        if m:
-            n, v = m.group(1, 2)
-            try:
-                v = int(v)
-            except ValueError:
-                pass
-            vars[n] = v
-        else:
-            m = undef_rx.match(line)
-            if m:
-                vars[m.group(1)] = 0
-    return vars
-
-
-def get_config_h_filename():
-    """Return the path of pyconfig.h."""
-    if _PYTHON_BUILD:
-        if os.name == "nt":
-            inc_dir = os.path.join(_PROJECT_BASE, "PC")
-        else:
-            inc_dir = _PROJECT_BASE
-    else:
-        inc_dir = get_path('platinclude')
-    return os.path.join(inc_dir, 'pyconfig.h')
-
-
-def get_scheme_names():
-    """Return a tuple containing the schemes names."""
-    return tuple(sorted(_SCHEMES.sections()))
-
-
-def get_path_names():
-    """Return a tuple containing the paths names."""
-    # xxx see if we want a static list
-    return _SCHEMES.options('posix_prefix')
-
-
-def get_paths(scheme=_get_default_scheme(), vars=None, expand=True):
-    """Return a mapping containing an install scheme.
-
-    ``scheme`` is the install scheme name. If not provided, it will
-    return the default scheme for the current platform.
-    """
-    _ensure_cfg_read()
-    if expand:
-        return _expand_vars(scheme, vars)
-    else:
-        return dict(_SCHEMES.items(scheme))
-
-
-def get_path(name, scheme=_get_default_scheme(), vars=None, expand=True):
-    """Return a path corresponding to the scheme.
-
-    ``scheme`` is the install scheme name.
-    """
-    return get_paths(scheme, vars, expand)[name]
-
-
-def get_config_vars(*args):
-    """With no arguments, return a dictionary of all configuration
-    variables relevant for the current platform.
-
-    On Unix, this means every variable defined in Python's installed Makefile;
-    On Windows and Mac OS it's a much smaller set.
-
-    With arguments, return a list of values that result from looking up
-    each argument in the configuration variable dictionary.
-    """
-    global _CONFIG_VARS
-    if _CONFIG_VARS is None:
-        _CONFIG_VARS = {}
-        # Normalized versions of prefix and exec_prefix are handy to have;
-        # in fact, these are the standard versions used most places in the
-        # distutils2 module.
-        _CONFIG_VARS['prefix'] = _PREFIX
-        _CONFIG_VARS['exec_prefix'] = _EXEC_PREFIX
-        _CONFIG_VARS['py_version'] = _PY_VERSION
-        _CONFIG_VARS['py_version_short'] = _PY_VERSION_SHORT
-        _CONFIG_VARS['py_version_nodot'] = _PY_VERSION[0] + _PY_VERSION[2]
-        _CONFIG_VARS['base'] = _PREFIX
-        _CONFIG_VARS['platbase'] = _EXEC_PREFIX
-        _CONFIG_VARS['projectbase'] = _PROJECT_BASE
-        try:
-            _CONFIG_VARS['abiflags'] = sys.abiflags
-        except AttributeError:
-            # sys.abiflags may not be defined on all platforms.
-            _CONFIG_VARS['abiflags'] = ''
-
-        if os.name in ('nt', 'os2'):
-            _init_non_posix(_CONFIG_VARS)
-        if os.name == 'posix':
-            _init_posix(_CONFIG_VARS)
-        # Setting 'userbase' is done below the call to the
-        # init function to enable using 'get_config_var' in
-        # the init-function.
-        if sys.version >= '2.6':
-            _CONFIG_VARS['userbase'] = _getuserbase()
-
-        if 'srcdir' not in _CONFIG_VARS:
-            _CONFIG_VARS['srcdir'] = _PROJECT_BASE
-        else:
-            _CONFIG_VARS['srcdir'] = _safe_realpath(_CONFIG_VARS['srcdir'])
-
-        # Convert srcdir into an absolute path if it appears necessary.
-        # Normally it is relative to the build directory.  However, during
-        # testing, for example, we might be running a non-installed python
-        # from a different directory.
-        if _PYTHON_BUILD and os.name == "posix":
-            base = _PROJECT_BASE
-            try:
-                cwd = os.getcwd()
-            except OSError:
-                cwd = None
-            if (not os.path.isabs(_CONFIG_VARS['srcdir']) and
-                base != cwd):
-                # srcdir is relative and we are not in the same directory
-                # as the executable. Assume executable is in the build
-                # directory and make srcdir absolute.
-                srcdir = os.path.join(base, _CONFIG_VARS['srcdir'])
-                _CONFIG_VARS['srcdir'] = os.path.normpath(srcdir)
-
-        if sys.platform == 'darwin':
-            kernel_version = os.uname()[2]  # Kernel version (8.4.3)
-            major_version = int(kernel_version.split('.')[0])
-
-            if major_version < 8:
-                # On Mac OS X before 10.4, check if -arch and -isysroot
-                # are in CFLAGS or LDFLAGS and remove them if they are.
-                # This is needed when building extensions on a 10.3 system
-                # using a universal build of python.
-                for key in ('LDFLAGS', 'BASECFLAGS',
-                        # a number of derived variables. These need to be
-                        # patched up as well.
-                        'CFLAGS', 'PY_CFLAGS', 'BLDSHARED'):
-                    flags = _CONFIG_VARS[key]
-                    flags = re.sub(r'-arch\s+\w+\s', ' ', flags)
-                    flags = re.sub('-isysroot [^ \t]*', ' ', flags)
-                    _CONFIG_VARS[key] = flags
-            else:
-                # Allow the user to override the architecture flags using
-                # an environment variable.
-                # NOTE: This name was introduced by Apple in OSX 10.5 and
-                # is used by several scripting languages distributed with
-                # that OS release.
-                if 'ARCHFLAGS' in os.environ:
-                    arch = os.environ['ARCHFLAGS']
-                    for key in ('LDFLAGS', 'BASECFLAGS',
-                        # a number of derived variables. These need to be
-                        # patched up as well.
-                        'CFLAGS', 'PY_CFLAGS', 'BLDSHARED'):
-
-                        flags = _CONFIG_VARS[key]
-                        flags = re.sub(r'-arch\s+\w+\s', ' ', flags)
-                        flags = flags + ' ' + arch
-                        _CONFIG_VARS[key] = flags
-
-                # If we're on OSX 10.5 or later and the user tries to
-                # compiles an extension using an SDK that is not present
-                # on the current machine it is better to not use an SDK
-                # than to fail.
-                #
-                # The major usecase for this is users using a Python.org
-                # binary installer  on OSX 10.6: that installer uses
-                # the 10.4u SDK, but that SDK is not installed by default
-                # when you install Xcode.
-                #
-                CFLAGS = _CONFIG_VARS.get('CFLAGS', '')
-                m = re.search(r'-isysroot\s+(\S+)', CFLAGS)
-                if m is not None:
-                    sdk = m.group(1)
-                    if not os.path.exists(sdk):
-                        for key in ('LDFLAGS', 'BASECFLAGS',
-                             # a number of derived variables. These need to be
-                             # patched up as well.
-                            'CFLAGS', 'PY_CFLAGS', 'BLDSHARED'):
-
-                            flags = _CONFIG_VARS[key]
-                            flags = re.sub(r'-isysroot\s+\S+(\s|$)', ' ', flags)
-                            _CONFIG_VARS[key] = flags
-
-    if args:
-        vals = []
-        for name in args:
-            vals.append(_CONFIG_VARS.get(name))
-        return vals
-    else:
-        return _CONFIG_VARS
-
-
-def get_config_var(name):
-    """Return the value of a single variable using the dictionary returned by
-    'get_config_vars()'.
-
-    Equivalent to get_config_vars().get(name)
-    """
-    return get_config_vars().get(name)
-
-
-def get_platform():
-    """Return a string that identifies the current platform.
-
-    This is used mainly to distinguish platform-specific build directories and
-    platform-specific built distributions.  Typically includes the OS name
-    and version and the architecture (as supplied by 'os.uname()'),
-    although the exact information included depends on the OS; eg. for IRIX
-    the architecture isn't particularly important (IRIX only runs on SGI
-    hardware), but for Linux the kernel version isn't particularly
-    important.
-
-    Examples of returned values:
-       linux-i586
-       linux-alpha (?)
-       solaris-2.6-sun4u
-       irix-5.3
-       irix64-6.2
-
-    Windows will return one of:
-       win-amd64 (64bit Windows on AMD64 (aka x86_64, Intel64, EM64T, etc)
-       win-ia64 (64bit Windows on Itanium)
-       win32 (all others - specifically, sys.platform is returned)
-
-    For other non-POSIX platforms, currently just returns 'sys.platform'.
-    """
-    if os.name == 'nt':
-        # sniff sys.version for architecture.
-        prefix = " bit ("
-        i = sys.version.find(prefix)
-        if i == -1:
-            return sys.platform
-        j = sys.version.find(")", i)
-        look = sys.version[i+len(prefix):j].lower()
-        if look == 'amd64':
-            return 'win-amd64'
-        if look == 'itanium':
-            return 'win-ia64'
-        return sys.platform
-
-    if os.name != "posix" or not hasattr(os, 'uname'):
-        # XXX what about the architecture? NT is Intel or Alpha,
-        # Mac OS is M68k or PPC, etc.
-        return sys.platform
-
-    # Try to distinguish various flavours of Unix
-    osname, host, release, version, machine = os.uname()
-
-    # Convert the OS name to lowercase, remove '/' characters
-    # (to accommodate BSD/OS), and translate spaces (for "Power Macintosh")
-    osname = osname.lower().replace('/', '')
-    machine = machine.replace(' ', '_')
-    machine = machine.replace('/', '-')
-
-    if osname[:5] == "linux":
-        # At least on Linux/Intel, 'machine' is the processor --
-        # i386, etc.
-        # XXX what about Alpha, SPARC, etc?
-        return  "%s-%s" % (osname, machine)
-    elif osname[:5] == "sunos":
-        if release[0] >= "5":           # SunOS 5 == Solaris 2
-            osname = "solaris"
-            release = "%d.%s" % (int(release[0]) - 3, release[2:])
-        # fall through to standard osname-release-machine representation
-    elif osname[:4] == "irix":              # could be "irix64"!
-        return "%s-%s" % (osname, release)
-    elif osname[:3] == "aix":
-        return "%s-%s.%s" % (osname, version, release)
-    elif osname[:6] == "cygwin":
-        osname = "cygwin"
-        rel_re = re.compile(r'[\d.]+')
-        m = rel_re.match(release)
-        if m:
-            release = m.group()
-    elif osname[:6] == "darwin":
-        #
-        # For our purposes, we'll assume that the system version from
-        # distutils' perspective is what MACOSX_DEPLOYMENT_TARGET is set
-        # to. This makes the compatibility story a bit more sane because the
-        # machine is going to compile and link as if it were
-        # MACOSX_DEPLOYMENT_TARGET.
-        cfgvars = get_config_vars()
-        macver = cfgvars.get('MACOSX_DEPLOYMENT_TARGET')
-
-        if True:
-            # Always calculate the release of the running machine,
-            # needed to determine if we can build fat binaries or not.
-
-            macrelease = macver
-            # Get the system version. Reading this plist is a documented
-            # way to get the system version (see the documentation for
-            # the Gestalt Manager)
-            try:
-                f = open('/System/Library/CoreServices/SystemVersion.plist')
-            except IOError:
-                # We're on a plain darwin box, fall back to the default
-                # behaviour.
-                pass
-            else:
-                try:
-                    m = re.search(r'<key>ProductUserVisibleVersion</key>\s*'
-                                  r'<string>(.*?)</string>', f.read())
-                finally:
-                    f.close()
-                if m is not None:
-                    macrelease = '.'.join(m.group(1).split('.')[:2])
-                # else: fall back to the default behaviour
-
-        if not macver:
-            macver = macrelease
-
-        if macver:
-            release = macver
-            osname = "macosx"
-
-            if ((macrelease + '.') >= '10.4.' and
-                '-arch' in get_config_vars().get('CFLAGS', '').strip()):
-                # The universal build will build fat binaries, but not on
-                # systems before 10.4
-                #
-                # Try to detect 4-way universal builds, those have machine-type
-                # 'universal' instead of 'fat'.
-
-                machine = 'fat'
-                cflags = get_config_vars().get('CFLAGS')
-
-                archs = re.findall(r'-arch\s+(\S+)', cflags)
-                archs = tuple(sorted(set(archs)))
-
-                if len(archs) == 1:
-                    machine = archs[0]
-                elif archs == ('i386', 'ppc'):
-                    machine = 'fat'
-                elif archs == ('i386', 'x86_64'):
-                    machine = 'intel'
-                elif archs == ('i386', 'ppc', 'x86_64'):
-                    machine = 'fat3'
-                elif archs == ('ppc64', 'x86_64'):
-                    machine = 'fat64'
-                elif archs == ('i386', 'ppc', 'ppc64', 'x86_64'):
-                    machine = 'universal'
-                else:
-                    raise ValueError(
-                       "Don't know machine value for archs=%r" % (archs,))
-
-            elif machine == 'i386':
-                # On OSX the machine type returned by uname is always the
-                # 32-bit variant, even if the executable architecture is
-                # the 64-bit variant
-                if sys.maxsize >= 2**32:
-                    machine = 'x86_64'
-
-            elif machine in ('PowerPC', 'Power_Macintosh'):
-                # Pick a sane name for the PPC architecture.
-                # See 'i386' case
-                if sys.maxsize >= 2**32:
-                    machine = 'ppc64'
-                else:
-                    machine = 'ppc'
-
-    return "%s-%s-%s" % (osname, release, machine)
-
-
-def get_python_version():
-    return _PY_VERSION_SHORT
-
-
-def _print_dict(title, data):
-    for index, (key, value) in enumerate(sorted(data.items())):
-        if index == 0:
-            print('%s: ' % (title))
-        print('\t%s = "%s"' % (key, value))
-
-
-def _main():
-    """Display all information sysconfig detains."""
-    print('Platform: "%s"' % get_platform())
-    print('Python version: "%s"' % get_python_version())
-    print('Current installation scheme: "%s"' % _get_default_scheme())
-    print()
-    _print_dict('Paths', get_paths())
-    print()
-    _print_dict('Variables', get_config_vars())
-
-
-if __name__ == '__main__':
-    _main()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/tarfile.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/tarfile.py
deleted file mode 100644
index d66d856..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/_backport/tarfile.py
+++ /dev/null
@@ -1,2607 +0,0 @@
-#-------------------------------------------------------------------
-# tarfile.py
-#-------------------------------------------------------------------
-# Copyright (C) 2002 Lars Gustaebel <lars@gustaebel.de>
-# All rights reserved.
-#
-# Permission  is  hereby granted,  free  of charge,  to  any person
-# obtaining a  copy of  this software  and associated documentation
-# files  (the  "Software"),  to   deal  in  the  Software   without
-# restriction,  including  without limitation  the  rights to  use,
-# copy, modify, merge, publish, distribute, sublicense, and/or sell
-# copies  of  the  Software,  and to  permit  persons  to  whom the
-# Software  is  furnished  to  do  so,  subject  to  the  following
-# conditions:
-#
-# The above copyright  notice and this  permission notice shall  be
-# included in all copies or substantial portions of the Software.
-#
-# THE SOFTWARE IS PROVIDED "AS  IS", WITHOUT WARRANTY OF ANY  KIND,
-# EXPRESS OR IMPLIED, INCLUDING  BUT NOT LIMITED TO  THE WARRANTIES
-# OF  MERCHANTABILITY,  FITNESS   FOR  A  PARTICULAR   PURPOSE  AND
-# NONINFRINGEMENT.  IN  NO  EVENT SHALL  THE  AUTHORS  OR COPYRIGHT
-# HOLDERS  BE LIABLE  FOR ANY  CLAIM, DAMAGES  OR OTHER  LIABILITY,
-# WHETHER  IN AN  ACTION OF  CONTRACT, TORT  OR OTHERWISE,  ARISING
-# FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR
-# OTHER DEALINGS IN THE SOFTWARE.
-#
-from __future__ import print_function
-
-"""Read from and write to tar format archives.
-"""
-
-__version__ = "$Revision$"
-
-version     = "0.9.0"
-__author__  = "Lars Gust\u00e4bel (lars@gustaebel.de)"
-__date__    = "$Date: 2011-02-25 17:42:01 +0200 (Fri, 25 Feb 2011) $"
-__cvsid__   = "$Id: tarfile.py 88586 2011-02-25 15:42:01Z marc-andre.lemburg $"
-__credits__ = "Gustavo Niemeyer, Niels Gust\u00e4bel, Richard Townsend."
-
-#---------
-# Imports
-#---------
-import sys
-import os
-import stat
-import errno
-import time
-import struct
-import copy
-import re
-
-try:
-    import grp, pwd
-except ImportError:
-    grp = pwd = None
-
-# os.symlink on Windows prior to 6.0 raises NotImplementedError
-symlink_exception = (AttributeError, NotImplementedError)
-try:
-    # WindowsError (1314) will be raised if the caller does not hold the
-    # SeCreateSymbolicLinkPrivilege privilege
-    symlink_exception += (WindowsError,)
-except NameError:
-    pass
-
-# from tarfile import *
-__all__ = ["TarFile", "TarInfo", "is_tarfile", "TarError"]
-
-if sys.version_info[0] < 3:
-    import __builtin__ as builtins
-else:
-    import builtins
-
-_open = builtins.open   # Since 'open' is TarFile.open
-
-#---------------------------------------------------------
-# tar constants
-#---------------------------------------------------------
-NUL = b"\0"                     # the null character
-BLOCKSIZE = 512                 # length of processing blocks
-RECORDSIZE = BLOCKSIZE * 20     # length of records
-GNU_MAGIC = b"ustar  \0"        # magic gnu tar string
-POSIX_MAGIC = b"ustar\x0000"    # magic posix tar string
-
-LENGTH_NAME = 100               # maximum length of a filename
-LENGTH_LINK = 100               # maximum length of a linkname
-LENGTH_PREFIX = 155             # maximum length of the prefix field
-
-REGTYPE = b"0"                  # regular file
-AREGTYPE = b"\0"                # regular file
-LNKTYPE = b"1"                  # link (inside tarfile)
-SYMTYPE = b"2"                  # symbolic link
-CHRTYPE = b"3"                  # character special device
-BLKTYPE = b"4"                  # block special device
-DIRTYPE = b"5"                  # directory
-FIFOTYPE = b"6"                 # fifo special device
-CONTTYPE = b"7"                 # contiguous file
-
-GNUTYPE_LONGNAME = b"L"         # GNU tar longname
-GNUTYPE_LONGLINK = b"K"         # GNU tar longlink
-GNUTYPE_SPARSE = b"S"           # GNU tar sparse file
-
-XHDTYPE = b"x"                  # POSIX.1-2001 extended header
-XGLTYPE = b"g"                  # POSIX.1-2001 global header
-SOLARIS_XHDTYPE = b"X"          # Solaris extended header
-
-USTAR_FORMAT = 0                # POSIX.1-1988 (ustar) format
-GNU_FORMAT = 1                  # GNU tar format
-PAX_FORMAT = 2                  # POSIX.1-2001 (pax) format
-DEFAULT_FORMAT = GNU_FORMAT
-
-#---------------------------------------------------------
-# tarfile constants
-#---------------------------------------------------------
-# File types that tarfile supports:
-SUPPORTED_TYPES = (REGTYPE, AREGTYPE, LNKTYPE,
-                   SYMTYPE, DIRTYPE, FIFOTYPE,
-                   CONTTYPE, CHRTYPE, BLKTYPE,
-                   GNUTYPE_LONGNAME, GNUTYPE_LONGLINK,
-                   GNUTYPE_SPARSE)
-
-# File types that will be treated as a regular file.
-REGULAR_TYPES = (REGTYPE, AREGTYPE,
-                 CONTTYPE, GNUTYPE_SPARSE)
-
-# File types that are part of the GNU tar format.
-GNU_TYPES = (GNUTYPE_LONGNAME, GNUTYPE_LONGLINK,
-             GNUTYPE_SPARSE)
-
-# Fields from a pax header that override a TarInfo attribute.
-PAX_FIELDS = ("path", "linkpath", "size", "mtime",
-              "uid", "gid", "uname", "gname")
-
-# Fields from a pax header that are affected by hdrcharset.
-PAX_NAME_FIELDS = set(("path", "linkpath", "uname", "gname"))
-
-# Fields in a pax header that are numbers, all other fields
-# are treated as strings.
-PAX_NUMBER_FIELDS = {
-    "atime": float,
-    "ctime": float,
-    "mtime": float,
-    "uid": int,
-    "gid": int,
-    "size": int
-}
-
-#---------------------------------------------------------
-# Bits used in the mode field, values in octal.
-#---------------------------------------------------------
-S_IFLNK = 0o120000        # symbolic link
-S_IFREG = 0o100000        # regular file
-S_IFBLK = 0o060000        # block device
-S_IFDIR = 0o040000        # directory
-S_IFCHR = 0o020000        # character device
-S_IFIFO = 0o010000        # fifo
-
-TSUID   = 0o4000          # set UID on execution
-TSGID   = 0o2000          # set GID on execution
-TSVTX   = 0o1000          # reserved
-
-TUREAD  = 0o400           # read by owner
-TUWRITE = 0o200           # write by owner
-TUEXEC  = 0o100           # execute/search by owner
-TGREAD  = 0o040           # read by group
-TGWRITE = 0o020           # write by group
-TGEXEC  = 0o010           # execute/search by group
-TOREAD  = 0o004           # read by other
-TOWRITE = 0o002           # write by other
-TOEXEC  = 0o001           # execute/search by other
-
-#---------------------------------------------------------
-# initialization
-#---------------------------------------------------------
-if os.name in ("nt", "ce"):
-    ENCODING = "utf-8"
-else:
-    ENCODING = sys.getfilesystemencoding()
-
-#---------------------------------------------------------
-# Some useful functions
-#---------------------------------------------------------
-
-def stn(s, length, encoding, errors):
-    """Convert a string to a null-terminated bytes object.
-    """
-    s = s.encode(encoding, errors)
-    return s[:length] + (length - len(s)) * NUL
-
-def nts(s, encoding, errors):
-    """Convert a null-terminated bytes object to a string.
-    """
-    p = s.find(b"\0")
-    if p != -1:
-        s = s[:p]
-    return s.decode(encoding, errors)
-
-def nti(s):
-    """Convert a number field to a python number.
-    """
-    # There are two possible encodings for a number field, see
-    # itn() below.
-    if s[0] != chr(0o200):
-        try:
-            n = int(nts(s, "ascii", "strict") or "0", 8)
-        except ValueError:
-            raise InvalidHeaderError("invalid header")
-    else:
-        n = 0
-        for i in range(len(s) - 1):
-            n <<= 8
-            n += ord(s[i + 1])
-    return n
-
-def itn(n, digits=8, format=DEFAULT_FORMAT):
-    """Convert a python number to a number field.
-    """
-    # POSIX 1003.1-1988 requires numbers to be encoded as a string of
-    # octal digits followed by a null-byte, this allows values up to
-    # (8**(digits-1))-1. GNU tar allows storing numbers greater than
-    # that if necessary. A leading 0o200 byte indicates this particular
-    # encoding, the following digits-1 bytes are a big-endian
-    # representation. This allows values up to (256**(digits-1))-1.
-    if 0 <= n < 8 ** (digits - 1):
-        s = ("%0*o" % (digits - 1, n)).encode("ascii") + NUL
-    else:
-        if format != GNU_FORMAT or n >= 256 ** (digits - 1):
-            raise ValueError("overflow in number field")
-
-        if n < 0:
-            # XXX We mimic GNU tar's behaviour with negative numbers,
-            # this could raise OverflowError.
-            n = struct.unpack("L", struct.pack("l", n))[0]
-
-        s = bytearray()
-        for i in range(digits - 1):
-            s.insert(0, n & 0o377)
-            n >>= 8
-        s.insert(0, 0o200)
-    return s
-
-def calc_chksums(buf):
-    """Calculate the checksum for a member's header by summing up all
-       characters except for the chksum field which is treated as if
-       it was filled with spaces. According to the GNU tar sources,
-       some tars (Sun and NeXT) calculate chksum with signed char,
-       which will be different if there are chars in the buffer with
-       the high bit set. So we calculate two checksums, unsigned and
-       signed.
-    """
-    unsigned_chksum = 256 + sum(struct.unpack("148B", buf[:148]) + struct.unpack("356B", buf[156:512]))
-    signed_chksum = 256 + sum(struct.unpack("148b", buf[:148]) + struct.unpack("356b", buf[156:512]))
-    return unsigned_chksum, signed_chksum
-
-def copyfileobj(src, dst, length=None):
-    """Copy length bytes from fileobj src to fileobj dst.
-       If length is None, copy the entire content.
-    """
-    if length == 0:
-        return
-    if length is None:
-        while True:
-            buf = src.read(16*1024)
-            if not buf:
-                break
-            dst.write(buf)
-        return
-
-    BUFSIZE = 16 * 1024
-    blocks, remainder = divmod(length, BUFSIZE)
-    for b in range(blocks):
-        buf = src.read(BUFSIZE)
-        if len(buf) < BUFSIZE:
-            raise IOError("end of file reached")
-        dst.write(buf)
-
-    if remainder != 0:
-        buf = src.read(remainder)
-        if len(buf) < remainder:
-            raise IOError("end of file reached")
-        dst.write(buf)
-    return
-
-filemode_table = (
-    ((S_IFLNK,      "l"),
-     (S_IFREG,      "-"),
-     (S_IFBLK,      "b"),
-     (S_IFDIR,      "d"),
-     (S_IFCHR,      "c"),
-     (S_IFIFO,      "p")),
-
-    ((TUREAD,       "r"),),
-    ((TUWRITE,      "w"),),
-    ((TUEXEC|TSUID, "s"),
-     (TSUID,        "S"),
-     (TUEXEC,       "x")),
-
-    ((TGREAD,       "r"),),
-    ((TGWRITE,      "w"),),
-    ((TGEXEC|TSGID, "s"),
-     (TSGID,        "S"),
-     (TGEXEC,       "x")),
-
-    ((TOREAD,       "r"),),
-    ((TOWRITE,      "w"),),
-    ((TOEXEC|TSVTX, "t"),
-     (TSVTX,        "T"),
-     (TOEXEC,       "x"))
-)
-
-def filemode(mode):
-    """Convert a file's mode to a string of the form
-       -rwxrwxrwx.
-       Used by TarFile.list()
-    """
-    perm = []
-    for table in filemode_table:
-        for bit, char in table:
-            if mode & bit == bit:
-                perm.append(char)
-                break
-        else:
-            perm.append("-")
-    return "".join(perm)
-
-class TarError(Exception):
-    """Base exception."""
-    pass
-class ExtractError(TarError):
-    """General exception for extract errors."""
-    pass
-class ReadError(TarError):
-    """Exception for unreadable tar archives."""
-    pass
-class CompressionError(TarError):
-    """Exception for unavailable compression methods."""
-    pass
-class StreamError(TarError):
-    """Exception for unsupported operations on stream-like TarFiles."""
-    pass
-class HeaderError(TarError):
-    """Base exception for header errors."""
-    pass
-class EmptyHeaderError(HeaderError):
-    """Exception for empty headers."""
-    pass
-class TruncatedHeaderError(HeaderError):
-    """Exception for truncated headers."""
-    pass
-class EOFHeaderError(HeaderError):
-    """Exception for end of file headers."""
-    pass
-class InvalidHeaderError(HeaderError):
-    """Exception for invalid headers."""
-    pass
-class SubsequentHeaderError(HeaderError):
-    """Exception for missing and invalid extended headers."""
-    pass
-
-#---------------------------
-# internal stream interface
-#---------------------------
-class _LowLevelFile(object):
-    """Low-level file object. Supports reading and writing.
-       It is used instead of a regular file object for streaming
-       access.
-    """
-
-    def __init__(self, name, mode):
-        mode = {
-            "r": os.O_RDONLY,
-            "w": os.O_WRONLY | os.O_CREAT | os.O_TRUNC,
-        }[mode]
-        if hasattr(os, "O_BINARY"):
-            mode |= os.O_BINARY
-        self.fd = os.open(name, mode, 0o666)
-
-    def close(self):
-        os.close(self.fd)
-
-    def read(self, size):
-        return os.read(self.fd, size)
-
-    def write(self, s):
-        os.write(self.fd, s)
-
-class _Stream(object):
-    """Class that serves as an adapter between TarFile and
-       a stream-like object.  The stream-like object only
-       needs to have a read() or write() method and is accessed
-       blockwise.  Use of gzip or bzip2 compression is possible.
-       A stream-like object could be for example: sys.stdin,
-       sys.stdout, a socket, a tape device etc.
-
-       _Stream is intended to be used only internally.
-    """
-
-    def __init__(self, name, mode, comptype, fileobj, bufsize):
-        """Construct a _Stream object.
-        """
-        self._extfileobj = True
-        if fileobj is None:
-            fileobj = _LowLevelFile(name, mode)
-            self._extfileobj = False
-
-        if comptype == '*':
-            # Enable transparent compression detection for the
-            # stream interface
-            fileobj = _StreamProxy(fileobj)
-            comptype = fileobj.getcomptype()
-
-        self.name     = name or ""
-        self.mode     = mode
-        self.comptype = comptype
-        self.fileobj  = fileobj
-        self.bufsize  = bufsize
-        self.buf      = b""
-        self.pos      = 0
-        self.closed   = False
-
-        try:
-            if comptype == "gz":
-                try:
-                    import zlib
-                except ImportError:
-                    raise CompressionError("zlib module is not available")
-                self.zlib = zlib
-                self.crc = zlib.crc32(b"")
-                if mode == "r":
-                    self._init_read_gz()
-                else:
-                    self._init_write_gz()
-
-            if comptype == "bz2":
-                try:
-                    import bz2
-                except ImportError:
-                    raise CompressionError("bz2 module is not available")
-                if mode == "r":
-                    self.dbuf = b""
-                    self.cmp = bz2.BZ2Decompressor()
-                else:
-                    self.cmp = bz2.BZ2Compressor()
-        except:
-            if not self._extfileobj:
-                self.fileobj.close()
-            self.closed = True
-            raise
-
-    def __del__(self):
-        if hasattr(self, "closed") and not self.closed:
-            self.close()
-
-    def _init_write_gz(self):
-        """Initialize for writing with gzip compression.
-        """
-        self.cmp = self.zlib.compressobj(9, self.zlib.DEFLATED,
-                                            -self.zlib.MAX_WBITS,
-                                            self.zlib.DEF_MEM_LEVEL,
-                                            0)
-        timestamp = struct.pack("<L", int(time.time()))
-        self.__write(b"\037\213\010\010" + timestamp + b"\002\377")
-        if self.name.endswith(".gz"):
-            self.name = self.name[:-3]
-        # RFC1952 says we must use ISO-8859-1 for the FNAME field.
-        self.__write(self.name.encode("iso-8859-1", "replace") + NUL)
-
-    def write(self, s):
-        """Write string s to the stream.
-        """
-        if self.comptype == "gz":
-            self.crc = self.zlib.crc32(s, self.crc)
-        self.pos += len(s)
-        if self.comptype != "tar":
-            s = self.cmp.compress(s)
-        self.__write(s)
-
-    def __write(self, s):
-        """Write string s to the stream if a whole new block
-           is ready to be written.
-        """
-        self.buf += s
-        while len(self.buf) > self.bufsize:
-            self.fileobj.write(self.buf[:self.bufsize])
-            self.buf = self.buf[self.bufsize:]
-
-    def close(self):
-        """Close the _Stream object. No operation should be
-           done on it afterwards.
-        """
-        if self.closed:
-            return
-
-        if self.mode == "w" and self.comptype != "tar":
-            self.buf += self.cmp.flush()
-
-        if self.mode == "w" and self.buf:
-            self.fileobj.write(self.buf)
-            self.buf = b""
-            if self.comptype == "gz":
-                # The native zlib crc is an unsigned 32-bit integer, but
-                # the Python wrapper implicitly casts that to a signed C
-                # long.  So, on a 32-bit box self.crc may "look negative",
-                # while the same crc on a 64-bit box may "look positive".
-                # To avoid irksome warnings from the `struct` module, force
-                # it to look positive on all boxes.
-                self.fileobj.write(struct.pack("<L", self.crc & 0xffffffff))
-                self.fileobj.write(struct.pack("<L", self.pos & 0xffffFFFF))
-
-        if not self._extfileobj:
-            self.fileobj.close()
-
-        self.closed = True
-
-    def _init_read_gz(self):
-        """Initialize for reading a gzip compressed fileobj.
-        """
-        self.cmp = self.zlib.decompressobj(-self.zlib.MAX_WBITS)
-        self.dbuf = b""
-
-        # taken from gzip.GzipFile with some alterations
-        if self.__read(2) != b"\037\213":
-            raise ReadError("not a gzip file")
-        if self.__read(1) != b"\010":
-            raise CompressionError("unsupported compression method")
-
-        flag = ord(self.__read(1))
-        self.__read(6)
-
-        if flag & 4:
-            xlen = ord(self.__read(1)) + 256 * ord(self.__read(1))
-            self.read(xlen)
-        if flag & 8:
-            while True:
-                s = self.__read(1)
-                if not s or s == NUL:
-                    break
-        if flag & 16:
-            while True:
-                s = self.__read(1)
-                if not s or s == NUL:
-                    break
-        if flag & 2:
-            self.__read(2)
-
-    def tell(self):
-        """Return the stream's file pointer position.
-        """
-        return self.pos
-
-    def seek(self, pos=0):
-        """Set the stream's file pointer to pos. Negative seeking
-           is forbidden.
-        """
-        if pos - self.pos >= 0:
-            blocks, remainder = divmod(pos - self.pos, self.bufsize)
-            for i in range(blocks):
-                self.read(self.bufsize)
-            self.read(remainder)
-        else:
-            raise StreamError("seeking backwards is not allowed")
-        return self.pos
-
-    def read(self, size=None):
-        """Return the next size number of bytes from the stream.
-           If size is not defined, return all bytes of the stream
-           up to EOF.
-        """
-        if size is None:
-            t = []
-            while True:
-                buf = self._read(self.bufsize)
-                if not buf:
-                    break
-                t.append(buf)
-            buf = "".join(t)
-        else:
-            buf = self._read(size)
-        self.pos += len(buf)
-        return buf
-
-    def _read(self, size):
-        """Return size bytes from the stream.
-        """
-        if self.comptype == "tar":
-            return self.__read(size)
-
-        c = len(self.dbuf)
-        while c < size:
-            buf = self.__read(self.bufsize)
-            if not buf:
-                break
-            try:
-                buf = self.cmp.decompress(buf)
-            except IOError:
-                raise ReadError("invalid compressed data")
-            self.dbuf += buf
-            c += len(buf)
-        buf = self.dbuf[:size]
-        self.dbuf = self.dbuf[size:]
-        return buf
-
-    def __read(self, size):
-        """Return size bytes from stream. If internal buffer is empty,
-           read another block from the stream.
-        """
-        c = len(self.buf)
-        while c < size:
-            buf = self.fileobj.read(self.bufsize)
-            if not buf:
-                break
-            self.buf += buf
-            c += len(buf)
-        buf = self.buf[:size]
-        self.buf = self.buf[size:]
-        return buf
-# class _Stream
-
-class _StreamProxy(object):
-    """Small proxy class that enables transparent compression
-       detection for the Stream interface (mode 'r|*').
-    """
-
-    def __init__(self, fileobj):
-        self.fileobj = fileobj
-        self.buf = self.fileobj.read(BLOCKSIZE)
-
-    def read(self, size):
-        self.read = self.fileobj.read
-        return self.buf
-
-    def getcomptype(self):
-        if self.buf.startswith(b"\037\213\010"):
-            return "gz"
-        if self.buf.startswith(b"BZh91"):
-            return "bz2"
-        return "tar"
-
-    def close(self):
-        self.fileobj.close()
-# class StreamProxy
-
-class _BZ2Proxy(object):
-    """Small proxy class that enables external file object
-       support for "r:bz2" and "w:bz2" modes. This is actually
-       a workaround for a limitation in bz2 module's BZ2File
-       class which (unlike gzip.GzipFile) has no support for
-       a file object argument.
-    """
-
-    blocksize = 16 * 1024
-
-    def __init__(self, fileobj, mode):
-        self.fileobj = fileobj
-        self.mode = mode
-        self.name = getattr(self.fileobj, "name", None)
-        self.init()
-
-    def init(self):
-        import bz2
-        self.pos = 0
-        if self.mode == "r":
-            self.bz2obj = bz2.BZ2Decompressor()
-            self.fileobj.seek(0)
-            self.buf = b""
-        else:
-            self.bz2obj = bz2.BZ2Compressor()
-
-    def read(self, size):
-        x = len(self.buf)
-        while x < size:
-            raw = self.fileobj.read(self.blocksize)
-            if not raw:
-                break
-            data = self.bz2obj.decompress(raw)
-            self.buf += data
-            x += len(data)
-
-        buf = self.buf[:size]
-        self.buf = self.buf[size:]
-        self.pos += len(buf)
-        return buf
-
-    def seek(self, pos):
-        if pos < self.pos:
-            self.init()
-        self.read(pos - self.pos)
-
-    def tell(self):
-        return self.pos
-
-    def write(self, data):
-        self.pos += len(data)
-        raw = self.bz2obj.compress(data)
-        self.fileobj.write(raw)
-
-    def close(self):
-        if self.mode == "w":
-            raw = self.bz2obj.flush()
-            self.fileobj.write(raw)
-# class _BZ2Proxy
-
-#------------------------
-# Extraction file object
-#------------------------
-class _FileInFile(object):
-    """A thin wrapper around an existing file object that
-       provides a part of its data as an individual file
-       object.
-    """
-
-    def __init__(self, fileobj, offset, size, blockinfo=None):
-        self.fileobj = fileobj
-        self.offset = offset
-        self.size = size
-        self.position = 0
-
-        if blockinfo is None:
-            blockinfo = [(0, size)]
-
-        # Construct a map with data and zero blocks.
-        self.map_index = 0
-        self.map = []
-        lastpos = 0
-        realpos = self.offset
-        for offset, size in blockinfo:
-            if offset > lastpos:
-                self.map.append((False, lastpos, offset, None))
-            self.map.append((True, offset, offset + size, realpos))
-            realpos += size
-            lastpos = offset + size
-        if lastpos < self.size:
-            self.map.append((False, lastpos, self.size, None))
-
-    def seekable(self):
-        if not hasattr(self.fileobj, "seekable"):
-            # XXX gzip.GzipFile and bz2.BZ2File
-            return True
-        return self.fileobj.seekable()
-
-    def tell(self):
-        """Return the current file position.
-        """
-        return self.position
-
-    def seek(self, position):
-        """Seek to a position in the file.
-        """
-        self.position = position
-
-    def read(self, size=None):
-        """Read data from the file.
-        """
-        if size is None:
-            size = self.size - self.position
-        else:
-            size = min(size, self.size - self.position)
-
-        buf = b""
-        while size > 0:
-            while True:
-                data, start, stop, offset = self.map[self.map_index]
-                if start <= self.position < stop:
-                    break
-                else:
-                    self.map_index += 1
-                    if self.map_index == len(self.map):
-                        self.map_index = 0
-            length = min(size, stop - self.position)
-            if data:
-                self.fileobj.seek(offset + (self.position - start))
-                buf += self.fileobj.read(length)
-            else:
-                buf += NUL * length
-            size -= length
-            self.position += length
-        return buf
-#class _FileInFile
-
-
-class ExFileObject(object):
-    """File-like object for reading an archive member.
-       Is returned by TarFile.extractfile().
-    """
-    blocksize = 1024
-
-    def __init__(self, tarfile, tarinfo):
-        self.fileobj = _FileInFile(tarfile.fileobj,
-                                   tarinfo.offset_data,
-                                   tarinfo.size,
-                                   tarinfo.sparse)
-        self.name = tarinfo.name
-        self.mode = "r"
-        self.closed = False
-        self.size = tarinfo.size
-
-        self.position = 0
-        self.buffer = b""
-
-    def readable(self):
-        return True
-
-    def writable(self):
-        return False
-
-    def seekable(self):
-        return self.fileobj.seekable()
-
-    def read(self, size=None):
-        """Read at most size bytes from the file. If size is not
-           present or None, read all data until EOF is reached.
-        """
-        if self.closed:
-            raise ValueError("I/O operation on closed file")
-
-        buf = b""
-        if self.buffer:
-            if size is None:
-                buf = self.buffer
-                self.buffer = b""
-            else:
-                buf = self.buffer[:size]
-                self.buffer = self.buffer[size:]
-
-        if size is None:
-            buf += self.fileobj.read()
-        else:
-            buf += self.fileobj.read(size - len(buf))
-
-        self.position += len(buf)
-        return buf
-
-    # XXX TextIOWrapper uses the read1() method.
-    read1 = read
-
-    def readline(self, size=-1):
-        """Read one entire line from the file. If size is present
-           and non-negative, return a string with at most that
-           size, which may be an incomplete line.
-        """
-        if self.closed:
-            raise ValueError("I/O operation on closed file")
-
-        pos = self.buffer.find(b"\n") + 1
-        if pos == 0:
-            # no newline found.
-            while True:
-                buf = self.fileobj.read(self.blocksize)
-                self.buffer += buf
-                if not buf or b"\n" in buf:
-                    pos = self.buffer.find(b"\n") + 1
-                    if pos == 0:
-                        # no newline found.
-                        pos = len(self.buffer)
-                    break
-
-        if size != -1:
-            pos = min(size, pos)
-
-        buf = self.buffer[:pos]
-        self.buffer = self.buffer[pos:]
-        self.position += len(buf)
-        return buf
-
-    def readlines(self):
-        """Return a list with all remaining lines.
-        """
-        result = []
-        while True:
-            line = self.readline()
-            if not line: break
-            result.append(line)
-        return result
-
-    def tell(self):
-        """Return the current file position.
-        """
-        if self.closed:
-            raise ValueError("I/O operation on closed file")
-
-        return self.position
-
-    def seek(self, pos, whence=os.SEEK_SET):
-        """Seek to a position in the file.
-        """
-        if self.closed:
-            raise ValueError("I/O operation on closed file")
-
-        if whence == os.SEEK_SET:
-            self.position = min(max(pos, 0), self.size)
-        elif whence == os.SEEK_CUR:
-            if pos < 0:
-                self.position = max(self.position + pos, 0)
-            else:
-                self.position = min(self.position + pos, self.size)
-        elif whence == os.SEEK_END:
-            self.position = max(min(self.size + pos, self.size), 0)
-        else:
-            raise ValueError("Invalid argument")
-
-        self.buffer = b""
-        self.fileobj.seek(self.position)
-
-    def close(self):
-        """Close the file object.
-        """
-        self.closed = True
-
-    def __iter__(self):
-        """Get an iterator over the file's lines.
-        """
-        while True:
-            line = self.readline()
-            if not line:
-                break
-            yield line
-#class ExFileObject
-
-#------------------
-# Exported Classes
-#------------------
-class TarInfo(object):
-    """Informational class which holds the details about an
-       archive member given by a tar header block.
-       TarInfo objects are returned by TarFile.getmember(),
-       TarFile.getmembers() and TarFile.gettarinfo() and are
-       usually created internally.
-    """
-
-    __slots__ = ("name", "mode", "uid", "gid", "size", "mtime",
-                 "chksum", "type", "linkname", "uname", "gname",
-                 "devmajor", "devminor",
-                 "offset", "offset_data", "pax_headers", "sparse",
-                 "tarfile", "_sparse_structs", "_link_target")
-
-    def __init__(self, name=""):
-        """Construct a TarInfo object. name is the optional name
-           of the member.
-        """
-        self.name = name        # member name
-        self.mode = 0o644       # file permissions
-        self.uid = 0            # user id
-        self.gid = 0            # group id
-        self.size = 0           # file size
-        self.mtime = 0          # modification time
-        self.chksum = 0         # header checksum
-        self.type = REGTYPE     # member type
-        self.linkname = ""      # link name
-        self.uname = ""         # user name
-        self.gname = ""         # group name
-        self.devmajor = 0       # device major number
-        self.devminor = 0       # device minor number
-
-        self.offset = 0         # the tar header starts here
-        self.offset_data = 0    # the file's data starts here
-
-        self.sparse = None      # sparse member information
-        self.pax_headers = {}   # pax header information
-
-    # In pax headers the "name" and "linkname" field are called
-    # "path" and "linkpath".
-    def _getpath(self):
-        return self.name
-    def _setpath(self, name):
-        self.name = name
-    path = property(_getpath, _setpath)
-
-    def _getlinkpath(self):
-        return self.linkname
-    def _setlinkpath(self, linkname):
-        self.linkname = linkname
-    linkpath = property(_getlinkpath, _setlinkpath)
-
-    def __repr__(self):
-        return "<%s %r at %#x>" % (self.__class__.__name__,self.name,id(self))
-
-    def get_info(self):
-        """Return the TarInfo's attributes as a dictionary.
-        """
-        info = {
-            "name":     self.name,
-            "mode":     self.mode & 0o7777,
-            "uid":      self.uid,
-            "gid":      self.gid,
-            "size":     self.size,
-            "mtime":    self.mtime,
-            "chksum":   self.chksum,
-            "type":     self.type,
-            "linkname": self.linkname,
-            "uname":    self.uname,
-            "gname":    self.gname,
-            "devmajor": self.devmajor,
-            "devminor": self.devminor
-        }
-
-        if info["type"] == DIRTYPE and not info["name"].endswith("/"):
-            info["name"] += "/"
-
-        return info
-
-    def tobuf(self, format=DEFAULT_FORMAT, encoding=ENCODING, errors="surrogateescape"):
-        """Return a tar header as a string of 512 byte blocks.
-        """
-        info = self.get_info()
-
-        if format == USTAR_FORMAT:
-            return self.create_ustar_header(info, encoding, errors)
-        elif format == GNU_FORMAT:
-            return self.create_gnu_header(info, encoding, errors)
-        elif format == PAX_FORMAT:
-            return self.create_pax_header(info, encoding)
-        else:
-            raise ValueError("invalid format")
-
-    def create_ustar_header(self, info, encoding, errors):
-        """Return the object as a ustar header block.
-        """
-        info["magic"] = POSIX_MAGIC
-
-        if len(info["linkname"]) > LENGTH_LINK:
-            raise ValueError("linkname is too long")
-
-        if len(info["name"]) > LENGTH_NAME:
-            info["prefix"], info["name"] = self._posix_split_name(info["name"])
-
-        return self._create_header(info, USTAR_FORMAT, encoding, errors)
-
-    def create_gnu_header(self, info, encoding, errors):
-        """Return the object as a GNU header block sequence.
-        """
-        info["magic"] = GNU_MAGIC
-
-        buf = b""
-        if len(info["linkname"]) > LENGTH_LINK:
-            buf += self._create_gnu_long_header(info["linkname"], GNUTYPE_LONGLINK, encoding, errors)
-
-        if len(info["name"]) > LENGTH_NAME:
-            buf += self._create_gnu_long_header(info["name"], GNUTYPE_LONGNAME, encoding, errors)
-
-        return buf + self._create_header(info, GNU_FORMAT, encoding, errors)
-
-    def create_pax_header(self, info, encoding):
-        """Return the object as a ustar header block. If it cannot be
-           represented this way, prepend a pax extended header sequence
-           with supplement information.
-        """
-        info["magic"] = POSIX_MAGIC
-        pax_headers = self.pax_headers.copy()
-
-        # Test string fields for values that exceed the field length or cannot
-        # be represented in ASCII encoding.
-        for name, hname, length in (
-                ("name", "path", LENGTH_NAME), ("linkname", "linkpath", LENGTH_LINK),
-                ("uname", "uname", 32), ("gname", "gname", 32)):
-
-            if hname in pax_headers:
-                # The pax header has priority.
-                continue
-
-            # Try to encode the string as ASCII.
-            try:
-                info[name].encode("ascii", "strict")
-            except UnicodeEncodeError:
-                pax_headers[hname] = info[name]
-                continue
-
-            if len(info[name]) > length:
-                pax_headers[hname] = info[name]
-
-        # Test number fields for values that exceed the field limit or values
-        # that like to be stored as float.
-        for name, digits in (("uid", 8), ("gid", 8), ("size", 12), ("mtime", 12)):
-            if name in pax_headers:
-                # The pax header has priority. Avoid overflow.
-                info[name] = 0
-                continue
-
-            val = info[name]
-            if not 0 <= val < 8 ** (digits - 1) or isinstance(val, float):
-                pax_headers[name] = str(val)
-                info[name] = 0
-
-        # Create a pax extended header if necessary.
-        if pax_headers:
-            buf = self._create_pax_generic_header(pax_headers, XHDTYPE, encoding)
-        else:
-            buf = b""
-
-        return buf + self._create_header(info, USTAR_FORMAT, "ascii", "replace")
-
-    @classmethod
-    def create_pax_global_header(cls, pax_headers):
-        """Return the object as a pax global header block sequence.
-        """
-        return cls._create_pax_generic_header(pax_headers, XGLTYPE, "utf8")
-
-    def _posix_split_name(self, name):
-        """Split a name longer than 100 chars into a prefix
-           and a name part.
-        """
-        prefix = name[:LENGTH_PREFIX + 1]
-        while prefix and prefix[-1] != "/":
-            prefix = prefix[:-1]
-
-        name = name[len(prefix):]
-        prefix = prefix[:-1]
-
-        if not prefix or len(name) > LENGTH_NAME:
-            raise ValueError("name is too long")
-        return prefix, name
-
-    @staticmethod
-    def _create_header(info, format, encoding, errors):
-        """Return a header block. info is a dictionary with file
-           information, format must be one of the *_FORMAT constants.
-        """
-        parts = [
-            stn(info.get("name", ""), 100, encoding, errors),
-            itn(info.get("mode", 0) & 0o7777, 8, format),
-            itn(info.get("uid", 0), 8, format),
-            itn(info.get("gid", 0), 8, format),
-            itn(info.get("size", 0), 12, format),
-            itn(info.get("mtime", 0), 12, format),
-            b"        ", # checksum field
-            info.get("type", REGTYPE),
-            stn(info.get("linkname", ""), 100, encoding, errors),
-            info.get("magic", POSIX_MAGIC),
-            stn(info.get("uname", ""), 32, encoding, errors),
-            stn(info.get("gname", ""), 32, encoding, errors),
-            itn(info.get("devmajor", 0), 8, format),
-            itn(info.get("devminor", 0), 8, format),
-            stn(info.get("prefix", ""), 155, encoding, errors)
-        ]
-
-        buf = struct.pack("%ds" % BLOCKSIZE, b"".join(parts))
-        chksum = calc_chksums(buf[-BLOCKSIZE:])[0]
-        buf = buf[:-364] + ("%06o\0" % chksum).encode("ascii") + buf[-357:]
-        return buf
-
-    @staticmethod
-    def _create_payload(payload):
-        """Return the string payload filled with zero bytes
-           up to the next 512 byte border.
-        """
-        blocks, remainder = divmod(len(payload), BLOCKSIZE)
-        if remainder > 0:
-            payload += (BLOCKSIZE - remainder) * NUL
-        return payload
-
-    @classmethod
-    def _create_gnu_long_header(cls, name, type, encoding, errors):
-        """Return a GNUTYPE_LONGNAME or GNUTYPE_LONGLINK sequence
-           for name.
-        """
-        name = name.encode(encoding, errors) + NUL
-
-        info = {}
-        info["name"] = "././@LongLink"
-        info["type"] = type
-        info["size"] = len(name)
-        info["magic"] = GNU_MAGIC
-
-        # create extended header + name blocks.
-        return cls._create_header(info, USTAR_FORMAT, encoding, errors) + \
-                cls._create_payload(name)
-
-    @classmethod
-    def _create_pax_generic_header(cls, pax_headers, type, encoding):
-        """Return a POSIX.1-2008 extended or global header sequence
-           that contains a list of keyword, value pairs. The values
-           must be strings.
-        """
-        # Check if one of the fields contains surrogate characters and thereby
-        # forces hdrcharset=BINARY, see _proc_pax() for more information.
-        binary = False
-        for keyword, value in pax_headers.items():
-            try:
-                value.encode("utf8", "strict")
-            except UnicodeEncodeError:
-                binary = True
-                break
-
-        records = b""
-        if binary:
-            # Put the hdrcharset field at the beginning of the header.
-            records += b"21 hdrcharset=BINARY\n"
-
-        for keyword, value in pax_headers.items():
-            keyword = keyword.encode("utf8")
-            if binary:
-                # Try to restore the original byte representation of `value'.
-                # Needless to say, that the encoding must match the string.
-                value = value.encode(encoding, "surrogateescape")
-            else:
-                value = value.encode("utf8")
-
-            l = len(keyword) + len(value) + 3   # ' ' + '=' + '\n'
-            n = p = 0
-            while True:
-                n = l + len(str(p))
-                if n == p:
-                    break
-                p = n
-            records += bytes(str(p), "ascii") + b" " + keyword + b"=" + value + b"\n"
-
-        # We use a hardcoded "././@PaxHeader" name like star does
-        # instead of the one that POSIX recommends.
-        info = {}
-        info["name"] = "././@PaxHeader"
-        info["type"] = type
-        info["size"] = len(records)
-        info["magic"] = POSIX_MAGIC
-
-        # Create pax header + record blocks.
-        return cls._create_header(info, USTAR_FORMAT, "ascii", "replace") + \
-                cls._create_payload(records)
-
-    @classmethod
-    def frombuf(cls, buf, encoding, errors):
-        """Construct a TarInfo object from a 512 byte bytes object.
-        """
-        if len(buf) == 0:
-            raise EmptyHeaderError("empty header")
-        if len(buf) != BLOCKSIZE:
-            raise TruncatedHeaderError("truncated header")
-        if buf.count(NUL) == BLOCKSIZE:
-            raise EOFHeaderError("end of file header")
-
-        chksum = nti(buf[148:156])
-        if chksum not in calc_chksums(buf):
-            raise InvalidHeaderError("bad checksum")
-
-        obj = cls()
-        obj.name = nts(buf[0:100], encoding, errors)
-        obj.mode = nti(buf[100:108])
-        obj.uid = nti(buf[108:116])
-        obj.gid = nti(buf[116:124])
-        obj.size = nti(buf[124:136])
-        obj.mtime = nti(buf[136:148])
-        obj.chksum = chksum
-        obj.type = buf[156:157]
-        obj.linkname = nts(buf[157:257], encoding, errors)
-        obj.uname = nts(buf[265:297], encoding, errors)
-        obj.gname = nts(buf[297:329], encoding, errors)
-        obj.devmajor = nti(buf[329:337])
-        obj.devminor = nti(buf[337:345])
-        prefix = nts(buf[345:500], encoding, errors)
-
-        # Old V7 tar format represents a directory as a regular
-        # file with a trailing slash.
-        if obj.type == AREGTYPE and obj.name.endswith("/"):
-            obj.type = DIRTYPE
-
-        # The old GNU sparse format occupies some of the unused
-        # space in the buffer for up to 4 sparse structures.
-        # Save the them for later processing in _proc_sparse().
-        if obj.type == GNUTYPE_SPARSE:
-            pos = 386
-            structs = []
-            for i in range(4):
-                try:
-                    offset = nti(buf[pos:pos + 12])
-                    numbytes = nti(buf[pos + 12:pos + 24])
-                except ValueError:
-                    break
-                structs.append((offset, numbytes))
-                pos += 24
-            isextended = bool(buf[482])
-            origsize = nti(buf[483:495])
-            obj._sparse_structs = (structs, isextended, origsize)
-
-        # Remove redundant slashes from directories.
-        if obj.isdir():
-            obj.name = obj.name.rstrip("/")
-
-        # Reconstruct a ustar longname.
-        if prefix and obj.type not in GNU_TYPES:
-            obj.name = prefix + "/" + obj.name
-        return obj
-
-    @classmethod
-    def fromtarfile(cls, tarfile):
-        """Return the next TarInfo object from TarFile object
-           tarfile.
-        """
-        buf = tarfile.fileobj.read(BLOCKSIZE)
-        obj = cls.frombuf(buf, tarfile.encoding, tarfile.errors)
-        obj.offset = tarfile.fileobj.tell() - BLOCKSIZE
-        return obj._proc_member(tarfile)
-
-    #--------------------------------------------------------------------------
-    # The following are methods that are called depending on the type of a
-    # member. The entry point is _proc_member() which can be overridden in a
-    # subclass to add custom _proc_*() methods. A _proc_*() method MUST
-    # implement the following
-    # operations:
-    # 1. Set self.offset_data to the position where the data blocks begin,
-    #    if there is data that follows.
-    # 2. Set tarfile.offset to the position where the next member's header will
-    #    begin.
-    # 3. Return self or another valid TarInfo object.
-    def _proc_member(self, tarfile):
-        """Choose the right processing method depending on
-           the type and call it.
-        """
-        if self.type in (GNUTYPE_LONGNAME, GNUTYPE_LONGLINK):
-            return self._proc_gnulong(tarfile)
-        elif self.type == GNUTYPE_SPARSE:
-            return self._proc_sparse(tarfile)
-        elif self.type in (XHDTYPE, XGLTYPE, SOLARIS_XHDTYPE):
-            return self._proc_pax(tarfile)
-        else:
-            return self._proc_builtin(tarfile)
-
-    def _proc_builtin(self, tarfile):
-        """Process a builtin type or an unknown type which
-           will be treated as a regular file.
-        """
-        self.offset_data = tarfile.fileobj.tell()
-        offset = self.offset_data
-        if self.isreg() or self.type not in SUPPORTED_TYPES:
-            # Skip the following data blocks.
-            offset += self._block(self.size)
-        tarfile.offset = offset
-
-        # Patch the TarInfo object with saved global
-        # header information.
-        self._apply_pax_info(tarfile.pax_headers, tarfile.encoding, tarfile.errors)
-
-        return self
-
-    def _proc_gnulong(self, tarfile):
-        """Process the blocks that hold a GNU longname
-           or longlink member.
-        """
-        buf = tarfile.fileobj.read(self._block(self.size))
-
-        # Fetch the next header and process it.
-        try:
-            next = self.fromtarfile(tarfile)
-        except HeaderError:
-            raise SubsequentHeaderError("missing or bad subsequent header")
-
-        # Patch the TarInfo object from the next header with
-        # the longname information.
-        next.offset = self.offset
-        if self.type == GNUTYPE_LONGNAME:
-            next.name = nts(buf, tarfile.encoding, tarfile.errors)
-        elif self.type == GNUTYPE_LONGLINK:
-            next.linkname = nts(buf, tarfile.encoding, tarfile.errors)
-
-        return next
-
-    def _proc_sparse(self, tarfile):
-        """Process a GNU sparse header plus extra headers.
-        """
-        # We already collected some sparse structures in frombuf().
-        structs, isextended, origsize = self._sparse_structs
-        del self._sparse_structs
-
-        # Collect sparse structures from extended header blocks.
-        while isextended:
-            buf = tarfile.fileobj.read(BLOCKSIZE)
-            pos = 0
-            for i in range(21):
-                try:
-                    offset = nti(buf[pos:pos + 12])
-                    numbytes = nti(buf[pos + 12:pos + 24])
-                except ValueError:
-                    break
-                if offset and numbytes:
-                    structs.append((offset, numbytes))
-                pos += 24
-            isextended = bool(buf[504])
-        self.sparse = structs
-
-        self.offset_data = tarfile.fileobj.tell()
-        tarfile.offset = self.offset_data + self._block(self.size)
-        self.size = origsize
-        return self
-
-    def _proc_pax(self, tarfile):
-        """Process an extended or global header as described in
-           POSIX.1-2008.
-        """
-        # Read the header information.
-        buf = tarfile.fileobj.read(self._block(self.size))
-
-        # A pax header stores supplemental information for either
-        # the following file (extended) or all following files
-        # (global).
-        if self.type == XGLTYPE:
-            pax_headers = tarfile.pax_headers
-        else:
-            pax_headers = tarfile.pax_headers.copy()
-
-        # Check if the pax header contains a hdrcharset field. This tells us
-        # the encoding of the path, linkpath, uname and gname fields. Normally,
-        # these fields are UTF-8 encoded but since POSIX.1-2008 tar
-        # implementations are allowed to store them as raw binary strings if
-        # the translation to UTF-8 fails.
-        match = re.search(br"\d+ hdrcharset=([^\n]+)\n", buf)
-        if match is not None:
-            pax_headers["hdrcharset"] = match.group(1).decode("utf8")
-
-        # For the time being, we don't care about anything other than "BINARY".
-        # The only other value that is currently allowed by the standard is
-        # "ISO-IR 10646 2000 UTF-8" in other words UTF-8.
-        hdrcharset = pax_headers.get("hdrcharset")
-        if hdrcharset == "BINARY":
-            encoding = tarfile.encoding
-        else:
-            encoding = "utf8"
-
-        # Parse pax header information. A record looks like that:
-        # "%d %s=%s\n" % (length, keyword, value). length is the size
-        # of the complete record including the length field itself and
-        # the newline. keyword and value are both UTF-8 encoded strings.
-        regex = re.compile(br"(\d+) ([^=]+)=")
-        pos = 0
-        while True:
-            match = regex.match(buf, pos)
-            if not match:
-                break
-
-            length, keyword = match.groups()
-            length = int(length)
-            value = buf[match.end(2) + 1:match.start(1) + length - 1]
-
-            # Normally, we could just use "utf8" as the encoding and "strict"
-            # as the error handler, but we better not take the risk. For
-            # example, GNU tar <= 1.23 is known to store filenames it cannot
-            # translate to UTF-8 as raw strings (unfortunately without a
-            # hdrcharset=BINARY header).
-            # We first try the strict standard encoding, and if that fails we
-            # fall back on the user's encoding and error handler.
-            keyword = self._decode_pax_field(keyword, "utf8", "utf8",
-                    tarfile.errors)
-            if keyword in PAX_NAME_FIELDS:
-                value = self._decode_pax_field(value, encoding, tarfile.encoding,
-                        tarfile.errors)
-            else:
-                value = self._decode_pax_field(value, "utf8", "utf8",
-                        tarfile.errors)
-
-            pax_headers[keyword] = value
-            pos += length
-
-        # Fetch the next header.
-        try:
-            next = self.fromtarfile(tarfile)
-        except HeaderError:
-            raise SubsequentHeaderError("missing or bad subsequent header")
-
-        # Process GNU sparse information.
-        if "GNU.sparse.map" in pax_headers:
-            # GNU extended sparse format version 0.1.
-            self._proc_gnusparse_01(next, pax_headers)
-
-        elif "GNU.sparse.size" in pax_headers:
-            # GNU extended sparse format version 0.0.
-            self._proc_gnusparse_00(next, pax_headers, buf)
-
-        elif pax_headers.get("GNU.sparse.major") == "1" and pax_headers.get("GNU.sparse.minor") == "0":
-            # GNU extended sparse format version 1.0.
-            self._proc_gnusparse_10(next, pax_headers, tarfile)
-
-        if self.type in (XHDTYPE, SOLARIS_XHDTYPE):
-            # Patch the TarInfo object with the extended header info.
-            next._apply_pax_info(pax_headers, tarfile.encoding, tarfile.errors)
-            next.offset = self.offset
-
-            if "size" in pax_headers:
-                # If the extended header replaces the size field,
-                # we need to recalculate the offset where the next
-                # header starts.
-                offset = next.offset_data
-                if next.isreg() or next.type not in SUPPORTED_TYPES:
-                    offset += next._block(next.size)
-                tarfile.offset = offset
-
-        return next
-
-    def _proc_gnusparse_00(self, next, pax_headers, buf):
-        """Process a GNU tar extended sparse header, version 0.0.
-        """
-        offsets = []
-        for match in re.finditer(br"\d+ GNU.sparse.offset=(\d+)\n", buf):
-            offsets.append(int(match.group(1)))
-        numbytes = []
-        for match in re.finditer(br"\d+ GNU.sparse.numbytes=(\d+)\n", buf):
-            numbytes.append(int(match.group(1)))
-        next.sparse = list(zip(offsets, numbytes))
-
-    def _proc_gnusparse_01(self, next, pax_headers):
-        """Process a GNU tar extended sparse header, version 0.1.
-        """
-        sparse = [int(x) for x in pax_headers["GNU.sparse.map"].split(",")]
-        next.sparse = list(zip(sparse[::2], sparse[1::2]))
-
-    def _proc_gnusparse_10(self, next, pax_headers, tarfile):
-        """Process a GNU tar extended sparse header, version 1.0.
-        """
-        fields = None
-        sparse = []
-        buf = tarfile.fileobj.read(BLOCKSIZE)
-        fields, buf = buf.split(b"\n", 1)
-        fields = int(fields)
-        while len(sparse) < fields * 2:
-            if b"\n" not in buf:
-                buf += tarfile.fileobj.read(BLOCKSIZE)
-            number, buf = buf.split(b"\n", 1)
-            sparse.append(int(number))
-        next.offset_data = tarfile.fileobj.tell()
-        next.sparse = list(zip(sparse[::2], sparse[1::2]))
-
-    def _apply_pax_info(self, pax_headers, encoding, errors):
-        """Replace fields with supplemental information from a previous
-           pax extended or global header.
-        """
-        for keyword, value in pax_headers.items():
-            if keyword == "GNU.sparse.name":
-                setattr(self, "path", value)
-            elif keyword == "GNU.sparse.size":
-                setattr(self, "size", int(value))
-            elif keyword == "GNU.sparse.realsize":
-                setattr(self, "size", int(value))
-            elif keyword in PAX_FIELDS:
-                if keyword in PAX_NUMBER_FIELDS:
-                    try:
-                        value = PAX_NUMBER_FIELDS[keyword](value)
-                    except ValueError:
-                        value = 0
-                if keyword == "path":
-                    value = value.rstrip("/")
-                setattr(self, keyword, value)
-
-        self.pax_headers = pax_headers.copy()
-
-    def _decode_pax_field(self, value, encoding, fallback_encoding, fallback_errors):
-        """Decode a single field from a pax record.
-        """
-        try:
-            return value.decode(encoding, "strict")
-        except UnicodeDecodeError:
-            return value.decode(fallback_encoding, fallback_errors)
-
-    def _block(self, count):
-        """Round up a byte count by BLOCKSIZE and return it,
-           e.g. _block(834) => 1024.
-        """
-        blocks, remainder = divmod(count, BLOCKSIZE)
-        if remainder:
-            blocks += 1
-        return blocks * BLOCKSIZE
-
-    def isreg(self):
-        return self.type in REGULAR_TYPES
-    def isfile(self):
-        return self.isreg()
-    def isdir(self):
-        return self.type == DIRTYPE
-    def issym(self):
-        return self.type == SYMTYPE
-    def islnk(self):
-        return self.type == LNKTYPE
-    def ischr(self):
-        return self.type == CHRTYPE
-    def isblk(self):
-        return self.type == BLKTYPE
-    def isfifo(self):
-        return self.type == FIFOTYPE
-    def issparse(self):
-        return self.sparse is not None
-    def isdev(self):
-        return self.type in (CHRTYPE, BLKTYPE, FIFOTYPE)
-# class TarInfo
-
-class TarFile(object):
-    """The TarFile Class provides an interface to tar archives.
-    """
-
-    debug = 0                   # May be set from 0 (no msgs) to 3 (all msgs)
-
-    dereference = False         # If true, add content of linked file to the
-                                # tar file, else the link.
-
-    ignore_zeros = False        # If true, skips empty or invalid blocks and
-                                # continues processing.
-
-    errorlevel = 1              # If 0, fatal errors only appear in debug
-                                # messages (if debug >= 0). If > 0, errors
-                                # are passed to the caller as exceptions.
-
-    format = DEFAULT_FORMAT     # The format to use when creating an archive.
-
-    encoding = ENCODING         # Encoding for 8-bit character strings.
-
-    errors = None               # Error handler for unicode conversion.
-
-    tarinfo = TarInfo           # The default TarInfo class to use.
-
-    fileobject = ExFileObject   # The default ExFileObject class to use.
-
-    def __init__(self, name=None, mode="r", fileobj=None, format=None,
-            tarinfo=None, dereference=None, ignore_zeros=None, encoding=None,
-            errors="surrogateescape", pax_headers=None, debug=None, errorlevel=None):
-        """Open an (uncompressed) tar archive `name'. `mode' is either 'r' to
-           read from an existing archive, 'a' to append data to an existing
-           file or 'w' to create a new file overwriting an existing one. `mode'
-           defaults to 'r'.
-           If `fileobj' is given, it is used for reading or writing data. If it
-           can be determined, `mode' is overridden by `fileobj's mode.
-           `fileobj' is not closed, when TarFile is closed.
-        """
-        if len(mode) > 1 or mode not in "raw":
-            raise ValueError("mode must be 'r', 'a' or 'w'")
-        self.mode = mode
-        self._mode = {"r": "rb", "a": "r+b", "w": "wb"}[mode]
-
-        if not fileobj:
-            if self.mode == "a" and not os.path.exists(name):
-                # Create nonexistent files in append mode.
-                self.mode = "w"
-                self._mode = "wb"
-            fileobj = bltn_open(name, self._mode)
-            self._extfileobj = False
-        else:
-            if name is None and hasattr(fileobj, "name"):
-                name = fileobj.name
-            if hasattr(fileobj, "mode"):
-                self._mode = fileobj.mode
-            self._extfileobj = True
-        self.name = os.path.abspath(name) if name else None
-        self.fileobj = fileobj
-
-        # Init attributes.
-        if format is not None:
-            self.format = format
-        if tarinfo is not None:
-            self.tarinfo = tarinfo
-        if dereference is not None:
-            self.dereference = dereference
-        if ignore_zeros is not None:
-            self.ignore_zeros = ignore_zeros
-        if encoding is not None:
-            self.encoding = encoding
-        self.errors = errors
-
-        if pax_headers is not None and self.format == PAX_FORMAT:
-            self.pax_headers = pax_headers
-        else:
-            self.pax_headers = {}
-
-        if debug is not None:
-            self.debug = debug
-        if errorlevel is not None:
-            self.errorlevel = errorlevel
-
-        # Init datastructures.
-        self.closed = False
-        self.members = []       # list of members as TarInfo objects
-        self._loaded = False    # flag if all members have been read
-        self.offset = self.fileobj.tell()
-                                # current position in the archive file
-        self.inodes = {}        # dictionary caching the inodes of
-                                # archive members already added
-
-        try:
-            if self.mode == "r":
-                self.firstmember = None
-                self.firstmember = self.next()
-
-            if self.mode == "a":
-                # Move to the end of the archive,
-                # before the first empty block.
-                while True:
-                    self.fileobj.seek(self.offset)
-                    try:
-                        tarinfo = self.tarinfo.fromtarfile(self)
-                        self.members.append(tarinfo)
-                    except EOFHeaderError:
-                        self.fileobj.seek(self.offset)
-                        break
-                    except HeaderError as e:
-                        raise ReadError(str(e))
-
-            if self.mode in "aw":
-                self._loaded = True
-
-                if self.pax_headers:
-                    buf = self.tarinfo.create_pax_global_header(self.pax_headers.copy())
-                    self.fileobj.write(buf)
-                    self.offset += len(buf)
-        except:
-            if not self._extfileobj:
-                self.fileobj.close()
-            self.closed = True
-            raise
-
-    #--------------------------------------------------------------------------
-    # Below are the classmethods which act as alternate constructors to the
-    # TarFile class. The open() method is the only one that is needed for
-    # public use; it is the "super"-constructor and is able to select an
-    # adequate "sub"-constructor for a particular compression using the mapping
-    # from OPEN_METH.
-    #
-    # This concept allows one to subclass TarFile without losing the comfort of
-    # the super-constructor. A sub-constructor is registered and made available
-    # by adding it to the mapping in OPEN_METH.
-
-    @classmethod
-    def open(cls, name=None, mode="r", fileobj=None, bufsize=RECORDSIZE, **kwargs):
-        """Open a tar archive for reading, writing or appending. Return
-           an appropriate TarFile class.
-
-           mode:
-           'r' or 'r:*' open for reading with transparent compression
-           'r:'         open for reading exclusively uncompressed
-           'r:gz'       open for reading with gzip compression
-           'r:bz2'      open for reading with bzip2 compression
-           'a' or 'a:'  open for appending, creating the file if necessary
-           'w' or 'w:'  open for writing without compression
-           'w:gz'       open for writing with gzip compression
-           'w:bz2'      open for writing with bzip2 compression
-
-           'r|*'        open a stream of tar blocks with transparent compression
-           'r|'         open an uncompressed stream of tar blocks for reading
-           'r|gz'       open a gzip compressed stream of tar blocks
-           'r|bz2'      open a bzip2 compressed stream of tar blocks
-           'w|'         open an uncompressed stream for writing
-           'w|gz'       open a gzip compressed stream for writing
-           'w|bz2'      open a bzip2 compressed stream for writing
-        """
-
-        if not name and not fileobj:
-            raise ValueError("nothing to open")
-
-        if mode in ("r", "r:*"):
-            # Find out which *open() is appropriate for opening the file.
-            for comptype in cls.OPEN_METH:
-                func = getattr(cls, cls.OPEN_METH[comptype])
-                if fileobj is not None:
-                    saved_pos = fileobj.tell()
-                try:
-                    return func(name, "r", fileobj, **kwargs)
-                except (ReadError, CompressionError) as e:
-                    if fileobj is not None:
-                        fileobj.seek(saved_pos)
-                    continue
-            raise ReadError("file could not be opened successfully")
-
-        elif ":" in mode:
-            filemode, comptype = mode.split(":", 1)
-            filemode = filemode or "r"
-            comptype = comptype or "tar"
-
-            # Select the *open() function according to
-            # given compression.
-            if comptype in cls.OPEN_METH:
-                func = getattr(cls, cls.OPEN_METH[comptype])
-            else:
-                raise CompressionError("unknown compression type %r" % comptype)
-            return func(name, filemode, fileobj, **kwargs)
-
-        elif "|" in mode:
-            filemode, comptype = mode.split("|", 1)
-            filemode = filemode or "r"
-            comptype = comptype or "tar"
-
-            if filemode not in "rw":
-                raise ValueError("mode must be 'r' or 'w'")
-
-            stream = _Stream(name, filemode, comptype, fileobj, bufsize)
-            try:
-                t = cls(name, filemode, stream, **kwargs)
-            except:
-                stream.close()
-                raise
-            t._extfileobj = False
-            return t
-
-        elif mode in "aw":
-            return cls.taropen(name, mode, fileobj, **kwargs)
-
-        raise ValueError("undiscernible mode")
-
-    @classmethod
-    def taropen(cls, name, mode="r", fileobj=None, **kwargs):
-        """Open uncompressed tar archive name for reading or writing.
-        """
-        if len(mode) > 1 or mode not in "raw":
-            raise ValueError("mode must be 'r', 'a' or 'w'")
-        return cls(name, mode, fileobj, **kwargs)
-
-    @classmethod
-    def gzopen(cls, name, mode="r", fileobj=None, compresslevel=9, **kwargs):
-        """Open gzip compressed tar archive name for reading or writing.
-           Appending is not allowed.
-        """
-        if len(mode) > 1 or mode not in "rw":
-            raise ValueError("mode must be 'r' or 'w'")
-
-        try:
-            import gzip
-            gzip.GzipFile
-        except (ImportError, AttributeError):
-            raise CompressionError("gzip module is not available")
-
-        extfileobj = fileobj is not None
-        try:
-            fileobj = gzip.GzipFile(name, mode + "b", compresslevel, fileobj)
-            t = cls.taropen(name, mode, fileobj, **kwargs)
-        except IOError:
-            if not extfileobj and fileobj is not None:
-                fileobj.close()
-            if fileobj is None:
-                raise
-            raise ReadError("not a gzip file")
-        except:
-            if not extfileobj and fileobj is not None:
-                fileobj.close()
-            raise
-        t._extfileobj = extfileobj
-        return t
-
-    @classmethod
-    def bz2open(cls, name, mode="r", fileobj=None, compresslevel=9, **kwargs):
-        """Open bzip2 compressed tar archive name for reading or writing.
-           Appending is not allowed.
-        """
-        if len(mode) > 1 or mode not in "rw":
-            raise ValueError("mode must be 'r' or 'w'.")
-
-        try:
-            import bz2
-        except ImportError:
-            raise CompressionError("bz2 module is not available")
-
-        if fileobj is not None:
-            fileobj = _BZ2Proxy(fileobj, mode)
-        else:
-            fileobj = bz2.BZ2File(name, mode, compresslevel=compresslevel)
-
-        try:
-            t = cls.taropen(name, mode, fileobj, **kwargs)
-        except (IOError, EOFError):
-            fileobj.close()
-            raise ReadError("not a bzip2 file")
-        t._extfileobj = False
-        return t
-
-    # All *open() methods are registered here.
-    OPEN_METH = {
-        "tar": "taropen",   # uncompressed tar
-        "gz":  "gzopen",    # gzip compressed tar
-        "bz2": "bz2open"    # bzip2 compressed tar
-    }
-
-    #--------------------------------------------------------------------------
-    # The public methods which TarFile provides:
-
-    def close(self):
-        """Close the TarFile. In write-mode, two finishing zero blocks are
-           appended to the archive.
-        """
-        if self.closed:
-            return
-
-        if self.mode in "aw":
-            self.fileobj.write(NUL * (BLOCKSIZE * 2))
-            self.offset += (BLOCKSIZE * 2)
-            # fill up the end with zero-blocks
-            # (like option -b20 for tar does)
-            blocks, remainder = divmod(self.offset, RECORDSIZE)
-            if remainder > 0:
-                self.fileobj.write(NUL * (RECORDSIZE - remainder))
-
-        if not self._extfileobj:
-            self.fileobj.close()
-        self.closed = True
-
-    def getmember(self, name):
-        """Return a TarInfo object for member `name'. If `name' can not be
-           found in the archive, KeyError is raised. If a member occurs more
-           than once in the archive, its last occurrence is assumed to be the
-           most up-to-date version.
-        """
-        tarinfo = self._getmember(name)
-        if tarinfo is None:
-            raise KeyError("filename %r not found" % name)
-        return tarinfo
-
-    def getmembers(self):
-        """Return the members of the archive as a list of TarInfo objects. The
-           list has the same order as the members in the archive.
-        """
-        self._check()
-        if not self._loaded:    # if we want to obtain a list of
-            self._load()        # all members, we first have to
-                                # scan the whole archive.
-        return self.members
-
-    def getnames(self):
-        """Return the members of the archive as a list of their names. It has
-           the same order as the list returned by getmembers().
-        """
-        return [tarinfo.name for tarinfo in self.getmembers()]
-
-    def gettarinfo(self, name=None, arcname=None, fileobj=None):
-        """Create a TarInfo object for either the file `name' or the file
-           object `fileobj' (using os.fstat on its file descriptor). You can
-           modify some of the TarInfo's attributes before you add it using
-           addfile(). If given, `arcname' specifies an alternative name for the
-           file in the archive.
-        """
-        self._check("aw")
-
-        # When fileobj is given, replace name by
-        # fileobj's real name.
-        if fileobj is not None:
-            name = fileobj.name
-
-        # Building the name of the member in the archive.
-        # Backward slashes are converted to forward slashes,
-        # Absolute paths are turned to relative paths.
-        if arcname is None:
-            arcname = name
-        drv, arcname = os.path.splitdrive(arcname)
-        arcname = arcname.replace(os.sep, "/")
-        arcname = arcname.lstrip("/")
-
-        # Now, fill the TarInfo object with
-        # information specific for the file.
-        tarinfo = self.tarinfo()
-        tarinfo.tarfile = self
-
-        # Use os.stat or os.lstat, depending on platform
-        # and if symlinks shall be resolved.
-        if fileobj is None:
-            if hasattr(os, "lstat") and not self.dereference:
-                statres = os.lstat(name)
-            else:
-                statres = os.stat(name)
-        else:
-            statres = os.fstat(fileobj.fileno())
-        linkname = ""
-
-        stmd = statres.st_mode
-        if stat.S_ISREG(stmd):
-            inode = (statres.st_ino, statres.st_dev)
-            if not self.dereference and statres.st_nlink > 1 and \
-                    inode in self.inodes and arcname != self.inodes[inode]:
-                # Is it a hardlink to an already
-                # archived file?
-                type = LNKTYPE
-                linkname = self.inodes[inode]
-            else:
-                # The inode is added only if its valid.
-                # For win32 it is always 0.
-                type = REGTYPE
-                if inode[0]:
-                    self.inodes[inode] = arcname
-        elif stat.S_ISDIR(stmd):
-            type = DIRTYPE
-        elif stat.S_ISFIFO(stmd):
-            type = FIFOTYPE
-        elif stat.S_ISLNK(stmd):
-            type = SYMTYPE
-            linkname = os.readlink(name)
-        elif stat.S_ISCHR(stmd):
-            type = CHRTYPE
-        elif stat.S_ISBLK(stmd):
-            type = BLKTYPE
-        else:
-            return None
-
-        # Fill the TarInfo object with all
-        # information we can get.
-        tarinfo.name = arcname
-        tarinfo.mode = stmd
-        tarinfo.uid = statres.st_uid
-        tarinfo.gid = statres.st_gid
-        if type == REGTYPE:
-            tarinfo.size = statres.st_size
-        else:
-            tarinfo.size = 0
-        tarinfo.mtime = statres.st_mtime
-        tarinfo.type = type
-        tarinfo.linkname = linkname
-        if pwd:
-            try:
-                tarinfo.uname = pwd.getpwuid(tarinfo.uid)[0]
-            except KeyError:
-                pass
-        if grp:
-            try:
-                tarinfo.gname = grp.getgrgid(tarinfo.gid)[0]
-            except KeyError:
-                pass
-
-        if type in (CHRTYPE, BLKTYPE):
-            if hasattr(os, "major") and hasattr(os, "minor"):
-                tarinfo.devmajor = os.major(statres.st_rdev)
-                tarinfo.devminor = os.minor(statres.st_rdev)
-        return tarinfo
-
-    def list(self, verbose=True):
-        """Print a table of contents to sys.stdout. If `verbose' is False, only
-           the names of the members are printed. If it is True, an `ls -l'-like
-           output is produced.
-        """
-        self._check()
-
-        for tarinfo in self:
-            if verbose:
-                print(filemode(tarinfo.mode), end=' ')
-                print("%s/%s" % (tarinfo.uname or tarinfo.uid,
-                                 tarinfo.gname or tarinfo.gid), end=' ')
-                if tarinfo.ischr() or tarinfo.isblk():
-                    print("%10s" % ("%d,%d" \
-                                    % (tarinfo.devmajor, tarinfo.devminor)), end=' ')
-                else:
-                    print("%10d" % tarinfo.size, end=' ')
-                print("%d-%02d-%02d %02d:%02d:%02d" \
-                      % time.localtime(tarinfo.mtime)[:6], end=' ')
-
-            print(tarinfo.name + ("/" if tarinfo.isdir() else ""), end=' ')
-
-            if verbose:
-                if tarinfo.issym():
-                    print("->", tarinfo.linkname, end=' ')
-                if tarinfo.islnk():
-                    print("link to", tarinfo.linkname, end=' ')
-            print()
-
-    def add(self, name, arcname=None, recursive=True, exclude=None, filter=None):
-        """Add the file `name' to the archive. `name' may be any type of file
-           (directory, fifo, symbolic link, etc.). If given, `arcname'
-           specifies an alternative name for the file in the archive.
-           Directories are added recursively by default. This can be avoided by
-           setting `recursive' to False. `exclude' is a function that should
-           return True for each filename to be excluded. `filter' is a function
-           that expects a TarInfo object argument and returns the changed
-           TarInfo object, if it returns None the TarInfo object will be
-           excluded from the archive.
-        """
-        self._check("aw")
-
-        if arcname is None:
-            arcname = name
-
-        # Exclude pathnames.
-        if exclude is not None:
-            import warnings
-            warnings.warn("use the filter argument instead",
-                    DeprecationWarning, 2)
-            if exclude(name):
-                self._dbg(2, "tarfile: Excluded %r" % name)
-                return
-
-        # Skip if somebody tries to archive the archive...
-        if self.name is not None and os.path.abspath(name) == self.name:
-            self._dbg(2, "tarfile: Skipped %r" % name)
-            return
-
-        self._dbg(1, name)
-
-        # Create a TarInfo object from the file.
-        tarinfo = self.gettarinfo(name, arcname)
-
-        if tarinfo is None:
-            self._dbg(1, "tarfile: Unsupported type %r" % name)
-            return
-
-        # Change or exclude the TarInfo object.
-        if filter is not None:
-            tarinfo = filter(tarinfo)
-            if tarinfo is None:
-                self._dbg(2, "tarfile: Excluded %r" % name)
-                return
-
-        # Append the tar header and data to the archive.
-        if tarinfo.isreg():
-            f = bltn_open(name, "rb")
-            self.addfile(tarinfo, f)
-            f.close()
-
-        elif tarinfo.isdir():
-            self.addfile(tarinfo)
-            if recursive:
-                for f in os.listdir(name):
-                    self.add(os.path.join(name, f), os.path.join(arcname, f),
-                            recursive, exclude, filter=filter)
-
-        else:
-            self.addfile(tarinfo)
-
-    def addfile(self, tarinfo, fileobj=None):
-        """Add the TarInfo object `tarinfo' to the archive. If `fileobj' is
-           given, tarinfo.size bytes are read from it and added to the archive.
-           You can create TarInfo objects using gettarinfo().
-           On Windows platforms, `fileobj' should always be opened with mode
-           'rb' to avoid irritation about the file size.
-        """
-        self._check("aw")
-
-        tarinfo = copy.copy(tarinfo)
-
-        buf = tarinfo.tobuf(self.format, self.encoding, self.errors)
-        self.fileobj.write(buf)
-        self.offset += len(buf)
-
-        # If there's data to follow, append it.
-        if fileobj is not None:
-            copyfileobj(fileobj, self.fileobj, tarinfo.size)
-            blocks, remainder = divmod(tarinfo.size, BLOCKSIZE)
-            if remainder > 0:
-                self.fileobj.write(NUL * (BLOCKSIZE - remainder))
-                blocks += 1
-            self.offset += blocks * BLOCKSIZE
-
-        self.members.append(tarinfo)
-
-    def extractall(self, path=".", members=None):
-        """Extract all members from the archive to the current working
-           directory and set owner, modification time and permissions on
-           directories afterwards. `path' specifies a different directory
-           to extract to. `members' is optional and must be a subset of the
-           list returned by getmembers().
-        """
-        directories = []
-
-        if members is None:
-            members = self
-
-        for tarinfo in members:
-            if tarinfo.isdir():
-                # Extract directories with a safe mode.
-                directories.append(tarinfo)
-                tarinfo = copy.copy(tarinfo)
-                tarinfo.mode = 0o700
-            # Do not set_attrs directories, as we will do that further down
-            self.extract(tarinfo, path, set_attrs=not tarinfo.isdir())
-
-        # Reverse sort directories.
-        directories.sort(key=lambda a: a.name)
-        directories.reverse()
-
-        # Set correct owner, mtime and filemode on directories.
-        for tarinfo in directories:
-            dirpath = os.path.join(path, tarinfo.name)
-            try:
-                self.chown(tarinfo, dirpath)
-                self.utime(tarinfo, dirpath)
-                self.chmod(tarinfo, dirpath)
-            except ExtractError as e:
-                if self.errorlevel > 1:
-                    raise
-                else:
-                    self._dbg(1, "tarfile: %s" % e)
-
-    def extract(self, member, path="", set_attrs=True):
-        """Extract a member from the archive to the current working directory,
-           using its full name. Its file information is extracted as accurately
-           as possible. `member' may be a filename or a TarInfo object. You can
-           specify a different directory using `path'. File attributes (owner,
-           mtime, mode) are set unless `set_attrs' is False.
-        """
-        self._check("r")
-
-        if isinstance(member, str):
-            tarinfo = self.getmember(member)
-        else:
-            tarinfo = member
-
-        # Prepare the link target for makelink().
-        if tarinfo.islnk():
-            tarinfo._link_target = os.path.join(path, tarinfo.linkname)
-
-        try:
-            self._extract_member(tarinfo, os.path.join(path, tarinfo.name),
-                                 set_attrs=set_attrs)
-        except EnvironmentError as e:
-            if self.errorlevel > 0:
-                raise
-            else:
-                if e.filename is None:
-                    self._dbg(1, "tarfile: %s" % e.strerror)
-                else:
-                    self._dbg(1, "tarfile: %s %r" % (e.strerror, e.filename))
-        except ExtractError as e:
-            if self.errorlevel > 1:
-                raise
-            else:
-                self._dbg(1, "tarfile: %s" % e)
-
-    def extractfile(self, member):
-        """Extract a member from the archive as a file object. `member' may be
-           a filename or a TarInfo object. If `member' is a regular file, a
-           file-like object is returned. If `member' is a link, a file-like
-           object is constructed from the link's target. If `member' is none of
-           the above, None is returned.
-           The file-like object is read-only and provides the following
-           methods: read(), readline(), readlines(), seek() and tell()
-        """
-        self._check("r")
-
-        if isinstance(member, str):
-            tarinfo = self.getmember(member)
-        else:
-            tarinfo = member
-
-        if tarinfo.isreg():
-            return self.fileobject(self, tarinfo)
-
-        elif tarinfo.type not in SUPPORTED_TYPES:
-            # If a member's type is unknown, it is treated as a
-            # regular file.
-            return self.fileobject(self, tarinfo)
-
-        elif tarinfo.islnk() or tarinfo.issym():
-            if isinstance(self.fileobj, _Stream):
-                # A small but ugly workaround for the case that someone tries
-                # to extract a (sym)link as a file-object from a non-seekable
-                # stream of tar blocks.
-                raise StreamError("cannot extract (sym)link as file object")
-            else:
-                # A (sym)link's file object is its target's file object.
-                return self.extractfile(self._find_link_target(tarinfo))
-        else:
-            # If there's no data associated with the member (directory, chrdev,
-            # blkdev, etc.), return None instead of a file object.
-            return None
-
-    def _extract_member(self, tarinfo, targetpath, set_attrs=True):
-        """Extract the TarInfo object tarinfo to a physical
-           file called targetpath.
-        """
-        # Fetch the TarInfo object for the given name
-        # and build the destination pathname, replacing
-        # forward slashes to platform specific separators.
-        targetpath = targetpath.rstrip("/")
-        targetpath = targetpath.replace("/", os.sep)
-
-        # Create all upper directories.
-        upperdirs = os.path.dirname(targetpath)
-        if upperdirs and not os.path.exists(upperdirs):
-            # Create directories that are not part of the archive with
-            # default permissions.
-            os.makedirs(upperdirs)
-
-        if tarinfo.islnk() or tarinfo.issym():
-            self._dbg(1, "%s -> %s" % (tarinfo.name, tarinfo.linkname))
-        else:
-            self._dbg(1, tarinfo.name)
-
-        if tarinfo.isreg():
-            self.makefile(tarinfo, targetpath)
-        elif tarinfo.isdir():
-            self.makedir(tarinfo, targetpath)
-        elif tarinfo.isfifo():
-            self.makefifo(tarinfo, targetpath)
-        elif tarinfo.ischr() or tarinfo.isblk():
-            self.makedev(tarinfo, targetpath)
-        elif tarinfo.islnk() or tarinfo.issym():
-            self.makelink(tarinfo, targetpath)
-        elif tarinfo.type not in SUPPORTED_TYPES:
-            self.makeunknown(tarinfo, targetpath)
-        else:
-            self.makefile(tarinfo, targetpath)
-
-        if set_attrs:
-            self.chown(tarinfo, targetpath)
-            if not tarinfo.issym():
-                self.chmod(tarinfo, targetpath)
-                self.utime(tarinfo, targetpath)
-
-    #--------------------------------------------------------------------------
-    # Below are the different file methods. They are called via
-    # _extract_member() when extract() is called. They can be replaced in a
-    # subclass to implement other functionality.
-
-    def makedir(self, tarinfo, targetpath):
-        """Make a directory called targetpath.
-        """
-        try:
-            # Use a safe mode for the directory, the real mode is set
-            # later in _extract_member().
-            os.mkdir(targetpath, 0o700)
-        except EnvironmentError as e:
-            if e.errno != errno.EEXIST:
-                raise
-
-    def makefile(self, tarinfo, targetpath):
-        """Make a file called targetpath.
-        """
-        source = self.fileobj
-        source.seek(tarinfo.offset_data)
-        target = bltn_open(targetpath, "wb")
-        if tarinfo.sparse is not None:
-            for offset, size in tarinfo.sparse:
-                target.seek(offset)
-                copyfileobj(source, target, size)
-        else:
-            copyfileobj(source, target, tarinfo.size)
-        target.seek(tarinfo.size)
-        target.truncate()
-        target.close()
-
-    def makeunknown(self, tarinfo, targetpath):
-        """Make a file from a TarInfo object with an unknown type
-           at targetpath.
-        """
-        self.makefile(tarinfo, targetpath)
-        self._dbg(1, "tarfile: Unknown file type %r, " \
-                     "extracted as regular file." % tarinfo.type)
-
-    def makefifo(self, tarinfo, targetpath):
-        """Make a fifo called targetpath.
-        """
-        if hasattr(os, "mkfifo"):
-            os.mkfifo(targetpath)
-        else:
-            raise ExtractError("fifo not supported by system")
-
-    def makedev(self, tarinfo, targetpath):
-        """Make a character or block device called targetpath.
-        """
-        if not hasattr(os, "mknod") or not hasattr(os, "makedev"):
-            raise ExtractError("special devices not supported by system")
-
-        mode = tarinfo.mode
-        if tarinfo.isblk():
-            mode |= stat.S_IFBLK
-        else:
-            mode |= stat.S_IFCHR
-
-        os.mknod(targetpath, mode,
-                 os.makedev(tarinfo.devmajor, tarinfo.devminor))
-
-    def makelink(self, tarinfo, targetpath):
-        """Make a (symbolic) link called targetpath. If it cannot be created
-          (platform limitation), we try to make a copy of the referenced file
-          instead of a link.
-        """
-        try:
-            # For systems that support symbolic and hard links.
-            if tarinfo.issym():
-                os.symlink(tarinfo.linkname, targetpath)
-            else:
-                # See extract().
-                if os.path.exists(tarinfo._link_target):
-                    os.link(tarinfo._link_target, targetpath)
-                else:
-                    self._extract_member(self._find_link_target(tarinfo),
-                                         targetpath)
-        except symlink_exception:
-            if tarinfo.issym():
-                linkpath = os.path.join(os.path.dirname(tarinfo.name),
-                                        tarinfo.linkname)
-            else:
-                linkpath = tarinfo.linkname
-        else:
-            try:
-                self._extract_member(self._find_link_target(tarinfo),
-                                     targetpath)
-            except KeyError:
-                raise ExtractError("unable to resolve link inside archive")
-
-    def chown(self, tarinfo, targetpath):
-        """Set owner of targetpath according to tarinfo.
-        """
-        if pwd and hasattr(os, "geteuid") and os.geteuid() == 0:
-            # We have to be root to do so.
-            try:
-                g = grp.getgrnam(tarinfo.gname)[2]
-            except KeyError:
-                g = tarinfo.gid
-            try:
-                u = pwd.getpwnam(tarinfo.uname)[2]
-            except KeyError:
-                u = tarinfo.uid
-            try:
-                if tarinfo.issym() and hasattr(os, "lchown"):
-                    os.lchown(targetpath, u, g)
-                else:
-                    if sys.platform != "os2emx":
-                        os.chown(targetpath, u, g)
-            except EnvironmentError as e:
-                raise ExtractError("could not change owner")
-
-    def chmod(self, tarinfo, targetpath):
-        """Set file permissions of targetpath according to tarinfo.
-        """
-        if hasattr(os, 'chmod'):
-            try:
-                os.chmod(targetpath, tarinfo.mode)
-            except EnvironmentError as e:
-                raise ExtractError("could not change mode")
-
-    def utime(self, tarinfo, targetpath):
-        """Set modification time of targetpath according to tarinfo.
-        """
-        if not hasattr(os, 'utime'):
-            return
-        try:
-            os.utime(targetpath, (tarinfo.mtime, tarinfo.mtime))
-        except EnvironmentError as e:
-            raise ExtractError("could not change modification time")
-
-    #--------------------------------------------------------------------------
-    def next(self):
-        """Return the next member of the archive as a TarInfo object, when
-           TarFile is opened for reading. Return None if there is no more
-           available.
-        """
-        self._check("ra")
-        if self.firstmember is not None:
-            m = self.firstmember
-            self.firstmember = None
-            return m
-
-        # Read the next block.
-        self.fileobj.seek(self.offset)
-        tarinfo = None
-        while True:
-            try:
-                tarinfo = self.tarinfo.fromtarfile(self)
-            except EOFHeaderError as e:
-                if self.ignore_zeros:
-                    self._dbg(2, "0x%X: %s" % (self.offset, e))
-                    self.offset += BLOCKSIZE
-                    continue
-            except InvalidHeaderError as e:
-                if self.ignore_zeros:
-                    self._dbg(2, "0x%X: %s" % (self.offset, e))
-                    self.offset += BLOCKSIZE
-                    continue
-                elif self.offset == 0:
-                    raise ReadError(str(e))
-            except EmptyHeaderError:
-                if self.offset == 0:
-                    raise ReadError("empty file")
-            except TruncatedHeaderError as e:
-                if self.offset == 0:
-                    raise ReadError(str(e))
-            except SubsequentHeaderError as e:
-                raise ReadError(str(e))
-            break
-
-        if tarinfo is not None:
-            self.members.append(tarinfo)
-        else:
-            self._loaded = True
-
-        return tarinfo
-
-    #--------------------------------------------------------------------------
-    # Little helper methods:
-
-    def _getmember(self, name, tarinfo=None, normalize=False):
-        """Find an archive member by name from bottom to top.
-           If tarinfo is given, it is used as the starting point.
-        """
-        # Ensure that all members have been loaded.
-        members = self.getmembers()
-
-        # Limit the member search list up to tarinfo.
-        if tarinfo is not None:
-            members = members[:members.index(tarinfo)]
-
-        if normalize:
-            name = os.path.normpath(name)
-
-        for member in reversed(members):
-            if normalize:
-                member_name = os.path.normpath(member.name)
-            else:
-                member_name = member.name
-
-            if name == member_name:
-                return member
-
-    def _load(self):
-        """Read through the entire archive file and look for readable
-           members.
-        """
-        while True:
-            tarinfo = self.next()
-            if tarinfo is None:
-                break
-        self._loaded = True
-
-    def _check(self, mode=None):
-        """Check if TarFile is still open, and if the operation's mode
-           corresponds to TarFile's mode.
-        """
-        if self.closed:
-            raise IOError("%s is closed" % self.__class__.__name__)
-        if mode is not None and self.mode not in mode:
-            raise IOError("bad operation for mode %r" % self.mode)
-
-    def _find_link_target(self, tarinfo):
-        """Find the target member of a symlink or hardlink member in the
-           archive.
-        """
-        if tarinfo.issym():
-            # Always search the entire archive.
-            linkname = os.path.dirname(tarinfo.name) + "/" + tarinfo.linkname
-            limit = None
-        else:
-            # Search the archive before the link, because a hard link is
-            # just a reference to an already archived file.
-            linkname = tarinfo.linkname
-            limit = tarinfo
-
-        member = self._getmember(linkname, tarinfo=limit, normalize=True)
-        if member is None:
-            raise KeyError("linkname %r not found" % linkname)
-        return member
-
-    def __iter__(self):
-        """Provide an iterator object.
-        """
-        if self._loaded:
-            return iter(self.members)
-        else:
-            return TarIter(self)
-
-    def _dbg(self, level, msg):
-        """Write debugging output to sys.stderr.
-        """
-        if level <= self.debug:
-            print(msg, file=sys.stderr)
-
-    def __enter__(self):
-        self._check()
-        return self
-
-    def __exit__(self, type, value, traceback):
-        if type is None:
-            self.close()
-        else:
-            # An exception occurred. We must not call close() because
-            # it would try to write end-of-archive blocks and padding.
-            if not self._extfileobj:
-                self.fileobj.close()
-            self.closed = True
-# class TarFile
-
-class TarIter(object):
-    """Iterator Class.
-
-       for tarinfo in TarFile(...):
-           suite...
-    """
-
-    def __init__(self, tarfile):
-        """Construct a TarIter object.
-        """
-        self.tarfile = tarfile
-        self.index = 0
-    def __iter__(self):
-        """Return iterator object.
-        """
-        return self
-
-    def __next__(self):
-        """Return the next item using TarFile's next() method.
-           When all members have been read, set TarFile as _loaded.
-        """
-        # Fix for SF #1100429: Under rare circumstances it can
-        # happen that getmembers() is called during iteration,
-        # which will cause TarIter to stop prematurely.
-        if not self.tarfile._loaded:
-            tarinfo = self.tarfile.next()
-            if not tarinfo:
-                self.tarfile._loaded = True
-                raise StopIteration
-        else:
-            try:
-                tarinfo = self.tarfile.members[self.index]
-            except IndexError:
-                raise StopIteration
-        self.index += 1
-        return tarinfo
-
-    next = __next__ # for Python 2.x
-
-#--------------------
-# exported functions
-#--------------------
-def is_tarfile(name):
-    """Return True if name points to a tar archive that we
-       are able to handle, else return False.
-    """
-    try:
-        t = open(name)
-        t.close()
-        return True
-    except TarError:
-        return False
-
-bltn_open = open
-open = TarFile.open
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/compat.py
deleted file mode 100644
index ff328c8..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/compat.py
+++ /dev/null
@@ -1,1120 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2013-2017 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-from __future__ import absolute_import
-
-import os
-import re
-import sys
-
-try:
-    import ssl
-except ImportError:  # pragma: no cover
-    ssl = None
-
-if sys.version_info[0] < 3:  # pragma: no cover
-    from StringIO import StringIO
-    string_types = basestring,
-    text_type = unicode
-    from types import FileType as file_type
-    import __builtin__ as builtins
-    import ConfigParser as configparser
-    from ._backport import shutil
-    from urlparse import urlparse, urlunparse, urljoin, urlsplit, urlunsplit
-    from urllib import (urlretrieve, quote as _quote, unquote, url2pathname,
-                        pathname2url, ContentTooShortError, splittype)
-
-    def quote(s):
-        if isinstance(s, unicode):
-            s = s.encode('utf-8')
-        return _quote(s)
-
-    import urllib2
-    from urllib2 import (Request, urlopen, URLError, HTTPError,
-                         HTTPBasicAuthHandler, HTTPPasswordMgr,
-                         HTTPHandler, HTTPRedirectHandler,
-                         build_opener)
-    if ssl:
-        from urllib2 import HTTPSHandler
-    import httplib
-    import xmlrpclib
-    import Queue as queue
-    from HTMLParser import HTMLParser
-    import htmlentitydefs
-    raw_input = raw_input
-    from itertools import ifilter as filter
-    from itertools import ifilterfalse as filterfalse
-
-    _userprog = None
-    def splituser(host):
-        """splituser('user[:passwd]@host[:port]') --> 'user[:passwd]', 'host[:port]'."""
-        global _userprog
-        if _userprog is None:
-            import re
-            _userprog = re.compile('^(.*)@(.*)$')
-
-        match = _userprog.match(host)
-        if match: return match.group(1, 2)
-        return None, host
-
-else:  # pragma: no cover
-    from io import StringIO
-    string_types = str,
-    text_type = str
-    from io import TextIOWrapper as file_type
-    import builtins
-    import configparser
-    import shutil
-    from urllib.parse import (urlparse, urlunparse, urljoin, splituser, quote,
-                              unquote, urlsplit, urlunsplit, splittype)
-    from urllib.request import (urlopen, urlretrieve, Request, url2pathname,
-                                pathname2url,
-                                HTTPBasicAuthHandler, HTTPPasswordMgr,
-                                HTTPHandler, HTTPRedirectHandler,
-                                build_opener)
-    if ssl:
-        from urllib.request import HTTPSHandler
-    from urllib.error import HTTPError, URLError, ContentTooShortError
-    import http.client as httplib
-    import urllib.request as urllib2
-    import xmlrpc.client as xmlrpclib
-    import queue
-    from html.parser import HTMLParser
-    import html.entities as htmlentitydefs
-    raw_input = input
-    from itertools import filterfalse
-    filter = filter
-
-try:
-    from ssl import match_hostname, CertificateError
-except ImportError: # pragma: no cover
-    class CertificateError(ValueError):
-        pass
-
-
-    def _dnsname_match(dn, hostname, max_wildcards=1):
-        """Matching according to RFC 6125, section 6.4.3
-
-        http://tools.ietf.org/html/rfc6125#section-6.4.3
-        """
-        pats = []
-        if not dn:
-            return False
-
-        parts = dn.split('.')
-        leftmost, remainder = parts[0], parts[1:]
-
-        wildcards = leftmost.count('*')
-        if wildcards > max_wildcards:
-            # Issue #17980: avoid denials of service by refusing more
-            # than one wildcard per fragment.  A survey of established
-            # policy among SSL implementations showed it to be a
-            # reasonable choice.
-            raise CertificateError(
-                "too many wildcards in certificate DNS name: " + repr(dn))
-
-        # speed up common case w/o wildcards
-        if not wildcards:
-            return dn.lower() == hostname.lower()
-
-        # RFC 6125, section 6.4.3, subitem 1.
-        # The client SHOULD NOT attempt to match a presented identifier in which
-        # the wildcard character comprises a label other than the left-most label.
-        if leftmost == '*':
-            # When '*' is a fragment by itself, it matches a non-empty dotless
-            # fragment.
-            pats.append('[^.]+')
-        elif leftmost.startswith('xn--') or hostname.startswith('xn--'):
-            # RFC 6125, section 6.4.3, subitem 3.
-            # The client SHOULD NOT attempt to match a presented identifier
-            # where the wildcard character is embedded within an A-label or
-            # U-label of an internationalized domain name.
-            pats.append(re.escape(leftmost))
-        else:
-            # Otherwise, '*' matches any dotless string, e.g. www*
-            pats.append(re.escape(leftmost).replace(r'\*', '[^.]*'))
-
-        # add the remaining fragments, ignore any wildcards
-        for frag in remainder:
-            pats.append(re.escape(frag))
-
-        pat = re.compile(r'\A' + r'\.'.join(pats) + r'\Z', re.IGNORECASE)
-        return pat.match(hostname)
-
-
-    def match_hostname(cert, hostname):
-        """Verify that *cert* (in decoded format as returned by
-        SSLSocket.getpeercert()) matches the *hostname*.  RFC 2818 and RFC 6125
-        rules are followed, but IP addresses are not accepted for *hostname*.
-
-        CertificateError is raised on failure. On success, the function
-        returns nothing.
-        """
-        if not cert:
-            raise ValueError("empty or no certificate, match_hostname needs a "
-                             "SSL socket or SSL context with either "
-                             "CERT_OPTIONAL or CERT_REQUIRED")
-        dnsnames = []
-        san = cert.get('subjectAltName', ())
-        for key, value in san:
-            if key == 'DNS':
-                if _dnsname_match(value, hostname):
-                    return
-                dnsnames.append(value)
-        if not dnsnames:
-            # The subject is only checked when there is no dNSName entry
-            # in subjectAltName
-            for sub in cert.get('subject', ()):
-                for key, value in sub:
-                    # XXX according to RFC 2818, the most specific Common Name
-                    # must be used.
-                    if key == 'commonName':
-                        if _dnsname_match(value, hostname):
-                            return
-                        dnsnames.append(value)
-        if len(dnsnames) > 1:
-            raise CertificateError("hostname %r "
-                "doesn't match either of %s"
-                % (hostname, ', '.join(map(repr, dnsnames))))
-        elif len(dnsnames) == 1:
-            raise CertificateError("hostname %r "
-                "doesn't match %r"
-                % (hostname, dnsnames[0]))
-        else:
-            raise CertificateError("no appropriate commonName or "
-                "subjectAltName fields were found")
-
-
-try:
-    from types import SimpleNamespace as Container
-except ImportError:  # pragma: no cover
-    class Container(object):
-        """
-        A generic container for when multiple values need to be returned
-        """
-        def __init__(self, **kwargs):
-            self.__dict__.update(kwargs)
-
-
-try:
-    from shutil import which
-except ImportError:  # pragma: no cover
-    # Implementation from Python 3.3
-    def which(cmd, mode=os.F_OK | os.X_OK, path=None):
-        """Given a command, mode, and a PATH string, return the path which
-        conforms to the given mode on the PATH, or None if there is no such
-        file.
-
-        `mode` defaults to os.F_OK | os.X_OK. `path` defaults to the result
-        of os.environ.get("PATH"), or can be overridden with a custom search
-        path.
-
-        """
-        # Check that a given file can be accessed with the correct mode.
-        # Additionally check that `file` is not a directory, as on Windows
-        # directories pass the os.access check.
-        def _access_check(fn, mode):
-            return (os.path.exists(fn) and os.access(fn, mode)
-                    and not os.path.isdir(fn))
-
-        # If we're given a path with a directory part, look it up directly rather
-        # than referring to PATH directories. This includes checking relative to the
-        # current directory, e.g. ./script
-        if os.path.dirname(cmd):
-            if _access_check(cmd, mode):
-                return cmd
-            return None
-
-        if path is None:
-            path = os.environ.get("PATH", os.defpath)
-        if not path:
-            return None
-        path = path.split(os.pathsep)
-
-        if sys.platform == "win32":
-            # The current directory takes precedence on Windows.
-            if not os.curdir in path:
-                path.insert(0, os.curdir)
-
-            # PATHEXT is necessary to check on Windows.
-            pathext = os.environ.get("PATHEXT", "").split(os.pathsep)
-            # See if the given file matches any of the expected path extensions.
-            # This will allow us to short circuit when given "python.exe".
-            # If it does match, only test that one, otherwise we have to try
-            # others.
-            if any(cmd.lower().endswith(ext.lower()) for ext in pathext):
-                files = [cmd]
-            else:
-                files = [cmd + ext for ext in pathext]
-        else:
-            # On other platforms you don't have things like PATHEXT to tell you
-            # what file suffixes are executable, so just pass on cmd as-is.
-            files = [cmd]
-
-        seen = set()
-        for dir in path:
-            normdir = os.path.normcase(dir)
-            if not normdir in seen:
-                seen.add(normdir)
-                for thefile in files:
-                    name = os.path.join(dir, thefile)
-                    if _access_check(name, mode):
-                        return name
-        return None
-
-
-# ZipFile is a context manager in 2.7, but not in 2.6
-
-from zipfile import ZipFile as BaseZipFile
-
-if hasattr(BaseZipFile, '__enter__'):  # pragma: no cover
-    ZipFile = BaseZipFile
-else:  # pragma: no cover
-    from zipfile import ZipExtFile as BaseZipExtFile
-
-    class ZipExtFile(BaseZipExtFile):
-        def __init__(self, base):
-            self.__dict__.update(base.__dict__)
-
-        def __enter__(self):
-            return self
-
-        def __exit__(self, *exc_info):
-            self.close()
-            # return None, so if an exception occurred, it will propagate
-
-    class ZipFile(BaseZipFile):
-        def __enter__(self):
-            return self
-
-        def __exit__(self, *exc_info):
-            self.close()
-            # return None, so if an exception occurred, it will propagate
-
-        def open(self, *args, **kwargs):
-            base = BaseZipFile.open(self, *args, **kwargs)
-            return ZipExtFile(base)
-
-try:
-    from platform import python_implementation
-except ImportError: # pragma: no cover
-    def python_implementation():
-        """Return a string identifying the Python implementation."""
-        if 'PyPy' in sys.version:
-            return 'PyPy'
-        if os.name == 'java':
-            return 'Jython'
-        if sys.version.startswith('IronPython'):
-            return 'IronPython'
-        return 'CPython'
-
-try:
-    import sysconfig
-except ImportError: # pragma: no cover
-    from ._backport import sysconfig
-
-try:
-    callable = callable
-except NameError:   # pragma: no cover
-    from collections import Callable
-
-    def callable(obj):
-        return isinstance(obj, Callable)
-
-
-try:
-    fsencode = os.fsencode
-    fsdecode = os.fsdecode
-except AttributeError:  # pragma: no cover
-    # Issue #99: on some systems (e.g. containerised),
-    # sys.getfilesystemencoding() returns None, and we need a real value,
-    # so fall back to utf-8. From the CPython 2.7 docs relating to Unix and
-    # sys.getfilesystemencoding(): the return value is "the user’s preference
-    # according to the result of nl_langinfo(CODESET), or None if the
-    # nl_langinfo(CODESET) failed."
-    _fsencoding = sys.getfilesystemencoding() or 'utf-8'
-    if _fsencoding == 'mbcs':
-        _fserrors = 'strict'
-    else:
-        _fserrors = 'surrogateescape'
-
-    def fsencode(filename):
-        if isinstance(filename, bytes):
-            return filename
-        elif isinstance(filename, text_type):
-            return filename.encode(_fsencoding, _fserrors)
-        else:
-            raise TypeError("expect bytes or str, not %s" %
-                            type(filename).__name__)
-
-    def fsdecode(filename):
-        if isinstance(filename, text_type):
-            return filename
-        elif isinstance(filename, bytes):
-            return filename.decode(_fsencoding, _fserrors)
-        else:
-            raise TypeError("expect bytes or str, not %s" %
-                            type(filename).__name__)
-
-try:
-    from tokenize import detect_encoding
-except ImportError: # pragma: no cover
-    from codecs import BOM_UTF8, lookup
-    import re
-
-    cookie_re = re.compile(r"coding[:=]\s*([-\w.]+)")
-
-    def _get_normal_name(orig_enc):
-        """Imitates get_normal_name in tokenizer.c."""
-        # Only care about the first 12 characters.
-        enc = orig_enc[:12].lower().replace("_", "-")
-        if enc == "utf-8" or enc.startswith("utf-8-"):
-            return "utf-8"
-        if enc in ("latin-1", "iso-8859-1", "iso-latin-1") or \
-           enc.startswith(("latin-1-", "iso-8859-1-", "iso-latin-1-")):
-            return "iso-8859-1"
-        return orig_enc
-
-    def detect_encoding(readline):
-        """
-        The detect_encoding() function is used to detect the encoding that should
-        be used to decode a Python source file.  It requires one argument, readline,
-        in the same way as the tokenize() generator.
-
-        It will call readline a maximum of twice, and return the encoding used
-        (as a string) and a list of any lines (left as bytes) it has read in.
-
-        It detects the encoding from the presence of a utf-8 bom or an encoding
-        cookie as specified in pep-0263.  If both a bom and a cookie are present,
-        but disagree, a SyntaxError will be raised.  If the encoding cookie is an
-        invalid charset, raise a SyntaxError.  Note that if a utf-8 bom is found,
-        'utf-8-sig' is returned.
-
-        If no encoding is specified, then the default of 'utf-8' will be returned.
-        """
-        try:
-            filename = readline.__self__.name
-        except AttributeError:
-            filename = None
-        bom_found = False
-        encoding = None
-        default = 'utf-8'
-        def read_or_stop():
-            try:
-                return readline()
-            except StopIteration:
-                return b''
-
-        def find_cookie(line):
-            try:
-                # Decode as UTF-8. Either the line is an encoding declaration,
-                # in which case it should be pure ASCII, or it must be UTF-8
-                # per default encoding.
-                line_string = line.decode('utf-8')
-            except UnicodeDecodeError:
-                msg = "invalid or missing encoding declaration"
-                if filename is not None:
-                    msg = '{} for {!r}'.format(msg, filename)
-                raise SyntaxError(msg)
-
-            matches = cookie_re.findall(line_string)
-            if not matches:
-                return None
-            encoding = _get_normal_name(matches[0])
-            try:
-                codec = lookup(encoding)
-            except LookupError:
-                # This behaviour mimics the Python interpreter
-                if filename is None:
-                    msg = "unknown encoding: " + encoding
-                else:
-                    msg = "unknown encoding for {!r}: {}".format(filename,
-                            encoding)
-                raise SyntaxError(msg)
-
-            if bom_found:
-                if codec.name != 'utf-8':
-                    # This behaviour mimics the Python interpreter
-                    if filename is None:
-                        msg = 'encoding problem: utf-8'
-                    else:
-                        msg = 'encoding problem for {!r}: utf-8'.format(filename)
-                    raise SyntaxError(msg)
-                encoding += '-sig'
-            return encoding
-
-        first = read_or_stop()
-        if first.startswith(BOM_UTF8):
-            bom_found = True
-            first = first[3:]
-            default = 'utf-8-sig'
-        if not first:
-            return default, []
-
-        encoding = find_cookie(first)
-        if encoding:
-            return encoding, [first]
-
-        second = read_or_stop()
-        if not second:
-            return default, [first]
-
-        encoding = find_cookie(second)
-        if encoding:
-            return encoding, [first, second]
-
-        return default, [first, second]
-
-# For converting & <-> &amp; etc.
-try:
-    from html import escape
-except ImportError:
-    from cgi import escape
-if sys.version_info[:2] < (3, 4):
-    unescape = HTMLParser().unescape
-else:
-    from html import unescape
-
-try:
-    from collections import ChainMap
-except ImportError: # pragma: no cover
-    from collections import MutableMapping
-
-    try:
-        from reprlib import recursive_repr as _recursive_repr
-    except ImportError:
-        def _recursive_repr(fillvalue='...'):
-            '''
-            Decorator to make a repr function return fillvalue for a recursive
-            call
-            '''
-
-            def decorating_function(user_function):
-                repr_running = set()
-
-                def wrapper(self):
-                    key = id(self), get_ident()
-                    if key in repr_running:
-                        return fillvalue
-                    repr_running.add(key)
-                    try:
-                        result = user_function(self)
-                    finally:
-                        repr_running.discard(key)
-                    return result
-
-                # Can't use functools.wraps() here because of bootstrap issues
-                wrapper.__module__ = getattr(user_function, '__module__')
-                wrapper.__doc__ = getattr(user_function, '__doc__')
-                wrapper.__name__ = getattr(user_function, '__name__')
-                wrapper.__annotations__ = getattr(user_function, '__annotations__', {})
-                return wrapper
-
-            return decorating_function
-
-    class ChainMap(MutableMapping):
-        ''' A ChainMap groups multiple dicts (or other mappings) together
-        to create a single, updateable view.
-
-        The underlying mappings are stored in a list.  That list is public and can
-        accessed or updated using the *maps* attribute.  There is no other state.
-
-        Lookups search the underlying mappings successively until a key is found.
-        In contrast, writes, updates, and deletions only operate on the first
-        mapping.
-
-        '''
-
-        def __init__(self, *maps):
-            '''Initialize a ChainMap by setting *maps* to the given mappings.
-            If no mappings are provided, a single empty dictionary is used.
-
-            '''
-            self.maps = list(maps) or [{}]          # always at least one map
-
-        def __missing__(self, key):
-            raise KeyError(key)
-
-        def __getitem__(self, key):
-            for mapping in self.maps:
-                try:
-                    return mapping[key]             # can't use 'key in mapping' with defaultdict
-                except KeyError:
-                    pass
-            return self.__missing__(key)            # support subclasses that define __missing__
-
-        def get(self, key, default=None):
-            return self[key] if key in self else default
-
-        def __len__(self):
-            return len(set().union(*self.maps))     # reuses stored hash values if possible
-
-        def __iter__(self):
-            return iter(set().union(*self.maps))
-
-        def __contains__(self, key):
-            return any(key in m for m in self.maps)
-
-        def __bool__(self):
-            return any(self.maps)
-
-        @_recursive_repr()
-        def __repr__(self):
-            return '{0.__class__.__name__}({1})'.format(
-                self, ', '.join(map(repr, self.maps)))
-
-        @classmethod
-        def fromkeys(cls, iterable, *args):
-            'Create a ChainMap with a single dict created from the iterable.'
-            return cls(dict.fromkeys(iterable, *args))
-
-        def copy(self):
-            'New ChainMap or subclass with a new copy of maps[0] and refs to maps[1:]'
-            return self.__class__(self.maps[0].copy(), *self.maps[1:])
-
-        __copy__ = copy
-
-        def new_child(self):                        # like Django's Context.push()
-            'New ChainMap with a new dict followed by all previous maps.'
-            return self.__class__({}, *self.maps)
-
-        @property
-        def parents(self):                          # like Django's Context.pop()
-            'New ChainMap from maps[1:].'
-            return self.__class__(*self.maps[1:])
-
-        def __setitem__(self, key, value):
-            self.maps[0][key] = value
-
-        def __delitem__(self, key):
-            try:
-                del self.maps[0][key]
-            except KeyError:
-                raise KeyError('Key not found in the first mapping: {!r}'.format(key))
-
-        def popitem(self):
-            'Remove and return an item pair from maps[0]. Raise KeyError is maps[0] is empty.'
-            try:
-                return self.maps[0].popitem()
-            except KeyError:
-                raise KeyError('No keys found in the first mapping.')
-
-        def pop(self, key, *args):
-            'Remove *key* from maps[0] and return its value. Raise KeyError if *key* not in maps[0].'
-            try:
-                return self.maps[0].pop(key, *args)
-            except KeyError:
-                raise KeyError('Key not found in the first mapping: {!r}'.format(key))
-
-        def clear(self):
-            'Clear maps[0], leaving maps[1:] intact.'
-            self.maps[0].clear()
-
-try:
-    from importlib.util import cache_from_source  # Python >= 3.4
-except ImportError:  # pragma: no cover
-    try:
-        from imp import cache_from_source
-    except ImportError:  # pragma: no cover
-        def cache_from_source(path, debug_override=None):
-            assert path.endswith('.py')
-            if debug_override is None:
-                debug_override = __debug__
-            if debug_override:
-                suffix = 'c'
-            else:
-                suffix = 'o'
-            return path + suffix
-
-try:
-    from collections import OrderedDict
-except ImportError: # pragma: no cover
-## {{{ http://code.activestate.com/recipes/576693/ (r9)
-# Backport of OrderedDict() class that runs on Python 2.4, 2.5, 2.6, 2.7 and pypy.
-# Passes Python2.7's test suite and incorporates all the latest updates.
-    try:
-        from thread import get_ident as _get_ident
-    except ImportError:
-        from dummy_thread import get_ident as _get_ident
-
-    try:
-        from _abcoll import KeysView, ValuesView, ItemsView
-    except ImportError:
-        pass
-
-
-    class OrderedDict(dict):
-        'Dictionary that remembers insertion order'
-        # An inherited dict maps keys to values.
-        # The inherited dict provides __getitem__, __len__, __contains__, and get.
-        # The remaining methods are order-aware.
-        # Big-O running times for all methods are the same as for regular dictionaries.
-
-        # The internal self.__map dictionary maps keys to links in a doubly linked list.
-        # The circular doubly linked list starts and ends with a sentinel element.
-        # The sentinel element never gets deleted (this simplifies the algorithm).
-        # Each link is stored as a list of length three:  [PREV, NEXT, KEY].
-
-        def __init__(self, *args, **kwds):
-            '''Initialize an ordered dictionary.  Signature is the same as for
-            regular dictionaries, but keyword arguments are not recommended
-            because their insertion order is arbitrary.
-
-            '''
-            if len(args) > 1:
-                raise TypeError('expected at most 1 arguments, got %d' % len(args))
-            try:
-                self.__root
-            except AttributeError:
-                self.__root = root = []                     # sentinel node
-                root[:] = [root, root, None]
-                self.__map = {}
-            self.__update(*args, **kwds)
-
-        def __setitem__(self, key, value, dict_setitem=dict.__setitem__):
-            'od.__setitem__(i, y) <==> od[i]=y'
-            # Setting a new item creates a new link which goes at the end of the linked
-            # list, and the inherited dictionary is updated with the new key/value pair.
-            if key not in self:
-                root = self.__root
-                last = root[0]
-                last[1] = root[0] = self.__map[key] = [last, root, key]
-            dict_setitem(self, key, value)
-
-        def __delitem__(self, key, dict_delitem=dict.__delitem__):
-            'od.__delitem__(y) <==> del od[y]'
-            # Deleting an existing item uses self.__map to find the link which is
-            # then removed by updating the links in the predecessor and successor nodes.
-            dict_delitem(self, key)
-            link_prev, link_next, key = self.__map.pop(key)
-            link_prev[1] = link_next
-            link_next[0] = link_prev
-
-        def __iter__(self):
-            'od.__iter__() <==> iter(od)'
-            root = self.__root
-            curr = root[1]
-            while curr is not root:
-                yield curr[2]
-                curr = curr[1]
-
-        def __reversed__(self):
-            'od.__reversed__() <==> reversed(od)'
-            root = self.__root
-            curr = root[0]
-            while curr is not root:
-                yield curr[2]
-                curr = curr[0]
-
-        def clear(self):
-            'od.clear() -> None.  Remove all items from od.'
-            try:
-                for node in self.__map.itervalues():
-                    del node[:]
-                root = self.__root
-                root[:] = [root, root, None]
-                self.__map.clear()
-            except AttributeError:
-                pass
-            dict.clear(self)
-
-        def popitem(self, last=True):
-            '''od.popitem() -> (k, v), return and remove a (key, value) pair.
-            Pairs are returned in LIFO order if last is true or FIFO order if false.
-
-            '''
-            if not self:
-                raise KeyError('dictionary is empty')
-            root = self.__root
-            if last:
-                link = root[0]
-                link_prev = link[0]
-                link_prev[1] = root
-                root[0] = link_prev
-            else:
-                link = root[1]
-                link_next = link[1]
-                root[1] = link_next
-                link_next[0] = root
-            key = link[2]
-            del self.__map[key]
-            value = dict.pop(self, key)
-            return key, value
-
-        # -- the following methods do not depend on the internal structure --
-
-        def keys(self):
-            'od.keys() -> list of keys in od'
-            return list(self)
-
-        def values(self):
-            'od.values() -> list of values in od'
-            return [self[key] for key in self]
-
-        def items(self):
-            'od.items() -> list of (key, value) pairs in od'
-            return [(key, self[key]) for key in self]
-
-        def iterkeys(self):
-            'od.iterkeys() -> an iterator over the keys in od'
-            return iter(self)
-
-        def itervalues(self):
-            'od.itervalues -> an iterator over the values in od'
-            for k in self:
-                yield self[k]
-
-        def iteritems(self):
-            'od.iteritems -> an iterator over the (key, value) items in od'
-            for k in self:
-                yield (k, self[k])
-
-        def update(*args, **kwds):
-            '''od.update(E, **F) -> None.  Update od from dict/iterable E and F.
-
-            If E is a dict instance, does:           for k in E: od[k] = E[k]
-            If E has a .keys() method, does:         for k in E.keys(): od[k] = E[k]
-            Or if E is an iterable of items, does:   for k, v in E: od[k] = v
-            In either case, this is followed by:     for k, v in F.items(): od[k] = v
-
-            '''
-            if len(args) > 2:
-                raise TypeError('update() takes at most 2 positional '
-                                'arguments (%d given)' % (len(args),))
-            elif not args:
-                raise TypeError('update() takes at least 1 argument (0 given)')
-            self = args[0]
-            # Make progressively weaker assumptions about "other"
-            other = ()
-            if len(args) == 2:
-                other = args[1]
-            if isinstance(other, dict):
-                for key in other:
-                    self[key] = other[key]
-            elif hasattr(other, 'keys'):
-                for key in other.keys():
-                    self[key] = other[key]
-            else:
-                for key, value in other:
-                    self[key] = value
-            for key, value in kwds.items():
-                self[key] = value
-
-        __update = update  # let subclasses override update without breaking __init__
-
-        __marker = object()
-
-        def pop(self, key, default=__marker):
-            '''od.pop(k[,d]) -> v, remove specified key and return the corresponding value.
-            If key is not found, d is returned if given, otherwise KeyError is raised.
-
-            '''
-            if key in self:
-                result = self[key]
-                del self[key]
-                return result
-            if default is self.__marker:
-                raise KeyError(key)
-            return default
-
-        def setdefault(self, key, default=None):
-            'od.setdefault(k[,d]) -> od.get(k,d), also set od[k]=d if k not in od'
-            if key in self:
-                return self[key]
-            self[key] = default
-            return default
-
-        def __repr__(self, _repr_running=None):
-            'od.__repr__() <==> repr(od)'
-            if not _repr_running: _repr_running = {}
-            call_key = id(self), _get_ident()
-            if call_key in _repr_running:
-                return '...'
-            _repr_running[call_key] = 1
-            try:
-                if not self:
-                    return '%s()' % (self.__class__.__name__,)
-                return '%s(%r)' % (self.__class__.__name__, self.items())
-            finally:
-                del _repr_running[call_key]
-
-        def __reduce__(self):
-            'Return state information for pickling'
-            items = [[k, self[k]] for k in self]
-            inst_dict = vars(self).copy()
-            for k in vars(OrderedDict()):
-                inst_dict.pop(k, None)
-            if inst_dict:
-                return (self.__class__, (items,), inst_dict)
-            return self.__class__, (items,)
-
-        def copy(self):
-            'od.copy() -> a shallow copy of od'
-            return self.__class__(self)
-
-        @classmethod
-        def fromkeys(cls, iterable, value=None):
-            '''OD.fromkeys(S[, v]) -> New ordered dictionary with keys from S
-            and values equal to v (which defaults to None).
-
-            '''
-            d = cls()
-            for key in iterable:
-                d[key] = value
-            return d
-
-        def __eq__(self, other):
-            '''od.__eq__(y) <==> od==y.  Comparison to another OD is order-sensitive
-            while comparison to a regular mapping is order-insensitive.
-
-            '''
-            if isinstance(other, OrderedDict):
-                return len(self)==len(other) and self.items() == other.items()
-            return dict.__eq__(self, other)
-
-        def __ne__(self, other):
-            return not self == other
-
-        # -- the following methods are only used in Python 2.7 --
-
-        def viewkeys(self):
-            "od.viewkeys() -> a set-like object providing a view on od's keys"
-            return KeysView(self)
-
-        def viewvalues(self):
-            "od.viewvalues() -> an object providing a view on od's values"
-            return ValuesView(self)
-
-        def viewitems(self):
-            "od.viewitems() -> a set-like object providing a view on od's items"
-            return ItemsView(self)
-
-try:
-    from logging.config import BaseConfigurator, valid_ident
-except ImportError: # pragma: no cover
-    IDENTIFIER = re.compile('^[a-z_][a-z0-9_]*$', re.I)
-
-
-    def valid_ident(s):
-        m = IDENTIFIER.match(s)
-        if not m:
-            raise ValueError('Not a valid Python identifier: %r' % s)
-        return True
-
-
-    # The ConvertingXXX classes are wrappers around standard Python containers,
-    # and they serve to convert any suitable values in the container. The
-    # conversion converts base dicts, lists and tuples to their wrapped
-    # equivalents, whereas strings which match a conversion format are converted
-    # appropriately.
-    #
-    # Each wrapper should have a configurator attribute holding the actual
-    # configurator to use for conversion.
-
-    class ConvertingDict(dict):
-        """A converting dictionary wrapper."""
-
-        def __getitem__(self, key):
-            value = dict.__getitem__(self, key)
-            result = self.configurator.convert(value)
-            #If the converted value is different, save for next time
-            if value is not result:
-                self[key] = result
-                if type(result) in (ConvertingDict, ConvertingList,
-                                    ConvertingTuple):
-                    result.parent = self
-                    result.key = key
-            return result
-
-        def get(self, key, default=None):
-            value = dict.get(self, key, default)
-            result = self.configurator.convert(value)
-            #If the converted value is different, save for next time
-            if value is not result:
-                self[key] = result
-                if type(result) in (ConvertingDict, ConvertingList,
-                                    ConvertingTuple):
-                    result.parent = self
-                    result.key = key
-            return result
-
-    def pop(self, key, default=None):
-        value = dict.pop(self, key, default)
-        result = self.configurator.convert(value)
-        if value is not result:
-            if type(result) in (ConvertingDict, ConvertingList,
-                                ConvertingTuple):
-                result.parent = self
-                result.key = key
-        return result
-
-    class ConvertingList(list):
-        """A converting list wrapper."""
-        def __getitem__(self, key):
-            value = list.__getitem__(self, key)
-            result = self.configurator.convert(value)
-            #If the converted value is different, save for next time
-            if value is not result:
-                self[key] = result
-                if type(result) in (ConvertingDict, ConvertingList,
-                                    ConvertingTuple):
-                    result.parent = self
-                    result.key = key
-            return result
-
-        def pop(self, idx=-1):
-            value = list.pop(self, idx)
-            result = self.configurator.convert(value)
-            if value is not result:
-                if type(result) in (ConvertingDict, ConvertingList,
-                                    ConvertingTuple):
-                    result.parent = self
-            return result
-
-    class ConvertingTuple(tuple):
-        """A converting tuple wrapper."""
-        def __getitem__(self, key):
-            value = tuple.__getitem__(self, key)
-            result = self.configurator.convert(value)
-            if value is not result:
-                if type(result) in (ConvertingDict, ConvertingList,
-                                    ConvertingTuple):
-                    result.parent = self
-                    result.key = key
-            return result
-
-    class BaseConfigurator(object):
-        """
-        The configurator base class which defines some useful defaults.
-        """
-
-        CONVERT_PATTERN = re.compile(r'^(?P<prefix>[a-z]+)://(?P<suffix>.*)$')
-
-        WORD_PATTERN = re.compile(r'^\s*(\w+)\s*')
-        DOT_PATTERN = re.compile(r'^\.\s*(\w+)\s*')
-        INDEX_PATTERN = re.compile(r'^\[\s*(\w+)\s*\]\s*')
-        DIGIT_PATTERN = re.compile(r'^\d+$')
-
-        value_converters = {
-            'ext' : 'ext_convert',
-            'cfg' : 'cfg_convert',
-        }
-
-        # We might want to use a different one, e.g. importlib
-        importer = staticmethod(__import__)
-
-        def __init__(self, config):
-            self.config = ConvertingDict(config)
-            self.config.configurator = self
-
-        def resolve(self, s):
-            """
-            Resolve strings to objects using standard import and attribute
-            syntax.
-            """
-            name = s.split('.')
-            used = name.pop(0)
-            try:
-                found = self.importer(used)
-                for frag in name:
-                    used += '.' + frag
-                    try:
-                        found = getattr(found, frag)
-                    except AttributeError:
-                        self.importer(used)
-                        found = getattr(found, frag)
-                return found
-            except ImportError:
-                e, tb = sys.exc_info()[1:]
-                v = ValueError('Cannot resolve %r: %s' % (s, e))
-                v.__cause__, v.__traceback__ = e, tb
-                raise v
-
-        def ext_convert(self, value):
-            """Default converter for the ext:// protocol."""
-            return self.resolve(value)
-
-        def cfg_convert(self, value):
-            """Default converter for the cfg:// protocol."""
-            rest = value
-            m = self.WORD_PATTERN.match(rest)
-            if m is None:
-                raise ValueError("Unable to convert %r" % value)
-            else:
-                rest = rest[m.end():]
-                d = self.config[m.groups()[0]]
-                #print d, rest
-                while rest:
-                    m = self.DOT_PATTERN.match(rest)
-                    if m:
-                        d = d[m.groups()[0]]
-                    else:
-                        m = self.INDEX_PATTERN.match(rest)
-                        if m:
-                            idx = m.groups()[0]
-                            if not self.DIGIT_PATTERN.match(idx):
-                                d = d[idx]
-                            else:
-                                try:
-                                    n = int(idx) # try as number first (most likely)
-                                    d = d[n]
-                                except TypeError:
-                                    d = d[idx]
-                    if m:
-                        rest = rest[m.end():]
-                    else:
-                        raise ValueError('Unable to convert '
-                                         '%r at %r' % (value, rest))
-            #rest should be empty
-            return d
-
-        def convert(self, value):
-            """
-            Convert values to an appropriate type. dicts, lists and tuples are
-            replaced by their converting alternatives. Strings are checked to
-            see if they have a conversion format and are converted if they do.
-            """
-            if not isinstance(value, ConvertingDict) and isinstance(value, dict):
-                value = ConvertingDict(value)
-                value.configurator = self
-            elif not isinstance(value, ConvertingList) and isinstance(value, list):
-                value = ConvertingList(value)
-                value.configurator = self
-            elif not isinstance(value, ConvertingTuple) and\
-                     isinstance(value, tuple):
-                value = ConvertingTuple(value)
-                value.configurator = self
-            elif isinstance(value, string_types):
-                m = self.CONVERT_PATTERN.match(value)
-                if m:
-                    d = m.groupdict()
-                    prefix = d['prefix']
-                    converter = self.value_converters.get(prefix, None)
-                    if converter:
-                        suffix = d['suffix']
-                        converter = getattr(self, converter)
-                        value = converter(suffix)
-            return value
-
-        def configure_custom(self, config):
-            """Configure an object with a user-supplied factory."""
-            c = config.pop('()')
-            if not callable(c):
-                c = self.resolve(c)
-            props = config.pop('.', None)
-            # Check for valid identifiers
-            kwargs = dict([(k, config[k]) for k in config if valid_ident(k)])
-            result = c(**kwargs)
-            if props:
-                for name, value in props.items():
-                    setattr(result, name, value)
-            return result
-
-        def as_tuple(self, value):
-            """Utility function which converts lists to tuples."""
-            if isinstance(value, list):
-                value = tuple(value)
-            return value
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/database.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/database.py
deleted file mode 100644
index b13cdac..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/database.py
+++ /dev/null
@@ -1,1339 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012-2017 The Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""PEP 376 implementation."""
-
-from __future__ import unicode_literals
-
-import base64
-import codecs
-import contextlib
-import hashlib
-import logging
-import os
-import posixpath
-import sys
-import zipimport
-
-from . import DistlibException, resources
-from .compat import StringIO
-from .version import get_scheme, UnsupportedVersionError
-from .metadata import (Metadata, METADATA_FILENAME, WHEEL_METADATA_FILENAME,
-                       LEGACY_METADATA_FILENAME)
-from .util import (parse_requirement, cached_property, parse_name_and_version,
-                   read_exports, write_exports, CSVReader, CSVWriter)
-
-
-__all__ = ['Distribution', 'BaseInstalledDistribution',
-           'InstalledDistribution', 'EggInfoDistribution',
-           'DistributionPath']
-
-
-logger = logging.getLogger(__name__)
-
-EXPORTS_FILENAME = 'pydist-exports.json'
-COMMANDS_FILENAME = 'pydist-commands.json'
-
-DIST_FILES = ('INSTALLER', METADATA_FILENAME, 'RECORD', 'REQUESTED',
-              'RESOURCES', EXPORTS_FILENAME, 'SHARED')
-
-DISTINFO_EXT = '.dist-info'
-
-
-class _Cache(object):
-    """
-    A simple cache mapping names and .dist-info paths to distributions
-    """
-    def __init__(self):
-        """
-        Initialise an instance. There is normally one for each DistributionPath.
-        """
-        self.name = {}
-        self.path = {}
-        self.generated = False
-
-    def clear(self):
-        """
-        Clear the cache, setting it to its initial state.
-        """
-        self.name.clear()
-        self.path.clear()
-        self.generated = False
-
-    def add(self, dist):
-        """
-        Add a distribution to the cache.
-        :param dist: The distribution to add.
-        """
-        if dist.path not in self.path:
-            self.path[dist.path] = dist
-            self.name.setdefault(dist.key, []).append(dist)
-
-
-class DistributionPath(object):
-    """
-    Represents a set of distributions installed on a path (typically sys.path).
-    """
-    def __init__(self, path=None, include_egg=False):
-        """
-        Create an instance from a path, optionally including legacy (distutils/
-        setuptools/distribute) distributions.
-        :param path: The path to use, as a list of directories. If not specified,
-                     sys.path is used.
-        :param include_egg: If True, this instance will look for and return legacy
-                            distributions as well as those based on PEP 376.
-        """
-        if path is None:
-            path = sys.path
-        self.path = path
-        self._include_dist = True
-        self._include_egg = include_egg
-
-        self._cache = _Cache()
-        self._cache_egg = _Cache()
-        self._cache_enabled = True
-        self._scheme = get_scheme('default')
-
-    def _get_cache_enabled(self):
-        return self._cache_enabled
-
-    def _set_cache_enabled(self, value):
-        self._cache_enabled = value
-
-    cache_enabled = property(_get_cache_enabled, _set_cache_enabled)
-
-    def clear_cache(self):
-        """
-        Clears the internal cache.
-        """
-        self._cache.clear()
-        self._cache_egg.clear()
-
-
-    def _yield_distributions(self):
-        """
-        Yield .dist-info and/or .egg(-info) distributions.
-        """
-        # We need to check if we've seen some resources already, because on
-        # some Linux systems (e.g. some Debian/Ubuntu variants) there are
-        # symlinks which alias other files in the environment.
-        seen = set()
-        for path in self.path:
-            finder = resources.finder_for_path(path)
-            if finder is None:
-                continue
-            r = finder.find('')
-            if not r or not r.is_container:
-                continue
-            rset = sorted(r.resources)
-            for entry in rset:
-                r = finder.find(entry)
-                if not r or r.path in seen:
-                    continue
-                if self._include_dist and entry.endswith(DISTINFO_EXT):
-                    possible_filenames = [METADATA_FILENAME,
-                                          WHEEL_METADATA_FILENAME,
-                                          LEGACY_METADATA_FILENAME]
-                    for metadata_filename in possible_filenames:
-                        metadata_path = posixpath.join(entry, metadata_filename)
-                        pydist = finder.find(metadata_path)
-                        if pydist:
-                            break
-                    else:
-                        continue
-
-                    with contextlib.closing(pydist.as_stream()) as stream:
-                        metadata = Metadata(fileobj=stream, scheme='legacy')
-                    logger.debug('Found %s', r.path)
-                    seen.add(r.path)
-                    yield new_dist_class(r.path, metadata=metadata,
-                                         env=self)
-                elif self._include_egg and entry.endswith(('.egg-info',
-                                                          '.egg')):
-                    logger.debug('Found %s', r.path)
-                    seen.add(r.path)
-                    yield old_dist_class(r.path, self)
-
-    def _generate_cache(self):
-        """
-        Scan the path for distributions and populate the cache with
-        those that are found.
-        """
-        gen_dist = not self._cache.generated
-        gen_egg = self._include_egg and not self._cache_egg.generated
-        if gen_dist or gen_egg:
-            for dist in self._yield_distributions():
-                if isinstance(dist, InstalledDistribution):
-                    self._cache.add(dist)
-                else:
-                    self._cache_egg.add(dist)
-
-            if gen_dist:
-                self._cache.generated = True
-            if gen_egg:
-                self._cache_egg.generated = True
-
-    @classmethod
-    def distinfo_dirname(cls, name, version):
-        """
-        The *name* and *version* parameters are converted into their
-        filename-escaped form, i.e. any ``'-'`` characters are replaced
-        with ``'_'`` other than the one in ``'dist-info'`` and the one
-        separating the name from the version number.
-
-        :parameter name: is converted to a standard distribution name by replacing
-                         any runs of non- alphanumeric characters with a single
-                         ``'-'``.
-        :type name: string
-        :parameter version: is converted to a standard version string. Spaces
-                            become dots, and all other non-alphanumeric characters
-                            (except dots) become dashes, with runs of multiple
-                            dashes condensed to a single dash.
-        :type version: string
-        :returns: directory name
-        :rtype: string"""
-        name = name.replace('-', '_')
-        return '-'.join([name, version]) + DISTINFO_EXT
-
-    def get_distributions(self):
-        """
-        Provides an iterator that looks for distributions and returns
-        :class:`InstalledDistribution` or
-        :class:`EggInfoDistribution` instances for each one of them.
-
-        :rtype: iterator of :class:`InstalledDistribution` and
-                :class:`EggInfoDistribution` instances
-        """
-        if not self._cache_enabled:
-            for dist in self._yield_distributions():
-                yield dist
-        else:
-            self._generate_cache()
-
-            for dist in self._cache.path.values():
-                yield dist
-
-            if self._include_egg:
-                for dist in self._cache_egg.path.values():
-                    yield dist
-
-    def get_distribution(self, name):
-        """
-        Looks for a named distribution on the path.
-
-        This function only returns the first result found, as no more than one
-        value is expected. If nothing is found, ``None`` is returned.
-
-        :rtype: :class:`InstalledDistribution`, :class:`EggInfoDistribution`
-                or ``None``
-        """
-        result = None
-        name = name.lower()
-        if not self._cache_enabled:
-            for dist in self._yield_distributions():
-                if dist.key == name:
-                    result = dist
-                    break
-        else:
-            self._generate_cache()
-
-            if name in self._cache.name:
-                result = self._cache.name[name][0]
-            elif self._include_egg and name in self._cache_egg.name:
-                result = self._cache_egg.name[name][0]
-        return result
-
-    def provides_distribution(self, name, version=None):
-        """
-        Iterates over all distributions to find which distributions provide *name*.
-        If a *version* is provided, it will be used to filter the results.
-
-        This function only returns the first result found, since no more than
-        one values are expected. If the directory is not found, returns ``None``.
-
-        :parameter version: a version specifier that indicates the version
-                            required, conforming to the format in ``PEP-345``
-
-        :type name: string
-        :type version: string
-        """
-        matcher = None
-        if version is not None:
-            try:
-                matcher = self._scheme.matcher('%s (%s)' % (name, version))
-            except ValueError:
-                raise DistlibException('invalid name or version: %r, %r' %
-                                      (name, version))
-
-        for dist in self.get_distributions():
-            # We hit a problem on Travis where enum34 was installed and doesn't
-            # have a provides attribute ...
-            if not hasattr(dist, 'provides'):
-                logger.debug('No "provides": %s', dist)
-            else:
-                provided = dist.provides
-
-                for p in provided:
-                    p_name, p_ver = parse_name_and_version(p)
-                    if matcher is None:
-                        if p_name == name:
-                            yield dist
-                            break
-                    else:
-                        if p_name == name and matcher.match(p_ver):
-                            yield dist
-                            break
-
-    def get_file_path(self, name, relative_path):
-        """
-        Return the path to a resource file.
-        """
-        dist = self.get_distribution(name)
-        if dist is None:
-            raise LookupError('no distribution named %r found' % name)
-        return dist.get_resource_path(relative_path)
-
-    def get_exported_entries(self, category, name=None):
-        """
-        Return all of the exported entries in a particular category.
-
-        :param category: The category to search for entries.
-        :param name: If specified, only entries with that name are returned.
-        """
-        for dist in self.get_distributions():
-            r = dist.exports
-            if category in r:
-                d = r[category]
-                if name is not None:
-                    if name in d:
-                        yield d[name]
-                else:
-                    for v in d.values():
-                        yield v
-
-
-class Distribution(object):
-    """
-    A base class for distributions, whether installed or from indexes.
-    Either way, it must have some metadata, so that's all that's needed
-    for construction.
-    """
-
-    build_time_dependency = False
-    """
-    Set to True if it's known to be only a build-time dependency (i.e.
-    not needed after installation).
-    """
-
-    requested = False
-    """A boolean that indicates whether the ``REQUESTED`` metadata file is
-    present (in other words, whether the package was installed by user
-    request or it was installed as a dependency)."""
-
-    def __init__(self, metadata):
-        """
-        Initialise an instance.
-        :param metadata: The instance of :class:`Metadata` describing this
-        distribution.
-        """
-        self.metadata = metadata
-        self.name = metadata.name
-        self.key = self.name.lower()    # for case-insensitive comparisons
-        self.version = metadata.version
-        self.locator = None
-        self.digest = None
-        self.extras = None      # additional features requested
-        self.context = None     # environment marker overrides
-        self.download_urls = set()
-        self.digests = {}
-
-    @property
-    def source_url(self):
-        """
-        The source archive download URL for this distribution.
-        """
-        return self.metadata.source_url
-
-    download_url = source_url   # Backward compatibility
-
-    @property
-    def name_and_version(self):
-        """
-        A utility property which displays the name and version in parentheses.
-        """
-        return '%s (%s)' % (self.name, self.version)
-
-    @property
-    def provides(self):
-        """
-        A set of distribution names and versions provided by this distribution.
-        :return: A set of "name (version)" strings.
-        """
-        plist = self.metadata.provides
-        s = '%s (%s)' % (self.name, self.version)
-        if s not in plist:
-            plist.append(s)
-        return plist
-
-    def _get_requirements(self, req_attr):
-        md = self.metadata
-        logger.debug('Getting requirements from metadata %r', md.todict())
-        reqts = getattr(md, req_attr)
-        return set(md.get_requirements(reqts, extras=self.extras,
-                                       env=self.context))
-
-    @property
-    def run_requires(self):
-        return self._get_requirements('run_requires')
-
-    @property
-    def meta_requires(self):
-        return self._get_requirements('meta_requires')
-
-    @property
-    def build_requires(self):
-        return self._get_requirements('build_requires')
-
-    @property
-    def test_requires(self):
-        return self._get_requirements('test_requires')
-
-    @property
-    def dev_requires(self):
-        return self._get_requirements('dev_requires')
-
-    def matches_requirement(self, req):
-        """
-        Say if this instance matches (fulfills) a requirement.
-        :param req: The requirement to match.
-        :rtype req: str
-        :return: True if it matches, else False.
-        """
-        # Requirement may contain extras - parse to lose those
-        # from what's passed to the matcher
-        r = parse_requirement(req)
-        scheme = get_scheme(self.metadata.scheme)
-        try:
-            matcher = scheme.matcher(r.requirement)
-        except UnsupportedVersionError:
-            # XXX compat-mode if cannot read the version
-            logger.warning('could not read version %r - using name only',
-                           req)
-            name = req.split()[0]
-            matcher = scheme.matcher(name)
-
-        name = matcher.key   # case-insensitive
-
-        result = False
-        for p in self.provides:
-            p_name, p_ver = parse_name_and_version(p)
-            if p_name != name:
-                continue
-            try:
-                result = matcher.match(p_ver)
-                break
-            except UnsupportedVersionError:
-                pass
-        return result
-
-    def __repr__(self):
-        """
-        Return a textual representation of this instance,
-        """
-        if self.source_url:
-            suffix = ' [%s]' % self.source_url
-        else:
-            suffix = ''
-        return '<Distribution %s (%s)%s>' % (self.name, self.version, suffix)
-
-    def __eq__(self, other):
-        """
-        See if this distribution is the same as another.
-        :param other: The distribution to compare with. To be equal to one
-                      another. distributions must have the same type, name,
-                      version and source_url.
-        :return: True if it is the same, else False.
-        """
-        if type(other) is not type(self):
-            result = False
-        else:
-            result = (self.name == other.name and
-                      self.version == other.version and
-                      self.source_url == other.source_url)
-        return result
-
-    def __hash__(self):
-        """
-        Compute hash in a way which matches the equality test.
-        """
-        return hash(self.name) + hash(self.version) + hash(self.source_url)
-
-
-class BaseInstalledDistribution(Distribution):
-    """
-    This is the base class for installed distributions (whether PEP 376 or
-    legacy).
-    """
-
-    hasher = None
-
-    def __init__(self, metadata, path, env=None):
-        """
-        Initialise an instance.
-        :param metadata: An instance of :class:`Metadata` which describes the
-                         distribution. This will normally have been initialised
-                         from a metadata file in the ``path``.
-        :param path:     The path of the ``.dist-info`` or ``.egg-info``
-                         directory for the distribution.
-        :param env:      This is normally the :class:`DistributionPath`
-                         instance where this distribution was found.
-        """
-        super(BaseInstalledDistribution, self).__init__(metadata)
-        self.path = path
-        self.dist_path = env
-
-    def get_hash(self, data, hasher=None):
-        """
-        Get the hash of some data, using a particular hash algorithm, if
-        specified.
-
-        :param data: The data to be hashed.
-        :type data: bytes
-        :param hasher: The name of a hash implementation, supported by hashlib,
-                       or ``None``. Examples of valid values are ``'sha1'``,
-                       ``'sha224'``, ``'sha384'``, '``sha256'``, ``'md5'`` and
-                       ``'sha512'``. If no hasher is specified, the ``hasher``
-                       attribute of the :class:`InstalledDistribution` instance
-                       is used. If the hasher is determined to be ``None``, MD5
-                       is used as the hashing algorithm.
-        :returns: The hash of the data. If a hasher was explicitly specified,
-                  the returned hash will be prefixed with the specified hasher
-                  followed by '='.
-        :rtype: str
-        """
-        if hasher is None:
-            hasher = self.hasher
-        if hasher is None:
-            hasher = hashlib.md5
-            prefix = ''
-        else:
-            hasher = getattr(hashlib, hasher)
-            prefix = '%s=' % self.hasher
-        digest = hasher(data).digest()
-        digest = base64.urlsafe_b64encode(digest).rstrip(b'=').decode('ascii')
-        return '%s%s' % (prefix, digest)
-
-
-class InstalledDistribution(BaseInstalledDistribution):
-    """
-    Created with the *path* of the ``.dist-info`` directory provided to the
-    constructor. It reads the metadata contained in ``pydist.json`` when it is
-    instantiated., or uses a passed in Metadata instance (useful for when
-    dry-run mode is being used).
-    """
-
-    hasher = 'sha256'
-
-    def __init__(self, path, metadata=None, env=None):
-        self.modules = []
-        self.finder = finder = resources.finder_for_path(path)
-        if finder is None:
-            raise ValueError('finder unavailable for %s' % path)
-        if env and env._cache_enabled and path in env._cache.path:
-            metadata = env._cache.path[path].metadata
-        elif metadata is None:
-            r = finder.find(METADATA_FILENAME)
-            # Temporary - for Wheel 0.23 support
-            if r is None:
-                r = finder.find(WHEEL_METADATA_FILENAME)
-            # Temporary - for legacy support
-            if r is None:
-                r = finder.find('METADATA')
-            if r is None:
-                raise ValueError('no %s found in %s' % (METADATA_FILENAME,
-                                                        path))
-            with contextlib.closing(r.as_stream()) as stream:
-                metadata = Metadata(fileobj=stream, scheme='legacy')
-
-        super(InstalledDistribution, self).__init__(metadata, path, env)
-
-        if env and env._cache_enabled:
-            env._cache.add(self)
-
-        r = finder.find('REQUESTED')
-        self.requested = r is not None
-        p  = os.path.join(path, 'top_level.txt')
-        if os.path.exists(p):
-            with open(p, 'rb') as f:
-                data = f.read()
-            self.modules = data.splitlines()
-
-    def __repr__(self):
-        return '<InstalledDistribution %r %s at %r>' % (
-            self.name, self.version, self.path)
-
-    def __str__(self):
-        return "%s %s" % (self.name, self.version)
-
-    def _get_records(self):
-        """
-        Get the list of installed files for the distribution
-        :return: A list of tuples of path, hash and size. Note that hash and
-                 size might be ``None`` for some entries. The path is exactly
-                 as stored in the file (which is as in PEP 376).
-        """
-        results = []
-        r = self.get_distinfo_resource('RECORD')
-        with contextlib.closing(r.as_stream()) as stream:
-            with CSVReader(stream=stream) as record_reader:
-                # Base location is parent dir of .dist-info dir
-                #base_location = os.path.dirname(self.path)
-                #base_location = os.path.abspath(base_location)
-                for row in record_reader:
-                    missing = [None for i in range(len(row), 3)]
-                    path, checksum, size = row + missing
-                    #if not os.path.isabs(path):
-                    #    path = path.replace('/', os.sep)
-                    #    path = os.path.join(base_location, path)
-                    results.append((path, checksum, size))
-        return results
-
-    @cached_property
-    def exports(self):
-        """
-        Return the information exported by this distribution.
-        :return: A dictionary of exports, mapping an export category to a dict
-                 of :class:`ExportEntry` instances describing the individual
-                 export entries, and keyed by name.
-        """
-        result = {}
-        r = self.get_distinfo_resource(EXPORTS_FILENAME)
-        if r:
-            result = self.read_exports()
-        return result
-
-    def read_exports(self):
-        """
-        Read exports data from a file in .ini format.
-
-        :return: A dictionary of exports, mapping an export category to a list
-                 of :class:`ExportEntry` instances describing the individual
-                 export entries.
-        """
-        result = {}
-        r = self.get_distinfo_resource(EXPORTS_FILENAME)
-        if r:
-            with contextlib.closing(r.as_stream()) as stream:
-                result = read_exports(stream)
-        return result
-
-    def write_exports(self, exports):
-        """
-        Write a dictionary of exports to a file in .ini format.
-        :param exports: A dictionary of exports, mapping an export category to
-                        a list of :class:`ExportEntry` instances describing the
-                        individual export entries.
-        """
-        rf = self.get_distinfo_file(EXPORTS_FILENAME)
-        with open(rf, 'w') as f:
-            write_exports(exports, f)
-
-    def get_resource_path(self, relative_path):
-        """
-        NOTE: This API may change in the future.
-
-        Return the absolute path to a resource file with the given relative
-        path.
-
-        :param relative_path: The path, relative to .dist-info, of the resource
-                              of interest.
-        :return: The absolute path where the resource is to be found.
-        """
-        r = self.get_distinfo_resource('RESOURCES')
-        with contextlib.closing(r.as_stream()) as stream:
-            with CSVReader(stream=stream) as resources_reader:
-                for relative, destination in resources_reader:
-                    if relative == relative_path:
-                        return destination
-        raise KeyError('no resource file with relative path %r '
-                       'is installed' % relative_path)
-
-    def list_installed_files(self):
-        """
-        Iterates over the ``RECORD`` entries and returns a tuple
-        ``(path, hash, size)`` for each line.
-
-        :returns: iterator of (path, hash, size)
-        """
-        for result in self._get_records():
-            yield result
-
-    def write_installed_files(self, paths, prefix, dry_run=False):
-        """
-        Writes the ``RECORD`` file, using the ``paths`` iterable passed in. Any
-        existing ``RECORD`` file is silently overwritten.
-
-        prefix is used to determine when to write absolute paths.
-        """
-        prefix = os.path.join(prefix, '')
-        base = os.path.dirname(self.path)
-        base_under_prefix = base.startswith(prefix)
-        base = os.path.join(base, '')
-        record_path = self.get_distinfo_file('RECORD')
-        logger.info('creating %s', record_path)
-        if dry_run:
-            return None
-        with CSVWriter(record_path) as writer:
-            for path in paths:
-                if os.path.isdir(path) or path.endswith(('.pyc', '.pyo')):
-                    # do not put size and hash, as in PEP-376
-                    hash_value = size = ''
-                else:
-                    size = '%d' % os.path.getsize(path)
-                    with open(path, 'rb') as fp:
-                        hash_value = self.get_hash(fp.read())
-                if path.startswith(base) or (base_under_prefix and
-                                             path.startswith(prefix)):
-                    path = os.path.relpath(path, base)
-                writer.writerow((path, hash_value, size))
-
-            # add the RECORD file itself
-            if record_path.startswith(base):
-                record_path = os.path.relpath(record_path, base)
-            writer.writerow((record_path, '', ''))
-        return record_path
-
-    def check_installed_files(self):
-        """
-        Checks that the hashes and sizes of the files in ``RECORD`` are
-        matched by the files themselves. Returns a (possibly empty) list of
-        mismatches. Each entry in the mismatch list will be a tuple consisting
-        of the path, 'exists', 'size' or 'hash' according to what didn't match
-        (existence is checked first, then size, then hash), the expected
-        value and the actual value.
-        """
-        mismatches = []
-        base = os.path.dirname(self.path)
-        record_path = self.get_distinfo_file('RECORD')
-        for path, hash_value, size in self.list_installed_files():
-            if not os.path.isabs(path):
-                path = os.path.join(base, path)
-            if path == record_path:
-                continue
-            if not os.path.exists(path):
-                mismatches.append((path, 'exists', True, False))
-            elif os.path.isfile(path):
-                actual_size = str(os.path.getsize(path))
-                if size and actual_size != size:
-                    mismatches.append((path, 'size', size, actual_size))
-                elif hash_value:
-                    if '=' in hash_value:
-                        hasher = hash_value.split('=', 1)[0]
-                    else:
-                        hasher = None
-
-                    with open(path, 'rb') as f:
-                        actual_hash = self.get_hash(f.read(), hasher)
-                        if actual_hash != hash_value:
-                            mismatches.append((path, 'hash', hash_value, actual_hash))
-        return mismatches
-
-    @cached_property
-    def shared_locations(self):
-        """
-        A dictionary of shared locations whose keys are in the set 'prefix',
-        'purelib', 'platlib', 'scripts', 'headers', 'data' and 'namespace'.
-        The corresponding value is the absolute path of that category for
-        this distribution, and takes into account any paths selected by the
-        user at installation time (e.g. via command-line arguments). In the
-        case of the 'namespace' key, this would be a list of absolute paths
-        for the roots of namespace packages in this distribution.
-
-        The first time this property is accessed, the relevant information is
-        read from the SHARED file in the .dist-info directory.
-        """
-        result = {}
-        shared_path = os.path.join(self.path, 'SHARED')
-        if os.path.isfile(shared_path):
-            with codecs.open(shared_path, 'r', encoding='utf-8') as f:
-                lines = f.read().splitlines()
-            for line in lines:
-                key, value = line.split('=', 1)
-                if key == 'namespace':
-                    result.setdefault(key, []).append(value)
-                else:
-                    result[key] = value
-        return result
-
-    def write_shared_locations(self, paths, dry_run=False):
-        """
-        Write shared location information to the SHARED file in .dist-info.
-        :param paths: A dictionary as described in the documentation for
-        :meth:`shared_locations`.
-        :param dry_run: If True, the action is logged but no file is actually
-                        written.
-        :return: The path of the file written to.
-        """
-        shared_path = os.path.join(self.path, 'SHARED')
-        logger.info('creating %s', shared_path)
-        if dry_run:
-            return None
-        lines = []
-        for key in ('prefix', 'lib', 'headers', 'scripts', 'data'):
-            path = paths[key]
-            if os.path.isdir(paths[key]):
-                lines.append('%s=%s' % (key,  path))
-        for ns in paths.get('namespace', ()):
-            lines.append('namespace=%s' % ns)
-
-        with codecs.open(shared_path, 'w', encoding='utf-8') as f:
-            f.write('\n'.join(lines))
-        return shared_path
-
-    def get_distinfo_resource(self, path):
-        if path not in DIST_FILES:
-            raise DistlibException('invalid path for a dist-info file: '
-                                   '%r at %r' % (path, self.path))
-        finder = resources.finder_for_path(self.path)
-        if finder is None:
-            raise DistlibException('Unable to get a finder for %s' % self.path)
-        return finder.find(path)
-
-    def get_distinfo_file(self, path):
-        """
-        Returns a path located under the ``.dist-info`` directory. Returns a
-        string representing the path.
-
-        :parameter path: a ``'/'``-separated path relative to the
-                         ``.dist-info`` directory or an absolute path;
-                         If *path* is an absolute path and doesn't start
-                         with the ``.dist-info`` directory path,
-                         a :class:`DistlibException` is raised
-        :type path: str
-        :rtype: str
-        """
-        # Check if it is an absolute path  # XXX use relpath, add tests
-        if path.find(os.sep) >= 0:
-            # it's an absolute path?
-            distinfo_dirname, path = path.split(os.sep)[-2:]
-            if distinfo_dirname != self.path.split(os.sep)[-1]:
-                raise DistlibException(
-                    'dist-info file %r does not belong to the %r %s '
-                    'distribution' % (path, self.name, self.version))
-
-        # The file must be relative
-        if path not in DIST_FILES:
-            raise DistlibException('invalid path for a dist-info file: '
-                                   '%r at %r' % (path, self.path))
-
-        return os.path.join(self.path, path)
-
-    def list_distinfo_files(self):
-        """
-        Iterates over the ``RECORD`` entries and returns paths for each line if
-        the path is pointing to a file located in the ``.dist-info`` directory
-        or one of its subdirectories.
-
-        :returns: iterator of paths
-        """
-        base = os.path.dirname(self.path)
-        for path, checksum, size in self._get_records():
-            # XXX add separator or use real relpath algo
-            if not os.path.isabs(path):
-                path = os.path.join(base, path)
-            if path.startswith(self.path):
-                yield path
-
-    def __eq__(self, other):
-        return (isinstance(other, InstalledDistribution) and
-                self.path == other.path)
-
-    # See http://docs.python.org/reference/datamodel#object.__hash__
-    __hash__ = object.__hash__
-
-
-class EggInfoDistribution(BaseInstalledDistribution):
-    """Created with the *path* of the ``.egg-info`` directory or file provided
-    to the constructor. It reads the metadata contained in the file itself, or
-    if the given path happens to be a directory, the metadata is read from the
-    file ``PKG-INFO`` under that directory."""
-
-    requested = True    # as we have no way of knowing, assume it was
-    shared_locations = {}
-
-    def __init__(self, path, env=None):
-        def set_name_and_version(s, n, v):
-            s.name = n
-            s.key = n.lower()   # for case-insensitive comparisons
-            s.version = v
-
-        self.path = path
-        self.dist_path = env
-        if env and env._cache_enabled and path in env._cache_egg.path:
-            metadata = env._cache_egg.path[path].metadata
-            set_name_and_version(self, metadata.name, metadata.version)
-        else:
-            metadata = self._get_metadata(path)
-
-            # Need to be set before caching
-            set_name_and_version(self, metadata.name, metadata.version)
-
-            if env and env._cache_enabled:
-                env._cache_egg.add(self)
-        super(EggInfoDistribution, self).__init__(metadata, path, env)
-
-    def _get_metadata(self, path):
-        requires = None
-
-        def parse_requires_data(data):
-            """Create a list of dependencies from a requires.txt file.
-
-            *data*: the contents of a setuptools-produced requires.txt file.
-            """
-            reqs = []
-            lines = data.splitlines()
-            for line in lines:
-                line = line.strip()
-                if line.startswith('['):
-                    logger.warning('Unexpected line: quitting requirement scan: %r',
-                                   line)
-                    break
-                r = parse_requirement(line)
-                if not r:
-                    logger.warning('Not recognised as a requirement: %r', line)
-                    continue
-                if r.extras:
-                    logger.warning('extra requirements in requires.txt are '
-                                   'not supported')
-                if not r.constraints:
-                    reqs.append(r.name)
-                else:
-                    cons = ', '.join('%s%s' % c for c in r.constraints)
-                    reqs.append('%s (%s)' % (r.name, cons))
-            return reqs
-
-        def parse_requires_path(req_path):
-            """Create a list of dependencies from a requires.txt file.
-
-            *req_path*: the path to a setuptools-produced requires.txt file.
-            """
-
-            reqs = []
-            try:
-                with codecs.open(req_path, 'r', 'utf-8') as fp:
-                    reqs = parse_requires_data(fp.read())
-            except IOError:
-                pass
-            return reqs
-
-        tl_path = tl_data = None
-        if path.endswith('.egg'):
-            if os.path.isdir(path):
-                p = os.path.join(path, 'EGG-INFO')
-                meta_path = os.path.join(p, 'PKG-INFO')
-                metadata = Metadata(path=meta_path, scheme='legacy')
-                req_path = os.path.join(p, 'requires.txt')
-                tl_path = os.path.join(p, 'top_level.txt')
-                requires = parse_requires_path(req_path)
-            else:
-                # FIXME handle the case where zipfile is not available
-                zipf = zipimport.zipimporter(path)
-                fileobj = StringIO(
-                    zipf.get_data('EGG-INFO/PKG-INFO').decode('utf8'))
-                metadata = Metadata(fileobj=fileobj, scheme='legacy')
-                try:
-                    data = zipf.get_data('EGG-INFO/requires.txt')
-                    tl_data = zipf.get_data('EGG-INFO/top_level.txt').decode('utf-8')
-                    requires = parse_requires_data(data.decode('utf-8'))
-                except IOError:
-                    requires = None
-        elif path.endswith('.egg-info'):
-            if os.path.isdir(path):
-                req_path = os.path.join(path, 'requires.txt')
-                requires = parse_requires_path(req_path)
-                path = os.path.join(path, 'PKG-INFO')
-                tl_path = os.path.join(path, 'top_level.txt')
-            metadata = Metadata(path=path, scheme='legacy')
-        else:
-            raise DistlibException('path must end with .egg-info or .egg, '
-                                   'got %r' % path)
-
-        if requires:
-            metadata.add_requirements(requires)
-        # look for top-level modules in top_level.txt, if present
-        if tl_data is None:
-            if tl_path is not None and os.path.exists(tl_path):
-                with open(tl_path, 'rb') as f:
-                    tl_data = f.read().decode('utf-8')
-        if not tl_data:
-            tl_data = []
-        else:
-            tl_data = tl_data.splitlines()
-        self.modules = tl_data
-        return metadata
-
-    def __repr__(self):
-        return '<EggInfoDistribution %r %s at %r>' % (
-            self.name, self.version, self.path)
-
-    def __str__(self):
-        return "%s %s" % (self.name, self.version)
-
-    def check_installed_files(self):
-        """
-        Checks that the hashes and sizes of the files in ``RECORD`` are
-        matched by the files themselves. Returns a (possibly empty) list of
-        mismatches. Each entry in the mismatch list will be a tuple consisting
-        of the path, 'exists', 'size' or 'hash' according to what didn't match
-        (existence is checked first, then size, then hash), the expected
-        value and the actual value.
-        """
-        mismatches = []
-        record_path = os.path.join(self.path, 'installed-files.txt')
-        if os.path.exists(record_path):
-            for path, _, _ in self.list_installed_files():
-                if path == record_path:
-                    continue
-                if not os.path.exists(path):
-                    mismatches.append((path, 'exists', True, False))
-        return mismatches
-
-    def list_installed_files(self):
-        """
-        Iterates over the ``installed-files.txt`` entries and returns a tuple
-        ``(path, hash, size)`` for each line.
-
-        :returns: a list of (path, hash, size)
-        """
-
-        def _md5(path):
-            f = open(path, 'rb')
-            try:
-                content = f.read()
-            finally:
-                f.close()
-            return hashlib.md5(content).hexdigest()
-
-        def _size(path):
-            return os.stat(path).st_size
-
-        record_path = os.path.join(self.path, 'installed-files.txt')
-        result = []
-        if os.path.exists(record_path):
-            with codecs.open(record_path, 'r', encoding='utf-8') as f:
-                for line in f:
-                    line = line.strip()
-                    p = os.path.normpath(os.path.join(self.path, line))
-                    # "./" is present as a marker between installed files
-                    # and installation metadata files
-                    if not os.path.exists(p):
-                        logger.warning('Non-existent file: %s', p)
-                        if p.endswith(('.pyc', '.pyo')):
-                            continue
-                        #otherwise fall through and fail
-                    if not os.path.isdir(p):
-                        result.append((p, _md5(p), _size(p)))
-            result.append((record_path, None, None))
-        return result
-
-    def list_distinfo_files(self, absolute=False):
-        """
-        Iterates over the ``installed-files.txt`` entries and returns paths for
-        each line if the path is pointing to a file located in the
-        ``.egg-info`` directory or one of its subdirectories.
-
-        :parameter absolute: If *absolute* is ``True``, each returned path is
-                          transformed into a local absolute path. Otherwise the
-                          raw value from ``installed-files.txt`` is returned.
-        :type absolute: boolean
-        :returns: iterator of paths
-        """
-        record_path = os.path.join(self.path, 'installed-files.txt')
-        if os.path.exists(record_path):
-            skip = True
-            with codecs.open(record_path, 'r', encoding='utf-8') as f:
-                for line in f:
-                    line = line.strip()
-                    if line == './':
-                        skip = False
-                        continue
-                    if not skip:
-                        p = os.path.normpath(os.path.join(self.path, line))
-                        if p.startswith(self.path):
-                            if absolute:
-                                yield p
-                            else:
-                                yield line
-
-    def __eq__(self, other):
-        return (isinstance(other, EggInfoDistribution) and
-                self.path == other.path)
-
-    # See http://docs.python.org/reference/datamodel#object.__hash__
-    __hash__ = object.__hash__
-
-new_dist_class = InstalledDistribution
-old_dist_class = EggInfoDistribution
-
-
-class DependencyGraph(object):
-    """
-    Represents a dependency graph between distributions.
-
-    The dependency relationships are stored in an ``adjacency_list`` that maps
-    distributions to a list of ``(other, label)`` tuples where  ``other``
-    is a distribution and the edge is labeled with ``label`` (i.e. the version
-    specifier, if such was provided). Also, for more efficient traversal, for
-    every distribution ``x``, a list of predecessors is kept in
-    ``reverse_list[x]``. An edge from distribution ``a`` to
-    distribution ``b`` means that ``a`` depends on ``b``. If any missing
-    dependencies are found, they are stored in ``missing``, which is a
-    dictionary that maps distributions to a list of requirements that were not
-    provided by any other distributions.
-    """
-
-    def __init__(self):
-        self.adjacency_list = {}
-        self.reverse_list = {}
-        self.missing = {}
-
-    def add_distribution(self, distribution):
-        """Add the *distribution* to the graph.
-
-        :type distribution: :class:`distutils2.database.InstalledDistribution`
-                            or :class:`distutils2.database.EggInfoDistribution`
-        """
-        self.adjacency_list[distribution] = []
-        self.reverse_list[distribution] = []
-        #self.missing[distribution] = []
-
-    def add_edge(self, x, y, label=None):
-        """Add an edge from distribution *x* to distribution *y* with the given
-        *label*.
-
-        :type x: :class:`distutils2.database.InstalledDistribution` or
-                 :class:`distutils2.database.EggInfoDistribution`
-        :type y: :class:`distutils2.database.InstalledDistribution` or
-                 :class:`distutils2.database.EggInfoDistribution`
-        :type label: ``str`` or ``None``
-        """
-        self.adjacency_list[x].append((y, label))
-        # multiple edges are allowed, so be careful
-        if x not in self.reverse_list[y]:
-            self.reverse_list[y].append(x)
-
-    def add_missing(self, distribution, requirement):
-        """
-        Add a missing *requirement* for the given *distribution*.
-
-        :type distribution: :class:`distutils2.database.InstalledDistribution`
-                            or :class:`distutils2.database.EggInfoDistribution`
-        :type requirement: ``str``
-        """
-        logger.debug('%s missing %r', distribution, requirement)
-        self.missing.setdefault(distribution, []).append(requirement)
-
-    def _repr_dist(self, dist):
-        return '%s %s' % (dist.name, dist.version)
-
-    def repr_node(self, dist, level=1):
-        """Prints only a subgraph"""
-        output = [self._repr_dist(dist)]
-        for other, label in self.adjacency_list[dist]:
-            dist = self._repr_dist(other)
-            if label is not None:
-                dist = '%s [%s]' % (dist, label)
-            output.append('    ' * level + str(dist))
-            suboutput = self.repr_node(other, level + 1)
-            subs = suboutput.split('\n')
-            output.extend(subs[1:])
-        return '\n'.join(output)
-
-    def to_dot(self, f, skip_disconnected=True):
-        """Writes a DOT output for the graph to the provided file *f*.
-
-        If *skip_disconnected* is set to ``True``, then all distributions
-        that are not dependent on any other distribution are skipped.
-
-        :type f: has to support ``file``-like operations
-        :type skip_disconnected: ``bool``
-        """
-        disconnected = []
-
-        f.write("digraph dependencies {\n")
-        for dist, adjs in self.adjacency_list.items():
-            if len(adjs) == 0 and not skip_disconnected:
-                disconnected.append(dist)
-            for other, label in adjs:
-                if not label is None:
-                    f.write('"%s" -> "%s" [label="%s"]\n' %
-                            (dist.name, other.name, label))
-                else:
-                    f.write('"%s" -> "%s"\n' % (dist.name, other.name))
-        if not skip_disconnected and len(disconnected) > 0:
-            f.write('subgraph disconnected {\n')
-            f.write('label = "Disconnected"\n')
-            f.write('bgcolor = red\n')
-
-            for dist in disconnected:
-                f.write('"%s"' % dist.name)
-                f.write('\n')
-            f.write('}\n')
-        f.write('}\n')
-
-    def topological_sort(self):
-        """
-        Perform a topological sort of the graph.
-        :return: A tuple, the first element of which is a topologically sorted
-                 list of distributions, and the second element of which is a
-                 list of distributions that cannot be sorted because they have
-                 circular dependencies and so form a cycle.
-        """
-        result = []
-        # Make a shallow copy of the adjacency list
-        alist = {}
-        for k, v in self.adjacency_list.items():
-            alist[k] = v[:]
-        while True:
-            # See what we can remove in this run
-            to_remove = []
-            for k, v in list(alist.items())[:]:
-                if not v:
-                    to_remove.append(k)
-                    del alist[k]
-            if not to_remove:
-                # What's left in alist (if anything) is a cycle.
-                break
-            # Remove from the adjacency list of others
-            for k, v in alist.items():
-                alist[k] = [(d, r) for d, r in v if d not in to_remove]
-            logger.debug('Moving to result: %s',
-                         ['%s (%s)' % (d.name, d.version) for d in to_remove])
-            result.extend(to_remove)
-        return result, list(alist.keys())
-
-    def __repr__(self):
-        """Representation of the graph"""
-        output = []
-        for dist, adjs in self.adjacency_list.items():
-            output.append(self.repr_node(dist))
-        return '\n'.join(output)
-
-
-def make_graph(dists, scheme='default'):
-    """Makes a dependency graph from the given distributions.
-
-    :parameter dists: a list of distributions
-    :type dists: list of :class:`distutils2.database.InstalledDistribution` and
-                 :class:`distutils2.database.EggInfoDistribution` instances
-    :rtype: a :class:`DependencyGraph` instance
-    """
-    scheme = get_scheme(scheme)
-    graph = DependencyGraph()
-    provided = {}  # maps names to lists of (version, dist) tuples
-
-    # first, build the graph and find out what's provided
-    for dist in dists:
-        graph.add_distribution(dist)
-
-        for p in dist.provides:
-            name, version = parse_name_and_version(p)
-            logger.debug('Add to provided: %s, %s, %s', name, version, dist)
-            provided.setdefault(name, []).append((version, dist))
-
-    # now make the edges
-    for dist in dists:
-        requires = (dist.run_requires | dist.meta_requires |
-                    dist.build_requires | dist.dev_requires)
-        for req in requires:
-            try:
-                matcher = scheme.matcher(req)
-            except UnsupportedVersionError:
-                # XXX compat-mode if cannot read the version
-                logger.warning('could not read version %r - using name only',
-                               req)
-                name = req.split()[0]
-                matcher = scheme.matcher(name)
-
-            name = matcher.key   # case-insensitive
-
-            matched = False
-            if name in provided:
-                for version, provider in provided[name]:
-                    try:
-                        match = matcher.match(version)
-                    except UnsupportedVersionError:
-                        match = False
-
-                    if match:
-                        graph.add_edge(dist, provider, req)
-                        matched = True
-                        break
-            if not matched:
-                graph.add_missing(dist, req)
-    return graph
-
-
-def get_dependent_dists(dists, dist):
-    """Recursively generate a list of distributions from *dists* that are
-    dependent on *dist*.
-
-    :param dists: a list of distributions
-    :param dist: a distribution, member of *dists* for which we are interested
-    """
-    if dist not in dists:
-        raise DistlibException('given distribution %r is not a member '
-                               'of the list' % dist.name)
-    graph = make_graph(dists)
-
-    dep = [dist]  # dependent distributions
-    todo = graph.reverse_list[dist]  # list of nodes we should inspect
-
-    while todo:
-        d = todo.pop()
-        dep.append(d)
-        for succ in graph.reverse_list[d]:
-            if succ not in dep:
-                todo.append(succ)
-
-    dep.pop(0)  # remove dist from dep, was there to prevent infinite loops
-    return dep
-
-
-def get_required_dists(dists, dist):
-    """Recursively generate a list of distributions from *dists* that are
-    required by *dist*.
-
-    :param dists: a list of distributions
-    :param dist: a distribution, member of *dists* for which we are interested
-    """
-    if dist not in dists:
-        raise DistlibException('given distribution %r is not a member '
-                               'of the list' % dist.name)
-    graph = make_graph(dists)
-
-    req = []  # required distributions
-    todo = graph.adjacency_list[dist]  # list of nodes we should inspect
-
-    while todo:
-        d = todo.pop()[0]
-        req.append(d)
-        for pred in graph.adjacency_list[d]:
-            if pred not in req:
-                todo.append(pred)
-
-    return req
-
-
-def make_dist(name, version, **kwargs):
-    """
-    A convenience method for making a dist given just a name and version.
-    """
-    summary = kwargs.pop('summary', 'Placeholder for summary')
-    md = Metadata(**kwargs)
-    md.name = name
-    md.version = version
-    md.summary = summary or 'Placeholder for summary'
-    return Distribution(md)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/index.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/index.py
deleted file mode 100644
index 2406be2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/index.py
+++ /dev/null
@@ -1,516 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2013 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-import hashlib
-import logging
-import os
-import shutil
-import subprocess
-import tempfile
-try:
-    from threading import Thread
-except ImportError:
-    from dummy_threading import Thread
-
-from . import DistlibException
-from .compat import (HTTPBasicAuthHandler, Request, HTTPPasswordMgr,
-                     urlparse, build_opener, string_types)
-from .util import cached_property, zip_dir, ServerProxy
-
-logger = logging.getLogger(__name__)
-
-DEFAULT_INDEX = 'https://pypi.python.org/pypi'
-DEFAULT_REALM = 'pypi'
-
-class PackageIndex(object):
-    """
-    This class represents a package index compatible with PyPI, the Python
-    Package Index.
-    """
-
-    boundary = b'----------ThIs_Is_tHe_distlib_index_bouNdaRY_$'
-
-    def __init__(self, url=None):
-        """
-        Initialise an instance.
-
-        :param url: The URL of the index. If not specified, the URL for PyPI is
-                    used.
-        """
-        self.url = url or DEFAULT_INDEX
-        self.read_configuration()
-        scheme, netloc, path, params, query, frag = urlparse(self.url)
-        if params or query or frag or scheme not in ('http', 'https'):
-            raise DistlibException('invalid repository: %s' % self.url)
-        self.password_handler = None
-        self.ssl_verifier = None
-        self.gpg = None
-        self.gpg_home = None
-        with open(os.devnull, 'w') as sink:
-            # Use gpg by default rather than gpg2, as gpg2 insists on
-            # prompting for passwords
-            for s in ('gpg', 'gpg2'):
-                try:
-                    rc = subprocess.check_call([s, '--version'], stdout=sink,
-                                               stderr=sink)
-                    if rc == 0:
-                        self.gpg = s
-                        break
-                except OSError:
-                    pass
-
-    def _get_pypirc_command(self):
-        """
-        Get the distutils command for interacting with PyPI configurations.
-        :return: the command.
-        """
-        from distutils.core import Distribution
-        from distutils.config import PyPIRCCommand
-        d = Distribution()
-        return PyPIRCCommand(d)
-
-    def read_configuration(self):
-        """
-        Read the PyPI access configuration as supported by distutils, getting
-        PyPI to do the actual work. This populates ``username``, ``password``,
-        ``realm`` and ``url`` attributes from the configuration.
-        """
-        # get distutils to do the work
-        c = self._get_pypirc_command()
-        c.repository = self.url
-        cfg = c._read_pypirc()
-        self.username = cfg.get('username')
-        self.password = cfg.get('password')
-        self.realm = cfg.get('realm', 'pypi')
-        self.url = cfg.get('repository', self.url)
-
-    def save_configuration(self):
-        """
-        Save the PyPI access configuration. You must have set ``username`` and
-        ``password`` attributes before calling this method.
-
-        Again, distutils is used to do the actual work.
-        """
-        self.check_credentials()
-        # get distutils to do the work
-        c = self._get_pypirc_command()
-        c._store_pypirc(self.username, self.password)
-
-    def check_credentials(self):
-        """
-        Check that ``username`` and ``password`` have been set, and raise an
-        exception if not.
-        """
-        if self.username is None or self.password is None:
-            raise DistlibException('username and password must be set')
-        pm = HTTPPasswordMgr()
-        _, netloc, _, _, _, _ = urlparse(self.url)
-        pm.add_password(self.realm, netloc, self.username, self.password)
-        self.password_handler = HTTPBasicAuthHandler(pm)
-
-    def register(self, metadata):
-        """
-        Register a distribution on PyPI, using the provided metadata.
-
-        :param metadata: A :class:`Metadata` instance defining at least a name
-                         and version number for the distribution to be
-                         registered.
-        :return: The HTTP response received from PyPI upon submission of the
-                request.
-        """
-        self.check_credentials()
-        metadata.validate()
-        d = metadata.todict()
-        d[':action'] = 'verify'
-        request = self.encode_request(d.items(), [])
-        response = self.send_request(request)
-        d[':action'] = 'submit'
-        request = self.encode_request(d.items(), [])
-        return self.send_request(request)
-
-    def _reader(self, name, stream, outbuf):
-        """
-        Thread runner for reading lines of from a subprocess into a buffer.
-
-        :param name: The logical name of the stream (used for logging only).
-        :param stream: The stream to read from. This will typically a pipe
-                       connected to the output stream of a subprocess.
-        :param outbuf: The list to append the read lines to.
-        """
-        while True:
-            s = stream.readline()
-            if not s:
-                break
-            s = s.decode('utf-8').rstrip()
-            outbuf.append(s)
-            logger.debug('%s: %s' % (name, s))
-        stream.close()
-
-    def get_sign_command(self, filename, signer, sign_password,
-                         keystore=None):
-        """
-        Return a suitable command for signing a file.
-
-        :param filename: The pathname to the file to be signed.
-        :param signer: The identifier of the signer of the file.
-        :param sign_password: The passphrase for the signer's
-                              private key used for signing.
-        :param keystore: The path to a directory which contains the keys
-                         used in verification. If not specified, the
-                         instance's ``gpg_home`` attribute is used instead.
-        :return: The signing command as a list suitable to be
-                 passed to :class:`subprocess.Popen`.
-        """
-        cmd = [self.gpg, '--status-fd', '2', '--no-tty']
-        if keystore is None:
-            keystore = self.gpg_home
-        if keystore:
-            cmd.extend(['--homedir', keystore])
-        if sign_password is not None:
-            cmd.extend(['--batch', '--passphrase-fd', '0'])
-        td = tempfile.mkdtemp()
-        sf = os.path.join(td, os.path.basename(filename) + '.asc')
-        cmd.extend(['--detach-sign', '--armor', '--local-user',
-                    signer, '--output', sf, filename])
-        logger.debug('invoking: %s', ' '.join(cmd))
-        return cmd, sf
-
-    def run_command(self, cmd, input_data=None):
-        """
-        Run a command in a child process , passing it any input data specified.
-
-        :param cmd: The command to run.
-        :param input_data: If specified, this must be a byte string containing
-                           data to be sent to the child process.
-        :return: A tuple consisting of the subprocess' exit code, a list of
-                 lines read from the subprocess' ``stdout``, and a list of
-                 lines read from the subprocess' ``stderr``.
-        """
-        kwargs = {
-            'stdout': subprocess.PIPE,
-            'stderr': subprocess.PIPE,
-        }
-        if input_data is not None:
-            kwargs['stdin'] = subprocess.PIPE
-        stdout = []
-        stderr = []
-        p = subprocess.Popen(cmd, **kwargs)
-        # We don't use communicate() here because we may need to
-        # get clever with interacting with the command
-        t1 = Thread(target=self._reader, args=('stdout', p.stdout, stdout))
-        t1.start()
-        t2 = Thread(target=self._reader, args=('stderr', p.stderr, stderr))
-        t2.start()
-        if input_data is not None:
-            p.stdin.write(input_data)
-            p.stdin.close()
-
-        p.wait()
-        t1.join()
-        t2.join()
-        return p.returncode, stdout, stderr
-
-    def sign_file(self, filename, signer, sign_password, keystore=None):
-        """
-        Sign a file.
-
-        :param filename: The pathname to the file to be signed.
-        :param signer: The identifier of the signer of the file.
-        :param sign_password: The passphrase for the signer's
-                              private key used for signing.
-        :param keystore: The path to a directory which contains the keys
-                         used in signing. If not specified, the instance's
-                         ``gpg_home`` attribute is used instead.
-        :return: The absolute pathname of the file where the signature is
-                 stored.
-        """
-        cmd, sig_file = self.get_sign_command(filename, signer, sign_password,
-                                              keystore)
-        rc, stdout, stderr = self.run_command(cmd,
-                                              sign_password.encode('utf-8'))
-        if rc != 0:
-            raise DistlibException('sign command failed with error '
-                                   'code %s' % rc)
-        return sig_file
-
-    def upload_file(self, metadata, filename, signer=None, sign_password=None,
-                    filetype='sdist', pyversion='source', keystore=None):
-        """
-        Upload a release file to the index.
-
-        :param metadata: A :class:`Metadata` instance defining at least a name
-                         and version number for the file to be uploaded.
-        :param filename: The pathname of the file to be uploaded.
-        :param signer: The identifier of the signer of the file.
-        :param sign_password: The passphrase for the signer's
-                              private key used for signing.
-        :param filetype: The type of the file being uploaded. This is the
-                        distutils command which produced that file, e.g.
-                        ``sdist`` or ``bdist_wheel``.
-        :param pyversion: The version of Python which the release relates
-                          to. For code compatible with any Python, this would
-                          be ``source``, otherwise it would be e.g. ``3.2``.
-        :param keystore: The path to a directory which contains the keys
-                         used in signing. If not specified, the instance's
-                         ``gpg_home`` attribute is used instead.
-        :return: The HTTP response received from PyPI upon submission of the
-                request.
-        """
-        self.check_credentials()
-        if not os.path.exists(filename):
-            raise DistlibException('not found: %s' % filename)
-        metadata.validate()
-        d = metadata.todict()
-        sig_file = None
-        if signer:
-            if not self.gpg:
-                logger.warning('no signing program available - not signed')
-            else:
-                sig_file = self.sign_file(filename, signer, sign_password,
-                                          keystore)
-        with open(filename, 'rb') as f:
-            file_data = f.read()
-        md5_digest = hashlib.md5(file_data).hexdigest()
-        sha256_digest = hashlib.sha256(file_data).hexdigest()
-        d.update({
-            ':action': 'file_upload',
-            'protocol_version': '1',
-            'filetype': filetype,
-            'pyversion': pyversion,
-            'md5_digest': md5_digest,
-            'sha256_digest': sha256_digest,
-        })
-        files = [('content', os.path.basename(filename), file_data)]
-        if sig_file:
-            with open(sig_file, 'rb') as f:
-                sig_data = f.read()
-            files.append(('gpg_signature', os.path.basename(sig_file),
-                         sig_data))
-            shutil.rmtree(os.path.dirname(sig_file))
-        request = self.encode_request(d.items(), files)
-        return self.send_request(request)
-
-    def upload_documentation(self, metadata, doc_dir):
-        """
-        Upload documentation to the index.
-
-        :param metadata: A :class:`Metadata` instance defining at least a name
-                         and version number for the documentation to be
-                         uploaded.
-        :param doc_dir: The pathname of the directory which contains the
-                        documentation. This should be the directory that
-                        contains the ``index.html`` for the documentation.
-        :return: The HTTP response received from PyPI upon submission of the
-                request.
-        """
-        self.check_credentials()
-        if not os.path.isdir(doc_dir):
-            raise DistlibException('not a directory: %r' % doc_dir)
-        fn = os.path.join(doc_dir, 'index.html')
-        if not os.path.exists(fn):
-            raise DistlibException('not found: %r' % fn)
-        metadata.validate()
-        name, version = metadata.name, metadata.version
-        zip_data = zip_dir(doc_dir).getvalue()
-        fields = [(':action', 'doc_upload'),
-                  ('name', name), ('version', version)]
-        files = [('content', name, zip_data)]
-        request = self.encode_request(fields, files)
-        return self.send_request(request)
-
-    def get_verify_command(self, signature_filename, data_filename,
-                           keystore=None):
-        """
-        Return a suitable command for verifying a file.
-
-        :param signature_filename: The pathname to the file containing the
-                                   signature.
-        :param data_filename: The pathname to the file containing the
-                              signed data.
-        :param keystore: The path to a directory which contains the keys
-                         used in verification. If not specified, the
-                         instance's ``gpg_home`` attribute is used instead.
-        :return: The verifying command as a list suitable to be
-                 passed to :class:`subprocess.Popen`.
-        """
-        cmd = [self.gpg, '--status-fd', '2', '--no-tty']
-        if keystore is None:
-            keystore = self.gpg_home
-        if keystore:
-            cmd.extend(['--homedir', keystore])
-        cmd.extend(['--verify', signature_filename, data_filename])
-        logger.debug('invoking: %s', ' '.join(cmd))
-        return cmd
-
-    def verify_signature(self, signature_filename, data_filename,
-                         keystore=None):
-        """
-        Verify a signature for a file.
-
-        :param signature_filename: The pathname to the file containing the
-                                   signature.
-        :param data_filename: The pathname to the file containing the
-                              signed data.
-        :param keystore: The path to a directory which contains the keys
-                         used in verification. If not specified, the
-                         instance's ``gpg_home`` attribute is used instead.
-        :return: True if the signature was verified, else False.
-        """
-        if not self.gpg:
-            raise DistlibException('verification unavailable because gpg '
-                                   'unavailable')
-        cmd = self.get_verify_command(signature_filename, data_filename,
-                                      keystore)
-        rc, stdout, stderr = self.run_command(cmd)
-        if rc not in (0, 1):
-            raise DistlibException('verify command failed with error '
-                             'code %s' % rc)
-        return rc == 0
-
-    def download_file(self, url, destfile, digest=None, reporthook=None):
-        """
-        This is a convenience method for downloading a file from an URL.
-        Normally, this will be a file from the index, though currently
-        no check is made for this (i.e. a file can be downloaded from
-        anywhere).
-
-        The method is just like the :func:`urlretrieve` function in the
-        standard library, except that it allows digest computation to be
-        done during download and checking that the downloaded data
-        matched any expected value.
-
-        :param url: The URL of the file to be downloaded (assumed to be
-                    available via an HTTP GET request).
-        :param destfile: The pathname where the downloaded file is to be
-                         saved.
-        :param digest: If specified, this must be a (hasher, value)
-                       tuple, where hasher is the algorithm used (e.g.
-                       ``'md5'``) and ``value`` is the expected value.
-        :param reporthook: The same as for :func:`urlretrieve` in the
-                           standard library.
-        """
-        if digest is None:
-            digester = None
-            logger.debug('No digest specified')
-        else:
-            if isinstance(digest, (list, tuple)):
-                hasher, digest = digest
-            else:
-                hasher = 'md5'
-            digester = getattr(hashlib, hasher)()
-            logger.debug('Digest specified: %s' % digest)
-        # The following code is equivalent to urlretrieve.
-        # We need to do it this way so that we can compute the
-        # digest of the file as we go.
-        with open(destfile, 'wb') as dfp:
-            # addinfourl is not a context manager on 2.x
-            # so we have to use try/finally
-            sfp = self.send_request(Request(url))
-            try:
-                headers = sfp.info()
-                blocksize = 8192
-                size = -1
-                read = 0
-                blocknum = 0
-                if "content-length" in headers:
-                    size = int(headers["Content-Length"])
-                if reporthook:
-                    reporthook(blocknum, blocksize, size)
-                while True:
-                    block = sfp.read(blocksize)
-                    if not block:
-                        break
-                    read += len(block)
-                    dfp.write(block)
-                    if digester:
-                        digester.update(block)
-                    blocknum += 1
-                    if reporthook:
-                        reporthook(blocknum, blocksize, size)
-            finally:
-                sfp.close()
-
-        # check that we got the whole file, if we can
-        if size >= 0 and read < size:
-            raise DistlibException(
-                'retrieval incomplete: got only %d out of %d bytes'
-                % (read, size))
-        # if we have a digest, it must match.
-        if digester:
-            actual = digester.hexdigest()
-            if digest != actual:
-                raise DistlibException('%s digest mismatch for %s: expected '
-                                       '%s, got %s' % (hasher, destfile,
-                                                       digest, actual))
-            logger.debug('Digest verified: %s', digest)
-
-    def send_request(self, req):
-        """
-        Send a standard library :class:`Request` to PyPI and return its
-        response.
-
-        :param req: The request to send.
-        :return: The HTTP response from PyPI (a standard library HTTPResponse).
-        """
-        handlers = []
-        if self.password_handler:
-            handlers.append(self.password_handler)
-        if self.ssl_verifier:
-            handlers.append(self.ssl_verifier)
-        opener = build_opener(*handlers)
-        return opener.open(req)
-
-    def encode_request(self, fields, files):
-        """
-        Encode fields and files for posting to an HTTP server.
-
-        :param fields: The fields to send as a list of (fieldname, value)
-                       tuples.
-        :param files: The files to send as a list of (fieldname, filename,
-                      file_bytes) tuple.
-        """
-        # Adapted from packaging, which in turn was adapted from
-        # http://code.activestate.com/recipes/146306
-
-        parts = []
-        boundary = self.boundary
-        for k, values in fields:
-            if not isinstance(values, (list, tuple)):
-                values = [values]
-
-            for v in values:
-                parts.extend((
-                    b'--' + boundary,
-                    ('Content-Disposition: form-data; name="%s"' %
-                     k).encode('utf-8'),
-                    b'',
-                    v.encode('utf-8')))
-        for key, filename, value in files:
-            parts.extend((
-                b'--' + boundary,
-                ('Content-Disposition: form-data; name="%s"; filename="%s"' %
-                 (key, filename)).encode('utf-8'),
-                b'',
-                value))
-
-        parts.extend((b'--' + boundary + b'--', b''))
-
-        body = b'\r\n'.join(parts)
-        ct = b'multipart/form-data; boundary=' + boundary
-        headers = {
-            'Content-type': ct,
-            'Content-length': str(len(body))
-        }
-        return Request(self.url, body, headers)
-
-    def search(self, terms, operator=None):
-        if isinstance(terms, string_types):
-            terms = {'name': terms}
-        rpc_proxy = ServerProxy(self.url, timeout=3.0)
-        try:
-            return rpc_proxy.search(terms, operator or 'and')
-        finally:
-            rpc_proxy('close')()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/locators.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/locators.py
deleted file mode 100644
index 5c655c3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/locators.py
+++ /dev/null
@@ -1,1295 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012-2015 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-
-import gzip
-from io import BytesIO
-import json
-import logging
-import os
-import posixpath
-import re
-try:
-    import threading
-except ImportError:  # pragma: no cover
-    import dummy_threading as threading
-import zlib
-
-from . import DistlibException
-from .compat import (urljoin, urlparse, urlunparse, url2pathname, pathname2url,
-                     queue, quote, unescape, string_types, build_opener,
-                     HTTPRedirectHandler as BaseRedirectHandler, text_type,
-                     Request, HTTPError, URLError)
-from .database import Distribution, DistributionPath, make_dist
-from .metadata import Metadata, MetadataInvalidError
-from .util import (cached_property, parse_credentials, ensure_slash,
-                   split_filename, get_project_data, parse_requirement,
-                   parse_name_and_version, ServerProxy, normalize_name)
-from .version import get_scheme, UnsupportedVersionError
-from .wheel import Wheel, is_compatible
-
-logger = logging.getLogger(__name__)
-
-HASHER_HASH = re.compile(r'^(\w+)=([a-f0-9]+)')
-CHARSET = re.compile(r';\s*charset\s*=\s*(.*)\s*$', re.I)
-HTML_CONTENT_TYPE = re.compile('text/html|application/x(ht)?ml')
-DEFAULT_INDEX = 'https://pypi.python.org/pypi'
-
-def get_all_distribution_names(url=None):
-    """
-    Return all distribution names known by an index.
-    :param url: The URL of the index.
-    :return: A list of all known distribution names.
-    """
-    if url is None:
-        url = DEFAULT_INDEX
-    client = ServerProxy(url, timeout=3.0)
-    try:
-        return client.list_packages()
-    finally:
-        client('close')()
-
-class RedirectHandler(BaseRedirectHandler):
-    """
-    A class to work around a bug in some Python 3.2.x releases.
-    """
-    # There's a bug in the base version for some 3.2.x
-    # (e.g. 3.2.2 on Ubuntu Oneiric). If a Location header
-    # returns e.g. /abc, it bails because it says the scheme ''
-    # is bogus, when actually it should use the request's
-    # URL for the scheme. See Python issue #13696.
-    def http_error_302(self, req, fp, code, msg, headers):
-        # Some servers (incorrectly) return multiple Location headers
-        # (so probably same goes for URI).  Use first header.
-        newurl = None
-        for key in ('location', 'uri'):
-            if key in headers:
-                newurl = headers[key]
-                break
-        if newurl is None:  # pragma: no cover
-            return
-        urlparts = urlparse(newurl)
-        if urlparts.scheme == '':
-            newurl = urljoin(req.get_full_url(), newurl)
-            if hasattr(headers, 'replace_header'):
-                headers.replace_header(key, newurl)
-            else:
-                headers[key] = newurl
-        return BaseRedirectHandler.http_error_302(self, req, fp, code, msg,
-                                                  headers)
-
-    http_error_301 = http_error_303 = http_error_307 = http_error_302
-
-class Locator(object):
-    """
-    A base class for locators - things that locate distributions.
-    """
-    source_extensions = ('.tar.gz', '.tar.bz2', '.tar', '.zip', '.tgz', '.tbz')
-    binary_extensions = ('.egg', '.exe', '.whl')
-    excluded_extensions = ('.pdf',)
-
-    # A list of tags indicating which wheels you want to match. The default
-    # value of None matches against the tags compatible with the running
-    # Python. If you want to match other values, set wheel_tags on a locator
-    # instance to a list of tuples (pyver, abi, arch) which you want to match.
-    wheel_tags = None
-
-    downloadable_extensions = source_extensions + ('.whl',)
-
-    def __init__(self, scheme='default'):
-        """
-        Initialise an instance.
-        :param scheme: Because locators look for most recent versions, they
-                       need to know the version scheme to use. This specifies
-                       the current PEP-recommended scheme - use ``'legacy'``
-                       if you need to support existing distributions on PyPI.
-        """
-        self._cache = {}
-        self.scheme = scheme
-        # Because of bugs in some of the handlers on some of the platforms,
-        # we use our own opener rather than just using urlopen.
-        self.opener = build_opener(RedirectHandler())
-        # If get_project() is called from locate(), the matcher instance
-        # is set from the requirement passed to locate(). See issue #18 for
-        # why this can be useful to know.
-        self.matcher = None
-        self.errors = queue.Queue()
-
-    def get_errors(self):
-        """
-        Return any errors which have occurred.
-        """
-        result = []
-        while not self.errors.empty():  # pragma: no cover
-            try:
-                e = self.errors.get(False)
-                result.append(e)
-            except self.errors.Empty:
-                continue
-            self.errors.task_done()
-        return result
-
-    def clear_errors(self):
-        """
-        Clear any errors which may have been logged.
-        """
-        # Just get the errors and throw them away
-        self.get_errors()
-
-    def clear_cache(self):
-        self._cache.clear()
-
-    def _get_scheme(self):
-        return self._scheme
-
-    def _set_scheme(self, value):
-        self._scheme = value
-
-    scheme = property(_get_scheme, _set_scheme)
-
-    def _get_project(self, name):
-        """
-        For a given project, get a dictionary mapping available versions to Distribution
-        instances.
-
-        This should be implemented in subclasses.
-
-        If called from a locate() request, self.matcher will be set to a
-        matcher for the requirement to satisfy, otherwise it will be None.
-        """
-        raise NotImplementedError('Please implement in the subclass')
-
-    def get_distribution_names(self):
-        """
-        Return all the distribution names known to this locator.
-        """
-        raise NotImplementedError('Please implement in the subclass')
-
-    def get_project(self, name):
-        """
-        For a given project, get a dictionary mapping available versions to Distribution
-        instances.
-
-        This calls _get_project to do all the work, and just implements a caching layer on top.
-        """
-        if self._cache is None:  # pragma: no cover
-            result = self._get_project(name)
-        elif name in self._cache:
-            result = self._cache[name]
-        else:
-            self.clear_errors()
-            result = self._get_project(name)
-            self._cache[name] = result
-        return result
-
-    def score_url(self, url):
-        """
-        Give an url a score which can be used to choose preferred URLs
-        for a given project release.
-        """
-        t = urlparse(url)
-        basename = posixpath.basename(t.path)
-        compatible = True
-        is_wheel = basename.endswith('.whl')
-        is_downloadable = basename.endswith(self.downloadable_extensions)
-        if is_wheel:
-            compatible = is_compatible(Wheel(basename), self.wheel_tags)
-        return (t.scheme == 'https', 'pypi.python.org' in t.netloc,
-                is_downloadable, is_wheel, compatible, basename)
-
-    def prefer_url(self, url1, url2):
-        """
-        Choose one of two URLs where both are candidates for distribution
-        archives for the same version of a distribution (for example,
-        .tar.gz vs. zip).
-
-        The current implementation favours https:// URLs over http://, archives
-        from PyPI over those from other locations, wheel compatibility (if a
-        wheel) and then the archive name.
-        """
-        result = url2
-        if url1:
-            s1 = self.score_url(url1)
-            s2 = self.score_url(url2)
-            if s1 > s2:
-                result = url1
-            if result != url2:
-                logger.debug('Not replacing %r with %r', url1, url2)
-            else:
-                logger.debug('Replacing %r with %r', url1, url2)
-        return result
-
-    def split_filename(self, filename, project_name):
-        """
-        Attempt to split a filename in project name, version and Python version.
-        """
-        return split_filename(filename, project_name)
-
-    def convert_url_to_download_info(self, url, project_name):
-        """
-        See if a URL is a candidate for a download URL for a project (the URL
-        has typically been scraped from an HTML page).
-
-        If it is, a dictionary is returned with keys "name", "version",
-        "filename" and "url"; otherwise, None is returned.
-        """
-        def same_project(name1, name2):
-            return normalize_name(name1) == normalize_name(name2)
-
-        result = None
-        scheme, netloc, path, params, query, frag = urlparse(url)
-        if frag.lower().startswith('egg='):  # pragma: no cover
-            logger.debug('%s: version hint in fragment: %r',
-                         project_name, frag)
-        m = HASHER_HASH.match(frag)
-        if m:
-            algo, digest = m.groups()
-        else:
-            algo, digest = None, None
-        origpath = path
-        if path and path[-1] == '/':  # pragma: no cover
-            path = path[:-1]
-        if path.endswith('.whl'):
-            try:
-                wheel = Wheel(path)
-                if not is_compatible(wheel, self.wheel_tags):
-                    logger.debug('Wheel not compatible: %s', path)
-                else:
-                    if project_name is None:
-                        include = True
-                    else:
-                        include = same_project(wheel.name, project_name)
-                    if include:
-                        result = {
-                            'name': wheel.name,
-                            'version': wheel.version,
-                            'filename': wheel.filename,
-                            'url': urlunparse((scheme, netloc, origpath,
-                                               params, query, '')),
-                            'python-version': ', '.join(
-                                ['.'.join(list(v[2:])) for v in wheel.pyver]),
-                        }
-            except Exception as e:  # pragma: no cover
-                logger.warning('invalid path for wheel: %s', path)
-        elif not path.endswith(self.downloadable_extensions):  # pragma: no cover
-            logger.debug('Not downloadable: %s', path)
-        else:  # downloadable extension
-            path = filename = posixpath.basename(path)
-            for ext in self.downloadable_extensions:
-                if path.endswith(ext):
-                    path = path[:-len(ext)]
-                    t = self.split_filename(path, project_name)
-                    if not t:  # pragma: no cover
-                        logger.debug('No match for project/version: %s', path)
-                    else:
-                        name, version, pyver = t
-                        if not project_name or same_project(project_name, name):
-                            result = {
-                                'name': name,
-                                'version': version,
-                                'filename': filename,
-                                'url': urlunparse((scheme, netloc, origpath,
-                                                   params, query, '')),
-                                #'packagetype': 'sdist',
-                            }
-                            if pyver:  # pragma: no cover
-                                result['python-version'] = pyver
-                    break
-        if result and algo:
-            result['%s_digest' % algo] = digest
-        return result
-
-    def _get_digest(self, info):
-        """
-        Get a digest from a dictionary by looking at keys of the form
-        'algo_digest'.
-
-        Returns a 2-tuple (algo, digest) if found, else None. Currently
-        looks only for SHA256, then MD5.
-        """
-        result = None
-        for algo in ('sha256', 'md5'):
-            key = '%s_digest' % algo
-            if key in info:
-                result = (algo, info[key])
-                break
-        return result
-
-    def _update_version_data(self, result, info):
-        """
-        Update a result dictionary (the final result from _get_project) with a
-        dictionary for a specific version, which typically holds information
-        gleaned from a filename or URL for an archive for the distribution.
-        """
-        name = info.pop('name')
-        version = info.pop('version')
-        if version in result:
-            dist = result[version]
-            md = dist.metadata
-        else:
-            dist = make_dist(name, version, scheme=self.scheme)
-            md = dist.metadata
-        dist.digest = digest = self._get_digest(info)
-        url = info['url']
-        result['digests'][url] = digest
-        if md.source_url != info['url']:
-            md.source_url = self.prefer_url(md.source_url, url)
-            result['urls'].setdefault(version, set()).add(url)
-        dist.locator = self
-        result[version] = dist
-
-    def locate(self, requirement, prereleases=False):
-        """
-        Find the most recent distribution which matches the given
-        requirement.
-
-        :param requirement: A requirement of the form 'foo (1.0)' or perhaps
-                            'foo (>= 1.0, < 2.0, != 1.3)'
-        :param prereleases: If ``True``, allow pre-release versions
-                            to be located. Otherwise, pre-release versions
-                            are not returned.
-        :return: A :class:`Distribution` instance, or ``None`` if no such
-                 distribution could be located.
-        """
-        result = None
-        r = parse_requirement(requirement)
-        if r is None:  # pragma: no cover
-            raise DistlibException('Not a valid requirement: %r' % requirement)
-        scheme = get_scheme(self.scheme)
-        self.matcher = matcher = scheme.matcher(r.requirement)
-        logger.debug('matcher: %s (%s)', matcher, type(matcher).__name__)
-        versions = self.get_project(r.name)
-        if len(versions) > 2:   # urls and digests keys are present
-            # sometimes, versions are invalid
-            slist = []
-            vcls = matcher.version_class
-            for k in versions:
-                if k in ('urls', 'digests'):
-                    continue
-                try:
-                    if not matcher.match(k):
-                        logger.debug('%s did not match %r', matcher, k)
-                    else:
-                        if prereleases or not vcls(k).is_prerelease:
-                            slist.append(k)
-                        else:
-                            logger.debug('skipping pre-release '
-                                         'version %s of %s', k, matcher.name)
-                except Exception:  # pragma: no cover
-                    logger.warning('error matching %s with %r', matcher, k)
-                    pass # slist.append(k)
-            if len(slist) > 1:
-                slist = sorted(slist, key=scheme.key)
-            if slist:
-                logger.debug('sorted list: %s', slist)
-                version = slist[-1]
-                result = versions[version]
-        if result:
-            if r.extras:
-                result.extras = r.extras
-            result.download_urls = versions.get('urls', {}).get(version, set())
-            d = {}
-            sd = versions.get('digests', {})
-            for url in result.download_urls:
-                if url in sd:  # pragma: no cover
-                    d[url] = sd[url]
-            result.digests = d
-        self.matcher = None
-        return result
-
-
-class PyPIRPCLocator(Locator):
-    """
-    This locator uses XML-RPC to locate distributions. It therefore
-    cannot be used with simple mirrors (that only mirror file content).
-    """
-    def __init__(self, url, **kwargs):
-        """
-        Initialise an instance.
-
-        :param url: The URL to use for XML-RPC.
-        :param kwargs: Passed to the superclass constructor.
-        """
-        super(PyPIRPCLocator, self).__init__(**kwargs)
-        self.base_url = url
-        self.client = ServerProxy(url, timeout=3.0)
-
-    def get_distribution_names(self):
-        """
-        Return all the distribution names known to this locator.
-        """
-        return set(self.client.list_packages())
-
-    def _get_project(self, name):
-        result = {'urls': {}, 'digests': {}}
-        versions = self.client.package_releases(name, True)
-        for v in versions:
-            urls = self.client.release_urls(name, v)
-            data = self.client.release_data(name, v)
-            metadata = Metadata(scheme=self.scheme)
-            metadata.name = data['name']
-            metadata.version = data['version']
-            metadata.license = data.get('license')
-            metadata.keywords = data.get('keywords', [])
-            metadata.summary = data.get('summary')
-            dist = Distribution(metadata)
-            if urls:
-                info = urls[0]
-                metadata.source_url = info['url']
-                dist.digest = self._get_digest(info)
-                dist.locator = self
-                result[v] = dist
-                for info in urls:
-                    url = info['url']
-                    digest = self._get_digest(info)
-                    result['urls'].setdefault(v, set()).add(url)
-                    result['digests'][url] = digest
-        return result
-
-class PyPIJSONLocator(Locator):
-    """
-    This locator uses PyPI's JSON interface. It's very limited in functionality
-    and probably not worth using.
-    """
-    def __init__(self, url, **kwargs):
-        super(PyPIJSONLocator, self).__init__(**kwargs)
-        self.base_url = ensure_slash(url)
-
-    def get_distribution_names(self):
-        """
-        Return all the distribution names known to this locator.
-        """
-        raise NotImplementedError('Not available from this locator')
-
-    def _get_project(self, name):
-        result = {'urls': {}, 'digests': {}}
-        url = urljoin(self.base_url, '%s/json' % quote(name))
-        try:
-            resp = self.opener.open(url)
-            data = resp.read().decode() # for now
-            d = json.loads(data)
-            md = Metadata(scheme=self.scheme)
-            data = d['info']
-            md.name = data['name']
-            md.version = data['version']
-            md.license = data.get('license')
-            md.keywords = data.get('keywords', [])
-            md.summary = data.get('summary')
-            dist = Distribution(md)
-            dist.locator = self
-            urls = d['urls']
-            result[md.version] = dist
-            for info in d['urls']:
-                url = info['url']
-                dist.download_urls.add(url)
-                dist.digests[url] = self._get_digest(info)
-                result['urls'].setdefault(md.version, set()).add(url)
-                result['digests'][url] = self._get_digest(info)
-            # Now get other releases
-            for version, infos in d['releases'].items():
-                if version == md.version:
-                    continue    # already done
-                omd = Metadata(scheme=self.scheme)
-                omd.name = md.name
-                omd.version = version
-                odist = Distribution(omd)
-                odist.locator = self
-                result[version] = odist
-                for info in infos:
-                    url = info['url']
-                    odist.download_urls.add(url)
-                    odist.digests[url] = self._get_digest(info)
-                    result['urls'].setdefault(version, set()).add(url)
-                    result['digests'][url] = self._get_digest(info)
-#            for info in urls:
-#                md.source_url = info['url']
-#                dist.digest = self._get_digest(info)
-#                dist.locator = self
-#                for info in urls:
-#                    url = info['url']
-#                    result['urls'].setdefault(md.version, set()).add(url)
-#                    result['digests'][url] = self._get_digest(info)
-        except Exception as e:
-            self.errors.put(text_type(e))
-            logger.exception('JSON fetch failed: %s', e)
-        return result
-
-
-class Page(object):
-    """
-    This class represents a scraped HTML page.
-    """
-    # The following slightly hairy-looking regex just looks for the contents of
-    # an anchor link, which has an attribute "href" either immediately preceded
-    # or immediately followed by a "rel" attribute. The attribute values can be
-    # declared with double quotes, single quotes or no quotes - which leads to
-    # the length of the expression.
-    _href = re.compile("""
-(rel\\s*=\\s*(?:"(?P<rel1>[^"]*)"|'(?P<rel2>[^']*)'|(?P<rel3>[^>\\s\n]*))\\s+)?
-href\\s*=\\s*(?:"(?P<url1>[^"]*)"|'(?P<url2>[^']*)'|(?P<url3>[^>\\s\n]*))
-(\\s+rel\\s*=\\s*(?:"(?P<rel4>[^"]*)"|'(?P<rel5>[^']*)'|(?P<rel6>[^>\\s\n]*)))?
-""", re.I | re.S | re.X)
-    _base = re.compile(r"""<base\s+href\s*=\s*['"]?([^'">]+)""", re.I | re.S)
-
-    def __init__(self, data, url):
-        """
-        Initialise an instance with the Unicode page contents and the URL they
-        came from.
-        """
-        self.data = data
-        self.base_url = self.url = url
-        m = self._base.search(self.data)
-        if m:
-            self.base_url = m.group(1)
-
-    _clean_re = re.compile(r'[^a-z0-9$&+,/:;=?@.#%_\\|-]', re.I)
-
-    @cached_property
-    def links(self):
-        """
-        Return the URLs of all the links on a page together with information
-        about their "rel" attribute, for determining which ones to treat as
-        downloads and which ones to queue for further scraping.
-        """
-        def clean(url):
-            "Tidy up an URL."
-            scheme, netloc, path, params, query, frag = urlparse(url)
-            return urlunparse((scheme, netloc, quote(path),
-                               params, query, frag))
-
-        result = set()
-        for match in self._href.finditer(self.data):
-            d = match.groupdict('')
-            rel = (d['rel1'] or d['rel2'] or d['rel3'] or
-                   d['rel4'] or d['rel5'] or d['rel6'])
-            url = d['url1'] or d['url2'] or d['url3']
-            url = urljoin(self.base_url, url)
-            url = unescape(url)
-            url = self._clean_re.sub(lambda m: '%%%2x' % ord(m.group(0)), url)
-            result.add((url, rel))
-        # We sort the result, hoping to bring the most recent versions
-        # to the front
-        result = sorted(result, key=lambda t: t[0], reverse=True)
-        return result
-
-
-class SimpleScrapingLocator(Locator):
-    """
-    A locator which scrapes HTML pages to locate downloads for a distribution.
-    This runs multiple threads to do the I/O; performance is at least as good
-    as pip's PackageFinder, which works in an analogous fashion.
-    """
-
-    # These are used to deal with various Content-Encoding schemes.
-    decoders = {
-        'deflate': zlib.decompress,
-        'gzip': lambda b: gzip.GzipFile(fileobj=BytesIO(d)).read(),
-        'none': lambda b: b,
-    }
-
-    def __init__(self, url, timeout=None, num_workers=10, **kwargs):
-        """
-        Initialise an instance.
-        :param url: The root URL to use for scraping.
-        :param timeout: The timeout, in seconds, to be applied to requests.
-                        This defaults to ``None`` (no timeout specified).
-        :param num_workers: The number of worker threads you want to do I/O,
-                            This defaults to 10.
-        :param kwargs: Passed to the superclass.
-        """
-        super(SimpleScrapingLocator, self).__init__(**kwargs)
-        self.base_url = ensure_slash(url)
-        self.timeout = timeout
-        self._page_cache = {}
-        self._seen = set()
-        self._to_fetch = queue.Queue()
-        self._bad_hosts = set()
-        self.skip_externals = False
-        self.num_workers = num_workers
-        self._lock = threading.RLock()
-        # See issue #45: we need to be resilient when the locator is used
-        # in a thread, e.g. with concurrent.futures. We can't use self._lock
-        # as it is for coordinating our internal threads - the ones created
-        # in _prepare_threads.
-        self._gplock = threading.RLock()
-        self.platform_check = False  # See issue #112
-
-    def _prepare_threads(self):
-        """
-        Threads are created only when get_project is called, and terminate
-        before it returns. They are there primarily to parallelise I/O (i.e.
-        fetching web pages).
-        """
-        self._threads = []
-        for i in range(self.num_workers):
-            t = threading.Thread(target=self._fetch)
-            t.setDaemon(True)
-            t.start()
-            self._threads.append(t)
-
-    def _wait_threads(self):
-        """
-        Tell all the threads to terminate (by sending a sentinel value) and
-        wait for them to do so.
-        """
-        # Note that you need two loops, since you can't say which
-        # thread will get each sentinel
-        for t in self._threads:
-            self._to_fetch.put(None)    # sentinel
-        for t in self._threads:
-            t.join()
-        self._threads = []
-
-    def _get_project(self, name):
-        result = {'urls': {}, 'digests': {}}
-        with self._gplock:
-            self.result = result
-            self.project_name = name
-            url = urljoin(self.base_url, '%s/' % quote(name))
-            self._seen.clear()
-            self._page_cache.clear()
-            self._prepare_threads()
-            try:
-                logger.debug('Queueing %s', url)
-                self._to_fetch.put(url)
-                self._to_fetch.join()
-            finally:
-                self._wait_threads()
-            del self.result
-        return result
-
-    platform_dependent = re.compile(r'\b(linux_(i\d86|x86_64|arm\w+)|'
-                                    r'win(32|_amd64)|macosx_?\d+)\b', re.I)
-
-    def _is_platform_dependent(self, url):
-        """
-        Does an URL refer to a platform-specific download?
-        """
-        return self.platform_dependent.search(url)
-
-    def _process_download(self, url):
-        """
-        See if an URL is a suitable download for a project.
-
-        If it is, register information in the result dictionary (for
-        _get_project) about the specific version it's for.
-
-        Note that the return value isn't actually used other than as a boolean
-        value.
-        """
-        if self.platform_check and self._is_platform_dependent(url):
-            info = None
-        else:
-            info = self.convert_url_to_download_info(url, self.project_name)
-        logger.debug('process_download: %s -> %s', url, info)
-        if info:
-            with self._lock:    # needed because self.result is shared
-                self._update_version_data(self.result, info)
-        return info
-
-    def _should_queue(self, link, referrer, rel):
-        """
-        Determine whether a link URL from a referring page and with a
-        particular "rel" attribute should be queued for scraping.
-        """
-        scheme, netloc, path, _, _, _ = urlparse(link)
-        if path.endswith(self.source_extensions + self.binary_extensions +
-                         self.excluded_extensions):
-            result = False
-        elif self.skip_externals and not link.startswith(self.base_url):
-            result = False
-        elif not referrer.startswith(self.base_url):
-            result = False
-        elif rel not in ('homepage', 'download'):
-            result = False
-        elif scheme not in ('http', 'https', 'ftp'):
-            result = False
-        elif self._is_platform_dependent(link):
-            result = False
-        else:
-            host = netloc.split(':', 1)[0]
-            if host.lower() == 'localhost':
-                result = False
-            else:
-                result = True
-        logger.debug('should_queue: %s (%s) from %s -> %s', link, rel,
-                     referrer, result)
-        return result
-
-    def _fetch(self):
-        """
-        Get a URL to fetch from the work queue, get the HTML page, examine its
-        links for download candidates and candidates for further scraping.
-
-        This is a handy method to run in a thread.
-        """
-        while True:
-            url = self._to_fetch.get()
-            try:
-                if url:
-                    page = self.get_page(url)
-                    if page is None:    # e.g. after an error
-                        continue
-                    for link, rel in page.links:
-                        if link not in self._seen:
-                            try:
-                                self._seen.add(link)
-                                if (not self._process_download(link) and
-                                    self._should_queue(link, url, rel)):
-                                    logger.debug('Queueing %s from %s', link, url)
-                                    self._to_fetch.put(link)
-                            except MetadataInvalidError:  # e.g. invalid versions
-                                pass
-            except Exception as e:  # pragma: no cover
-                self.errors.put(text_type(e))
-            finally:
-                # always do this, to avoid hangs :-)
-                self._to_fetch.task_done()
-            if not url:
-                #logger.debug('Sentinel seen, quitting.')
-                break
-
-    def get_page(self, url):
-        """
-        Get the HTML for an URL, possibly from an in-memory cache.
-
-        XXX TODO Note: this cache is never actually cleared. It's assumed that
-        the data won't get stale over the lifetime of a locator instance (not
-        necessarily true for the default_locator).
-        """
-        # http://peak.telecommunity.com/DevCenter/EasyInstall#package-index-api
-        scheme, netloc, path, _, _, _ = urlparse(url)
-        if scheme == 'file' and os.path.isdir(url2pathname(path)):
-            url = urljoin(ensure_slash(url), 'index.html')
-
-        if url in self._page_cache:
-            result = self._page_cache[url]
-            logger.debug('Returning %s from cache: %s', url, result)
-        else:
-            host = netloc.split(':', 1)[0]
-            result = None
-            if host in self._bad_hosts:
-                logger.debug('Skipping %s due to bad host %s', url, host)
-            else:
-                req = Request(url, headers={'Accept-encoding': 'identity'})
-                try:
-                    logger.debug('Fetching %s', url)
-                    resp = self.opener.open(req, timeout=self.timeout)
-                    logger.debug('Fetched %s', url)
-                    headers = resp.info()
-                    content_type = headers.get('Content-Type', '')
-                    if HTML_CONTENT_TYPE.match(content_type):
-                        final_url = resp.geturl()
-                        data = resp.read()
-                        encoding = headers.get('Content-Encoding')
-                        if encoding:
-                            decoder = self.decoders[encoding]   # fail if not found
-                            data = decoder(data)
-                        encoding = 'utf-8'
-                        m = CHARSET.search(content_type)
-                        if m:
-                            encoding = m.group(1)
-                        try:
-                            data = data.decode(encoding)
-                        except UnicodeError:  # pragma: no cover
-                            data = data.decode('latin-1')    # fallback
-                        result = Page(data, final_url)
-                        self._page_cache[final_url] = result
-                except HTTPError as e:
-                    if e.code != 404:
-                        logger.exception('Fetch failed: %s: %s', url, e)
-                except URLError as e:  # pragma: no cover
-                    logger.exception('Fetch failed: %s: %s', url, e)
-                    with self._lock:
-                        self._bad_hosts.add(host)
-                except Exception as e:  # pragma: no cover
-                    logger.exception('Fetch failed: %s: %s', url, e)
-                finally:
-                    self._page_cache[url] = result   # even if None (failure)
-        return result
-
-    _distname_re = re.compile('<a href=[^>]*>([^<]+)<')
-
-    def get_distribution_names(self):
-        """
-        Return all the distribution names known to this locator.
-        """
-        result = set()
-        page = self.get_page(self.base_url)
-        if not page:
-            raise DistlibException('Unable to get %s' % self.base_url)
-        for match in self._distname_re.finditer(page.data):
-            result.add(match.group(1))
-        return result
-
-class DirectoryLocator(Locator):
-    """
-    This class locates distributions in a directory tree.
-    """
-
-    def __init__(self, path, **kwargs):
-        """
-        Initialise an instance.
-        :param path: The root of the directory tree to search.
-        :param kwargs: Passed to the superclass constructor,
-                       except for:
-                       * recursive - if True (the default), subdirectories are
-                         recursed into. If False, only the top-level directory
-                         is searched,
-        """
-        self.recursive = kwargs.pop('recursive', True)
-        super(DirectoryLocator, self).__init__(**kwargs)
-        path = os.path.abspath(path)
-        if not os.path.isdir(path):  # pragma: no cover
-            raise DistlibException('Not a directory: %r' % path)
-        self.base_dir = path
-
-    def should_include(self, filename, parent):
-        """
-        Should a filename be considered as a candidate for a distribution
-        archive? As well as the filename, the directory which contains it
-        is provided, though not used by the current implementation.
-        """
-        return filename.endswith(self.downloadable_extensions)
-
-    def _get_project(self, name):
-        result = {'urls': {}, 'digests': {}}
-        for root, dirs, files in os.walk(self.base_dir):
-            for fn in files:
-                if self.should_include(fn, root):
-                    fn = os.path.join(root, fn)
-                    url = urlunparse(('file', '',
-                                      pathname2url(os.path.abspath(fn)),
-                                      '', '', ''))
-                    info = self.convert_url_to_download_info(url, name)
-                    if info:
-                        self._update_version_data(result, info)
-            if not self.recursive:
-                break
-        return result
-
-    def get_distribution_names(self):
-        """
-        Return all the distribution names known to this locator.
-        """
-        result = set()
-        for root, dirs, files in os.walk(self.base_dir):
-            for fn in files:
-                if self.should_include(fn, root):
-                    fn = os.path.join(root, fn)
-                    url = urlunparse(('file', '',
-                                      pathname2url(os.path.abspath(fn)),
-                                      '', '', ''))
-                    info = self.convert_url_to_download_info(url, None)
-                    if info:
-                        result.add(info['name'])
-            if not self.recursive:
-                break
-        return result
-
-class JSONLocator(Locator):
-    """
-    This locator uses special extended metadata (not available on PyPI) and is
-    the basis of performant dependency resolution in distlib. Other locators
-    require archive downloads before dependencies can be determined! As you
-    might imagine, that can be slow.
-    """
-    def get_distribution_names(self):
-        """
-        Return all the distribution names known to this locator.
-        """
-        raise NotImplementedError('Not available from this locator')
-
-    def _get_project(self, name):
-        result = {'urls': {}, 'digests': {}}
-        data = get_project_data(name)
-        if data:
-            for info in data.get('files', []):
-                if info['ptype'] != 'sdist' or info['pyversion'] != 'source':
-                    continue
-                # We don't store summary in project metadata as it makes
-                # the data bigger for no benefit during dependency
-                # resolution
-                dist = make_dist(data['name'], info['version'],
-                                 summary=data.get('summary',
-                                                  'Placeholder for summary'),
-                                 scheme=self.scheme)
-                md = dist.metadata
-                md.source_url = info['url']
-                # TODO SHA256 digest
-                if 'digest' in info and info['digest']:
-                    dist.digest = ('md5', info['digest'])
-                md.dependencies = info.get('requirements', {})
-                dist.exports = info.get('exports', {})
-                result[dist.version] = dist
-                result['urls'].setdefault(dist.version, set()).add(info['url'])
-        return result
-
-class DistPathLocator(Locator):
-    """
-    This locator finds installed distributions in a path. It can be useful for
-    adding to an :class:`AggregatingLocator`.
-    """
-    def __init__(self, distpath, **kwargs):
-        """
-        Initialise an instance.
-
-        :param distpath: A :class:`DistributionPath` instance to search.
-        """
-        super(DistPathLocator, self).__init__(**kwargs)
-        assert isinstance(distpath, DistributionPath)
-        self.distpath = distpath
-
-    def _get_project(self, name):
-        dist = self.distpath.get_distribution(name)
-        if dist is None:
-            result = {'urls': {}, 'digests': {}}
-        else:
-            result = {
-                dist.version: dist,
-                'urls': {dist.version: set([dist.source_url])},
-                'digests': {dist.version: set([None])}
-            }
-        return result
-
-
-class AggregatingLocator(Locator):
-    """
-    This class allows you to chain and/or merge a list of locators.
-    """
-    def __init__(self, *locators, **kwargs):
-        """
-        Initialise an instance.
-
-        :param locators: The list of locators to search.
-        :param kwargs: Passed to the superclass constructor,
-                       except for:
-                       * merge - if False (the default), the first successful
-                         search from any of the locators is returned. If True,
-                         the results from all locators are merged (this can be
-                         slow).
-        """
-        self.merge = kwargs.pop('merge', False)
-        self.locators = locators
-        super(AggregatingLocator, self).__init__(**kwargs)
-
-    def clear_cache(self):
-        super(AggregatingLocator, self).clear_cache()
-        for locator in self.locators:
-            locator.clear_cache()
-
-    def _set_scheme(self, value):
-        self._scheme = value
-        for locator in self.locators:
-            locator.scheme = value
-
-    scheme = property(Locator.scheme.fget, _set_scheme)
-
-    def _get_project(self, name):
-        result = {}
-        for locator in self.locators:
-            d = locator.get_project(name)
-            if d:
-                if self.merge:
-                    files = result.get('urls', {})
-                    digests = result.get('digests', {})
-                    # next line could overwrite result['urls'], result['digests']
-                    result.update(d)
-                    df = result.get('urls')
-                    if files and df:
-                        for k, v in files.items():
-                            if k in df:
-                                df[k] |= v
-                            else:
-                                df[k] = v
-                    dd = result.get('digests')
-                    if digests and dd:
-                        dd.update(digests)
-                else:
-                    # See issue #18. If any dists are found and we're looking
-                    # for specific constraints, we only return something if
-                    # a match is found. For example, if a DirectoryLocator
-                    # returns just foo (1.0) while we're looking for
-                    # foo (>= 2.0), we'll pretend there was nothing there so
-                    # that subsequent locators can be queried. Otherwise we
-                    # would just return foo (1.0) which would then lead to a
-                    # failure to find foo (>= 2.0), because other locators
-                    # weren't searched. Note that this only matters when
-                    # merge=False.
-                    if self.matcher is None:
-                        found = True
-                    else:
-                        found = False
-                        for k in d:
-                            if self.matcher.match(k):
-                                found = True
-                                break
-                    if found:
-                        result = d
-                        break
-        return result
-
-    def get_distribution_names(self):
-        """
-        Return all the distribution names known to this locator.
-        """
-        result = set()
-        for locator in self.locators:
-            try:
-                result |= locator.get_distribution_names()
-            except NotImplementedError:
-                pass
-        return result
-
-
-# We use a legacy scheme simply because most of the dists on PyPI use legacy
-# versions which don't conform to PEP 426 / PEP 440.
-default_locator = AggregatingLocator(
-                    JSONLocator(),
-                    SimpleScrapingLocator('https://pypi.python.org/simple/',
-                                          timeout=3.0),
-                    scheme='legacy')
-
-locate = default_locator.locate
-
-NAME_VERSION_RE = re.compile(r'(?P<name>[\w-]+)\s*'
-                             r'\(\s*(==\s*)?(?P<ver>[^)]+)\)$')
-
-class DependencyFinder(object):
-    """
-    Locate dependencies for distributions.
-    """
-
-    def __init__(self, locator=None):
-        """
-        Initialise an instance, using the specified locator
-        to locate distributions.
-        """
-        self.locator = locator or default_locator
-        self.scheme = get_scheme(self.locator.scheme)
-
-    def add_distribution(self, dist):
-        """
-        Add a distribution to the finder. This will update internal information
-        about who provides what.
-        :param dist: The distribution to add.
-        """
-        logger.debug('adding distribution %s', dist)
-        name = dist.key
-        self.dists_by_name[name] = dist
-        self.dists[(name, dist.version)] = dist
-        for p in dist.provides:
-            name, version = parse_name_and_version(p)
-            logger.debug('Add to provided: %s, %s, %s', name, version, dist)
-            self.provided.setdefault(name, set()).add((version, dist))
-
-    def remove_distribution(self, dist):
-        """
-        Remove a distribution from the finder. This will update internal
-        information about who provides what.
-        :param dist: The distribution to remove.
-        """
-        logger.debug('removing distribution %s', dist)
-        name = dist.key
-        del self.dists_by_name[name]
-        del self.dists[(name, dist.version)]
-        for p in dist.provides:
-            name, version = parse_name_and_version(p)
-            logger.debug('Remove from provided: %s, %s, %s', name, version, dist)
-            s = self.provided[name]
-            s.remove((version, dist))
-            if not s:
-                del self.provided[name]
-
-    def get_matcher(self, reqt):
-        """
-        Get a version matcher for a requirement.
-        :param reqt: The requirement
-        :type reqt: str
-        :return: A version matcher (an instance of
-                 :class:`distlib.version.Matcher`).
-        """
-        try:
-            matcher = self.scheme.matcher(reqt)
-        except UnsupportedVersionError:  # pragma: no cover
-            # XXX compat-mode if cannot read the version
-            name = reqt.split()[0]
-            matcher = self.scheme.matcher(name)
-        return matcher
-
-    def find_providers(self, reqt):
-        """
-        Find the distributions which can fulfill a requirement.
-
-        :param reqt: The requirement.
-         :type reqt: str
-        :return: A set of distribution which can fulfill the requirement.
-        """
-        matcher = self.get_matcher(reqt)
-        name = matcher.key   # case-insensitive
-        result = set()
-        provided = self.provided
-        if name in provided:
-            for version, provider in provided[name]:
-                try:
-                    match = matcher.match(version)
-                except UnsupportedVersionError:
-                    match = False
-
-                if match:
-                    result.add(provider)
-                    break
-        return result
-
-    def try_to_replace(self, provider, other, problems):
-        """
-        Attempt to replace one provider with another. This is typically used
-        when resolving dependencies from multiple sources, e.g. A requires
-        (B >= 1.0) while C requires (B >= 1.1).
-
-        For successful replacement, ``provider`` must meet all the requirements
-        which ``other`` fulfills.
-
-        :param provider: The provider we are trying to replace with.
-        :param other: The provider we're trying to replace.
-        :param problems: If False is returned, this will contain what
-                         problems prevented replacement. This is currently
-                         a tuple of the literal string 'cantreplace',
-                         ``provider``, ``other``  and the set of requirements
-                         that ``provider`` couldn't fulfill.
-        :return: True if we can replace ``other`` with ``provider``, else
-                 False.
-        """
-        rlist = self.reqts[other]
-        unmatched = set()
-        for s in rlist:
-            matcher = self.get_matcher(s)
-            if not matcher.match(provider.version):
-                unmatched.add(s)
-        if unmatched:
-            # can't replace other with provider
-            problems.add(('cantreplace', provider, other,
-                          frozenset(unmatched)))
-            result = False
-        else:
-            # can replace other with provider
-            self.remove_distribution(other)
-            del self.reqts[other]
-            for s in rlist:
-                self.reqts.setdefault(provider, set()).add(s)
-            self.add_distribution(provider)
-            result = True
-        return result
-
-    def find(self, requirement, meta_extras=None, prereleases=False):
-        """
-        Find a distribution and all distributions it depends on.
-
-        :param requirement: The requirement specifying the distribution to
-                            find, or a Distribution instance.
-        :param meta_extras: A list of meta extras such as :test:, :build: and
-                            so on.
-        :param prereleases: If ``True``, allow pre-release versions to be
-                            returned - otherwise, don't return prereleases
-                            unless they're all that's available.
-
-        Return a set of :class:`Distribution` instances and a set of
-        problems.
-
-        The distributions returned should be such that they have the
-        :attr:`required` attribute set to ``True`` if they were
-        from the ``requirement`` passed to ``find()``, and they have the
-        :attr:`build_time_dependency` attribute set to ``True`` unless they
-        are post-installation dependencies of the ``requirement``.
-
-        The problems should be a tuple consisting of the string
-        ``'unsatisfied'`` and the requirement which couldn't be satisfied
-        by any distribution known to the locator.
-        """
-
-        self.provided = {}
-        self.dists = {}
-        self.dists_by_name = {}
-        self.reqts = {}
-
-        meta_extras = set(meta_extras or [])
-        if ':*:' in meta_extras:
-            meta_extras.remove(':*:')
-            # :meta: and :run: are implicitly included
-            meta_extras |= set([':test:', ':build:', ':dev:'])
-
-        if isinstance(requirement, Distribution):
-            dist = odist = requirement
-            logger.debug('passed %s as requirement', odist)
-        else:
-            dist = odist = self.locator.locate(requirement,
-                                               prereleases=prereleases)
-            if dist is None:
-                raise DistlibException('Unable to locate %r' % requirement)
-            logger.debug('located %s', odist)
-        dist.requested = True
-        problems = set()
-        todo = set([dist])
-        install_dists = set([odist])
-        while todo:
-            dist = todo.pop()
-            name = dist.key     # case-insensitive
-            if name not in self.dists_by_name:
-                self.add_distribution(dist)
-            else:
-                #import pdb; pdb.set_trace()
-                other = self.dists_by_name[name]
-                if other != dist:
-                    self.try_to_replace(dist, other, problems)
-
-            ireqts = dist.run_requires | dist.meta_requires
-            sreqts = dist.build_requires
-            ereqts = set()
-            if meta_extras and dist in install_dists:
-                for key in ('test', 'build', 'dev'):
-                    e = ':%s:' % key
-                    if e in meta_extras:
-                        ereqts |= getattr(dist, '%s_requires' % key)
-            all_reqts = ireqts | sreqts | ereqts
-            for r in all_reqts:
-                providers = self.find_providers(r)
-                if not providers:
-                    logger.debug('No providers found for %r', r)
-                    provider = self.locator.locate(r, prereleases=prereleases)
-                    # If no provider is found and we didn't consider
-                    # prereleases, consider them now.
-                    if provider is None and not prereleases:
-                        provider = self.locator.locate(r, prereleases=True)
-                    if provider is None:
-                        logger.debug('Cannot satisfy %r', r)
-                        problems.add(('unsatisfied', r))
-                    else:
-                        n, v = provider.key, provider.version
-                        if (n, v) not in self.dists:
-                            todo.add(provider)
-                        providers.add(provider)
-                        if r in ireqts and dist in install_dists:
-                            install_dists.add(provider)
-                            logger.debug('Adding %s to install_dists',
-                                         provider.name_and_version)
-                for p in providers:
-                    name = p.key
-                    if name not in self.dists_by_name:
-                        self.reqts.setdefault(p, set()).add(r)
-                    else:
-                        other = self.dists_by_name[name]
-                        if other != p:
-                            # see if other can be replaced by p
-                            self.try_to_replace(p, other, problems)
-
-        dists = set(self.dists.values())
-        for dist in dists:
-            dist.build_time_dependency = dist not in install_dists
-            if dist.build_time_dependency:
-                logger.debug('%s is a build-time dependency only.',
-                             dist.name_and_version)
-        logger.debug('find done for %s', odist)
-        return dists, problems
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/manifest.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/manifest.py
deleted file mode 100644
index ca0fe44..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/manifest.py
+++ /dev/null
@@ -1,393 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012-2013 Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""
-Class representing the list of files in a distribution.
-
-Equivalent to distutils.filelist, but fixes some problems.
-"""
-import fnmatch
-import logging
-import os
-import re
-import sys
-
-from . import DistlibException
-from .compat import fsdecode
-from .util import convert_path
-
-
-__all__ = ['Manifest']
-
-logger = logging.getLogger(__name__)
-
-# a \ followed by some spaces + EOL
-_COLLAPSE_PATTERN = re.compile('\\\\w*\n', re.M)
-_COMMENTED_LINE = re.compile('#.*?(?=\n)|\n(?=$)', re.M | re.S)
-
-#
-# Due to the different results returned by fnmatch.translate, we need
-# to do slightly different processing for Python 2.7 and 3.2 ... this needed
-# to be brought in for Python 3.6 onwards.
-#
-_PYTHON_VERSION = sys.version_info[:2]
-
-class Manifest(object):
-    """A list of files built by on exploring the filesystem and filtered by
-    applying various patterns to what we find there.
-    """
-
-    def __init__(self, base=None):
-        """
-        Initialise an instance.
-
-        :param base: The base directory to explore under.
-        """
-        self.base = os.path.abspath(os.path.normpath(base or os.getcwd()))
-        self.prefix = self.base + os.sep
-        self.allfiles = None
-        self.files = set()
-
-    #
-    # Public API
-    #
-
-    def findall(self):
-        """Find all files under the base and set ``allfiles`` to the absolute
-        pathnames of files found.
-        """
-        from stat import S_ISREG, S_ISDIR, S_ISLNK
-
-        self.allfiles = allfiles = []
-        root = self.base
-        stack = [root]
-        pop = stack.pop
-        push = stack.append
-
-        while stack:
-            root = pop()
-            names = os.listdir(root)
-
-            for name in names:
-                fullname = os.path.join(root, name)
-
-                # Avoid excess stat calls -- just one will do, thank you!
-                stat = os.stat(fullname)
-                mode = stat.st_mode
-                if S_ISREG(mode):
-                    allfiles.append(fsdecode(fullname))
-                elif S_ISDIR(mode) and not S_ISLNK(mode):
-                    push(fullname)
-
-    def add(self, item):
-        """
-        Add a file to the manifest.
-
-        :param item: The pathname to add. This can be relative to the base.
-        """
-        if not item.startswith(self.prefix):
-            item = os.path.join(self.base, item)
-        self.files.add(os.path.normpath(item))
-
-    def add_many(self, items):
-        """
-        Add a list of files to the manifest.
-
-        :param items: The pathnames to add. These can be relative to the base.
-        """
-        for item in items:
-            self.add(item)
-
-    def sorted(self, wantdirs=False):
-        """
-        Return sorted files in directory order
-        """
-
-        def add_dir(dirs, d):
-            dirs.add(d)
-            logger.debug('add_dir added %s', d)
-            if d != self.base:
-                parent, _ = os.path.split(d)
-                assert parent not in ('', '/')
-                add_dir(dirs, parent)
-
-        result = set(self.files)    # make a copy!
-        if wantdirs:
-            dirs = set()
-            for f in result:
-                add_dir(dirs, os.path.dirname(f))
-            result |= dirs
-        return [os.path.join(*path_tuple) for path_tuple in
-                sorted(os.path.split(path) for path in result)]
-
-    def clear(self):
-        """Clear all collected files."""
-        self.files = set()
-        self.allfiles = []
-
-    def process_directive(self, directive):
-        """
-        Process a directive which either adds some files from ``allfiles`` to
-        ``files``, or removes some files from ``files``.
-
-        :param directive: The directive to process. This should be in a format
-                     compatible with distutils ``MANIFEST.in`` files:
-
-                     http://docs.python.org/distutils/sourcedist.html#commands
-        """
-        # Parse the line: split it up, make sure the right number of words
-        # is there, and return the relevant words.  'action' is always
-        # defined: it's the first word of the line.  Which of the other
-        # three are defined depends on the action; it'll be either
-        # patterns, (dir and patterns), or (dirpattern).
-        action, patterns, thedir, dirpattern = self._parse_directive(directive)
-
-        # OK, now we know that the action is valid and we have the
-        # right number of words on the line for that action -- so we
-        # can proceed with minimal error-checking.
-        if action == 'include':
-            for pattern in patterns:
-                if not self._include_pattern(pattern, anchor=True):
-                    logger.warning('no files found matching %r', pattern)
-
-        elif action == 'exclude':
-            for pattern in patterns:
-                found = self._exclude_pattern(pattern, anchor=True)
-                #if not found:
-                #    logger.warning('no previously-included files '
-                #                   'found matching %r', pattern)
-
-        elif action == 'global-include':
-            for pattern in patterns:
-                if not self._include_pattern(pattern, anchor=False):
-                    logger.warning('no files found matching %r '
-                                   'anywhere in distribution', pattern)
-
-        elif action == 'global-exclude':
-            for pattern in patterns:
-                found = self._exclude_pattern(pattern, anchor=False)
-                #if not found:
-                #    logger.warning('no previously-included files '
-                #                   'matching %r found anywhere in '
-                #                   'distribution', pattern)
-
-        elif action == 'recursive-include':
-            for pattern in patterns:
-                if not self._include_pattern(pattern, prefix=thedir):
-                    logger.warning('no files found matching %r '
-                                   'under directory %r', pattern, thedir)
-
-        elif action == 'recursive-exclude':
-            for pattern in patterns:
-                found = self._exclude_pattern(pattern, prefix=thedir)
-                #if not found:
-                #    logger.warning('no previously-included files '
-                #                   'matching %r found under directory %r',
-                #                   pattern, thedir)
-
-        elif action == 'graft':
-            if not self._include_pattern(None, prefix=dirpattern):
-                logger.warning('no directories found matching %r',
-                               dirpattern)
-
-        elif action == 'prune':
-            if not self._exclude_pattern(None, prefix=dirpattern):
-                logger.warning('no previously-included directories found '
-                               'matching %r', dirpattern)
-        else:   # pragma: no cover
-            # This should never happen, as it should be caught in
-            # _parse_template_line
-            raise DistlibException(
-                'invalid action %r' % action)
-
-    #
-    # Private API
-    #
-
-    def _parse_directive(self, directive):
-        """
-        Validate a directive.
-        :param directive: The directive to validate.
-        :return: A tuple of action, patterns, thedir, dir_patterns
-        """
-        words = directive.split()
-        if len(words) == 1 and words[0] not in ('include', 'exclude',
-                                                'global-include',
-                                                'global-exclude',
-                                                'recursive-include',
-                                                'recursive-exclude',
-                                                'graft', 'prune'):
-            # no action given, let's use the default 'include'
-            words.insert(0, 'include')
-
-        action = words[0]
-        patterns = thedir = dir_pattern = None
-
-        if action in ('include', 'exclude',
-                      'global-include', 'global-exclude'):
-            if len(words) < 2:
-                raise DistlibException(
-                    '%r expects <pattern1> <pattern2> ...' % action)
-
-            patterns = [convert_path(word) for word in words[1:]]
-
-        elif action in ('recursive-include', 'recursive-exclude'):
-            if len(words) < 3:
-                raise DistlibException(
-                    '%r expects <dir> <pattern1> <pattern2> ...' % action)
-
-            thedir = convert_path(words[1])
-            patterns = [convert_path(word) for word in words[2:]]
-
-        elif action in ('graft', 'prune'):
-            if len(words) != 2:
-                raise DistlibException(
-                    '%r expects a single <dir_pattern>' % action)
-
-            dir_pattern = convert_path(words[1])
-
-        else:
-            raise DistlibException('unknown action %r' % action)
-
-        return action, patterns, thedir, dir_pattern
-
-    def _include_pattern(self, pattern, anchor=True, prefix=None,
-                         is_regex=False):
-        """Select strings (presumably filenames) from 'self.files' that
-        match 'pattern', a Unix-style wildcard (glob) pattern.
-
-        Patterns are not quite the same as implemented by the 'fnmatch'
-        module: '*' and '?'  match non-special characters, where "special"
-        is platform-dependent: slash on Unix; colon, slash, and backslash on
-        DOS/Windows; and colon on Mac OS.
-
-        If 'anchor' is true (the default), then the pattern match is more
-        stringent: "*.py" will match "foo.py" but not "foo/bar.py".  If
-        'anchor' is false, both of these will match.
-
-        If 'prefix' is supplied, then only filenames starting with 'prefix'
-        (itself a pattern) and ending with 'pattern', with anything in between
-        them, will match.  'anchor' is ignored in this case.
-
-        If 'is_regex' is true, 'anchor' and 'prefix' are ignored, and
-        'pattern' is assumed to be either a string containing a regex or a
-        regex object -- no translation is done, the regex is just compiled
-        and used as-is.
-
-        Selected strings will be added to self.files.
-
-        Return True if files are found.
-        """
-        # XXX docstring lying about what the special chars are?
-        found = False
-        pattern_re = self._translate_pattern(pattern, anchor, prefix, is_regex)
-
-        # delayed loading of allfiles list
-        if self.allfiles is None:
-            self.findall()
-
-        for name in self.allfiles:
-            if pattern_re.search(name):
-                self.files.add(name)
-                found = True
-        return found
-
-    def _exclude_pattern(self, pattern, anchor=True, prefix=None,
-                         is_regex=False):
-        """Remove strings (presumably filenames) from 'files' that match
-        'pattern'.
-
-        Other parameters are the same as for 'include_pattern()', above.
-        The list 'self.files' is modified in place. Return True if files are
-        found.
-
-        This API is public to allow e.g. exclusion of SCM subdirs, e.g. when
-        packaging source distributions
-        """
-        found = False
-        pattern_re = self._translate_pattern(pattern, anchor, prefix, is_regex)
-        for f in list(self.files):
-            if pattern_re.search(f):
-                self.files.remove(f)
-                found = True
-        return found
-
-    def _translate_pattern(self, pattern, anchor=True, prefix=None,
-                           is_regex=False):
-        """Translate a shell-like wildcard pattern to a compiled regular
-        expression.
-
-        Return the compiled regex.  If 'is_regex' true,
-        then 'pattern' is directly compiled to a regex (if it's a string)
-        or just returned as-is (assumes it's a regex object).
-        """
-        if is_regex:
-            if isinstance(pattern, str):
-                return re.compile(pattern)
-            else:
-                return pattern
-
-        if _PYTHON_VERSION > (3, 2):
-            # ditch start and end characters
-            start, _, end = self._glob_to_re('_').partition('_')
-
-        if pattern:
-            pattern_re = self._glob_to_re(pattern)
-            if _PYTHON_VERSION > (3, 2):
-                assert pattern_re.startswith(start) and pattern_re.endswith(end)
-        else:
-            pattern_re = ''
-
-        base = re.escape(os.path.join(self.base, ''))
-        if prefix is not None:
-            # ditch end of pattern character
-            if _PYTHON_VERSION <= (3, 2):
-                empty_pattern = self._glob_to_re('')
-                prefix_re = self._glob_to_re(prefix)[:-len(empty_pattern)]
-            else:
-                prefix_re = self._glob_to_re(prefix)
-                assert prefix_re.startswith(start) and prefix_re.endswith(end)
-                prefix_re = prefix_re[len(start): len(prefix_re) - len(end)]
-            sep = os.sep
-            if os.sep == '\\':
-                sep = r'\\'
-            if _PYTHON_VERSION <= (3, 2):
-                pattern_re = '^' + base + sep.join((prefix_re,
-                                                    '.*' + pattern_re))
-            else:
-                pattern_re = pattern_re[len(start): len(pattern_re) - len(end)]
-                pattern_re = r'%s%s%s%s.*%s%s' % (start, base, prefix_re, sep,
-                                                  pattern_re, end)
-        else:  # no prefix -- respect anchor flag
-            if anchor:
-                if _PYTHON_VERSION <= (3, 2):
-                    pattern_re = '^' + base + pattern_re
-                else:
-                    pattern_re = r'%s%s%s' % (start, base, pattern_re[len(start):])
-
-        return re.compile(pattern_re)
-
-    def _glob_to_re(self, pattern):
-        """Translate a shell-like glob pattern to a regular expression.
-
-        Return a string containing the regex.  Differs from
-        'fnmatch.translate()' in that '*' does not match "special characters"
-        (which are platform-specific).
-        """
-        pattern_re = fnmatch.translate(pattern)
-
-        # '?' and '*' in the glob pattern become '.' and '.*' in the RE, which
-        # IMHO is wrong -- '?' and '*' aren't supposed to match slash in Unix,
-        # and by extension they shouldn't match such "special characters" under
-        # any OS.  So change all non-escaped dots in the RE to match any
-        # character except the special characters (currently: just os.sep).
-        sep = os.sep
-        if os.sep == '\\':
-            # we're using a regex to manipulate a regex, so we need
-            # to escape the backslash twice
-            sep = r'\\\\'
-        escaped = r'\1[^%s]' % sep
-        pattern_re = re.sub(r'((?<!\\)(\\\\)*)\.', escaped, pattern_re)
-        return pattern_re
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/markers.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/markers.py
deleted file mode 100644
index ee1f3e2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/markers.py
+++ /dev/null
@@ -1,131 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012-2017 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""
-Parser for the environment markers micro-language defined in PEP 508.
-"""
-
-# Note: In PEP 345, the micro-language was Python compatible, so the ast
-# module could be used to parse it. However, PEP 508 introduced operators such
-# as ~= and === which aren't in Python, necessitating a different approach.
-
-import os
-import sys
-import platform
-import re
-
-from .compat import python_implementation, urlparse, string_types
-from .util import in_venv, parse_marker
-
-__all__ = ['interpret']
-
-def _is_literal(o):
-    if not isinstance(o, string_types) or not o:
-        return False
-    return o[0] in '\'"'
-
-class Evaluator(object):
-    """
-    This class is used to evaluate marker expessions.
-    """
-
-    operations = {
-        '==': lambda x, y: x == y,
-        '===': lambda x, y: x == y,
-        '~=': lambda x, y: x == y or x > y,
-        '!=': lambda x, y: x != y,
-        '<':  lambda x, y: x < y,
-        '<=':  lambda x, y: x == y or x < y,
-        '>':  lambda x, y: x > y,
-        '>=':  lambda x, y: x == y or x > y,
-        'and': lambda x, y: x and y,
-        'or': lambda x, y: x or y,
-        'in': lambda x, y: x in y,
-        'not in': lambda x, y: x not in y,
-    }
-
-    def evaluate(self, expr, context):
-        """
-        Evaluate a marker expression returned by the :func:`parse_requirement`
-        function in the specified context.
-        """
-        if isinstance(expr, string_types):
-            if expr[0] in '\'"':
-                result = expr[1:-1]
-            else:
-                if expr not in context:
-                    raise SyntaxError('unknown variable: %s' % expr)
-                result = context[expr]
-        else:
-            assert isinstance(expr, dict)
-            op = expr['op']
-            if op not in self.operations:
-                raise NotImplementedError('op not implemented: %s' % op)
-            elhs = expr['lhs']
-            erhs = expr['rhs']
-            if _is_literal(expr['lhs']) and _is_literal(expr['rhs']):
-                raise SyntaxError('invalid comparison: %s %s %s' % (elhs, op, erhs))
-
-            lhs = self.evaluate(elhs, context)
-            rhs = self.evaluate(erhs, context)
-            result = self.operations[op](lhs, rhs)
-        return result
-
-def default_context():
-    def format_full_version(info):
-        version = '%s.%s.%s' % (info.major, info.minor, info.micro)
-        kind = info.releaselevel
-        if kind != 'final':
-            version += kind[0] + str(info.serial)
-        return version
-
-    if hasattr(sys, 'implementation'):
-        implementation_version = format_full_version(sys.implementation.version)
-        implementation_name = sys.implementation.name
-    else:
-        implementation_version = '0'
-        implementation_name = ''
-
-    result = {
-        'implementation_name': implementation_name,
-        'implementation_version': implementation_version,
-        'os_name': os.name,
-        'platform_machine': platform.machine(),
-        'platform_python_implementation': platform.python_implementation(),
-        'platform_release': platform.release(),
-        'platform_system': platform.system(),
-        'platform_version': platform.version(),
-        'platform_in_venv': str(in_venv()),
-        'python_full_version': platform.python_version(),
-        'python_version': platform.python_version()[:3],
-        'sys_platform': sys.platform,
-    }
-    return result
-
-DEFAULT_CONTEXT = default_context()
-del default_context
-
-evaluator = Evaluator()
-
-def interpret(marker, execution_context=None):
-    """
-    Interpret a marker and return a result depending on environment.
-
-    :param marker: The marker to interpret.
-    :type marker: str
-    :param execution_context: The context used for name lookup.
-    :type execution_context: mapping
-    """
-    try:
-        expr, rest = parse_marker(marker)
-    except Exception as e:
-        raise SyntaxError('Unable to interpret marker syntax: %s: %s' % (marker, e))
-    if rest and rest[0] != '#':
-        raise SyntaxError('unexpected trailing data in marker: %s: %s' % (marker, rest))
-    context = dict(DEFAULT_CONTEXT)
-    if execution_context:
-        context.update(execution_context)
-    return evaluator.evaluate(expr, context)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/metadata.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/metadata.py
deleted file mode 100644
index 77eed7f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/metadata.py
+++ /dev/null
@@ -1,1094 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012 The Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""Implementation of the Metadata for Python packages PEPs.
-
-Supports all metadata formats (1.0, 1.1, 1.2, and 2.0 experimental).
-"""
-from __future__ import unicode_literals
-
-import codecs
-from email import message_from_file
-import json
-import logging
-import re
-
-
-from . import DistlibException, __version__
-from .compat import StringIO, string_types, text_type
-from .markers import interpret
-from .util import extract_by_key, get_extras
-from .version import get_scheme, PEP440_VERSION_RE
-
-logger = logging.getLogger(__name__)
-
-
-class MetadataMissingError(DistlibException):
-    """A required metadata is missing"""
-
-
-class MetadataConflictError(DistlibException):
-    """Attempt to read or write metadata fields that are conflictual."""
-
-
-class MetadataUnrecognizedVersionError(DistlibException):
-    """Unknown metadata version number."""
-
-
-class MetadataInvalidError(DistlibException):
-    """A metadata value is invalid"""
-
-# public API of this module
-__all__ = ['Metadata', 'PKG_INFO_ENCODING', 'PKG_INFO_PREFERRED_VERSION']
-
-# Encoding used for the PKG-INFO files
-PKG_INFO_ENCODING = 'utf-8'
-
-# preferred version. Hopefully will be changed
-# to 1.2 once PEP 345 is supported everywhere
-PKG_INFO_PREFERRED_VERSION = '1.1'
-
-_LINE_PREFIX_1_2 = re.compile('\n       \\|')
-_LINE_PREFIX_PRE_1_2 = re.compile('\n        ')
-_241_FIELDS = ('Metadata-Version', 'Name', 'Version', 'Platform',
-               'Summary', 'Description',
-               'Keywords', 'Home-page', 'Author', 'Author-email',
-               'License')
-
-_314_FIELDS = ('Metadata-Version', 'Name', 'Version', 'Platform',
-               'Supported-Platform', 'Summary', 'Description',
-               'Keywords', 'Home-page', 'Author', 'Author-email',
-               'License', 'Classifier', 'Download-URL', 'Obsoletes',
-               'Provides', 'Requires')
-
-_314_MARKERS = ('Obsoletes', 'Provides', 'Requires', 'Classifier',
-                'Download-URL')
-
-_345_FIELDS = ('Metadata-Version', 'Name', 'Version', 'Platform',
-               'Supported-Platform', 'Summary', 'Description',
-               'Keywords', 'Home-page', 'Author', 'Author-email',
-               'Maintainer', 'Maintainer-email', 'License',
-               'Classifier', 'Download-URL', 'Obsoletes-Dist',
-               'Project-URL', 'Provides-Dist', 'Requires-Dist',
-               'Requires-Python', 'Requires-External')
-
-_345_MARKERS = ('Provides-Dist', 'Requires-Dist', 'Requires-Python',
-                'Obsoletes-Dist', 'Requires-External', 'Maintainer',
-                'Maintainer-email', 'Project-URL')
-
-_426_FIELDS = ('Metadata-Version', 'Name', 'Version', 'Platform',
-               'Supported-Platform', 'Summary', 'Description',
-               'Keywords', 'Home-page', 'Author', 'Author-email',
-               'Maintainer', 'Maintainer-email', 'License',
-               'Classifier', 'Download-URL', 'Obsoletes-Dist',
-               'Project-URL', 'Provides-Dist', 'Requires-Dist',
-               'Requires-Python', 'Requires-External', 'Private-Version',
-               'Obsoleted-By', 'Setup-Requires-Dist', 'Extension',
-               'Provides-Extra')
-
-_426_MARKERS = ('Private-Version', 'Provides-Extra', 'Obsoleted-By',
-                'Setup-Requires-Dist', 'Extension')
-
-# See issue #106: Sometimes 'Requires' occurs wrongly in the metadata. Include
-# it in the tuple literal below to allow it (for now)
-_566_FIELDS = _426_FIELDS + ('Description-Content-Type', 'Requires')
-
-_566_MARKERS = ('Description-Content-Type',)
-
-_ALL_FIELDS = set()
-_ALL_FIELDS.update(_241_FIELDS)
-_ALL_FIELDS.update(_314_FIELDS)
-_ALL_FIELDS.update(_345_FIELDS)
-_ALL_FIELDS.update(_426_FIELDS)
-_ALL_FIELDS.update(_566_FIELDS)
-
-EXTRA_RE = re.compile(r'''extra\s*==\s*("([^"]+)"|'([^']+)')''')
-
-
-def _version2fieldlist(version):
-    if version == '1.0':
-        return _241_FIELDS
-    elif version == '1.1':
-        return _314_FIELDS
-    elif version == '1.2':
-        return _345_FIELDS
-    elif version in ('1.3', '2.1'):
-        return _345_FIELDS + _566_FIELDS
-    elif version == '2.0':
-        return _426_FIELDS
-    raise MetadataUnrecognizedVersionError(version)
-
-
-def _best_version(fields):
-    """Detect the best version depending on the fields used."""
-    def _has_marker(keys, markers):
-        for marker in markers:
-            if marker in keys:
-                return True
-        return False
-
-    keys = []
-    for key, value in fields.items():
-        if value in ([], 'UNKNOWN', None):
-            continue
-        keys.append(key)
-
-    possible_versions = ['1.0', '1.1', '1.2', '1.3', '2.0', '2.1']
-
-    # first let's try to see if a field is not part of one of the version
-    for key in keys:
-        if key not in _241_FIELDS and '1.0' in possible_versions:
-            possible_versions.remove('1.0')
-            logger.debug('Removed 1.0 due to %s', key)
-        if key not in _314_FIELDS and '1.1' in possible_versions:
-            possible_versions.remove('1.1')
-            logger.debug('Removed 1.1 due to %s', key)
-        if key not in _345_FIELDS and '1.2' in possible_versions:
-            possible_versions.remove('1.2')
-            logger.debug('Removed 1.2 due to %s', key)
-        if key not in _566_FIELDS and '1.3' in possible_versions:
-            possible_versions.remove('1.3')
-            logger.debug('Removed 1.3 due to %s', key)
-        if key not in _566_FIELDS and '2.1' in possible_versions:
-            if key != 'Description':  # In 2.1, description allowed after headers
-                possible_versions.remove('2.1')
-                logger.debug('Removed 2.1 due to %s', key)
-        if key not in _426_FIELDS and '2.0' in possible_versions:
-            possible_versions.remove('2.0')
-            logger.debug('Removed 2.0 due to %s', key)
-
-    # possible_version contains qualified versions
-    if len(possible_versions) == 1:
-        return possible_versions[0]   # found !
-    elif len(possible_versions) == 0:
-        logger.debug('Out of options - unknown metadata set: %s', fields)
-        raise MetadataConflictError('Unknown metadata set')
-
-    # let's see if one unique marker is found
-    is_1_1 = '1.1' in possible_versions and _has_marker(keys, _314_MARKERS)
-    is_1_2 = '1.2' in possible_versions and _has_marker(keys, _345_MARKERS)
-    is_2_1 = '2.1' in possible_versions and _has_marker(keys, _566_MARKERS)
-    is_2_0 = '2.0' in possible_versions and _has_marker(keys, _426_MARKERS)
-    if int(is_1_1) + int(is_1_2) + int(is_2_1) + int(is_2_0) > 1:
-        raise MetadataConflictError('You used incompatible 1.1/1.2/2.0/2.1 fields')
-
-    # we have the choice, 1.0, or 1.2, or 2.0
-    #   - 1.0 has a broken Summary field but works with all tools
-    #   - 1.1 is to avoid
-    #   - 1.2 fixes Summary but has little adoption
-    #   - 2.0 adds more features and is very new
-    if not is_1_1 and not is_1_2 and not is_2_1 and not is_2_0:
-        # we couldn't find any specific marker
-        if PKG_INFO_PREFERRED_VERSION in possible_versions:
-            return PKG_INFO_PREFERRED_VERSION
-    if is_1_1:
-        return '1.1'
-    if is_1_2:
-        return '1.2'
-    if is_2_1:
-        return '2.1'
-
-    return '2.0'
-
-_ATTR2FIELD = {
-    'metadata_version': 'Metadata-Version',
-    'name': 'Name',
-    'version': 'Version',
-    'platform': 'Platform',
-    'supported_platform': 'Supported-Platform',
-    'summary': 'Summary',
-    'description': 'Description',
-    'keywords': 'Keywords',
-    'home_page': 'Home-page',
-    'author': 'Author',
-    'author_email': 'Author-email',
-    'maintainer': 'Maintainer',
-    'maintainer_email': 'Maintainer-email',
-    'license': 'License',
-    'classifier': 'Classifier',
-    'download_url': 'Download-URL',
-    'obsoletes_dist': 'Obsoletes-Dist',
-    'provides_dist': 'Provides-Dist',
-    'requires_dist': 'Requires-Dist',
-    'setup_requires_dist': 'Setup-Requires-Dist',
-    'requires_python': 'Requires-Python',
-    'requires_external': 'Requires-External',
-    'requires': 'Requires',
-    'provides': 'Provides',
-    'obsoletes': 'Obsoletes',
-    'project_url': 'Project-URL',
-    'private_version': 'Private-Version',
-    'obsoleted_by': 'Obsoleted-By',
-    'extension': 'Extension',
-    'provides_extra': 'Provides-Extra',
-}
-
-_PREDICATE_FIELDS = ('Requires-Dist', 'Obsoletes-Dist', 'Provides-Dist')
-_VERSIONS_FIELDS = ('Requires-Python',)
-_VERSION_FIELDS = ('Version',)
-_LISTFIELDS = ('Platform', 'Classifier', 'Obsoletes',
-               'Requires', 'Provides', 'Obsoletes-Dist',
-               'Provides-Dist', 'Requires-Dist', 'Requires-External',
-               'Project-URL', 'Supported-Platform', 'Setup-Requires-Dist',
-               'Provides-Extra', 'Extension')
-_LISTTUPLEFIELDS = ('Project-URL',)
-
-_ELEMENTSFIELD = ('Keywords',)
-
-_UNICODEFIELDS = ('Author', 'Maintainer', 'Summary', 'Description')
-
-_MISSING = object()
-
-_FILESAFE = re.compile('[^A-Za-z0-9.]+')
-
-
-def _get_name_and_version(name, version, for_filename=False):
-    """Return the distribution name with version.
-
-    If for_filename is true, return a filename-escaped form."""
-    if for_filename:
-        # For both name and version any runs of non-alphanumeric or '.'
-        # characters are replaced with a single '-'.  Additionally any
-        # spaces in the version string become '.'
-        name = _FILESAFE.sub('-', name)
-        version = _FILESAFE.sub('-', version.replace(' ', '.'))
-    return '%s-%s' % (name, version)
-
-
-class LegacyMetadata(object):
-    """The legacy metadata of a release.
-
-    Supports versions 1.0, 1.1 and 1.2 (auto-detected). You can
-    instantiate the class with one of these arguments (or none):
-    - *path*, the path to a metadata file
-    - *fileobj* give a file-like object with metadata as content
-    - *mapping* is a dict-like object
-    - *scheme* is a version scheme name
-    """
-    # TODO document the mapping API and UNKNOWN default key
-
-    def __init__(self, path=None, fileobj=None, mapping=None,
-                 scheme='default'):
-        if [path, fileobj, mapping].count(None) < 2:
-            raise TypeError('path, fileobj and mapping are exclusive')
-        self._fields = {}
-        self.requires_files = []
-        self._dependencies = None
-        self.scheme = scheme
-        if path is not None:
-            self.read(path)
-        elif fileobj is not None:
-            self.read_file(fileobj)
-        elif mapping is not None:
-            self.update(mapping)
-            self.set_metadata_version()
-
-    def set_metadata_version(self):
-        self._fields['Metadata-Version'] = _best_version(self._fields)
-
-    def _write_field(self, fileobj, name, value):
-        fileobj.write('%s: %s\n' % (name, value))
-
-    def __getitem__(self, name):
-        return self.get(name)
-
-    def __setitem__(self, name, value):
-        return self.set(name, value)
-
-    def __delitem__(self, name):
-        field_name = self._convert_name(name)
-        try:
-            del self._fields[field_name]
-        except KeyError:
-            raise KeyError(name)
-
-    def __contains__(self, name):
-        return (name in self._fields or
-                self._convert_name(name) in self._fields)
-
-    def _convert_name(self, name):
-        if name in _ALL_FIELDS:
-            return name
-        name = name.replace('-', '_').lower()
-        return _ATTR2FIELD.get(name, name)
-
-    def _default_value(self, name):
-        if name in _LISTFIELDS or name in _ELEMENTSFIELD:
-            return []
-        return 'UNKNOWN'
-
-    def _remove_line_prefix(self, value):
-        if self.metadata_version in ('1.0', '1.1'):
-            return _LINE_PREFIX_PRE_1_2.sub('\n', value)
-        else:
-            return _LINE_PREFIX_1_2.sub('\n', value)
-
-    def __getattr__(self, name):
-        if name in _ATTR2FIELD:
-            return self[name]
-        raise AttributeError(name)
-
-    #
-    # Public API
-    #
-
-#    dependencies = property(_get_dependencies, _set_dependencies)
-
-    def get_fullname(self, filesafe=False):
-        """Return the distribution name with version.
-
-        If filesafe is true, return a filename-escaped form."""
-        return _get_name_and_version(self['Name'], self['Version'], filesafe)
-
-    def is_field(self, name):
-        """return True if name is a valid metadata key"""
-        name = self._convert_name(name)
-        return name in _ALL_FIELDS
-
-    def is_multi_field(self, name):
-        name = self._convert_name(name)
-        return name in _LISTFIELDS
-
-    def read(self, filepath):
-        """Read the metadata values from a file path."""
-        fp = codecs.open(filepath, 'r', encoding='utf-8')
-        try:
-            self.read_file(fp)
-        finally:
-            fp.close()
-
-    def read_file(self, fileob):
-        """Read the metadata values from a file object."""
-        msg = message_from_file(fileob)
-        self._fields['Metadata-Version'] = msg['metadata-version']
-
-        # When reading, get all the fields we can
-        for field in _ALL_FIELDS:
-            if field not in msg:
-                continue
-            if field in _LISTFIELDS:
-                # we can have multiple lines
-                values = msg.get_all(field)
-                if field in _LISTTUPLEFIELDS and values is not None:
-                    values = [tuple(value.split(',')) for value in values]
-                self.set(field, values)
-            else:
-                # single line
-                value = msg[field]
-                if value is not None and value != 'UNKNOWN':
-                    self.set(field, value)
-        # logger.debug('Attempting to set metadata for %s', self)
-        # self.set_metadata_version()
-
-    def write(self, filepath, skip_unknown=False):
-        """Write the metadata fields to filepath."""
-        fp = codecs.open(filepath, 'w', encoding='utf-8')
-        try:
-            self.write_file(fp, skip_unknown)
-        finally:
-            fp.close()
-
-    def write_file(self, fileobject, skip_unknown=False):
-        """Write the PKG-INFO format data to a file object."""
-        self.set_metadata_version()
-
-        for field in _version2fieldlist(self['Metadata-Version']):
-            values = self.get(field)
-            if skip_unknown and values in ('UNKNOWN', [], ['UNKNOWN']):
-                continue
-            if field in _ELEMENTSFIELD:
-                self._write_field(fileobject, field, ','.join(values))
-                continue
-            if field not in _LISTFIELDS:
-                if field == 'Description':
-                    if self.metadata_version in ('1.0', '1.1'):
-                        values = values.replace('\n', '\n        ')
-                    else:
-                        values = values.replace('\n', '\n       |')
-                values = [values]
-
-            if field in _LISTTUPLEFIELDS:
-                values = [','.join(value) for value in values]
-
-            for value in values:
-                self._write_field(fileobject, field, value)
-
-    def update(self, other=None, **kwargs):
-        """Set metadata values from the given iterable `other` and kwargs.
-
-        Behavior is like `dict.update`: If `other` has a ``keys`` method,
-        they are looped over and ``self[key]`` is assigned ``other[key]``.
-        Else, ``other`` is an iterable of ``(key, value)`` iterables.
-
-        Keys that don't match a metadata field or that have an empty value are
-        dropped.
-        """
-        def _set(key, value):
-            if key in _ATTR2FIELD and value:
-                self.set(self._convert_name(key), value)
-
-        if not other:
-            # other is None or empty container
-            pass
-        elif hasattr(other, 'keys'):
-            for k in other.keys():
-                _set(k, other[k])
-        else:
-            for k, v in other:
-                _set(k, v)
-
-        if kwargs:
-            for k, v in kwargs.items():
-                _set(k, v)
-
-    def set(self, name, value):
-        """Control then set a metadata field."""
-        name = self._convert_name(name)
-
-        if ((name in _ELEMENTSFIELD or name == 'Platform') and
-            not isinstance(value, (list, tuple))):
-            if isinstance(value, string_types):
-                value = [v.strip() for v in value.split(',')]
-            else:
-                value = []
-        elif (name in _LISTFIELDS and
-              not isinstance(value, (list, tuple))):
-            if isinstance(value, string_types):
-                value = [value]
-            else:
-                value = []
-
-        if logger.isEnabledFor(logging.WARNING):
-            project_name = self['Name']
-
-            scheme = get_scheme(self.scheme)
-            if name in _PREDICATE_FIELDS and value is not None:
-                for v in value:
-                    # check that the values are valid
-                    if not scheme.is_valid_matcher(v.split(';')[0]):
-                        logger.warning(
-                            "'%s': '%s' is not valid (field '%s')",
-                            project_name, v, name)
-            # FIXME this rejects UNKNOWN, is that right?
-            elif name in _VERSIONS_FIELDS and value is not None:
-                if not scheme.is_valid_constraint_list(value):
-                    logger.warning("'%s': '%s' is not a valid version (field '%s')",
-                                   project_name, value, name)
-            elif name in _VERSION_FIELDS and value is not None:
-                if not scheme.is_valid_version(value):
-                    logger.warning("'%s': '%s' is not a valid version (field '%s')",
-                                   project_name, value, name)
-
-        if name in _UNICODEFIELDS:
-            if name == 'Description':
-                value = self._remove_line_prefix(value)
-
-        self._fields[name] = value
-
-    def get(self, name, default=_MISSING):
-        """Get a metadata field."""
-        name = self._convert_name(name)
-        if name not in self._fields:
-            if default is _MISSING:
-                default = self._default_value(name)
-            return default
-        if name in _UNICODEFIELDS:
-            value = self._fields[name]
-            return value
-        elif name in _LISTFIELDS:
-            value = self._fields[name]
-            if value is None:
-                return []
-            res = []
-            for val in value:
-                if name not in _LISTTUPLEFIELDS:
-                    res.append(val)
-                else:
-                    # That's for Project-URL
-                    res.append((val[0], val[1]))
-            return res
-
-        elif name in _ELEMENTSFIELD:
-            value = self._fields[name]
-            if isinstance(value, string_types):
-                return value.split(',')
-        return self._fields[name]
-
-    def check(self, strict=False):
-        """Check if the metadata is compliant. If strict is True then raise if
-        no Name or Version are provided"""
-        self.set_metadata_version()
-
-        # XXX should check the versions (if the file was loaded)
-        missing, warnings = [], []
-
-        for attr in ('Name', 'Version'):  # required by PEP 345
-            if attr not in self:
-                missing.append(attr)
-
-        if strict and missing != []:
-            msg = 'missing required metadata: %s' % ', '.join(missing)
-            raise MetadataMissingError(msg)
-
-        for attr in ('Home-page', 'Author'):
-            if attr not in self:
-                missing.append(attr)
-
-        # checking metadata 1.2 (XXX needs to check 1.1, 1.0)
-        if self['Metadata-Version'] != '1.2':
-            return missing, warnings
-
-        scheme = get_scheme(self.scheme)
-
-        def are_valid_constraints(value):
-            for v in value:
-                if not scheme.is_valid_matcher(v.split(';')[0]):
-                    return False
-            return True
-
-        for fields, controller in ((_PREDICATE_FIELDS, are_valid_constraints),
-                                   (_VERSIONS_FIELDS,
-                                    scheme.is_valid_constraint_list),
-                                   (_VERSION_FIELDS,
-                                    scheme.is_valid_version)):
-            for field in fields:
-                value = self.get(field, None)
-                if value is not None and not controller(value):
-                    warnings.append("Wrong value for '%s': %s" % (field, value))
-
-        return missing, warnings
-
-    def todict(self, skip_missing=False):
-        """Return fields as a dict.
-
-        Field names will be converted to use the underscore-lowercase style
-        instead of hyphen-mixed case (i.e. home_page instead of Home-page).
-        """
-        self.set_metadata_version()
-
-        mapping_1_0 = (
-            ('metadata_version', 'Metadata-Version'),
-            ('name', 'Name'),
-            ('version', 'Version'),
-            ('summary', 'Summary'),
-            ('home_page', 'Home-page'),
-            ('author', 'Author'),
-            ('author_email', 'Author-email'),
-            ('license', 'License'),
-            ('description', 'Description'),
-            ('keywords', 'Keywords'),
-            ('platform', 'Platform'),
-            ('classifiers', 'Classifier'),
-            ('download_url', 'Download-URL'),
-        )
-
-        data = {}
-        for key, field_name in mapping_1_0:
-            if not skip_missing or field_name in self._fields:
-                data[key] = self[field_name]
-
-        if self['Metadata-Version'] == '1.2':
-            mapping_1_2 = (
-                ('requires_dist', 'Requires-Dist'),
-                ('requires_python', 'Requires-Python'),
-                ('requires_external', 'Requires-External'),
-                ('provides_dist', 'Provides-Dist'),
-                ('obsoletes_dist', 'Obsoletes-Dist'),
-                ('project_url', 'Project-URL'),
-                ('maintainer', 'Maintainer'),
-                ('maintainer_email', 'Maintainer-email'),
-            )
-            for key, field_name in mapping_1_2:
-                if not skip_missing or field_name in self._fields:
-                    if key != 'project_url':
-                        data[key] = self[field_name]
-                    else:
-                        data[key] = [','.join(u) for u in self[field_name]]
-
-        elif self['Metadata-Version'] == '1.1':
-            mapping_1_1 = (
-                ('provides', 'Provides'),
-                ('requires', 'Requires'),
-                ('obsoletes', 'Obsoletes'),
-            )
-            for key, field_name in mapping_1_1:
-                if not skip_missing or field_name in self._fields:
-                    data[key] = self[field_name]
-
-        return data
-
-    def add_requirements(self, requirements):
-        if self['Metadata-Version'] == '1.1':
-            # we can't have 1.1 metadata *and* Setuptools requires
-            for field in ('Obsoletes', 'Requires', 'Provides'):
-                if field in self:
-                    del self[field]
-        self['Requires-Dist'] += requirements
-
-    # Mapping API
-    # TODO could add iter* variants
-
-    def keys(self):
-        return list(_version2fieldlist(self['Metadata-Version']))
-
-    def __iter__(self):
-        for key in self.keys():
-            yield key
-
-    def values(self):
-        return [self[key] for key in self.keys()]
-
-    def items(self):
-        return [(key, self[key]) for key in self.keys()]
-
-    def __repr__(self):
-        return '<%s %s %s>' % (self.__class__.__name__, self.name,
-                               self.version)
-
-
-METADATA_FILENAME = 'pydist.json'
-WHEEL_METADATA_FILENAME = 'metadata.json'
-LEGACY_METADATA_FILENAME = 'METADATA'
-
-
-class Metadata(object):
-    """
-    The metadata of a release. This implementation uses 2.0 (JSON)
-    metadata where possible. If not possible, it wraps a LegacyMetadata
-    instance which handles the key-value metadata format.
-    """
-
-    METADATA_VERSION_MATCHER = re.compile(r'^\d+(\.\d+)*$')
-
-    NAME_MATCHER = re.compile('^[0-9A-Z]([0-9A-Z_.-]*[0-9A-Z])?$', re.I)
-
-    VERSION_MATCHER = PEP440_VERSION_RE
-
-    SUMMARY_MATCHER = re.compile('.{1,2047}')
-
-    METADATA_VERSION = '2.0'
-
-    GENERATOR = 'distlib (%s)' % __version__
-
-    MANDATORY_KEYS = {
-        'name': (),
-        'version': (),
-        'summary': ('legacy',),
-    }
-
-    INDEX_KEYS = ('name version license summary description author '
-                  'author_email keywords platform home_page classifiers '
-                  'download_url')
-
-    DEPENDENCY_KEYS = ('extras run_requires test_requires build_requires '
-                       'dev_requires provides meta_requires obsoleted_by '
-                       'supports_environments')
-
-    SYNTAX_VALIDATORS = {
-        'metadata_version': (METADATA_VERSION_MATCHER, ()),
-        'name': (NAME_MATCHER, ('legacy',)),
-        'version': (VERSION_MATCHER, ('legacy',)),
-        'summary': (SUMMARY_MATCHER, ('legacy',)),
-    }
-
-    __slots__ = ('_legacy', '_data', 'scheme')
-
-    def __init__(self, path=None, fileobj=None, mapping=None,
-                 scheme='default'):
-        if [path, fileobj, mapping].count(None) < 2:
-            raise TypeError('path, fileobj and mapping are exclusive')
-        self._legacy = None
-        self._data = None
-        self.scheme = scheme
-        #import pdb; pdb.set_trace()
-        if mapping is not None:
-            try:
-                self._validate_mapping(mapping, scheme)
-                self._data = mapping
-            except MetadataUnrecognizedVersionError:
-                self._legacy = LegacyMetadata(mapping=mapping, scheme=scheme)
-                self.validate()
-        else:
-            data = None
-            if path:
-                with open(path, 'rb') as f:
-                    data = f.read()
-            elif fileobj:
-                data = fileobj.read()
-            if data is None:
-                # Initialised with no args - to be added
-                self._data = {
-                    'metadata_version': self.METADATA_VERSION,
-                    'generator': self.GENERATOR,
-                }
-            else:
-                if not isinstance(data, text_type):
-                    data = data.decode('utf-8')
-                try:
-                    self._data = json.loads(data)
-                    self._validate_mapping(self._data, scheme)
-                except ValueError:
-                    # Note: MetadataUnrecognizedVersionError does not
-                    # inherit from ValueError (it's a DistlibException,
-                    # which should not inherit from ValueError).
-                    # The ValueError comes from the json.load - if that
-                    # succeeds and we get a validation error, we want
-                    # that to propagate
-                    self._legacy = LegacyMetadata(fileobj=StringIO(data),
-                                                  scheme=scheme)
-                    self.validate()
-
-    common_keys = set(('name', 'version', 'license', 'keywords', 'summary'))
-
-    none_list = (None, list)
-    none_dict = (None, dict)
-
-    mapped_keys = {
-        'run_requires': ('Requires-Dist', list),
-        'build_requires': ('Setup-Requires-Dist', list),
-        'dev_requires': none_list,
-        'test_requires': none_list,
-        'meta_requires': none_list,
-        'extras': ('Provides-Extra', list),
-        'modules': none_list,
-        'namespaces': none_list,
-        'exports': none_dict,
-        'commands': none_dict,
-        'classifiers': ('Classifier', list),
-        'source_url': ('Download-URL', None),
-        'metadata_version': ('Metadata-Version', None),
-    }
-
-    del none_list, none_dict
-
-    def __getattribute__(self, key):
-        common = object.__getattribute__(self, 'common_keys')
-        mapped = object.__getattribute__(self, 'mapped_keys')
-        if key in mapped:
-            lk, maker = mapped[key]
-            if self._legacy:
-                if lk is None:
-                    result = None if maker is None else maker()
-                else:
-                    result = self._legacy.get(lk)
-            else:
-                value = None if maker is None else maker()
-                if key not in ('commands', 'exports', 'modules', 'namespaces',
-                               'classifiers'):
-                    result = self._data.get(key, value)
-                else:
-                    # special cases for PEP 459
-                    sentinel = object()
-                    result = sentinel
-                    d = self._data.get('extensions')
-                    if d:
-                        if key == 'commands':
-                            result = d.get('python.commands', value)
-                        elif key == 'classifiers':
-                            d = d.get('python.details')
-                            if d:
-                                result = d.get(key, value)
-                        else:
-                            d = d.get('python.exports')
-                            if not d:
-                                d = self._data.get('python.exports')
-                            if d:
-                                result = d.get(key, value)
-                    if result is sentinel:
-                        result = value
-        elif key not in common:
-            result = object.__getattribute__(self, key)
-        elif self._legacy:
-            result = self._legacy.get(key)
-        else:
-            result = self._data.get(key)
-        return result
-
-    def _validate_value(self, key, value, scheme=None):
-        if key in self.SYNTAX_VALIDATORS:
-            pattern, exclusions = self.SYNTAX_VALIDATORS[key]
-            if (scheme or self.scheme) not in exclusions:
-                m = pattern.match(value)
-                if not m:
-                    raise MetadataInvalidError("'%s' is an invalid value for "
-                                               "the '%s' property" % (value,
-                                                                    key))
-
-    def __setattr__(self, key, value):
-        self._validate_value(key, value)
-        common = object.__getattribute__(self, 'common_keys')
-        mapped = object.__getattribute__(self, 'mapped_keys')
-        if key in mapped:
-            lk, _ = mapped[key]
-            if self._legacy:
-                if lk is None:
-                    raise NotImplementedError
-                self._legacy[lk] = value
-            elif key not in ('commands', 'exports', 'modules', 'namespaces',
-                             'classifiers'):
-                self._data[key] = value
-            else:
-                # special cases for PEP 459
-                d = self._data.setdefault('extensions', {})
-                if key == 'commands':
-                    d['python.commands'] = value
-                elif key == 'classifiers':
-                    d = d.setdefault('python.details', {})
-                    d[key] = value
-                else:
-                    d = d.setdefault('python.exports', {})
-                    d[key] = value
-        elif key not in common:
-            object.__setattr__(self, key, value)
-        else:
-            if key == 'keywords':
-                if isinstance(value, string_types):
-                    value = value.strip()
-                    if value:
-                        value = value.split()
-                    else:
-                        value = []
-            if self._legacy:
-                self._legacy[key] = value
-            else:
-                self._data[key] = value
-
-    @property
-    def name_and_version(self):
-        return _get_name_and_version(self.name, self.version, True)
-
-    @property
-    def provides(self):
-        if self._legacy:
-            result = self._legacy['Provides-Dist']
-        else:
-            result = self._data.setdefault('provides', [])
-        s = '%s (%s)' % (self.name, self.version)
-        if s not in result:
-            result.append(s)
-        return result
-
-    @provides.setter
-    def provides(self, value):
-        if self._legacy:
-            self._legacy['Provides-Dist'] = value
-        else:
-            self._data['provides'] = value
-
-    def get_requirements(self, reqts, extras=None, env=None):
-        """
-        Base method to get dependencies, given a set of extras
-        to satisfy and an optional environment context.
-        :param reqts: A list of sometimes-wanted dependencies,
-                      perhaps dependent on extras and environment.
-        :param extras: A list of optional components being requested.
-        :param env: An optional environment for marker evaluation.
-        """
-        if self._legacy:
-            result = reqts
-        else:
-            result = []
-            extras = get_extras(extras or [], self.extras)
-            for d in reqts:
-                if 'extra' not in d and 'environment' not in d:
-                    # unconditional
-                    include = True
-                else:
-                    if 'extra' not in d:
-                        # Not extra-dependent - only environment-dependent
-                        include = True
-                    else:
-                        include = d.get('extra') in extras
-                    if include:
-                        # Not excluded because of extras, check environment
-                        marker = d.get('environment')
-                        if marker:
-                            include = interpret(marker, env)
-                if include:
-                    result.extend(d['requires'])
-            for key in ('build', 'dev', 'test'):
-                e = ':%s:' % key
-                if e in extras:
-                    extras.remove(e)
-                    # A recursive call, but it should terminate since 'test'
-                    # has been removed from the extras
-                    reqts = self._data.get('%s_requires' % key, [])
-                    result.extend(self.get_requirements(reqts, extras=extras,
-                                                        env=env))
-        return result
-
-    @property
-    def dictionary(self):
-        if self._legacy:
-            return self._from_legacy()
-        return self._data
-
-    @property
-    def dependencies(self):
-        if self._legacy:
-            raise NotImplementedError
-        else:
-            return extract_by_key(self._data, self.DEPENDENCY_KEYS)
-
-    @dependencies.setter
-    def dependencies(self, value):
-        if self._legacy:
-            raise NotImplementedError
-        else:
-            self._data.update(value)
-
-    def _validate_mapping(self, mapping, scheme):
-        if mapping.get('metadata_version') != self.METADATA_VERSION:
-            raise MetadataUnrecognizedVersionError()
-        missing = []
-        for key, exclusions in self.MANDATORY_KEYS.items():
-            if key not in mapping:
-                if scheme not in exclusions:
-                    missing.append(key)
-        if missing:
-            msg = 'Missing metadata items: %s' % ', '.join(missing)
-            raise MetadataMissingError(msg)
-        for k, v in mapping.items():
-            self._validate_value(k, v, scheme)
-
-    def validate(self):
-        if self._legacy:
-            missing, warnings = self._legacy.check(True)
-            if missing or warnings:
-                logger.warning('Metadata: missing: %s, warnings: %s',
-                               missing, warnings)
-        else:
-            self._validate_mapping(self._data, self.scheme)
-
-    def todict(self):
-        if self._legacy:
-            return self._legacy.todict(True)
-        else:
-            result = extract_by_key(self._data, self.INDEX_KEYS)
-            return result
-
-    def _from_legacy(self):
-        assert self._legacy and not self._data
-        result = {
-            'metadata_version': self.METADATA_VERSION,
-            'generator': self.GENERATOR,
-        }
-        lmd = self._legacy.todict(True)     # skip missing ones
-        for k in ('name', 'version', 'license', 'summary', 'description',
-                  'classifier'):
-            if k in lmd:
-                if k == 'classifier':
-                    nk = 'classifiers'
-                else:
-                    nk = k
-                result[nk] = lmd[k]
-        kw = lmd.get('Keywords', [])
-        if kw == ['']:
-            kw = []
-        result['keywords'] = kw
-        keys = (('requires_dist', 'run_requires'),
-                ('setup_requires_dist', 'build_requires'))
-        for ok, nk in keys:
-            if ok in lmd and lmd[ok]:
-                result[nk] = [{'requires': lmd[ok]}]
-        result['provides'] = self.provides
-        author = {}
-        maintainer = {}
-        return result
-
-    LEGACY_MAPPING = {
-        'name': 'Name',
-        'version': 'Version',
-        'license': 'License',
-        'summary': 'Summary',
-        'description': 'Description',
-        'classifiers': 'Classifier',
-    }
-
-    def _to_legacy(self):
-        def process_entries(entries):
-            reqts = set()
-            for e in entries:
-                extra = e.get('extra')
-                env = e.get('environment')
-                rlist = e['requires']
-                for r in rlist:
-                    if not env and not extra:
-                        reqts.add(r)
-                    else:
-                        marker = ''
-                        if extra:
-                            marker = 'extra == "%s"' % extra
-                        if env:
-                            if marker:
-                                marker = '(%s) and %s' % (env, marker)
-                            else:
-                                marker = env
-                        reqts.add(';'.join((r, marker)))
-            return reqts
-
-        assert self._data and not self._legacy
-        result = LegacyMetadata()
-        nmd = self._data
-        for nk, ok in self.LEGACY_MAPPING.items():
-            if nk in nmd:
-                result[ok] = nmd[nk]
-        r1 = process_entries(self.run_requires + self.meta_requires)
-        r2 = process_entries(self.build_requires + self.dev_requires)
-        if self.extras:
-            result['Provides-Extra'] = sorted(self.extras)
-        result['Requires-Dist'] = sorted(r1)
-        result['Setup-Requires-Dist'] = sorted(r2)
-        # TODO: other fields such as contacts
-        return result
-
-    def write(self, path=None, fileobj=None, legacy=False, skip_unknown=True):
-        if [path, fileobj].count(None) != 1:
-            raise ValueError('Exactly one of path and fileobj is needed')
-        self.validate()
-        if legacy:
-            if self._legacy:
-                legacy_md = self._legacy
-            else:
-                legacy_md = self._to_legacy()
-            if path:
-                legacy_md.write(path, skip_unknown=skip_unknown)
-            else:
-                legacy_md.write_file(fileobj, skip_unknown=skip_unknown)
-        else:
-            if self._legacy:
-                d = self._from_legacy()
-            else:
-                d = self._data
-            if fileobj:
-                json.dump(d, fileobj, ensure_ascii=True, indent=2,
-                          sort_keys=True)
-            else:
-                with codecs.open(path, 'w', 'utf-8') as f:
-                    json.dump(d, f, ensure_ascii=True, indent=2,
-                              sort_keys=True)
-
-    def add_requirements(self, requirements):
-        if self._legacy:
-            self._legacy.add_requirements(requirements)
-        else:
-            run_requires = self._data.setdefault('run_requires', [])
-            always = None
-            for entry in run_requires:
-                if 'environment' not in entry and 'extra' not in entry:
-                    always = entry
-                    break
-            if always is None:
-                always = { 'requires': requirements }
-                run_requires.insert(0, always)
-            else:
-                rset = set(always['requires']) | set(requirements)
-                always['requires'] = sorted(rset)
-
-    def __repr__(self):
-        name = self.name or '(no name)'
-        version = self.version or 'no version'
-        return '<%s %s %s (%s)>' % (self.__class__.__name__,
-                                    self.metadata_version, name, version)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/resources.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/resources.py
deleted file mode 100644
index 1884016..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/resources.py
+++ /dev/null
@@ -1,355 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2013-2017 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-from __future__ import unicode_literals
-
-import bisect
-import io
-import logging
-import os
-import pkgutil
-import shutil
-import sys
-import types
-import zipimport
-
-from . import DistlibException
-from .util import cached_property, get_cache_base, path_to_cache_dir, Cache
-
-logger = logging.getLogger(__name__)
-
-
-cache = None    # created when needed
-
-
-class ResourceCache(Cache):
-    def __init__(self, base=None):
-        if base is None:
-            # Use native string to avoid issues on 2.x: see Python #20140.
-            base = os.path.join(get_cache_base(), str('resource-cache'))
-        super(ResourceCache, self).__init__(base)
-
-    def is_stale(self, resource, path):
-        """
-        Is the cache stale for the given resource?
-
-        :param resource: The :class:`Resource` being cached.
-        :param path: The path of the resource in the cache.
-        :return: True if the cache is stale.
-        """
-        # Cache invalidation is a hard problem :-)
-        return True
-
-    def get(self, resource):
-        """
-        Get a resource into the cache,
-
-        :param resource: A :class:`Resource` instance.
-        :return: The pathname of the resource in the cache.
-        """
-        prefix, path = resource.finder.get_cache_info(resource)
-        if prefix is None:
-            result = path
-        else:
-            result = os.path.join(self.base, self.prefix_to_dir(prefix), path)
-            dirname = os.path.dirname(result)
-            if not os.path.isdir(dirname):
-                os.makedirs(dirname)
-            if not os.path.exists(result):
-                stale = True
-            else:
-                stale = self.is_stale(resource, path)
-            if stale:
-                # write the bytes of the resource to the cache location
-                with open(result, 'wb') as f:
-                    f.write(resource.bytes)
-        return result
-
-
-class ResourceBase(object):
-    def __init__(self, finder, name):
-        self.finder = finder
-        self.name = name
-
-
-class Resource(ResourceBase):
-    """
-    A class representing an in-package resource, such as a data file. This is
-    not normally instantiated by user code, but rather by a
-    :class:`ResourceFinder` which manages the resource.
-    """
-    is_container = False        # Backwards compatibility
-
-    def as_stream(self):
-        """
-        Get the resource as a stream.
-
-        This is not a property to make it obvious that it returns a new stream
-        each time.
-        """
-        return self.finder.get_stream(self)
-
-    @cached_property
-    def file_path(self):
-        global cache
-        if cache is None:
-            cache = ResourceCache()
-        return cache.get(self)
-
-    @cached_property
-    def bytes(self):
-        return self.finder.get_bytes(self)
-
-    @cached_property
-    def size(self):
-        return self.finder.get_size(self)
-
-
-class ResourceContainer(ResourceBase):
-    is_container = True     # Backwards compatibility
-
-    @cached_property
-    def resources(self):
-        return self.finder.get_resources(self)
-
-
-class ResourceFinder(object):
-    """
-    Resource finder for file system resources.
-    """
-
-    if sys.platform.startswith('java'):
-        skipped_extensions = ('.pyc', '.pyo', '.class')
-    else:
-        skipped_extensions = ('.pyc', '.pyo')
-
-    def __init__(self, module):
-        self.module = module
-        self.loader = getattr(module, '__loader__', None)
-        self.base = os.path.dirname(getattr(module, '__file__', ''))
-
-    def _adjust_path(self, path):
-        return os.path.realpath(path)
-
-    def _make_path(self, resource_name):
-        # Issue #50: need to preserve type of path on Python 2.x
-        # like os.path._get_sep
-        if isinstance(resource_name, bytes):    # should only happen on 2.x
-            sep = b'/'
-        else:
-            sep = '/'
-        parts = resource_name.split(sep)
-        parts.insert(0, self.base)
-        result = os.path.join(*parts)
-        return self._adjust_path(result)
-
-    def _find(self, path):
-        return os.path.exists(path)
-
-    def get_cache_info(self, resource):
-        return None, resource.path
-
-    def find(self, resource_name):
-        path = self._make_path(resource_name)
-        if not self._find(path):
-            result = None
-        else:
-            if self._is_directory(path):
-                result = ResourceContainer(self, resource_name)
-            else:
-                result = Resource(self, resource_name)
-            result.path = path
-        return result
-
-    def get_stream(self, resource):
-        return open(resource.path, 'rb')
-
-    def get_bytes(self, resource):
-        with open(resource.path, 'rb') as f:
-            return f.read()
-
-    def get_size(self, resource):
-        return os.path.getsize(resource.path)
-
-    def get_resources(self, resource):
-        def allowed(f):
-            return (f != '__pycache__' and not
-                    f.endswith(self.skipped_extensions))
-        return set([f for f in os.listdir(resource.path) if allowed(f)])
-
-    def is_container(self, resource):
-        return self._is_directory(resource.path)
-
-    _is_directory = staticmethod(os.path.isdir)
-
-    def iterator(self, resource_name):
-        resource = self.find(resource_name)
-        if resource is not None:
-            todo = [resource]
-            while todo:
-                resource = todo.pop(0)
-                yield resource
-                if resource.is_container:
-                    rname = resource.name
-                    for name in resource.resources:
-                        if not rname:
-                            new_name = name
-                        else:
-                            new_name = '/'.join([rname, name])
-                        child = self.find(new_name)
-                        if child.is_container:
-                            todo.append(child)
-                        else:
-                            yield child
-
-
-class ZipResourceFinder(ResourceFinder):
-    """
-    Resource finder for resources in .zip files.
-    """
-    def __init__(self, module):
-        super(ZipResourceFinder, self).__init__(module)
-        archive = self.loader.archive
-        self.prefix_len = 1 + len(archive)
-        # PyPy doesn't have a _files attr on zipimporter, and you can't set one
-        if hasattr(self.loader, '_files'):
-            self._files = self.loader._files
-        else:
-            self._files = zipimport._zip_directory_cache[archive]
-        self.index = sorted(self._files)
-
-    def _adjust_path(self, path):
-        return path
-
-    def _find(self, path):
-        path = path[self.prefix_len:]
-        if path in self._files:
-            result = True
-        else:
-            if path and path[-1] != os.sep:
-                path = path + os.sep
-            i = bisect.bisect(self.index, path)
-            try:
-                result = self.index[i].startswith(path)
-            except IndexError:
-                result = False
-        if not result:
-            logger.debug('_find failed: %r %r', path, self.loader.prefix)
-        else:
-            logger.debug('_find worked: %r %r', path, self.loader.prefix)
-        return result
-
-    def get_cache_info(self, resource):
-        prefix = self.loader.archive
-        path = resource.path[1 + len(prefix):]
-        return prefix, path
-
-    def get_bytes(self, resource):
-        return self.loader.get_data(resource.path)
-
-    def get_stream(self, resource):
-        return io.BytesIO(self.get_bytes(resource))
-
-    def get_size(self, resource):
-        path = resource.path[self.prefix_len:]
-        return self._files[path][3]
-
-    def get_resources(self, resource):
-        path = resource.path[self.prefix_len:]
-        if path and path[-1] != os.sep:
-            path += os.sep
-        plen = len(path)
-        result = set()
-        i = bisect.bisect(self.index, path)
-        while i < len(self.index):
-            if not self.index[i].startswith(path):
-                break
-            s = self.index[i][plen:]
-            result.add(s.split(os.sep, 1)[0])   # only immediate children
-            i += 1
-        return result
-
-    def _is_directory(self, path):
-        path = path[self.prefix_len:]
-        if path and path[-1] != os.sep:
-            path += os.sep
-        i = bisect.bisect(self.index, path)
-        try:
-            result = self.index[i].startswith(path)
-        except IndexError:
-            result = False
-        return result
-
-_finder_registry = {
-    type(None): ResourceFinder,
-    zipimport.zipimporter: ZipResourceFinder
-}
-
-try:
-    # In Python 3.6, _frozen_importlib -> _frozen_importlib_external
-    try:
-        import _frozen_importlib_external as _fi
-    except ImportError:
-        import _frozen_importlib as _fi
-    _finder_registry[_fi.SourceFileLoader] = ResourceFinder
-    _finder_registry[_fi.FileFinder] = ResourceFinder
-    del _fi
-except (ImportError, AttributeError):
-    pass
-
-
-def register_finder(loader, finder_maker):
-    _finder_registry[type(loader)] = finder_maker
-
-_finder_cache = {}
-
-
-def finder(package):
-    """
-    Return a resource finder for a package.
-    :param package: The name of the package.
-    :return: A :class:`ResourceFinder` instance for the package.
-    """
-    if package in _finder_cache:
-        result = _finder_cache[package]
-    else:
-        if package not in sys.modules:
-            __import__(package)
-        module = sys.modules[package]
-        path = getattr(module, '__path__', None)
-        if path is None:
-            raise DistlibException('You cannot get a finder for a module, '
-                                   'only for a package')
-        loader = getattr(module, '__loader__', None)
-        finder_maker = _finder_registry.get(type(loader))
-        if finder_maker is None:
-            raise DistlibException('Unable to locate finder for %r' % package)
-        result = finder_maker(module)
-        _finder_cache[package] = result
-    return result
-
-
-_dummy_module = types.ModuleType(str('__dummy__'))
-
-
-def finder_for_path(path):
-    """
-    Return a resource finder for a path, which should represent a container.
-
-    :param path: The path.
-    :return: A :class:`ResourceFinder` instance for the path.
-    """
-    result = None
-    # calls any path hooks, gets importer into cache
-    pkgutil.get_importer(path)
-    loader = sys.path_importer_cache.get(path)
-    finder = _finder_registry.get(type(loader))
-    if finder:
-        module = _dummy_module
-        module.__file__ = os.path.join(path, '')
-        module.__loader__ = loader
-        result = finder(module)
-    return result
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/scripts.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/scripts.py
deleted file mode 100644
index 8e22cb9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/scripts.py
+++ /dev/null
@@ -1,417 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2013-2015 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-from io import BytesIO
-import logging
-import os
-import re
-import struct
-import sys
-
-from .compat import sysconfig, detect_encoding, ZipFile
-from .resources import finder
-from .util import (FileOperator, get_export_entry, convert_path,
-                   get_executable, in_venv)
-
-logger = logging.getLogger(__name__)
-
-_DEFAULT_MANIFEST = '''
-<?xml version="1.0" encoding="UTF-8" standalone="yes"?>
-<assembly xmlns="urn:schemas-microsoft-com:asm.v1" manifestVersion="1.0">
- <assemblyIdentity version="1.0.0.0"
- processorArchitecture="X86"
- name="%s"
- type="win32"/>
-
- <!-- Identify the application security requirements. -->
- <trustInfo xmlns="urn:schemas-microsoft-com:asm.v3">
- <security>
- <requestedPrivileges>
- <requestedExecutionLevel level="asInvoker" uiAccess="false"/>
- </requestedPrivileges>
- </security>
- </trustInfo>
-</assembly>'''.strip()
-
-# check if Python is called on the first line with this expression
-FIRST_LINE_RE = re.compile(b'^#!.*pythonw?[0-9.]*([ \t].*)?$')
-SCRIPT_TEMPLATE = r'''# -*- coding: utf-8 -*-
-if __name__ == '__main__':
-    import sys, re
-
-    def _resolve(module, func):
-        __import__(module)
-        mod = sys.modules[module]
-        parts = func.split('.')
-        result = getattr(mod, parts.pop(0))
-        for p in parts:
-            result = getattr(result, p)
-        return result
-
-    try:
-        sys.argv[0] = re.sub(r'(-script\.pyw?|\.exe)?$', '', sys.argv[0])
-
-        func = _resolve('%(module)s', '%(func)s')
-        rc = func() # None interpreted as 0
-    except Exception as e:  # only supporting Python >= 2.6
-        sys.stderr.write('%%s\n' %% e)
-        rc = 1
-    sys.exit(rc)
-'''
-
-
-def _enquote_executable(executable):
-    if ' ' in executable:
-        # make sure we quote only the executable in case of env
-        # for example /usr/bin/env "/dir with spaces/bin/jython"
-        # instead of "/usr/bin/env /dir with spaces/bin/jython"
-        # otherwise whole
-        if executable.startswith('/usr/bin/env '):
-            env, _executable = executable.split(' ', 1)
-            if ' ' in _executable and not _executable.startswith('"'):
-                executable = '%s "%s"' % (env, _executable)
-        else:
-            if not executable.startswith('"'):
-                executable = '"%s"' % executable
-    return executable
-
-
-class ScriptMaker(object):
-    """
-    A class to copy or create scripts from source scripts or callable
-    specifications.
-    """
-    script_template = SCRIPT_TEMPLATE
-
-    executable = None  # for shebangs
-
-    def __init__(self, source_dir, target_dir, add_launchers=True,
-                 dry_run=False, fileop=None):
-        self.source_dir = source_dir
-        self.target_dir = target_dir
-        self.add_launchers = add_launchers
-        self.force = False
-        self.clobber = False
-        # It only makes sense to set mode bits on POSIX.
-        self.set_mode = (os.name == 'posix') or (os.name == 'java' and
-                                                 os._name == 'posix')
-        self.variants = set(('', 'X.Y'))
-        self._fileop = fileop or FileOperator(dry_run)
-
-        self._is_nt = os.name == 'nt' or (
-            os.name == 'java' and os._name == 'nt')
-
-    def _get_alternate_executable(self, executable, options):
-        if options.get('gui', False) and self._is_nt:  # pragma: no cover
-            dn, fn = os.path.split(executable)
-            fn = fn.replace('python', 'pythonw')
-            executable = os.path.join(dn, fn)
-        return executable
-
-    if sys.platform.startswith('java'):  # pragma: no cover
-        def _is_shell(self, executable):
-            """
-            Determine if the specified executable is a script
-            (contains a #! line)
-            """
-            try:
-                with open(executable) as fp:
-                    return fp.read(2) == '#!'
-            except (OSError, IOError):
-                logger.warning('Failed to open %s', executable)
-                return False
-
-        def _fix_jython_executable(self, executable):
-            if self._is_shell(executable):
-                # Workaround for Jython is not needed on Linux systems.
-                import java
-
-                if java.lang.System.getProperty('os.name') == 'Linux':
-                    return executable
-            elif executable.lower().endswith('jython.exe'):
-                # Use wrapper exe for Jython on Windows
-                return executable
-            return '/usr/bin/env %s' % executable
-
-    def _build_shebang(self, executable, post_interp):
-        """
-        Build a shebang line. In the simple case (on Windows, or a shebang line
-        which is not too long or contains spaces) use a simple formulation for
-        the shebang. Otherwise, use /bin/sh as the executable, with a contrived
-        shebang which allows the script to run either under Python or sh, using
-        suitable quoting. Thanks to Harald Nordgren for his input.
-
-        See also: http://www.in-ulm.de/~mascheck/various/shebang/#length
-                  https://hg.mozilla.org/mozilla-central/file/tip/mach
-        """
-        if os.name != 'posix':
-            simple_shebang = True
-        else:
-            # Add 3 for '#!' prefix and newline suffix.
-            shebang_length = len(executable) + len(post_interp) + 3
-            if sys.platform == 'darwin':
-                max_shebang_length = 512
-            else:
-                max_shebang_length = 127
-            simple_shebang = ((b' ' not in executable) and
-                              (shebang_length <= max_shebang_length))
-
-        if simple_shebang:
-            result = b'#!' + executable + post_interp + b'\n'
-        else:
-            result = b'#!/bin/sh\n'
-            result += b"'''exec' " + executable + post_interp + b' "$0" "$@"\n'
-            result += b"' '''"
-        return result
-
-    def _get_shebang(self, encoding, post_interp=b'', options=None):
-        enquote = True
-        if self.executable:
-            executable = self.executable
-            enquote = False     # assume this will be taken care of
-        elif not sysconfig.is_python_build():
-            executable = get_executable()
-        elif in_venv():  # pragma: no cover
-            executable = os.path.join(sysconfig.get_path('scripts'),
-                            'python%s' % sysconfig.get_config_var('EXE'))
-        else:  # pragma: no cover
-            executable = os.path.join(
-                sysconfig.get_config_var('BINDIR'),
-               'python%s%s' % (sysconfig.get_config_var('VERSION'),
-                               sysconfig.get_config_var('EXE')))
-        if options:
-            executable = self._get_alternate_executable(executable, options)
-
-        if sys.platform.startswith('java'):  # pragma: no cover
-            executable = self._fix_jython_executable(executable)
-        # Normalise case for Windows
-        executable = os.path.normcase(executable)
-        # If the user didn't specify an executable, it may be necessary to
-        # cater for executable paths with spaces (not uncommon on Windows)
-        if enquote:
-            executable = _enquote_executable(executable)
-        # Issue #51: don't use fsencode, since we later try to
-        # check that the shebang is decodable using utf-8.
-        executable = executable.encode('utf-8')
-        # in case of IronPython, play safe and enable frames support
-        if (sys.platform == 'cli' and '-X:Frames' not in post_interp
-            and '-X:FullFrames' not in post_interp):  # pragma: no cover
-            post_interp += b' -X:Frames'
-        shebang = self._build_shebang(executable, post_interp)
-        # Python parser starts to read a script using UTF-8 until
-        # it gets a #coding:xxx cookie. The shebang has to be the
-        # first line of a file, the #coding:xxx cookie cannot be
-        # written before. So the shebang has to be decodable from
-        # UTF-8.
-        try:
-            shebang.decode('utf-8')
-        except UnicodeDecodeError:  # pragma: no cover
-            raise ValueError(
-                'The shebang (%r) is not decodable from utf-8' % shebang)
-        # If the script is encoded to a custom encoding (use a
-        # #coding:xxx cookie), the shebang has to be decodable from
-        # the script encoding too.
-        if encoding != 'utf-8':
-            try:
-                shebang.decode(encoding)
-            except UnicodeDecodeError:  # pragma: no cover
-                raise ValueError(
-                    'The shebang (%r) is not decodable '
-                    'from the script encoding (%r)' % (shebang, encoding))
-        return shebang
-
-    def _get_script_text(self, entry):
-        return self.script_template % dict(module=entry.prefix,
-                                           func=entry.suffix)
-
-    manifest = _DEFAULT_MANIFEST
-
-    def get_manifest(self, exename):
-        base = os.path.basename(exename)
-        return self.manifest % base
-
-    def _write_script(self, names, shebang, script_bytes, filenames, ext):
-        use_launcher = self.add_launchers and self._is_nt
-        linesep = os.linesep.encode('utf-8')
-        if not shebang.endswith(linesep):
-            shebang += linesep
-        if not use_launcher:
-            script_bytes = shebang + script_bytes
-        else:  # pragma: no cover
-            if ext == 'py':
-                launcher = self._get_launcher('t')
-            else:
-                launcher = self._get_launcher('w')
-            stream = BytesIO()
-            with ZipFile(stream, 'w') as zf:
-                zf.writestr('__main__.py', script_bytes)
-            zip_data = stream.getvalue()
-            script_bytes = launcher + shebang + zip_data
-        for name in names:
-            outname = os.path.join(self.target_dir, name)
-            if use_launcher:  # pragma: no cover
-                n, e = os.path.splitext(outname)
-                if e.startswith('.py'):
-                    outname = n
-                outname = '%s.exe' % outname
-                try:
-                    self._fileop.write_binary_file(outname, script_bytes)
-                except Exception:
-                    # Failed writing an executable - it might be in use.
-                    logger.warning('Failed to write executable - trying to '
-                                   'use .deleteme logic')
-                    dfname = '%s.deleteme' % outname
-                    if os.path.exists(dfname):
-                        os.remove(dfname)       # Not allowed to fail here
-                    os.rename(outname, dfname)  # nor here
-                    self._fileop.write_binary_file(outname, script_bytes)
-                    logger.debug('Able to replace executable using '
-                                 '.deleteme logic')
-                    try:
-                        os.remove(dfname)
-                    except Exception:
-                        pass    # still in use - ignore error
-            else:
-                if self._is_nt and not outname.endswith('.' + ext):  # pragma: no cover
-                    outname = '%s.%s' % (outname, ext)
-                if os.path.exists(outname) and not self.clobber:
-                    logger.warning('Skipping existing file %s', outname)
-                    continue
-                self._fileop.write_binary_file(outname, script_bytes)
-                if self.set_mode:
-                    self._fileop.set_executable_mode([outname])
-            filenames.append(outname)
-
-    def _make_script(self, entry, filenames, options=None):
-        post_interp = b''
-        if options:
-            args = options.get('interpreter_args', [])
-            if args:
-                args = ' %s' % ' '.join(args)
-                post_interp = args.encode('utf-8')
-        shebang = self._get_shebang('utf-8', post_interp, options=options)
-        script = self._get_script_text(entry).encode('utf-8')
-        name = entry.name
-        scriptnames = set()
-        if '' in self.variants:
-            scriptnames.add(name)
-        if 'X' in self.variants:
-            scriptnames.add('%s%s' % (name, sys.version[0]))
-        if 'X.Y' in self.variants:
-            scriptnames.add('%s-%s' % (name, sys.version[:3]))
-        if options and options.get('gui', False):
-            ext = 'pyw'
-        else:
-            ext = 'py'
-        self._write_script(scriptnames, shebang, script, filenames, ext)
-
-    def _copy_script(self, script, filenames):
-        adjust = False
-        script = os.path.join(self.source_dir, convert_path(script))
-        outname = os.path.join(self.target_dir, os.path.basename(script))
-        if not self.force and not self._fileop.newer(script, outname):
-            logger.debug('not copying %s (up-to-date)', script)
-            return
-
-        # Always open the file, but ignore failures in dry-run mode --
-        # that way, we'll get accurate feedback if we can read the
-        # script.
-        try:
-            f = open(script, 'rb')
-        except IOError:  # pragma: no cover
-            if not self.dry_run:
-                raise
-            f = None
-        else:
-            first_line = f.readline()
-            if not first_line:  # pragma: no cover
-                logger.warning('%s: %s is an empty file (skipping)',
-                               self.get_command_name(),  script)
-                return
-
-            match = FIRST_LINE_RE.match(first_line.replace(b'\r\n', b'\n'))
-            if match:
-                adjust = True
-                post_interp = match.group(1) or b''
-
-        if not adjust:
-            if f:
-                f.close()
-            self._fileop.copy_file(script, outname)
-            if self.set_mode:
-                self._fileop.set_executable_mode([outname])
-            filenames.append(outname)
-        else:
-            logger.info('copying and adjusting %s -> %s', script,
-                        self.target_dir)
-            if not self._fileop.dry_run:
-                encoding, lines = detect_encoding(f.readline)
-                f.seek(0)
-                shebang = self._get_shebang(encoding, post_interp)
-                if b'pythonw' in first_line:  # pragma: no cover
-                    ext = 'pyw'
-                else:
-                    ext = 'py'
-                n = os.path.basename(outname)
-                self._write_script([n], shebang, f.read(), filenames, ext)
-            if f:
-                f.close()
-
-    @property
-    def dry_run(self):
-        return self._fileop.dry_run
-
-    @dry_run.setter
-    def dry_run(self, value):
-        self._fileop.dry_run = value
-
-    if os.name == 'nt' or (os.name == 'java' and os._name == 'nt'):  # pragma: no cover
-        # Executable launcher support.
-        # Launchers are from https://bitbucket.org/vinay.sajip/simple_launcher/
-
-        def _get_launcher(self, kind):
-            if struct.calcsize('P') == 8:   # 64-bit
-                bits = '64'
-            else:
-                bits = '32'
-            name = '%s%s.exe' % (kind, bits)
-            # Issue 31: don't hardcode an absolute package name, but
-            # determine it relative to the current package
-            distlib_package = __name__.rsplit('.', 1)[0]
-            result = finder(distlib_package).find(name).bytes
-            return result
-
-    # Public API follows
-
-    def make(self, specification, options=None):
-        """
-        Make a script.
-
-        :param specification: The specification, which is either a valid export
-                              entry specification (to make a script from a
-                              callable) or a filename (to make a script by
-                              copying from a source location).
-        :param options: A dictionary of options controlling script generation.
-        :return: A list of all absolute pathnames written to.
-        """
-        filenames = []
-        entry = get_export_entry(specification)
-        if entry is None:
-            self._copy_script(specification, filenames)
-        else:
-            self._make_script(entry, filenames, options=options)
-        return filenames
-
-    def make_multiple(self, specifications, options=None):
-        """
-        Take a list of specifications and make scripts from them,
-        :param specifications: A list of specifications.
-        :return: A list of all absolute pathnames written to,
-        """
-        filenames = []
-        for specification in specifications:
-            filenames.extend(self.make(specification, options))
-        return filenames
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/t32.exe b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/t32.exe
deleted file mode 100644
index a09d926..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/t32.exe
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/t64.exe b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/t64.exe
deleted file mode 100644
index 9da9b40..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/t64.exe
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/util.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/util.py
deleted file mode 100644
index 9d4bfd3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/util.py
+++ /dev/null
@@ -1,1756 +0,0 @@
-#
-# Copyright (C) 2012-2017 The Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-import codecs
-from collections import deque
-import contextlib
-import csv
-from glob import iglob as std_iglob
-import io
-import json
-import logging
-import os
-import py_compile
-import re
-import socket
-try:
-    import ssl
-except ImportError:  # pragma: no cover
-    ssl = None
-import subprocess
-import sys
-import tarfile
-import tempfile
-import textwrap
-
-try:
-    import threading
-except ImportError:  # pragma: no cover
-    import dummy_threading as threading
-import time
-
-from . import DistlibException
-from .compat import (string_types, text_type, shutil, raw_input, StringIO,
-                     cache_from_source, urlopen, urljoin, httplib, xmlrpclib,
-                     splittype, HTTPHandler, BaseConfigurator, valid_ident,
-                     Container, configparser, URLError, ZipFile, fsdecode,
-                     unquote, urlparse)
-
-logger = logging.getLogger(__name__)
-
-#
-# Requirement parsing code as per PEP 508
-#
-
-IDENTIFIER = re.compile(r'^([\w\.-]+)\s*')
-VERSION_IDENTIFIER = re.compile(r'^([\w\.*+-]+)\s*')
-COMPARE_OP = re.compile(r'^(<=?|>=?|={2,3}|[~!]=)\s*')
-MARKER_OP = re.compile(r'^((<=?)|(>=?)|={2,3}|[~!]=|in|not\s+in)\s*')
-OR = re.compile(r'^or\b\s*')
-AND = re.compile(r'^and\b\s*')
-NON_SPACE = re.compile(r'(\S+)\s*')
-STRING_CHUNK = re.compile(r'([\s\w\.{}()*+#:;,/?!~`@$%^&=|<>\[\]-]+)')
-
-
-def parse_marker(marker_string):
-    """
-    Parse a marker string and return a dictionary containing a marker expression.
-
-    The dictionary will contain keys "op", "lhs" and "rhs" for non-terminals in
-    the expression grammar, or strings. A string contained in quotes is to be
-    interpreted as a literal string, and a string not contained in quotes is a
-    variable (such as os_name).
-    """
-    def marker_var(remaining):
-        # either identifier, or literal string
-        m = IDENTIFIER.match(remaining)
-        if m:
-            result = m.groups()[0]
-            remaining = remaining[m.end():]
-        elif not remaining:
-            raise SyntaxError('unexpected end of input')
-        else:
-            q = remaining[0]
-            if q not in '\'"':
-                raise SyntaxError('invalid expression: %s' % remaining)
-            oq = '\'"'.replace(q, '')
-            remaining = remaining[1:]
-            parts = [q]
-            while remaining:
-                # either a string chunk, or oq, or q to terminate
-                if remaining[0] == q:
-                    break
-                elif remaining[0] == oq:
-                    parts.append(oq)
-                    remaining = remaining[1:]
-                else:
-                    m = STRING_CHUNK.match(remaining)
-                    if not m:
-                        raise SyntaxError('error in string literal: %s' % remaining)
-                    parts.append(m.groups()[0])
-                    remaining = remaining[m.end():]
-            else:
-                s = ''.join(parts)
-                raise SyntaxError('unterminated string: %s' % s)
-            parts.append(q)
-            result = ''.join(parts)
-            remaining = remaining[1:].lstrip() # skip past closing quote
-        return result, remaining
-
-    def marker_expr(remaining):
-        if remaining and remaining[0] == '(':
-            result, remaining = marker(remaining[1:].lstrip())
-            if remaining[0] != ')':
-                raise SyntaxError('unterminated parenthesis: %s' % remaining)
-            remaining = remaining[1:].lstrip()
-        else:
-            lhs, remaining = marker_var(remaining)
-            while remaining:
-                m = MARKER_OP.match(remaining)
-                if not m:
-                    break
-                op = m.groups()[0]
-                remaining = remaining[m.end():]
-                rhs, remaining = marker_var(remaining)
-                lhs = {'op': op, 'lhs': lhs, 'rhs': rhs}
-            result = lhs
-        return result, remaining
-
-    def marker_and(remaining):
-        lhs, remaining = marker_expr(remaining)
-        while remaining:
-            m = AND.match(remaining)
-            if not m:
-                break
-            remaining = remaining[m.end():]
-            rhs, remaining = marker_expr(remaining)
-            lhs = {'op': 'and', 'lhs': lhs, 'rhs': rhs}
-        return lhs, remaining
-
-    def marker(remaining):
-        lhs, remaining = marker_and(remaining)
-        while remaining:
-            m = OR.match(remaining)
-            if not m:
-                break
-            remaining = remaining[m.end():]
-            rhs, remaining = marker_and(remaining)
-            lhs = {'op': 'or', 'lhs': lhs, 'rhs': rhs}
-        return lhs, remaining
-
-    return marker(marker_string)
-
-
-def parse_requirement(req):
-    """
-    Parse a requirement passed in as a string. Return a Container
-    whose attributes contain the various parts of the requirement.
-    """
-    remaining = req.strip()
-    if not remaining or remaining.startswith('#'):
-        return None
-    m = IDENTIFIER.match(remaining)
-    if not m:
-        raise SyntaxError('name expected: %s' % remaining)
-    distname = m.groups()[0]
-    remaining = remaining[m.end():]
-    extras = mark_expr = versions = uri = None
-    if remaining and remaining[0] == '[':
-        i = remaining.find(']', 1)
-        if i < 0:
-            raise SyntaxError('unterminated extra: %s' % remaining)
-        s = remaining[1:i]
-        remaining = remaining[i + 1:].lstrip()
-        extras = []
-        while s:
-            m = IDENTIFIER.match(s)
-            if not m:
-                raise SyntaxError('malformed extra: %s' % s)
-            extras.append(m.groups()[0])
-            s = s[m.end():]
-            if not s:
-                break
-            if s[0] != ',':
-                raise SyntaxError('comma expected in extras: %s' % s)
-            s = s[1:].lstrip()
-        if not extras:
-            extras = None
-    if remaining:
-        if remaining[0] == '@':
-            # it's a URI
-            remaining = remaining[1:].lstrip()
-            m = NON_SPACE.match(remaining)
-            if not m:
-                raise SyntaxError('invalid URI: %s' % remaining)
-            uri = m.groups()[0]
-            t = urlparse(uri)
-            # there are issues with Python and URL parsing, so this test
-            # is a bit crude. See bpo-20271, bpo-23505. Python doesn't
-            # always parse invalid URLs correctly - it should raise
-            # exceptions for malformed URLs
-            if not (t.scheme and t.netloc):
-                raise SyntaxError('Invalid URL: %s' % uri)
-            remaining = remaining[m.end():].lstrip()
-        else:
-
-            def get_versions(ver_remaining):
-                """
-                Return a list of operator, version tuples if any are
-                specified, else None.
-                """
-                m = COMPARE_OP.match(ver_remaining)
-                versions = None
-                if m:
-                    versions = []
-                    while True:
-                        op = m.groups()[0]
-                        ver_remaining = ver_remaining[m.end():]
-                        m = VERSION_IDENTIFIER.match(ver_remaining)
-                        if not m:
-                            raise SyntaxError('invalid version: %s' % ver_remaining)
-                        v = m.groups()[0]
-                        versions.append((op, v))
-                        ver_remaining = ver_remaining[m.end():]
-                        if not ver_remaining or ver_remaining[0] != ',':
-                            break
-                        ver_remaining = ver_remaining[1:].lstrip()
-                        m = COMPARE_OP.match(ver_remaining)
-                        if not m:
-                            raise SyntaxError('invalid constraint: %s' % ver_remaining)
-                    if not versions:
-                        versions = None
-                return versions, ver_remaining
-
-            if remaining[0] != '(':
-                versions, remaining = get_versions(remaining)
-            else:
-                i = remaining.find(')', 1)
-                if i < 0:
-                    raise SyntaxError('unterminated parenthesis: %s' % remaining)
-                s = remaining[1:i]
-                remaining = remaining[i + 1:].lstrip()
-                # As a special diversion from PEP 508, allow a version number
-                # a.b.c in parentheses as a synonym for ~= a.b.c (because this
-                # is allowed in earlier PEPs)
-                if COMPARE_OP.match(s):
-                    versions, _ = get_versions(s)
-                else:
-                    m = VERSION_IDENTIFIER.match(s)
-                    if not m:
-                        raise SyntaxError('invalid constraint: %s' % s)
-                    v = m.groups()[0]
-                    s = s[m.end():].lstrip()
-                    if s:
-                        raise SyntaxError('invalid constraint: %s' % s)
-                    versions = [('~=', v)]
-
-    if remaining:
-        if remaining[0] != ';':
-            raise SyntaxError('invalid requirement: %s' % remaining)
-        remaining = remaining[1:].lstrip()
-
-        mark_expr, remaining = parse_marker(remaining)
-
-    if remaining and remaining[0] != '#':
-        raise SyntaxError('unexpected trailing data: %s' % remaining)
-
-    if not versions:
-        rs = distname
-    else:
-        rs = '%s %s' % (distname, ', '.join(['%s %s' % con for con in versions]))
-    return Container(name=distname, extras=extras, constraints=versions,
-                     marker=mark_expr, url=uri, requirement=rs)
-
-
-def get_resources_dests(resources_root, rules):
-    """Find destinations for resources files"""
-
-    def get_rel_path(root, path):
-        # normalizes and returns a lstripped-/-separated path
-        root = root.replace(os.path.sep, '/')
-        path = path.replace(os.path.sep, '/')
-        assert path.startswith(root)
-        return path[len(root):].lstrip('/')
-
-    destinations = {}
-    for base, suffix, dest in rules:
-        prefix = os.path.join(resources_root, base)
-        for abs_base in iglob(prefix):
-            abs_glob = os.path.join(abs_base, suffix)
-            for abs_path in iglob(abs_glob):
-                resource_file = get_rel_path(resources_root, abs_path)
-                if dest is None:  # remove the entry if it was here
-                    destinations.pop(resource_file, None)
-                else:
-                    rel_path = get_rel_path(abs_base, abs_path)
-                    rel_dest = dest.replace(os.path.sep, '/').rstrip('/')
-                    destinations[resource_file] = rel_dest + '/' + rel_path
-    return destinations
-
-
-def in_venv():
-    if hasattr(sys, 'real_prefix'):
-        # virtualenv venvs
-        result = True
-    else:
-        # PEP 405 venvs
-        result = sys.prefix != getattr(sys, 'base_prefix', sys.prefix)
-    return result
-
-
-def get_executable():
-# The __PYVENV_LAUNCHER__ dance is apparently no longer needed, as
-# changes to the stub launcher mean that sys.executable always points
-# to the stub on OS X
-#    if sys.platform == 'darwin' and ('__PYVENV_LAUNCHER__'
-#                                     in os.environ):
-#        result =  os.environ['__PYVENV_LAUNCHER__']
-#    else:
-#        result = sys.executable
-#    return result
-    result = os.path.normcase(sys.executable)
-    if not isinstance(result, text_type):
-        result = fsdecode(result)
-    return result
-
-
-def proceed(prompt, allowed_chars, error_prompt=None, default=None):
-    p = prompt
-    while True:
-        s = raw_input(p)
-        p = prompt
-        if not s and default:
-            s = default
-        if s:
-            c = s[0].lower()
-            if c in allowed_chars:
-                break
-            if error_prompt:
-                p = '%c: %s\n%s' % (c, error_prompt, prompt)
-    return c
-
-
-def extract_by_key(d, keys):
-    if isinstance(keys, string_types):
-        keys = keys.split()
-    result = {}
-    for key in keys:
-        if key in d:
-            result[key] = d[key]
-    return result
-
-def read_exports(stream):
-    if sys.version_info[0] >= 3:
-        # needs to be a text stream
-        stream = codecs.getreader('utf-8')(stream)
-    # Try to load as JSON, falling back on legacy format
-    data = stream.read()
-    stream = StringIO(data)
-    try:
-        jdata = json.load(stream)
-        result = jdata['extensions']['python.exports']['exports']
-        for group, entries in result.items():
-            for k, v in entries.items():
-                s = '%s = %s' % (k, v)
-                entry = get_export_entry(s)
-                assert entry is not None
-                entries[k] = entry
-        return result
-    except Exception:
-        stream.seek(0, 0)
-
-    def read_stream(cp, stream):
-        if hasattr(cp, 'read_file'):
-            cp.read_file(stream)
-        else:
-            cp.readfp(stream)
-
-    cp = configparser.ConfigParser()
-    try:
-        read_stream(cp, stream)
-    except configparser.MissingSectionHeaderError:
-        stream.close()
-        data = textwrap.dedent(data)
-        stream = StringIO(data)
-        read_stream(cp, stream)
-
-    result = {}
-    for key in cp.sections():
-        result[key] = entries = {}
-        for name, value in cp.items(key):
-            s = '%s = %s' % (name, value)
-            entry = get_export_entry(s)
-            assert entry is not None
-            #entry.dist = self
-            entries[name] = entry
-    return result
-
-
-def write_exports(exports, stream):
-    if sys.version_info[0] >= 3:
-        # needs to be a text stream
-        stream = codecs.getwriter('utf-8')(stream)
-    cp = configparser.ConfigParser()
-    for k, v in exports.items():
-        # TODO check k, v for valid values
-        cp.add_section(k)
-        for entry in v.values():
-            if entry.suffix is None:
-                s = entry.prefix
-            else:
-                s = '%s:%s' % (entry.prefix, entry.suffix)
-            if entry.flags:
-                s = '%s [%s]' % (s, ', '.join(entry.flags))
-            cp.set(k, entry.name, s)
-    cp.write(stream)
-
-
-@contextlib.contextmanager
-def tempdir():
-    td = tempfile.mkdtemp()
-    try:
-        yield td
-    finally:
-        shutil.rmtree(td)
-
-@contextlib.contextmanager
-def chdir(d):
-    cwd = os.getcwd()
-    try:
-        os.chdir(d)
-        yield
-    finally:
-        os.chdir(cwd)
-
-
-@contextlib.contextmanager
-def socket_timeout(seconds=15):
-    cto = socket.getdefaulttimeout()
-    try:
-        socket.setdefaulttimeout(seconds)
-        yield
-    finally:
-        socket.setdefaulttimeout(cto)
-
-
-class cached_property(object):
-    def __init__(self, func):
-        self.func = func
-        #for attr in ('__name__', '__module__', '__doc__'):
-        #    setattr(self, attr, getattr(func, attr, None))
-
-    def __get__(self, obj, cls=None):
-        if obj is None:
-            return self
-        value = self.func(obj)
-        object.__setattr__(obj, self.func.__name__, value)
-        #obj.__dict__[self.func.__name__] = value = self.func(obj)
-        return value
-
-def convert_path(pathname):
-    """Return 'pathname' as a name that will work on the native filesystem.
-
-    The path is split on '/' and put back together again using the current
-    directory separator.  Needed because filenames in the setup script are
-    always supplied in Unix style, and have to be converted to the local
-    convention before we can actually use them in the filesystem.  Raises
-    ValueError on non-Unix-ish systems if 'pathname' either starts or
-    ends with a slash.
-    """
-    if os.sep == '/':
-        return pathname
-    if not pathname:
-        return pathname
-    if pathname[0] == '/':
-        raise ValueError("path '%s' cannot be absolute" % pathname)
-    if pathname[-1] == '/':
-        raise ValueError("path '%s' cannot end with '/'" % pathname)
-
-    paths = pathname.split('/')
-    while os.curdir in paths:
-        paths.remove(os.curdir)
-    if not paths:
-        return os.curdir
-    return os.path.join(*paths)
-
-
-class FileOperator(object):
-    def __init__(self, dry_run=False):
-        self.dry_run = dry_run
-        self.ensured = set()
-        self._init_record()
-
-    def _init_record(self):
-        self.record = False
-        self.files_written = set()
-        self.dirs_created = set()
-
-    def record_as_written(self, path):
-        if self.record:
-            self.files_written.add(path)
-
-    def newer(self, source, target):
-        """Tell if the target is newer than the source.
-
-        Returns true if 'source' exists and is more recently modified than
-        'target', or if 'source' exists and 'target' doesn't.
-
-        Returns false if both exist and 'target' is the same age or younger
-        than 'source'. Raise PackagingFileError if 'source' does not exist.
-
-        Note that this test is not very accurate: files created in the same
-        second will have the same "age".
-        """
-        if not os.path.exists(source):
-            raise DistlibException("file '%r' does not exist" %
-                                   os.path.abspath(source))
-        if not os.path.exists(target):
-            return True
-
-        return os.stat(source).st_mtime > os.stat(target).st_mtime
-
-    def copy_file(self, infile, outfile, check=True):
-        """Copy a file respecting dry-run and force flags.
-        """
-        self.ensure_dir(os.path.dirname(outfile))
-        logger.info('Copying %s to %s', infile, outfile)
-        if not self.dry_run:
-            msg = None
-            if check:
-                if os.path.islink(outfile):
-                    msg = '%s is a symlink' % outfile
-                elif os.path.exists(outfile) and not os.path.isfile(outfile):
-                    msg = '%s is a non-regular file' % outfile
-            if msg:
-                raise ValueError(msg + ' which would be overwritten')
-            shutil.copyfile(infile, outfile)
-        self.record_as_written(outfile)
-
-    def copy_stream(self, instream, outfile, encoding=None):
-        assert not os.path.isdir(outfile)
-        self.ensure_dir(os.path.dirname(outfile))
-        logger.info('Copying stream %s to %s', instream, outfile)
-        if not self.dry_run:
-            if encoding is None:
-                outstream = open(outfile, 'wb')
-            else:
-                outstream = codecs.open(outfile, 'w', encoding=encoding)
-            try:
-                shutil.copyfileobj(instream, outstream)
-            finally:
-                outstream.close()
-        self.record_as_written(outfile)
-
-    def write_binary_file(self, path, data):
-        self.ensure_dir(os.path.dirname(path))
-        if not self.dry_run:
-            if os.path.exists(path):
-                os.remove(path)
-            with open(path, 'wb') as f:
-                f.write(data)
-        self.record_as_written(path)
-
-    def write_text_file(self, path, data, encoding):
-        self.write_binary_file(path, data.encode(encoding))
-
-    def set_mode(self, bits, mask, files):
-        if os.name == 'posix' or (os.name == 'java' and os._name == 'posix'):
-            # Set the executable bits (owner, group, and world) on
-            # all the files specified.
-            for f in files:
-                if self.dry_run:
-                    logger.info("changing mode of %s", f)
-                else:
-                    mode = (os.stat(f).st_mode | bits) & mask
-                    logger.info("changing mode of %s to %o", f, mode)
-                    os.chmod(f, mode)
-
-    set_executable_mode = lambda s, f: s.set_mode(0o555, 0o7777, f)
-
-    def ensure_dir(self, path):
-        path = os.path.abspath(path)
-        if path not in self.ensured and not os.path.exists(path):
-            self.ensured.add(path)
-            d, f = os.path.split(path)
-            self.ensure_dir(d)
-            logger.info('Creating %s' % path)
-            if not self.dry_run:
-                os.mkdir(path)
-            if self.record:
-                self.dirs_created.add(path)
-
-    def byte_compile(self, path, optimize=False, force=False, prefix=None, hashed_invalidation=False):
-        dpath = cache_from_source(path, not optimize)
-        logger.info('Byte-compiling %s to %s', path, dpath)
-        if not self.dry_run:
-            if force or self.newer(path, dpath):
-                if not prefix:
-                    diagpath = None
-                else:
-                    assert path.startswith(prefix)
-                    diagpath = path[len(prefix):]
-            compile_kwargs = {}
-            if hashed_invalidation and hasattr(py_compile, 'PycInvalidationMode'):
-                compile_kwargs['invalidation_mode'] = py_compile.PycInvalidationMode.CHECKED_HASH
-            py_compile.compile(path, dpath, diagpath, True, **compile_kwargs)     # raise error
-        self.record_as_written(dpath)
-        return dpath
-
-    def ensure_removed(self, path):
-        if os.path.exists(path):
-            if os.path.isdir(path) and not os.path.islink(path):
-                logger.debug('Removing directory tree at %s', path)
-                if not self.dry_run:
-                    shutil.rmtree(path)
-                if self.record:
-                    if path in self.dirs_created:
-                        self.dirs_created.remove(path)
-            else:
-                if os.path.islink(path):
-                    s = 'link'
-                else:
-                    s = 'file'
-                logger.debug('Removing %s %s', s, path)
-                if not self.dry_run:
-                    os.remove(path)
-                if self.record:
-                    if path in self.files_written:
-                        self.files_written.remove(path)
-
-    def is_writable(self, path):
-        result = False
-        while not result:
-            if os.path.exists(path):
-                result = os.access(path, os.W_OK)
-                break
-            parent = os.path.dirname(path)
-            if parent == path:
-                break
-            path = parent
-        return result
-
-    def commit(self):
-        """
-        Commit recorded changes, turn off recording, return
-        changes.
-        """
-        assert self.record
-        result = self.files_written, self.dirs_created
-        self._init_record()
-        return result
-
-    def rollback(self):
-        if not self.dry_run:
-            for f in list(self.files_written):
-                if os.path.exists(f):
-                    os.remove(f)
-            # dirs should all be empty now, except perhaps for
-            # __pycache__ subdirs
-            # reverse so that subdirs appear before their parents
-            dirs = sorted(self.dirs_created, reverse=True)
-            for d in dirs:
-                flist = os.listdir(d)
-                if flist:
-                    assert flist == ['__pycache__']
-                    sd = os.path.join(d, flist[0])
-                    os.rmdir(sd)
-                os.rmdir(d)     # should fail if non-empty
-        self._init_record()
-
-def resolve(module_name, dotted_path):
-    if module_name in sys.modules:
-        mod = sys.modules[module_name]
-    else:
-        mod = __import__(module_name)
-    if dotted_path is None:
-        result = mod
-    else:
-        parts = dotted_path.split('.')
-        result = getattr(mod, parts.pop(0))
-        for p in parts:
-            result = getattr(result, p)
-    return result
-
-
-class ExportEntry(object):
-    def __init__(self, name, prefix, suffix, flags):
-        self.name = name
-        self.prefix = prefix
-        self.suffix = suffix
-        self.flags = flags
-
-    @cached_property
-    def value(self):
-        return resolve(self.prefix, self.suffix)
-
-    def __repr__(self):  # pragma: no cover
-        return '<ExportEntry %s = %s:%s %s>' % (self.name, self.prefix,
-                                                self.suffix, self.flags)
-
-    def __eq__(self, other):
-        if not isinstance(other, ExportEntry):
-            result = False
-        else:
-            result = (self.name == other.name and
-                      self.prefix == other.prefix and
-                      self.suffix == other.suffix and
-                      self.flags == other.flags)
-        return result
-
-    __hash__ = object.__hash__
-
-
-ENTRY_RE = re.compile(r'''(?P<name>(\w|[-.+])+)
-                      \s*=\s*(?P<callable>(\w+)([:\.]\w+)*)
-                      \s*(\[\s*(?P<flags>\w+(=\w+)?(,\s*\w+(=\w+)?)*)\s*\])?
-                      ''', re.VERBOSE)
-
-def get_export_entry(specification):
-    m = ENTRY_RE.search(specification)
-    if not m:
-        result = None
-        if '[' in specification or ']' in specification:
-            raise DistlibException("Invalid specification "
-                                   "'%s'" % specification)
-    else:
-        d = m.groupdict()
-        name = d['name']
-        path = d['callable']
-        colons = path.count(':')
-        if colons == 0:
-            prefix, suffix = path, None
-        else:
-            if colons != 1:
-                raise DistlibException("Invalid specification "
-                                       "'%s'" % specification)
-            prefix, suffix = path.split(':')
-        flags = d['flags']
-        if flags is None:
-            if '[' in specification or ']' in specification:
-                raise DistlibException("Invalid specification "
-                                       "'%s'" % specification)
-            flags = []
-        else:
-            flags = [f.strip() for f in flags.split(',')]
-        result = ExportEntry(name, prefix, suffix, flags)
-    return result
-
-
-def get_cache_base(suffix=None):
-    """
-    Return the default base location for distlib caches. If the directory does
-    not exist, it is created. Use the suffix provided for the base directory,
-    and default to '.distlib' if it isn't provided.
-
-    On Windows, if LOCALAPPDATA is defined in the environment, then it is
-    assumed to be a directory, and will be the parent directory of the result.
-    On POSIX, and on Windows if LOCALAPPDATA is not defined, the user's home
-    directory - using os.expanduser('~') - will be the parent directory of
-    the result.
-
-    The result is just the directory '.distlib' in the parent directory as
-    determined above, or with the name specified with ``suffix``.
-    """
-    if suffix is None:
-        suffix = '.distlib'
-    if os.name == 'nt' and 'LOCALAPPDATA' in os.environ:
-        result = os.path.expandvars('$localappdata')
-    else:
-        # Assume posix, or old Windows
-        result = os.path.expanduser('~')
-    # we use 'isdir' instead of 'exists', because we want to
-    # fail if there's a file with that name
-    if os.path.isdir(result):
-        usable = os.access(result, os.W_OK)
-        if not usable:
-            logger.warning('Directory exists but is not writable: %s', result)
-    else:
-        try:
-            os.makedirs(result)
-            usable = True
-        except OSError:
-            logger.warning('Unable to create %s', result, exc_info=True)
-            usable = False
-    if not usable:
-        result = tempfile.mkdtemp()
-        logger.warning('Default location unusable, using %s', result)
-    return os.path.join(result, suffix)
-
-
-def path_to_cache_dir(path):
-    """
-    Convert an absolute path to a directory name for use in a cache.
-
-    The algorithm used is:
-
-    #. On Windows, any ``':'`` in the drive is replaced with ``'---'``.
-    #. Any occurrence of ``os.sep`` is replaced with ``'--'``.
-    #. ``'.cache'`` is appended.
-    """
-    d, p = os.path.splitdrive(os.path.abspath(path))
-    if d:
-        d = d.replace(':', '---')
-    p = p.replace(os.sep, '--')
-    return d + p + '.cache'
-
-
-def ensure_slash(s):
-    if not s.endswith('/'):
-        return s + '/'
-    return s
-
-
-def parse_credentials(netloc):
-    username = password = None
-    if '@' in netloc:
-        prefix, netloc = netloc.split('@', 1)
-        if ':' not in prefix:
-            username = prefix
-        else:
-            username, password = prefix.split(':', 1)
-    return username, password, netloc
-
-
-def get_process_umask():
-    result = os.umask(0o22)
-    os.umask(result)
-    return result
-
-def is_string_sequence(seq):
-    result = True
-    i = None
-    for i, s in enumerate(seq):
-        if not isinstance(s, string_types):
-            result = False
-            break
-    assert i is not None
-    return result
-
-PROJECT_NAME_AND_VERSION = re.compile('([a-z0-9_]+([.-][a-z_][a-z0-9_]*)*)-'
-                                      '([a-z0-9_.+-]+)', re.I)
-PYTHON_VERSION = re.compile(r'-py(\d\.?\d?)')
-
-
-def split_filename(filename, project_name=None):
-    """
-    Extract name, version, python version from a filename (no extension)
-
-    Return name, version, pyver or None
-    """
-    result = None
-    pyver = None
-    filename = unquote(filename).replace(' ', '-')
-    m = PYTHON_VERSION.search(filename)
-    if m:
-        pyver = m.group(1)
-        filename = filename[:m.start()]
-    if project_name and len(filename) > len(project_name) + 1:
-        m = re.match(re.escape(project_name) + r'\b', filename)
-        if m:
-            n = m.end()
-            result = filename[:n], filename[n + 1:], pyver
-    if result is None:
-        m = PROJECT_NAME_AND_VERSION.match(filename)
-        if m:
-            result = m.group(1), m.group(3), pyver
-    return result
-
-# Allow spaces in name because of legacy dists like "Twisted Core"
-NAME_VERSION_RE = re.compile(r'(?P<name>[\w .-]+)\s*'
-                             r'\(\s*(?P<ver>[^\s)]+)\)$')
-
-def parse_name_and_version(p):
-    """
-    A utility method used to get name and version from a string.
-
-    From e.g. a Provides-Dist value.
-
-    :param p: A value in a form 'foo (1.0)'
-    :return: The name and version as a tuple.
-    """
-    m = NAME_VERSION_RE.match(p)
-    if not m:
-        raise DistlibException('Ill-formed name/version string: \'%s\'' % p)
-    d = m.groupdict()
-    return d['name'].strip().lower(), d['ver']
-
-def get_extras(requested, available):
-    result = set()
-    requested = set(requested or [])
-    available = set(available or [])
-    if '*' in requested:
-        requested.remove('*')
-        result |= available
-    for r in requested:
-        if r == '-':
-            result.add(r)
-        elif r.startswith('-'):
-            unwanted = r[1:]
-            if unwanted not in available:
-                logger.warning('undeclared extra: %s' % unwanted)
-            if unwanted in result:
-                result.remove(unwanted)
-        else:
-            if r not in available:
-                logger.warning('undeclared extra: %s' % r)
-            result.add(r)
-    return result
-#
-# Extended metadata functionality
-#
-
-def _get_external_data(url):
-    result = {}
-    try:
-        # urlopen might fail if it runs into redirections,
-        # because of Python issue #13696. Fixed in locators
-        # using a custom redirect handler.
-        resp = urlopen(url)
-        headers = resp.info()
-        ct = headers.get('Content-Type')
-        if not ct.startswith('application/json'):
-            logger.debug('Unexpected response for JSON request: %s', ct)
-        else:
-            reader = codecs.getreader('utf-8')(resp)
-            #data = reader.read().decode('utf-8')
-            #result = json.loads(data)
-            result = json.load(reader)
-    except Exception as e:
-        logger.exception('Failed to get external data for %s: %s', url, e)
-    return result
-
-_external_data_base_url = 'https://www.red-dove.com/pypi/projects/'
-
-def get_project_data(name):
-    url = '%s/%s/project.json' % (name[0].upper(), name)
-    url = urljoin(_external_data_base_url, url)
-    result = _get_external_data(url)
-    return result
-
-def get_package_data(name, version):
-    url = '%s/%s/package-%s.json' % (name[0].upper(), name, version)
-    url = urljoin(_external_data_base_url, url)
-    return _get_external_data(url)
-
-
-class Cache(object):
-    """
-    A class implementing a cache for resources that need to live in the file system
-    e.g. shared libraries. This class was moved from resources to here because it
-    could be used by other modules, e.g. the wheel module.
-    """
-
-    def __init__(self, base):
-        """
-        Initialise an instance.
-
-        :param base: The base directory where the cache should be located.
-        """
-        # we use 'isdir' instead of 'exists', because we want to
-        # fail if there's a file with that name
-        if not os.path.isdir(base):  # pragma: no cover
-            os.makedirs(base)
-        if (os.stat(base).st_mode & 0o77) != 0:
-            logger.warning('Directory \'%s\' is not private', base)
-        self.base = os.path.abspath(os.path.normpath(base))
-
-    def prefix_to_dir(self, prefix):
-        """
-        Converts a resource prefix to a directory name in the cache.
-        """
-        return path_to_cache_dir(prefix)
-
-    def clear(self):
-        """
-        Clear the cache.
-        """
-        not_removed = []
-        for fn in os.listdir(self.base):
-            fn = os.path.join(self.base, fn)
-            try:
-                if os.path.islink(fn) or os.path.isfile(fn):
-                    os.remove(fn)
-                elif os.path.isdir(fn):
-                    shutil.rmtree(fn)
-            except Exception:
-                not_removed.append(fn)
-        return not_removed
-
-
-class EventMixin(object):
-    """
-    A very simple publish/subscribe system.
-    """
-    def __init__(self):
-        self._subscribers = {}
-
-    def add(self, event, subscriber, append=True):
-        """
-        Add a subscriber for an event.
-
-        :param event: The name of an event.
-        :param subscriber: The subscriber to be added (and called when the
-                           event is published).
-        :param append: Whether to append or prepend the subscriber to an
-                       existing subscriber list for the event.
-        """
-        subs = self._subscribers
-        if event not in subs:
-            subs[event] = deque([subscriber])
-        else:
-            sq = subs[event]
-            if append:
-                sq.append(subscriber)
-            else:
-                sq.appendleft(subscriber)
-
-    def remove(self, event, subscriber):
-        """
-        Remove a subscriber for an event.
-
-        :param event: The name of an event.
-        :param subscriber: The subscriber to be removed.
-        """
-        subs = self._subscribers
-        if event not in subs:
-            raise ValueError('No subscribers: %r' % event)
-        subs[event].remove(subscriber)
-
-    def get_subscribers(self, event):
-        """
-        Return an iterator for the subscribers for an event.
-        :param event: The event to return subscribers for.
-        """
-        return iter(self._subscribers.get(event, ()))
-
-    def publish(self, event, *args, **kwargs):
-        """
-        Publish a event and return a list of values returned by its
-        subscribers.
-
-        :param event: The event to publish.
-        :param args: The positional arguments to pass to the event's
-                     subscribers.
-        :param kwargs: The keyword arguments to pass to the event's
-                       subscribers.
-        """
-        result = []
-        for subscriber in self.get_subscribers(event):
-            try:
-                value = subscriber(event, *args, **kwargs)
-            except Exception:
-                logger.exception('Exception during event publication')
-                value = None
-            result.append(value)
-        logger.debug('publish %s: args = %s, kwargs = %s, result = %s',
-                     event, args, kwargs, result)
-        return result
-
-#
-# Simple sequencing
-#
-class Sequencer(object):
-    def __init__(self):
-        self._preds = {}
-        self._succs = {}
-        self._nodes = set()     # nodes with no preds/succs
-
-    def add_node(self, node):
-        self._nodes.add(node)
-
-    def remove_node(self, node, edges=False):
-        if node in self._nodes:
-            self._nodes.remove(node)
-        if edges:
-            for p in set(self._preds.get(node, ())):
-                self.remove(p, node)
-            for s in set(self._succs.get(node, ())):
-                self.remove(node, s)
-            # Remove empties
-            for k, v in list(self._preds.items()):
-                if not v:
-                    del self._preds[k]
-            for k, v in list(self._succs.items()):
-                if not v:
-                    del self._succs[k]
-
-    def add(self, pred, succ):
-        assert pred != succ
-        self._preds.setdefault(succ, set()).add(pred)
-        self._succs.setdefault(pred, set()).add(succ)
-
-    def remove(self, pred, succ):
-        assert pred != succ
-        try:
-            preds = self._preds[succ]
-            succs = self._succs[pred]
-        except KeyError:  # pragma: no cover
-            raise ValueError('%r not a successor of anything' % succ)
-        try:
-            preds.remove(pred)
-            succs.remove(succ)
-        except KeyError:  # pragma: no cover
-            raise ValueError('%r not a successor of %r' % (succ, pred))
-
-    def is_step(self, step):
-        return (step in self._preds or step in self._succs or
-                step in self._nodes)
-
-    def get_steps(self, final):
-        if not self.is_step(final):
-            raise ValueError('Unknown: %r' % final)
-        result = []
-        todo = []
-        seen = set()
-        todo.append(final)
-        while todo:
-            step = todo.pop(0)
-            if step in seen:
-                # if a step was already seen,
-                # move it to the end (so it will appear earlier
-                # when reversed on return) ... but not for the
-                # final step, as that would be confusing for
-                # users
-                if step != final:
-                    result.remove(step)
-                    result.append(step)
-            else:
-                seen.add(step)
-                result.append(step)
-                preds = self._preds.get(step, ())
-                todo.extend(preds)
-        return reversed(result)
-
-    @property
-    def strong_connections(self):
-        #http://en.wikipedia.org/wiki/Tarjan%27s_strongly_connected_components_algorithm
-        index_counter = [0]
-        stack = []
-        lowlinks = {}
-        index = {}
-        result = []
-
-        graph = self._succs
-
-        def strongconnect(node):
-            # set the depth index for this node to the smallest unused index
-            index[node] = index_counter[0]
-            lowlinks[node] = index_counter[0]
-            index_counter[0] += 1
-            stack.append(node)
-
-            # Consider successors
-            try:
-                successors = graph[node]
-            except Exception:
-                successors = []
-            for successor in successors:
-                if successor not in lowlinks:
-                    # Successor has not yet been visited
-                    strongconnect(successor)
-                    lowlinks[node] = min(lowlinks[node],lowlinks[successor])
-                elif successor in stack:
-                    # the successor is in the stack and hence in the current
-                    # strongly connected component (SCC)
-                    lowlinks[node] = min(lowlinks[node],index[successor])
-
-            # If `node` is a root node, pop the stack and generate an SCC
-            if lowlinks[node] == index[node]:
-                connected_component = []
-
-                while True:
-                    successor = stack.pop()
-                    connected_component.append(successor)
-                    if successor == node: break
-                component = tuple(connected_component)
-                # storing the result
-                result.append(component)
-
-        for node in graph:
-            if node not in lowlinks:
-                strongconnect(node)
-
-        return result
-
-    @property
-    def dot(self):
-        result = ['digraph G {']
-        for succ in self._preds:
-            preds = self._preds[succ]
-            for pred in preds:
-                result.append('  %s -> %s;' % (pred, succ))
-        for node in self._nodes:
-            result.append('  %s;' % node)
-        result.append('}')
-        return '\n'.join(result)
-
-#
-# Unarchiving functionality for zip, tar, tgz, tbz, whl
-#
-
-ARCHIVE_EXTENSIONS = ('.tar.gz', '.tar.bz2', '.tar', '.zip',
-                      '.tgz', '.tbz', '.whl')
-
-def unarchive(archive_filename, dest_dir, format=None, check=True):
-
-    def check_path(path):
-        if not isinstance(path, text_type):
-            path = path.decode('utf-8')
-        p = os.path.abspath(os.path.join(dest_dir, path))
-        if not p.startswith(dest_dir) or p[plen] != os.sep:
-            raise ValueError('path outside destination: %r' % p)
-
-    dest_dir = os.path.abspath(dest_dir)
-    plen = len(dest_dir)
-    archive = None
-    if format is None:
-        if archive_filename.endswith(('.zip', '.whl')):
-            format = 'zip'
-        elif archive_filename.endswith(('.tar.gz', '.tgz')):
-            format = 'tgz'
-            mode = 'r:gz'
-        elif archive_filename.endswith(('.tar.bz2', '.tbz')):
-            format = 'tbz'
-            mode = 'r:bz2'
-        elif archive_filename.endswith('.tar'):
-            format = 'tar'
-            mode = 'r'
-        else:  # pragma: no cover
-            raise ValueError('Unknown format for %r' % archive_filename)
-    try:
-        if format == 'zip':
-            archive = ZipFile(archive_filename, 'r')
-            if check:
-                names = archive.namelist()
-                for name in names:
-                    check_path(name)
-        else:
-            archive = tarfile.open(archive_filename, mode)
-            if check:
-                names = archive.getnames()
-                for name in names:
-                    check_path(name)
-        if format != 'zip' and sys.version_info[0] < 3:
-            # See Python issue 17153. If the dest path contains Unicode,
-            # tarfile extraction fails on Python 2.x if a member path name
-            # contains non-ASCII characters - it leads to an implicit
-            # bytes -> unicode conversion using ASCII to decode.
-            for tarinfo in archive.getmembers():
-                if not isinstance(tarinfo.name, text_type):
-                    tarinfo.name = tarinfo.name.decode('utf-8')
-        archive.extractall(dest_dir)
-
-    finally:
-        if archive:
-            archive.close()
-
-
-def zip_dir(directory):
-    """zip a directory tree into a BytesIO object"""
-    result = io.BytesIO()
-    dlen = len(directory)
-    with ZipFile(result, "w") as zf:
-        for root, dirs, files in os.walk(directory):
-            for name in files:
-                full = os.path.join(root, name)
-                rel = root[dlen:]
-                dest = os.path.join(rel, name)
-                zf.write(full, dest)
-    return result
-
-#
-# Simple progress bar
-#
-
-UNITS = ('', 'K', 'M', 'G','T','P')
-
-
-class Progress(object):
-    unknown = 'UNKNOWN'
-
-    def __init__(self, minval=0, maxval=100):
-        assert maxval is None or maxval >= minval
-        self.min = self.cur = minval
-        self.max = maxval
-        self.started = None
-        self.elapsed = 0
-        self.done = False
-
-    def update(self, curval):
-        assert self.min <= curval
-        assert self.max is None or curval <= self.max
-        self.cur = curval
-        now = time.time()
-        if self.started is None:
-            self.started = now
-        else:
-            self.elapsed = now - self.started
-
-    def increment(self, incr):
-        assert incr >= 0
-        self.update(self.cur + incr)
-
-    def start(self):
-        self.update(self.min)
-        return self
-
-    def stop(self):
-        if self.max is not None:
-            self.update(self.max)
-        self.done = True
-
-    @property
-    def maximum(self):
-        return self.unknown if self.max is None else self.max
-
-    @property
-    def percentage(self):
-        if self.done:
-            result = '100 %'
-        elif self.max is None:
-            result = ' ?? %'
-        else:
-            v = 100.0 * (self.cur - self.min) / (self.max - self.min)
-            result = '%3d %%' % v
-        return result
-
-    def format_duration(self, duration):
-        if (duration <= 0) and self.max is None or self.cur == self.min:
-            result = '??:??:??'
-        #elif duration < 1:
-        #    result = '--:--:--'
-        else:
-            result = time.strftime('%H:%M:%S', time.gmtime(duration))
-        return result
-
-    @property
-    def ETA(self):
-        if self.done:
-            prefix = 'Done'
-            t = self.elapsed
-            #import pdb; pdb.set_trace()
-        else:
-            prefix = 'ETA '
-            if self.max is None:
-                t = -1
-            elif self.elapsed == 0 or (self.cur == self.min):
-                t = 0
-            else:
-                #import pdb; pdb.set_trace()
-                t = float(self.max - self.min)
-                t /= self.cur - self.min
-                t = (t - 1) * self.elapsed
-        return '%s: %s' % (prefix, self.format_duration(t))
-
-    @property
-    def speed(self):
-        if self.elapsed == 0:
-            result = 0.0
-        else:
-            result = (self.cur - self.min) / self.elapsed
-        for unit in UNITS:
-            if result < 1000:
-                break
-            result /= 1000.0
-        return '%d %sB/s' % (result, unit)
-
-#
-# Glob functionality
-#
-
-RICH_GLOB = re.compile(r'\{([^}]*)\}')
-_CHECK_RECURSIVE_GLOB = re.compile(r'[^/\\,{]\*\*|\*\*[^/\\,}]')
-_CHECK_MISMATCH_SET = re.compile(r'^[^{]*\}|\{[^}]*$')
-
-
-def iglob(path_glob):
-    """Extended globbing function that supports ** and {opt1,opt2,opt3}."""
-    if _CHECK_RECURSIVE_GLOB.search(path_glob):
-        msg = """invalid glob %r: recursive glob "**" must be used alone"""
-        raise ValueError(msg % path_glob)
-    if _CHECK_MISMATCH_SET.search(path_glob):
-        msg = """invalid glob %r: mismatching set marker '{' or '}'"""
-        raise ValueError(msg % path_glob)
-    return _iglob(path_glob)
-
-
-def _iglob(path_glob):
-    rich_path_glob = RICH_GLOB.split(path_glob, 1)
-    if len(rich_path_glob) > 1:
-        assert len(rich_path_glob) == 3, rich_path_glob
-        prefix, set, suffix = rich_path_glob
-        for item in set.split(','):
-            for path in _iglob(''.join((prefix, item, suffix))):
-                yield path
-    else:
-        if '**' not in path_glob:
-            for item in std_iglob(path_glob):
-                yield item
-        else:
-            prefix, radical = path_glob.split('**', 1)
-            if prefix == '':
-                prefix = '.'
-            if radical == '':
-                radical = '*'
-            else:
-                # we support both
-                radical = radical.lstrip('/')
-                radical = radical.lstrip('\\')
-            for path, dir, files in os.walk(prefix):
-                path = os.path.normpath(path)
-                for fn in _iglob(os.path.join(path, radical)):
-                    yield fn
-
-if ssl:
-    from .compat import (HTTPSHandler as BaseHTTPSHandler, match_hostname,
-                         CertificateError)
-
-
-#
-# HTTPSConnection which verifies certificates/matches domains
-#
-
-    class HTTPSConnection(httplib.HTTPSConnection):
-        ca_certs = None # set this to the path to the certs file (.pem)
-        check_domain = True # only used if ca_certs is not None
-
-        # noinspection PyPropertyAccess
-        def connect(self):
-            sock = socket.create_connection((self.host, self.port), self.timeout)
-            if getattr(self, '_tunnel_host', False):
-                self.sock = sock
-                self._tunnel()
-
-            if not hasattr(ssl, 'SSLContext'):
-                # For 2.x
-                if self.ca_certs:
-                    cert_reqs = ssl.CERT_REQUIRED
-                else:
-                    cert_reqs = ssl.CERT_NONE
-                self.sock = ssl.wrap_socket(sock, self.key_file, self.cert_file,
-                                            cert_reqs=cert_reqs,
-                                            ssl_version=ssl.PROTOCOL_SSLv23,
-                                            ca_certs=self.ca_certs)
-            else:  # pragma: no cover
-                context = ssl.SSLContext(ssl.PROTOCOL_SSLv23)
-                context.options |= ssl.OP_NO_SSLv2
-                if self.cert_file:
-                    context.load_cert_chain(self.cert_file, self.key_file)
-                kwargs = {}
-                if self.ca_certs:
-                    context.verify_mode = ssl.CERT_REQUIRED
-                    context.load_verify_locations(cafile=self.ca_certs)
-                    if getattr(ssl, 'HAS_SNI', False):
-                        kwargs['server_hostname'] = self.host
-                self.sock = context.wrap_socket(sock, **kwargs)
-            if self.ca_certs and self.check_domain:
-                try:
-                    match_hostname(self.sock.getpeercert(), self.host)
-                    logger.debug('Host verified: %s', self.host)
-                except CertificateError:  # pragma: no cover
-                    self.sock.shutdown(socket.SHUT_RDWR)
-                    self.sock.close()
-                    raise
-
-    class HTTPSHandler(BaseHTTPSHandler):
-        def __init__(self, ca_certs, check_domain=True):
-            BaseHTTPSHandler.__init__(self)
-            self.ca_certs = ca_certs
-            self.check_domain = check_domain
-
-        def _conn_maker(self, *args, **kwargs):
-            """
-            This is called to create a connection instance. Normally you'd
-            pass a connection class to do_open, but it doesn't actually check for
-            a class, and just expects a callable. As long as we behave just as a
-            constructor would have, we should be OK. If it ever changes so that
-            we *must* pass a class, we'll create an UnsafeHTTPSConnection class
-            which just sets check_domain to False in the class definition, and
-            choose which one to pass to do_open.
-            """
-            result = HTTPSConnection(*args, **kwargs)
-            if self.ca_certs:
-                result.ca_certs = self.ca_certs
-                result.check_domain = self.check_domain
-            return result
-
-        def https_open(self, req):
-            try:
-                return self.do_open(self._conn_maker, req)
-            except URLError as e:
-                if 'certificate verify failed' in str(e.reason):
-                    raise CertificateError('Unable to verify server certificate '
-                                           'for %s' % req.host)
-                else:
-                    raise
-
-    #
-    # To prevent against mixing HTTP traffic with HTTPS (examples: A Man-In-The-
-    # Middle proxy using HTTP listens on port 443, or an index mistakenly serves
-    # HTML containing a http://xyz link when it should be https://xyz),
-    # you can use the following handler class, which does not allow HTTP traffic.
-    #
-    # It works by inheriting from HTTPHandler - so build_opener won't add a
-    # handler for HTTP itself.
-    #
-    class HTTPSOnlyHandler(HTTPSHandler, HTTPHandler):
-        def http_open(self, req):
-            raise URLError('Unexpected HTTP request on what should be a secure '
-                           'connection: %s' % req)
-
-#
-# XML-RPC with timeouts
-#
-
-_ver_info = sys.version_info[:2]
-
-if _ver_info == (2, 6):
-    class HTTP(httplib.HTTP):
-        def __init__(self, host='', port=None, **kwargs):
-            if port == 0:   # 0 means use port 0, not the default port
-                port = None
-            self._setup(self._connection_class(host, port, **kwargs))
-
-
-    if ssl:
-        class HTTPS(httplib.HTTPS):
-            def __init__(self, host='', port=None, **kwargs):
-                if port == 0:   # 0 means use port 0, not the default port
-                    port = None
-                self._setup(self._connection_class(host, port, **kwargs))
-
-
-class Transport(xmlrpclib.Transport):
-    def __init__(self, timeout, use_datetime=0):
-        self.timeout = timeout
-        xmlrpclib.Transport.__init__(self, use_datetime)
-
-    def make_connection(self, host):
-        h, eh, x509 = self.get_host_info(host)
-        if _ver_info == (2, 6):
-            result = HTTP(h, timeout=self.timeout)
-        else:
-            if not self._connection or host != self._connection[0]:
-                self._extra_headers = eh
-                self._connection = host, httplib.HTTPConnection(h)
-            result = self._connection[1]
-        return result
-
-if ssl:
-    class SafeTransport(xmlrpclib.SafeTransport):
-        def __init__(self, timeout, use_datetime=0):
-            self.timeout = timeout
-            xmlrpclib.SafeTransport.__init__(self, use_datetime)
-
-        def make_connection(self, host):
-            h, eh, kwargs = self.get_host_info(host)
-            if not kwargs:
-                kwargs = {}
-            kwargs['timeout'] = self.timeout
-            if _ver_info == (2, 6):
-                result = HTTPS(host, None, **kwargs)
-            else:
-                if not self._connection or host != self._connection[0]:
-                    self._extra_headers = eh
-                    self._connection = host, httplib.HTTPSConnection(h, None,
-                                                                     **kwargs)
-                result = self._connection[1]
-            return result
-
-
-class ServerProxy(xmlrpclib.ServerProxy):
-    def __init__(self, uri, **kwargs):
-        self.timeout = timeout = kwargs.pop('timeout', None)
-        # The above classes only come into play if a timeout
-        # is specified
-        if timeout is not None:
-            scheme, _ = splittype(uri)
-            use_datetime = kwargs.get('use_datetime', 0)
-            if scheme == 'https':
-                tcls = SafeTransport
-            else:
-                tcls = Transport
-            kwargs['transport'] = t = tcls(timeout, use_datetime=use_datetime)
-            self.transport = t
-        xmlrpclib.ServerProxy.__init__(self, uri, **kwargs)
-
-#
-# CSV functionality. This is provided because on 2.x, the csv module can't
-# handle Unicode. However, we need to deal with Unicode in e.g. RECORD files.
-#
-
-def _csv_open(fn, mode, **kwargs):
-    if sys.version_info[0] < 3:
-        mode += 'b'
-    else:
-        kwargs['newline'] = ''
-        # Python 3 determines encoding from locale. Force 'utf-8'
-        # file encoding to match other forced utf-8 encoding
-        kwargs['encoding'] = 'utf-8'
-    return open(fn, mode, **kwargs)
-
-
-class CSVBase(object):
-    defaults = {
-        'delimiter': str(','),      # The strs are used because we need native
-        'quotechar': str('"'),      # str in the csv API (2.x won't take
-        'lineterminator': str('\n') # Unicode)
-    }
-
-    def __enter__(self):
-        return self
-
-    def __exit__(self, *exc_info):
-        self.stream.close()
-
-
-class CSVReader(CSVBase):
-    def __init__(self, **kwargs):
-        if 'stream' in kwargs:
-            stream = kwargs['stream']
-            if sys.version_info[0] >= 3:
-                # needs to be a text stream
-                stream = codecs.getreader('utf-8')(stream)
-            self.stream = stream
-        else:
-            self.stream = _csv_open(kwargs['path'], 'r')
-        self.reader = csv.reader(self.stream, **self.defaults)
-
-    def __iter__(self):
-        return self
-
-    def next(self):
-        result = next(self.reader)
-        if sys.version_info[0] < 3:
-            for i, item in enumerate(result):
-                if not isinstance(item, text_type):
-                    result[i] = item.decode('utf-8')
-        return result
-
-    __next__ = next
-
-class CSVWriter(CSVBase):
-    def __init__(self, fn, **kwargs):
-        self.stream = _csv_open(fn, 'w')
-        self.writer = csv.writer(self.stream, **self.defaults)
-
-    def writerow(self, row):
-        if sys.version_info[0] < 3:
-            r = []
-            for item in row:
-                if isinstance(item, text_type):
-                    item = item.encode('utf-8')
-                r.append(item)
-            row = r
-        self.writer.writerow(row)
-
-#
-#   Configurator functionality
-#
-
-class Configurator(BaseConfigurator):
-
-    value_converters = dict(BaseConfigurator.value_converters)
-    value_converters['inc'] = 'inc_convert'
-
-    def __init__(self, config, base=None):
-        super(Configurator, self).__init__(config)
-        self.base = base or os.getcwd()
-
-    def configure_custom(self, config):
-        def convert(o):
-            if isinstance(o, (list, tuple)):
-                result = type(o)([convert(i) for i in o])
-            elif isinstance(o, dict):
-                if '()' in o:
-                    result = self.configure_custom(o)
-                else:
-                    result = {}
-                    for k in o:
-                        result[k] = convert(o[k])
-            else:
-                result = self.convert(o)
-            return result
-
-        c = config.pop('()')
-        if not callable(c):
-            c = self.resolve(c)
-        props = config.pop('.', None)
-        # Check for valid identifiers
-        args = config.pop('[]', ())
-        if args:
-            args = tuple([convert(o) for o in args])
-        items = [(k, convert(config[k])) for k in config if valid_ident(k)]
-        kwargs = dict(items)
-        result = c(*args, **kwargs)
-        if props:
-            for n, v in props.items():
-                setattr(result, n, convert(v))
-        return result
-
-    def __getitem__(self, key):
-        result = self.config[key]
-        if isinstance(result, dict) and '()' in result:
-            self.config[key] = result = self.configure_custom(result)
-        return result
-
-    def inc_convert(self, value):
-        """Default converter for the inc:// protocol."""
-        if not os.path.isabs(value):
-            value = os.path.join(self.base, value)
-        with codecs.open(value, 'r', encoding='utf-8') as f:
-            result = json.load(f)
-        return result
-
-
-class SubprocessMixin(object):
-    """
-    Mixin for running subprocesses and capturing their output
-    """
-    def __init__(self, verbose=False, progress=None):
-        self.verbose = verbose
-        self.progress = progress
-
-    def reader(self, stream, context):
-        """
-        Read lines from a subprocess' output stream and either pass to a progress
-        callable (if specified) or write progress information to sys.stderr.
-        """
-        progress = self.progress
-        verbose = self.verbose
-        while True:
-            s = stream.readline()
-            if not s:
-                break
-            if progress is not None:
-                progress(s, context)
-            else:
-                if not verbose:
-                    sys.stderr.write('.')
-                else:
-                    sys.stderr.write(s.decode('utf-8'))
-                sys.stderr.flush()
-        stream.close()
-
-    def run_command(self, cmd, **kwargs):
-        p = subprocess.Popen(cmd, stdout=subprocess.PIPE,
-                             stderr=subprocess.PIPE, **kwargs)
-        t1 = threading.Thread(target=self.reader, args=(p.stdout, 'stdout'))
-        t1.start()
-        t2 = threading.Thread(target=self.reader, args=(p.stderr, 'stderr'))
-        t2.start()
-        p.wait()
-        t1.join()
-        t2.join()
-        if self.progress is not None:
-            self.progress('done.', 'main')
-        elif self.verbose:
-            sys.stderr.write('done.\n')
-        return p
-
-
-def normalize_name(name):
-    """Normalize a python package name a la PEP 503"""
-    # https://www.python.org/dev/peps/pep-0503/#normalized-names
-    return re.sub('[-_.]+', '-', name).lower()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/version.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/version.py
deleted file mode 100644
index 3eebe18..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/version.py
+++ /dev/null
@@ -1,736 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2012-2017 The Python Software Foundation.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-"""
-Implementation of a flexible versioning scheme providing support for PEP-440,
-setuptools-compatible and semantic versioning.
-"""
-
-import logging
-import re
-
-from .compat import string_types
-from .util import parse_requirement
-
-__all__ = ['NormalizedVersion', 'NormalizedMatcher',
-           'LegacyVersion', 'LegacyMatcher',
-           'SemanticVersion', 'SemanticMatcher',
-           'UnsupportedVersionError', 'get_scheme']
-
-logger = logging.getLogger(__name__)
-
-
-class UnsupportedVersionError(ValueError):
-    """This is an unsupported version."""
-    pass
-
-
-class Version(object):
-    def __init__(self, s):
-        self._string = s = s.strip()
-        self._parts = parts = self.parse(s)
-        assert isinstance(parts, tuple)
-        assert len(parts) > 0
-
-    def parse(self, s):
-        raise NotImplementedError('please implement in a subclass')
-
-    def _check_compatible(self, other):
-        if type(self) != type(other):
-            raise TypeError('cannot compare %r and %r' % (self, other))
-
-    def __eq__(self, other):
-        self._check_compatible(other)
-        return self._parts == other._parts
-
-    def __ne__(self, other):
-        return not self.__eq__(other)
-
-    def __lt__(self, other):
-        self._check_compatible(other)
-        return self._parts < other._parts
-
-    def __gt__(self, other):
-        return not (self.__lt__(other) or self.__eq__(other))
-
-    def __le__(self, other):
-        return self.__lt__(other) or self.__eq__(other)
-
-    def __ge__(self, other):
-        return self.__gt__(other) or self.__eq__(other)
-
-    # See http://docs.python.org/reference/datamodel#object.__hash__
-    def __hash__(self):
-        return hash(self._parts)
-
-    def __repr__(self):
-        return "%s('%s')" % (self.__class__.__name__, self._string)
-
-    def __str__(self):
-        return self._string
-
-    @property
-    def is_prerelease(self):
-        raise NotImplementedError('Please implement in subclasses.')
-
-
-class Matcher(object):
-    version_class = None
-
-    # value is either a callable or the name of a method
-    _operators = {
-        '<': lambda v, c, p: v < c,
-        '>': lambda v, c, p: v > c,
-        '<=': lambda v, c, p: v == c or v < c,
-        '>=': lambda v, c, p: v == c or v > c,
-        '==': lambda v, c, p: v == c,
-        '===': lambda v, c, p: v == c,
-        # by default, compatible => >=.
-        '~=': lambda v, c, p: v == c or v > c,
-        '!=': lambda v, c, p: v != c,
-    }
-
-    # this is a method only to support alternative implementations
-    # via overriding
-    def parse_requirement(self, s):
-        return parse_requirement(s)
-
-    def __init__(self, s):
-        if self.version_class is None:
-            raise ValueError('Please specify a version class')
-        self._string = s = s.strip()
-        r = self.parse_requirement(s)
-        if not r:
-            raise ValueError('Not valid: %r' % s)
-        self.name = r.name
-        self.key = self.name.lower()    # for case-insensitive comparisons
-        clist = []
-        if r.constraints:
-            # import pdb; pdb.set_trace()
-            for op, s in r.constraints:
-                if s.endswith('.*'):
-                    if op not in ('==', '!='):
-                        raise ValueError('\'.*\' not allowed for '
-                                         '%r constraints' % op)
-                    # Could be a partial version (e.g. for '2.*') which
-                    # won't parse as a version, so keep it as a string
-                    vn, prefix = s[:-2], True
-                    # Just to check that vn is a valid version
-                    self.version_class(vn)
-                else:
-                    # Should parse as a version, so we can create an
-                    # instance for the comparison
-                    vn, prefix = self.version_class(s), False
-                clist.append((op, vn, prefix))
-        self._parts = tuple(clist)
-
-    def match(self, version):
-        """
-        Check if the provided version matches the constraints.
-
-        :param version: The version to match against this instance.
-        :type version: String or :class:`Version` instance.
-        """
-        if isinstance(version, string_types):
-            version = self.version_class(version)
-        for operator, constraint, prefix in self._parts:
-            f = self._operators.get(operator)
-            if isinstance(f, string_types):
-                f = getattr(self, f)
-            if not f:
-                msg = ('%r not implemented '
-                       'for %s' % (operator, self.__class__.__name__))
-                raise NotImplementedError(msg)
-            if not f(version, constraint, prefix):
-                return False
-        return True
-
-    @property
-    def exact_version(self):
-        result = None
-        if len(self._parts) == 1 and self._parts[0][0] in ('==', '==='):
-            result = self._parts[0][1]
-        return result
-
-    def _check_compatible(self, other):
-        if type(self) != type(other) or self.name != other.name:
-            raise TypeError('cannot compare %s and %s' % (self, other))
-
-    def __eq__(self, other):
-        self._check_compatible(other)
-        return self.key == other.key and self._parts == other._parts
-
-    def __ne__(self, other):
-        return not self.__eq__(other)
-
-    # See http://docs.python.org/reference/datamodel#object.__hash__
-    def __hash__(self):
-        return hash(self.key) + hash(self._parts)
-
-    def __repr__(self):
-        return "%s(%r)" % (self.__class__.__name__, self._string)
-
-    def __str__(self):
-        return self._string
-
-
-PEP440_VERSION_RE = re.compile(r'^v?(\d+!)?(\d+(\.\d+)*)((a|b|c|rc)(\d+))?'
-                               r'(\.(post)(\d+))?(\.(dev)(\d+))?'
-                               r'(\+([a-zA-Z\d]+(\.[a-zA-Z\d]+)?))?$')
-
-
-def _pep_440_key(s):
-    s = s.strip()
-    m = PEP440_VERSION_RE.match(s)
-    if not m:
-        raise UnsupportedVersionError('Not a valid version: %s' % s)
-    groups = m.groups()
-    nums = tuple(int(v) for v in groups[1].split('.'))
-    while len(nums) > 1 and nums[-1] == 0:
-        nums = nums[:-1]
-
-    if not groups[0]:
-        epoch = 0
-    else:
-        epoch = int(groups[0])
-    pre = groups[4:6]
-    post = groups[7:9]
-    dev = groups[10:12]
-    local = groups[13]
-    if pre == (None, None):
-        pre = ()
-    else:
-        pre = pre[0], int(pre[1])
-    if post == (None, None):
-        post = ()
-    else:
-        post = post[0], int(post[1])
-    if dev == (None, None):
-        dev = ()
-    else:
-        dev = dev[0], int(dev[1])
-    if local is None:
-        local = ()
-    else:
-        parts = []
-        for part in local.split('.'):
-            # to ensure that numeric compares as > lexicographic, avoid
-            # comparing them directly, but encode a tuple which ensures
-            # correct sorting
-            if part.isdigit():
-                part = (1, int(part))
-            else:
-                part = (0, part)
-            parts.append(part)
-        local = tuple(parts)
-    if not pre:
-        # either before pre-release, or final release and after
-        if not post and dev:
-            # before pre-release
-            pre = ('a', -1)     # to sort before a0
-        else:
-            pre = ('z',)        # to sort after all pre-releases
-    # now look at the state of post and dev.
-    if not post:
-        post = ('_',)   # sort before 'a'
-    if not dev:
-        dev = ('final',)
-
-    #print('%s -> %s' % (s, m.groups()))
-    return epoch, nums, pre, post, dev, local
-
-
-_normalized_key = _pep_440_key
-
-
-class NormalizedVersion(Version):
-    """A rational version.
-
-    Good:
-        1.2         # equivalent to "1.2.0"
-        1.2.0
-        1.2a1
-        1.2.3a2
-        1.2.3b1
-        1.2.3c1
-        1.2.3.4
-        TODO: fill this out
-
-    Bad:
-        1           # minimum two numbers
-        1.2a        # release level must have a release serial
-        1.2.3b
-    """
-    def parse(self, s):
-        result = _normalized_key(s)
-        # _normalized_key loses trailing zeroes in the release
-        # clause, since that's needed to ensure that X.Y == X.Y.0 == X.Y.0.0
-        # However, PEP 440 prefix matching needs it: for example,
-        # (~= 1.4.5.0) matches differently to (~= 1.4.5.0.0).
-        m = PEP440_VERSION_RE.match(s)      # must succeed
-        groups = m.groups()
-        self._release_clause = tuple(int(v) for v in groups[1].split('.'))
-        return result
-
-    PREREL_TAGS = set(['a', 'b', 'c', 'rc', 'dev'])
-
-    @property
-    def is_prerelease(self):
-        return any(t[0] in self.PREREL_TAGS for t in self._parts if t)
-
-
-def _match_prefix(x, y):
-    x = str(x)
-    y = str(y)
-    if x == y:
-        return True
-    if not x.startswith(y):
-        return False
-    n = len(y)
-    return x[n] == '.'
-
-
-class NormalizedMatcher(Matcher):
-    version_class = NormalizedVersion
-
-    # value is either a callable or the name of a method
-    _operators = {
-        '~=': '_match_compatible',
-        '<': '_match_lt',
-        '>': '_match_gt',
-        '<=': '_match_le',
-        '>=': '_match_ge',
-        '==': '_match_eq',
-        '===': '_match_arbitrary',
-        '!=': '_match_ne',
-    }
-
-    def _adjust_local(self, version, constraint, prefix):
-        if prefix:
-            strip_local = '+' not in constraint and version._parts[-1]
-        else:
-            # both constraint and version are
-            # NormalizedVersion instances.
-            # If constraint does not have a local component,
-            # ensure the version doesn't, either.
-            strip_local = not constraint._parts[-1] and version._parts[-1]
-        if strip_local:
-            s = version._string.split('+', 1)[0]
-            version = self.version_class(s)
-        return version, constraint
-
-    def _match_lt(self, version, constraint, prefix):
-        version, constraint = self._adjust_local(version, constraint, prefix)
-        if version >= constraint:
-            return False
-        release_clause = constraint._release_clause
-        pfx = '.'.join([str(i) for i in release_clause])
-        return not _match_prefix(version, pfx)
-
-    def _match_gt(self, version, constraint, prefix):
-        version, constraint = self._adjust_local(version, constraint, prefix)
-        if version <= constraint:
-            return False
-        release_clause = constraint._release_clause
-        pfx = '.'.join([str(i) for i in release_clause])
-        return not _match_prefix(version, pfx)
-
-    def _match_le(self, version, constraint, prefix):
-        version, constraint = self._adjust_local(version, constraint, prefix)
-        return version <= constraint
-
-    def _match_ge(self, version, constraint, prefix):
-        version, constraint = self._adjust_local(version, constraint, prefix)
-        return version >= constraint
-
-    def _match_eq(self, version, constraint, prefix):
-        version, constraint = self._adjust_local(version, constraint, prefix)
-        if not prefix:
-            result = (version == constraint)
-        else:
-            result = _match_prefix(version, constraint)
-        return result
-
-    def _match_arbitrary(self, version, constraint, prefix):
-        return str(version) == str(constraint)
-
-    def _match_ne(self, version, constraint, prefix):
-        version, constraint = self._adjust_local(version, constraint, prefix)
-        if not prefix:
-            result = (version != constraint)
-        else:
-            result = not _match_prefix(version, constraint)
-        return result
-
-    def _match_compatible(self, version, constraint, prefix):
-        version, constraint = self._adjust_local(version, constraint, prefix)
-        if version == constraint:
-            return True
-        if version < constraint:
-            return False
-#        if not prefix:
-#            return True
-        release_clause = constraint._release_clause
-        if len(release_clause) > 1:
-            release_clause = release_clause[:-1]
-        pfx = '.'.join([str(i) for i in release_clause])
-        return _match_prefix(version, pfx)
-
-_REPLACEMENTS = (
-    (re.compile('[.+-]$'), ''),                     # remove trailing puncts
-    (re.compile(r'^[.](\d)'), r'0.\1'),             # .N -> 0.N at start
-    (re.compile('^[.-]'), ''),                      # remove leading puncts
-    (re.compile(r'^\((.*)\)$'), r'\1'),             # remove parentheses
-    (re.compile(r'^v(ersion)?\s*(\d+)'), r'\2'),    # remove leading v(ersion)
-    (re.compile(r'^r(ev)?\s*(\d+)'), r'\2'),        # remove leading v(ersion)
-    (re.compile('[.]{2,}'), '.'),                   # multiple runs of '.'
-    (re.compile(r'\b(alfa|apha)\b'), 'alpha'),      # misspelt alpha
-    (re.compile(r'\b(pre-alpha|prealpha)\b'),
-                'pre.alpha'),                       # standardise
-    (re.compile(r'\(beta\)$'), 'beta'),             # remove parentheses
-)
-
-_SUFFIX_REPLACEMENTS = (
-    (re.compile('^[:~._+-]+'), ''),                   # remove leading puncts
-    (re.compile('[,*")([\\]]'), ''),                  # remove unwanted chars
-    (re.compile('[~:+_ -]'), '.'),                    # replace illegal chars
-    (re.compile('[.]{2,}'), '.'),                   # multiple runs of '.'
-    (re.compile(r'\.$'), ''),                       # trailing '.'
-)
-
-_NUMERIC_PREFIX = re.compile(r'(\d+(\.\d+)*)')
-
-
-def _suggest_semantic_version(s):
-    """
-    Try to suggest a semantic form for a version for which
-    _suggest_normalized_version couldn't come up with anything.
-    """
-    result = s.strip().lower()
-    for pat, repl in _REPLACEMENTS:
-        result = pat.sub(repl, result)
-    if not result:
-        result = '0.0.0'
-
-    # Now look for numeric prefix, and separate it out from
-    # the rest.
-    #import pdb; pdb.set_trace()
-    m = _NUMERIC_PREFIX.match(result)
-    if not m:
-        prefix = '0.0.0'
-        suffix = result
-    else:
-        prefix = m.groups()[0].split('.')
-        prefix = [int(i) for i in prefix]
-        while len(prefix) < 3:
-            prefix.append(0)
-        if len(prefix) == 3:
-            suffix = result[m.end():]
-        else:
-            suffix = '.'.join([str(i) for i in prefix[3:]]) + result[m.end():]
-            prefix = prefix[:3]
-        prefix = '.'.join([str(i) for i in prefix])
-        suffix = suffix.strip()
-    if suffix:
-        #import pdb; pdb.set_trace()
-        # massage the suffix.
-        for pat, repl in _SUFFIX_REPLACEMENTS:
-            suffix = pat.sub(repl, suffix)
-
-    if not suffix:
-        result = prefix
-    else:
-        sep = '-' if 'dev' in suffix else '+'
-        result = prefix + sep + suffix
-    if not is_semver(result):
-        result = None
-    return result
-
-
-def _suggest_normalized_version(s):
-    """Suggest a normalized version close to the given version string.
-
-    If you have a version string that isn't rational (i.e. NormalizedVersion
-    doesn't like it) then you might be able to get an equivalent (or close)
-    rational version from this function.
-
-    This does a number of simple normalizations to the given string, based
-    on observation of versions currently in use on PyPI. Given a dump of
-    those version during PyCon 2009, 4287 of them:
-    - 2312 (53.93%) match NormalizedVersion without change
-      with the automatic suggestion
-    - 3474 (81.04%) match when using this suggestion method
-
-    @param s {str} An irrational version string.
-    @returns A rational version string, or None, if couldn't determine one.
-    """
-    try:
-        _normalized_key(s)
-        return s   # already rational
-    except UnsupportedVersionError:
-        pass
-
-    rs = s.lower()
-
-    # part of this could use maketrans
-    for orig, repl in (('-alpha', 'a'), ('-beta', 'b'), ('alpha', 'a'),
-                       ('beta', 'b'), ('rc', 'c'), ('-final', ''),
-                       ('-pre', 'c'),
-                       ('-release', ''), ('.release', ''), ('-stable', ''),
-                       ('+', '.'), ('_', '.'), (' ', ''), ('.final', ''),
-                       ('final', '')):
-        rs = rs.replace(orig, repl)
-
-    # if something ends with dev or pre, we add a 0
-    rs = re.sub(r"pre$", r"pre0", rs)
-    rs = re.sub(r"dev$", r"dev0", rs)
-
-    # if we have something like "b-2" or "a.2" at the end of the
-    # version, that is probably beta, alpha, etc
-    # let's remove the dash or dot
-    rs = re.sub(r"([abc]|rc)[\-\.](\d+)$", r"\1\2", rs)
-
-    # 1.0-dev-r371 -> 1.0.dev371
-    # 0.1-dev-r79 -> 0.1.dev79
-    rs = re.sub(r"[\-\.](dev)[\-\.]?r?(\d+)$", r".\1\2", rs)
-
-    # Clean: 2.0.a.3, 2.0.b1, 0.9.0~c1
-    rs = re.sub(r"[.~]?([abc])\.?", r"\1", rs)
-
-    # Clean: v0.3, v1.0
-    if rs.startswith('v'):
-        rs = rs[1:]
-
-    # Clean leading '0's on numbers.
-    #TODO: unintended side-effect on, e.g., "2003.05.09"
-    # PyPI stats: 77 (~2%) better
-    rs = re.sub(r"\b0+(\d+)(?!\d)", r"\1", rs)
-
-    # Clean a/b/c with no version. E.g. "1.0a" -> "1.0a0". Setuptools infers
-    # zero.
-    # PyPI stats: 245 (7.56%) better
-    rs = re.sub(r"(\d+[abc])$", r"\g<1>0", rs)
-
-    # the 'dev-rNNN' tag is a dev tag
-    rs = re.sub(r"\.?(dev-r|dev\.r)\.?(\d+)$", r".dev\2", rs)
-
-    # clean the - when used as a pre delimiter
-    rs = re.sub(r"-(a|b|c)(\d+)$", r"\1\2", rs)
-
-    # a terminal "dev" or "devel" can be changed into ".dev0"
-    rs = re.sub(r"[\.\-](dev|devel)$", r".dev0", rs)
-
-    # a terminal "dev" can be changed into ".dev0"
-    rs = re.sub(r"(?![\.\-])dev$", r".dev0", rs)
-
-    # a terminal "final" or "stable" can be removed
-    rs = re.sub(r"(final|stable)$", "", rs)
-
-    # The 'r' and the '-' tags are post release tags
-    #   0.4a1.r10       ->  0.4a1.post10
-    #   0.9.33-17222    ->  0.9.33.post17222
-    #   0.9.33-r17222   ->  0.9.33.post17222
-    rs = re.sub(r"\.?(r|-|-r)\.?(\d+)$", r".post\2", rs)
-
-    # Clean 'r' instead of 'dev' usage:
-    #   0.9.33+r17222   ->  0.9.33.dev17222
-    #   1.0dev123       ->  1.0.dev123
-    #   1.0.git123      ->  1.0.dev123
-    #   1.0.bzr123      ->  1.0.dev123
-    #   0.1a0dev.123    ->  0.1a0.dev123
-    # PyPI stats:  ~150 (~4%) better
-    rs = re.sub(r"\.?(dev|git|bzr)\.?(\d+)$", r".dev\2", rs)
-
-    # Clean '.pre' (normalized from '-pre' above) instead of 'c' usage:
-    #   0.2.pre1        ->  0.2c1
-    #   0.2-c1         ->  0.2c1
-    #   1.0preview123   ->  1.0c123
-    # PyPI stats: ~21 (0.62%) better
-    rs = re.sub(r"\.?(pre|preview|-c)(\d+)$", r"c\g<2>", rs)
-
-    # Tcl/Tk uses "px" for their post release markers
-    rs = re.sub(r"p(\d+)$", r".post\1", rs)
-
-    try:
-        _normalized_key(rs)
-    except UnsupportedVersionError:
-        rs = None
-    return rs
-
-#
-#   Legacy version processing (distribute-compatible)
-#
-
-_VERSION_PART = re.compile(r'([a-z]+|\d+|[\.-])', re.I)
-_VERSION_REPLACE = {
-    'pre': 'c',
-    'preview': 'c',
-    '-': 'final-',
-    'rc': 'c',
-    'dev': '@',
-    '': None,
-    '.': None,
-}
-
-
-def _legacy_key(s):
-    def get_parts(s):
-        result = []
-        for p in _VERSION_PART.split(s.lower()):
-            p = _VERSION_REPLACE.get(p, p)
-            if p:
-                if '0' <= p[:1] <= '9':
-                    p = p.zfill(8)
-                else:
-                    p = '*' + p
-                result.append(p)
-        result.append('*final')
-        return result
-
-    result = []
-    for p in get_parts(s):
-        if p.startswith('*'):
-            if p < '*final':
-                while result and result[-1] == '*final-':
-                    result.pop()
-            while result and result[-1] == '00000000':
-                result.pop()
-        result.append(p)
-    return tuple(result)
-
-
-class LegacyVersion(Version):
-    def parse(self, s):
-        return _legacy_key(s)
-
-    @property
-    def is_prerelease(self):
-        result = False
-        for x in self._parts:
-            if (isinstance(x, string_types) and x.startswith('*') and
-                x < '*final'):
-                result = True
-                break
-        return result
-
-
-class LegacyMatcher(Matcher):
-    version_class = LegacyVersion
-
-    _operators = dict(Matcher._operators)
-    _operators['~='] = '_match_compatible'
-
-    numeric_re = re.compile(r'^(\d+(\.\d+)*)')
-
-    def _match_compatible(self, version, constraint, prefix):
-        if version < constraint:
-            return False
-        m = self.numeric_re.match(str(constraint))
-        if not m:
-            logger.warning('Cannot compute compatible match for version %s '
-                           ' and constraint %s', version, constraint)
-            return True
-        s = m.groups()[0]
-        if '.' in s:
-            s = s.rsplit('.', 1)[0]
-        return _match_prefix(version, s)
-
-#
-#   Semantic versioning
-#
-
-_SEMVER_RE = re.compile(r'^(\d+)\.(\d+)\.(\d+)'
-                        r'(-[a-z0-9]+(\.[a-z0-9-]+)*)?'
-                        r'(\+[a-z0-9]+(\.[a-z0-9-]+)*)?$', re.I)
-
-
-def is_semver(s):
-    return _SEMVER_RE.match(s)
-
-
-def _semantic_key(s):
-    def make_tuple(s, absent):
-        if s is None:
-            result = (absent,)
-        else:
-            parts = s[1:].split('.')
-            # We can't compare ints and strings on Python 3, so fudge it
-            # by zero-filling numeric values so simulate a numeric comparison
-            result = tuple([p.zfill(8) if p.isdigit() else p for p in parts])
-        return result
-
-    m = is_semver(s)
-    if not m:
-        raise UnsupportedVersionError(s)
-    groups = m.groups()
-    major, minor, patch = [int(i) for i in groups[:3]]
-    # choose the '|' and '*' so that versions sort correctly
-    pre, build = make_tuple(groups[3], '|'), make_tuple(groups[5], '*')
-    return (major, minor, patch), pre, build
-
-
-class SemanticVersion(Version):
-    def parse(self, s):
-        return _semantic_key(s)
-
-    @property
-    def is_prerelease(self):
-        return self._parts[1][0] != '|'
-
-
-class SemanticMatcher(Matcher):
-    version_class = SemanticVersion
-
-
-class VersionScheme(object):
-    def __init__(self, key, matcher, suggester=None):
-        self.key = key
-        self.matcher = matcher
-        self.suggester = suggester
-
-    def is_valid_version(self, s):
-        try:
-            self.matcher.version_class(s)
-            result = True
-        except UnsupportedVersionError:
-            result = False
-        return result
-
-    def is_valid_matcher(self, s):
-        try:
-            self.matcher(s)
-            result = True
-        except UnsupportedVersionError:
-            result = False
-        return result
-
-    def is_valid_constraint_list(self, s):
-        """
-        Used for processing some metadata fields
-        """
-        return self.is_valid_matcher('dummy_name (%s)' % s)
-
-    def suggest(self, s):
-        if self.suggester is None:
-            result = None
-        else:
-            result = self.suggester(s)
-        return result
-
-_SCHEMES = {
-    'normalized': VersionScheme(_normalized_key, NormalizedMatcher,
-                                _suggest_normalized_version),
-    'legacy': VersionScheme(_legacy_key, LegacyMatcher, lambda self, s: s),
-    'semantic': VersionScheme(_semantic_key, SemanticMatcher,
-                              _suggest_semantic_version),
-}
-
-_SCHEMES['default'] = _SCHEMES['normalized']
-
-
-def get_scheme(name):
-    if name not in _SCHEMES:
-        raise ValueError('unknown scheme name: %r' % name)
-    return _SCHEMES[name]
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/w32.exe b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/w32.exe
deleted file mode 100644
index 732215a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/w32.exe
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/w64.exe b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/w64.exe
deleted file mode 100644
index c41bd0a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/w64.exe
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/wheel.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/wheel.py
deleted file mode 100644
index b04bfae..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distlib/wheel.py
+++ /dev/null
@@ -1,988 +0,0 @@
-# -*- coding: utf-8 -*-
-#
-# Copyright (C) 2013-2017 Vinay Sajip.
-# Licensed to the Python Software Foundation under a contributor agreement.
-# See LICENSE.txt and CONTRIBUTORS.txt.
-#
-from __future__ import unicode_literals
-
-import base64
-import codecs
-import datetime
-import distutils.util
-from email import message_from_file
-import hashlib
-import imp
-import json
-import logging
-import os
-import posixpath
-import re
-import shutil
-import sys
-import tempfile
-import zipfile
-
-from . import __version__, DistlibException
-from .compat import sysconfig, ZipFile, fsdecode, text_type, filter
-from .database import InstalledDistribution
-from .metadata import Metadata, METADATA_FILENAME, WHEEL_METADATA_FILENAME
-from .util import (FileOperator, convert_path, CSVReader, CSVWriter, Cache,
-                   cached_property, get_cache_base, read_exports, tempdir)
-from .version import NormalizedVersion, UnsupportedVersionError
-
-logger = logging.getLogger(__name__)
-
-cache = None    # created when needed
-
-if hasattr(sys, 'pypy_version_info'):  # pragma: no cover
-    IMP_PREFIX = 'pp'
-elif sys.platform.startswith('java'):  # pragma: no cover
-    IMP_PREFIX = 'jy'
-elif sys.platform == 'cli':  # pragma: no cover
-    IMP_PREFIX = 'ip'
-else:
-    IMP_PREFIX = 'cp'
-
-VER_SUFFIX = sysconfig.get_config_var('py_version_nodot')
-if not VER_SUFFIX:   # pragma: no cover
-    VER_SUFFIX = '%s%s' % sys.version_info[:2]
-PYVER = 'py' + VER_SUFFIX
-IMPVER = IMP_PREFIX + VER_SUFFIX
-
-ARCH = distutils.util.get_platform().replace('-', '_').replace('.', '_')
-
-ABI = sysconfig.get_config_var('SOABI')
-if ABI and ABI.startswith('cpython-'):
-    ABI = ABI.replace('cpython-', 'cp')
-else:
-    def _derive_abi():
-        parts = ['cp', VER_SUFFIX]
-        if sysconfig.get_config_var('Py_DEBUG'):
-            parts.append('d')
-        if sysconfig.get_config_var('WITH_PYMALLOC'):
-            parts.append('m')
-        if sysconfig.get_config_var('Py_UNICODE_SIZE') == 4:
-            parts.append('u')
-        return ''.join(parts)
-    ABI = _derive_abi()
-    del _derive_abi
-
-FILENAME_RE = re.compile(r'''
-(?P<nm>[^-]+)
--(?P<vn>\d+[^-]*)
-(-(?P<bn>\d+[^-]*))?
--(?P<py>\w+\d+(\.\w+\d+)*)
--(?P<bi>\w+)
--(?P<ar>\w+(\.\w+)*)
-\.whl$
-''', re.IGNORECASE | re.VERBOSE)
-
-NAME_VERSION_RE = re.compile(r'''
-(?P<nm>[^-]+)
--(?P<vn>\d+[^-]*)
-(-(?P<bn>\d+[^-]*))?$
-''', re.IGNORECASE | re.VERBOSE)
-
-SHEBANG_RE = re.compile(br'\s*#![^\r\n]*')
-SHEBANG_DETAIL_RE = re.compile(br'^(\s*#!("[^"]+"|\S+))\s+(.*)$')
-SHEBANG_PYTHON = b'#!python'
-SHEBANG_PYTHONW = b'#!pythonw'
-
-if os.sep == '/':
-    to_posix = lambda o: o
-else:
-    to_posix = lambda o: o.replace(os.sep, '/')
-
-
-class Mounter(object):
-    def __init__(self):
-        self.impure_wheels = {}
-        self.libs = {}
-
-    def add(self, pathname, extensions):
-        self.impure_wheels[pathname] = extensions
-        self.libs.update(extensions)
-
-    def remove(self, pathname):
-        extensions = self.impure_wheels.pop(pathname)
-        for k, v in extensions:
-            if k in self.libs:
-                del self.libs[k]
-
-    def find_module(self, fullname, path=None):
-        if fullname in self.libs:
-            result = self
-        else:
-            result = None
-        return result
-
-    def load_module(self, fullname):
-        if fullname in sys.modules:
-            result = sys.modules[fullname]
-        else:
-            if fullname not in self.libs:
-                raise ImportError('unable to find extension for %s' % fullname)
-            result = imp.load_dynamic(fullname, self.libs[fullname])
-            result.__loader__ = self
-            parts = fullname.rsplit('.', 1)
-            if len(parts) > 1:
-                result.__package__ = parts[0]
-        return result
-
-_hook = Mounter()
-
-
-class Wheel(object):
-    """
-    Class to build and install from Wheel files (PEP 427).
-    """
-
-    wheel_version = (1, 1)
-    hash_kind = 'sha256'
-
-    def __init__(self, filename=None, sign=False, verify=False):
-        """
-        Initialise an instance using a (valid) filename.
-        """
-        self.sign = sign
-        self.should_verify = verify
-        self.buildver = ''
-        self.pyver = [PYVER]
-        self.abi = ['none']
-        self.arch = ['any']
-        self.dirname = os.getcwd()
-        if filename is None:
-            self.name = 'dummy'
-            self.version = '0.1'
-            self._filename = self.filename
-        else:
-            m = NAME_VERSION_RE.match(filename)
-            if m:
-                info = m.groupdict('')
-                self.name = info['nm']
-                # Reinstate the local version separator
-                self.version = info['vn'].replace('_', '-')
-                self.buildver = info['bn']
-                self._filename = self.filename
-            else:
-                dirname, filename = os.path.split(filename)
-                m = FILENAME_RE.match(filename)
-                if not m:
-                    raise DistlibException('Invalid name or '
-                                           'filename: %r' % filename)
-                if dirname:
-                    self.dirname = os.path.abspath(dirname)
-                self._filename = filename
-                info = m.groupdict('')
-                self.name = info['nm']
-                self.version = info['vn']
-                self.buildver = info['bn']
-                self.pyver = info['py'].split('.')
-                self.abi = info['bi'].split('.')
-                self.arch = info['ar'].split('.')
-
-    @property
-    def filename(self):
-        """
-        Build and return a filename from the various components.
-        """
-        if self.buildver:
-            buildver = '-' + self.buildver
-        else:
-            buildver = ''
-        pyver = '.'.join(self.pyver)
-        abi = '.'.join(self.abi)
-        arch = '.'.join(self.arch)
-        # replace - with _ as a local version separator
-        version = self.version.replace('-', '_')
-        return '%s-%s%s-%s-%s-%s.whl' % (self.name, version, buildver,
-                                         pyver, abi, arch)
-
-    @property
-    def exists(self):
-        path = os.path.join(self.dirname, self.filename)
-        return os.path.isfile(path)
-
-    @property
-    def tags(self):
-        for pyver in self.pyver:
-            for abi in self.abi:
-                for arch in self.arch:
-                    yield pyver, abi, arch
-
-    @cached_property
-    def metadata(self):
-        pathname = os.path.join(self.dirname, self.filename)
-        name_ver = '%s-%s' % (self.name, self.version)
-        info_dir = '%s.dist-info' % name_ver
-        wrapper = codecs.getreader('utf-8')
-        with ZipFile(pathname, 'r') as zf:
-            wheel_metadata = self.get_wheel_metadata(zf)
-            wv = wheel_metadata['Wheel-Version'].split('.', 1)
-            file_version = tuple([int(i) for i in wv])
-            if file_version < (1, 1):
-                fns = [WHEEL_METADATA_FILENAME, METADATA_FILENAME, 'METADATA']
-            else:
-                fns = [WHEEL_METADATA_FILENAME, METADATA_FILENAME]
-            result = None
-            for fn in fns:
-                try:
-                    metadata_filename = posixpath.join(info_dir, fn)
-                    with zf.open(metadata_filename) as bf:
-                        wf = wrapper(bf)
-                        result = Metadata(fileobj=wf)
-                        if result:
-                            break
-                except KeyError:
-                    pass
-            if not result:
-                raise ValueError('Invalid wheel, because metadata is '
-                                 'missing: looked in %s' % ', '.join(fns))
-        return result
-
-    def get_wheel_metadata(self, zf):
-        name_ver = '%s-%s' % (self.name, self.version)
-        info_dir = '%s.dist-info' % name_ver
-        metadata_filename = posixpath.join(info_dir, 'WHEEL')
-        with zf.open(metadata_filename) as bf:
-            wf = codecs.getreader('utf-8')(bf)
-            message = message_from_file(wf)
-        return dict(message)
-
-    @cached_property
-    def info(self):
-        pathname = os.path.join(self.dirname, self.filename)
-        with ZipFile(pathname, 'r') as zf:
-            result = self.get_wheel_metadata(zf)
-        return result
-
-    def process_shebang(self, data):
-        m = SHEBANG_RE.match(data)
-        if m:
-            end = m.end()
-            shebang, data_after_shebang = data[:end], data[end:]
-            # Preserve any arguments after the interpreter
-            if b'pythonw' in shebang.lower():
-                shebang_python = SHEBANG_PYTHONW
-            else:
-                shebang_python = SHEBANG_PYTHON
-            m = SHEBANG_DETAIL_RE.match(shebang)
-            if m:
-                args = b' ' + m.groups()[-1]
-            else:
-                args = b''
-            shebang = shebang_python + args
-            data = shebang + data_after_shebang
-        else:
-            cr = data.find(b'\r')
-            lf = data.find(b'\n')
-            if cr < 0 or cr > lf:
-                term = b'\n'
-            else:
-                if data[cr:cr + 2] == b'\r\n':
-                    term = b'\r\n'
-                else:
-                    term = b'\r'
-            data = SHEBANG_PYTHON + term + data
-        return data
-
-    def get_hash(self, data, hash_kind=None):
-        if hash_kind is None:
-            hash_kind = self.hash_kind
-        try:
-            hasher = getattr(hashlib, hash_kind)
-        except AttributeError:
-            raise DistlibException('Unsupported hash algorithm: %r' % hash_kind)
-        result = hasher(data).digest()
-        result = base64.urlsafe_b64encode(result).rstrip(b'=').decode('ascii')
-        return hash_kind, result
-
-    def write_record(self, records, record_path, base):
-        records = list(records) # make a copy for sorting
-        p = to_posix(os.path.relpath(record_path, base))
-        records.append((p, '', ''))
-        records.sort()
-        with CSVWriter(record_path) as writer:
-            for row in records:
-                writer.writerow(row)
-
-    def write_records(self, info, libdir, archive_paths):
-        records = []
-        distinfo, info_dir = info
-        hasher = getattr(hashlib, self.hash_kind)
-        for ap, p in archive_paths:
-            with open(p, 'rb') as f:
-                data = f.read()
-            digest = '%s=%s' % self.get_hash(data)
-            size = os.path.getsize(p)
-            records.append((ap, digest, size))
-
-        p = os.path.join(distinfo, 'RECORD')
-        self.write_record(records, p, libdir)
-        ap = to_posix(os.path.join(info_dir, 'RECORD'))
-        archive_paths.append((ap, p))
-
-    def build_zip(self, pathname, archive_paths):
-        with ZipFile(pathname, 'w', zipfile.ZIP_DEFLATED) as zf:
-            for ap, p in archive_paths:
-                logger.debug('Wrote %s to %s in wheel', p, ap)
-                zf.write(p, ap)
-
-    def build(self, paths, tags=None, wheel_version=None):
-        """
-        Build a wheel from files in specified paths, and use any specified tags
-        when determining the name of the wheel.
-        """
-        if tags is None:
-            tags = {}
-
-        libkey = list(filter(lambda o: o in paths, ('purelib', 'platlib')))[0]
-        if libkey == 'platlib':
-            is_pure = 'false'
-            default_pyver = [IMPVER]
-            default_abi = [ABI]
-            default_arch = [ARCH]
-        else:
-            is_pure = 'true'
-            default_pyver = [PYVER]
-            default_abi = ['none']
-            default_arch = ['any']
-
-        self.pyver = tags.get('pyver', default_pyver)
-        self.abi = tags.get('abi', default_abi)
-        self.arch = tags.get('arch', default_arch)
-
-        libdir = paths[libkey]
-
-        name_ver = '%s-%s' % (self.name, self.version)
-        data_dir = '%s.data' % name_ver
-        info_dir = '%s.dist-info' % name_ver
-
-        archive_paths = []
-
-        # First, stuff which is not in site-packages
-        for key in ('data', 'headers', 'scripts'):
-            if key not in paths:
-                continue
-            path = paths[key]
-            if os.path.isdir(path):
-                for root, dirs, files in os.walk(path):
-                    for fn in files:
-                        p = fsdecode(os.path.join(root, fn))
-                        rp = os.path.relpath(p, path)
-                        ap = to_posix(os.path.join(data_dir, key, rp))
-                        archive_paths.append((ap, p))
-                        if key == 'scripts' and not p.endswith('.exe'):
-                            with open(p, 'rb') as f:
-                                data = f.read()
-                            data = self.process_shebang(data)
-                            with open(p, 'wb') as f:
-                                f.write(data)
-
-        # Now, stuff which is in site-packages, other than the
-        # distinfo stuff.
-        path = libdir
-        distinfo = None
-        for root, dirs, files in os.walk(path):
-            if root == path:
-                # At the top level only, save distinfo for later
-                # and skip it for now
-                for i, dn in enumerate(dirs):
-                    dn = fsdecode(dn)
-                    if dn.endswith('.dist-info'):
-                        distinfo = os.path.join(root, dn)
-                        del dirs[i]
-                        break
-                assert distinfo, '.dist-info directory expected, not found'
-
-            for fn in files:
-                # comment out next suite to leave .pyc files in
-                if fsdecode(fn).endswith(('.pyc', '.pyo')):
-                    continue
-                p = os.path.join(root, fn)
-                rp = to_posix(os.path.relpath(p, path))
-                archive_paths.append((rp, p))
-
-        # Now distinfo. Assumed to be flat, i.e. os.listdir is enough.
-        files = os.listdir(distinfo)
-        for fn in files:
-            if fn not in ('RECORD', 'INSTALLER', 'SHARED', 'WHEEL'):
-                p = fsdecode(os.path.join(distinfo, fn))
-                ap = to_posix(os.path.join(info_dir, fn))
-                archive_paths.append((ap, p))
-
-        wheel_metadata = [
-            'Wheel-Version: %d.%d' % (wheel_version or self.wheel_version),
-            'Generator: distlib %s' % __version__,
-            'Root-Is-Purelib: %s' % is_pure,
-        ]
-        for pyver, abi, arch in self.tags:
-            wheel_metadata.append('Tag: %s-%s-%s' % (pyver, abi, arch))
-        p = os.path.join(distinfo, 'WHEEL')
-        with open(p, 'w') as f:
-            f.write('\n'.join(wheel_metadata))
-        ap = to_posix(os.path.join(info_dir, 'WHEEL'))
-        archive_paths.append((ap, p))
-
-        # Now, at last, RECORD.
-        # Paths in here are archive paths - nothing else makes sense.
-        self.write_records((distinfo, info_dir), libdir, archive_paths)
-        # Now, ready to build the zip file
-        pathname = os.path.join(self.dirname, self.filename)
-        self.build_zip(pathname, archive_paths)
-        return pathname
-
-    def install(self, paths, maker, **kwargs):
-        """
-        Install a wheel to the specified paths. If kwarg ``warner`` is
-        specified, it should be a callable, which will be called with two
-        tuples indicating the wheel version of this software and the wheel
-        version in the file, if there is a discrepancy in the versions.
-        This can be used to issue any warnings to raise any exceptions.
-        If kwarg ``lib_only`` is True, only the purelib/platlib files are
-        installed, and the headers, scripts, data and dist-info metadata are
-        not written. If kwarg ``bytecode_hashed_invalidation`` is True, written
-        bytecode will try to use file-hash based invalidation (PEP-552) on
-        supported interpreter versions (CPython 2.7+).
-
-        The return value is a :class:`InstalledDistribution` instance unless
-        ``options.lib_only`` is True, in which case the return value is ``None``.
-        """
-
-        dry_run = maker.dry_run
-        warner = kwargs.get('warner')
-        lib_only = kwargs.get('lib_only', False)
-        bc_hashed_invalidation = kwargs.get('bytecode_hashed_invalidation', False)
-
-        pathname = os.path.join(self.dirname, self.filename)
-        name_ver = '%s-%s' % (self.name, self.version)
-        data_dir = '%s.data' % name_ver
-        info_dir = '%s.dist-info' % name_ver
-
-        metadata_name = posixpath.join(info_dir, METADATA_FILENAME)
-        wheel_metadata_name = posixpath.join(info_dir, 'WHEEL')
-        record_name = posixpath.join(info_dir, 'RECORD')
-
-        wrapper = codecs.getreader('utf-8')
-
-        with ZipFile(pathname, 'r') as zf:
-            with zf.open(wheel_metadata_name) as bwf:
-                wf = wrapper(bwf)
-                message = message_from_file(wf)
-            wv = message['Wheel-Version'].split('.', 1)
-            file_version = tuple([int(i) for i in wv])
-            if (file_version != self.wheel_version) and warner:
-                warner(self.wheel_version, file_version)
-
-            if message['Root-Is-Purelib'] == 'true':
-                libdir = paths['purelib']
-            else:
-                libdir = paths['platlib']
-
-            records = {}
-            with zf.open(record_name) as bf:
-                with CSVReader(stream=bf) as reader:
-                    for row in reader:
-                        p = row[0]
-                        records[p] = row
-
-            data_pfx = posixpath.join(data_dir, '')
-            info_pfx = posixpath.join(info_dir, '')
-            script_pfx = posixpath.join(data_dir, 'scripts', '')
-
-            # make a new instance rather than a copy of maker's,
-            # as we mutate it
-            fileop = FileOperator(dry_run=dry_run)
-            fileop.record = True    # so we can rollback if needed
-
-            bc = not sys.dont_write_bytecode    # Double negatives. Lovely!
-
-            outfiles = []   # for RECORD writing
-
-            # for script copying/shebang processing
-            workdir = tempfile.mkdtemp()
-            # set target dir later
-            # we default add_launchers to False, as the
-            # Python Launcher should be used instead
-            maker.source_dir = workdir
-            maker.target_dir = None
-            try:
-                for zinfo in zf.infolist():
-                    arcname = zinfo.filename
-                    if isinstance(arcname, text_type):
-                        u_arcname = arcname
-                    else:
-                        u_arcname = arcname.decode('utf-8')
-                    # The signature file won't be in RECORD,
-                    # and we  don't currently don't do anything with it
-                    if u_arcname.endswith('/RECORD.jws'):
-                        continue
-                    row = records[u_arcname]
-                    if row[2] and str(zinfo.file_size) != row[2]:
-                        raise DistlibException('size mismatch for '
-                                               '%s' % u_arcname)
-                    if row[1]:
-                        kind, value = row[1].split('=', 1)
-                        with zf.open(arcname) as bf:
-                            data = bf.read()
-                        _, digest = self.get_hash(data, kind)
-                        if digest != value:
-                            raise DistlibException('digest mismatch for '
-                                                   '%s' % arcname)
-
-                    if lib_only and u_arcname.startswith((info_pfx, data_pfx)):
-                        logger.debug('lib_only: skipping %s', u_arcname)
-                        continue
-                    is_script = (u_arcname.startswith(script_pfx)
-                                 and not u_arcname.endswith('.exe'))
-
-                    if u_arcname.startswith(data_pfx):
-                        _, where, rp = u_arcname.split('/', 2)
-                        outfile = os.path.join(paths[where], convert_path(rp))
-                    else:
-                        # meant for site-packages.
-                        if u_arcname in (wheel_metadata_name, record_name):
-                            continue
-                        outfile = os.path.join(libdir, convert_path(u_arcname))
-                    if not is_script:
-                        with zf.open(arcname) as bf:
-                            fileop.copy_stream(bf, outfile)
-                        outfiles.append(outfile)
-                        # Double check the digest of the written file
-                        if not dry_run and row[1]:
-                            with open(outfile, 'rb') as bf:
-                                data = bf.read()
-                                _, newdigest = self.get_hash(data, kind)
-                                if newdigest != digest:
-                                    raise DistlibException('digest mismatch '
-                                                           'on write for '
-                                                           '%s' % outfile)
-                        if bc and outfile.endswith('.py'):
-                            try:
-                                pyc = fileop.byte_compile(outfile,
-                                                          hashed_invalidation=bc_hashed_invalidation)
-                                outfiles.append(pyc)
-                            except Exception:
-                                # Don't give up if byte-compilation fails,
-                                # but log it and perhaps warn the user
-                                logger.warning('Byte-compilation failed',
-                                               exc_info=True)
-                    else:
-                        fn = os.path.basename(convert_path(arcname))
-                        workname = os.path.join(workdir, fn)
-                        with zf.open(arcname) as bf:
-                            fileop.copy_stream(bf, workname)
-
-                        dn, fn = os.path.split(outfile)
-                        maker.target_dir = dn
-                        filenames = maker.make(fn)
-                        fileop.set_executable_mode(filenames)
-                        outfiles.extend(filenames)
-
-                if lib_only:
-                    logger.debug('lib_only: returning None')
-                    dist = None
-                else:
-                    # Generate scripts
-
-                    # Try to get pydist.json so we can see if there are
-                    # any commands to generate. If this fails (e.g. because
-                    # of a legacy wheel), log a warning but don't give up.
-                    commands = None
-                    file_version = self.info['Wheel-Version']
-                    if file_version == '1.0':
-                        # Use legacy info
-                        ep = posixpath.join(info_dir, 'entry_points.txt')
-                        try:
-                            with zf.open(ep) as bwf:
-                                epdata = read_exports(bwf)
-                            commands = {}
-                            for key in ('console', 'gui'):
-                                k = '%s_scripts' % key
-                                if k in epdata:
-                                    commands['wrap_%s' % key] = d = {}
-                                    for v in epdata[k].values():
-                                        s = '%s:%s' % (v.prefix, v.suffix)
-                                        if v.flags:
-                                            s += ' %s' % v.flags
-                                        d[v.name] = s
-                        except Exception:
-                            logger.warning('Unable to read legacy script '
-                                           'metadata, so cannot generate '
-                                           'scripts')
-                    else:
-                        try:
-                            with zf.open(metadata_name) as bwf:
-                                wf = wrapper(bwf)
-                                commands = json.load(wf).get('extensions')
-                                if commands:
-                                    commands = commands.get('python.commands')
-                        except Exception:
-                            logger.warning('Unable to read JSON metadata, so '
-                                           'cannot generate scripts')
-                    if commands:
-                        console_scripts = commands.get('wrap_console', {})
-                        gui_scripts = commands.get('wrap_gui', {})
-                        if console_scripts or gui_scripts:
-                            script_dir = paths.get('scripts', '')
-                            if not os.path.isdir(script_dir):
-                                raise ValueError('Valid script path not '
-                                                 'specified')
-                            maker.target_dir = script_dir
-                            for k, v in console_scripts.items():
-                                script = '%s = %s' % (k, v)
-                                filenames = maker.make(script)
-                                fileop.set_executable_mode(filenames)
-
-                            if gui_scripts:
-                                options = {'gui': True }
-                                for k, v in gui_scripts.items():
-                                    script = '%s = %s' % (k, v)
-                                    filenames = maker.make(script, options)
-                                    fileop.set_executable_mode(filenames)
-
-                    p = os.path.join(libdir, info_dir)
-                    dist = InstalledDistribution(p)
-
-                    # Write SHARED
-                    paths = dict(paths)     # don't change passed in dict
-                    del paths['purelib']
-                    del paths['platlib']
-                    paths['lib'] = libdir
-                    p = dist.write_shared_locations(paths, dry_run)
-                    if p:
-                        outfiles.append(p)
-
-                    # Write RECORD
-                    dist.write_installed_files(outfiles, paths['prefix'],
-                                               dry_run)
-                return dist
-            except Exception:  # pragma: no cover
-                logger.exception('installation failed.')
-                fileop.rollback()
-                raise
-            finally:
-                shutil.rmtree(workdir)
-
-    def _get_dylib_cache(self):
-        global cache
-        if cache is None:
-            # Use native string to avoid issues on 2.x: see Python #20140.
-            base = os.path.join(get_cache_base(), str('dylib-cache'),
-                                sys.version[:3])
-            cache = Cache(base)
-        return cache
-
-    def _get_extensions(self):
-        pathname = os.path.join(self.dirname, self.filename)
-        name_ver = '%s-%s' % (self.name, self.version)
-        info_dir = '%s.dist-info' % name_ver
-        arcname = posixpath.join(info_dir, 'EXTENSIONS')
-        wrapper = codecs.getreader('utf-8')
-        result = []
-        with ZipFile(pathname, 'r') as zf:
-            try:
-                with zf.open(arcname) as bf:
-                    wf = wrapper(bf)
-                    extensions = json.load(wf)
-                    cache = self._get_dylib_cache()
-                    prefix = cache.prefix_to_dir(pathname)
-                    cache_base = os.path.join(cache.base, prefix)
-                    if not os.path.isdir(cache_base):
-                        os.makedirs(cache_base)
-                    for name, relpath in extensions.items():
-                        dest = os.path.join(cache_base, convert_path(relpath))
-                        if not os.path.exists(dest):
-                            extract = True
-                        else:
-                            file_time = os.stat(dest).st_mtime
-                            file_time = datetime.datetime.fromtimestamp(file_time)
-                            info = zf.getinfo(relpath)
-                            wheel_time = datetime.datetime(*info.date_time)
-                            extract = wheel_time > file_time
-                        if extract:
-                            zf.extract(relpath, cache_base)
-                        result.append((name, dest))
-            except KeyError:
-                pass
-        return result
-
-    def is_compatible(self):
-        """
-        Determine if a wheel is compatible with the running system.
-        """
-        return is_compatible(self)
-
-    def is_mountable(self):
-        """
-        Determine if a wheel is asserted as mountable by its metadata.
-        """
-        return True # for now - metadata details TBD
-
-    def mount(self, append=False):
-        pathname = os.path.abspath(os.path.join(self.dirname, self.filename))
-        if not self.is_compatible():
-            msg = 'Wheel %s not compatible with this Python.' % pathname
-            raise DistlibException(msg)
-        if not self.is_mountable():
-            msg = 'Wheel %s is marked as not mountable.' % pathname
-            raise DistlibException(msg)
-        if pathname in sys.path:
-            logger.debug('%s already in path', pathname)
-        else:
-            if append:
-                sys.path.append(pathname)
-            else:
-                sys.path.insert(0, pathname)
-            extensions = self._get_extensions()
-            if extensions:
-                if _hook not in sys.meta_path:
-                    sys.meta_path.append(_hook)
-                _hook.add(pathname, extensions)
-
-    def unmount(self):
-        pathname = os.path.abspath(os.path.join(self.dirname, self.filename))
-        if pathname not in sys.path:
-            logger.debug('%s not in path', pathname)
-        else:
-            sys.path.remove(pathname)
-            if pathname in _hook.impure_wheels:
-                _hook.remove(pathname)
-            if not _hook.impure_wheels:
-                if _hook in sys.meta_path:
-                    sys.meta_path.remove(_hook)
-
-    def verify(self):
-        pathname = os.path.join(self.dirname, self.filename)
-        name_ver = '%s-%s' % (self.name, self.version)
-        data_dir = '%s.data' % name_ver
-        info_dir = '%s.dist-info' % name_ver
-
-        metadata_name = posixpath.join(info_dir, METADATA_FILENAME)
-        wheel_metadata_name = posixpath.join(info_dir, 'WHEEL')
-        record_name = posixpath.join(info_dir, 'RECORD')
-
-        wrapper = codecs.getreader('utf-8')
-
-        with ZipFile(pathname, 'r') as zf:
-            with zf.open(wheel_metadata_name) as bwf:
-                wf = wrapper(bwf)
-                message = message_from_file(wf)
-            wv = message['Wheel-Version'].split('.', 1)
-            file_version = tuple([int(i) for i in wv])
-            # TODO version verification
-
-            records = {}
-            with zf.open(record_name) as bf:
-                with CSVReader(stream=bf) as reader:
-                    for row in reader:
-                        p = row[0]
-                        records[p] = row
-
-            for zinfo in zf.infolist():
-                arcname = zinfo.filename
-                if isinstance(arcname, text_type):
-                    u_arcname = arcname
-                else:
-                    u_arcname = arcname.decode('utf-8')
-                if '..' in u_arcname:
-                    raise DistlibException('invalid entry in '
-                                           'wheel: %r' % u_arcname)
-
-                # The signature file won't be in RECORD,
-                # and we  don't currently don't do anything with it
-                if u_arcname.endswith('/RECORD.jws'):
-                    continue
-                row = records[u_arcname]
-                if row[2] and str(zinfo.file_size) != row[2]:
-                    raise DistlibException('size mismatch for '
-                                           '%s' % u_arcname)
-                if row[1]:
-                    kind, value = row[1].split('=', 1)
-                    with zf.open(arcname) as bf:
-                        data = bf.read()
-                    _, digest = self.get_hash(data, kind)
-                    if digest != value:
-                        raise DistlibException('digest mismatch for '
-                                               '%s' % arcname)
-
-    def update(self, modifier, dest_dir=None, **kwargs):
-        """
-        Update the contents of a wheel in a generic way. The modifier should
-        be a callable which expects a dictionary argument: its keys are
-        archive-entry paths, and its values are absolute filesystem paths
-        where the contents the corresponding archive entries can be found. The
-        modifier is free to change the contents of the files pointed to, add
-        new entries and remove entries, before returning. This method will
-        extract the entire contents of the wheel to a temporary location, call
-        the modifier, and then use the passed (and possibly updated)
-        dictionary to write a new wheel. If ``dest_dir`` is specified, the new
-        wheel is written there -- otherwise, the original wheel is overwritten.
-
-        The modifier should return True if it updated the wheel, else False.
-        This method returns the same value the modifier returns.
-        """
-
-        def get_version(path_map, info_dir):
-            version = path = None
-            key = '%s/%s' % (info_dir, METADATA_FILENAME)
-            if key not in path_map:
-                key = '%s/PKG-INFO' % info_dir
-            if key in path_map:
-                path = path_map[key]
-                version = Metadata(path=path).version
-            return version, path
-
-        def update_version(version, path):
-            updated = None
-            try:
-                v = NormalizedVersion(version)
-                i = version.find('-')
-                if i < 0:
-                    updated = '%s+1' % version
-                else:
-                    parts = [int(s) for s in version[i + 1:].split('.')]
-                    parts[-1] += 1
-                    updated = '%s+%s' % (version[:i],
-                                         '.'.join(str(i) for i in parts))
-            except UnsupportedVersionError:
-                logger.debug('Cannot update non-compliant (PEP-440) '
-                             'version %r', version)
-            if updated:
-                md = Metadata(path=path)
-                md.version = updated
-                legacy = not path.endswith(METADATA_FILENAME)
-                md.write(path=path, legacy=legacy)
-                logger.debug('Version updated from %r to %r', version,
-                             updated)
-
-        pathname = os.path.join(self.dirname, self.filename)
-        name_ver = '%s-%s' % (self.name, self.version)
-        info_dir = '%s.dist-info' % name_ver
-        record_name = posixpath.join(info_dir, 'RECORD')
-        with tempdir() as workdir:
-            with ZipFile(pathname, 'r') as zf:
-                path_map = {}
-                for zinfo in zf.infolist():
-                    arcname = zinfo.filename
-                    if isinstance(arcname, text_type):
-                        u_arcname = arcname
-                    else:
-                        u_arcname = arcname.decode('utf-8')
-                    if u_arcname == record_name:
-                        continue
-                    if '..' in u_arcname:
-                        raise DistlibException('invalid entry in '
-                                               'wheel: %r' % u_arcname)
-                    zf.extract(zinfo, workdir)
-                    path = os.path.join(workdir, convert_path(u_arcname))
-                    path_map[u_arcname] = path
-
-            # Remember the version.
-            original_version, _ = get_version(path_map, info_dir)
-            # Files extracted. Call the modifier.
-            modified = modifier(path_map, **kwargs)
-            if modified:
-                # Something changed - need to build a new wheel.
-                current_version, path = get_version(path_map, info_dir)
-                if current_version and (current_version == original_version):
-                    # Add or update local version to signify changes.
-                    update_version(current_version, path)
-                # Decide where the new wheel goes.
-                if dest_dir is None:
-                    fd, newpath = tempfile.mkstemp(suffix='.whl',
-                                                   prefix='wheel-update-',
-                                                   dir=workdir)
-                    os.close(fd)
-                else:
-                    if not os.path.isdir(dest_dir):
-                        raise DistlibException('Not a directory: %r' % dest_dir)
-                    newpath = os.path.join(dest_dir, self.filename)
-                archive_paths = list(path_map.items())
-                distinfo = os.path.join(workdir, info_dir)
-                info = distinfo, info_dir
-                self.write_records(info, workdir, archive_paths)
-                self.build_zip(newpath, archive_paths)
-                if dest_dir is None:
-                    shutil.copyfile(newpath, pathname)
-        return modified
-
-def compatible_tags():
-    """
-    Return (pyver, abi, arch) tuples compatible with this Python.
-    """
-    versions = [VER_SUFFIX]
-    major = VER_SUFFIX[0]
-    for minor in range(sys.version_info[1] - 1, - 1, -1):
-        versions.append(''.join([major, str(minor)]))
-
-    abis = []
-    for suffix, _, _ in imp.get_suffixes():
-        if suffix.startswith('.abi'):
-            abis.append(suffix.split('.', 2)[1])
-    abis.sort()
-    if ABI != 'none':
-        abis.insert(0, ABI)
-    abis.append('none')
-    result = []
-
-    arches = [ARCH]
-    if sys.platform == 'darwin':
-        m = re.match(r'(\w+)_(\d+)_(\d+)_(\w+)$', ARCH)
-        if m:
-            name, major, minor, arch = m.groups()
-            minor = int(minor)
-            matches = [arch]
-            if arch in ('i386', 'ppc'):
-                matches.append('fat')
-            if arch in ('i386', 'ppc', 'x86_64'):
-                matches.append('fat3')
-            if arch in ('ppc64', 'x86_64'):
-                matches.append('fat64')
-            if arch in ('i386', 'x86_64'):
-                matches.append('intel')
-            if arch in ('i386', 'x86_64', 'intel', 'ppc', 'ppc64'):
-                matches.append('universal')
-            while minor >= 0:
-                for match in matches:
-                    s = '%s_%s_%s_%s' % (name, major, minor, match)
-                    if s != ARCH:   # already there
-                        arches.append(s)
-                minor -= 1
-
-    # Most specific - our Python version, ABI and arch
-    for abi in abis:
-        for arch in arches:
-            result.append((''.join((IMP_PREFIX, versions[0])), abi, arch))
-
-    # where no ABI / arch dependency, but IMP_PREFIX dependency
-    for i, version in enumerate(versions):
-        result.append((''.join((IMP_PREFIX, version)), 'none', 'any'))
-        if i == 0:
-            result.append((''.join((IMP_PREFIX, version[0])), 'none', 'any'))
-
-    # no IMP_PREFIX, ABI or arch dependency
-    for i, version in enumerate(versions):
-        result.append((''.join(('py', version)), 'none', 'any'))
-        if i == 0:
-            result.append((''.join(('py', version[0])), 'none', 'any'))
-    return set(result)
-
-
-COMPATIBLE_TAGS = compatible_tags()
-
-del compatible_tags
-
-
-def is_compatible(wheel, tags=None):
-    if not isinstance(wheel, Wheel):
-        wheel = Wheel(wheel)    # assume it's a filename
-    result = False
-    if tags is None:
-        tags = COMPATIBLE_TAGS
-    for ver, abi, arch in tags:
-        if ver in wheel.pyver and abi in wheel.abi and arch in wheel.arch:
-            result = True
-            break
-    return result
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distro.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distro.py
deleted file mode 100644
index aa4defc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/distro.py
+++ /dev/null
@@ -1,1197 +0,0 @@
-# Copyright 2015,2016,2017 Nir Cohen
-#
-# Licensed under the Apache License, Version 2.0 (the "License");
-# you may not use this file except in compliance with the License.
-# You may obtain a copy of the License at
-#
-# http://www.apache.org/licenses/LICENSE-2.0
-#
-# Unless required by applicable law or agreed to in writing, software
-# distributed under the License is distributed on an "AS IS" BASIS,
-# WITHOUT WARRANTIES OR CONDITIONS OF ANY KIND, either express or implied.
-# See the License for the specific language governing permissions and
-# limitations under the License.
-
-"""
-The ``distro`` package (``distro`` stands for Linux Distribution) provides
-information about the Linux distribution it runs on, such as a reliable
-machine-readable distro ID, or version information.
-
-It is a renewed alternative implementation for Python's original
-:py:func:`platform.linux_distribution` function, but it provides much more
-functionality. An alternative implementation became necessary because Python
-3.5 deprecated this function, and Python 3.7 is expected to remove it
-altogether. Its predecessor function :py:func:`platform.dist` was already
-deprecated since Python 2.6 and is also expected to be removed in Python 3.7.
-Still, there are many cases in which access to OS distribution information
-is needed. See `Python issue 1322 <https://bugs.python.org/issue1322>`_ for
-more information.
-"""
-
-import os
-import re
-import sys
-import json
-import shlex
-import logging
-import argparse
-import subprocess
-
-
-_UNIXCONFDIR = os.environ.get('UNIXCONFDIR', '/etc')
-_OS_RELEASE_BASENAME = 'os-release'
-
-#: Translation table for normalizing the "ID" attribute defined in os-release
-#: files, for use by the :func:`distro.id` method.
-#:
-#: * Key: Value as defined in the os-release file, translated to lower case,
-#:   with blanks translated to underscores.
-#:
-#: * Value: Normalized value.
-NORMALIZED_OS_ID = {}
-
-#: Translation table for normalizing the "Distributor ID" attribute returned by
-#: the lsb_release command, for use by the :func:`distro.id` method.
-#:
-#: * Key: Value as returned by the lsb_release command, translated to lower
-#:   case, with blanks translated to underscores.
-#:
-#: * Value: Normalized value.
-NORMALIZED_LSB_ID = {
-    'enterpriseenterprise': 'oracle',  # Oracle Enterprise Linux
-    'redhatenterpriseworkstation': 'rhel',  # RHEL 6, 7 Workstation
-    'redhatenterpriseserver': 'rhel',  # RHEL 6, 7 Server
-}
-
-#: Translation table for normalizing the distro ID derived from the file name
-#: of distro release files, for use by the :func:`distro.id` method.
-#:
-#: * Key: Value as derived from the file name of a distro release file,
-#:   translated to lower case, with blanks translated to underscores.
-#:
-#: * Value: Normalized value.
-NORMALIZED_DISTRO_ID = {
-    'redhat': 'rhel',  # RHEL 6.x, 7.x
-}
-
-# Pattern for content of distro release file (reversed)
-_DISTRO_RELEASE_CONTENT_REVERSED_PATTERN = re.compile(
-    r'(?:[^)]*\)(.*)\()? *(?:STL )?([\d.+\-a-z]*\d) *(?:esaeler *)?(.+)')
-
-# Pattern for base file name of distro release file
-_DISTRO_RELEASE_BASENAME_PATTERN = re.compile(
-    r'(\w+)[-_](release|version)$')
-
-# Base file names to be ignored when searching for distro release file
-_DISTRO_RELEASE_IGNORE_BASENAMES = (
-    'debian_version',
-    'lsb-release',
-    'oem-release',
-    _OS_RELEASE_BASENAME,
-    'system-release'
-)
-
-
-def linux_distribution(full_distribution_name=True):
-    """
-    Return information about the current OS distribution as a tuple
-    ``(id_name, version, codename)`` with items as follows:
-
-    * ``id_name``:  If *full_distribution_name* is false, the result of
-      :func:`distro.id`. Otherwise, the result of :func:`distro.name`.
-
-    * ``version``:  The result of :func:`distro.version`.
-
-    * ``codename``:  The result of :func:`distro.codename`.
-
-    The interface of this function is compatible with the original
-    :py:func:`platform.linux_distribution` function, supporting a subset of
-    its parameters.
-
-    The data it returns may not exactly be the same, because it uses more data
-    sources than the original function, and that may lead to different data if
-    the OS distribution is not consistent across multiple data sources it
-    provides (there are indeed such distributions ...).
-
-    Another reason for differences is the fact that the :func:`distro.id`
-    method normalizes the distro ID string to a reliable machine-readable value
-    for a number of popular OS distributions.
-    """
-    return _distro.linux_distribution(full_distribution_name)
-
-
-def id():
-    """
-    Return the distro ID of the current distribution, as a
-    machine-readable string.
-
-    For a number of OS distributions, the returned distro ID value is
-    *reliable*, in the sense that it is documented and that it does not change
-    across releases of the distribution.
-
-    This package maintains the following reliable distro ID values:
-
-    ==============  =========================================
-    Distro ID       Distribution
-    ==============  =========================================
-    "ubuntu"        Ubuntu
-    "debian"        Debian
-    "rhel"          RedHat Enterprise Linux
-    "centos"        CentOS
-    "fedora"        Fedora
-    "sles"          SUSE Linux Enterprise Server
-    "opensuse"      openSUSE
-    "amazon"        Amazon Linux
-    "arch"          Arch Linux
-    "cloudlinux"    CloudLinux OS
-    "exherbo"       Exherbo Linux
-    "gentoo"        GenToo Linux
-    "ibm_powerkvm"  IBM PowerKVM
-    "kvmibm"        KVM for IBM z Systems
-    "linuxmint"     Linux Mint
-    "mageia"        Mageia
-    "mandriva"      Mandriva Linux
-    "parallels"     Parallels
-    "pidora"        Pidora
-    "raspbian"      Raspbian
-    "oracle"        Oracle Linux (and Oracle Enterprise Linux)
-    "scientific"    Scientific Linux
-    "slackware"     Slackware
-    "xenserver"     XenServer
-    "openbsd"       OpenBSD
-    "netbsd"        NetBSD
-    "freebsd"       FreeBSD
-    ==============  =========================================
-
-    If you have a need to get distros for reliable IDs added into this set,
-    or if you find that the :func:`distro.id` function returns a different
-    distro ID for one of the listed distros, please create an issue in the
-    `distro issue tracker`_.
-
-    **Lookup hierarchy and transformations:**
-
-    First, the ID is obtained from the following sources, in the specified
-    order. The first available and non-empty value is used:
-
-    * the value of the "ID" attribute of the os-release file,
-
-    * the value of the "Distributor ID" attribute returned by the lsb_release
-      command,
-
-    * the first part of the file name of the distro release file,
-
-    The so determined ID value then passes the following transformations,
-    before it is returned by this method:
-
-    * it is translated to lower case,
-
-    * blanks (which should not be there anyway) are translated to underscores,
-
-    * a normalization of the ID is performed, based upon
-      `normalization tables`_. The purpose of this normalization is to ensure
-      that the ID is as reliable as possible, even across incompatible changes
-      in the OS distributions. A common reason for an incompatible change is
-      the addition of an os-release file, or the addition of the lsb_release
-      command, with ID values that differ from what was previously determined
-      from the distro release file name.
-    """
-    return _distro.id()
-
-
-def name(pretty=False):
-    """
-    Return the name of the current OS distribution, as a human-readable
-    string.
-
-    If *pretty* is false, the name is returned without version or codename.
-    (e.g. "CentOS Linux")
-
-    If *pretty* is true, the version and codename are appended.
-    (e.g. "CentOS Linux 7.1.1503 (Core)")
-
-    **Lookup hierarchy:**
-
-    The name is obtained from the following sources, in the specified order.
-    The first available and non-empty value is used:
-
-    * If *pretty* is false:
-
-      - the value of the "NAME" attribute of the os-release file,
-
-      - the value of the "Distributor ID" attribute returned by the lsb_release
-        command,
-
-      - the value of the "<name>" field of the distro release file.
-
-    * If *pretty* is true:
-
-      - the value of the "PRETTY_NAME" attribute of the os-release file,
-
-      - the value of the "Description" attribute returned by the lsb_release
-        command,
-
-      - the value of the "<name>" field of the distro release file, appended
-        with the value of the pretty version ("<version_id>" and "<codename>"
-        fields) of the distro release file, if available.
-    """
-    return _distro.name(pretty)
-
-
-def version(pretty=False, best=False):
-    """
-    Return the version of the current OS distribution, as a human-readable
-    string.
-
-    If *pretty* is false, the version is returned without codename (e.g.
-    "7.0").
-
-    If *pretty* is true, the codename in parenthesis is appended, if the
-    codename is non-empty (e.g. "7.0 (Maipo)").
-
-    Some distributions provide version numbers with different precisions in
-    the different sources of distribution information. Examining the different
-    sources in a fixed priority order does not always yield the most precise
-    version (e.g. for Debian 8.2, or CentOS 7.1).
-
-    The *best* parameter can be used to control the approach for the returned
-    version:
-
-    If *best* is false, the first non-empty version number in priority order of
-    the examined sources is returned.
-
-    If *best* is true, the most precise version number out of all examined
-    sources is returned.
-
-    **Lookup hierarchy:**
-
-    In all cases, the version number is obtained from the following sources.
-    If *best* is false, this order represents the priority order:
-
-    * the value of the "VERSION_ID" attribute of the os-release file,
-    * the value of the "Release" attribute returned by the lsb_release
-      command,
-    * the version number parsed from the "<version_id>" field of the first line
-      of the distro release file,
-    * the version number parsed from the "PRETTY_NAME" attribute of the
-      os-release file, if it follows the format of the distro release files.
-    * the version number parsed from the "Description" attribute returned by
-      the lsb_release command, if it follows the format of the distro release
-      files.
-    """
-    return _distro.version(pretty, best)
-
-
-def version_parts(best=False):
-    """
-    Return the version of the current OS distribution as a tuple
-    ``(major, minor, build_number)`` with items as follows:
-
-    * ``major``:  The result of :func:`distro.major_version`.
-
-    * ``minor``:  The result of :func:`distro.minor_version`.
-
-    * ``build_number``:  The result of :func:`distro.build_number`.
-
-    For a description of the *best* parameter, see the :func:`distro.version`
-    method.
-    """
-    return _distro.version_parts(best)
-
-
-def major_version(best=False):
-    """
-    Return the major version of the current OS distribution, as a string,
-    if provided.
-    Otherwise, the empty string is returned. The major version is the first
-    part of the dot-separated version string.
-
-    For a description of the *best* parameter, see the :func:`distro.version`
-    method.
-    """
-    return _distro.major_version(best)
-
-
-def minor_version(best=False):
-    """
-    Return the minor version of the current OS distribution, as a string,
-    if provided.
-    Otherwise, the empty string is returned. The minor version is the second
-    part of the dot-separated version string.
-
-    For a description of the *best* parameter, see the :func:`distro.version`
-    method.
-    """
-    return _distro.minor_version(best)
-
-
-def build_number(best=False):
-    """
-    Return the build number of the current OS distribution, as a string,
-    if provided.
-    Otherwise, the empty string is returned. The build number is the third part
-    of the dot-separated version string.
-
-    For a description of the *best* parameter, see the :func:`distro.version`
-    method.
-    """
-    return _distro.build_number(best)
-
-
-def like():
-    """
-    Return a space-separated list of distro IDs of distributions that are
-    closely related to the current OS distribution in regards to packaging
-    and programming interfaces, for example distributions the current
-    distribution is a derivative from.
-
-    **Lookup hierarchy:**
-
-    This information item is only provided by the os-release file.
-    For details, see the description of the "ID_LIKE" attribute in the
-    `os-release man page
-    <http://www.freedesktop.org/software/systemd/man/os-release.html>`_.
-    """
-    return _distro.like()
-
-
-def codename():
-    """
-    Return the codename for the release of the current OS distribution,
-    as a string.
-
-    If the distribution does not have a codename, an empty string is returned.
-
-    Note that the returned codename is not always really a codename. For
-    example, openSUSE returns "x86_64". This function does not handle such
-    cases in any special way and just returns the string it finds, if any.
-
-    **Lookup hierarchy:**
-
-    * the codename within the "VERSION" attribute of the os-release file, if
-      provided,
-
-    * the value of the "Codename" attribute returned by the lsb_release
-      command,
-
-    * the value of the "<codename>" field of the distro release file.
-    """
-    return _distro.codename()
-
-
-def info(pretty=False, best=False):
-    """
-    Return certain machine-readable information items about the current OS
-    distribution in a dictionary, as shown in the following example:
-
-    .. sourcecode:: python
-
-        {
-            'id': 'rhel',
-            'version': '7.0',
-            'version_parts': {
-                'major': '7',
-                'minor': '0',
-                'build_number': ''
-            },
-            'like': 'fedora',
-            'codename': 'Maipo'
-        }
-
-    The dictionary structure and keys are always the same, regardless of which
-    information items are available in the underlying data sources. The values
-    for the various keys are as follows:
-
-    * ``id``:  The result of :func:`distro.id`.
-
-    * ``version``:  The result of :func:`distro.version`.
-
-    * ``version_parts -> major``:  The result of :func:`distro.major_version`.
-
-    * ``version_parts -> minor``:  The result of :func:`distro.minor_version`.
-
-    * ``version_parts -> build_number``:  The result of
-      :func:`distro.build_number`.
-
-    * ``like``:  The result of :func:`distro.like`.
-
-    * ``codename``:  The result of :func:`distro.codename`.
-
-    For a description of the *pretty* and *best* parameters, see the
-    :func:`distro.version` method.
-    """
-    return _distro.info(pretty, best)
-
-
-def os_release_info():
-    """
-    Return a dictionary containing key-value pairs for the information items
-    from the os-release file data source of the current OS distribution.
-
-    See `os-release file`_ for details about these information items.
-    """
-    return _distro.os_release_info()
-
-
-def lsb_release_info():
-    """
-    Return a dictionary containing key-value pairs for the information items
-    from the lsb_release command data source of the current OS distribution.
-
-    See `lsb_release command output`_ for details about these information
-    items.
-    """
-    return _distro.lsb_release_info()
-
-
-def distro_release_info():
-    """
-    Return a dictionary containing key-value pairs for the information items
-    from the distro release file data source of the current OS distribution.
-
-    See `distro release file`_ for details about these information items.
-    """
-    return _distro.distro_release_info()
-
-
-def uname_info():
-    """
-    Return a dictionary containing key-value pairs for the information items
-    from the distro release file data source of the current OS distribution.
-    """
-    return _distro.uname_info()
-
-
-def os_release_attr(attribute):
-    """
-    Return a single named information item from the os-release file data source
-    of the current OS distribution.
-
-    Parameters:
-
-    * ``attribute`` (string): Key of the information item.
-
-    Returns:
-
-    * (string): Value of the information item, if the item exists.
-      The empty string, if the item does not exist.
-
-    See `os-release file`_ for details about these information items.
-    """
-    return _distro.os_release_attr(attribute)
-
-
-def lsb_release_attr(attribute):
-    """
-    Return a single named information item from the lsb_release command output
-    data source of the current OS distribution.
-
-    Parameters:
-
-    * ``attribute`` (string): Key of the information item.
-
-    Returns:
-
-    * (string): Value of the information item, if the item exists.
-      The empty string, if the item does not exist.
-
-    See `lsb_release command output`_ for details about these information
-    items.
-    """
-    return _distro.lsb_release_attr(attribute)
-
-
-def distro_release_attr(attribute):
-    """
-    Return a single named information item from the distro release file
-    data source of the current OS distribution.
-
-    Parameters:
-
-    * ``attribute`` (string): Key of the information item.
-
-    Returns:
-
-    * (string): Value of the information item, if the item exists.
-      The empty string, if the item does not exist.
-
-    See `distro release file`_ for details about these information items.
-    """
-    return _distro.distro_release_attr(attribute)
-
-
-def uname_attr(attribute):
-    """
-    Return a single named information item from the distro release file
-    data source of the current OS distribution.
-
-    Parameters:
-
-    * ``attribute`` (string): Key of the information item.
-
-    Returns:
-
-    * (string): Value of the information item, if the item exists.
-                The empty string, if the item does not exist.
-    """
-    return _distro.uname_attr(attribute)
-
-
-class cached_property(object):
-    """A version of @property which caches the value.  On access, it calls the
-    underlying function and sets the value in `__dict__` so future accesses
-    will not re-call the property.
-    """
-    def __init__(self, f):
-        self._fname = f.__name__
-        self._f = f
-
-    def __get__(self, obj, owner):
-        assert obj is not None, 'call {} on an instance'.format(self._fname)
-        ret = obj.__dict__[self._fname] = self._f(obj)
-        return ret
-
-
-class LinuxDistribution(object):
-    """
-    Provides information about a OS distribution.
-
-    This package creates a private module-global instance of this class with
-    default initialization arguments, that is used by the
-    `consolidated accessor functions`_ and `single source accessor functions`_.
-    By using default initialization arguments, that module-global instance
-    returns data about the current OS distribution (i.e. the distro this
-    package runs on).
-
-    Normally, it is not necessary to create additional instances of this class.
-    However, in situations where control is needed over the exact data sources
-    that are used, instances of this class can be created with a specific
-    distro release file, or a specific os-release file, or without invoking the
-    lsb_release command.
-    """
-
-    def __init__(self,
-                 include_lsb=True,
-                 os_release_file='',
-                 distro_release_file='',
-                 include_uname=True):
-        """
-        The initialization method of this class gathers information from the
-        available data sources, and stores that in private instance attributes.
-        Subsequent access to the information items uses these private instance
-        attributes, so that the data sources are read only once.
-
-        Parameters:
-
-        * ``include_lsb`` (bool): Controls whether the
-          `lsb_release command output`_ is included as a data source.
-
-          If the lsb_release command is not available in the program execution
-          path, the data source for the lsb_release command will be empty.
-
-        * ``os_release_file`` (string): The path name of the
-          `os-release file`_ that is to be used as a data source.
-
-          An empty string (the default) will cause the default path name to
-          be used (see `os-release file`_ for details).
-
-          If the specified or defaulted os-release file does not exist, the
-          data source for the os-release file will be empty.
-
-        * ``distro_release_file`` (string): The path name of the
-          `distro release file`_ that is to be used as a data source.
-
-          An empty string (the default) will cause a default search algorithm
-          to be used (see `distro release file`_ for details).
-
-          If the specified distro release file does not exist, or if no default
-          distro release file can be found, the data source for the distro
-          release file will be empty.
-
-        * ``include_name`` (bool): Controls whether uname command output is
-          included as a data source. If the uname command is not available in
-          the program execution path the data source for the uname command will
-          be empty.
-
-        Public instance attributes:
-
-        * ``os_release_file`` (string): The path name of the
-          `os-release file`_ that is actually used as a data source. The
-          empty string if no distro release file is used as a data source.
-
-        * ``distro_release_file`` (string): The path name of the
-          `distro release file`_ that is actually used as a data source. The
-          empty string if no distro release file is used as a data source.
-
-        * ``include_lsb`` (bool): The result of the ``include_lsb`` parameter.
-          This controls whether the lsb information will be loaded.
-
-        * ``include_uname`` (bool): The result of the ``include_uname``
-          parameter. This controls whether the uname information will
-          be loaded.
-
-        Raises:
-
-        * :py:exc:`IOError`: Some I/O issue with an os-release file or distro
-          release file.
-
-        * :py:exc:`subprocess.CalledProcessError`: The lsb_release command had
-          some issue (other than not being available in the program execution
-          path).
-
-        * :py:exc:`UnicodeError`: A data source has unexpected characters or
-          uses an unexpected encoding.
-        """
-        self.os_release_file = os_release_file or \
-            os.path.join(_UNIXCONFDIR, _OS_RELEASE_BASENAME)
-        self.distro_release_file = distro_release_file or ''  # updated later
-        self.include_lsb = include_lsb
-        self.include_uname = include_uname
-
-    def __repr__(self):
-        """Return repr of all info
-        """
-        return \
-            "LinuxDistribution(" \
-            "os_release_file={self.os_release_file!r}, " \
-            "distro_release_file={self.distro_release_file!r}, " \
-            "include_lsb={self.include_lsb!r}, " \
-            "include_uname={self.include_uname!r}, " \
-            "_os_release_info={self._os_release_info!r}, " \
-            "_lsb_release_info={self._lsb_release_info!r}, " \
-            "_distro_release_info={self._distro_release_info!r}, " \
-            "_uname_info={self._uname_info!r})".format(
-                self=self)
-
-    def linux_distribution(self, full_distribution_name=True):
-        """
-        Return information about the OS distribution that is compatible
-        with Python's :func:`platform.linux_distribution`, supporting a subset
-        of its parameters.
-
-        For details, see :func:`distro.linux_distribution`.
-        """
-        return (
-            self.name() if full_distribution_name else self.id(),
-            self.version(),
-            self.codename()
-        )
-
-    def id(self):
-        """Return the distro ID of the OS distribution, as a string.
-
-        For details, see :func:`distro.id`.
-        """
-        def normalize(distro_id, table):
-            distro_id = distro_id.lower().replace(' ', '_')
-            return table.get(distro_id, distro_id)
-
-        distro_id = self.os_release_attr('id')
-        if distro_id:
-            return normalize(distro_id, NORMALIZED_OS_ID)
-
-        distro_id = self.lsb_release_attr('distributor_id')
-        if distro_id:
-            return normalize(distro_id, NORMALIZED_LSB_ID)
-
-        distro_id = self.distro_release_attr('id')
-        if distro_id:
-            return normalize(distro_id, NORMALIZED_DISTRO_ID)
-
-        distro_id = self.uname_attr('id')
-        if distro_id:
-            return normalize(distro_id, NORMALIZED_DISTRO_ID)
-
-        return ''
-
-    def name(self, pretty=False):
-        """
-        Return the name of the OS distribution, as a string.
-
-        For details, see :func:`distro.name`.
-        """
-        name = self.os_release_attr('name') \
-            or self.lsb_release_attr('distributor_id') \
-            or self.distro_release_attr('name') \
-            or self.uname_attr('name')
-        if pretty:
-            name = self.os_release_attr('pretty_name') \
-                or self.lsb_release_attr('description')
-            if not name:
-                name = self.distro_release_attr('name') \
-                       or self.uname_attr('name')
-                version = self.version(pretty=True)
-                if version:
-                    name = name + ' ' + version
-        return name or ''
-
-    def version(self, pretty=False, best=False):
-        """
-        Return the version of the OS distribution, as a string.
-
-        For details, see :func:`distro.version`.
-        """
-        versions = [
-            self.os_release_attr('version_id'),
-            self.lsb_release_attr('release'),
-            self.distro_release_attr('version_id'),
-            self._parse_distro_release_content(
-                self.os_release_attr('pretty_name')).get('version_id', ''),
-            self._parse_distro_release_content(
-                self.lsb_release_attr('description')).get('version_id', ''),
-            self.uname_attr('release')
-        ]
-        version = ''
-        if best:
-            # This algorithm uses the last version in priority order that has
-            # the best precision. If the versions are not in conflict, that
-            # does not matter; otherwise, using the last one instead of the
-            # first one might be considered a surprise.
-            for v in versions:
-                if v.count(".") > version.count(".") or version == '':
-                    version = v
-        else:
-            for v in versions:
-                if v != '':
-                    version = v
-                    break
-        if pretty and version and self.codename():
-            version = u'{0} ({1})'.format(version, self.codename())
-        return version
-
-    def version_parts(self, best=False):
-        """
-        Return the version of the OS distribution, as a tuple of version
-        numbers.
-
-        For details, see :func:`distro.version_parts`.
-        """
-        version_str = self.version(best=best)
-        if version_str:
-            version_regex = re.compile(r'(\d+)\.?(\d+)?\.?(\d+)?')
-            matches = version_regex.match(version_str)
-            if matches:
-                major, minor, build_number = matches.groups()
-                return major, minor or '', build_number or ''
-        return '', '', ''
-
-    def major_version(self, best=False):
-        """
-        Return the major version number of the current distribution.
-
-        For details, see :func:`distro.major_version`.
-        """
-        return self.version_parts(best)[0]
-
-    def minor_version(self, best=False):
-        """
-        Return the minor version number of the current distribution.
-
-        For details, see :func:`distro.minor_version`.
-        """
-        return self.version_parts(best)[1]
-
-    def build_number(self, best=False):
-        """
-        Return the build number of the current distribution.
-
-        For details, see :func:`distro.build_number`.
-        """
-        return self.version_parts(best)[2]
-
-    def like(self):
-        """
-        Return the IDs of distributions that are like the OS distribution.
-
-        For details, see :func:`distro.like`.
-        """
-        return self.os_release_attr('id_like') or ''
-
-    def codename(self):
-        """
-        Return the codename of the OS distribution.
-
-        For details, see :func:`distro.codename`.
-        """
-        return self.os_release_attr('codename') \
-            or self.lsb_release_attr('codename') \
-            or self.distro_release_attr('codename') \
-            or ''
-
-    def info(self, pretty=False, best=False):
-        """
-        Return certain machine-readable information about the OS
-        distribution.
-
-        For details, see :func:`distro.info`.
-        """
-        return dict(
-            id=self.id(),
-            version=self.version(pretty, best),
-            version_parts=dict(
-                major=self.major_version(best),
-                minor=self.minor_version(best),
-                build_number=self.build_number(best)
-            ),
-            like=self.like(),
-            codename=self.codename(),
-        )
-
-    def os_release_info(self):
-        """
-        Return a dictionary containing key-value pairs for the information
-        items from the os-release file data source of the OS distribution.
-
-        For details, see :func:`distro.os_release_info`.
-        """
-        return self._os_release_info
-
-    def lsb_release_info(self):
-        """
-        Return a dictionary containing key-value pairs for the information
-        items from the lsb_release command data source of the OS
-        distribution.
-
-        For details, see :func:`distro.lsb_release_info`.
-        """
-        return self._lsb_release_info
-
-    def distro_release_info(self):
-        """
-        Return a dictionary containing key-value pairs for the information
-        items from the distro release file data source of the OS
-        distribution.
-
-        For details, see :func:`distro.distro_release_info`.
-        """
-        return self._distro_release_info
-
-    def uname_info(self):
-        """
-        Return a dictionary containing key-value pairs for the information
-        items from the uname command data source of the OS distribution.
-
-        For details, see :func:`distro.uname_info`.
-        """
-
-    def os_release_attr(self, attribute):
-        """
-        Return a single named information item from the os-release file data
-        source of the OS distribution.
-
-        For details, see :func:`distro.os_release_attr`.
-        """
-        return self._os_release_info.get(attribute, '')
-
-    def lsb_release_attr(self, attribute):
-        """
-        Return a single named information item from the lsb_release command
-        output data source of the OS distribution.
-
-        For details, see :func:`distro.lsb_release_attr`.
-        """
-        return self._lsb_release_info.get(attribute, '')
-
-    def distro_release_attr(self, attribute):
-        """
-        Return a single named information item from the distro release file
-        data source of the OS distribution.
-
-        For details, see :func:`distro.distro_release_attr`.
-        """
-        return self._distro_release_info.get(attribute, '')
-
-    def uname_attr(self, attribute):
-        """
-        Return a single named information item from the uname command
-        output data source of the OS distribution.
-
-        For details, see :func:`distro.uname_release_attr`.
-        """
-        return self._uname_info.get(attribute, '')
-
-    @cached_property
-    def _os_release_info(self):
-        """
-        Get the information items from the specified os-release file.
-
-        Returns:
-            A dictionary containing all information items.
-        """
-        if os.path.isfile(self.os_release_file):
-            with open(self.os_release_file) as release_file:
-                return self._parse_os_release_content(release_file)
-        return {}
-
-    @staticmethod
-    def _parse_os_release_content(lines):
-        """
-        Parse the lines of an os-release file.
-
-        Parameters:
-
-        * lines: Iterable through the lines in the os-release file.
-                 Each line must be a unicode string or a UTF-8 encoded byte
-                 string.
-
-        Returns:
-            A dictionary containing all information items.
-        """
-        props = {}
-        lexer = shlex.shlex(lines, posix=True)
-        lexer.whitespace_split = True
-
-        # The shlex module defines its `wordchars` variable using literals,
-        # making it dependent on the encoding of the Python source file.
-        # In Python 2.6 and 2.7, the shlex source file is encoded in
-        # 'iso-8859-1', and the `wordchars` variable is defined as a byte
-        # string. This causes a UnicodeDecodeError to be raised when the
-        # parsed content is a unicode object. The following fix resolves that
-        # (... but it should be fixed in shlex...):
-        if sys.version_info[0] == 2 and isinstance(lexer.wordchars, bytes):
-            lexer.wordchars = lexer.wordchars.decode('iso-8859-1')
-
-        tokens = list(lexer)
-        for token in tokens:
-            # At this point, all shell-like parsing has been done (i.e.
-            # comments processed, quotes and backslash escape sequences
-            # processed, multi-line values assembled, trailing newlines
-            # stripped, etc.), so the tokens are now either:
-            # * variable assignments: var=value
-            # * commands or their arguments (not allowed in os-release)
-            if '=' in token:
-                k, v = token.split('=', 1)
-                if isinstance(v, bytes):
-                    v = v.decode('utf-8')
-                props[k.lower()] = v
-                if k == 'VERSION':
-                    # this handles cases in which the codename is in
-                    # the `(CODENAME)` (rhel, centos, fedora) format
-                    # or in the `, CODENAME` format (Ubuntu).
-                    codename = re.search(r'(\(\D+\))|,(\s+)?\D+', v)
-                    if codename:
-                        codename = codename.group()
-                        codename = codename.strip('()')
-                        codename = codename.strip(',')
-                        codename = codename.strip()
-                        # codename appears within paranthese.
-                        props['codename'] = codename
-                    else:
-                        props['codename'] = ''
-            else:
-                # Ignore any tokens that are not variable assignments
-                pass
-        return props
-
-    @cached_property
-    def _lsb_release_info(self):
-        """
-        Get the information items from the lsb_release command output.
-
-        Returns:
-            A dictionary containing all information items.
-        """
-        if not self.include_lsb:
-            return {}
-        with open(os.devnull, 'w') as devnull:
-            try:
-                cmd = ('lsb_release', '-a')
-                stdout = subprocess.check_output(cmd, stderr=devnull)
-            except OSError:  # Command not found
-                return {}
-        content = stdout.decode(sys.getfilesystemencoding()).splitlines()
-        return self._parse_lsb_release_content(content)
-
-    @staticmethod
-    def _parse_lsb_release_content(lines):
-        """
-        Parse the output of the lsb_release command.
-
-        Parameters:
-
-        * lines: Iterable through the lines of the lsb_release output.
-                 Each line must be a unicode string or a UTF-8 encoded byte
-                 string.
-
-        Returns:
-            A dictionary containing all information items.
-        """
-        props = {}
-        for line in lines:
-            kv = line.strip('\n').split(':', 1)
-            if len(kv) != 2:
-                # Ignore lines without colon.
-                continue
-            k, v = kv
-            props.update({k.replace(' ', '_').lower(): v.strip()})
-        return props
-
-    @cached_property
-    def _uname_info(self):
-        with open(os.devnull, 'w') as devnull:
-            try:
-                cmd = ('uname', '-rs')
-                stdout = subprocess.check_output(cmd, stderr=devnull)
-            except OSError:
-                return {}
-        content = stdout.decode(sys.getfilesystemencoding()).splitlines()
-        return self._parse_uname_content(content)
-
-    @staticmethod
-    def _parse_uname_content(lines):
-        props = {}
-        match = re.search(r'^([^\s]+)\s+([\d\.]+)', lines[0].strip())
-        if match:
-            name, version = match.groups()
-
-            # This is to prevent the Linux kernel version from
-            # appearing as the 'best' version on otherwise
-            # identifiable distributions.
-            if name == 'Linux':
-                return {}
-            props['id'] = name.lower()
-            props['name'] = name
-            props['release'] = version
-        return props
-
-    @cached_property
-    def _distro_release_info(self):
-        """
-        Get the information items from the specified distro release file.
-
-        Returns:
-            A dictionary containing all information items.
-        """
-        if self.distro_release_file:
-            # If it was specified, we use it and parse what we can, even if
-            # its file name or content does not match the expected pattern.
-            distro_info = self._parse_distro_release_file(
-                self.distro_release_file)
-            basename = os.path.basename(self.distro_release_file)
-            # The file name pattern for user-specified distro release files
-            # is somewhat more tolerant (compared to when searching for the
-            # file), because we want to use what was specified as best as
-            # possible.
-            match = _DISTRO_RELEASE_BASENAME_PATTERN.match(basename)
-            if match:
-                distro_info['id'] = match.group(1)
-            return distro_info
-        else:
-            try:
-                basenames = os.listdir(_UNIXCONFDIR)
-                # We sort for repeatability in cases where there are multiple
-                # distro specific files; e.g. CentOS, Oracle, Enterprise all
-                # containing `redhat-release` on top of their own.
-                basenames.sort()
-            except OSError:
-                # This may occur when /etc is not readable but we can't be
-                # sure about the *-release files. Check common entries of
-                # /etc for information. If they turn out to not be there the
-                # error is handled in `_parse_distro_release_file()`.
-                basenames = ['SuSE-release',
-                             'arch-release',
-                             'base-release',
-                             'centos-release',
-                             'fedora-release',
-                             'gentoo-release',
-                             'mageia-release',
-                             'mandrake-release',
-                             'mandriva-release',
-                             'mandrivalinux-release',
-                             'manjaro-release',
-                             'oracle-release',
-                             'redhat-release',
-                             'sl-release',
-                             'slackware-version']
-            for basename in basenames:
-                if basename in _DISTRO_RELEASE_IGNORE_BASENAMES:
-                    continue
-                match = _DISTRO_RELEASE_BASENAME_PATTERN.match(basename)
-                if match:
-                    filepath = os.path.join(_UNIXCONFDIR, basename)
-                    distro_info = self._parse_distro_release_file(filepath)
-                    if 'name' in distro_info:
-                        # The name is always present if the pattern matches
-                        self.distro_release_file = filepath
-                        distro_info['id'] = match.group(1)
-                        return distro_info
-            return {}
-
-    def _parse_distro_release_file(self, filepath):
-        """
-        Parse a distro release file.
-
-        Parameters:
-
-        * filepath: Path name of the distro release file.
-
-        Returns:
-            A dictionary containing all information items.
-        """
-        try:
-            with open(filepath) as fp:
-                # Only parse the first line. For instance, on SLES there
-                # are multiple lines. We don't want them...
-                return self._parse_distro_release_content(fp.readline())
-        except (OSError, IOError):
-            # Ignore not being able to read a specific, seemingly version
-            # related file.
-            # See https://github.com/nir0s/distro/issues/162
-            return {}
-
-    @staticmethod
-    def _parse_distro_release_content(line):
-        """
-        Parse a line from a distro release file.
-
-        Parameters:
-        * line: Line from the distro release file. Must be a unicode string
-                or a UTF-8 encoded byte string.
-
-        Returns:
-            A dictionary containing all information items.
-        """
-        if isinstance(line, bytes):
-            line = line.decode('utf-8')
-        matches = _DISTRO_RELEASE_CONTENT_REVERSED_PATTERN.match(
-            line.strip()[::-1])
-        distro_info = {}
-        if matches:
-            # regexp ensures non-None
-            distro_info['name'] = matches.group(3)[::-1]
-            if matches.group(2):
-                distro_info['version_id'] = matches.group(2)[::-1]
-            if matches.group(1):
-                distro_info['codename'] = matches.group(1)[::-1]
-        elif line:
-            distro_info['name'] = line.strip()
-        return distro_info
-
-
-_distro = LinuxDistribution()
-
-
-def main():
-    logger = logging.getLogger(__name__)
-    logger.setLevel(logging.DEBUG)
-    logger.addHandler(logging.StreamHandler(sys.stdout))
-
-    parser = argparse.ArgumentParser(description="OS distro info tool")
-    parser.add_argument(
-        '--json',
-        '-j',
-        help="Output in machine readable format",
-        action="store_true")
-    args = parser.parse_args()
-
-    if args.json:
-        logger.info(json.dumps(info(), indent=4, sort_keys=True))
-    else:
-        logger.info('Name: %s', name(pretty=True))
-        distribution_version = version(pretty=True)
-        logger.info('Version: %s', distribution_version)
-        distribution_codename = codename()
-        logger.info('Codename: %s', distribution_codename)
-
-
-if __name__ == '__main__':
-    main()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__init__.py
deleted file mode 100644
index 0491234..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__init__.py
+++ /dev/null
@@ -1,35 +0,0 @@
-"""
-HTML parsing library based on the `WHATWG HTML specification
-<https://whatwg.org/html>`_. The parser is designed to be compatible with
-existing HTML found in the wild and implements well-defined error recovery that
-is largely compatible with modern desktop web browsers.
-
-Example usage::
-
-    from pip._vendor import html5lib
-    with open("my_document.html", "rb") as f:
-        tree = html5lib.parse(f)
-
-For convenience, this module re-exports the following names:
-
-* :func:`~.html5parser.parse`
-* :func:`~.html5parser.parseFragment`
-* :class:`~.html5parser.HTMLParser`
-* :func:`~.treebuilders.getTreeBuilder`
-* :func:`~.treewalkers.getTreeWalker`
-* :func:`~.serializer.serialize`
-"""
-
-from __future__ import absolute_import, division, unicode_literals
-
-from .html5parser import HTMLParser, parse, parseFragment
-from .treebuilders import getTreeBuilder
-from .treewalkers import getTreeWalker
-from .serializer import serialize
-
-__all__ = ["HTMLParser", "parse", "parseFragment", "getTreeBuilder",
-           "getTreeWalker", "serialize"]
-
-# this has to be at the top level, see how setup.py parses this
-#: Distribution version number.
-__version__ = "1.0.1"
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 5f745b2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_ihatexml.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_ihatexml.cpython-37.pyc
deleted file mode 100644
index 8342445..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_ihatexml.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_inputstream.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_inputstream.cpython-37.pyc
deleted file mode 100644
index 2ae54df..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_inputstream.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_tokenizer.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_tokenizer.cpython-37.pyc
deleted file mode 100644
index cf3f4ca..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_tokenizer.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_utils.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_utils.cpython-37.pyc
deleted file mode 100644
index 734558e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/_utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/constants.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/constants.cpython-37.pyc
deleted file mode 100644
index 43efcea..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/constants.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/html5parser.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/html5parser.cpython-37.pyc
deleted file mode 100644
index 51dd003..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/html5parser.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/serializer.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/serializer.cpython-37.pyc
deleted file mode 100644
index e27c531..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/__pycache__/serializer.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_ihatexml.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_ihatexml.py
deleted file mode 100644
index 4c77717..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_ihatexml.py
+++ /dev/null
@@ -1,288 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-import re
-import warnings
-
-from .constants import DataLossWarning
-
-baseChar = """
-[#x0041-#x005A] | [#x0061-#x007A] | [#x00C0-#x00D6] | [#x00D8-#x00F6] |
-[#x00F8-#x00FF] | [#x0100-#x0131] | [#x0134-#x013E] | [#x0141-#x0148] |
-[#x014A-#x017E] | [#x0180-#x01C3] | [#x01CD-#x01F0] | [#x01F4-#x01F5] |
-[#x01FA-#x0217] | [#x0250-#x02A8] | [#x02BB-#x02C1] | #x0386 |
-[#x0388-#x038A] | #x038C | [#x038E-#x03A1] | [#x03A3-#x03CE] |
-[#x03D0-#x03D6] | #x03DA | #x03DC | #x03DE | #x03E0 | [#x03E2-#x03F3] |
-[#x0401-#x040C] | [#x040E-#x044F] | [#x0451-#x045C] | [#x045E-#x0481] |
-[#x0490-#x04C4] | [#x04C7-#x04C8] | [#x04CB-#x04CC] | [#x04D0-#x04EB] |
-[#x04EE-#x04F5] | [#x04F8-#x04F9] | [#x0531-#x0556] | #x0559 |
-[#x0561-#x0586] | [#x05D0-#x05EA] | [#x05F0-#x05F2] | [#x0621-#x063A] |
-[#x0641-#x064A] | [#x0671-#x06B7] | [#x06BA-#x06BE] | [#x06C0-#x06CE] |
-[#x06D0-#x06D3] | #x06D5 | [#x06E5-#x06E6] | [#x0905-#x0939] | #x093D |
-[#x0958-#x0961] | [#x0985-#x098C] | [#x098F-#x0990] | [#x0993-#x09A8] |
-[#x09AA-#x09B0] | #x09B2 | [#x09B6-#x09B9] | [#x09DC-#x09DD] |
-[#x09DF-#x09E1] | [#x09F0-#x09F1] | [#x0A05-#x0A0A] | [#x0A0F-#x0A10] |
-[#x0A13-#x0A28] | [#x0A2A-#x0A30] | [#x0A32-#x0A33] | [#x0A35-#x0A36] |
-[#x0A38-#x0A39] | [#x0A59-#x0A5C] | #x0A5E | [#x0A72-#x0A74] |
-[#x0A85-#x0A8B] | #x0A8D | [#x0A8F-#x0A91] | [#x0A93-#x0AA8] |
-[#x0AAA-#x0AB0] | [#x0AB2-#x0AB3] | [#x0AB5-#x0AB9] | #x0ABD | #x0AE0 |
-[#x0B05-#x0B0C] | [#x0B0F-#x0B10] | [#x0B13-#x0B28] | [#x0B2A-#x0B30] |
-[#x0B32-#x0B33] | [#x0B36-#x0B39] | #x0B3D | [#x0B5C-#x0B5D] |
-[#x0B5F-#x0B61] | [#x0B85-#x0B8A] | [#x0B8E-#x0B90] | [#x0B92-#x0B95] |
-[#x0B99-#x0B9A] | #x0B9C | [#x0B9E-#x0B9F] | [#x0BA3-#x0BA4] |
-[#x0BA8-#x0BAA] | [#x0BAE-#x0BB5] | [#x0BB7-#x0BB9] | [#x0C05-#x0C0C] |
-[#x0C0E-#x0C10] | [#x0C12-#x0C28] | [#x0C2A-#x0C33] | [#x0C35-#x0C39] |
-[#x0C60-#x0C61] | [#x0C85-#x0C8C] | [#x0C8E-#x0C90] | [#x0C92-#x0CA8] |
-[#x0CAA-#x0CB3] | [#x0CB5-#x0CB9] | #x0CDE | [#x0CE0-#x0CE1] |
-[#x0D05-#x0D0C] | [#x0D0E-#x0D10] | [#x0D12-#x0D28] | [#x0D2A-#x0D39] |
-[#x0D60-#x0D61] | [#x0E01-#x0E2E] | #x0E30 | [#x0E32-#x0E33] |
-[#x0E40-#x0E45] | [#x0E81-#x0E82] | #x0E84 | [#x0E87-#x0E88] | #x0E8A |
-#x0E8D | [#x0E94-#x0E97] | [#x0E99-#x0E9F] | [#x0EA1-#x0EA3] | #x0EA5 |
-#x0EA7 | [#x0EAA-#x0EAB] | [#x0EAD-#x0EAE] | #x0EB0 | [#x0EB2-#x0EB3] |
-#x0EBD | [#x0EC0-#x0EC4] | [#x0F40-#x0F47] | [#x0F49-#x0F69] |
-[#x10A0-#x10C5] | [#x10D0-#x10F6] | #x1100 | [#x1102-#x1103] |
-[#x1105-#x1107] | #x1109 | [#x110B-#x110C] | [#x110E-#x1112] | #x113C |
-#x113E | #x1140 | #x114C | #x114E | #x1150 | [#x1154-#x1155] | #x1159 |
-[#x115F-#x1161] | #x1163 | #x1165 | #x1167 | #x1169 | [#x116D-#x116E] |
-[#x1172-#x1173] | #x1175 | #x119E | #x11A8 | #x11AB | [#x11AE-#x11AF] |
-[#x11B7-#x11B8] | #x11BA | [#x11BC-#x11C2] | #x11EB | #x11F0 | #x11F9 |
-[#x1E00-#x1E9B] | [#x1EA0-#x1EF9] | [#x1F00-#x1F15] | [#x1F18-#x1F1D] |
-[#x1F20-#x1F45] | [#x1F48-#x1F4D] | [#x1F50-#x1F57] | #x1F59 | #x1F5B |
-#x1F5D | [#x1F5F-#x1F7D] | [#x1F80-#x1FB4] | [#x1FB6-#x1FBC] | #x1FBE |
-[#x1FC2-#x1FC4] | [#x1FC6-#x1FCC] | [#x1FD0-#x1FD3] | [#x1FD6-#x1FDB] |
-[#x1FE0-#x1FEC] | [#x1FF2-#x1FF4] | [#x1FF6-#x1FFC] | #x2126 |
-[#x212A-#x212B] | #x212E | [#x2180-#x2182] | [#x3041-#x3094] |
-[#x30A1-#x30FA] | [#x3105-#x312C] | [#xAC00-#xD7A3]"""
-
-ideographic = """[#x4E00-#x9FA5] | #x3007 | [#x3021-#x3029]"""
-
-combiningCharacter = """
-[#x0300-#x0345] | [#x0360-#x0361] | [#x0483-#x0486] | [#x0591-#x05A1] |
-[#x05A3-#x05B9] | [#x05BB-#x05BD] | #x05BF | [#x05C1-#x05C2] | #x05C4 |
-[#x064B-#x0652] | #x0670 | [#x06D6-#x06DC] | [#x06DD-#x06DF] |
-[#x06E0-#x06E4] | [#x06E7-#x06E8] | [#x06EA-#x06ED] | [#x0901-#x0903] |
-#x093C | [#x093E-#x094C] | #x094D | [#x0951-#x0954] | [#x0962-#x0963] |
-[#x0981-#x0983] | #x09BC | #x09BE | #x09BF | [#x09C0-#x09C4] |
-[#x09C7-#x09C8] | [#x09CB-#x09CD] | #x09D7 | [#x09E2-#x09E3] | #x0A02 |
-#x0A3C | #x0A3E | #x0A3F | [#x0A40-#x0A42] | [#x0A47-#x0A48] |
-[#x0A4B-#x0A4D] | [#x0A70-#x0A71] | [#x0A81-#x0A83] | #x0ABC |
-[#x0ABE-#x0AC5] | [#x0AC7-#x0AC9] | [#x0ACB-#x0ACD] | [#x0B01-#x0B03] |
-#x0B3C | [#x0B3E-#x0B43] | [#x0B47-#x0B48] | [#x0B4B-#x0B4D] |
-[#x0B56-#x0B57] | [#x0B82-#x0B83] | [#x0BBE-#x0BC2] | [#x0BC6-#x0BC8] |
-[#x0BCA-#x0BCD] | #x0BD7 | [#x0C01-#x0C03] | [#x0C3E-#x0C44] |
-[#x0C46-#x0C48] | [#x0C4A-#x0C4D] | [#x0C55-#x0C56] | [#x0C82-#x0C83] |
-[#x0CBE-#x0CC4] | [#x0CC6-#x0CC8] | [#x0CCA-#x0CCD] | [#x0CD5-#x0CD6] |
-[#x0D02-#x0D03] | [#x0D3E-#x0D43] | [#x0D46-#x0D48] | [#x0D4A-#x0D4D] |
-#x0D57 | #x0E31 | [#x0E34-#x0E3A] | [#x0E47-#x0E4E] | #x0EB1 |
-[#x0EB4-#x0EB9] | [#x0EBB-#x0EBC] | [#x0EC8-#x0ECD] | [#x0F18-#x0F19] |
-#x0F35 | #x0F37 | #x0F39 | #x0F3E | #x0F3F | [#x0F71-#x0F84] |
-[#x0F86-#x0F8B] | [#x0F90-#x0F95] | #x0F97 | [#x0F99-#x0FAD] |
-[#x0FB1-#x0FB7] | #x0FB9 | [#x20D0-#x20DC] | #x20E1 | [#x302A-#x302F] |
-#x3099 | #x309A"""
-
-digit = """
-[#x0030-#x0039] | [#x0660-#x0669] | [#x06F0-#x06F9] | [#x0966-#x096F] |
-[#x09E6-#x09EF] | [#x0A66-#x0A6F] | [#x0AE6-#x0AEF] | [#x0B66-#x0B6F] |
-[#x0BE7-#x0BEF] | [#x0C66-#x0C6F] | [#x0CE6-#x0CEF] | [#x0D66-#x0D6F] |
-[#x0E50-#x0E59] | [#x0ED0-#x0ED9] | [#x0F20-#x0F29]"""
-
-extender = """
-#x00B7 | #x02D0 | #x02D1 | #x0387 | #x0640 | #x0E46 | #x0EC6 | #x3005 |
-#[#x3031-#x3035] | [#x309D-#x309E] | [#x30FC-#x30FE]"""
-
-letter = " | ".join([baseChar, ideographic])
-
-# Without the
-name = " | ".join([letter, digit, ".", "-", "_", combiningCharacter,
-                   extender])
-nameFirst = " | ".join([letter, "_"])
-
-reChar = re.compile(r"#x([\d|A-F]{4,4})")
-reCharRange = re.compile(r"\[#x([\d|A-F]{4,4})-#x([\d|A-F]{4,4})\]")
-
-
-def charStringToList(chars):
-    charRanges = [item.strip() for item in chars.split(" | ")]
-    rv = []
-    for item in charRanges:
-        foundMatch = False
-        for regexp in (reChar, reCharRange):
-            match = regexp.match(item)
-            if match is not None:
-                rv.append([hexToInt(item) for item in match.groups()])
-                if len(rv[-1]) == 1:
-                    rv[-1] = rv[-1] * 2
-                foundMatch = True
-                break
-        if not foundMatch:
-            assert len(item) == 1
-
-            rv.append([ord(item)] * 2)
-    rv = normaliseCharList(rv)
-    return rv
-
-
-def normaliseCharList(charList):
-    charList = sorted(charList)
-    for item in charList:
-        assert item[1] >= item[0]
-    rv = []
-    i = 0
-    while i < len(charList):
-        j = 1
-        rv.append(charList[i])
-        while i + j < len(charList) and charList[i + j][0] <= rv[-1][1] + 1:
-            rv[-1][1] = charList[i + j][1]
-            j += 1
-        i += j
-    return rv
-
-# We don't really support characters above the BMP :(
-max_unicode = int("FFFF", 16)
-
-
-def missingRanges(charList):
-    rv = []
-    if charList[0] != 0:
-        rv.append([0, charList[0][0] - 1])
-    for i, item in enumerate(charList[:-1]):
-        rv.append([item[1] + 1, charList[i + 1][0] - 1])
-    if charList[-1][1] != max_unicode:
-        rv.append([charList[-1][1] + 1, max_unicode])
-    return rv
-
-
-def listToRegexpStr(charList):
-    rv = []
-    for item in charList:
-        if item[0] == item[1]:
-            rv.append(escapeRegexp(chr(item[0])))
-        else:
-            rv.append(escapeRegexp(chr(item[0])) + "-" +
-                      escapeRegexp(chr(item[1])))
-    return "[%s]" % "".join(rv)
-
-
-def hexToInt(hex_str):
-    return int(hex_str, 16)
-
-
-def escapeRegexp(string):
-    specialCharacters = (".", "^", "$", "*", "+", "?", "{", "}",
-                         "[", "]", "|", "(", ")", "-")
-    for char in specialCharacters:
-        string = string.replace(char, "\\" + char)
-
-    return string
-
-# output from the above
-nonXmlNameBMPRegexp = re.compile('[\x00-,/:-@\\[-\\^`\\{-\xb6\xb8-\xbf\xd7\xf7\u0132-\u0133\u013f-\u0140\u0149\u017f\u01c4-\u01cc\u01f1-\u01f3\u01f6-\u01f9\u0218-\u024f\u02a9-\u02ba\u02c2-\u02cf\u02d2-\u02ff\u0346-\u035f\u0362-\u0385\u038b\u038d\u03a2\u03cf\u03d7-\u03d9\u03db\u03dd\u03df\u03e1\u03f4-\u0400\u040d\u0450\u045d\u0482\u0487-\u048f\u04c5-\u04c6\u04c9-\u04ca\u04cd-\u04cf\u04ec-\u04ed\u04f6-\u04f7\u04fa-\u0530\u0557-\u0558\u055a-\u0560\u0587-\u0590\u05a2\u05ba\u05be\u05c0\u05c3\u05c5-\u05cf\u05eb-\u05ef\u05f3-\u0620\u063b-\u063f\u0653-\u065f\u066a-\u066f\u06b8-\u06b9\u06bf\u06cf\u06d4\u06e9\u06ee-\u06ef\u06fa-\u0900\u0904\u093a-\u093b\u094e-\u0950\u0955-\u0957\u0964-\u0965\u0970-\u0980\u0984\u098d-\u098e\u0991-\u0992\u09a9\u09b1\u09b3-\u09b5\u09ba-\u09bb\u09bd\u09c5-\u09c6\u09c9-\u09ca\u09ce-\u09d6\u09d8-\u09db\u09de\u09e4-\u09e5\u09f2-\u0a01\u0a03-\u0a04\u0a0b-\u0a0e\u0a11-\u0a12\u0a29\u0a31\u0a34\u0a37\u0a3a-\u0a3b\u0a3d\u0a43-\u0a46\u0a49-\u0a4a\u0a4e-\u0a58\u0a5d\u0a5f-\u0a65\u0a75-\u0a80\u0a84\u0a8c\u0a8e\u0a92\u0aa9\u0ab1\u0ab4\u0aba-\u0abb\u0ac6\u0aca\u0ace-\u0adf\u0ae1-\u0ae5\u0af0-\u0b00\u0b04\u0b0d-\u0b0e\u0b11-\u0b12\u0b29\u0b31\u0b34-\u0b35\u0b3a-\u0b3b\u0b44-\u0b46\u0b49-\u0b4a\u0b4e-\u0b55\u0b58-\u0b5b\u0b5e\u0b62-\u0b65\u0b70-\u0b81\u0b84\u0b8b-\u0b8d\u0b91\u0b96-\u0b98\u0b9b\u0b9d\u0ba0-\u0ba2\u0ba5-\u0ba7\u0bab-\u0bad\u0bb6\u0bba-\u0bbd\u0bc3-\u0bc5\u0bc9\u0bce-\u0bd6\u0bd8-\u0be6\u0bf0-\u0c00\u0c04\u0c0d\u0c11\u0c29\u0c34\u0c3a-\u0c3d\u0c45\u0c49\u0c4e-\u0c54\u0c57-\u0c5f\u0c62-\u0c65\u0c70-\u0c81\u0c84\u0c8d\u0c91\u0ca9\u0cb4\u0cba-\u0cbd\u0cc5\u0cc9\u0cce-\u0cd4\u0cd7-\u0cdd\u0cdf\u0ce2-\u0ce5\u0cf0-\u0d01\u0d04\u0d0d\u0d11\u0d29\u0d3a-\u0d3d\u0d44-\u0d45\u0d49\u0d4e-\u0d56\u0d58-\u0d5f\u0d62-\u0d65\u0d70-\u0e00\u0e2f\u0e3b-\u0e3f\u0e4f\u0e5a-\u0e80\u0e83\u0e85-\u0e86\u0e89\u0e8b-\u0e8c\u0e8e-\u0e93\u0e98\u0ea0\u0ea4\u0ea6\u0ea8-\u0ea9\u0eac\u0eaf\u0eba\u0ebe-\u0ebf\u0ec5\u0ec7\u0ece-\u0ecf\u0eda-\u0f17\u0f1a-\u0f1f\u0f2a-\u0f34\u0f36\u0f38\u0f3a-\u0f3d\u0f48\u0f6a-\u0f70\u0f85\u0f8c-\u0f8f\u0f96\u0f98\u0fae-\u0fb0\u0fb8\u0fba-\u109f\u10c6-\u10cf\u10f7-\u10ff\u1101\u1104\u1108\u110a\u110d\u1113-\u113b\u113d\u113f\u1141-\u114b\u114d\u114f\u1151-\u1153\u1156-\u1158\u115a-\u115e\u1162\u1164\u1166\u1168\u116a-\u116c\u116f-\u1171\u1174\u1176-\u119d\u119f-\u11a7\u11a9-\u11aa\u11ac-\u11ad\u11b0-\u11b6\u11b9\u11bb\u11c3-\u11ea\u11ec-\u11ef\u11f1-\u11f8\u11fa-\u1dff\u1e9c-\u1e9f\u1efa-\u1eff\u1f16-\u1f17\u1f1e-\u1f1f\u1f46-\u1f47\u1f4e-\u1f4f\u1f58\u1f5a\u1f5c\u1f5e\u1f7e-\u1f7f\u1fb5\u1fbd\u1fbf-\u1fc1\u1fc5\u1fcd-\u1fcf\u1fd4-\u1fd5\u1fdc-\u1fdf\u1fed-\u1ff1\u1ff5\u1ffd-\u20cf\u20dd-\u20e0\u20e2-\u2125\u2127-\u2129\u212c-\u212d\u212f-\u217f\u2183-\u3004\u3006\u3008-\u3020\u3030\u3036-\u3040\u3095-\u3098\u309b-\u309c\u309f-\u30a0\u30fb\u30ff-\u3104\u312d-\u4dff\u9fa6-\uabff\ud7a4-\uffff]')  # noqa
-
-nonXmlNameFirstBMPRegexp = re.compile('[\x00-@\\[-\\^`\\{-\xbf\xd7\xf7\u0132-\u0133\u013f-\u0140\u0149\u017f\u01c4-\u01cc\u01f1-\u01f3\u01f6-\u01f9\u0218-\u024f\u02a9-\u02ba\u02c2-\u0385\u0387\u038b\u038d\u03a2\u03cf\u03d7-\u03d9\u03db\u03dd\u03df\u03e1\u03f4-\u0400\u040d\u0450\u045d\u0482-\u048f\u04c5-\u04c6\u04c9-\u04ca\u04cd-\u04cf\u04ec-\u04ed\u04f6-\u04f7\u04fa-\u0530\u0557-\u0558\u055a-\u0560\u0587-\u05cf\u05eb-\u05ef\u05f3-\u0620\u063b-\u0640\u064b-\u0670\u06b8-\u06b9\u06bf\u06cf\u06d4\u06d6-\u06e4\u06e7-\u0904\u093a-\u093c\u093e-\u0957\u0962-\u0984\u098d-\u098e\u0991-\u0992\u09a9\u09b1\u09b3-\u09b5\u09ba-\u09db\u09de\u09e2-\u09ef\u09f2-\u0a04\u0a0b-\u0a0e\u0a11-\u0a12\u0a29\u0a31\u0a34\u0a37\u0a3a-\u0a58\u0a5d\u0a5f-\u0a71\u0a75-\u0a84\u0a8c\u0a8e\u0a92\u0aa9\u0ab1\u0ab4\u0aba-\u0abc\u0abe-\u0adf\u0ae1-\u0b04\u0b0d-\u0b0e\u0b11-\u0b12\u0b29\u0b31\u0b34-\u0b35\u0b3a-\u0b3c\u0b3e-\u0b5b\u0b5e\u0b62-\u0b84\u0b8b-\u0b8d\u0b91\u0b96-\u0b98\u0b9b\u0b9d\u0ba0-\u0ba2\u0ba5-\u0ba7\u0bab-\u0bad\u0bb6\u0bba-\u0c04\u0c0d\u0c11\u0c29\u0c34\u0c3a-\u0c5f\u0c62-\u0c84\u0c8d\u0c91\u0ca9\u0cb4\u0cba-\u0cdd\u0cdf\u0ce2-\u0d04\u0d0d\u0d11\u0d29\u0d3a-\u0d5f\u0d62-\u0e00\u0e2f\u0e31\u0e34-\u0e3f\u0e46-\u0e80\u0e83\u0e85-\u0e86\u0e89\u0e8b-\u0e8c\u0e8e-\u0e93\u0e98\u0ea0\u0ea4\u0ea6\u0ea8-\u0ea9\u0eac\u0eaf\u0eb1\u0eb4-\u0ebc\u0ebe-\u0ebf\u0ec5-\u0f3f\u0f48\u0f6a-\u109f\u10c6-\u10cf\u10f7-\u10ff\u1101\u1104\u1108\u110a\u110d\u1113-\u113b\u113d\u113f\u1141-\u114b\u114d\u114f\u1151-\u1153\u1156-\u1158\u115a-\u115e\u1162\u1164\u1166\u1168\u116a-\u116c\u116f-\u1171\u1174\u1176-\u119d\u119f-\u11a7\u11a9-\u11aa\u11ac-\u11ad\u11b0-\u11b6\u11b9\u11bb\u11c3-\u11ea\u11ec-\u11ef\u11f1-\u11f8\u11fa-\u1dff\u1e9c-\u1e9f\u1efa-\u1eff\u1f16-\u1f17\u1f1e-\u1f1f\u1f46-\u1f47\u1f4e-\u1f4f\u1f58\u1f5a\u1f5c\u1f5e\u1f7e-\u1f7f\u1fb5\u1fbd\u1fbf-\u1fc1\u1fc5\u1fcd-\u1fcf\u1fd4-\u1fd5\u1fdc-\u1fdf\u1fed-\u1ff1\u1ff5\u1ffd-\u2125\u2127-\u2129\u212c-\u212d\u212f-\u217f\u2183-\u3006\u3008-\u3020\u302a-\u3040\u3095-\u30a0\u30fb-\u3104\u312d-\u4dff\u9fa6-\uabff\ud7a4-\uffff]')  # noqa
-
-# Simpler things
-nonPubidCharRegexp = re.compile("[^\x20\x0D\x0Aa-zA-Z0-9\\-'()+,./:=?;!*#@$_%]")
-
-
-class InfosetFilter(object):
-    replacementRegexp = re.compile(r"U[\dA-F]{5,5}")
-
-    def __init__(self,
-                 dropXmlnsLocalName=False,
-                 dropXmlnsAttrNs=False,
-                 preventDoubleDashComments=False,
-                 preventDashAtCommentEnd=False,
-                 replaceFormFeedCharacters=True,
-                 preventSingleQuotePubid=False):
-
-        self.dropXmlnsLocalName = dropXmlnsLocalName
-        self.dropXmlnsAttrNs = dropXmlnsAttrNs
-
-        self.preventDoubleDashComments = preventDoubleDashComments
-        self.preventDashAtCommentEnd = preventDashAtCommentEnd
-
-        self.replaceFormFeedCharacters = replaceFormFeedCharacters
-
-        self.preventSingleQuotePubid = preventSingleQuotePubid
-
-        self.replaceCache = {}
-
-    def coerceAttribute(self, name, namespace=None):
-        if self.dropXmlnsLocalName and name.startswith("xmlns:"):
-            warnings.warn("Attributes cannot begin with xmlns", DataLossWarning)
-            return None
-        elif (self.dropXmlnsAttrNs and
-              namespace == "http://www.w3.org/2000/xmlns/"):
-            warnings.warn("Attributes cannot be in the xml namespace", DataLossWarning)
-            return None
-        else:
-            return self.toXmlName(name)
-
-    def coerceElement(self, name):
-        return self.toXmlName(name)
-
-    def coerceComment(self, data):
-        if self.preventDoubleDashComments:
-            while "--" in data:
-                warnings.warn("Comments cannot contain adjacent dashes", DataLossWarning)
-                data = data.replace("--", "- -")
-            if data.endswith("-"):
-                warnings.warn("Comments cannot end in a dash", DataLossWarning)
-                data += " "
-        return data
-
-    def coerceCharacters(self, data):
-        if self.replaceFormFeedCharacters:
-            for _ in range(data.count("\x0C")):
-                warnings.warn("Text cannot contain U+000C", DataLossWarning)
-            data = data.replace("\x0C", " ")
-        # Other non-xml characters
-        return data
-
-    def coercePubid(self, data):
-        dataOutput = data
-        for char in nonPubidCharRegexp.findall(data):
-            warnings.warn("Coercing non-XML pubid", DataLossWarning)
-            replacement = self.getReplacementCharacter(char)
-            dataOutput = dataOutput.replace(char, replacement)
-        if self.preventSingleQuotePubid and dataOutput.find("'") >= 0:
-            warnings.warn("Pubid cannot contain single quote", DataLossWarning)
-            dataOutput = dataOutput.replace("'", self.getReplacementCharacter("'"))
-        return dataOutput
-
-    def toXmlName(self, name):
-        nameFirst = name[0]
-        nameRest = name[1:]
-        m = nonXmlNameFirstBMPRegexp.match(nameFirst)
-        if m:
-            warnings.warn("Coercing non-XML name", DataLossWarning)
-            nameFirstOutput = self.getReplacementCharacter(nameFirst)
-        else:
-            nameFirstOutput = nameFirst
-
-        nameRestOutput = nameRest
-        replaceChars = set(nonXmlNameBMPRegexp.findall(nameRest))
-        for char in replaceChars:
-            warnings.warn("Coercing non-XML name", DataLossWarning)
-            replacement = self.getReplacementCharacter(char)
-            nameRestOutput = nameRestOutput.replace(char, replacement)
-        return nameFirstOutput + nameRestOutput
-
-    def getReplacementCharacter(self, char):
-        if char in self.replaceCache:
-            replacement = self.replaceCache[char]
-        else:
-            replacement = self.escapeChar(char)
-        return replacement
-
-    def fromXmlName(self, name):
-        for item in set(self.replacementRegexp.findall(name)):
-            name = name.replace(item, self.unescapeChar(item))
-        return name
-
-    def escapeChar(self, char):
-        replacement = "U%05X" % ord(char)
-        self.replaceCache[char] = replacement
-        return replacement
-
-    def unescapeChar(self, charcode):
-        return chr(int(charcode[1:], 16))
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_inputstream.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_inputstream.py
deleted file mode 100644
index a65e55f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_inputstream.py
+++ /dev/null
@@ -1,923 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from pip._vendor.six import text_type, binary_type
-from pip._vendor.six.moves import http_client, urllib
-
-import codecs
-import re
-
-from pip._vendor import webencodings
-
-from .constants import EOF, spaceCharacters, asciiLetters, asciiUppercase
-from .constants import _ReparseException
-from . import _utils
-
-from io import StringIO
-
-try:
-    from io import BytesIO
-except ImportError:
-    BytesIO = StringIO
-
-# Non-unicode versions of constants for use in the pre-parser
-spaceCharactersBytes = frozenset([item.encode("ascii") for item in spaceCharacters])
-asciiLettersBytes = frozenset([item.encode("ascii") for item in asciiLetters])
-asciiUppercaseBytes = frozenset([item.encode("ascii") for item in asciiUppercase])
-spacesAngleBrackets = spaceCharactersBytes | frozenset([b">", b"<"])
-
-
-invalid_unicode_no_surrogate = "[\u0001-\u0008\u000B\u000E-\u001F\u007F-\u009F\uFDD0-\uFDEF\uFFFE\uFFFF\U0001FFFE\U0001FFFF\U0002FFFE\U0002FFFF\U0003FFFE\U0003FFFF\U0004FFFE\U0004FFFF\U0005FFFE\U0005FFFF\U0006FFFE\U0006FFFF\U0007FFFE\U0007FFFF\U0008FFFE\U0008FFFF\U0009FFFE\U0009FFFF\U000AFFFE\U000AFFFF\U000BFFFE\U000BFFFF\U000CFFFE\U000CFFFF\U000DFFFE\U000DFFFF\U000EFFFE\U000EFFFF\U000FFFFE\U000FFFFF\U0010FFFE\U0010FFFF]"  # noqa
-
-if _utils.supports_lone_surrogates:
-    # Use one extra step of indirection and create surrogates with
-    # eval. Not using this indirection would introduce an illegal
-    # unicode literal on platforms not supporting such lone
-    # surrogates.
-    assert invalid_unicode_no_surrogate[-1] == "]" and invalid_unicode_no_surrogate.count("]") == 1
-    invalid_unicode_re = re.compile(invalid_unicode_no_surrogate[:-1] +
-                                    eval('"\\uD800-\\uDFFF"') +  # pylint:disable=eval-used
-                                    "]")
-else:
-    invalid_unicode_re = re.compile(invalid_unicode_no_surrogate)
-
-non_bmp_invalid_codepoints = set([0x1FFFE, 0x1FFFF, 0x2FFFE, 0x2FFFF, 0x3FFFE,
-                                  0x3FFFF, 0x4FFFE, 0x4FFFF, 0x5FFFE, 0x5FFFF,
-                                  0x6FFFE, 0x6FFFF, 0x7FFFE, 0x7FFFF, 0x8FFFE,
-                                  0x8FFFF, 0x9FFFE, 0x9FFFF, 0xAFFFE, 0xAFFFF,
-                                  0xBFFFE, 0xBFFFF, 0xCFFFE, 0xCFFFF, 0xDFFFE,
-                                  0xDFFFF, 0xEFFFE, 0xEFFFF, 0xFFFFE, 0xFFFFF,
-                                  0x10FFFE, 0x10FFFF])
-
-ascii_punctuation_re = re.compile("[\u0009-\u000D\u0020-\u002F\u003A-\u0040\u005C\u005B-\u0060\u007B-\u007E]")
-
-# Cache for charsUntil()
-charsUntilRegEx = {}
-
-
-class BufferedStream(object):
-    """Buffering for streams that do not have buffering of their own
-
-    The buffer is implemented as a list of chunks on the assumption that
-    joining many strings will be slow since it is O(n**2)
-    """
-
-    def __init__(self, stream):
-        self.stream = stream
-        self.buffer = []
-        self.position = [-1, 0]  # chunk number, offset
-
-    def tell(self):
-        pos = 0
-        for chunk in self.buffer[:self.position[0]]:
-            pos += len(chunk)
-        pos += self.position[1]
-        return pos
-
-    def seek(self, pos):
-        assert pos <= self._bufferedBytes()
-        offset = pos
-        i = 0
-        while len(self.buffer[i]) < offset:
-            offset -= len(self.buffer[i])
-            i += 1
-        self.position = [i, offset]
-
-    def read(self, bytes):
-        if not self.buffer:
-            return self._readStream(bytes)
-        elif (self.position[0] == len(self.buffer) and
-              self.position[1] == len(self.buffer[-1])):
-            return self._readStream(bytes)
-        else:
-            return self._readFromBuffer(bytes)
-
-    def _bufferedBytes(self):
-        return sum([len(item) for item in self.buffer])
-
-    def _readStream(self, bytes):
-        data = self.stream.read(bytes)
-        self.buffer.append(data)
-        self.position[0] += 1
-        self.position[1] = len(data)
-        return data
-
-    def _readFromBuffer(self, bytes):
-        remainingBytes = bytes
-        rv = []
-        bufferIndex = self.position[0]
-        bufferOffset = self.position[1]
-        while bufferIndex < len(self.buffer) and remainingBytes != 0:
-            assert remainingBytes > 0
-            bufferedData = self.buffer[bufferIndex]
-
-            if remainingBytes <= len(bufferedData) - bufferOffset:
-                bytesToRead = remainingBytes
-                self.position = [bufferIndex, bufferOffset + bytesToRead]
-            else:
-                bytesToRead = len(bufferedData) - bufferOffset
-                self.position = [bufferIndex, len(bufferedData)]
-                bufferIndex += 1
-            rv.append(bufferedData[bufferOffset:bufferOffset + bytesToRead])
-            remainingBytes -= bytesToRead
-
-            bufferOffset = 0
-
-        if remainingBytes:
-            rv.append(self._readStream(remainingBytes))
-
-        return b"".join(rv)
-
-
-def HTMLInputStream(source, **kwargs):
-    # Work around Python bug #20007: read(0) closes the connection.
-    # http://bugs.python.org/issue20007
-    if (isinstance(source, http_client.HTTPResponse) or
-        # Also check for addinfourl wrapping HTTPResponse
-        (isinstance(source, urllib.response.addbase) and
-         isinstance(source.fp, http_client.HTTPResponse))):
-        isUnicode = False
-    elif hasattr(source, "read"):
-        isUnicode = isinstance(source.read(0), text_type)
-    else:
-        isUnicode = isinstance(source, text_type)
-
-    if isUnicode:
-        encodings = [x for x in kwargs if x.endswith("_encoding")]
-        if encodings:
-            raise TypeError("Cannot set an encoding with a unicode input, set %r" % encodings)
-
-        return HTMLUnicodeInputStream(source, **kwargs)
-    else:
-        return HTMLBinaryInputStream(source, **kwargs)
-
-
-class HTMLUnicodeInputStream(object):
-    """Provides a unicode stream of characters to the HTMLTokenizer.
-
-    This class takes care of character encoding and removing or replacing
-    incorrect byte-sequences and also provides column and line tracking.
-
-    """
-
-    _defaultChunkSize = 10240
-
-    def __init__(self, source):
-        """Initialises the HTMLInputStream.
-
-        HTMLInputStream(source, [encoding]) -> Normalized stream from source
-        for use by html5lib.
-
-        source can be either a file-object, local filename or a string.
-
-        The optional encoding parameter must be a string that indicates
-        the encoding.  If specified, that encoding will be used,
-        regardless of any BOM or later declaration (such as in a meta
-        element)
-
-        """
-
-        if not _utils.supports_lone_surrogates:
-            # Such platforms will have already checked for such
-            # surrogate errors, so no need to do this checking.
-            self.reportCharacterErrors = None
-        elif len("\U0010FFFF") == 1:
-            self.reportCharacterErrors = self.characterErrorsUCS4
-        else:
-            self.reportCharacterErrors = self.characterErrorsUCS2
-
-        # List of where new lines occur
-        self.newLines = [0]
-
-        self.charEncoding = (lookupEncoding("utf-8"), "certain")
-        self.dataStream = self.openStream(source)
-
-        self.reset()
-
-    def reset(self):
-        self.chunk = ""
-        self.chunkSize = 0
-        self.chunkOffset = 0
-        self.errors = []
-
-        # number of (complete) lines in previous chunks
-        self.prevNumLines = 0
-        # number of columns in the last line of the previous chunk
-        self.prevNumCols = 0
-
-        # Deal with CR LF and surrogates split over chunk boundaries
-        self._bufferedCharacter = None
-
-    def openStream(self, source):
-        """Produces a file object from source.
-
-        source can be either a file object, local filename or a string.
-
-        """
-        # Already a file object
-        if hasattr(source, 'read'):
-            stream = source
-        else:
-            stream = StringIO(source)
-
-        return stream
-
-    def _position(self, offset):
-        chunk = self.chunk
-        nLines = chunk.count('\n', 0, offset)
-        positionLine = self.prevNumLines + nLines
-        lastLinePos = chunk.rfind('\n', 0, offset)
-        if lastLinePos == -1:
-            positionColumn = self.prevNumCols + offset
-        else:
-            positionColumn = offset - (lastLinePos + 1)
-        return (positionLine, positionColumn)
-
-    def position(self):
-        """Returns (line, col) of the current position in the stream."""
-        line, col = self._position(self.chunkOffset)
-        return (line + 1, col)
-
-    def char(self):
-        """ Read one character from the stream or queue if available. Return
-            EOF when EOF is reached.
-        """
-        # Read a new chunk from the input stream if necessary
-        if self.chunkOffset >= self.chunkSize:
-            if not self.readChunk():
-                return EOF
-
-        chunkOffset = self.chunkOffset
-        char = self.chunk[chunkOffset]
-        self.chunkOffset = chunkOffset + 1
-
-        return char
-
-    def readChunk(self, chunkSize=None):
-        if chunkSize is None:
-            chunkSize = self._defaultChunkSize
-
-        self.prevNumLines, self.prevNumCols = self._position(self.chunkSize)
-
-        self.chunk = ""
-        self.chunkSize = 0
-        self.chunkOffset = 0
-
-        data = self.dataStream.read(chunkSize)
-
-        # Deal with CR LF and surrogates broken across chunks
-        if self._bufferedCharacter:
-            data = self._bufferedCharacter + data
-            self._bufferedCharacter = None
-        elif not data:
-            # We have no more data, bye-bye stream
-            return False
-
-        if len(data) > 1:
-            lastv = ord(data[-1])
-            if lastv == 0x0D or 0xD800 <= lastv <= 0xDBFF:
-                self._bufferedCharacter = data[-1]
-                data = data[:-1]
-
-        if self.reportCharacterErrors:
-            self.reportCharacterErrors(data)
-
-        # Replace invalid characters
-        data = data.replace("\r\n", "\n")
-        data = data.replace("\r", "\n")
-
-        self.chunk = data
-        self.chunkSize = len(data)
-
-        return True
-
-    def characterErrorsUCS4(self, data):
-        for _ in range(len(invalid_unicode_re.findall(data))):
-            self.errors.append("invalid-codepoint")
-
-    def characterErrorsUCS2(self, data):
-        # Someone picked the wrong compile option
-        # You lose
-        skip = False
-        for match in invalid_unicode_re.finditer(data):
-            if skip:
-                continue
-            codepoint = ord(match.group())
-            pos = match.start()
-            # Pretty sure there should be endianness issues here
-            if _utils.isSurrogatePair(data[pos:pos + 2]):
-                # We have a surrogate pair!
-                char_val = _utils.surrogatePairToCodepoint(data[pos:pos + 2])
-                if char_val in non_bmp_invalid_codepoints:
-                    self.errors.append("invalid-codepoint")
-                skip = True
-            elif (codepoint >= 0xD800 and codepoint <= 0xDFFF and
-                  pos == len(data) - 1):
-                self.errors.append("invalid-codepoint")
-            else:
-                skip = False
-                self.errors.append("invalid-codepoint")
-
-    def charsUntil(self, characters, opposite=False):
-        """ Returns a string of characters from the stream up to but not
-        including any character in 'characters' or EOF. 'characters' must be
-        a container that supports the 'in' method and iteration over its
-        characters.
-        """
-
-        # Use a cache of regexps to find the required characters
-        try:
-            chars = charsUntilRegEx[(characters, opposite)]
-        except KeyError:
-            if __debug__:
-                for c in characters:
-                    assert(ord(c) < 128)
-            regex = "".join(["\\x%02x" % ord(c) for c in characters])
-            if not opposite:
-                regex = "^%s" % regex
-            chars = charsUntilRegEx[(characters, opposite)] = re.compile("[%s]+" % regex)
-
-        rv = []
-
-        while True:
-            # Find the longest matching prefix
-            m = chars.match(self.chunk, self.chunkOffset)
-            if m is None:
-                # If nothing matched, and it wasn't because we ran out of chunk,
-                # then stop
-                if self.chunkOffset != self.chunkSize:
-                    break
-            else:
-                end = m.end()
-                # If not the whole chunk matched, return everything
-                # up to the part that didn't match
-                if end != self.chunkSize:
-                    rv.append(self.chunk[self.chunkOffset:end])
-                    self.chunkOffset = end
-                    break
-            # If the whole remainder of the chunk matched,
-            # use it all and read the next chunk
-            rv.append(self.chunk[self.chunkOffset:])
-            if not self.readChunk():
-                # Reached EOF
-                break
-
-        r = "".join(rv)
-        return r
-
-    def unget(self, char):
-        # Only one character is allowed to be ungotten at once - it must
-        # be consumed again before any further call to unget
-        if char is not None:
-            if self.chunkOffset == 0:
-                # unget is called quite rarely, so it's a good idea to do
-                # more work here if it saves a bit of work in the frequently
-                # called char and charsUntil.
-                # So, just prepend the ungotten character onto the current
-                # chunk:
-                self.chunk = char + self.chunk
-                self.chunkSize += 1
-            else:
-                self.chunkOffset -= 1
-                assert self.chunk[self.chunkOffset] == char
-
-
-class HTMLBinaryInputStream(HTMLUnicodeInputStream):
-    """Provides a unicode stream of characters to the HTMLTokenizer.
-
-    This class takes care of character encoding and removing or replacing
-    incorrect byte-sequences and also provides column and line tracking.
-
-    """
-
-    def __init__(self, source, override_encoding=None, transport_encoding=None,
-                 same_origin_parent_encoding=None, likely_encoding=None,
-                 default_encoding="windows-1252", useChardet=True):
-        """Initialises the HTMLInputStream.
-
-        HTMLInputStream(source, [encoding]) -> Normalized stream from source
-        for use by html5lib.
-
-        source can be either a file-object, local filename or a string.
-
-        The optional encoding parameter must be a string that indicates
-        the encoding.  If specified, that encoding will be used,
-        regardless of any BOM or later declaration (such as in a meta
-        element)
-
-        """
-        # Raw Stream - for unicode objects this will encode to utf-8 and set
-        #              self.charEncoding as appropriate
-        self.rawStream = self.openStream(source)
-
-        HTMLUnicodeInputStream.__init__(self, self.rawStream)
-
-        # Encoding Information
-        # Number of bytes to use when looking for a meta element with
-        # encoding information
-        self.numBytesMeta = 1024
-        # Number of bytes to use when using detecting encoding using chardet
-        self.numBytesChardet = 100
-        # Things from args
-        self.override_encoding = override_encoding
-        self.transport_encoding = transport_encoding
-        self.same_origin_parent_encoding = same_origin_parent_encoding
-        self.likely_encoding = likely_encoding
-        self.default_encoding = default_encoding
-
-        # Determine encoding
-        self.charEncoding = self.determineEncoding(useChardet)
-        assert self.charEncoding[0] is not None
-
-        # Call superclass
-        self.reset()
-
-    def reset(self):
-        self.dataStream = self.charEncoding[0].codec_info.streamreader(self.rawStream, 'replace')
-        HTMLUnicodeInputStream.reset(self)
-
-    def openStream(self, source):
-        """Produces a file object from source.
-
-        source can be either a file object, local filename or a string.
-
-        """
-        # Already a file object
-        if hasattr(source, 'read'):
-            stream = source
-        else:
-            stream = BytesIO(source)
-
-        try:
-            stream.seek(stream.tell())
-        except:  # pylint:disable=bare-except
-            stream = BufferedStream(stream)
-
-        return stream
-
-    def determineEncoding(self, chardet=True):
-        # BOMs take precedence over everything
-        # This will also read past the BOM if present
-        charEncoding = self.detectBOM(), "certain"
-        if charEncoding[0] is not None:
-            return charEncoding
-
-        # If we've been overriden, we've been overriden
-        charEncoding = lookupEncoding(self.override_encoding), "certain"
-        if charEncoding[0] is not None:
-            return charEncoding
-
-        # Now check the transport layer
-        charEncoding = lookupEncoding(self.transport_encoding), "certain"
-        if charEncoding[0] is not None:
-            return charEncoding
-
-        # Look for meta elements with encoding information
-        charEncoding = self.detectEncodingMeta(), "tentative"
-        if charEncoding[0] is not None:
-            return charEncoding
-
-        # Parent document encoding
-        charEncoding = lookupEncoding(self.same_origin_parent_encoding), "tentative"
-        if charEncoding[0] is not None and not charEncoding[0].name.startswith("utf-16"):
-            return charEncoding
-
-        # "likely" encoding
-        charEncoding = lookupEncoding(self.likely_encoding), "tentative"
-        if charEncoding[0] is not None:
-            return charEncoding
-
-        # Guess with chardet, if available
-        if chardet:
-            try:
-                from pip._vendor.chardet.universaldetector import UniversalDetector
-            except ImportError:
-                pass
-            else:
-                buffers = []
-                detector = UniversalDetector()
-                while not detector.done:
-                    buffer = self.rawStream.read(self.numBytesChardet)
-                    assert isinstance(buffer, bytes)
-                    if not buffer:
-                        break
-                    buffers.append(buffer)
-                    detector.feed(buffer)
-                detector.close()
-                encoding = lookupEncoding(detector.result['encoding'])
-                self.rawStream.seek(0)
-                if encoding is not None:
-                    return encoding, "tentative"
-
-        # Try the default encoding
-        charEncoding = lookupEncoding(self.default_encoding), "tentative"
-        if charEncoding[0] is not None:
-            return charEncoding
-
-        # Fallback to html5lib's default if even that hasn't worked
-        return lookupEncoding("windows-1252"), "tentative"
-
-    def changeEncoding(self, newEncoding):
-        assert self.charEncoding[1] != "certain"
-        newEncoding = lookupEncoding(newEncoding)
-        if newEncoding is None:
-            return
-        if newEncoding.name in ("utf-16be", "utf-16le"):
-            newEncoding = lookupEncoding("utf-8")
-            assert newEncoding is not None
-        elif newEncoding == self.charEncoding[0]:
-            self.charEncoding = (self.charEncoding[0], "certain")
-        else:
-            self.rawStream.seek(0)
-            self.charEncoding = (newEncoding, "certain")
-            self.reset()
-            raise _ReparseException("Encoding changed from %s to %s" % (self.charEncoding[0], newEncoding))
-
-    def detectBOM(self):
-        """Attempts to detect at BOM at the start of the stream. If
-        an encoding can be determined from the BOM return the name of the
-        encoding otherwise return None"""
-        bomDict = {
-            codecs.BOM_UTF8: 'utf-8',
-            codecs.BOM_UTF16_LE: 'utf-16le', codecs.BOM_UTF16_BE: 'utf-16be',
-            codecs.BOM_UTF32_LE: 'utf-32le', codecs.BOM_UTF32_BE: 'utf-32be'
-        }
-
-        # Go to beginning of file and read in 4 bytes
-        string = self.rawStream.read(4)
-        assert isinstance(string, bytes)
-
-        # Try detecting the BOM using bytes from the string
-        encoding = bomDict.get(string[:3])         # UTF-8
-        seek = 3
-        if not encoding:
-            # Need to detect UTF-32 before UTF-16
-            encoding = bomDict.get(string)         # UTF-32
-            seek = 4
-            if not encoding:
-                encoding = bomDict.get(string[:2])  # UTF-16
-                seek = 2
-
-        # Set the read position past the BOM if one was found, otherwise
-        # set it to the start of the stream
-        if encoding:
-            self.rawStream.seek(seek)
-            return lookupEncoding(encoding)
-        else:
-            self.rawStream.seek(0)
-            return None
-
-    def detectEncodingMeta(self):
-        """Report the encoding declared by the meta element
-        """
-        buffer = self.rawStream.read(self.numBytesMeta)
-        assert isinstance(buffer, bytes)
-        parser = EncodingParser(buffer)
-        self.rawStream.seek(0)
-        encoding = parser.getEncoding()
-
-        if encoding is not None and encoding.name in ("utf-16be", "utf-16le"):
-            encoding = lookupEncoding("utf-8")
-
-        return encoding
-
-
-class EncodingBytes(bytes):
-    """String-like object with an associated position and various extra methods
-    If the position is ever greater than the string length then an exception is
-    raised"""
-    def __new__(self, value):
-        assert isinstance(value, bytes)
-        return bytes.__new__(self, value.lower())
-
-    def __init__(self, value):
-        # pylint:disable=unused-argument
-        self._position = -1
-
-    def __iter__(self):
-        return self
-
-    def __next__(self):
-        p = self._position = self._position + 1
-        if p >= len(self):
-            raise StopIteration
-        elif p < 0:
-            raise TypeError
-        return self[p:p + 1]
-
-    def next(self):
-        # Py2 compat
-        return self.__next__()
-
-    def previous(self):
-        p = self._position
-        if p >= len(self):
-            raise StopIteration
-        elif p < 0:
-            raise TypeError
-        self._position = p = p - 1
-        return self[p:p + 1]
-
-    def setPosition(self, position):
-        if self._position >= len(self):
-            raise StopIteration
-        self._position = position
-
-    def getPosition(self):
-        if self._position >= len(self):
-            raise StopIteration
-        if self._position >= 0:
-            return self._position
-        else:
-            return None
-
-    position = property(getPosition, setPosition)
-
-    def getCurrentByte(self):
-        return self[self.position:self.position + 1]
-
-    currentByte = property(getCurrentByte)
-
-    def skip(self, chars=spaceCharactersBytes):
-        """Skip past a list of characters"""
-        p = self.position               # use property for the error-checking
-        while p < len(self):
-            c = self[p:p + 1]
-            if c not in chars:
-                self._position = p
-                return c
-            p += 1
-        self._position = p
-        return None
-
-    def skipUntil(self, chars):
-        p = self.position
-        while p < len(self):
-            c = self[p:p + 1]
-            if c in chars:
-                self._position = p
-                return c
-            p += 1
-        self._position = p
-        return None
-
-    def matchBytes(self, bytes):
-        """Look for a sequence of bytes at the start of a string. If the bytes
-        are found return True and advance the position to the byte after the
-        match. Otherwise return False and leave the position alone"""
-        p = self.position
-        data = self[p:p + len(bytes)]
-        rv = data.startswith(bytes)
-        if rv:
-            self.position += len(bytes)
-        return rv
-
-    def jumpTo(self, bytes):
-        """Look for the next sequence of bytes matching a given sequence. If
-        a match is found advance the position to the last byte of the match"""
-        newPosition = self[self.position:].find(bytes)
-        if newPosition > -1:
-            # XXX: This is ugly, but I can't see a nicer way to fix this.
-            if self._position == -1:
-                self._position = 0
-            self._position += (newPosition + len(bytes) - 1)
-            return True
-        else:
-            raise StopIteration
-
-
-class EncodingParser(object):
-    """Mini parser for detecting character encoding from meta elements"""
-
-    def __init__(self, data):
-        """string - the data to work on for encoding detection"""
-        self.data = EncodingBytes(data)
-        self.encoding = None
-
-    def getEncoding(self):
-        methodDispatch = (
-            (b"<!--", self.handleComment),
-            (b"<meta", self.handleMeta),
-            (b"</", self.handlePossibleEndTag),
-            (b"<!", self.handleOther),
-            (b"<?", self.handleOther),
-            (b"<", self.handlePossibleStartTag))
-        for _ in self.data:
-            keepParsing = True
-            for key, method in methodDispatch:
-                if self.data.matchBytes(key):
-                    try:
-                        keepParsing = method()
-                        break
-                    except StopIteration:
-                        keepParsing = False
-                        break
-            if not keepParsing:
-                break
-
-        return self.encoding
-
-    def handleComment(self):
-        """Skip over comments"""
-        return self.data.jumpTo(b"-->")
-
-    def handleMeta(self):
-        if self.data.currentByte not in spaceCharactersBytes:
-            # if we have <meta not followed by a space so just keep going
-            return True
-        # We have a valid meta element we want to search for attributes
-        hasPragma = False
-        pendingEncoding = None
-        while True:
-            # Try to find the next attribute after the current position
-            attr = self.getAttribute()
-            if attr is None:
-                return True
-            else:
-                if attr[0] == b"http-equiv":
-                    hasPragma = attr[1] == b"content-type"
-                    if hasPragma and pendingEncoding is not None:
-                        self.encoding = pendingEncoding
-                        return False
-                elif attr[0] == b"charset":
-                    tentativeEncoding = attr[1]
-                    codec = lookupEncoding(tentativeEncoding)
-                    if codec is not None:
-                        self.encoding = codec
-                        return False
-                elif attr[0] == b"content":
-                    contentParser = ContentAttrParser(EncodingBytes(attr[1]))
-                    tentativeEncoding = contentParser.parse()
-                    if tentativeEncoding is not None:
-                        codec = lookupEncoding(tentativeEncoding)
-                        if codec is not None:
-                            if hasPragma:
-                                self.encoding = codec
-                                return False
-                            else:
-                                pendingEncoding = codec
-
-    def handlePossibleStartTag(self):
-        return self.handlePossibleTag(False)
-
-    def handlePossibleEndTag(self):
-        next(self.data)
-        return self.handlePossibleTag(True)
-
-    def handlePossibleTag(self, endTag):
-        data = self.data
-        if data.currentByte not in asciiLettersBytes:
-            # If the next byte is not an ascii letter either ignore this
-            # fragment (possible start tag case) or treat it according to
-            # handleOther
-            if endTag:
-                data.previous()
-                self.handleOther()
-            return True
-
-        c = data.skipUntil(spacesAngleBrackets)
-        if c == b"<":
-            # return to the first step in the overall "two step" algorithm
-            # reprocessing the < byte
-            data.previous()
-        else:
-            # Read all attributes
-            attr = self.getAttribute()
-            while attr is not None:
-                attr = self.getAttribute()
-        return True
-
-    def handleOther(self):
-        return self.data.jumpTo(b">")
-
-    def getAttribute(self):
-        """Return a name,value pair for the next attribute in the stream,
-        if one is found, or None"""
-        data = self.data
-        # Step 1 (skip chars)
-        c = data.skip(spaceCharactersBytes | frozenset([b"/"]))
-        assert c is None or len(c) == 1
-        # Step 2
-        if c in (b">", None):
-            return None
-        # Step 3
-        attrName = []
-        attrValue = []
-        # Step 4 attribute name
-        while True:
-            if c == b"=" and attrName:
-                break
-            elif c in spaceCharactersBytes:
-                # Step 6!
-                c = data.skip()
-                break
-            elif c in (b"/", b">"):
-                return b"".join(attrName), b""
-            elif c in asciiUppercaseBytes:
-                attrName.append(c.lower())
-            elif c is None:
-                return None
-            else:
-                attrName.append(c)
-            # Step 5
-            c = next(data)
-        # Step 7
-        if c != b"=":
-            data.previous()
-            return b"".join(attrName), b""
-        # Step 8
-        next(data)
-        # Step 9
-        c = data.skip()
-        # Step 10
-        if c in (b"'", b'"'):
-            # 10.1
-            quoteChar = c
-            while True:
-                # 10.2
-                c = next(data)
-                # 10.3
-                if c == quoteChar:
-                    next(data)
-                    return b"".join(attrName), b"".join(attrValue)
-                # 10.4
-                elif c in asciiUppercaseBytes:
-                    attrValue.append(c.lower())
-                # 10.5
-                else:
-                    attrValue.append(c)
-        elif c == b">":
-            return b"".join(attrName), b""
-        elif c in asciiUppercaseBytes:
-            attrValue.append(c.lower())
-        elif c is None:
-            return None
-        else:
-            attrValue.append(c)
-        # Step 11
-        while True:
-            c = next(data)
-            if c in spacesAngleBrackets:
-                return b"".join(attrName), b"".join(attrValue)
-            elif c in asciiUppercaseBytes:
-                attrValue.append(c.lower())
-            elif c is None:
-                return None
-            else:
-                attrValue.append(c)
-
-
-class ContentAttrParser(object):
-    def __init__(self, data):
-        assert isinstance(data, bytes)
-        self.data = data
-
-    def parse(self):
-        try:
-            # Check if the attr name is charset
-            # otherwise return
-            self.data.jumpTo(b"charset")
-            self.data.position += 1
-            self.data.skip()
-            if not self.data.currentByte == b"=":
-                # If there is no = sign keep looking for attrs
-                return None
-            self.data.position += 1
-            self.data.skip()
-            # Look for an encoding between matching quote marks
-            if self.data.currentByte in (b'"', b"'"):
-                quoteMark = self.data.currentByte
-                self.data.position += 1
-                oldPosition = self.data.position
-                if self.data.jumpTo(quoteMark):
-                    return self.data[oldPosition:self.data.position]
-                else:
-                    return None
-            else:
-                # Unquoted value
-                oldPosition = self.data.position
-                try:
-                    self.data.skipUntil(spaceCharactersBytes)
-                    return self.data[oldPosition:self.data.position]
-                except StopIteration:
-                    # Return the whole remaining value
-                    return self.data[oldPosition:]
-        except StopIteration:
-            return None
-
-
-def lookupEncoding(encoding):
-    """Return the python codec name corresponding to an encoding or None if the
-    string doesn't correspond to a valid encoding."""
-    if isinstance(encoding, binary_type):
-        try:
-            encoding = encoding.decode("ascii")
-        except UnicodeDecodeError:
-            return None
-
-    if encoding is not None:
-        try:
-            return webencodings.lookup(encoding)
-        except AttributeError:
-            return None
-    else:
-        return None
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_tokenizer.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_tokenizer.py
deleted file mode 100644
index 178f6e7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_tokenizer.py
+++ /dev/null
@@ -1,1721 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from pip._vendor.six import unichr as chr
-
-from collections import deque
-
-from .constants import spaceCharacters
-from .constants import entities
-from .constants import asciiLetters, asciiUpper2Lower
-from .constants import digits, hexDigits, EOF
-from .constants import tokenTypes, tagTokenTypes
-from .constants import replacementCharacters
-
-from ._inputstream import HTMLInputStream
-
-from ._trie import Trie
-
-entitiesTrie = Trie(entities)
-
-
-class HTMLTokenizer(object):
-    """ This class takes care of tokenizing HTML.
-
-    * self.currentToken
-      Holds the token that is currently being processed.
-
-    * self.state
-      Holds a reference to the method to be invoked... XXX
-
-    * self.stream
-      Points to HTMLInputStream object.
-    """
-
-    def __init__(self, stream, parser=None, **kwargs):
-
-        self.stream = HTMLInputStream(stream, **kwargs)
-        self.parser = parser
-
-        # Setup the initial tokenizer state
-        self.escapeFlag = False
-        self.lastFourChars = []
-        self.state = self.dataState
-        self.escape = False
-
-        # The current token being created
-        self.currentToken = None
-        super(HTMLTokenizer, self).__init__()
-
-    def __iter__(self):
-        """ This is where the magic happens.
-
-        We do our usually processing through the states and when we have a token
-        to return we yield the token which pauses processing until the next token
-        is requested.
-        """
-        self.tokenQueue = deque([])
-        # Start processing. When EOF is reached self.state will return False
-        # instead of True and the loop will terminate.
-        while self.state():
-            while self.stream.errors:
-                yield {"type": tokenTypes["ParseError"], "data": self.stream.errors.pop(0)}
-            while self.tokenQueue:
-                yield self.tokenQueue.popleft()
-
-    def consumeNumberEntity(self, isHex):
-        """This function returns either U+FFFD or the character based on the
-        decimal or hexadecimal representation. It also discards ";" if present.
-        If not present self.tokenQueue.append({"type": tokenTypes["ParseError"]}) is invoked.
-        """
-
-        allowed = digits
-        radix = 10
-        if isHex:
-            allowed = hexDigits
-            radix = 16
-
-        charStack = []
-
-        # Consume all the characters that are in range while making sure we
-        # don't hit an EOF.
-        c = self.stream.char()
-        while c in allowed and c is not EOF:
-            charStack.append(c)
-            c = self.stream.char()
-
-        # Convert the set of characters consumed to an int.
-        charAsInt = int("".join(charStack), radix)
-
-        # Certain characters get replaced with others
-        if charAsInt in replacementCharacters:
-            char = replacementCharacters[charAsInt]
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "illegal-codepoint-for-numeric-entity",
-                                    "datavars": {"charAsInt": charAsInt}})
-        elif ((0xD800 <= charAsInt <= 0xDFFF) or
-              (charAsInt > 0x10FFFF)):
-            char = "\uFFFD"
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "illegal-codepoint-for-numeric-entity",
-                                    "datavars": {"charAsInt": charAsInt}})
-        else:
-            # Should speed up this check somehow (e.g. move the set to a constant)
-            if ((0x0001 <= charAsInt <= 0x0008) or
-                (0x000E <= charAsInt <= 0x001F) or
-                (0x007F <= charAsInt <= 0x009F) or
-                (0xFDD0 <= charAsInt <= 0xFDEF) or
-                charAsInt in frozenset([0x000B, 0xFFFE, 0xFFFF, 0x1FFFE,
-                                        0x1FFFF, 0x2FFFE, 0x2FFFF, 0x3FFFE,
-                                        0x3FFFF, 0x4FFFE, 0x4FFFF, 0x5FFFE,
-                                        0x5FFFF, 0x6FFFE, 0x6FFFF, 0x7FFFE,
-                                        0x7FFFF, 0x8FFFE, 0x8FFFF, 0x9FFFE,
-                                        0x9FFFF, 0xAFFFE, 0xAFFFF, 0xBFFFE,
-                                        0xBFFFF, 0xCFFFE, 0xCFFFF, 0xDFFFE,
-                                        0xDFFFF, 0xEFFFE, 0xEFFFF, 0xFFFFE,
-                                        0xFFFFF, 0x10FFFE, 0x10FFFF])):
-                self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                        "data":
-                                        "illegal-codepoint-for-numeric-entity",
-                                        "datavars": {"charAsInt": charAsInt}})
-            try:
-                # Try/except needed as UCS-2 Python builds' unichar only works
-                # within the BMP.
-                char = chr(charAsInt)
-            except ValueError:
-                v = charAsInt - 0x10000
-                char = chr(0xD800 | (v >> 10)) + chr(0xDC00 | (v & 0x3FF))
-
-        # Discard the ; if present. Otherwise, put it back on the queue and
-        # invoke parseError on parser.
-        if c != ";":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "numeric-entity-without-semicolon"})
-            self.stream.unget(c)
-
-        return char
-
-    def consumeEntity(self, allowedChar=None, fromAttribute=False):
-        # Initialise to the default output for when no entity is matched
-        output = "&"
-
-        charStack = [self.stream.char()]
-        if (charStack[0] in spaceCharacters or charStack[0] in (EOF, "<", "&") or
-                (allowedChar is not None and allowedChar == charStack[0])):
-            self.stream.unget(charStack[0])
-
-        elif charStack[0] == "#":
-            # Read the next character to see if it's hex or decimal
-            hex = False
-            charStack.append(self.stream.char())
-            if charStack[-1] in ("x", "X"):
-                hex = True
-                charStack.append(self.stream.char())
-
-            # charStack[-1] should be the first digit
-            if (hex and charStack[-1] in hexDigits) \
-                    or (not hex and charStack[-1] in digits):
-                # At least one digit found, so consume the whole number
-                self.stream.unget(charStack[-1])
-                output = self.consumeNumberEntity(hex)
-            else:
-                # No digits found
-                self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                        "data": "expected-numeric-entity"})
-                self.stream.unget(charStack.pop())
-                output = "&" + "".join(charStack)
-
-        else:
-            # At this point in the process might have named entity. Entities
-            # are stored in the global variable "entities".
-            #
-            # Consume characters and compare to these to a substring of the
-            # entity names in the list until the substring no longer matches.
-            while (charStack[-1] is not EOF):
-                if not entitiesTrie.has_keys_with_prefix("".join(charStack)):
-                    break
-                charStack.append(self.stream.char())
-
-            # At this point we have a string that starts with some characters
-            # that may match an entity
-            # Try to find the longest entity the string will match to take care
-            # of &noti for instance.
-            try:
-                entityName = entitiesTrie.longest_prefix("".join(charStack[:-1]))
-                entityLength = len(entityName)
-            except KeyError:
-                entityName = None
-
-            if entityName is not None:
-                if entityName[-1] != ";":
-                    self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                            "named-entity-without-semicolon"})
-                if (entityName[-1] != ";" and fromAttribute and
-                    (charStack[entityLength] in asciiLetters or
-                     charStack[entityLength] in digits or
-                     charStack[entityLength] == "=")):
-                    self.stream.unget(charStack.pop())
-                    output = "&" + "".join(charStack)
-                else:
-                    output = entities[entityName]
-                    self.stream.unget(charStack.pop())
-                    output += "".join(charStack[entityLength:])
-            else:
-                self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                        "expected-named-entity"})
-                self.stream.unget(charStack.pop())
-                output = "&" + "".join(charStack)
-
-        if fromAttribute:
-            self.currentToken["data"][-1][1] += output
-        else:
-            if output in spaceCharacters:
-                tokenType = "SpaceCharacters"
-            else:
-                tokenType = "Characters"
-            self.tokenQueue.append({"type": tokenTypes[tokenType], "data": output})
-
-    def processEntityInAttribute(self, allowedChar):
-        """This method replaces the need for "entityInAttributeValueState".
-        """
-        self.consumeEntity(allowedChar=allowedChar, fromAttribute=True)
-
-    def emitCurrentToken(self):
-        """This method is a generic handler for emitting the tags. It also sets
-        the state to "data" because that's what's needed after a token has been
-        emitted.
-        """
-        token = self.currentToken
-        # Add token to the queue to be yielded
-        if (token["type"] in tagTokenTypes):
-            token["name"] = token["name"].translate(asciiUpper2Lower)
-            if token["type"] == tokenTypes["EndTag"]:
-                if token["data"]:
-                    self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                            "data": "attributes-in-end-tag"})
-                if token["selfClosing"]:
-                    self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                            "data": "self-closing-flag-on-end-tag"})
-        self.tokenQueue.append(token)
-        self.state = self.dataState
-
-    # Below are the various tokenizer states worked out.
-    def dataState(self):
-        data = self.stream.char()
-        if data == "&":
-            self.state = self.entityDataState
-        elif data == "<":
-            self.state = self.tagOpenState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\u0000"})
-        elif data is EOF:
-            # Tokenization ends.
-            return False
-        elif data in spaceCharacters:
-            # Directly after emitting a token you switch back to the "data
-            # state". At that point spaceCharacters are important so they are
-            # emitted separately.
-            self.tokenQueue.append({"type": tokenTypes["SpaceCharacters"], "data":
-                                    data + self.stream.charsUntil(spaceCharacters, True)})
-            # No need to update lastFourChars here, since the first space will
-            # have already been appended to lastFourChars and will have broken
-            # any <!-- or --> sequences
-        else:
-            chars = self.stream.charsUntil(("&", "<", "\u0000"))
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data":
-                                    data + chars})
-        return True
-
-    def entityDataState(self):
-        self.consumeEntity()
-        self.state = self.dataState
-        return True
-
-    def rcdataState(self):
-        data = self.stream.char()
-        if data == "&":
-            self.state = self.characterReferenceInRcdata
-        elif data == "<":
-            self.state = self.rcdataLessThanSignState
-        elif data == EOF:
-            # Tokenization ends.
-            return False
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-        elif data in spaceCharacters:
-            # Directly after emitting a token you switch back to the "data
-            # state". At that point spaceCharacters are important so they are
-            # emitted separately.
-            self.tokenQueue.append({"type": tokenTypes["SpaceCharacters"], "data":
-                                    data + self.stream.charsUntil(spaceCharacters, True)})
-            # No need to update lastFourChars here, since the first space will
-            # have already been appended to lastFourChars and will have broken
-            # any <!-- or --> sequences
-        else:
-            chars = self.stream.charsUntil(("&", "<", "\u0000"))
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data":
-                                    data + chars})
-        return True
-
-    def characterReferenceInRcdata(self):
-        self.consumeEntity()
-        self.state = self.rcdataState
-        return True
-
-    def rawtextState(self):
-        data = self.stream.char()
-        if data == "<":
-            self.state = self.rawtextLessThanSignState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-        elif data == EOF:
-            # Tokenization ends.
-            return False
-        else:
-            chars = self.stream.charsUntil(("<", "\u0000"))
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data":
-                                    data + chars})
-        return True
-
-    def scriptDataState(self):
-        data = self.stream.char()
-        if data == "<":
-            self.state = self.scriptDataLessThanSignState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-        elif data == EOF:
-            # Tokenization ends.
-            return False
-        else:
-            chars = self.stream.charsUntil(("<", "\u0000"))
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data":
-                                    data + chars})
-        return True
-
-    def plaintextState(self):
-        data = self.stream.char()
-        if data == EOF:
-            # Tokenization ends.
-            return False
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data":
-                                    data + self.stream.charsUntil("\u0000")})
-        return True
-
-    def tagOpenState(self):
-        data = self.stream.char()
-        if data == "!":
-            self.state = self.markupDeclarationOpenState
-        elif data == "/":
-            self.state = self.closeTagOpenState
-        elif data in asciiLetters:
-            self.currentToken = {"type": tokenTypes["StartTag"],
-                                 "name": data, "data": [],
-                                 "selfClosing": False,
-                                 "selfClosingAcknowledged": False}
-            self.state = self.tagNameState
-        elif data == ">":
-            # XXX In theory it could be something besides a tag name. But
-            # do we really care?
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-tag-name-but-got-right-bracket"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<>"})
-            self.state = self.dataState
-        elif data == "?":
-            # XXX In theory it could be something besides a tag name. But
-            # do we really care?
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-tag-name-but-got-question-mark"})
-            self.stream.unget(data)
-            self.state = self.bogusCommentState
-        else:
-            # XXX
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-tag-name"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.stream.unget(data)
-            self.state = self.dataState
-        return True
-
-    def closeTagOpenState(self):
-        data = self.stream.char()
-        if data in asciiLetters:
-            self.currentToken = {"type": tokenTypes["EndTag"], "name": data,
-                                 "data": [], "selfClosing": False}
-            self.state = self.tagNameState
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-closing-tag-but-got-right-bracket"})
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-closing-tag-but-got-eof"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "</"})
-            self.state = self.dataState
-        else:
-            # XXX data can be _'_...
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-closing-tag-but-got-char",
-                                    "datavars": {"data": data}})
-            self.stream.unget(data)
-            self.state = self.bogusCommentState
-        return True
-
-    def tagNameState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.state = self.beforeAttributeNameState
-        elif data == ">":
-            self.emitCurrentToken()
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-tag-name"})
-            self.state = self.dataState
-        elif data == "/":
-            self.state = self.selfClosingStartTagState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["name"] += "\uFFFD"
-        else:
-            self.currentToken["name"] += data
-            # (Don't use charsUntil here, because tag names are
-            # very short and it's faster to not do anything fancy)
-        return True
-
-    def rcdataLessThanSignState(self):
-        data = self.stream.char()
-        if data == "/":
-            self.temporaryBuffer = ""
-            self.state = self.rcdataEndTagOpenState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.stream.unget(data)
-            self.state = self.rcdataState
-        return True
-
-    def rcdataEndTagOpenState(self):
-        data = self.stream.char()
-        if data in asciiLetters:
-            self.temporaryBuffer += data
-            self.state = self.rcdataEndTagNameState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "</"})
-            self.stream.unget(data)
-            self.state = self.rcdataState
-        return True
-
-    def rcdataEndTagNameState(self):
-        appropriate = self.currentToken and self.currentToken["name"].lower() == self.temporaryBuffer.lower()
-        data = self.stream.char()
-        if data in spaceCharacters and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.beforeAttributeNameState
-        elif data == "/" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.selfClosingStartTagState
-        elif data == ">" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.emitCurrentToken()
-            self.state = self.dataState
-        elif data in asciiLetters:
-            self.temporaryBuffer += data
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "</" + self.temporaryBuffer})
-            self.stream.unget(data)
-            self.state = self.rcdataState
-        return True
-
-    def rawtextLessThanSignState(self):
-        data = self.stream.char()
-        if data == "/":
-            self.temporaryBuffer = ""
-            self.state = self.rawtextEndTagOpenState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.stream.unget(data)
-            self.state = self.rawtextState
-        return True
-
-    def rawtextEndTagOpenState(self):
-        data = self.stream.char()
-        if data in asciiLetters:
-            self.temporaryBuffer += data
-            self.state = self.rawtextEndTagNameState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "</"})
-            self.stream.unget(data)
-            self.state = self.rawtextState
-        return True
-
-    def rawtextEndTagNameState(self):
-        appropriate = self.currentToken and self.currentToken["name"].lower() == self.temporaryBuffer.lower()
-        data = self.stream.char()
-        if data in spaceCharacters and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.beforeAttributeNameState
-        elif data == "/" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.selfClosingStartTagState
-        elif data == ">" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.emitCurrentToken()
-            self.state = self.dataState
-        elif data in asciiLetters:
-            self.temporaryBuffer += data
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "</" + self.temporaryBuffer})
-            self.stream.unget(data)
-            self.state = self.rawtextState
-        return True
-
-    def scriptDataLessThanSignState(self):
-        data = self.stream.char()
-        if data == "/":
-            self.temporaryBuffer = ""
-            self.state = self.scriptDataEndTagOpenState
-        elif data == "!":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<!"})
-            self.state = self.scriptDataEscapeStartState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.stream.unget(data)
-            self.state = self.scriptDataState
-        return True
-
-    def scriptDataEndTagOpenState(self):
-        data = self.stream.char()
-        if data in asciiLetters:
-            self.temporaryBuffer += data
-            self.state = self.scriptDataEndTagNameState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "</"})
-            self.stream.unget(data)
-            self.state = self.scriptDataState
-        return True
-
-    def scriptDataEndTagNameState(self):
-        appropriate = self.currentToken and self.currentToken["name"].lower() == self.temporaryBuffer.lower()
-        data = self.stream.char()
-        if data in spaceCharacters and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.beforeAttributeNameState
-        elif data == "/" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.selfClosingStartTagState
-        elif data == ">" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.emitCurrentToken()
-            self.state = self.dataState
-        elif data in asciiLetters:
-            self.temporaryBuffer += data
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "</" + self.temporaryBuffer})
-            self.stream.unget(data)
-            self.state = self.scriptDataState
-        return True
-
-    def scriptDataEscapeStartState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-            self.state = self.scriptDataEscapeStartDashState
-        else:
-            self.stream.unget(data)
-            self.state = self.scriptDataState
-        return True
-
-    def scriptDataEscapeStartDashState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-            self.state = self.scriptDataEscapedDashDashState
-        else:
-            self.stream.unget(data)
-            self.state = self.scriptDataState
-        return True
-
-    def scriptDataEscapedState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-            self.state = self.scriptDataEscapedDashState
-        elif data == "<":
-            self.state = self.scriptDataEscapedLessThanSignState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-        elif data == EOF:
-            self.state = self.dataState
-        else:
-            chars = self.stream.charsUntil(("<", "-", "\u0000"))
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data":
-                                    data + chars})
-        return True
-
-    def scriptDataEscapedDashState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-            self.state = self.scriptDataEscapedDashDashState
-        elif data == "<":
-            self.state = self.scriptDataEscapedLessThanSignState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-            self.state = self.scriptDataEscapedState
-        elif data == EOF:
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            self.state = self.scriptDataEscapedState
-        return True
-
-    def scriptDataEscapedDashDashState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-        elif data == "<":
-            self.state = self.scriptDataEscapedLessThanSignState
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": ">"})
-            self.state = self.scriptDataState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-            self.state = self.scriptDataEscapedState
-        elif data == EOF:
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            self.state = self.scriptDataEscapedState
-        return True
-
-    def scriptDataEscapedLessThanSignState(self):
-        data = self.stream.char()
-        if data == "/":
-            self.temporaryBuffer = ""
-            self.state = self.scriptDataEscapedEndTagOpenState
-        elif data in asciiLetters:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<" + data})
-            self.temporaryBuffer = data
-            self.state = self.scriptDataDoubleEscapeStartState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.stream.unget(data)
-            self.state = self.scriptDataEscapedState
-        return True
-
-    def scriptDataEscapedEndTagOpenState(self):
-        data = self.stream.char()
-        if data in asciiLetters:
-            self.temporaryBuffer = data
-            self.state = self.scriptDataEscapedEndTagNameState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "</"})
-            self.stream.unget(data)
-            self.state = self.scriptDataEscapedState
-        return True
-
-    def scriptDataEscapedEndTagNameState(self):
-        appropriate = self.currentToken and self.currentToken["name"].lower() == self.temporaryBuffer.lower()
-        data = self.stream.char()
-        if data in spaceCharacters and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.beforeAttributeNameState
-        elif data == "/" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.state = self.selfClosingStartTagState
-        elif data == ">" and appropriate:
-            self.currentToken = {"type": tokenTypes["EndTag"],
-                                 "name": self.temporaryBuffer,
-                                 "data": [], "selfClosing": False}
-            self.emitCurrentToken()
-            self.state = self.dataState
-        elif data in asciiLetters:
-            self.temporaryBuffer += data
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "</" + self.temporaryBuffer})
-            self.stream.unget(data)
-            self.state = self.scriptDataEscapedState
-        return True
-
-    def scriptDataDoubleEscapeStartState(self):
-        data = self.stream.char()
-        if data in (spaceCharacters | frozenset(("/", ">"))):
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            if self.temporaryBuffer.lower() == "script":
-                self.state = self.scriptDataDoubleEscapedState
-            else:
-                self.state = self.scriptDataEscapedState
-        elif data in asciiLetters:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            self.temporaryBuffer += data
-        else:
-            self.stream.unget(data)
-            self.state = self.scriptDataEscapedState
-        return True
-
-    def scriptDataDoubleEscapedState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-            self.state = self.scriptDataDoubleEscapedDashState
-        elif data == "<":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.state = self.scriptDataDoubleEscapedLessThanSignState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-        elif data == EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-script-in-script"})
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-        return True
-
-    def scriptDataDoubleEscapedDashState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-            self.state = self.scriptDataDoubleEscapedDashDashState
-        elif data == "<":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.state = self.scriptDataDoubleEscapedLessThanSignState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-            self.state = self.scriptDataDoubleEscapedState
-        elif data == EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-script-in-script"})
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            self.state = self.scriptDataDoubleEscapedState
-        return True
-
-    def scriptDataDoubleEscapedDashDashState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "-"})
-        elif data == "<":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "<"})
-            self.state = self.scriptDataDoubleEscapedLessThanSignState
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": ">"})
-            self.state = self.scriptDataState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": "\uFFFD"})
-            self.state = self.scriptDataDoubleEscapedState
-        elif data == EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-script-in-script"})
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            self.state = self.scriptDataDoubleEscapedState
-        return True
-
-    def scriptDataDoubleEscapedLessThanSignState(self):
-        data = self.stream.char()
-        if data == "/":
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": "/"})
-            self.temporaryBuffer = ""
-            self.state = self.scriptDataDoubleEscapeEndState
-        else:
-            self.stream.unget(data)
-            self.state = self.scriptDataDoubleEscapedState
-        return True
-
-    def scriptDataDoubleEscapeEndState(self):
-        data = self.stream.char()
-        if data in (spaceCharacters | frozenset(("/", ">"))):
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            if self.temporaryBuffer.lower() == "script":
-                self.state = self.scriptDataEscapedState
-            else:
-                self.state = self.scriptDataDoubleEscapedState
-        elif data in asciiLetters:
-            self.tokenQueue.append({"type": tokenTypes["Characters"], "data": data})
-            self.temporaryBuffer += data
-        else:
-            self.stream.unget(data)
-            self.state = self.scriptDataDoubleEscapedState
-        return True
-
-    def beforeAttributeNameState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.stream.charsUntil(spaceCharacters, True)
-        elif data in asciiLetters:
-            self.currentToken["data"].append([data, ""])
-            self.state = self.attributeNameState
-        elif data == ">":
-            self.emitCurrentToken()
-        elif data == "/":
-            self.state = self.selfClosingStartTagState
-        elif data in ("'", '"', "=", "<"):
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "invalid-character-in-attribute-name"})
-            self.currentToken["data"].append([data, ""])
-            self.state = self.attributeNameState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"].append(["\uFFFD", ""])
-            self.state = self.attributeNameState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-attribute-name-but-got-eof"})
-            self.state = self.dataState
-        else:
-            self.currentToken["data"].append([data, ""])
-            self.state = self.attributeNameState
-        return True
-
-    def attributeNameState(self):
-        data = self.stream.char()
-        leavingThisState = True
-        emitToken = False
-        if data == "=":
-            self.state = self.beforeAttributeValueState
-        elif data in asciiLetters:
-            self.currentToken["data"][-1][0] += data +\
-                self.stream.charsUntil(asciiLetters, True)
-            leavingThisState = False
-        elif data == ">":
-            # XXX If we emit here the attributes are converted to a dict
-            # without being checked and when the code below runs we error
-            # because data is a dict not a list
-            emitToken = True
-        elif data in spaceCharacters:
-            self.state = self.afterAttributeNameState
-        elif data == "/":
-            self.state = self.selfClosingStartTagState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"][-1][0] += "\uFFFD"
-            leavingThisState = False
-        elif data in ("'", '"', "<"):
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data":
-                                    "invalid-character-in-attribute-name"})
-            self.currentToken["data"][-1][0] += data
-            leavingThisState = False
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "eof-in-attribute-name"})
-            self.state = self.dataState
-        else:
-            self.currentToken["data"][-1][0] += data
-            leavingThisState = False
-
-        if leavingThisState:
-            # Attributes are not dropped at this stage. That happens when the
-            # start tag token is emitted so values can still be safely appended
-            # to attributes, but we do want to report the parse error in time.
-            self.currentToken["data"][-1][0] = (
-                self.currentToken["data"][-1][0].translate(asciiUpper2Lower))
-            for name, _ in self.currentToken["data"][:-1]:
-                if self.currentToken["data"][-1][0] == name:
-                    self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                            "duplicate-attribute"})
-                    break
-            # XXX Fix for above XXX
-            if emitToken:
-                self.emitCurrentToken()
-        return True
-
-    def afterAttributeNameState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.stream.charsUntil(spaceCharacters, True)
-        elif data == "=":
-            self.state = self.beforeAttributeValueState
-        elif data == ">":
-            self.emitCurrentToken()
-        elif data in asciiLetters:
-            self.currentToken["data"].append([data, ""])
-            self.state = self.attributeNameState
-        elif data == "/":
-            self.state = self.selfClosingStartTagState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"].append(["\uFFFD", ""])
-            self.state = self.attributeNameState
-        elif data in ("'", '"', "<"):
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "invalid-character-after-attribute-name"})
-            self.currentToken["data"].append([data, ""])
-            self.state = self.attributeNameState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-end-of-tag-but-got-eof"})
-            self.state = self.dataState
-        else:
-            self.currentToken["data"].append([data, ""])
-            self.state = self.attributeNameState
-        return True
-
-    def beforeAttributeValueState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.stream.charsUntil(spaceCharacters, True)
-        elif data == "\"":
-            self.state = self.attributeValueDoubleQuotedState
-        elif data == "&":
-            self.state = self.attributeValueUnQuotedState
-            self.stream.unget(data)
-        elif data == "'":
-            self.state = self.attributeValueSingleQuotedState
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-attribute-value-but-got-right-bracket"})
-            self.emitCurrentToken()
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"][-1][1] += "\uFFFD"
-            self.state = self.attributeValueUnQuotedState
-        elif data in ("=", "<", "`"):
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "equals-in-unquoted-attribute-value"})
-            self.currentToken["data"][-1][1] += data
-            self.state = self.attributeValueUnQuotedState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-attribute-value-but-got-eof"})
-            self.state = self.dataState
-        else:
-            self.currentToken["data"][-1][1] += data
-            self.state = self.attributeValueUnQuotedState
-        return True
-
-    def attributeValueDoubleQuotedState(self):
-        data = self.stream.char()
-        if data == "\"":
-            self.state = self.afterAttributeValueState
-        elif data == "&":
-            self.processEntityInAttribute('"')
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"][-1][1] += "\uFFFD"
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-attribute-value-double-quote"})
-            self.state = self.dataState
-        else:
-            self.currentToken["data"][-1][1] += data +\
-                self.stream.charsUntil(("\"", "&", "\u0000"))
-        return True
-
-    def attributeValueSingleQuotedState(self):
-        data = self.stream.char()
-        if data == "'":
-            self.state = self.afterAttributeValueState
-        elif data == "&":
-            self.processEntityInAttribute("'")
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"][-1][1] += "\uFFFD"
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-attribute-value-single-quote"})
-            self.state = self.dataState
-        else:
-            self.currentToken["data"][-1][1] += data +\
-                self.stream.charsUntil(("'", "&", "\u0000"))
-        return True
-
-    def attributeValueUnQuotedState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.state = self.beforeAttributeNameState
-        elif data == "&":
-            self.processEntityInAttribute(">")
-        elif data == ">":
-            self.emitCurrentToken()
-        elif data in ('"', "'", "=", "<", "`"):
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-character-in-unquoted-attribute-value"})
-            self.currentToken["data"][-1][1] += data
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"][-1][1] += "\uFFFD"
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-attribute-value-no-quotes"})
-            self.state = self.dataState
-        else:
-            self.currentToken["data"][-1][1] += data + self.stream.charsUntil(
-                frozenset(("&", ">", '"', "'", "=", "<", "`", "\u0000")) | spaceCharacters)
-        return True
-
-    def afterAttributeValueState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.state = self.beforeAttributeNameState
-        elif data == ">":
-            self.emitCurrentToken()
-        elif data == "/":
-            self.state = self.selfClosingStartTagState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-EOF-after-attribute-value"})
-            self.stream.unget(data)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-character-after-attribute-value"})
-            self.stream.unget(data)
-            self.state = self.beforeAttributeNameState
-        return True
-
-    def selfClosingStartTagState(self):
-        data = self.stream.char()
-        if data == ">":
-            self.currentToken["selfClosing"] = True
-            self.emitCurrentToken()
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data":
-                                    "unexpected-EOF-after-solidus-in-tag"})
-            self.stream.unget(data)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-character-after-solidus-in-tag"})
-            self.stream.unget(data)
-            self.state = self.beforeAttributeNameState
-        return True
-
-    def bogusCommentState(self):
-        # Make a new comment token and give it as value all the characters
-        # until the first > or EOF (charsUntil checks for EOF automatically)
-        # and emit it.
-        data = self.stream.charsUntil(">")
-        data = data.replace("\u0000", "\uFFFD")
-        self.tokenQueue.append(
-            {"type": tokenTypes["Comment"], "data": data})
-
-        # Eat the character directly after the bogus comment which is either a
-        # ">" or an EOF.
-        self.stream.char()
-        self.state = self.dataState
-        return True
-
-    def markupDeclarationOpenState(self):
-        charStack = [self.stream.char()]
-        if charStack[-1] == "-":
-            charStack.append(self.stream.char())
-            if charStack[-1] == "-":
-                self.currentToken = {"type": tokenTypes["Comment"], "data": ""}
-                self.state = self.commentStartState
-                return True
-        elif charStack[-1] in ('d', 'D'):
-            matched = True
-            for expected in (('o', 'O'), ('c', 'C'), ('t', 'T'),
-                             ('y', 'Y'), ('p', 'P'), ('e', 'E')):
-                charStack.append(self.stream.char())
-                if charStack[-1] not in expected:
-                    matched = False
-                    break
-            if matched:
-                self.currentToken = {"type": tokenTypes["Doctype"],
-                                     "name": "",
-                                     "publicId": None, "systemId": None,
-                                     "correct": True}
-                self.state = self.doctypeState
-                return True
-        elif (charStack[-1] == "[" and
-              self.parser is not None and
-              self.parser.tree.openElements and
-              self.parser.tree.openElements[-1].namespace != self.parser.tree.defaultNamespace):
-            matched = True
-            for expected in ["C", "D", "A", "T", "A", "["]:
-                charStack.append(self.stream.char())
-                if charStack[-1] != expected:
-                    matched = False
-                    break
-            if matched:
-                self.state = self.cdataSectionState
-                return True
-
-        self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                "expected-dashes-or-doctype"})
-
-        while charStack:
-            self.stream.unget(charStack.pop())
-        self.state = self.bogusCommentState
-        return True
-
-    def commentStartState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.state = self.commentStartDashState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"] += "\uFFFD"
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "incorrect-comment"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-comment"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["data"] += data
-            self.state = self.commentState
-        return True
-
-    def commentStartDashState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.state = self.commentEndState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"] += "-\uFFFD"
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "incorrect-comment"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-comment"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["data"] += "-" + data
-            self.state = self.commentState
-        return True
-
-    def commentState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.state = self.commentEndDashState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"] += "\uFFFD"
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "eof-in-comment"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["data"] += data + \
-                self.stream.charsUntil(("-", "\u0000"))
-        return True
-
-    def commentEndDashState(self):
-        data = self.stream.char()
-        if data == "-":
-            self.state = self.commentEndState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"] += "-\uFFFD"
-            self.state = self.commentState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-comment-end-dash"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["data"] += "-" + data
-            self.state = self.commentState
-        return True
-
-    def commentEndState(self):
-        data = self.stream.char()
-        if data == ">":
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"] += "--\uFFFD"
-            self.state = self.commentState
-        elif data == "!":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-bang-after-double-dash-in-comment"})
-            self.state = self.commentEndBangState
-        elif data == "-":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-dash-after-double-dash-in-comment"})
-            self.currentToken["data"] += data
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-comment-double-dash"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            # XXX
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-comment"})
-            self.currentToken["data"] += "--" + data
-            self.state = self.commentState
-        return True
-
-    def commentEndBangState(self):
-        data = self.stream.char()
-        if data == ">":
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data == "-":
-            self.currentToken["data"] += "--!"
-            self.state = self.commentEndDashState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["data"] += "--!\uFFFD"
-            self.state = self.commentState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-comment-end-bang-state"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["data"] += "--!" + data
-            self.state = self.commentState
-        return True
-
-    def doctypeState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.state = self.beforeDoctypeNameState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-doctype-name-but-got-eof"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "need-space-after-doctype"})
-            self.stream.unget(data)
-            self.state = self.beforeDoctypeNameState
-        return True
-
-    def beforeDoctypeNameState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            pass
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-doctype-name-but-got-right-bracket"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["name"] = "\uFFFD"
-            self.state = self.doctypeNameState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-doctype-name-but-got-eof"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["name"] = data
-            self.state = self.doctypeNameState
-        return True
-
-    def doctypeNameState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.currentToken["name"] = self.currentToken["name"].translate(asciiUpper2Lower)
-            self.state = self.afterDoctypeNameState
-        elif data == ">":
-            self.currentToken["name"] = self.currentToken["name"].translate(asciiUpper2Lower)
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["name"] += "\uFFFD"
-            self.state = self.doctypeNameState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype-name"})
-            self.currentToken["correct"] = False
-            self.currentToken["name"] = self.currentToken["name"].translate(asciiUpper2Lower)
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["name"] += data
-        return True
-
-    def afterDoctypeNameState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            pass
-        elif data == ">":
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.currentToken["correct"] = False
-            self.stream.unget(data)
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            if data in ("p", "P"):
-                matched = True
-                for expected in (("u", "U"), ("b", "B"), ("l", "L"),
-                                 ("i", "I"), ("c", "C")):
-                    data = self.stream.char()
-                    if data not in expected:
-                        matched = False
-                        break
-                if matched:
-                    self.state = self.afterDoctypePublicKeywordState
-                    return True
-            elif data in ("s", "S"):
-                matched = True
-                for expected in (("y", "Y"), ("s", "S"), ("t", "T"),
-                                 ("e", "E"), ("m", "M")):
-                    data = self.stream.char()
-                    if data not in expected:
-                        matched = False
-                        break
-                if matched:
-                    self.state = self.afterDoctypeSystemKeywordState
-                    return True
-
-            # All the characters read before the current 'data' will be
-            # [a-zA-Z], so they're garbage in the bogus doctype and can be
-            # discarded; only the latest character might be '>' or EOF
-            # and needs to be ungetted
-            self.stream.unget(data)
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "expected-space-or-right-bracket-in-doctype", "datavars":
-                                    {"data": data}})
-            self.currentToken["correct"] = False
-            self.state = self.bogusDoctypeState
-
-        return True
-
-    def afterDoctypePublicKeywordState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.state = self.beforeDoctypePublicIdentifierState
-        elif data in ("'", '"'):
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.stream.unget(data)
-            self.state = self.beforeDoctypePublicIdentifierState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.stream.unget(data)
-            self.state = self.beforeDoctypePublicIdentifierState
-        return True
-
-    def beforeDoctypePublicIdentifierState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            pass
-        elif data == "\"":
-            self.currentToken["publicId"] = ""
-            self.state = self.doctypePublicIdentifierDoubleQuotedState
-        elif data == "'":
-            self.currentToken["publicId"] = ""
-            self.state = self.doctypePublicIdentifierSingleQuotedState
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-end-of-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.currentToken["correct"] = False
-            self.state = self.bogusDoctypeState
-        return True
-
-    def doctypePublicIdentifierDoubleQuotedState(self):
-        data = self.stream.char()
-        if data == "\"":
-            self.state = self.afterDoctypePublicIdentifierState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["publicId"] += "\uFFFD"
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-end-of-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["publicId"] += data
-        return True
-
-    def doctypePublicIdentifierSingleQuotedState(self):
-        data = self.stream.char()
-        if data == "'":
-            self.state = self.afterDoctypePublicIdentifierState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["publicId"] += "\uFFFD"
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-end-of-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["publicId"] += data
-        return True
-
-    def afterDoctypePublicIdentifierState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.state = self.betweenDoctypePublicAndSystemIdentifiersState
-        elif data == ">":
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data == '"':
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.currentToken["systemId"] = ""
-            self.state = self.doctypeSystemIdentifierDoubleQuotedState
-        elif data == "'":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.currentToken["systemId"] = ""
-            self.state = self.doctypeSystemIdentifierSingleQuotedState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.currentToken["correct"] = False
-            self.state = self.bogusDoctypeState
-        return True
-
-    def betweenDoctypePublicAndSystemIdentifiersState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            pass
-        elif data == ">":
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data == '"':
-            self.currentToken["systemId"] = ""
-            self.state = self.doctypeSystemIdentifierDoubleQuotedState
-        elif data == "'":
-            self.currentToken["systemId"] = ""
-            self.state = self.doctypeSystemIdentifierSingleQuotedState
-        elif data == EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.currentToken["correct"] = False
-            self.state = self.bogusDoctypeState
-        return True
-
-    def afterDoctypeSystemKeywordState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            self.state = self.beforeDoctypeSystemIdentifierState
-        elif data in ("'", '"'):
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.stream.unget(data)
-            self.state = self.beforeDoctypeSystemIdentifierState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.stream.unget(data)
-            self.state = self.beforeDoctypeSystemIdentifierState
-        return True
-
-    def beforeDoctypeSystemIdentifierState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            pass
-        elif data == "\"":
-            self.currentToken["systemId"] = ""
-            self.state = self.doctypeSystemIdentifierDoubleQuotedState
-        elif data == "'":
-            self.currentToken["systemId"] = ""
-            self.state = self.doctypeSystemIdentifierSingleQuotedState
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.currentToken["correct"] = False
-            self.state = self.bogusDoctypeState
-        return True
-
-    def doctypeSystemIdentifierDoubleQuotedState(self):
-        data = self.stream.char()
-        if data == "\"":
-            self.state = self.afterDoctypeSystemIdentifierState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["systemId"] += "\uFFFD"
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-end-of-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["systemId"] += data
-        return True
-
-    def doctypeSystemIdentifierSingleQuotedState(self):
-        data = self.stream.char()
-        if data == "'":
-            self.state = self.afterDoctypeSystemIdentifierState
-        elif data == "\u0000":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                    "data": "invalid-codepoint"})
-            self.currentToken["systemId"] += "\uFFFD"
-        elif data == ">":
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-end-of-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.currentToken["systemId"] += data
-        return True
-
-    def afterDoctypeSystemIdentifierState(self):
-        data = self.stream.char()
-        if data in spaceCharacters:
-            pass
-        elif data == ">":
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "eof-in-doctype"})
-            self.currentToken["correct"] = False
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            self.tokenQueue.append({"type": tokenTypes["ParseError"], "data":
-                                    "unexpected-char-in-doctype"})
-            self.state = self.bogusDoctypeState
-        return True
-
-    def bogusDoctypeState(self):
-        data = self.stream.char()
-        if data == ">":
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        elif data is EOF:
-            # XXX EMIT
-            self.stream.unget(data)
-            self.tokenQueue.append(self.currentToken)
-            self.state = self.dataState
-        else:
-            pass
-        return True
-
-    def cdataSectionState(self):
-        data = []
-        while True:
-            data.append(self.stream.charsUntil("]"))
-            data.append(self.stream.charsUntil(">"))
-            char = self.stream.char()
-            if char == EOF:
-                break
-            else:
-                assert char == ">"
-                if data[-1][-2:] == "]]":
-                    data[-1] = data[-1][:-2]
-                    break
-                else:
-                    data.append(char)
-
-        data = "".join(data)  # pylint:disable=redefined-variable-type
-        # Deal with null here rather than in the parser
-        nullCount = data.count("\u0000")
-        if nullCount > 0:
-            for _ in range(nullCount):
-                self.tokenQueue.append({"type": tokenTypes["ParseError"],
-                                        "data": "invalid-codepoint"})
-            data = data.replace("\u0000", "\uFFFD")
-        if data:
-            self.tokenQueue.append({"type": tokenTypes["Characters"],
-                                    "data": data})
-        self.state = self.dataState
-        return True
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__init__.py
deleted file mode 100644
index a5ba4bf..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__init__.py
+++ /dev/null
@@ -1,14 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from .py import Trie as PyTrie
-
-Trie = PyTrie
-
-# pylint:disable=wrong-import-position
-try:
-    from .datrie import Trie as DATrie
-except ImportError:
-    pass
-else:
-    Trie = DATrie
-# pylint:enable=wrong-import-position
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index dc6dd17..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/_base.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/_base.cpython-37.pyc
deleted file mode 100644
index 0ac68ce..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/_base.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/datrie.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/datrie.cpython-37.pyc
deleted file mode 100644
index e19e983..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/datrie.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/py.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/py.cpython-37.pyc
deleted file mode 100644
index a5e09f2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/__pycache__/py.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/_base.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/_base.py
deleted file mode 100644
index a1158bb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/_base.py
+++ /dev/null
@@ -1,37 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from collections import Mapping
-
-
-class Trie(Mapping):
-    """Abstract base class for tries"""
-
-    def keys(self, prefix=None):
-        # pylint:disable=arguments-differ
-        keys = super(Trie, self).keys()
-
-        if prefix is None:
-            return set(keys)
-
-        return {x for x in keys if x.startswith(prefix)}
-
-    def has_keys_with_prefix(self, prefix):
-        for key in self.keys():
-            if key.startswith(prefix):
-                return True
-
-        return False
-
-    def longest_prefix(self, prefix):
-        if prefix in self:
-            return prefix
-
-        for i in range(1, len(prefix) + 1):
-            if prefix[:-i] in self:
-                return prefix[:-i]
-
-        raise KeyError(prefix)
-
-    def longest_prefix_item(self, prefix):
-        lprefix = self.longest_prefix(prefix)
-        return (lprefix, self[lprefix])
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/datrie.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/datrie.py
deleted file mode 100644
index e2e5f86..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/datrie.py
+++ /dev/null
@@ -1,44 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from datrie import Trie as DATrie
-from pip._vendor.six import text_type
-
-from ._base import Trie as ABCTrie
-
-
-class Trie(ABCTrie):
-    def __init__(self, data):
-        chars = set()
-        for key in data.keys():
-            if not isinstance(key, text_type):
-                raise TypeError("All keys must be strings")
-            for char in key:
-                chars.add(char)
-
-        self._data = DATrie("".join(chars))
-        for key, value in data.items():
-            self._data[key] = value
-
-    def __contains__(self, key):
-        return key in self._data
-
-    def __len__(self):
-        return len(self._data)
-
-    def __iter__(self):
-        raise NotImplementedError()
-
-    def __getitem__(self, key):
-        return self._data[key]
-
-    def keys(self, prefix=None):
-        return self._data.keys(prefix)
-
-    def has_keys_with_prefix(self, prefix):
-        return self._data.has_keys_with_prefix(prefix)
-
-    def longest_prefix(self, prefix):
-        return self._data.longest_prefix(prefix)
-
-    def longest_prefix_item(self, prefix):
-        return self._data.longest_prefix_item(prefix)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/py.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/py.py
deleted file mode 100644
index c178b21..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_trie/py.py
+++ /dev/null
@@ -1,67 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-from pip._vendor.six import text_type
-
-from bisect import bisect_left
-
-from ._base import Trie as ABCTrie
-
-
-class Trie(ABCTrie):
-    def __init__(self, data):
-        if not all(isinstance(x, text_type) for x in data.keys()):
-            raise TypeError("All keys must be strings")
-
-        self._data = data
-        self._keys = sorted(data.keys())
-        self._cachestr = ""
-        self._cachepoints = (0, len(data))
-
-    def __contains__(self, key):
-        return key in self._data
-
-    def __len__(self):
-        return len(self._data)
-
-    def __iter__(self):
-        return iter(self._data)
-
-    def __getitem__(self, key):
-        return self._data[key]
-
-    def keys(self, prefix=None):
-        if prefix is None or prefix == "" or not self._keys:
-            return set(self._keys)
-
-        if prefix.startswith(self._cachestr):
-            lo, hi = self._cachepoints
-            start = i = bisect_left(self._keys, prefix, lo, hi)
-        else:
-            start = i = bisect_left(self._keys, prefix)
-
-        keys = set()
-        if start == len(self._keys):
-            return keys
-
-        while self._keys[i].startswith(prefix):
-            keys.add(self._keys[i])
-            i += 1
-
-        self._cachestr = prefix
-        self._cachepoints = (start, i)
-
-        return keys
-
-    def has_keys_with_prefix(self, prefix):
-        if prefix in self._data:
-            return True
-
-        if prefix.startswith(self._cachestr):
-            lo, hi = self._cachepoints
-            i = bisect_left(self._keys, prefix, lo, hi)
-        else:
-            i = bisect_left(self._keys, prefix)
-
-        if i == len(self._keys):
-            return False
-
-        return self._keys[i].startswith(prefix)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_utils.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_utils.py
deleted file mode 100644
index 0703afb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/_utils.py
+++ /dev/null
@@ -1,124 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from types import ModuleType
-
-from pip._vendor.six import text_type
-
-try:
-    import xml.etree.cElementTree as default_etree
-except ImportError:
-    import xml.etree.ElementTree as default_etree
-
-
-__all__ = ["default_etree", "MethodDispatcher", "isSurrogatePair",
-           "surrogatePairToCodepoint", "moduleFactoryFactory",
-           "supports_lone_surrogates"]
-
-
-# Platforms not supporting lone surrogates (\uD800-\uDFFF) should be
-# caught by the below test. In general this would be any platform
-# using UTF-16 as its encoding of unicode strings, such as
-# Jython. This is because UTF-16 itself is based on the use of such
-# surrogates, and there is no mechanism to further escape such
-# escapes.
-try:
-    _x = eval('"\\uD800"')  # pylint:disable=eval-used
-    if not isinstance(_x, text_type):
-        # We need this with u"" because of http://bugs.jython.org/issue2039
-        _x = eval('u"\\uD800"')  # pylint:disable=eval-used
-        assert isinstance(_x, text_type)
-except:  # pylint:disable=bare-except
-    supports_lone_surrogates = False
-else:
-    supports_lone_surrogates = True
-
-
-class MethodDispatcher(dict):
-    """Dict with 2 special properties:
-
-    On initiation, keys that are lists, sets or tuples are converted to
-    multiple keys so accessing any one of the items in the original
-    list-like object returns the matching value
-
-    md = MethodDispatcher({("foo", "bar"):"baz"})
-    md["foo"] == "baz"
-
-    A default value which can be set through the default attribute.
-    """
-
-    def __init__(self, items=()):
-        # Using _dictEntries instead of directly assigning to self is about
-        # twice as fast. Please do careful performance testing before changing
-        # anything here.
-        _dictEntries = []
-        for name, value in items:
-            if isinstance(name, (list, tuple, frozenset, set)):
-                for item in name:
-                    _dictEntries.append((item, value))
-            else:
-                _dictEntries.append((name, value))
-        dict.__init__(self, _dictEntries)
-        assert len(self) == len(_dictEntries)
-        self.default = None
-
-    def __getitem__(self, key):
-        return dict.get(self, key, self.default)
-
-
-# Some utility functions to deal with weirdness around UCS2 vs UCS4
-# python builds
-
-def isSurrogatePair(data):
-    return (len(data) == 2 and
-            ord(data[0]) >= 0xD800 and ord(data[0]) <= 0xDBFF and
-            ord(data[1]) >= 0xDC00 and ord(data[1]) <= 0xDFFF)
-
-
-def surrogatePairToCodepoint(data):
-    char_val = (0x10000 + (ord(data[0]) - 0xD800) * 0x400 +
-                (ord(data[1]) - 0xDC00))
-    return char_val
-
-# Module Factory Factory (no, this isn't Java, I know)
-# Here to stop this being duplicated all over the place.
-
-
-def moduleFactoryFactory(factory):
-    moduleCache = {}
-
-    def moduleFactory(baseModule, *args, **kwargs):
-        if isinstance(ModuleType.__name__, type("")):
-            name = "_%s_factory" % baseModule.__name__
-        else:
-            name = b"_%s_factory" % baseModule.__name__
-
-        kwargs_tuple = tuple(kwargs.items())
-
-        try:
-            return moduleCache[name][args][kwargs_tuple]
-        except KeyError:
-            mod = ModuleType(name)
-            objs = factory(baseModule, *args, **kwargs)
-            mod.__dict__.update(objs)
-            if "name" not in moduleCache:
-                moduleCache[name] = {}
-            if "args" not in moduleCache[name]:
-                moduleCache[name][args] = {}
-            if "kwargs" not in moduleCache[name][args]:
-                moduleCache[name][args][kwargs_tuple] = {}
-            moduleCache[name][args][kwargs_tuple] = mod
-            return mod
-
-    return moduleFactory
-
-
-def memoize(func):
-    cache = {}
-
-    def wrapped(*args, **kwargs):
-        key = (tuple(args), tuple(kwargs.items()))
-        if key not in cache:
-            cache[key] = func(*args, **kwargs)
-        return cache[key]
-
-    return wrapped
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/constants.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/constants.py
deleted file mode 100644
index 1ff8041..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/constants.py
+++ /dev/null
@@ -1,2947 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-import string
-
-EOF = None
-
-E = {
-    "null-character":
-        "Null character in input stream, replaced with U+FFFD.",
-    "invalid-codepoint":
-        "Invalid codepoint in stream.",
-    "incorrectly-placed-solidus":
-        "Solidus (/) incorrectly placed in tag.",
-    "incorrect-cr-newline-entity":
-        "Incorrect CR newline entity, replaced with LF.",
-    "illegal-windows-1252-entity":
-        "Entity used with illegal number (windows-1252 reference).",
-    "cant-convert-numeric-entity":
-        "Numeric entity couldn't be converted to character "
-        "(codepoint U+%(charAsInt)08x).",
-    "illegal-codepoint-for-numeric-entity":
-        "Numeric entity represents an illegal codepoint: "
-        "U+%(charAsInt)08x.",
-    "numeric-entity-without-semicolon":
-        "Numeric entity didn't end with ';'.",
-    "expected-numeric-entity-but-got-eof":
-        "Numeric entity expected. Got end of file instead.",
-    "expected-numeric-entity":
-        "Numeric entity expected but none found.",
-    "named-entity-without-semicolon":
-        "Named entity didn't end with ';'.",
-    "expected-named-entity":
-        "Named entity expected. Got none.",
-    "attributes-in-end-tag":
-        "End tag contains unexpected attributes.",
-    'self-closing-flag-on-end-tag':
-        "End tag contains unexpected self-closing flag.",
-    "expected-tag-name-but-got-right-bracket":
-        "Expected tag name. Got '>' instead.",
-    "expected-tag-name-but-got-question-mark":
-        "Expected tag name. Got '?' instead. (HTML doesn't "
-        "support processing instructions.)",
-    "expected-tag-name":
-        "Expected tag name. Got something else instead",
-    "expected-closing-tag-but-got-right-bracket":
-        "Expected closing tag. Got '>' instead. Ignoring '</>'.",
-    "expected-closing-tag-but-got-eof":
-        "Expected closing tag. Unexpected end of file.",
-    "expected-closing-tag-but-got-char":
-        "Expected closing tag. Unexpected character '%(data)s' found.",
-    "eof-in-tag-name":
-        "Unexpected end of file in the tag name.",
-    "expected-attribute-name-but-got-eof":
-        "Unexpected end of file. Expected attribute name instead.",
-    "eof-in-attribute-name":
-        "Unexpected end of file in attribute name.",
-    "invalid-character-in-attribute-name":
-        "Invalid character in attribute name",
-    "duplicate-attribute":
-        "Dropped duplicate attribute on tag.",
-    "expected-end-of-tag-name-but-got-eof":
-        "Unexpected end of file. Expected = or end of tag.",
-    "expected-attribute-value-but-got-eof":
-        "Unexpected end of file. Expected attribute value.",
-    "expected-attribute-value-but-got-right-bracket":
-        "Expected attribute value. Got '>' instead.",
-    'equals-in-unquoted-attribute-value':
-        "Unexpected = in unquoted attribute",
-    'unexpected-character-in-unquoted-attribute-value':
-        "Unexpected character in unquoted attribute",
-    "invalid-character-after-attribute-name":
-        "Unexpected character after attribute name.",
-    "unexpected-character-after-attribute-value":
-        "Unexpected character after attribute value.",
-    "eof-in-attribute-value-double-quote":
-        "Unexpected end of file in attribute value (\").",
-    "eof-in-attribute-value-single-quote":
-        "Unexpected end of file in attribute value (').",
-    "eof-in-attribute-value-no-quotes":
-        "Unexpected end of file in attribute value.",
-    "unexpected-EOF-after-solidus-in-tag":
-        "Unexpected end of file in tag. Expected >",
-    "unexpected-character-after-solidus-in-tag":
-        "Unexpected character after / in tag. Expected >",
-    "expected-dashes-or-doctype":
-        "Expected '--' or 'DOCTYPE'. Not found.",
-    "unexpected-bang-after-double-dash-in-comment":
-        "Unexpected ! after -- in comment",
-    "unexpected-space-after-double-dash-in-comment":
-        "Unexpected space after -- in comment",
-    "incorrect-comment":
-        "Incorrect comment.",
-    "eof-in-comment":
-        "Unexpected end of file in comment.",
-    "eof-in-comment-end-dash":
-        "Unexpected end of file in comment (-)",
-    "unexpected-dash-after-double-dash-in-comment":
-        "Unexpected '-' after '--' found in comment.",
-    "eof-in-comment-double-dash":
-        "Unexpected end of file in comment (--).",
-    "eof-in-comment-end-space-state":
-        "Unexpected end of file in comment.",
-    "eof-in-comment-end-bang-state":
-        "Unexpected end of file in comment.",
-    "unexpected-char-in-comment":
-        "Unexpected character in comment found.",
-    "need-space-after-doctype":
-        "No space after literal string 'DOCTYPE'.",
-    "expected-doctype-name-but-got-right-bracket":
-        "Unexpected > character. Expected DOCTYPE name.",
-    "expected-doctype-name-but-got-eof":
-        "Unexpected end of file. Expected DOCTYPE name.",
-    "eof-in-doctype-name":
-        "Unexpected end of file in DOCTYPE name.",
-    "eof-in-doctype":
-        "Unexpected end of file in DOCTYPE.",
-    "expected-space-or-right-bracket-in-doctype":
-        "Expected space or '>'. Got '%(data)s'",
-    "unexpected-end-of-doctype":
-        "Unexpected end of DOCTYPE.",
-    "unexpected-char-in-doctype":
-        "Unexpected character in DOCTYPE.",
-    "eof-in-innerhtml":
-        "XXX innerHTML EOF",
-    "unexpected-doctype":
-        "Unexpected DOCTYPE. Ignored.",
-    "non-html-root":
-        "html needs to be the first start tag.",
-    "expected-doctype-but-got-eof":
-        "Unexpected End of file. Expected DOCTYPE.",
-    "unknown-doctype":
-        "Erroneous DOCTYPE.",
-    "expected-doctype-but-got-chars":
-        "Unexpected non-space characters. Expected DOCTYPE.",
-    "expected-doctype-but-got-start-tag":
-        "Unexpected start tag (%(name)s). Expected DOCTYPE.",
-    "expected-doctype-but-got-end-tag":
-        "Unexpected end tag (%(name)s). Expected DOCTYPE.",
-    "end-tag-after-implied-root":
-        "Unexpected end tag (%(name)s) after the (implied) root element.",
-    "expected-named-closing-tag-but-got-eof":
-        "Unexpected end of file. Expected end tag (%(name)s).",
-    "two-heads-are-not-better-than-one":
-        "Unexpected start tag head in existing head. Ignored.",
-    "unexpected-end-tag":
-        "Unexpected end tag (%(name)s). Ignored.",
-    "unexpected-start-tag-out-of-my-head":
-        "Unexpected start tag (%(name)s) that can be in head. Moved.",
-    "unexpected-start-tag":
-        "Unexpected start tag (%(name)s).",
-    "missing-end-tag":
-        "Missing end tag (%(name)s).",
-    "missing-end-tags":
-        "Missing end tags (%(name)s).",
-    "unexpected-start-tag-implies-end-tag":
-        "Unexpected start tag (%(startName)s) "
-        "implies end tag (%(endName)s).",
-    "unexpected-start-tag-treated-as":
-        "Unexpected start tag (%(originalName)s). Treated as %(newName)s.",
-    "deprecated-tag":
-        "Unexpected start tag %(name)s. Don't use it!",
-    "unexpected-start-tag-ignored":
-        "Unexpected start tag %(name)s. Ignored.",
-    "expected-one-end-tag-but-got-another":
-        "Unexpected end tag (%(gotName)s). "
-        "Missing end tag (%(expectedName)s).",
-    "end-tag-too-early":
-        "End tag (%(name)s) seen too early. Expected other end tag.",
-    "end-tag-too-early-named":
-        "Unexpected end tag (%(gotName)s). Expected end tag (%(expectedName)s).",
-    "end-tag-too-early-ignored":
-        "End tag (%(name)s) seen too early. Ignored.",
-    "adoption-agency-1.1":
-        "End tag (%(name)s) violates step 1, "
-        "paragraph 1 of the adoption agency algorithm.",
-    "adoption-agency-1.2":
-        "End tag (%(name)s) violates step 1, "
-        "paragraph 2 of the adoption agency algorithm.",
-    "adoption-agency-1.3":
-        "End tag (%(name)s) violates step 1, "
-        "paragraph 3 of the adoption agency algorithm.",
-    "adoption-agency-4.4":
-        "End tag (%(name)s) violates step 4, "
-        "paragraph 4 of the adoption agency algorithm.",
-    "unexpected-end-tag-treated-as":
-        "Unexpected end tag (%(originalName)s). Treated as %(newName)s.",
-    "no-end-tag":
-        "This element (%(name)s) has no end tag.",
-    "unexpected-implied-end-tag-in-table":
-        "Unexpected implied end tag (%(name)s) in the table phase.",
-    "unexpected-implied-end-tag-in-table-body":
-        "Unexpected implied end tag (%(name)s) in the table body phase.",
-    "unexpected-char-implies-table-voodoo":
-        "Unexpected non-space characters in "
-        "table context caused voodoo mode.",
-    "unexpected-hidden-input-in-table":
-        "Unexpected input with type hidden in table context.",
-    "unexpected-form-in-table":
-        "Unexpected form in table context.",
-    "unexpected-start-tag-implies-table-voodoo":
-        "Unexpected start tag (%(name)s) in "
-        "table context caused voodoo mode.",
-    "unexpected-end-tag-implies-table-voodoo":
-        "Unexpected end tag (%(name)s) in "
-        "table context caused voodoo mode.",
-    "unexpected-cell-in-table-body":
-        "Unexpected table cell start tag (%(name)s) "
-        "in the table body phase.",
-    "unexpected-cell-end-tag":
-        "Got table cell end tag (%(name)s) "
-        "while required end tags are missing.",
-    "unexpected-end-tag-in-table-body":
-        "Unexpected end tag (%(name)s) in the table body phase. Ignored.",
-    "unexpected-implied-end-tag-in-table-row":
-        "Unexpected implied end tag (%(name)s) in the table row phase.",
-    "unexpected-end-tag-in-table-row":
-        "Unexpected end tag (%(name)s) in the table row phase. Ignored.",
-    "unexpected-select-in-select":
-        "Unexpected select start tag in the select phase "
-        "treated as select end tag.",
-    "unexpected-input-in-select":
-        "Unexpected input start tag in the select phase.",
-    "unexpected-start-tag-in-select":
-        "Unexpected start tag token (%(name)s in the select phase. "
-        "Ignored.",
-    "unexpected-end-tag-in-select":
-        "Unexpected end tag (%(name)s) in the select phase. Ignored.",
-    "unexpected-table-element-start-tag-in-select-in-table":
-        "Unexpected table element start tag (%(name)s) in the select in table phase.",
-    "unexpected-table-element-end-tag-in-select-in-table":
-        "Unexpected table element end tag (%(name)s) in the select in table phase.",
-    "unexpected-char-after-body":
-        "Unexpected non-space characters in the after body phase.",
-    "unexpected-start-tag-after-body":
-        "Unexpected start tag token (%(name)s)"
-        " in the after body phase.",
-    "unexpected-end-tag-after-body":
-        "Unexpected end tag token (%(name)s)"
-        " in the after body phase.",
-    "unexpected-char-in-frameset":
-        "Unexpected characters in the frameset phase. Characters ignored.",
-    "unexpected-start-tag-in-frameset":
-        "Unexpected start tag token (%(name)s)"
-        " in the frameset phase. Ignored.",
-    "unexpected-frameset-in-frameset-innerhtml":
-        "Unexpected end tag token (frameset) "
-        "in the frameset phase (innerHTML).",
-    "unexpected-end-tag-in-frameset":
-        "Unexpected end tag token (%(name)s)"
-        " in the frameset phase. Ignored.",
-    "unexpected-char-after-frameset":
-        "Unexpected non-space characters in the "
-        "after frameset phase. Ignored.",
-    "unexpected-start-tag-after-frameset":
-        "Unexpected start tag (%(name)s)"
-        " in the after frameset phase. Ignored.",
-    "unexpected-end-tag-after-frameset":
-        "Unexpected end tag (%(name)s)"
-        " in the after frameset phase. Ignored.",
-    "unexpected-end-tag-after-body-innerhtml":
-        "Unexpected end tag after body(innerHtml)",
-    "expected-eof-but-got-char":
-        "Unexpected non-space characters. Expected end of file.",
-    "expected-eof-but-got-start-tag":
-        "Unexpected start tag (%(name)s)"
-        ". Expected end of file.",
-    "expected-eof-but-got-end-tag":
-        "Unexpected end tag (%(name)s)"
-        ". Expected end of file.",
-    "eof-in-table":
-        "Unexpected end of file. Expected table content.",
-    "eof-in-select":
-        "Unexpected end of file. Expected select content.",
-    "eof-in-frameset":
-        "Unexpected end of file. Expected frameset content.",
-    "eof-in-script-in-script":
-        "Unexpected end of file. Expected script content.",
-    "eof-in-foreign-lands":
-        "Unexpected end of file. Expected foreign content",
-    "non-void-element-with-trailing-solidus":
-        "Trailing solidus not allowed on element %(name)s",
-    "unexpected-html-element-in-foreign-content":
-        "Element %(name)s not allowed in a non-html context",
-    "unexpected-end-tag-before-html":
-        "Unexpected end tag (%(name)s) before html.",
-    "unexpected-inhead-noscript-tag":
-        "Element %(name)s not allowed in a inhead-noscript context",
-    "eof-in-head-noscript":
-        "Unexpected end of file. Expected inhead-noscript content",
-    "char-in-head-noscript":
-        "Unexpected non-space character. Expected inhead-noscript content",
-    "XXX-undefined-error":
-        "Undefined error (this sucks and should be fixed)",
-}
-
-namespaces = {
-    "html": "http://www.w3.org/1999/xhtml",
-    "mathml": "http://www.w3.org/1998/Math/MathML",
-    "svg": "http://www.w3.org/2000/svg",
-    "xlink": "http://www.w3.org/1999/xlink",
-    "xml": "http://www.w3.org/XML/1998/namespace",
-    "xmlns": "http://www.w3.org/2000/xmlns/"
-}
-
-scopingElements = frozenset([
-    (namespaces["html"], "applet"),
-    (namespaces["html"], "caption"),
-    (namespaces["html"], "html"),
-    (namespaces["html"], "marquee"),
-    (namespaces["html"], "object"),
-    (namespaces["html"], "table"),
-    (namespaces["html"], "td"),
-    (namespaces["html"], "th"),
-    (namespaces["mathml"], "mi"),
-    (namespaces["mathml"], "mo"),
-    (namespaces["mathml"], "mn"),
-    (namespaces["mathml"], "ms"),
-    (namespaces["mathml"], "mtext"),
-    (namespaces["mathml"], "annotation-xml"),
-    (namespaces["svg"], "foreignObject"),
-    (namespaces["svg"], "desc"),
-    (namespaces["svg"], "title"),
-])
-
-formattingElements = frozenset([
-    (namespaces["html"], "a"),
-    (namespaces["html"], "b"),
-    (namespaces["html"], "big"),
-    (namespaces["html"], "code"),
-    (namespaces["html"], "em"),
-    (namespaces["html"], "font"),
-    (namespaces["html"], "i"),
-    (namespaces["html"], "nobr"),
-    (namespaces["html"], "s"),
-    (namespaces["html"], "small"),
-    (namespaces["html"], "strike"),
-    (namespaces["html"], "strong"),
-    (namespaces["html"], "tt"),
-    (namespaces["html"], "u")
-])
-
-specialElements = frozenset([
-    (namespaces["html"], "address"),
-    (namespaces["html"], "applet"),
-    (namespaces["html"], "area"),
-    (namespaces["html"], "article"),
-    (namespaces["html"], "aside"),
-    (namespaces["html"], "base"),
-    (namespaces["html"], "basefont"),
-    (namespaces["html"], "bgsound"),
-    (namespaces["html"], "blockquote"),
-    (namespaces["html"], "body"),
-    (namespaces["html"], "br"),
-    (namespaces["html"], "button"),
-    (namespaces["html"], "caption"),
-    (namespaces["html"], "center"),
-    (namespaces["html"], "col"),
-    (namespaces["html"], "colgroup"),
-    (namespaces["html"], "command"),
-    (namespaces["html"], "dd"),
-    (namespaces["html"], "details"),
-    (namespaces["html"], "dir"),
-    (namespaces["html"], "div"),
-    (namespaces["html"], "dl"),
-    (namespaces["html"], "dt"),
-    (namespaces["html"], "embed"),
-    (namespaces["html"], "fieldset"),
-    (namespaces["html"], "figure"),
-    (namespaces["html"], "footer"),
-    (namespaces["html"], "form"),
-    (namespaces["html"], "frame"),
-    (namespaces["html"], "frameset"),
-    (namespaces["html"], "h1"),
-    (namespaces["html"], "h2"),
-    (namespaces["html"], "h3"),
-    (namespaces["html"], "h4"),
-    (namespaces["html"], "h5"),
-    (namespaces["html"], "h6"),
-    (namespaces["html"], "head"),
-    (namespaces["html"], "header"),
-    (namespaces["html"], "hr"),
-    (namespaces["html"], "html"),
-    (namespaces["html"], "iframe"),
-    # Note that image is commented out in the spec as "this isn't an
-    # element that can end up on the stack, so it doesn't matter,"
-    (namespaces["html"], "image"),
-    (namespaces["html"], "img"),
-    (namespaces["html"], "input"),
-    (namespaces["html"], "isindex"),
-    (namespaces["html"], "li"),
-    (namespaces["html"], "link"),
-    (namespaces["html"], "listing"),
-    (namespaces["html"], "marquee"),
-    (namespaces["html"], "menu"),
-    (namespaces["html"], "meta"),
-    (namespaces["html"], "nav"),
-    (namespaces["html"], "noembed"),
-    (namespaces["html"], "noframes"),
-    (namespaces["html"], "noscript"),
-    (namespaces["html"], "object"),
-    (namespaces["html"], "ol"),
-    (namespaces["html"], "p"),
-    (namespaces["html"], "param"),
-    (namespaces["html"], "plaintext"),
-    (namespaces["html"], "pre"),
-    (namespaces["html"], "script"),
-    (namespaces["html"], "section"),
-    (namespaces["html"], "select"),
-    (namespaces["html"], "style"),
-    (namespaces["html"], "table"),
-    (namespaces["html"], "tbody"),
-    (namespaces["html"], "td"),
-    (namespaces["html"], "textarea"),
-    (namespaces["html"], "tfoot"),
-    (namespaces["html"], "th"),
-    (namespaces["html"], "thead"),
-    (namespaces["html"], "title"),
-    (namespaces["html"], "tr"),
-    (namespaces["html"], "ul"),
-    (namespaces["html"], "wbr"),
-    (namespaces["html"], "xmp"),
-    (namespaces["svg"], "foreignObject")
-])
-
-htmlIntegrationPointElements = frozenset([
-    (namespaces["mathml"], "annotation-xml"),
-    (namespaces["svg"], "foreignObject"),
-    (namespaces["svg"], "desc"),
-    (namespaces["svg"], "title")
-])
-
-mathmlTextIntegrationPointElements = frozenset([
-    (namespaces["mathml"], "mi"),
-    (namespaces["mathml"], "mo"),
-    (namespaces["mathml"], "mn"),
-    (namespaces["mathml"], "ms"),
-    (namespaces["mathml"], "mtext")
-])
-
-adjustSVGAttributes = {
-    "attributename": "attributeName",
-    "attributetype": "attributeType",
-    "basefrequency": "baseFrequency",
-    "baseprofile": "baseProfile",
-    "calcmode": "calcMode",
-    "clippathunits": "clipPathUnits",
-    "contentscripttype": "contentScriptType",
-    "contentstyletype": "contentStyleType",
-    "diffuseconstant": "diffuseConstant",
-    "edgemode": "edgeMode",
-    "externalresourcesrequired": "externalResourcesRequired",
-    "filterres": "filterRes",
-    "filterunits": "filterUnits",
-    "glyphref": "glyphRef",
-    "gradienttransform": "gradientTransform",
-    "gradientunits": "gradientUnits",
-    "kernelmatrix": "kernelMatrix",
-    "kernelunitlength": "kernelUnitLength",
-    "keypoints": "keyPoints",
-    "keysplines": "keySplines",
-    "keytimes": "keyTimes",
-    "lengthadjust": "lengthAdjust",
-    "limitingconeangle": "limitingConeAngle",
-    "markerheight": "markerHeight",
-    "markerunits": "markerUnits",
-    "markerwidth": "markerWidth",
-    "maskcontentunits": "maskContentUnits",
-    "maskunits": "maskUnits",
-    "numoctaves": "numOctaves",
-    "pathlength": "pathLength",
-    "patterncontentunits": "patternContentUnits",
-    "patterntransform": "patternTransform",
-    "patternunits": "patternUnits",
-    "pointsatx": "pointsAtX",
-    "pointsaty": "pointsAtY",
-    "pointsatz": "pointsAtZ",
-    "preservealpha": "preserveAlpha",
-    "preserveaspectratio": "preserveAspectRatio",
-    "primitiveunits": "primitiveUnits",
-    "refx": "refX",
-    "refy": "refY",
-    "repeatcount": "repeatCount",
-    "repeatdur": "repeatDur",
-    "requiredextensions": "requiredExtensions",
-    "requiredfeatures": "requiredFeatures",
-    "specularconstant": "specularConstant",
-    "specularexponent": "specularExponent",
-    "spreadmethod": "spreadMethod",
-    "startoffset": "startOffset",
-    "stddeviation": "stdDeviation",
-    "stitchtiles": "stitchTiles",
-    "surfacescale": "surfaceScale",
-    "systemlanguage": "systemLanguage",
-    "tablevalues": "tableValues",
-    "targetx": "targetX",
-    "targety": "targetY",
-    "textlength": "textLength",
-    "viewbox": "viewBox",
-    "viewtarget": "viewTarget",
-    "xchannelselector": "xChannelSelector",
-    "ychannelselector": "yChannelSelector",
-    "zoomandpan": "zoomAndPan"
-}
-
-adjustMathMLAttributes = {"definitionurl": "definitionURL"}
-
-adjustForeignAttributes = {
-    "xlink:actuate": ("xlink", "actuate", namespaces["xlink"]),
-    "xlink:arcrole": ("xlink", "arcrole", namespaces["xlink"]),
-    "xlink:href": ("xlink", "href", namespaces["xlink"]),
-    "xlink:role": ("xlink", "role", namespaces["xlink"]),
-    "xlink:show": ("xlink", "show", namespaces["xlink"]),
-    "xlink:title": ("xlink", "title", namespaces["xlink"]),
-    "xlink:type": ("xlink", "type", namespaces["xlink"]),
-    "xml:base": ("xml", "base", namespaces["xml"]),
-    "xml:lang": ("xml", "lang", namespaces["xml"]),
-    "xml:space": ("xml", "space", namespaces["xml"]),
-    "xmlns": (None, "xmlns", namespaces["xmlns"]),
-    "xmlns:xlink": ("xmlns", "xlink", namespaces["xmlns"])
-}
-
-unadjustForeignAttributes = dict([((ns, local), qname) for qname, (prefix, local, ns) in
-                                  adjustForeignAttributes.items()])
-
-spaceCharacters = frozenset([
-    "\t",
-    "\n",
-    "\u000C",
-    " ",
-    "\r"
-])
-
-tableInsertModeElements = frozenset([
-    "table",
-    "tbody",
-    "tfoot",
-    "thead",
-    "tr"
-])
-
-asciiLowercase = frozenset(string.ascii_lowercase)
-asciiUppercase = frozenset(string.ascii_uppercase)
-asciiLetters = frozenset(string.ascii_letters)
-digits = frozenset(string.digits)
-hexDigits = frozenset(string.hexdigits)
-
-asciiUpper2Lower = dict([(ord(c), ord(c.lower()))
-                         for c in string.ascii_uppercase])
-
-# Heading elements need to be ordered
-headingElements = (
-    "h1",
-    "h2",
-    "h3",
-    "h4",
-    "h5",
-    "h6"
-)
-
-voidElements = frozenset([
-    "base",
-    "command",
-    "event-source",
-    "link",
-    "meta",
-    "hr",
-    "br",
-    "img",
-    "embed",
-    "param",
-    "area",
-    "col",
-    "input",
-    "source",
-    "track"
-])
-
-cdataElements = frozenset(['title', 'textarea'])
-
-rcdataElements = frozenset([
-    'style',
-    'script',
-    'xmp',
-    'iframe',
-    'noembed',
-    'noframes',
-    'noscript'
-])
-
-booleanAttributes = {
-    "": frozenset(["irrelevant", "itemscope"]),
-    "style": frozenset(["scoped"]),
-    "img": frozenset(["ismap"]),
-    "audio": frozenset(["autoplay", "controls"]),
-    "video": frozenset(["autoplay", "controls"]),
-    "script": frozenset(["defer", "async"]),
-    "details": frozenset(["open"]),
-    "datagrid": frozenset(["multiple", "disabled"]),
-    "command": frozenset(["hidden", "disabled", "checked", "default"]),
-    "hr": frozenset(["noshade"]),
-    "menu": frozenset(["autosubmit"]),
-    "fieldset": frozenset(["disabled", "readonly"]),
-    "option": frozenset(["disabled", "readonly", "selected"]),
-    "optgroup": frozenset(["disabled", "readonly"]),
-    "button": frozenset(["disabled", "autofocus"]),
-    "input": frozenset(["disabled", "readonly", "required", "autofocus", "checked", "ismap"]),
-    "select": frozenset(["disabled", "readonly", "autofocus", "multiple"]),
-    "output": frozenset(["disabled", "readonly"]),
-    "iframe": frozenset(["seamless"]),
-}
-
-# entitiesWindows1252 has to be _ordered_ and needs to have an index. It
-# therefore can't be a frozenset.
-entitiesWindows1252 = (
-    8364,   # 0x80  0x20AC  EURO SIGN
-    65533,  # 0x81          UNDEFINED
-    8218,   # 0x82  0x201A  SINGLE LOW-9 QUOTATION MARK
-    402,    # 0x83  0x0192  LATIN SMALL LETTER F WITH HOOK
-    8222,   # 0x84  0x201E  DOUBLE LOW-9 QUOTATION MARK
-    8230,   # 0x85  0x2026  HORIZONTAL ELLIPSIS
-    8224,   # 0x86  0x2020  DAGGER
-    8225,   # 0x87  0x2021  DOUBLE DAGGER
-    710,    # 0x88  0x02C6  MODIFIER LETTER CIRCUMFLEX ACCENT
-    8240,   # 0x89  0x2030  PER MILLE SIGN
-    352,    # 0x8A  0x0160  LATIN CAPITAL LETTER S WITH CARON
-    8249,   # 0x8B  0x2039  SINGLE LEFT-POINTING ANGLE QUOTATION MARK
-    338,    # 0x8C  0x0152  LATIN CAPITAL LIGATURE OE
-    65533,  # 0x8D          UNDEFINED
-    381,    # 0x8E  0x017D  LATIN CAPITAL LETTER Z WITH CARON
-    65533,  # 0x8F          UNDEFINED
-    65533,  # 0x90          UNDEFINED
-    8216,   # 0x91  0x2018  LEFT SINGLE QUOTATION MARK
-    8217,   # 0x92  0x2019  RIGHT SINGLE QUOTATION MARK
-    8220,   # 0x93  0x201C  LEFT DOUBLE QUOTATION MARK
-    8221,   # 0x94  0x201D  RIGHT DOUBLE QUOTATION MARK
-    8226,   # 0x95  0x2022  BULLET
-    8211,   # 0x96  0x2013  EN DASH
-    8212,   # 0x97  0x2014  EM DASH
-    732,    # 0x98  0x02DC  SMALL TILDE
-    8482,   # 0x99  0x2122  TRADE MARK SIGN
-    353,    # 0x9A  0x0161  LATIN SMALL LETTER S WITH CARON
-    8250,   # 0x9B  0x203A  SINGLE RIGHT-POINTING ANGLE QUOTATION MARK
-    339,    # 0x9C  0x0153  LATIN SMALL LIGATURE OE
-    65533,  # 0x9D          UNDEFINED
-    382,    # 0x9E  0x017E  LATIN SMALL LETTER Z WITH CARON
-    376     # 0x9F  0x0178  LATIN CAPITAL LETTER Y WITH DIAERESIS
-)
-
-xmlEntities = frozenset(['lt;', 'gt;', 'amp;', 'apos;', 'quot;'])
-
-entities = {
-    "AElig": "\xc6",
-    "AElig;": "\xc6",
-    "AMP": "&",
-    "AMP;": "&",
-    "Aacute": "\xc1",
-    "Aacute;": "\xc1",
-    "Abreve;": "\u0102",
-    "Acirc": "\xc2",
-    "Acirc;": "\xc2",
-    "Acy;": "\u0410",
-    "Afr;": "\U0001d504",
-    "Agrave": "\xc0",
-    "Agrave;": "\xc0",
-    "Alpha;": "\u0391",
-    "Amacr;": "\u0100",
-    "And;": "\u2a53",
-    "Aogon;": "\u0104",
-    "Aopf;": "\U0001d538",
-    "ApplyFunction;": "\u2061",
-    "Aring": "\xc5",
-    "Aring;": "\xc5",
-    "Ascr;": "\U0001d49c",
-    "Assign;": "\u2254",
-    "Atilde": "\xc3",
-    "Atilde;": "\xc3",
-    "Auml": "\xc4",
-    "Auml;": "\xc4",
-    "Backslash;": "\u2216",
-    "Barv;": "\u2ae7",
-    "Barwed;": "\u2306",
-    "Bcy;": "\u0411",
-    "Because;": "\u2235",
-    "Bernoullis;": "\u212c",
-    "Beta;": "\u0392",
-    "Bfr;": "\U0001d505",
-    "Bopf;": "\U0001d539",
-    "Breve;": "\u02d8",
-    "Bscr;": "\u212c",
-    "Bumpeq;": "\u224e",
-    "CHcy;": "\u0427",
-    "COPY": "\xa9",
-    "COPY;": "\xa9",
-    "Cacute;": "\u0106",
-    "Cap;": "\u22d2",
-    "CapitalDifferentialD;": "\u2145",
-    "Cayleys;": "\u212d",
-    "Ccaron;": "\u010c",
-    "Ccedil": "\xc7",
-    "Ccedil;": "\xc7",
-    "Ccirc;": "\u0108",
-    "Cconint;": "\u2230",
-    "Cdot;": "\u010a",
-    "Cedilla;": "\xb8",
-    "CenterDot;": "\xb7",
-    "Cfr;": "\u212d",
-    "Chi;": "\u03a7",
-    "CircleDot;": "\u2299",
-    "CircleMinus;": "\u2296",
-    "CirclePlus;": "\u2295",
-    "CircleTimes;": "\u2297",
-    "ClockwiseContourIntegral;": "\u2232",
-    "CloseCurlyDoubleQuote;": "\u201d",
-    "CloseCurlyQuote;": "\u2019",
-    "Colon;": "\u2237",
-    "Colone;": "\u2a74",
-    "Congruent;": "\u2261",
-    "Conint;": "\u222f",
-    "ContourIntegral;": "\u222e",
-    "Copf;": "\u2102",
-    "Coproduct;": "\u2210",
-    "CounterClockwiseContourIntegral;": "\u2233",
-    "Cross;": "\u2a2f",
-    "Cscr;": "\U0001d49e",
-    "Cup;": "\u22d3",
-    "CupCap;": "\u224d",
-    "DD;": "\u2145",
-    "DDotrahd;": "\u2911",
-    "DJcy;": "\u0402",
-    "DScy;": "\u0405",
-    "DZcy;": "\u040f",
-    "Dagger;": "\u2021",
-    "Darr;": "\u21a1",
-    "Dashv;": "\u2ae4",
-    "Dcaron;": "\u010e",
-    "Dcy;": "\u0414",
-    "Del;": "\u2207",
-    "Delta;": "\u0394",
-    "Dfr;": "\U0001d507",
-    "DiacriticalAcute;": "\xb4",
-    "DiacriticalDot;": "\u02d9",
-    "DiacriticalDoubleAcute;": "\u02dd",
-    "DiacriticalGrave;": "`",
-    "DiacriticalTilde;": "\u02dc",
-    "Diamond;": "\u22c4",
-    "DifferentialD;": "\u2146",
-    "Dopf;": "\U0001d53b",
-    "Dot;": "\xa8",
-    "DotDot;": "\u20dc",
-    "DotEqual;": "\u2250",
-    "DoubleContourIntegral;": "\u222f",
-    "DoubleDot;": "\xa8",
-    "DoubleDownArrow;": "\u21d3",
-    "DoubleLeftArrow;": "\u21d0",
-    "DoubleLeftRightArrow;": "\u21d4",
-    "DoubleLeftTee;": "\u2ae4",
-    "DoubleLongLeftArrow;": "\u27f8",
-    "DoubleLongLeftRightArrow;": "\u27fa",
-    "DoubleLongRightArrow;": "\u27f9",
-    "DoubleRightArrow;": "\u21d2",
-    "DoubleRightTee;": "\u22a8",
-    "DoubleUpArrow;": "\u21d1",
-    "DoubleUpDownArrow;": "\u21d5",
-    "DoubleVerticalBar;": "\u2225",
-    "DownArrow;": "\u2193",
-    "DownArrowBar;": "\u2913",
-    "DownArrowUpArrow;": "\u21f5",
-    "DownBreve;": "\u0311",
-    "DownLeftRightVector;": "\u2950",
-    "DownLeftTeeVector;": "\u295e",
-    "DownLeftVector;": "\u21bd",
-    "DownLeftVectorBar;": "\u2956",
-    "DownRightTeeVector;": "\u295f",
-    "DownRightVector;": "\u21c1",
-    "DownRightVectorBar;": "\u2957",
-    "DownTee;": "\u22a4",
-    "DownTeeArrow;": "\u21a7",
-    "Downarrow;": "\u21d3",
-    "Dscr;": "\U0001d49f",
-    "Dstrok;": "\u0110",
-    "ENG;": "\u014a",
-    "ETH": "\xd0",
-    "ETH;": "\xd0",
-    "Eacute": "\xc9",
-    "Eacute;": "\xc9",
-    "Ecaron;": "\u011a",
-    "Ecirc": "\xca",
-    "Ecirc;": "\xca",
-    "Ecy;": "\u042d",
-    "Edot;": "\u0116",
-    "Efr;": "\U0001d508",
-    "Egrave": "\xc8",
-    "Egrave;": "\xc8",
-    "Element;": "\u2208",
-    "Emacr;": "\u0112",
-    "EmptySmallSquare;": "\u25fb",
-    "EmptyVerySmallSquare;": "\u25ab",
-    "Eogon;": "\u0118",
-    "Eopf;": "\U0001d53c",
-    "Epsilon;": "\u0395",
-    "Equal;": "\u2a75",
-    "EqualTilde;": "\u2242",
-    "Equilibrium;": "\u21cc",
-    "Escr;": "\u2130",
-    "Esim;": "\u2a73",
-    "Eta;": "\u0397",
-    "Euml": "\xcb",
-    "Euml;": "\xcb",
-    "Exists;": "\u2203",
-    "ExponentialE;": "\u2147",
-    "Fcy;": "\u0424",
-    "Ffr;": "\U0001d509",
-    "FilledSmallSquare;": "\u25fc",
-    "FilledVerySmallSquare;": "\u25aa",
-    "Fopf;": "\U0001d53d",
-    "ForAll;": "\u2200",
-    "Fouriertrf;": "\u2131",
-    "Fscr;": "\u2131",
-    "GJcy;": "\u0403",
-    "GT": ">",
-    "GT;": ">",
-    "Gamma;": "\u0393",
-    "Gammad;": "\u03dc",
-    "Gbreve;": "\u011e",
-    "Gcedil;": "\u0122",
-    "Gcirc;": "\u011c",
-    "Gcy;": "\u0413",
-    "Gdot;": "\u0120",
-    "Gfr;": "\U0001d50a",
-    "Gg;": "\u22d9",
-    "Gopf;": "\U0001d53e",
-    "GreaterEqual;": "\u2265",
-    "GreaterEqualLess;": "\u22db",
-    "GreaterFullEqual;": "\u2267",
-    "GreaterGreater;": "\u2aa2",
-    "GreaterLess;": "\u2277",
-    "GreaterSlantEqual;": "\u2a7e",
-    "GreaterTilde;": "\u2273",
-    "Gscr;": "\U0001d4a2",
-    "Gt;": "\u226b",
-    "HARDcy;": "\u042a",
-    "Hacek;": "\u02c7",
-    "Hat;": "^",
-    "Hcirc;": "\u0124",
-    "Hfr;": "\u210c",
-    "HilbertSpace;": "\u210b",
-    "Hopf;": "\u210d",
-    "HorizontalLine;": "\u2500",
-    "Hscr;": "\u210b",
-    "Hstrok;": "\u0126",
-    "HumpDownHump;": "\u224e",
-    "HumpEqual;": "\u224f",
-    "IEcy;": "\u0415",
-    "IJlig;": "\u0132",
-    "IOcy;": "\u0401",
-    "Iacute": "\xcd",
-    "Iacute;": "\xcd",
-    "Icirc": "\xce",
-    "Icirc;": "\xce",
-    "Icy;": "\u0418",
-    "Idot;": "\u0130",
-    "Ifr;": "\u2111",
-    "Igrave": "\xcc",
-    "Igrave;": "\xcc",
-    "Im;": "\u2111",
-    "Imacr;": "\u012a",
-    "ImaginaryI;": "\u2148",
-    "Implies;": "\u21d2",
-    "Int;": "\u222c",
-    "Integral;": "\u222b",
-    "Intersection;": "\u22c2",
-    "InvisibleComma;": "\u2063",
-    "InvisibleTimes;": "\u2062",
-    "Iogon;": "\u012e",
-    "Iopf;": "\U0001d540",
-    "Iota;": "\u0399",
-    "Iscr;": "\u2110",
-    "Itilde;": "\u0128",
-    "Iukcy;": "\u0406",
-    "Iuml": "\xcf",
-    "Iuml;": "\xcf",
-    "Jcirc;": "\u0134",
-    "Jcy;": "\u0419",
-    "Jfr;": "\U0001d50d",
-    "Jopf;": "\U0001d541",
-    "Jscr;": "\U0001d4a5",
-    "Jsercy;": "\u0408",
-    "Jukcy;": "\u0404",
-    "KHcy;": "\u0425",
-    "KJcy;": "\u040c",
-    "Kappa;": "\u039a",
-    "Kcedil;": "\u0136",
-    "Kcy;": "\u041a",
-    "Kfr;": "\U0001d50e",
-    "Kopf;": "\U0001d542",
-    "Kscr;": "\U0001d4a6",
-    "LJcy;": "\u0409",
-    "LT": "<",
-    "LT;": "<",
-    "Lacute;": "\u0139",
-    "Lambda;": "\u039b",
-    "Lang;": "\u27ea",
-    "Laplacetrf;": "\u2112",
-    "Larr;": "\u219e",
-    "Lcaron;": "\u013d",
-    "Lcedil;": "\u013b",
-    "Lcy;": "\u041b",
-    "LeftAngleBracket;": "\u27e8",
-    "LeftArrow;": "\u2190",
-    "LeftArrowBar;": "\u21e4",
-    "LeftArrowRightArrow;": "\u21c6",
-    "LeftCeiling;": "\u2308",
-    "LeftDoubleBracket;": "\u27e6",
-    "LeftDownTeeVector;": "\u2961",
-    "LeftDownVector;": "\u21c3",
-    "LeftDownVectorBar;": "\u2959",
-    "LeftFloor;": "\u230a",
-    "LeftRightArrow;": "\u2194",
-    "LeftRightVector;": "\u294e",
-    "LeftTee;": "\u22a3",
-    "LeftTeeArrow;": "\u21a4",
-    "LeftTeeVector;": "\u295a",
-    "LeftTriangle;": "\u22b2",
-    "LeftTriangleBar;": "\u29cf",
-    "LeftTriangleEqual;": "\u22b4",
-    "LeftUpDownVector;": "\u2951",
-    "LeftUpTeeVector;": "\u2960",
-    "LeftUpVector;": "\u21bf",
-    "LeftUpVectorBar;": "\u2958",
-    "LeftVector;": "\u21bc",
-    "LeftVectorBar;": "\u2952",
-    "Leftarrow;": "\u21d0",
-    "Leftrightarrow;": "\u21d4",
-    "LessEqualGreater;": "\u22da",
-    "LessFullEqual;": "\u2266",
-    "LessGreater;": "\u2276",
-    "LessLess;": "\u2aa1",
-    "LessSlantEqual;": "\u2a7d",
-    "LessTilde;": "\u2272",
-    "Lfr;": "\U0001d50f",
-    "Ll;": "\u22d8",
-    "Lleftarrow;": "\u21da",
-    "Lmidot;": "\u013f",
-    "LongLeftArrow;": "\u27f5",
-    "LongLeftRightArrow;": "\u27f7",
-    "LongRightArrow;": "\u27f6",
-    "Longleftarrow;": "\u27f8",
-    "Longleftrightarrow;": "\u27fa",
-    "Longrightarrow;": "\u27f9",
-    "Lopf;": "\U0001d543",
-    "LowerLeftArrow;": "\u2199",
-    "LowerRightArrow;": "\u2198",
-    "Lscr;": "\u2112",
-    "Lsh;": "\u21b0",
-    "Lstrok;": "\u0141",
-    "Lt;": "\u226a",
-    "Map;": "\u2905",
-    "Mcy;": "\u041c",
-    "MediumSpace;": "\u205f",
-    "Mellintrf;": "\u2133",
-    "Mfr;": "\U0001d510",
-    "MinusPlus;": "\u2213",
-    "Mopf;": "\U0001d544",
-    "Mscr;": "\u2133",
-    "Mu;": "\u039c",
-    "NJcy;": "\u040a",
-    "Nacute;": "\u0143",
-    "Ncaron;": "\u0147",
-    "Ncedil;": "\u0145",
-    "Ncy;": "\u041d",
-    "NegativeMediumSpace;": "\u200b",
-    "NegativeThickSpace;": "\u200b",
-    "NegativeThinSpace;": "\u200b",
-    "NegativeVeryThinSpace;": "\u200b",
-    "NestedGreaterGreater;": "\u226b",
-    "NestedLessLess;": "\u226a",
-    "NewLine;": "\n",
-    "Nfr;": "\U0001d511",
-    "NoBreak;": "\u2060",
-    "NonBreakingSpace;": "\xa0",
-    "Nopf;": "\u2115",
-    "Not;": "\u2aec",
-    "NotCongruent;": "\u2262",
-    "NotCupCap;": "\u226d",
-    "NotDoubleVerticalBar;": "\u2226",
-    "NotElement;": "\u2209",
-    "NotEqual;": "\u2260",
-    "NotEqualTilde;": "\u2242\u0338",
-    "NotExists;": "\u2204",
-    "NotGreater;": "\u226f",
-    "NotGreaterEqual;": "\u2271",
-    "NotGreaterFullEqual;": "\u2267\u0338",
-    "NotGreaterGreater;": "\u226b\u0338",
-    "NotGreaterLess;": "\u2279",
-    "NotGreaterSlantEqual;": "\u2a7e\u0338",
-    "NotGreaterTilde;": "\u2275",
-    "NotHumpDownHump;": "\u224e\u0338",
-    "NotHumpEqual;": "\u224f\u0338",
-    "NotLeftTriangle;": "\u22ea",
-    "NotLeftTriangleBar;": "\u29cf\u0338",
-    "NotLeftTriangleEqual;": "\u22ec",
-    "NotLess;": "\u226e",
-    "NotLessEqual;": "\u2270",
-    "NotLessGreater;": "\u2278",
-    "NotLessLess;": "\u226a\u0338",
-    "NotLessSlantEqual;": "\u2a7d\u0338",
-    "NotLessTilde;": "\u2274",
-    "NotNestedGreaterGreater;": "\u2aa2\u0338",
-    "NotNestedLessLess;": "\u2aa1\u0338",
-    "NotPrecedes;": "\u2280",
-    "NotPrecedesEqual;": "\u2aaf\u0338",
-    "NotPrecedesSlantEqual;": "\u22e0",
-    "NotReverseElement;": "\u220c",
-    "NotRightTriangle;": "\u22eb",
-    "NotRightTriangleBar;": "\u29d0\u0338",
-    "NotRightTriangleEqual;": "\u22ed",
-    "NotSquareSubset;": "\u228f\u0338",
-    "NotSquareSubsetEqual;": "\u22e2",
-    "NotSquareSuperset;": "\u2290\u0338",
-    "NotSquareSupersetEqual;": "\u22e3",
-    "NotSubset;": "\u2282\u20d2",
-    "NotSubsetEqual;": "\u2288",
-    "NotSucceeds;": "\u2281",
-    "NotSucceedsEqual;": "\u2ab0\u0338",
-    "NotSucceedsSlantEqual;": "\u22e1",
-    "NotSucceedsTilde;": "\u227f\u0338",
-    "NotSuperset;": "\u2283\u20d2",
-    "NotSupersetEqual;": "\u2289",
-    "NotTilde;": "\u2241",
-    "NotTildeEqual;": "\u2244",
-    "NotTildeFullEqual;": "\u2247",
-    "NotTildeTilde;": "\u2249",
-    "NotVerticalBar;": "\u2224",
-    "Nscr;": "\U0001d4a9",
-    "Ntilde": "\xd1",
-    "Ntilde;": "\xd1",
-    "Nu;": "\u039d",
-    "OElig;": "\u0152",
-    "Oacute": "\xd3",
-    "Oacute;": "\xd3",
-    "Ocirc": "\xd4",
-    "Ocirc;": "\xd4",
-    "Ocy;": "\u041e",
-    "Odblac;": "\u0150",
-    "Ofr;": "\U0001d512",
-    "Ograve": "\xd2",
-    "Ograve;": "\xd2",
-    "Omacr;": "\u014c",
-    "Omega;": "\u03a9",
-    "Omicron;": "\u039f",
-    "Oopf;": "\U0001d546",
-    "OpenCurlyDoubleQuote;": "\u201c",
-    "OpenCurlyQuote;": "\u2018",
-    "Or;": "\u2a54",
-    "Oscr;": "\U0001d4aa",
-    "Oslash": "\xd8",
-    "Oslash;": "\xd8",
-    "Otilde": "\xd5",
-    "Otilde;": "\xd5",
-    "Otimes;": "\u2a37",
-    "Ouml": "\xd6",
-    "Ouml;": "\xd6",
-    "OverBar;": "\u203e",
-    "OverBrace;": "\u23de",
-    "OverBracket;": "\u23b4",
-    "OverParenthesis;": "\u23dc",
-    "PartialD;": "\u2202",
-    "Pcy;": "\u041f",
-    "Pfr;": "\U0001d513",
-    "Phi;": "\u03a6",
-    "Pi;": "\u03a0",
-    "PlusMinus;": "\xb1",
-    "Poincareplane;": "\u210c",
-    "Popf;": "\u2119",
-    "Pr;": "\u2abb",
-    "Precedes;": "\u227a",
-    "PrecedesEqual;": "\u2aaf",
-    "PrecedesSlantEqual;": "\u227c",
-    "PrecedesTilde;": "\u227e",
-    "Prime;": "\u2033",
-    "Product;": "\u220f",
-    "Proportion;": "\u2237",
-    "Proportional;": "\u221d",
-    "Pscr;": "\U0001d4ab",
-    "Psi;": "\u03a8",
-    "QUOT": "\"",
-    "QUOT;": "\"",
-    "Qfr;": "\U0001d514",
-    "Qopf;": "\u211a",
-    "Qscr;": "\U0001d4ac",
-    "RBarr;": "\u2910",
-    "REG": "\xae",
-    "REG;": "\xae",
-    "Racute;": "\u0154",
-    "Rang;": "\u27eb",
-    "Rarr;": "\u21a0",
-    "Rarrtl;": "\u2916",
-    "Rcaron;": "\u0158",
-    "Rcedil;": "\u0156",
-    "Rcy;": "\u0420",
-    "Re;": "\u211c",
-    "ReverseElement;": "\u220b",
-    "ReverseEquilibrium;": "\u21cb",
-    "ReverseUpEquilibrium;": "\u296f",
-    "Rfr;": "\u211c",
-    "Rho;": "\u03a1",
-    "RightAngleBracket;": "\u27e9",
-    "RightArrow;": "\u2192",
-    "RightArrowBar;": "\u21e5",
-    "RightArrowLeftArrow;": "\u21c4",
-    "RightCeiling;": "\u2309",
-    "RightDoubleBracket;": "\u27e7",
-    "RightDownTeeVector;": "\u295d",
-    "RightDownVector;": "\u21c2",
-    "RightDownVectorBar;": "\u2955",
-    "RightFloor;": "\u230b",
-    "RightTee;": "\u22a2",
-    "RightTeeArrow;": "\u21a6",
-    "RightTeeVector;": "\u295b",
-    "RightTriangle;": "\u22b3",
-    "RightTriangleBar;": "\u29d0",
-    "RightTriangleEqual;": "\u22b5",
-    "RightUpDownVector;": "\u294f",
-    "RightUpTeeVector;": "\u295c",
-    "RightUpVector;": "\u21be",
-    "RightUpVectorBar;": "\u2954",
-    "RightVector;": "\u21c0",
-    "RightVectorBar;": "\u2953",
-    "Rightarrow;": "\u21d2",
-    "Ropf;": "\u211d",
-    "RoundImplies;": "\u2970",
-    "Rrightarrow;": "\u21db",
-    "Rscr;": "\u211b",
-    "Rsh;": "\u21b1",
-    "RuleDelayed;": "\u29f4",
-    "SHCHcy;": "\u0429",
-    "SHcy;": "\u0428",
-    "SOFTcy;": "\u042c",
-    "Sacute;": "\u015a",
-    "Sc;": "\u2abc",
-    "Scaron;": "\u0160",
-    "Scedil;": "\u015e",
-    "Scirc;": "\u015c",
-    "Scy;": "\u0421",
-    "Sfr;": "\U0001d516",
-    "ShortDownArrow;": "\u2193",
-    "ShortLeftArrow;": "\u2190",
-    "ShortRightArrow;": "\u2192",
-    "ShortUpArrow;": "\u2191",
-    "Sigma;": "\u03a3",
-    "SmallCircle;": "\u2218",
-    "Sopf;": "\U0001d54a",
-    "Sqrt;": "\u221a",
-    "Square;": "\u25a1",
-    "SquareIntersection;": "\u2293",
-    "SquareSubset;": "\u228f",
-    "SquareSubsetEqual;": "\u2291",
-    "SquareSuperset;": "\u2290",
-    "SquareSupersetEqual;": "\u2292",
-    "SquareUnion;": "\u2294",
-    "Sscr;": "\U0001d4ae",
-    "Star;": "\u22c6",
-    "Sub;": "\u22d0",
-    "Subset;": "\u22d0",
-    "SubsetEqual;": "\u2286",
-    "Succeeds;": "\u227b",
-    "SucceedsEqual;": "\u2ab0",
-    "SucceedsSlantEqual;": "\u227d",
-    "SucceedsTilde;": "\u227f",
-    "SuchThat;": "\u220b",
-    "Sum;": "\u2211",
-    "Sup;": "\u22d1",
-    "Superset;": "\u2283",
-    "SupersetEqual;": "\u2287",
-    "Supset;": "\u22d1",
-    "THORN": "\xde",
-    "THORN;": "\xde",
-    "TRADE;": "\u2122",
-    "TSHcy;": "\u040b",
-    "TScy;": "\u0426",
-    "Tab;": "\t",
-    "Tau;": "\u03a4",
-    "Tcaron;": "\u0164",
-    "Tcedil;": "\u0162",
-    "Tcy;": "\u0422",
-    "Tfr;": "\U0001d517",
-    "Therefore;": "\u2234",
-    "Theta;": "\u0398",
-    "ThickSpace;": "\u205f\u200a",
-    "ThinSpace;": "\u2009",
-    "Tilde;": "\u223c",
-    "TildeEqual;": "\u2243",
-    "TildeFullEqual;": "\u2245",
-    "TildeTilde;": "\u2248",
-    "Topf;": "\U0001d54b",
-    "TripleDot;": "\u20db",
-    "Tscr;": "\U0001d4af",
-    "Tstrok;": "\u0166",
-    "Uacute": "\xda",
-    "Uacute;": "\xda",
-    "Uarr;": "\u219f",
-    "Uarrocir;": "\u2949",
-    "Ubrcy;": "\u040e",
-    "Ubreve;": "\u016c",
-    "Ucirc": "\xdb",
-    "Ucirc;": "\xdb",
-    "Ucy;": "\u0423",
-    "Udblac;": "\u0170",
-    "Ufr;": "\U0001d518",
-    "Ugrave": "\xd9",
-    "Ugrave;": "\xd9",
-    "Umacr;": "\u016a",
-    "UnderBar;": "_",
-    "UnderBrace;": "\u23df",
-    "UnderBracket;": "\u23b5",
-    "UnderParenthesis;": "\u23dd",
-    "Union;": "\u22c3",
-    "UnionPlus;": "\u228e",
-    "Uogon;": "\u0172",
-    "Uopf;": "\U0001d54c",
-    "UpArrow;": "\u2191",
-    "UpArrowBar;": "\u2912",
-    "UpArrowDownArrow;": "\u21c5",
-    "UpDownArrow;": "\u2195",
-    "UpEquilibrium;": "\u296e",
-    "UpTee;": "\u22a5",
-    "UpTeeArrow;": "\u21a5",
-    "Uparrow;": "\u21d1",
-    "Updownarrow;": "\u21d5",
-    "UpperLeftArrow;": "\u2196",
-    "UpperRightArrow;": "\u2197",
-    "Upsi;": "\u03d2",
-    "Upsilon;": "\u03a5",
-    "Uring;": "\u016e",
-    "Uscr;": "\U0001d4b0",
-    "Utilde;": "\u0168",
-    "Uuml": "\xdc",
-    "Uuml;": "\xdc",
-    "VDash;": "\u22ab",
-    "Vbar;": "\u2aeb",
-    "Vcy;": "\u0412",
-    "Vdash;": "\u22a9",
-    "Vdashl;": "\u2ae6",
-    "Vee;": "\u22c1",
-    "Verbar;": "\u2016",
-    "Vert;": "\u2016",
-    "VerticalBar;": "\u2223",
-    "VerticalLine;": "|",
-    "VerticalSeparator;": "\u2758",
-    "VerticalTilde;": "\u2240",
-    "VeryThinSpace;": "\u200a",
-    "Vfr;": "\U0001d519",
-    "Vopf;": "\U0001d54d",
-    "Vscr;": "\U0001d4b1",
-    "Vvdash;": "\u22aa",
-    "Wcirc;": "\u0174",
-    "Wedge;": "\u22c0",
-    "Wfr;": "\U0001d51a",
-    "Wopf;": "\U0001d54e",
-    "Wscr;": "\U0001d4b2",
-    "Xfr;": "\U0001d51b",
-    "Xi;": "\u039e",
-    "Xopf;": "\U0001d54f",
-    "Xscr;": "\U0001d4b3",
-    "YAcy;": "\u042f",
-    "YIcy;": "\u0407",
-    "YUcy;": "\u042e",
-    "Yacute": "\xdd",
-    "Yacute;": "\xdd",
-    "Ycirc;": "\u0176",
-    "Ycy;": "\u042b",
-    "Yfr;": "\U0001d51c",
-    "Yopf;": "\U0001d550",
-    "Yscr;": "\U0001d4b4",
-    "Yuml;": "\u0178",
-    "ZHcy;": "\u0416",
-    "Zacute;": "\u0179",
-    "Zcaron;": "\u017d",
-    "Zcy;": "\u0417",
-    "Zdot;": "\u017b",
-    "ZeroWidthSpace;": "\u200b",
-    "Zeta;": "\u0396",
-    "Zfr;": "\u2128",
-    "Zopf;": "\u2124",
-    "Zscr;": "\U0001d4b5",
-    "aacute": "\xe1",
-    "aacute;": "\xe1",
-    "abreve;": "\u0103",
-    "ac;": "\u223e",
-    "acE;": "\u223e\u0333",
-    "acd;": "\u223f",
-    "acirc": "\xe2",
-    "acirc;": "\xe2",
-    "acute": "\xb4",
-    "acute;": "\xb4",
-    "acy;": "\u0430",
-    "aelig": "\xe6",
-    "aelig;": "\xe6",
-    "af;": "\u2061",
-    "afr;": "\U0001d51e",
-    "agrave": "\xe0",
-    "agrave;": "\xe0",
-    "alefsym;": "\u2135",
-    "aleph;": "\u2135",
-    "alpha;": "\u03b1",
-    "amacr;": "\u0101",
-    "amalg;": "\u2a3f",
-    "amp": "&",
-    "amp;": "&",
-    "and;": "\u2227",
-    "andand;": "\u2a55",
-    "andd;": "\u2a5c",
-    "andslope;": "\u2a58",
-    "andv;": "\u2a5a",
-    "ang;": "\u2220",
-    "ange;": "\u29a4",
-    "angle;": "\u2220",
-    "angmsd;": "\u2221",
-    "angmsdaa;": "\u29a8",
-    "angmsdab;": "\u29a9",
-    "angmsdac;": "\u29aa",
-    "angmsdad;": "\u29ab",
-    "angmsdae;": "\u29ac",
-    "angmsdaf;": "\u29ad",
-    "angmsdag;": "\u29ae",
-    "angmsdah;": "\u29af",
-    "angrt;": "\u221f",
-    "angrtvb;": "\u22be",
-    "angrtvbd;": "\u299d",
-    "angsph;": "\u2222",
-    "angst;": "\xc5",
-    "angzarr;": "\u237c",
-    "aogon;": "\u0105",
-    "aopf;": "\U0001d552",
-    "ap;": "\u2248",
-    "apE;": "\u2a70",
-    "apacir;": "\u2a6f",
-    "ape;": "\u224a",
-    "apid;": "\u224b",
-    "apos;": "'",
-    "approx;": "\u2248",
-    "approxeq;": "\u224a",
-    "aring": "\xe5",
-    "aring;": "\xe5",
-    "ascr;": "\U0001d4b6",
-    "ast;": "*",
-    "asymp;": "\u2248",
-    "asympeq;": "\u224d",
-    "atilde": "\xe3",
-    "atilde;": "\xe3",
-    "auml": "\xe4",
-    "auml;": "\xe4",
-    "awconint;": "\u2233",
-    "awint;": "\u2a11",
-    "bNot;": "\u2aed",
-    "backcong;": "\u224c",
-    "backepsilon;": "\u03f6",
-    "backprime;": "\u2035",
-    "backsim;": "\u223d",
-    "backsimeq;": "\u22cd",
-    "barvee;": "\u22bd",
-    "barwed;": "\u2305",
-    "barwedge;": "\u2305",
-    "bbrk;": "\u23b5",
-    "bbrktbrk;": "\u23b6",
-    "bcong;": "\u224c",
-    "bcy;": "\u0431",
-    "bdquo;": "\u201e",
-    "becaus;": "\u2235",
-    "because;": "\u2235",
-    "bemptyv;": "\u29b0",
-    "bepsi;": "\u03f6",
-    "bernou;": "\u212c",
-    "beta;": "\u03b2",
-    "beth;": "\u2136",
-    "between;": "\u226c",
-    "bfr;": "\U0001d51f",
-    "bigcap;": "\u22c2",
-    "bigcirc;": "\u25ef",
-    "bigcup;": "\u22c3",
-    "bigodot;": "\u2a00",
-    "bigoplus;": "\u2a01",
-    "bigotimes;": "\u2a02",
-    "bigsqcup;": "\u2a06",
-    "bigstar;": "\u2605",
-    "bigtriangledown;": "\u25bd",
-    "bigtriangleup;": "\u25b3",
-    "biguplus;": "\u2a04",
-    "bigvee;": "\u22c1",
-    "bigwedge;": "\u22c0",
-    "bkarow;": "\u290d",
-    "blacklozenge;": "\u29eb",
-    "blacksquare;": "\u25aa",
-    "blacktriangle;": "\u25b4",
-    "blacktriangledown;": "\u25be",
-    "blacktriangleleft;": "\u25c2",
-    "blacktriangleright;": "\u25b8",
-    "blank;": "\u2423",
-    "blk12;": "\u2592",
-    "blk14;": "\u2591",
-    "blk34;": "\u2593",
-    "block;": "\u2588",
-    "bne;": "=\u20e5",
-    "bnequiv;": "\u2261\u20e5",
-    "bnot;": "\u2310",
-    "bopf;": "\U0001d553",
-    "bot;": "\u22a5",
-    "bottom;": "\u22a5",
-    "bowtie;": "\u22c8",
-    "boxDL;": "\u2557",
-    "boxDR;": "\u2554",
-    "boxDl;": "\u2556",
-    "boxDr;": "\u2553",
-    "boxH;": "\u2550",
-    "boxHD;": "\u2566",
-    "boxHU;": "\u2569",
-    "boxHd;": "\u2564",
-    "boxHu;": "\u2567",
-    "boxUL;": "\u255d",
-    "boxUR;": "\u255a",
-    "boxUl;": "\u255c",
-    "boxUr;": "\u2559",
-    "boxV;": "\u2551",
-    "boxVH;": "\u256c",
-    "boxVL;": "\u2563",
-    "boxVR;": "\u2560",
-    "boxVh;": "\u256b",
-    "boxVl;": "\u2562",
-    "boxVr;": "\u255f",
-    "boxbox;": "\u29c9",
-    "boxdL;": "\u2555",
-    "boxdR;": "\u2552",
-    "boxdl;": "\u2510",
-    "boxdr;": "\u250c",
-    "boxh;": "\u2500",
-    "boxhD;": "\u2565",
-    "boxhU;": "\u2568",
-    "boxhd;": "\u252c",
-    "boxhu;": "\u2534",
-    "boxminus;": "\u229f",
-    "boxplus;": "\u229e",
-    "boxtimes;": "\u22a0",
-    "boxuL;": "\u255b",
-    "boxuR;": "\u2558",
-    "boxul;": "\u2518",
-    "boxur;": "\u2514",
-    "boxv;": "\u2502",
-    "boxvH;": "\u256a",
-    "boxvL;": "\u2561",
-    "boxvR;": "\u255e",
-    "boxvh;": "\u253c",
-    "boxvl;": "\u2524",
-    "boxvr;": "\u251c",
-    "bprime;": "\u2035",
-    "breve;": "\u02d8",
-    "brvbar": "\xa6",
-    "brvbar;": "\xa6",
-    "bscr;": "\U0001d4b7",
-    "bsemi;": "\u204f",
-    "bsim;": "\u223d",
-    "bsime;": "\u22cd",
-    "bsol;": "\\",
-    "bsolb;": "\u29c5",
-    "bsolhsub;": "\u27c8",
-    "bull;": "\u2022",
-    "bullet;": "\u2022",
-    "bump;": "\u224e",
-    "bumpE;": "\u2aae",
-    "bumpe;": "\u224f",
-    "bumpeq;": "\u224f",
-    "cacute;": "\u0107",
-    "cap;": "\u2229",
-    "capand;": "\u2a44",
-    "capbrcup;": "\u2a49",
-    "capcap;": "\u2a4b",
-    "capcup;": "\u2a47",
-    "capdot;": "\u2a40",
-    "caps;": "\u2229\ufe00",
-    "caret;": "\u2041",
-    "caron;": "\u02c7",
-    "ccaps;": "\u2a4d",
-    "ccaron;": "\u010d",
-    "ccedil": "\xe7",
-    "ccedil;": "\xe7",
-    "ccirc;": "\u0109",
-    "ccups;": "\u2a4c",
-    "ccupssm;": "\u2a50",
-    "cdot;": "\u010b",
-    "cedil": "\xb8",
-    "cedil;": "\xb8",
-    "cemptyv;": "\u29b2",
-    "cent": "\xa2",
-    "cent;": "\xa2",
-    "centerdot;": "\xb7",
-    "cfr;": "\U0001d520",
-    "chcy;": "\u0447",
-    "check;": "\u2713",
-    "checkmark;": "\u2713",
-    "chi;": "\u03c7",
-    "cir;": "\u25cb",
-    "cirE;": "\u29c3",
-    "circ;": "\u02c6",
-    "circeq;": "\u2257",
-    "circlearrowleft;": "\u21ba",
-    "circlearrowright;": "\u21bb",
-    "circledR;": "\xae",
-    "circledS;": "\u24c8",
-    "circledast;": "\u229b",
-    "circledcirc;": "\u229a",
-    "circleddash;": "\u229d",
-    "cire;": "\u2257",
-    "cirfnint;": "\u2a10",
-    "cirmid;": "\u2aef",
-    "cirscir;": "\u29c2",
-    "clubs;": "\u2663",
-    "clubsuit;": "\u2663",
-    "colon;": ":",
-    "colone;": "\u2254",
-    "coloneq;": "\u2254",
-    "comma;": ",",
-    "commat;": "@",
-    "comp;": "\u2201",
-    "compfn;": "\u2218",
-    "complement;": "\u2201",
-    "complexes;": "\u2102",
-    "cong;": "\u2245",
-    "congdot;": "\u2a6d",
-    "conint;": "\u222e",
-    "copf;": "\U0001d554",
-    "coprod;": "\u2210",
-    "copy": "\xa9",
-    "copy;": "\xa9",
-    "copysr;": "\u2117",
-    "crarr;": "\u21b5",
-    "cross;": "\u2717",
-    "cscr;": "\U0001d4b8",
-    "csub;": "\u2acf",
-    "csube;": "\u2ad1",
-    "csup;": "\u2ad0",
-    "csupe;": "\u2ad2",
-    "ctdot;": "\u22ef",
-    "cudarrl;": "\u2938",
-    "cudarrr;": "\u2935",
-    "cuepr;": "\u22de",
-    "cuesc;": "\u22df",
-    "cularr;": "\u21b6",
-    "cularrp;": "\u293d",
-    "cup;": "\u222a",
-    "cupbrcap;": "\u2a48",
-    "cupcap;": "\u2a46",
-    "cupcup;": "\u2a4a",
-    "cupdot;": "\u228d",
-    "cupor;": "\u2a45",
-    "cups;": "\u222a\ufe00",
-    "curarr;": "\u21b7",
-    "curarrm;": "\u293c",
-    "curlyeqprec;": "\u22de",
-    "curlyeqsucc;": "\u22df",
-    "curlyvee;": "\u22ce",
-    "curlywedge;": "\u22cf",
-    "curren": "\xa4",
-    "curren;": "\xa4",
-    "curvearrowleft;": "\u21b6",
-    "curvearrowright;": "\u21b7",
-    "cuvee;": "\u22ce",
-    "cuwed;": "\u22cf",
-    "cwconint;": "\u2232",
-    "cwint;": "\u2231",
-    "cylcty;": "\u232d",
-    "dArr;": "\u21d3",
-    "dHar;": "\u2965",
-    "dagger;": "\u2020",
-    "daleth;": "\u2138",
-    "darr;": "\u2193",
-    "dash;": "\u2010",
-    "dashv;": "\u22a3",
-    "dbkarow;": "\u290f",
-    "dblac;": "\u02dd",
-    "dcaron;": "\u010f",
-    "dcy;": "\u0434",
-    "dd;": "\u2146",
-    "ddagger;": "\u2021",
-    "ddarr;": "\u21ca",
-    "ddotseq;": "\u2a77",
-    "deg": "\xb0",
-    "deg;": "\xb0",
-    "delta;": "\u03b4",
-    "demptyv;": "\u29b1",
-    "dfisht;": "\u297f",
-    "dfr;": "\U0001d521",
-    "dharl;": "\u21c3",
-    "dharr;": "\u21c2",
-    "diam;": "\u22c4",
-    "diamond;": "\u22c4",
-    "diamondsuit;": "\u2666",
-    "diams;": "\u2666",
-    "die;": "\xa8",
-    "digamma;": "\u03dd",
-    "disin;": "\u22f2",
-    "div;": "\xf7",
-    "divide": "\xf7",
-    "divide;": "\xf7",
-    "divideontimes;": "\u22c7",
-    "divonx;": "\u22c7",
-    "djcy;": "\u0452",
-    "dlcorn;": "\u231e",
-    "dlcrop;": "\u230d",
-    "dollar;": "$",
-    "dopf;": "\U0001d555",
-    "dot;": "\u02d9",
-    "doteq;": "\u2250",
-    "doteqdot;": "\u2251",
-    "dotminus;": "\u2238",
-    "dotplus;": "\u2214",
-    "dotsquare;": "\u22a1",
-    "doublebarwedge;": "\u2306",
-    "downarrow;": "\u2193",
-    "downdownarrows;": "\u21ca",
-    "downharpoonleft;": "\u21c3",
-    "downharpoonright;": "\u21c2",
-    "drbkarow;": "\u2910",
-    "drcorn;": "\u231f",
-    "drcrop;": "\u230c",
-    "dscr;": "\U0001d4b9",
-    "dscy;": "\u0455",
-    "dsol;": "\u29f6",
-    "dstrok;": "\u0111",
-    "dtdot;": "\u22f1",
-    "dtri;": "\u25bf",
-    "dtrif;": "\u25be",
-    "duarr;": "\u21f5",
-    "duhar;": "\u296f",
-    "dwangle;": "\u29a6",
-    "dzcy;": "\u045f",
-    "dzigrarr;": "\u27ff",
-    "eDDot;": "\u2a77",
-    "eDot;": "\u2251",
-    "eacute": "\xe9",
-    "eacute;": "\xe9",
-    "easter;": "\u2a6e",
-    "ecaron;": "\u011b",
-    "ecir;": "\u2256",
-    "ecirc": "\xea",
-    "ecirc;": "\xea",
-    "ecolon;": "\u2255",
-    "ecy;": "\u044d",
-    "edot;": "\u0117",
-    "ee;": "\u2147",
-    "efDot;": "\u2252",
-    "efr;": "\U0001d522",
-    "eg;": "\u2a9a",
-    "egrave": "\xe8",
-    "egrave;": "\xe8",
-    "egs;": "\u2a96",
-    "egsdot;": "\u2a98",
-    "el;": "\u2a99",
-    "elinters;": "\u23e7",
-    "ell;": "\u2113",
-    "els;": "\u2a95",
-    "elsdot;": "\u2a97",
-    "emacr;": "\u0113",
-    "empty;": "\u2205",
-    "emptyset;": "\u2205",
-    "emptyv;": "\u2205",
-    "emsp13;": "\u2004",
-    "emsp14;": "\u2005",
-    "emsp;": "\u2003",
-    "eng;": "\u014b",
-    "ensp;": "\u2002",
-    "eogon;": "\u0119",
-    "eopf;": "\U0001d556",
-    "epar;": "\u22d5",
-    "eparsl;": "\u29e3",
-    "eplus;": "\u2a71",
-    "epsi;": "\u03b5",
-    "epsilon;": "\u03b5",
-    "epsiv;": "\u03f5",
-    "eqcirc;": "\u2256",
-    "eqcolon;": "\u2255",
-    "eqsim;": "\u2242",
-    "eqslantgtr;": "\u2a96",
-    "eqslantless;": "\u2a95",
-    "equals;": "=",
-    "equest;": "\u225f",
-    "equiv;": "\u2261",
-    "equivDD;": "\u2a78",
-    "eqvparsl;": "\u29e5",
-    "erDot;": "\u2253",
-    "erarr;": "\u2971",
-    "escr;": "\u212f",
-    "esdot;": "\u2250",
-    "esim;": "\u2242",
-    "eta;": "\u03b7",
-    "eth": "\xf0",
-    "eth;": "\xf0",
-    "euml": "\xeb",
-    "euml;": "\xeb",
-    "euro;": "\u20ac",
-    "excl;": "!",
-    "exist;": "\u2203",
-    "expectation;": "\u2130",
-    "exponentiale;": "\u2147",
-    "fallingdotseq;": "\u2252",
-    "fcy;": "\u0444",
-    "female;": "\u2640",
-    "ffilig;": "\ufb03",
-    "fflig;": "\ufb00",
-    "ffllig;": "\ufb04",
-    "ffr;": "\U0001d523",
-    "filig;": "\ufb01",
-    "fjlig;": "fj",
-    "flat;": "\u266d",
-    "fllig;": "\ufb02",
-    "fltns;": "\u25b1",
-    "fnof;": "\u0192",
-    "fopf;": "\U0001d557",
-    "forall;": "\u2200",
-    "fork;": "\u22d4",
-    "forkv;": "\u2ad9",
-    "fpartint;": "\u2a0d",
-    "frac12": "\xbd",
-    "frac12;": "\xbd",
-    "frac13;": "\u2153",
-    "frac14": "\xbc",
-    "frac14;": "\xbc",
-    "frac15;": "\u2155",
-    "frac16;": "\u2159",
-    "frac18;": "\u215b",
-    "frac23;": "\u2154",
-    "frac25;": "\u2156",
-    "frac34": "\xbe",
-    "frac34;": "\xbe",
-    "frac35;": "\u2157",
-    "frac38;": "\u215c",
-    "frac45;": "\u2158",
-    "frac56;": "\u215a",
-    "frac58;": "\u215d",
-    "frac78;": "\u215e",
-    "frasl;": "\u2044",
-    "frown;": "\u2322",
-    "fscr;": "\U0001d4bb",
-    "gE;": "\u2267",
-    "gEl;": "\u2a8c",
-    "gacute;": "\u01f5",
-    "gamma;": "\u03b3",
-    "gammad;": "\u03dd",
-    "gap;": "\u2a86",
-    "gbreve;": "\u011f",
-    "gcirc;": "\u011d",
-    "gcy;": "\u0433",
-    "gdot;": "\u0121",
-    "ge;": "\u2265",
-    "gel;": "\u22db",
-    "geq;": "\u2265",
-    "geqq;": "\u2267",
-    "geqslant;": "\u2a7e",
-    "ges;": "\u2a7e",
-    "gescc;": "\u2aa9",
-    "gesdot;": "\u2a80",
-    "gesdoto;": "\u2a82",
-    "gesdotol;": "\u2a84",
-    "gesl;": "\u22db\ufe00",
-    "gesles;": "\u2a94",
-    "gfr;": "\U0001d524",
-    "gg;": "\u226b",
-    "ggg;": "\u22d9",
-    "gimel;": "\u2137",
-    "gjcy;": "\u0453",
-    "gl;": "\u2277",
-    "glE;": "\u2a92",
-    "gla;": "\u2aa5",
-    "glj;": "\u2aa4",
-    "gnE;": "\u2269",
-    "gnap;": "\u2a8a",
-    "gnapprox;": "\u2a8a",
-    "gne;": "\u2a88",
-    "gneq;": "\u2a88",
-    "gneqq;": "\u2269",
-    "gnsim;": "\u22e7",
-    "gopf;": "\U0001d558",
-    "grave;": "`",
-    "gscr;": "\u210a",
-    "gsim;": "\u2273",
-    "gsime;": "\u2a8e",
-    "gsiml;": "\u2a90",
-    "gt": ">",
-    "gt;": ">",
-    "gtcc;": "\u2aa7",
-    "gtcir;": "\u2a7a",
-    "gtdot;": "\u22d7",
-    "gtlPar;": "\u2995",
-    "gtquest;": "\u2a7c",
-    "gtrapprox;": "\u2a86",
-    "gtrarr;": "\u2978",
-    "gtrdot;": "\u22d7",
-    "gtreqless;": "\u22db",
-    "gtreqqless;": "\u2a8c",
-    "gtrless;": "\u2277",
-    "gtrsim;": "\u2273",
-    "gvertneqq;": "\u2269\ufe00",
-    "gvnE;": "\u2269\ufe00",
-    "hArr;": "\u21d4",
-    "hairsp;": "\u200a",
-    "half;": "\xbd",
-    "hamilt;": "\u210b",
-    "hardcy;": "\u044a",
-    "harr;": "\u2194",
-    "harrcir;": "\u2948",
-    "harrw;": "\u21ad",
-    "hbar;": "\u210f",
-    "hcirc;": "\u0125",
-    "hearts;": "\u2665",
-    "heartsuit;": "\u2665",
-    "hellip;": "\u2026",
-    "hercon;": "\u22b9",
-    "hfr;": "\U0001d525",
-    "hksearow;": "\u2925",
-    "hkswarow;": "\u2926",
-    "hoarr;": "\u21ff",
-    "homtht;": "\u223b",
-    "hookleftarrow;": "\u21a9",
-    "hookrightarrow;": "\u21aa",
-    "hopf;": "\U0001d559",
-    "horbar;": "\u2015",
-    "hscr;": "\U0001d4bd",
-    "hslash;": "\u210f",
-    "hstrok;": "\u0127",
-    "hybull;": "\u2043",
-    "hyphen;": "\u2010",
-    "iacute": "\xed",
-    "iacute;": "\xed",
-    "ic;": "\u2063",
-    "icirc": "\xee",
-    "icirc;": "\xee",
-    "icy;": "\u0438",
-    "iecy;": "\u0435",
-    "iexcl": "\xa1",
-    "iexcl;": "\xa1",
-    "iff;": "\u21d4",
-    "ifr;": "\U0001d526",
-    "igrave": "\xec",
-    "igrave;": "\xec",
-    "ii;": "\u2148",
-    "iiiint;": "\u2a0c",
-    "iiint;": "\u222d",
-    "iinfin;": "\u29dc",
-    "iiota;": "\u2129",
-    "ijlig;": "\u0133",
-    "imacr;": "\u012b",
-    "image;": "\u2111",
-    "imagline;": "\u2110",
-    "imagpart;": "\u2111",
-    "imath;": "\u0131",
-    "imof;": "\u22b7",
-    "imped;": "\u01b5",
-    "in;": "\u2208",
-    "incare;": "\u2105",
-    "infin;": "\u221e",
-    "infintie;": "\u29dd",
-    "inodot;": "\u0131",
-    "int;": "\u222b",
-    "intcal;": "\u22ba",
-    "integers;": "\u2124",
-    "intercal;": "\u22ba",
-    "intlarhk;": "\u2a17",
-    "intprod;": "\u2a3c",
-    "iocy;": "\u0451",
-    "iogon;": "\u012f",
-    "iopf;": "\U0001d55a",
-    "iota;": "\u03b9",
-    "iprod;": "\u2a3c",
-    "iquest": "\xbf",
-    "iquest;": "\xbf",
-    "iscr;": "\U0001d4be",
-    "isin;": "\u2208",
-    "isinE;": "\u22f9",
-    "isindot;": "\u22f5",
-    "isins;": "\u22f4",
-    "isinsv;": "\u22f3",
-    "isinv;": "\u2208",
-    "it;": "\u2062",
-    "itilde;": "\u0129",
-    "iukcy;": "\u0456",
-    "iuml": "\xef",
-    "iuml;": "\xef",
-    "jcirc;": "\u0135",
-    "jcy;": "\u0439",
-    "jfr;": "\U0001d527",
-    "jmath;": "\u0237",
-    "jopf;": "\U0001d55b",
-    "jscr;": "\U0001d4bf",
-    "jsercy;": "\u0458",
-    "jukcy;": "\u0454",
-    "kappa;": "\u03ba",
-    "kappav;": "\u03f0",
-    "kcedil;": "\u0137",
-    "kcy;": "\u043a",
-    "kfr;": "\U0001d528",
-    "kgreen;": "\u0138",
-    "khcy;": "\u0445",
-    "kjcy;": "\u045c",
-    "kopf;": "\U0001d55c",
-    "kscr;": "\U0001d4c0",
-    "lAarr;": "\u21da",
-    "lArr;": "\u21d0",
-    "lAtail;": "\u291b",
-    "lBarr;": "\u290e",
-    "lE;": "\u2266",
-    "lEg;": "\u2a8b",
-    "lHar;": "\u2962",
-    "lacute;": "\u013a",
-    "laemptyv;": "\u29b4",
-    "lagran;": "\u2112",
-    "lambda;": "\u03bb",
-    "lang;": "\u27e8",
-    "langd;": "\u2991",
-    "langle;": "\u27e8",
-    "lap;": "\u2a85",
-    "laquo": "\xab",
-    "laquo;": "\xab",
-    "larr;": "\u2190",
-    "larrb;": "\u21e4",
-    "larrbfs;": "\u291f",
-    "larrfs;": "\u291d",
-    "larrhk;": "\u21a9",
-    "larrlp;": "\u21ab",
-    "larrpl;": "\u2939",
-    "larrsim;": "\u2973",
-    "larrtl;": "\u21a2",
-    "lat;": "\u2aab",
-    "latail;": "\u2919",
-    "late;": "\u2aad",
-    "lates;": "\u2aad\ufe00",
-    "lbarr;": "\u290c",
-    "lbbrk;": "\u2772",
-    "lbrace;": "{",
-    "lbrack;": "[",
-    "lbrke;": "\u298b",
-    "lbrksld;": "\u298f",
-    "lbrkslu;": "\u298d",
-    "lcaron;": "\u013e",
-    "lcedil;": "\u013c",
-    "lceil;": "\u2308",
-    "lcub;": "{",
-    "lcy;": "\u043b",
-    "ldca;": "\u2936",
-    "ldquo;": "\u201c",
-    "ldquor;": "\u201e",
-    "ldrdhar;": "\u2967",
-    "ldrushar;": "\u294b",
-    "ldsh;": "\u21b2",
-    "le;": "\u2264",
-    "leftarrow;": "\u2190",
-    "leftarrowtail;": "\u21a2",
-    "leftharpoondown;": "\u21bd",
-    "leftharpoonup;": "\u21bc",
-    "leftleftarrows;": "\u21c7",
-    "leftrightarrow;": "\u2194",
-    "leftrightarrows;": "\u21c6",
-    "leftrightharpoons;": "\u21cb",
-    "leftrightsquigarrow;": "\u21ad",
-    "leftthreetimes;": "\u22cb",
-    "leg;": "\u22da",
-    "leq;": "\u2264",
-    "leqq;": "\u2266",
-    "leqslant;": "\u2a7d",
-    "les;": "\u2a7d",
-    "lescc;": "\u2aa8",
-    "lesdot;": "\u2a7f",
-    "lesdoto;": "\u2a81",
-    "lesdotor;": "\u2a83",
-    "lesg;": "\u22da\ufe00",
-    "lesges;": "\u2a93",
-    "lessapprox;": "\u2a85",
-    "lessdot;": "\u22d6",
-    "lesseqgtr;": "\u22da",
-    "lesseqqgtr;": "\u2a8b",
-    "lessgtr;": "\u2276",
-    "lesssim;": "\u2272",
-    "lfisht;": "\u297c",
-    "lfloor;": "\u230a",
-    "lfr;": "\U0001d529",
-    "lg;": "\u2276",
-    "lgE;": "\u2a91",
-    "lhard;": "\u21bd",
-    "lharu;": "\u21bc",
-    "lharul;": "\u296a",
-    "lhblk;": "\u2584",
-    "ljcy;": "\u0459",
-    "ll;": "\u226a",
-    "llarr;": "\u21c7",
-    "llcorner;": "\u231e",
-    "llhard;": "\u296b",
-    "lltri;": "\u25fa",
-    "lmidot;": "\u0140",
-    "lmoust;": "\u23b0",
-    "lmoustache;": "\u23b0",
-    "lnE;": "\u2268",
-    "lnap;": "\u2a89",
-    "lnapprox;": "\u2a89",
-    "lne;": "\u2a87",
-    "lneq;": "\u2a87",
-    "lneqq;": "\u2268",
-    "lnsim;": "\u22e6",
-    "loang;": "\u27ec",
-    "loarr;": "\u21fd",
-    "lobrk;": "\u27e6",
-    "longleftarrow;": "\u27f5",
-    "longleftrightarrow;": "\u27f7",
-    "longmapsto;": "\u27fc",
-    "longrightarrow;": "\u27f6",
-    "looparrowleft;": "\u21ab",
-    "looparrowright;": "\u21ac",
-    "lopar;": "\u2985",
-    "lopf;": "\U0001d55d",
-    "loplus;": "\u2a2d",
-    "lotimes;": "\u2a34",
-    "lowast;": "\u2217",
-    "lowbar;": "_",
-    "loz;": "\u25ca",
-    "lozenge;": "\u25ca",
-    "lozf;": "\u29eb",
-    "lpar;": "(",
-    "lparlt;": "\u2993",
-    "lrarr;": "\u21c6",
-    "lrcorner;": "\u231f",
-    "lrhar;": "\u21cb",
-    "lrhard;": "\u296d",
-    "lrm;": "\u200e",
-    "lrtri;": "\u22bf",
-    "lsaquo;": "\u2039",
-    "lscr;": "\U0001d4c1",
-    "lsh;": "\u21b0",
-    "lsim;": "\u2272",
-    "lsime;": "\u2a8d",
-    "lsimg;": "\u2a8f",
-    "lsqb;": "[",
-    "lsquo;": "\u2018",
-    "lsquor;": "\u201a",
-    "lstrok;": "\u0142",
-    "lt": "<",
-    "lt;": "<",
-    "ltcc;": "\u2aa6",
-    "ltcir;": "\u2a79",
-    "ltdot;": "\u22d6",
-    "lthree;": "\u22cb",
-    "ltimes;": "\u22c9",
-    "ltlarr;": "\u2976",
-    "ltquest;": "\u2a7b",
-    "ltrPar;": "\u2996",
-    "ltri;": "\u25c3",
-    "ltrie;": "\u22b4",
-    "ltrif;": "\u25c2",
-    "lurdshar;": "\u294a",
-    "luruhar;": "\u2966",
-    "lvertneqq;": "\u2268\ufe00",
-    "lvnE;": "\u2268\ufe00",
-    "mDDot;": "\u223a",
-    "macr": "\xaf",
-    "macr;": "\xaf",
-    "male;": "\u2642",
-    "malt;": "\u2720",
-    "maltese;": "\u2720",
-    "map;": "\u21a6",
-    "mapsto;": "\u21a6",
-    "mapstodown;": "\u21a7",
-    "mapstoleft;": "\u21a4",
-    "mapstoup;": "\u21a5",
-    "marker;": "\u25ae",
-    "mcomma;": "\u2a29",
-    "mcy;": "\u043c",
-    "mdash;": "\u2014",
-    "measuredangle;": "\u2221",
-    "mfr;": "\U0001d52a",
-    "mho;": "\u2127",
-    "micro": "\xb5",
-    "micro;": "\xb5",
-    "mid;": "\u2223",
-    "midast;": "*",
-    "midcir;": "\u2af0",
-    "middot": "\xb7",
-    "middot;": "\xb7",
-    "minus;": "\u2212",
-    "minusb;": "\u229f",
-    "minusd;": "\u2238",
-    "minusdu;": "\u2a2a",
-    "mlcp;": "\u2adb",
-    "mldr;": "\u2026",
-    "mnplus;": "\u2213",
-    "models;": "\u22a7",
-    "mopf;": "\U0001d55e",
-    "mp;": "\u2213",
-    "mscr;": "\U0001d4c2",
-    "mstpos;": "\u223e",
-    "mu;": "\u03bc",
-    "multimap;": "\u22b8",
-    "mumap;": "\u22b8",
-    "nGg;": "\u22d9\u0338",
-    "nGt;": "\u226b\u20d2",
-    "nGtv;": "\u226b\u0338",
-    "nLeftarrow;": "\u21cd",
-    "nLeftrightarrow;": "\u21ce",
-    "nLl;": "\u22d8\u0338",
-    "nLt;": "\u226a\u20d2",
-    "nLtv;": "\u226a\u0338",
-    "nRightarrow;": "\u21cf",
-    "nVDash;": "\u22af",
-    "nVdash;": "\u22ae",
-    "nabla;": "\u2207",
-    "nacute;": "\u0144",
-    "nang;": "\u2220\u20d2",
-    "nap;": "\u2249",
-    "napE;": "\u2a70\u0338",
-    "napid;": "\u224b\u0338",
-    "napos;": "\u0149",
-    "napprox;": "\u2249",
-    "natur;": "\u266e",
-    "natural;": "\u266e",
-    "naturals;": "\u2115",
-    "nbsp": "\xa0",
-    "nbsp;": "\xa0",
-    "nbump;": "\u224e\u0338",
-    "nbumpe;": "\u224f\u0338",
-    "ncap;": "\u2a43",
-    "ncaron;": "\u0148",
-    "ncedil;": "\u0146",
-    "ncong;": "\u2247",
-    "ncongdot;": "\u2a6d\u0338",
-    "ncup;": "\u2a42",
-    "ncy;": "\u043d",
-    "ndash;": "\u2013",
-    "ne;": "\u2260",
-    "neArr;": "\u21d7",
-    "nearhk;": "\u2924",
-    "nearr;": "\u2197",
-    "nearrow;": "\u2197",
-    "nedot;": "\u2250\u0338",
-    "nequiv;": "\u2262",
-    "nesear;": "\u2928",
-    "nesim;": "\u2242\u0338",
-    "nexist;": "\u2204",
-    "nexists;": "\u2204",
-    "nfr;": "\U0001d52b",
-    "ngE;": "\u2267\u0338",
-    "nge;": "\u2271",
-    "ngeq;": "\u2271",
-    "ngeqq;": "\u2267\u0338",
-    "ngeqslant;": "\u2a7e\u0338",
-    "nges;": "\u2a7e\u0338",
-    "ngsim;": "\u2275",
-    "ngt;": "\u226f",
-    "ngtr;": "\u226f",
-    "nhArr;": "\u21ce",
-    "nharr;": "\u21ae",
-    "nhpar;": "\u2af2",
-    "ni;": "\u220b",
-    "nis;": "\u22fc",
-    "nisd;": "\u22fa",
-    "niv;": "\u220b",
-    "njcy;": "\u045a",
-    "nlArr;": "\u21cd",
-    "nlE;": "\u2266\u0338",
-    "nlarr;": "\u219a",
-    "nldr;": "\u2025",
-    "nle;": "\u2270",
-    "nleftarrow;": "\u219a",
-    "nleftrightarrow;": "\u21ae",
-    "nleq;": "\u2270",
-    "nleqq;": "\u2266\u0338",
-    "nleqslant;": "\u2a7d\u0338",
-    "nles;": "\u2a7d\u0338",
-    "nless;": "\u226e",
-    "nlsim;": "\u2274",
-    "nlt;": "\u226e",
-    "nltri;": "\u22ea",
-    "nltrie;": "\u22ec",
-    "nmid;": "\u2224",
-    "nopf;": "\U0001d55f",
-    "not": "\xac",
-    "not;": "\xac",
-    "notin;": "\u2209",
-    "notinE;": "\u22f9\u0338",
-    "notindot;": "\u22f5\u0338",
-    "notinva;": "\u2209",
-    "notinvb;": "\u22f7",
-    "notinvc;": "\u22f6",
-    "notni;": "\u220c",
-    "notniva;": "\u220c",
-    "notnivb;": "\u22fe",
-    "notnivc;": "\u22fd",
-    "npar;": "\u2226",
-    "nparallel;": "\u2226",
-    "nparsl;": "\u2afd\u20e5",
-    "npart;": "\u2202\u0338",
-    "npolint;": "\u2a14",
-    "npr;": "\u2280",
-    "nprcue;": "\u22e0",
-    "npre;": "\u2aaf\u0338",
-    "nprec;": "\u2280",
-    "npreceq;": "\u2aaf\u0338",
-    "nrArr;": "\u21cf",
-    "nrarr;": "\u219b",
-    "nrarrc;": "\u2933\u0338",
-    "nrarrw;": "\u219d\u0338",
-    "nrightarrow;": "\u219b",
-    "nrtri;": "\u22eb",
-    "nrtrie;": "\u22ed",
-    "nsc;": "\u2281",
-    "nsccue;": "\u22e1",
-    "nsce;": "\u2ab0\u0338",
-    "nscr;": "\U0001d4c3",
-    "nshortmid;": "\u2224",
-    "nshortparallel;": "\u2226",
-    "nsim;": "\u2241",
-    "nsime;": "\u2244",
-    "nsimeq;": "\u2244",
-    "nsmid;": "\u2224",
-    "nspar;": "\u2226",
-    "nsqsube;": "\u22e2",
-    "nsqsupe;": "\u22e3",
-    "nsub;": "\u2284",
-    "nsubE;": "\u2ac5\u0338",
-    "nsube;": "\u2288",
-    "nsubset;": "\u2282\u20d2",
-    "nsubseteq;": "\u2288",
-    "nsubseteqq;": "\u2ac5\u0338",
-    "nsucc;": "\u2281",
-    "nsucceq;": "\u2ab0\u0338",
-    "nsup;": "\u2285",
-    "nsupE;": "\u2ac6\u0338",
-    "nsupe;": "\u2289",
-    "nsupset;": "\u2283\u20d2",
-    "nsupseteq;": "\u2289",
-    "nsupseteqq;": "\u2ac6\u0338",
-    "ntgl;": "\u2279",
-    "ntilde": "\xf1",
-    "ntilde;": "\xf1",
-    "ntlg;": "\u2278",
-    "ntriangleleft;": "\u22ea",
-    "ntrianglelefteq;": "\u22ec",
-    "ntriangleright;": "\u22eb",
-    "ntrianglerighteq;": "\u22ed",
-    "nu;": "\u03bd",
-    "num;": "#",
-    "numero;": "\u2116",
-    "numsp;": "\u2007",
-    "nvDash;": "\u22ad",
-    "nvHarr;": "\u2904",
-    "nvap;": "\u224d\u20d2",
-    "nvdash;": "\u22ac",
-    "nvge;": "\u2265\u20d2",
-    "nvgt;": ">\u20d2",
-    "nvinfin;": "\u29de",
-    "nvlArr;": "\u2902",
-    "nvle;": "\u2264\u20d2",
-    "nvlt;": "<\u20d2",
-    "nvltrie;": "\u22b4\u20d2",
-    "nvrArr;": "\u2903",
-    "nvrtrie;": "\u22b5\u20d2",
-    "nvsim;": "\u223c\u20d2",
-    "nwArr;": "\u21d6",
-    "nwarhk;": "\u2923",
-    "nwarr;": "\u2196",
-    "nwarrow;": "\u2196",
-    "nwnear;": "\u2927",
-    "oS;": "\u24c8",
-    "oacute": "\xf3",
-    "oacute;": "\xf3",
-    "oast;": "\u229b",
-    "ocir;": "\u229a",
-    "ocirc": "\xf4",
-    "ocirc;": "\xf4",
-    "ocy;": "\u043e",
-    "odash;": "\u229d",
-    "odblac;": "\u0151",
-    "odiv;": "\u2a38",
-    "odot;": "\u2299",
-    "odsold;": "\u29bc",
-    "oelig;": "\u0153",
-    "ofcir;": "\u29bf",
-    "ofr;": "\U0001d52c",
-    "ogon;": "\u02db",
-    "ograve": "\xf2",
-    "ograve;": "\xf2",
-    "ogt;": "\u29c1",
-    "ohbar;": "\u29b5",
-    "ohm;": "\u03a9",
-    "oint;": "\u222e",
-    "olarr;": "\u21ba",
-    "olcir;": "\u29be",
-    "olcross;": "\u29bb",
-    "oline;": "\u203e",
-    "olt;": "\u29c0",
-    "omacr;": "\u014d",
-    "omega;": "\u03c9",
-    "omicron;": "\u03bf",
-    "omid;": "\u29b6",
-    "ominus;": "\u2296",
-    "oopf;": "\U0001d560",
-    "opar;": "\u29b7",
-    "operp;": "\u29b9",
-    "oplus;": "\u2295",
-    "or;": "\u2228",
-    "orarr;": "\u21bb",
-    "ord;": "\u2a5d",
-    "order;": "\u2134",
-    "orderof;": "\u2134",
-    "ordf": "\xaa",
-    "ordf;": "\xaa",
-    "ordm": "\xba",
-    "ordm;": "\xba",
-    "origof;": "\u22b6",
-    "oror;": "\u2a56",
-    "orslope;": "\u2a57",
-    "orv;": "\u2a5b",
-    "oscr;": "\u2134",
-    "oslash": "\xf8",
-    "oslash;": "\xf8",
-    "osol;": "\u2298",
-    "otilde": "\xf5",
-    "otilde;": "\xf5",
-    "otimes;": "\u2297",
-    "otimesas;": "\u2a36",
-    "ouml": "\xf6",
-    "ouml;": "\xf6",
-    "ovbar;": "\u233d",
-    "par;": "\u2225",
-    "para": "\xb6",
-    "para;": "\xb6",
-    "parallel;": "\u2225",
-    "parsim;": "\u2af3",
-    "parsl;": "\u2afd",
-    "part;": "\u2202",
-    "pcy;": "\u043f",
-    "percnt;": "%",
-    "period;": ".",
-    "permil;": "\u2030",
-    "perp;": "\u22a5",
-    "pertenk;": "\u2031",
-    "pfr;": "\U0001d52d",
-    "phi;": "\u03c6",
-    "phiv;": "\u03d5",
-    "phmmat;": "\u2133",
-    "phone;": "\u260e",
-    "pi;": "\u03c0",
-    "pitchfork;": "\u22d4",
-    "piv;": "\u03d6",
-    "planck;": "\u210f",
-    "planckh;": "\u210e",
-    "plankv;": "\u210f",
-    "plus;": "+",
-    "plusacir;": "\u2a23",
-    "plusb;": "\u229e",
-    "pluscir;": "\u2a22",
-    "plusdo;": "\u2214",
-    "plusdu;": "\u2a25",
-    "pluse;": "\u2a72",
-    "plusmn": "\xb1",
-    "plusmn;": "\xb1",
-    "plussim;": "\u2a26",
-    "plustwo;": "\u2a27",
-    "pm;": "\xb1",
-    "pointint;": "\u2a15",
-    "popf;": "\U0001d561",
-    "pound": "\xa3",
-    "pound;": "\xa3",
-    "pr;": "\u227a",
-    "prE;": "\u2ab3",
-    "prap;": "\u2ab7",
-    "prcue;": "\u227c",
-    "pre;": "\u2aaf",
-    "prec;": "\u227a",
-    "precapprox;": "\u2ab7",
-    "preccurlyeq;": "\u227c",
-    "preceq;": "\u2aaf",
-    "precnapprox;": "\u2ab9",
-    "precneqq;": "\u2ab5",
-    "precnsim;": "\u22e8",
-    "precsim;": "\u227e",
-    "prime;": "\u2032",
-    "primes;": "\u2119",
-    "prnE;": "\u2ab5",
-    "prnap;": "\u2ab9",
-    "prnsim;": "\u22e8",
-    "prod;": "\u220f",
-    "profalar;": "\u232e",
-    "profline;": "\u2312",
-    "profsurf;": "\u2313",
-    "prop;": "\u221d",
-    "propto;": "\u221d",
-    "prsim;": "\u227e",
-    "prurel;": "\u22b0",
-    "pscr;": "\U0001d4c5",
-    "psi;": "\u03c8",
-    "puncsp;": "\u2008",
-    "qfr;": "\U0001d52e",
-    "qint;": "\u2a0c",
-    "qopf;": "\U0001d562",
-    "qprime;": "\u2057",
-    "qscr;": "\U0001d4c6",
-    "quaternions;": "\u210d",
-    "quatint;": "\u2a16",
-    "quest;": "?",
-    "questeq;": "\u225f",
-    "quot": "\"",
-    "quot;": "\"",
-    "rAarr;": "\u21db",
-    "rArr;": "\u21d2",
-    "rAtail;": "\u291c",
-    "rBarr;": "\u290f",
-    "rHar;": "\u2964",
-    "race;": "\u223d\u0331",
-    "racute;": "\u0155",
-    "radic;": "\u221a",
-    "raemptyv;": "\u29b3",
-    "rang;": "\u27e9",
-    "rangd;": "\u2992",
-    "range;": "\u29a5",
-    "rangle;": "\u27e9",
-    "raquo": "\xbb",
-    "raquo;": "\xbb",
-    "rarr;": "\u2192",
-    "rarrap;": "\u2975",
-    "rarrb;": "\u21e5",
-    "rarrbfs;": "\u2920",
-    "rarrc;": "\u2933",
-    "rarrfs;": "\u291e",
-    "rarrhk;": "\u21aa",
-    "rarrlp;": "\u21ac",
-    "rarrpl;": "\u2945",
-    "rarrsim;": "\u2974",
-    "rarrtl;": "\u21a3",
-    "rarrw;": "\u219d",
-    "ratail;": "\u291a",
-    "ratio;": "\u2236",
-    "rationals;": "\u211a",
-    "rbarr;": "\u290d",
-    "rbbrk;": "\u2773",
-    "rbrace;": "}",
-    "rbrack;": "]",
-    "rbrke;": "\u298c",
-    "rbrksld;": "\u298e",
-    "rbrkslu;": "\u2990",
-    "rcaron;": "\u0159",
-    "rcedil;": "\u0157",
-    "rceil;": "\u2309",
-    "rcub;": "}",
-    "rcy;": "\u0440",
-    "rdca;": "\u2937",
-    "rdldhar;": "\u2969",
-    "rdquo;": "\u201d",
-    "rdquor;": "\u201d",
-    "rdsh;": "\u21b3",
-    "real;": "\u211c",
-    "realine;": "\u211b",
-    "realpart;": "\u211c",
-    "reals;": "\u211d",
-    "rect;": "\u25ad",
-    "reg": "\xae",
-    "reg;": "\xae",
-    "rfisht;": "\u297d",
-    "rfloor;": "\u230b",
-    "rfr;": "\U0001d52f",
-    "rhard;": "\u21c1",
-    "rharu;": "\u21c0",
-    "rharul;": "\u296c",
-    "rho;": "\u03c1",
-    "rhov;": "\u03f1",
-    "rightarrow;": "\u2192",
-    "rightarrowtail;": "\u21a3",
-    "rightharpoondown;": "\u21c1",
-    "rightharpoonup;": "\u21c0",
-    "rightleftarrows;": "\u21c4",
-    "rightleftharpoons;": "\u21cc",
-    "rightrightarrows;": "\u21c9",
-    "rightsquigarrow;": "\u219d",
-    "rightthreetimes;": "\u22cc",
-    "ring;": "\u02da",
-    "risingdotseq;": "\u2253",
-    "rlarr;": "\u21c4",
-    "rlhar;": "\u21cc",
-    "rlm;": "\u200f",
-    "rmoust;": "\u23b1",
-    "rmoustache;": "\u23b1",
-    "rnmid;": "\u2aee",
-    "roang;": "\u27ed",
-    "roarr;": "\u21fe",
-    "robrk;": "\u27e7",
-    "ropar;": "\u2986",
-    "ropf;": "\U0001d563",
-    "roplus;": "\u2a2e",
-    "rotimes;": "\u2a35",
-    "rpar;": ")",
-    "rpargt;": "\u2994",
-    "rppolint;": "\u2a12",
-    "rrarr;": "\u21c9",
-    "rsaquo;": "\u203a",
-    "rscr;": "\U0001d4c7",
-    "rsh;": "\u21b1",
-    "rsqb;": "]",
-    "rsquo;": "\u2019",
-    "rsquor;": "\u2019",
-    "rthree;": "\u22cc",
-    "rtimes;": "\u22ca",
-    "rtri;": "\u25b9",
-    "rtrie;": "\u22b5",
-    "rtrif;": "\u25b8",
-    "rtriltri;": "\u29ce",
-    "ruluhar;": "\u2968",
-    "rx;": "\u211e",
-    "sacute;": "\u015b",
-    "sbquo;": "\u201a",
-    "sc;": "\u227b",
-    "scE;": "\u2ab4",
-    "scap;": "\u2ab8",
-    "scaron;": "\u0161",
-    "sccue;": "\u227d",
-    "sce;": "\u2ab0",
-    "scedil;": "\u015f",
-    "scirc;": "\u015d",
-    "scnE;": "\u2ab6",
-    "scnap;": "\u2aba",
-    "scnsim;": "\u22e9",
-    "scpolint;": "\u2a13",
-    "scsim;": "\u227f",
-    "scy;": "\u0441",
-    "sdot;": "\u22c5",
-    "sdotb;": "\u22a1",
-    "sdote;": "\u2a66",
-    "seArr;": "\u21d8",
-    "searhk;": "\u2925",
-    "searr;": "\u2198",
-    "searrow;": "\u2198",
-    "sect": "\xa7",
-    "sect;": "\xa7",
-    "semi;": ";",
-    "seswar;": "\u2929",
-    "setminus;": "\u2216",
-    "setmn;": "\u2216",
-    "sext;": "\u2736",
-    "sfr;": "\U0001d530",
-    "sfrown;": "\u2322",
-    "sharp;": "\u266f",
-    "shchcy;": "\u0449",
-    "shcy;": "\u0448",
-    "shortmid;": "\u2223",
-    "shortparallel;": "\u2225",
-    "shy": "\xad",
-    "shy;": "\xad",
-    "sigma;": "\u03c3",
-    "sigmaf;": "\u03c2",
-    "sigmav;": "\u03c2",
-    "sim;": "\u223c",
-    "simdot;": "\u2a6a",
-    "sime;": "\u2243",
-    "simeq;": "\u2243",
-    "simg;": "\u2a9e",
-    "simgE;": "\u2aa0",
-    "siml;": "\u2a9d",
-    "simlE;": "\u2a9f",
-    "simne;": "\u2246",
-    "simplus;": "\u2a24",
-    "simrarr;": "\u2972",
-    "slarr;": "\u2190",
-    "smallsetminus;": "\u2216",
-    "smashp;": "\u2a33",
-    "smeparsl;": "\u29e4",
-    "smid;": "\u2223",
-    "smile;": "\u2323",
-    "smt;": "\u2aaa",
-    "smte;": "\u2aac",
-    "smtes;": "\u2aac\ufe00",
-    "softcy;": "\u044c",
-    "sol;": "/",
-    "solb;": "\u29c4",
-    "solbar;": "\u233f",
-    "sopf;": "\U0001d564",
-    "spades;": "\u2660",
-    "spadesuit;": "\u2660",
-    "spar;": "\u2225",
-    "sqcap;": "\u2293",
-    "sqcaps;": "\u2293\ufe00",
-    "sqcup;": "\u2294",
-    "sqcups;": "\u2294\ufe00",
-    "sqsub;": "\u228f",
-    "sqsube;": "\u2291",
-    "sqsubset;": "\u228f",
-    "sqsubseteq;": "\u2291",
-    "sqsup;": "\u2290",
-    "sqsupe;": "\u2292",
-    "sqsupset;": "\u2290",
-    "sqsupseteq;": "\u2292",
-    "squ;": "\u25a1",
-    "square;": "\u25a1",
-    "squarf;": "\u25aa",
-    "squf;": "\u25aa",
-    "srarr;": "\u2192",
-    "sscr;": "\U0001d4c8",
-    "ssetmn;": "\u2216",
-    "ssmile;": "\u2323",
-    "sstarf;": "\u22c6",
-    "star;": "\u2606",
-    "starf;": "\u2605",
-    "straightepsilon;": "\u03f5",
-    "straightphi;": "\u03d5",
-    "strns;": "\xaf",
-    "sub;": "\u2282",
-    "subE;": "\u2ac5",
-    "subdot;": "\u2abd",
-    "sube;": "\u2286",
-    "subedot;": "\u2ac3",
-    "submult;": "\u2ac1",
-    "subnE;": "\u2acb",
-    "subne;": "\u228a",
-    "subplus;": "\u2abf",
-    "subrarr;": "\u2979",
-    "subset;": "\u2282",
-    "subseteq;": "\u2286",
-    "subseteqq;": "\u2ac5",
-    "subsetneq;": "\u228a",
-    "subsetneqq;": "\u2acb",
-    "subsim;": "\u2ac7",
-    "subsub;": "\u2ad5",
-    "subsup;": "\u2ad3",
-    "succ;": "\u227b",
-    "succapprox;": "\u2ab8",
-    "succcurlyeq;": "\u227d",
-    "succeq;": "\u2ab0",
-    "succnapprox;": "\u2aba",
-    "succneqq;": "\u2ab6",
-    "succnsim;": "\u22e9",
-    "succsim;": "\u227f",
-    "sum;": "\u2211",
-    "sung;": "\u266a",
-    "sup1": "\xb9",
-    "sup1;": "\xb9",
-    "sup2": "\xb2",
-    "sup2;": "\xb2",
-    "sup3": "\xb3",
-    "sup3;": "\xb3",
-    "sup;": "\u2283",
-    "supE;": "\u2ac6",
-    "supdot;": "\u2abe",
-    "supdsub;": "\u2ad8",
-    "supe;": "\u2287",
-    "supedot;": "\u2ac4",
-    "suphsol;": "\u27c9",
-    "suphsub;": "\u2ad7",
-    "suplarr;": "\u297b",
-    "supmult;": "\u2ac2",
-    "supnE;": "\u2acc",
-    "supne;": "\u228b",
-    "supplus;": "\u2ac0",
-    "supset;": "\u2283",
-    "supseteq;": "\u2287",
-    "supseteqq;": "\u2ac6",
-    "supsetneq;": "\u228b",
-    "supsetneqq;": "\u2acc",
-    "supsim;": "\u2ac8",
-    "supsub;": "\u2ad4",
-    "supsup;": "\u2ad6",
-    "swArr;": "\u21d9",
-    "swarhk;": "\u2926",
-    "swarr;": "\u2199",
-    "swarrow;": "\u2199",
-    "swnwar;": "\u292a",
-    "szlig": "\xdf",
-    "szlig;": "\xdf",
-    "target;": "\u2316",
-    "tau;": "\u03c4",
-    "tbrk;": "\u23b4",
-    "tcaron;": "\u0165",
-    "tcedil;": "\u0163",
-    "tcy;": "\u0442",
-    "tdot;": "\u20db",
-    "telrec;": "\u2315",
-    "tfr;": "\U0001d531",
-    "there4;": "\u2234",
-    "therefore;": "\u2234",
-    "theta;": "\u03b8",
-    "thetasym;": "\u03d1",
-    "thetav;": "\u03d1",
-    "thickapprox;": "\u2248",
-    "thicksim;": "\u223c",
-    "thinsp;": "\u2009",
-    "thkap;": "\u2248",
-    "thksim;": "\u223c",
-    "thorn": "\xfe",
-    "thorn;": "\xfe",
-    "tilde;": "\u02dc",
-    "times": "\xd7",
-    "times;": "\xd7",
-    "timesb;": "\u22a0",
-    "timesbar;": "\u2a31",
-    "timesd;": "\u2a30",
-    "tint;": "\u222d",
-    "toea;": "\u2928",
-    "top;": "\u22a4",
-    "topbot;": "\u2336",
-    "topcir;": "\u2af1",
-    "topf;": "\U0001d565",
-    "topfork;": "\u2ada",
-    "tosa;": "\u2929",
-    "tprime;": "\u2034",
-    "trade;": "\u2122",
-    "triangle;": "\u25b5",
-    "triangledown;": "\u25bf",
-    "triangleleft;": "\u25c3",
-    "trianglelefteq;": "\u22b4",
-    "triangleq;": "\u225c",
-    "triangleright;": "\u25b9",
-    "trianglerighteq;": "\u22b5",
-    "tridot;": "\u25ec",
-    "trie;": "\u225c",
-    "triminus;": "\u2a3a",
-    "triplus;": "\u2a39",
-    "trisb;": "\u29cd",
-    "tritime;": "\u2a3b",
-    "trpezium;": "\u23e2",
-    "tscr;": "\U0001d4c9",
-    "tscy;": "\u0446",
-    "tshcy;": "\u045b",
-    "tstrok;": "\u0167",
-    "twixt;": "\u226c",
-    "twoheadleftarrow;": "\u219e",
-    "twoheadrightarrow;": "\u21a0",
-    "uArr;": "\u21d1",
-    "uHar;": "\u2963",
-    "uacute": "\xfa",
-    "uacute;": "\xfa",
-    "uarr;": "\u2191",
-    "ubrcy;": "\u045e",
-    "ubreve;": "\u016d",
-    "ucirc": "\xfb",
-    "ucirc;": "\xfb",
-    "ucy;": "\u0443",
-    "udarr;": "\u21c5",
-    "udblac;": "\u0171",
-    "udhar;": "\u296e",
-    "ufisht;": "\u297e",
-    "ufr;": "\U0001d532",
-    "ugrave": "\xf9",
-    "ugrave;": "\xf9",
-    "uharl;": "\u21bf",
-    "uharr;": "\u21be",
-    "uhblk;": "\u2580",
-    "ulcorn;": "\u231c",
-    "ulcorner;": "\u231c",
-    "ulcrop;": "\u230f",
-    "ultri;": "\u25f8",
-    "umacr;": "\u016b",
-    "uml": "\xa8",
-    "uml;": "\xa8",
-    "uogon;": "\u0173",
-    "uopf;": "\U0001d566",
-    "uparrow;": "\u2191",
-    "updownarrow;": "\u2195",
-    "upharpoonleft;": "\u21bf",
-    "upharpoonright;": "\u21be",
-    "uplus;": "\u228e",
-    "upsi;": "\u03c5",
-    "upsih;": "\u03d2",
-    "upsilon;": "\u03c5",
-    "upuparrows;": "\u21c8",
-    "urcorn;": "\u231d",
-    "urcorner;": "\u231d",
-    "urcrop;": "\u230e",
-    "uring;": "\u016f",
-    "urtri;": "\u25f9",
-    "uscr;": "\U0001d4ca",
-    "utdot;": "\u22f0",
-    "utilde;": "\u0169",
-    "utri;": "\u25b5",
-    "utrif;": "\u25b4",
-    "uuarr;": "\u21c8",
-    "uuml": "\xfc",
-    "uuml;": "\xfc",
-    "uwangle;": "\u29a7",
-    "vArr;": "\u21d5",
-    "vBar;": "\u2ae8",
-    "vBarv;": "\u2ae9",
-    "vDash;": "\u22a8",
-    "vangrt;": "\u299c",
-    "varepsilon;": "\u03f5",
-    "varkappa;": "\u03f0",
-    "varnothing;": "\u2205",
-    "varphi;": "\u03d5",
-    "varpi;": "\u03d6",
-    "varpropto;": "\u221d",
-    "varr;": "\u2195",
-    "varrho;": "\u03f1",
-    "varsigma;": "\u03c2",
-    "varsubsetneq;": "\u228a\ufe00",
-    "varsubsetneqq;": "\u2acb\ufe00",
-    "varsupsetneq;": "\u228b\ufe00",
-    "varsupsetneqq;": "\u2acc\ufe00",
-    "vartheta;": "\u03d1",
-    "vartriangleleft;": "\u22b2",
-    "vartriangleright;": "\u22b3",
-    "vcy;": "\u0432",
-    "vdash;": "\u22a2",
-    "vee;": "\u2228",
-    "veebar;": "\u22bb",
-    "veeeq;": "\u225a",
-    "vellip;": "\u22ee",
-    "verbar;": "|",
-    "vert;": "|",
-    "vfr;": "\U0001d533",
-    "vltri;": "\u22b2",
-    "vnsub;": "\u2282\u20d2",
-    "vnsup;": "\u2283\u20d2",
-    "vopf;": "\U0001d567",
-    "vprop;": "\u221d",
-    "vrtri;": "\u22b3",
-    "vscr;": "\U0001d4cb",
-    "vsubnE;": "\u2acb\ufe00",
-    "vsubne;": "\u228a\ufe00",
-    "vsupnE;": "\u2acc\ufe00",
-    "vsupne;": "\u228b\ufe00",
-    "vzigzag;": "\u299a",
-    "wcirc;": "\u0175",
-    "wedbar;": "\u2a5f",
-    "wedge;": "\u2227",
-    "wedgeq;": "\u2259",
-    "weierp;": "\u2118",
-    "wfr;": "\U0001d534",
-    "wopf;": "\U0001d568",
-    "wp;": "\u2118",
-    "wr;": "\u2240",
-    "wreath;": "\u2240",
-    "wscr;": "\U0001d4cc",
-    "xcap;": "\u22c2",
-    "xcirc;": "\u25ef",
-    "xcup;": "\u22c3",
-    "xdtri;": "\u25bd",
-    "xfr;": "\U0001d535",
-    "xhArr;": "\u27fa",
-    "xharr;": "\u27f7",
-    "xi;": "\u03be",
-    "xlArr;": "\u27f8",
-    "xlarr;": "\u27f5",
-    "xmap;": "\u27fc",
-    "xnis;": "\u22fb",
-    "xodot;": "\u2a00",
-    "xopf;": "\U0001d569",
-    "xoplus;": "\u2a01",
-    "xotime;": "\u2a02",
-    "xrArr;": "\u27f9",
-    "xrarr;": "\u27f6",
-    "xscr;": "\U0001d4cd",
-    "xsqcup;": "\u2a06",
-    "xuplus;": "\u2a04",
-    "xutri;": "\u25b3",
-    "xvee;": "\u22c1",
-    "xwedge;": "\u22c0",
-    "yacute": "\xfd",
-    "yacute;": "\xfd",
-    "yacy;": "\u044f",
-    "ycirc;": "\u0177",
-    "ycy;": "\u044b",
-    "yen": "\xa5",
-    "yen;": "\xa5",
-    "yfr;": "\U0001d536",
-    "yicy;": "\u0457",
-    "yopf;": "\U0001d56a",
-    "yscr;": "\U0001d4ce",
-    "yucy;": "\u044e",
-    "yuml": "\xff",
-    "yuml;": "\xff",
-    "zacute;": "\u017a",
-    "zcaron;": "\u017e",
-    "zcy;": "\u0437",
-    "zdot;": "\u017c",
-    "zeetrf;": "\u2128",
-    "zeta;": "\u03b6",
-    "zfr;": "\U0001d537",
-    "zhcy;": "\u0436",
-    "zigrarr;": "\u21dd",
-    "zopf;": "\U0001d56b",
-    "zscr;": "\U0001d4cf",
-    "zwj;": "\u200d",
-    "zwnj;": "\u200c",
-}
-
-replacementCharacters = {
-    0x0: "\uFFFD",
-    0x0d: "\u000D",
-    0x80: "\u20AC",
-    0x81: "\u0081",
-    0x82: "\u201A",
-    0x83: "\u0192",
-    0x84: "\u201E",
-    0x85: "\u2026",
-    0x86: "\u2020",
-    0x87: "\u2021",
-    0x88: "\u02C6",
-    0x89: "\u2030",
-    0x8A: "\u0160",
-    0x8B: "\u2039",
-    0x8C: "\u0152",
-    0x8D: "\u008D",
-    0x8E: "\u017D",
-    0x8F: "\u008F",
-    0x90: "\u0090",
-    0x91: "\u2018",
-    0x92: "\u2019",
-    0x93: "\u201C",
-    0x94: "\u201D",
-    0x95: "\u2022",
-    0x96: "\u2013",
-    0x97: "\u2014",
-    0x98: "\u02DC",
-    0x99: "\u2122",
-    0x9A: "\u0161",
-    0x9B: "\u203A",
-    0x9C: "\u0153",
-    0x9D: "\u009D",
-    0x9E: "\u017E",
-    0x9F: "\u0178",
-}
-
-tokenTypes = {
-    "Doctype": 0,
-    "Characters": 1,
-    "SpaceCharacters": 2,
-    "StartTag": 3,
-    "EndTag": 4,
-    "EmptyTag": 5,
-    "Comment": 6,
-    "ParseError": 7
-}
-
-tagTokenTypes = frozenset([tokenTypes["StartTag"], tokenTypes["EndTag"],
-                           tokenTypes["EmptyTag"]])
-
-
-prefixes = dict([(v, k) for k, v in namespaces.items()])
-prefixes["http://www.w3.org/1998/Math/MathML"] = "math"
-
-
-class DataLossWarning(UserWarning):
-    """Raised when the current tree is unable to represent the input data"""
-    pass
-
-
-class _ReparseException(Exception):
-    pass
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/__init__.py
deleted file mode 100644
index e69de29..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/__init__.py
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/alphabeticalattributes.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/alphabeticalattributes.py
deleted file mode 100644
index 5ba926e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/alphabeticalattributes.py
+++ /dev/null
@@ -1,29 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from . import base
-
-from collections import OrderedDict
-
-
-def _attr_key(attr):
-    """Return an appropriate key for an attribute for sorting
-
-    Attributes have a namespace that can be either ``None`` or a string. We
-    can't compare the two because they're different types, so we convert
-    ``None`` to an empty string first.
-
-    """
-    return (attr[0][0] or ''), attr[0][1]
-
-
-class Filter(base.Filter):
-    """Alphabetizes attributes for elements"""
-    def __iter__(self):
-        for token in base.Filter.__iter__(self):
-            if token["type"] in ("StartTag", "EmptyTag"):
-                attrs = OrderedDict()
-                for name, value in sorted(token["data"].items(),
-                                          key=_attr_key):
-                    attrs[name] = value
-                token["data"] = attrs
-            yield token
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/base.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/base.py
deleted file mode 100644
index c7dbaed..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/base.py
+++ /dev/null
@@ -1,12 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-
-class Filter(object):
-    def __init__(self, source):
-        self.source = source
-
-    def __iter__(self):
-        return iter(self.source)
-
-    def __getattr__(self, name):
-        return getattr(self.source, name)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/inject_meta_charset.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/inject_meta_charset.py
deleted file mode 100644
index aefb5c8..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/inject_meta_charset.py
+++ /dev/null
@@ -1,73 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from . import base
-
-
-class Filter(base.Filter):
-    """Injects ``<meta charset=ENCODING>`` tag into head of document"""
-    def __init__(self, source, encoding):
-        """Creates a Filter
-
-        :arg source: the source token stream
-
-        :arg encoding: the encoding to set
-
-        """
-        base.Filter.__init__(self, source)
-        self.encoding = encoding
-
-    def __iter__(self):
-        state = "pre_head"
-        meta_found = (self.encoding is None)
-        pending = []
-
-        for token in base.Filter.__iter__(self):
-            type = token["type"]
-            if type == "StartTag":
-                if token["name"].lower() == "head":
-                    state = "in_head"
-
-            elif type == "EmptyTag":
-                if token["name"].lower() == "meta":
-                    # replace charset with actual encoding
-                    has_http_equiv_content_type = False
-                    for (namespace, name), value in token["data"].items():
-                        if namespace is not None:
-                            continue
-                        elif name.lower() == 'charset':
-                            token["data"][(namespace, name)] = self.encoding
-                            meta_found = True
-                            break
-                        elif name == 'http-equiv' and value.lower() == 'content-type':
-                            has_http_equiv_content_type = True
-                    else:
-                        if has_http_equiv_content_type and (None, "content") in token["data"]:
-                            token["data"][(None, "content")] = 'text/html; charset=%s' % self.encoding
-                            meta_found = True
-
-                elif token["name"].lower() == "head" and not meta_found:
-                    # insert meta into empty head
-                    yield {"type": "StartTag", "name": "head",
-                           "data": token["data"]}
-                    yield {"type": "EmptyTag", "name": "meta",
-                           "data": {(None, "charset"): self.encoding}}
-                    yield {"type": "EndTag", "name": "head"}
-                    meta_found = True
-                    continue
-
-            elif type == "EndTag":
-                if token["name"].lower() == "head" and pending:
-                    # insert meta into head (if necessary) and flush pending queue
-                    yield pending.pop(0)
-                    if not meta_found:
-                        yield {"type": "EmptyTag", "name": "meta",
-                               "data": {(None, "charset"): self.encoding}}
-                    while pending:
-                        yield pending.pop(0)
-                    meta_found = True
-                    state = "post_head"
-
-            if state == "in_head":
-                pending.append(token)
-            else:
-                yield token
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/lint.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/lint.py
deleted file mode 100644
index fcc07ee..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/lint.py
+++ /dev/null
@@ -1,93 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from pip._vendor.six import text_type
-
-from . import base
-from ..constants import namespaces, voidElements
-
-from ..constants import spaceCharacters
-spaceCharacters = "".join(spaceCharacters)
-
-
-class Filter(base.Filter):
-    """Lints the token stream for errors
-
-    If it finds any errors, it'll raise an ``AssertionError``.
-
-    """
-    def __init__(self, source, require_matching_tags=True):
-        """Creates a Filter
-
-        :arg source: the source token stream
-
-        :arg require_matching_tags: whether or not to require matching tags
-
-        """
-        super(Filter, self).__init__(source)
-        self.require_matching_tags = require_matching_tags
-
-    def __iter__(self):
-        open_elements = []
-        for token in base.Filter.__iter__(self):
-            type = token["type"]
-            if type in ("StartTag", "EmptyTag"):
-                namespace = token["namespace"]
-                name = token["name"]
-                assert namespace is None or isinstance(namespace, text_type)
-                assert namespace != ""
-                assert isinstance(name, text_type)
-                assert name != ""
-                assert isinstance(token["data"], dict)
-                if (not namespace or namespace == namespaces["html"]) and name in voidElements:
-                    assert type == "EmptyTag"
-                else:
-                    assert type == "StartTag"
-                if type == "StartTag" and self.require_matching_tags:
-                    open_elements.append((namespace, name))
-                for (namespace, name), value in token["data"].items():
-                    assert namespace is None or isinstance(namespace, text_type)
-                    assert namespace != ""
-                    assert isinstance(name, text_type)
-                    assert name != ""
-                    assert isinstance(value, text_type)
-
-            elif type == "EndTag":
-                namespace = token["namespace"]
-                name = token["name"]
-                assert namespace is None or isinstance(namespace, text_type)
-                assert namespace != ""
-                assert isinstance(name, text_type)
-                assert name != ""
-                if (not namespace or namespace == namespaces["html"]) and name in voidElements:
-                    assert False, "Void element reported as EndTag token: %(tag)s" % {"tag": name}
-                elif self.require_matching_tags:
-                    start = open_elements.pop()
-                    assert start == (namespace, name)
-
-            elif type == "Comment":
-                data = token["data"]
-                assert isinstance(data, text_type)
-
-            elif type in ("Characters", "SpaceCharacters"):
-                data = token["data"]
-                assert isinstance(data, text_type)
-                assert data != ""
-                if type == "SpaceCharacters":
-                    assert data.strip(spaceCharacters) == ""
-
-            elif type == "Doctype":
-                name = token["name"]
-                assert name is None or isinstance(name, text_type)
-                assert token["publicId"] is None or isinstance(name, text_type)
-                assert token["systemId"] is None or isinstance(name, text_type)
-
-            elif type == "Entity":
-                assert isinstance(token["name"], text_type)
-
-            elif type == "SerializerError":
-                assert isinstance(token["data"], text_type)
-
-            else:
-                assert False, "Unknown token type: %(type)s" % {"type": type}
-
-            yield token
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/optionaltags.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/optionaltags.py
deleted file mode 100644
index 4a86501..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/optionaltags.py
+++ /dev/null
@@ -1,207 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from . import base
-
-
-class Filter(base.Filter):
-    """Removes optional tags from the token stream"""
-    def slider(self):
-        previous1 = previous2 = None
-        for token in self.source:
-            if previous1 is not None:
-                yield previous2, previous1, token
-            previous2 = previous1
-            previous1 = token
-        if previous1 is not None:
-            yield previous2, previous1, None
-
-    def __iter__(self):
-        for previous, token, next in self.slider():
-            type = token["type"]
-            if type == "StartTag":
-                if (token["data"] or
-                        not self.is_optional_start(token["name"], previous, next)):
-                    yield token
-            elif type == "EndTag":
-                if not self.is_optional_end(token["name"], next):
-                    yield token
-            else:
-                yield token
-
-    def is_optional_start(self, tagname, previous, next):
-        type = next and next["type"] or None
-        if tagname in 'html':
-            # An html element's start tag may be omitted if the first thing
-            # inside the html element is not a space character or a comment.
-            return type not in ("Comment", "SpaceCharacters")
-        elif tagname == 'head':
-            # A head element's start tag may be omitted if the first thing
-            # inside the head element is an element.
-            # XXX: we also omit the start tag if the head element is empty
-            if type in ("StartTag", "EmptyTag"):
-                return True
-            elif type == "EndTag":
-                return next["name"] == "head"
-        elif tagname == 'body':
-            # A body element's start tag may be omitted if the first thing
-            # inside the body element is not a space character or a comment,
-            # except if the first thing inside the body element is a script
-            # or style element and the node immediately preceding the body
-            # element is a head element whose end tag has been omitted.
-            if type in ("Comment", "SpaceCharacters"):
-                return False
-            elif type == "StartTag":
-                # XXX: we do not look at the preceding event, so we never omit
-                # the body element's start tag if it's followed by a script or
-                # a style element.
-                return next["name"] not in ('script', 'style')
-            else:
-                return True
-        elif tagname == 'colgroup':
-            # A colgroup element's start tag may be omitted if the first thing
-            # inside the colgroup element is a col element, and if the element
-            # is not immediately preceded by another colgroup element whose
-            # end tag has been omitted.
-            if type in ("StartTag", "EmptyTag"):
-                # XXX: we do not look at the preceding event, so instead we never
-                # omit the colgroup element's end tag when it is immediately
-                # followed by another colgroup element. See is_optional_end.
-                return next["name"] == "col"
-            else:
-                return False
-        elif tagname == 'tbody':
-            # A tbody element's start tag may be omitted if the first thing
-            # inside the tbody element is a tr element, and if the element is
-            # not immediately preceded by a tbody, thead, or tfoot element
-            # whose end tag has been omitted.
-            if type == "StartTag":
-                # omit the thead and tfoot elements' end tag when they are
-                # immediately followed by a tbody element. See is_optional_end.
-                if previous and previous['type'] == 'EndTag' and \
-                        previous['name'] in ('tbody', 'thead', 'tfoot'):
-                    return False
-                return next["name"] == 'tr'
-            else:
-                return False
-        return False
-
-    def is_optional_end(self, tagname, next):
-        type = next and next["type"] or None
-        if tagname in ('html', 'head', 'body'):
-            # An html element's end tag may be omitted if the html element
-            # is not immediately followed by a space character or a comment.
-            return type not in ("Comment", "SpaceCharacters")
-        elif tagname in ('li', 'optgroup', 'tr'):
-            # A li element's end tag may be omitted if the li element is
-            # immediately followed by another li element or if there is
-            # no more content in the parent element.
-            # An optgroup element's end tag may be omitted if the optgroup
-            # element is immediately followed by another optgroup element,
-            # or if there is no more content in the parent element.
-            # A tr element's end tag may be omitted if the tr element is
-            # immediately followed by another tr element, or if there is
-            # no more content in the parent element.
-            if type == "StartTag":
-                return next["name"] == tagname
-            else:
-                return type == "EndTag" or type is None
-        elif tagname in ('dt', 'dd'):
-            # A dt element's end tag may be omitted if the dt element is
-            # immediately followed by another dt element or a dd element.
-            # A dd element's end tag may be omitted if the dd element is
-            # immediately followed by another dd element or a dt element,
-            # or if there is no more content in the parent element.
-            if type == "StartTag":
-                return next["name"] in ('dt', 'dd')
-            elif tagname == 'dd':
-                return type == "EndTag" or type is None
-            else:
-                return False
-        elif tagname == 'p':
-            # A p element's end tag may be omitted if the p element is
-            # immediately followed by an address, article, aside,
-            # blockquote, datagrid, dialog, dir, div, dl, fieldset,
-            # footer, form, h1, h2, h3, h4, h5, h6, header, hr, menu,
-            # nav, ol, p, pre, section, table, or ul, element, or if
-            # there is no more content in the parent element.
-            if type in ("StartTag", "EmptyTag"):
-                return next["name"] in ('address', 'article', 'aside',
-                                        'blockquote', 'datagrid', 'dialog',
-                                        'dir', 'div', 'dl', 'fieldset', 'footer',
-                                        'form', 'h1', 'h2', 'h3', 'h4', 'h5', 'h6',
-                                        'header', 'hr', 'menu', 'nav', 'ol',
-                                        'p', 'pre', 'section', 'table', 'ul')
-            else:
-                return type == "EndTag" or type is None
-        elif tagname == 'option':
-            # An option element's end tag may be omitted if the option
-            # element is immediately followed by another option element,
-            # or if it is immediately followed by an <code>optgroup</code>
-            # element, or if there is no more content in the parent
-            # element.
-            if type == "StartTag":
-                return next["name"] in ('option', 'optgroup')
-            else:
-                return type == "EndTag" or type is None
-        elif tagname in ('rt', 'rp'):
-            # An rt element's end tag may be omitted if the rt element is
-            # immediately followed by an rt or rp element, or if there is
-            # no more content in the parent element.
-            # An rp element's end tag may be omitted if the rp element is
-            # immediately followed by an rt or rp element, or if there is
-            # no more content in the parent element.
-            if type == "StartTag":
-                return next["name"] in ('rt', 'rp')
-            else:
-                return type == "EndTag" or type is None
-        elif tagname == 'colgroup':
-            # A colgroup element's end tag may be omitted if the colgroup
-            # element is not immediately followed by a space character or
-            # a comment.
-            if type in ("Comment", "SpaceCharacters"):
-                return False
-            elif type == "StartTag":
-                # XXX: we also look for an immediately following colgroup
-                # element. See is_optional_start.
-                return next["name"] != 'colgroup'
-            else:
-                return True
-        elif tagname in ('thead', 'tbody'):
-            # A thead element's end tag may be omitted if the thead element
-            # is immediately followed by a tbody or tfoot element.
-            # A tbody element's end tag may be omitted if the tbody element
-            # is immediately followed by a tbody or tfoot element, or if
-            # there is no more content in the parent element.
-            # A tfoot element's end tag may be omitted if the tfoot element
-            # is immediately followed by a tbody element, or if there is no
-            # more content in the parent element.
-            # XXX: we never omit the end tag when the following element is
-            # a tbody. See is_optional_start.
-            if type == "StartTag":
-                return next["name"] in ['tbody', 'tfoot']
-            elif tagname == 'tbody':
-                return type == "EndTag" or type is None
-            else:
-                return False
-        elif tagname == 'tfoot':
-            # A tfoot element's end tag may be omitted if the tfoot element
-            # is immediately followed by a tbody element, or if there is no
-            # more content in the parent element.
-            # XXX: we never omit the end tag when the following element is
-            # a tbody. See is_optional_start.
-            if type == "StartTag":
-                return next["name"] == 'tbody'
-            else:
-                return type == "EndTag" or type is None
-        elif tagname in ('td', 'th'):
-            # A td element's end tag may be omitted if the td element is
-            # immediately followed by a td or th element, or if there is
-            # no more content in the parent element.
-            # A th element's end tag may be omitted if the th element is
-            # immediately followed by a td or th element, or if there is
-            # no more content in the parent element.
-            if type == "StartTag":
-                return next["name"] in ('td', 'th')
-            else:
-                return type == "EndTag" or type is None
-        return False
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/sanitizer.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/sanitizer.py
deleted file mode 100644
index af8e77b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/sanitizer.py
+++ /dev/null
@@ -1,896 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-import re
-from xml.sax.saxutils import escape, unescape
-
-from pip._vendor.six.moves import urllib_parse as urlparse
-
-from . import base
-from ..constants import namespaces, prefixes
-
-__all__ = ["Filter"]
-
-
-allowed_elements = frozenset((
-    (namespaces['html'], 'a'),
-    (namespaces['html'], 'abbr'),
-    (namespaces['html'], 'acronym'),
-    (namespaces['html'], 'address'),
-    (namespaces['html'], 'area'),
-    (namespaces['html'], 'article'),
-    (namespaces['html'], 'aside'),
-    (namespaces['html'], 'audio'),
-    (namespaces['html'], 'b'),
-    (namespaces['html'], 'big'),
-    (namespaces['html'], 'blockquote'),
-    (namespaces['html'], 'br'),
-    (namespaces['html'], 'button'),
-    (namespaces['html'], 'canvas'),
-    (namespaces['html'], 'caption'),
-    (namespaces['html'], 'center'),
-    (namespaces['html'], 'cite'),
-    (namespaces['html'], 'code'),
-    (namespaces['html'], 'col'),
-    (namespaces['html'], 'colgroup'),
-    (namespaces['html'], 'command'),
-    (namespaces['html'], 'datagrid'),
-    (namespaces['html'], 'datalist'),
-    (namespaces['html'], 'dd'),
-    (namespaces['html'], 'del'),
-    (namespaces['html'], 'details'),
-    (namespaces['html'], 'dfn'),
-    (namespaces['html'], 'dialog'),
-    (namespaces['html'], 'dir'),
-    (namespaces['html'], 'div'),
-    (namespaces['html'], 'dl'),
-    (namespaces['html'], 'dt'),
-    (namespaces['html'], 'em'),
-    (namespaces['html'], 'event-source'),
-    (namespaces['html'], 'fieldset'),
-    (namespaces['html'], 'figcaption'),
-    (namespaces['html'], 'figure'),
-    (namespaces['html'], 'footer'),
-    (namespaces['html'], 'font'),
-    (namespaces['html'], 'form'),
-    (namespaces['html'], 'header'),
-    (namespaces['html'], 'h1'),
-    (namespaces['html'], 'h2'),
-    (namespaces['html'], 'h3'),
-    (namespaces['html'], 'h4'),
-    (namespaces['html'], 'h5'),
-    (namespaces['html'], 'h6'),
-    (namespaces['html'], 'hr'),
-    (namespaces['html'], 'i'),
-    (namespaces['html'], 'img'),
-    (namespaces['html'], 'input'),
-    (namespaces['html'], 'ins'),
-    (namespaces['html'], 'keygen'),
-    (namespaces['html'], 'kbd'),
-    (namespaces['html'], 'label'),
-    (namespaces['html'], 'legend'),
-    (namespaces['html'], 'li'),
-    (namespaces['html'], 'm'),
-    (namespaces['html'], 'map'),
-    (namespaces['html'], 'menu'),
-    (namespaces['html'], 'meter'),
-    (namespaces['html'], 'multicol'),
-    (namespaces['html'], 'nav'),
-    (namespaces['html'], 'nextid'),
-    (namespaces['html'], 'ol'),
-    (namespaces['html'], 'output'),
-    (namespaces['html'], 'optgroup'),
-    (namespaces['html'], 'option'),
-    (namespaces['html'], 'p'),
-    (namespaces['html'], 'pre'),
-    (namespaces['html'], 'progress'),
-    (namespaces['html'], 'q'),
-    (namespaces['html'], 's'),
-    (namespaces['html'], 'samp'),
-    (namespaces['html'], 'section'),
-    (namespaces['html'], 'select'),
-    (namespaces['html'], 'small'),
-    (namespaces['html'], 'sound'),
-    (namespaces['html'], 'source'),
-    (namespaces['html'], 'spacer'),
-    (namespaces['html'], 'span'),
-    (namespaces['html'], 'strike'),
-    (namespaces['html'], 'strong'),
-    (namespaces['html'], 'sub'),
-    (namespaces['html'], 'sup'),
-    (namespaces['html'], 'table'),
-    (namespaces['html'], 'tbody'),
-    (namespaces['html'], 'td'),
-    (namespaces['html'], 'textarea'),
-    (namespaces['html'], 'time'),
-    (namespaces['html'], 'tfoot'),
-    (namespaces['html'], 'th'),
-    (namespaces['html'], 'thead'),
-    (namespaces['html'], 'tr'),
-    (namespaces['html'], 'tt'),
-    (namespaces['html'], 'u'),
-    (namespaces['html'], 'ul'),
-    (namespaces['html'], 'var'),
-    (namespaces['html'], 'video'),
-    (namespaces['mathml'], 'maction'),
-    (namespaces['mathml'], 'math'),
-    (namespaces['mathml'], 'merror'),
-    (namespaces['mathml'], 'mfrac'),
-    (namespaces['mathml'], 'mi'),
-    (namespaces['mathml'], 'mmultiscripts'),
-    (namespaces['mathml'], 'mn'),
-    (namespaces['mathml'], 'mo'),
-    (namespaces['mathml'], 'mover'),
-    (namespaces['mathml'], 'mpadded'),
-    (namespaces['mathml'], 'mphantom'),
-    (namespaces['mathml'], 'mprescripts'),
-    (namespaces['mathml'], 'mroot'),
-    (namespaces['mathml'], 'mrow'),
-    (namespaces['mathml'], 'mspace'),
-    (namespaces['mathml'], 'msqrt'),
-    (namespaces['mathml'], 'mstyle'),
-    (namespaces['mathml'], 'msub'),
-    (namespaces['mathml'], 'msubsup'),
-    (namespaces['mathml'], 'msup'),
-    (namespaces['mathml'], 'mtable'),
-    (namespaces['mathml'], 'mtd'),
-    (namespaces['mathml'], 'mtext'),
-    (namespaces['mathml'], 'mtr'),
-    (namespaces['mathml'], 'munder'),
-    (namespaces['mathml'], 'munderover'),
-    (namespaces['mathml'], 'none'),
-    (namespaces['svg'], 'a'),
-    (namespaces['svg'], 'animate'),
-    (namespaces['svg'], 'animateColor'),
-    (namespaces['svg'], 'animateMotion'),
-    (namespaces['svg'], 'animateTransform'),
-    (namespaces['svg'], 'clipPath'),
-    (namespaces['svg'], 'circle'),
-    (namespaces['svg'], 'defs'),
-    (namespaces['svg'], 'desc'),
-    (namespaces['svg'], 'ellipse'),
-    (namespaces['svg'], 'font-face'),
-    (namespaces['svg'], 'font-face-name'),
-    (namespaces['svg'], 'font-face-src'),
-    (namespaces['svg'], 'g'),
-    (namespaces['svg'], 'glyph'),
-    (namespaces['svg'], 'hkern'),
-    (namespaces['svg'], 'linearGradient'),
-    (namespaces['svg'], 'line'),
-    (namespaces['svg'], 'marker'),
-    (namespaces['svg'], 'metadata'),
-    (namespaces['svg'], 'missing-glyph'),
-    (namespaces['svg'], 'mpath'),
-    (namespaces['svg'], 'path'),
-    (namespaces['svg'], 'polygon'),
-    (namespaces['svg'], 'polyline'),
-    (namespaces['svg'], 'radialGradient'),
-    (namespaces['svg'], 'rect'),
-    (namespaces['svg'], 'set'),
-    (namespaces['svg'], 'stop'),
-    (namespaces['svg'], 'svg'),
-    (namespaces['svg'], 'switch'),
-    (namespaces['svg'], 'text'),
-    (namespaces['svg'], 'title'),
-    (namespaces['svg'], 'tspan'),
-    (namespaces['svg'], 'use'),
-))
-
-allowed_attributes = frozenset((
-    # HTML attributes
-    (None, 'abbr'),
-    (None, 'accept'),
-    (None, 'accept-charset'),
-    (None, 'accesskey'),
-    (None, 'action'),
-    (None, 'align'),
-    (None, 'alt'),
-    (None, 'autocomplete'),
-    (None, 'autofocus'),
-    (None, 'axis'),
-    (None, 'background'),
-    (None, 'balance'),
-    (None, 'bgcolor'),
-    (None, 'bgproperties'),
-    (None, 'border'),
-    (None, 'bordercolor'),
-    (None, 'bordercolordark'),
-    (None, 'bordercolorlight'),
-    (None, 'bottompadding'),
-    (None, 'cellpadding'),
-    (None, 'cellspacing'),
-    (None, 'ch'),
-    (None, 'challenge'),
-    (None, 'char'),
-    (None, 'charoff'),
-    (None, 'choff'),
-    (None, 'charset'),
-    (None, 'checked'),
-    (None, 'cite'),
-    (None, 'class'),
-    (None, 'clear'),
-    (None, 'color'),
-    (None, 'cols'),
-    (None, 'colspan'),
-    (None, 'compact'),
-    (None, 'contenteditable'),
-    (None, 'controls'),
-    (None, 'coords'),
-    (None, 'data'),
-    (None, 'datafld'),
-    (None, 'datapagesize'),
-    (None, 'datasrc'),
-    (None, 'datetime'),
-    (None, 'default'),
-    (None, 'delay'),
-    (None, 'dir'),
-    (None, 'disabled'),
-    (None, 'draggable'),
-    (None, 'dynsrc'),
-    (None, 'enctype'),
-    (None, 'end'),
-    (None, 'face'),
-    (None, 'for'),
-    (None, 'form'),
-    (None, 'frame'),
-    (None, 'galleryimg'),
-    (None, 'gutter'),
-    (None, 'headers'),
-    (None, 'height'),
-    (None, 'hidefocus'),
-    (None, 'hidden'),
-    (None, 'high'),
-    (None, 'href'),
-    (None, 'hreflang'),
-    (None, 'hspace'),
-    (None, 'icon'),
-    (None, 'id'),
-    (None, 'inputmode'),
-    (None, 'ismap'),
-    (None, 'keytype'),
-    (None, 'label'),
-    (None, 'leftspacing'),
-    (None, 'lang'),
-    (None, 'list'),
-    (None, 'longdesc'),
-    (None, 'loop'),
-    (None, 'loopcount'),
-    (None, 'loopend'),
-    (None, 'loopstart'),
-    (None, 'low'),
-    (None, 'lowsrc'),
-    (None, 'max'),
-    (None, 'maxlength'),
-    (None, 'media'),
-    (None, 'method'),
-    (None, 'min'),
-    (None, 'multiple'),
-    (None, 'name'),
-    (None, 'nohref'),
-    (None, 'noshade'),
-    (None, 'nowrap'),
-    (None, 'open'),
-    (None, 'optimum'),
-    (None, 'pattern'),
-    (None, 'ping'),
-    (None, 'point-size'),
-    (None, 'poster'),
-    (None, 'pqg'),
-    (None, 'preload'),
-    (None, 'prompt'),
-    (None, 'radiogroup'),
-    (None, 'readonly'),
-    (None, 'rel'),
-    (None, 'repeat-max'),
-    (None, 'repeat-min'),
-    (None, 'replace'),
-    (None, 'required'),
-    (None, 'rev'),
-    (None, 'rightspacing'),
-    (None, 'rows'),
-    (None, 'rowspan'),
-    (None, 'rules'),
-    (None, 'scope'),
-    (None, 'selected'),
-    (None, 'shape'),
-    (None, 'size'),
-    (None, 'span'),
-    (None, 'src'),
-    (None, 'start'),
-    (None, 'step'),
-    (None, 'style'),
-    (None, 'summary'),
-    (None, 'suppress'),
-    (None, 'tabindex'),
-    (None, 'target'),
-    (None, 'template'),
-    (None, 'title'),
-    (None, 'toppadding'),
-    (None, 'type'),
-    (None, 'unselectable'),
-    (None, 'usemap'),
-    (None, 'urn'),
-    (None, 'valign'),
-    (None, 'value'),
-    (None, 'variable'),
-    (None, 'volume'),
-    (None, 'vspace'),
-    (None, 'vrml'),
-    (None, 'width'),
-    (None, 'wrap'),
-    (namespaces['xml'], 'lang'),
-    # MathML attributes
-    (None, 'actiontype'),
-    (None, 'align'),
-    (None, 'columnalign'),
-    (None, 'columnalign'),
-    (None, 'columnalign'),
-    (None, 'columnlines'),
-    (None, 'columnspacing'),
-    (None, 'columnspan'),
-    (None, 'depth'),
-    (None, 'display'),
-    (None, 'displaystyle'),
-    (None, 'equalcolumns'),
-    (None, 'equalrows'),
-    (None, 'fence'),
-    (None, 'fontstyle'),
-    (None, 'fontweight'),
-    (None, 'frame'),
-    (None, 'height'),
-    (None, 'linethickness'),
-    (None, 'lspace'),
-    (None, 'mathbackground'),
-    (None, 'mathcolor'),
-    (None, 'mathvariant'),
-    (None, 'mathvariant'),
-    (None, 'maxsize'),
-    (None, 'minsize'),
-    (None, 'other'),
-    (None, 'rowalign'),
-    (None, 'rowalign'),
-    (None, 'rowalign'),
-    (None, 'rowlines'),
-    (None, 'rowspacing'),
-    (None, 'rowspan'),
-    (None, 'rspace'),
-    (None, 'scriptlevel'),
-    (None, 'selection'),
-    (None, 'separator'),
-    (None, 'stretchy'),
-    (None, 'width'),
-    (None, 'width'),
-    (namespaces['xlink'], 'href'),
-    (namespaces['xlink'], 'show'),
-    (namespaces['xlink'], 'type'),
-    # SVG attributes
-    (None, 'accent-height'),
-    (None, 'accumulate'),
-    (None, 'additive'),
-    (None, 'alphabetic'),
-    (None, 'arabic-form'),
-    (None, 'ascent'),
-    (None, 'attributeName'),
-    (None, 'attributeType'),
-    (None, 'baseProfile'),
-    (None, 'bbox'),
-    (None, 'begin'),
-    (None, 'by'),
-    (None, 'calcMode'),
-    (None, 'cap-height'),
-    (None, 'class'),
-    (None, 'clip-path'),
-    (None, 'color'),
-    (None, 'color-rendering'),
-    (None, 'content'),
-    (None, 'cx'),
-    (None, 'cy'),
-    (None, 'd'),
-    (None, 'dx'),
-    (None, 'dy'),
-    (None, 'descent'),
-    (None, 'display'),
-    (None, 'dur'),
-    (None, 'end'),
-    (None, 'fill'),
-    (None, 'fill-opacity'),
-    (None, 'fill-rule'),
-    (None, 'font-family'),
-    (None, 'font-size'),
-    (None, 'font-stretch'),
-    (None, 'font-style'),
-    (None, 'font-variant'),
-    (None, 'font-weight'),
-    (None, 'from'),
-    (None, 'fx'),
-    (None, 'fy'),
-    (None, 'g1'),
-    (None, 'g2'),
-    (None, 'glyph-name'),
-    (None, 'gradientUnits'),
-    (None, 'hanging'),
-    (None, 'height'),
-    (None, 'horiz-adv-x'),
-    (None, 'horiz-origin-x'),
-    (None, 'id'),
-    (None, 'ideographic'),
-    (None, 'k'),
-    (None, 'keyPoints'),
-    (None, 'keySplines'),
-    (None, 'keyTimes'),
-    (None, 'lang'),
-    (None, 'marker-end'),
-    (None, 'marker-mid'),
-    (None, 'marker-start'),
-    (None, 'markerHeight'),
-    (None, 'markerUnits'),
-    (None, 'markerWidth'),
-    (None, 'mathematical'),
-    (None, 'max'),
-    (None, 'min'),
-    (None, 'name'),
-    (None, 'offset'),
-    (None, 'opacity'),
-    (None, 'orient'),
-    (None, 'origin'),
-    (None, 'overline-position'),
-    (None, 'overline-thickness'),
-    (None, 'panose-1'),
-    (None, 'path'),
-    (None, 'pathLength'),
-    (None, 'points'),
-    (None, 'preserveAspectRatio'),
-    (None, 'r'),
-    (None, 'refX'),
-    (None, 'refY'),
-    (None, 'repeatCount'),
-    (None, 'repeatDur'),
-    (None, 'requiredExtensions'),
-    (None, 'requiredFeatures'),
-    (None, 'restart'),
-    (None, 'rotate'),
-    (None, 'rx'),
-    (None, 'ry'),
-    (None, 'slope'),
-    (None, 'stemh'),
-    (None, 'stemv'),
-    (None, 'stop-color'),
-    (None, 'stop-opacity'),
-    (None, 'strikethrough-position'),
-    (None, 'strikethrough-thickness'),
-    (None, 'stroke'),
-    (None, 'stroke-dasharray'),
-    (None, 'stroke-dashoffset'),
-    (None, 'stroke-linecap'),
-    (None, 'stroke-linejoin'),
-    (None, 'stroke-miterlimit'),
-    (None, 'stroke-opacity'),
-    (None, 'stroke-width'),
-    (None, 'systemLanguage'),
-    (None, 'target'),
-    (None, 'text-anchor'),
-    (None, 'to'),
-    (None, 'transform'),
-    (None, 'type'),
-    (None, 'u1'),
-    (None, 'u2'),
-    (None, 'underline-position'),
-    (None, 'underline-thickness'),
-    (None, 'unicode'),
-    (None, 'unicode-range'),
-    (None, 'units-per-em'),
-    (None, 'values'),
-    (None, 'version'),
-    (None, 'viewBox'),
-    (None, 'visibility'),
-    (None, 'width'),
-    (None, 'widths'),
-    (None, 'x'),
-    (None, 'x-height'),
-    (None, 'x1'),
-    (None, 'x2'),
-    (namespaces['xlink'], 'actuate'),
-    (namespaces['xlink'], 'arcrole'),
-    (namespaces['xlink'], 'href'),
-    (namespaces['xlink'], 'role'),
-    (namespaces['xlink'], 'show'),
-    (namespaces['xlink'], 'title'),
-    (namespaces['xlink'], 'type'),
-    (namespaces['xml'], 'base'),
-    (namespaces['xml'], 'lang'),
-    (namespaces['xml'], 'space'),
-    (None, 'y'),
-    (None, 'y1'),
-    (None, 'y2'),
-    (None, 'zoomAndPan'),
-))
-
-attr_val_is_uri = frozenset((
-    (None, 'href'),
-    (None, 'src'),
-    (None, 'cite'),
-    (None, 'action'),
-    (None, 'longdesc'),
-    (None, 'poster'),
-    (None, 'background'),
-    (None, 'datasrc'),
-    (None, 'dynsrc'),
-    (None, 'lowsrc'),
-    (None, 'ping'),
-    (namespaces['xlink'], 'href'),
-    (namespaces['xml'], 'base'),
-))
-
-svg_attr_val_allows_ref = frozenset((
-    (None, 'clip-path'),
-    (None, 'color-profile'),
-    (None, 'cursor'),
-    (None, 'fill'),
-    (None, 'filter'),
-    (None, 'marker'),
-    (None, 'marker-start'),
-    (None, 'marker-mid'),
-    (None, 'marker-end'),
-    (None, 'mask'),
-    (None, 'stroke'),
-))
-
-svg_allow_local_href = frozenset((
-    (None, 'altGlyph'),
-    (None, 'animate'),
-    (None, 'animateColor'),
-    (None, 'animateMotion'),
-    (None, 'animateTransform'),
-    (None, 'cursor'),
-    (None, 'feImage'),
-    (None, 'filter'),
-    (None, 'linearGradient'),
-    (None, 'pattern'),
-    (None, 'radialGradient'),
-    (None, 'textpath'),
-    (None, 'tref'),
-    (None, 'set'),
-    (None, 'use')
-))
-
-allowed_css_properties = frozenset((
-    'azimuth',
-    'background-color',
-    'border-bottom-color',
-    'border-collapse',
-    'border-color',
-    'border-left-color',
-    'border-right-color',
-    'border-top-color',
-    'clear',
-    'color',
-    'cursor',
-    'direction',
-    'display',
-    'elevation',
-    'float',
-    'font',
-    'font-family',
-    'font-size',
-    'font-style',
-    'font-variant',
-    'font-weight',
-    'height',
-    'letter-spacing',
-    'line-height',
-    'overflow',
-    'pause',
-    'pause-after',
-    'pause-before',
-    'pitch',
-    'pitch-range',
-    'richness',
-    'speak',
-    'speak-header',
-    'speak-numeral',
-    'speak-punctuation',
-    'speech-rate',
-    'stress',
-    'text-align',
-    'text-decoration',
-    'text-indent',
-    'unicode-bidi',
-    'vertical-align',
-    'voice-family',
-    'volume',
-    'white-space',
-    'width',
-))
-
-allowed_css_keywords = frozenset((
-    'auto',
-    'aqua',
-    'black',
-    'block',
-    'blue',
-    'bold',
-    'both',
-    'bottom',
-    'brown',
-    'center',
-    'collapse',
-    'dashed',
-    'dotted',
-    'fuchsia',
-    'gray',
-    'green',
-    '!important',
-    'italic',
-    'left',
-    'lime',
-    'maroon',
-    'medium',
-    'none',
-    'navy',
-    'normal',
-    'nowrap',
-    'olive',
-    'pointer',
-    'purple',
-    'red',
-    'right',
-    'solid',
-    'silver',
-    'teal',
-    'top',
-    'transparent',
-    'underline',
-    'white',
-    'yellow',
-))
-
-allowed_svg_properties = frozenset((
-    'fill',
-    'fill-opacity',
-    'fill-rule',
-    'stroke',
-    'stroke-width',
-    'stroke-linecap',
-    'stroke-linejoin',
-    'stroke-opacity',
-))
-
-allowed_protocols = frozenset((
-    'ed2k',
-    'ftp',
-    'http',
-    'https',
-    'irc',
-    'mailto',
-    'news',
-    'gopher',
-    'nntp',
-    'telnet',
-    'webcal',
-    'xmpp',
-    'callto',
-    'feed',
-    'urn',
-    'aim',
-    'rsync',
-    'tag',
-    'ssh',
-    'sftp',
-    'rtsp',
-    'afs',
-    'data',
-))
-
-allowed_content_types = frozenset((
-    'image/png',
-    'image/jpeg',
-    'image/gif',
-    'image/webp',
-    'image/bmp',
-    'text/plain',
-))
-
-
-data_content_type = re.compile(r'''
-                                ^
-                                # Match a content type <application>/<type>
-                                (?P<content_type>[-a-zA-Z0-9.]+/[-a-zA-Z0-9.]+)
-                                # Match any character set and encoding
-                                (?:(?:;charset=(?:[-a-zA-Z0-9]+)(?:;(?:base64))?)
-                                  |(?:;(?:base64))?(?:;charset=(?:[-a-zA-Z0-9]+))?)
-                                # Assume the rest is data
-                                ,.*
-                                $
-                                ''',
-                               re.VERBOSE)
-
-
-class Filter(base.Filter):
-    """Sanitizes token stream of XHTML+MathML+SVG and of inline style attributes"""
-    def __init__(self,
-                 source,
-                 allowed_elements=allowed_elements,
-                 allowed_attributes=allowed_attributes,
-                 allowed_css_properties=allowed_css_properties,
-                 allowed_css_keywords=allowed_css_keywords,
-                 allowed_svg_properties=allowed_svg_properties,
-                 allowed_protocols=allowed_protocols,
-                 allowed_content_types=allowed_content_types,
-                 attr_val_is_uri=attr_val_is_uri,
-                 svg_attr_val_allows_ref=svg_attr_val_allows_ref,
-                 svg_allow_local_href=svg_allow_local_href):
-        """Creates a Filter
-
-        :arg allowed_elements: set of elements to allow--everything else will
-            be escaped
-
-        :arg allowed_attributes: set of attributes to allow in
-            elements--everything else will be stripped
-
-        :arg allowed_css_properties: set of CSS properties to allow--everything
-            else will be stripped
-
-        :arg allowed_css_keywords: set of CSS keywords to allow--everything
-            else will be stripped
-
-        :arg allowed_svg_properties: set of SVG properties to allow--everything
-            else will be removed
-
-        :arg allowed_protocols: set of allowed protocols for URIs
-
-        :arg allowed_content_types: set of allowed content types for ``data`` URIs.
-
-        :arg attr_val_is_uri: set of attributes that have URI values--values
-            that have a scheme not listed in ``allowed_protocols`` are removed
-
-        :arg svg_attr_val_allows_ref: set of SVG attributes that can have
-            references
-
-        :arg svg_allow_local_href: set of SVG elements that can have local
-            hrefs--these are removed
-
-        """
-        super(Filter, self).__init__(source)
-        self.allowed_elements = allowed_elements
-        self.allowed_attributes = allowed_attributes
-        self.allowed_css_properties = allowed_css_properties
-        self.allowed_css_keywords = allowed_css_keywords
-        self.allowed_svg_properties = allowed_svg_properties
-        self.allowed_protocols = allowed_protocols
-        self.allowed_content_types = allowed_content_types
-        self.attr_val_is_uri = attr_val_is_uri
-        self.svg_attr_val_allows_ref = svg_attr_val_allows_ref
-        self.svg_allow_local_href = svg_allow_local_href
-
-    def __iter__(self):
-        for token in base.Filter.__iter__(self):
-            token = self.sanitize_token(token)
-            if token:
-                yield token
-
-    # Sanitize the +html+, escaping all elements not in ALLOWED_ELEMENTS, and
-    # stripping out all attributes not in ALLOWED_ATTRIBUTES. Style attributes
-    # are parsed, and a restricted set, specified by ALLOWED_CSS_PROPERTIES and
-    # ALLOWED_CSS_KEYWORDS, are allowed through. attributes in ATTR_VAL_IS_URI
-    # are scanned, and only URI schemes specified in ALLOWED_PROTOCOLS are
-    # allowed.
-    #
-    #   sanitize_html('<script> do_nasty_stuff() </script>')
-    #    => &lt;script> do_nasty_stuff() &lt;/script>
-    #   sanitize_html('<a href="javascript: sucker();">Click here for $100</a>')
-    #    => <a>Click here for $100</a>
-    def sanitize_token(self, token):
-
-        # accommodate filters which use token_type differently
-        token_type = token["type"]
-        if token_type in ("StartTag", "EndTag", "EmptyTag"):
-            name = token["name"]
-            namespace = token["namespace"]
-            if ((namespace, name) in self.allowed_elements or
-                (namespace is None and
-                 (namespaces["html"], name) in self.allowed_elements)):
-                return self.allowed_token(token)
-            else:
-                return self.disallowed_token(token)
-        elif token_type == "Comment":
-            pass
-        else:
-            return token
-
-    def allowed_token(self, token):
-        if "data" in token:
-            attrs = token["data"]
-            attr_names = set(attrs.keys())
-
-            # Remove forbidden attributes
-            for to_remove in (attr_names - self.allowed_attributes):
-                del token["data"][to_remove]
-                attr_names.remove(to_remove)
-
-            # Remove attributes with disallowed URL values
-            for attr in (attr_names & self.attr_val_is_uri):
-                assert attr in attrs
-                # I don't have a clue where this regexp comes from or why it matches those
-                # characters, nor why we call unescape. I just know it's always been here.
-                # Should you be worried by this comment in a sanitizer? Yes. On the other hand, all
-                # this will do is remove *more* than it otherwise would.
-                val_unescaped = re.sub("[`\x00-\x20\x7f-\xa0\\s]+", '',
-                                       unescape(attrs[attr])).lower()
-                # remove replacement characters from unescaped characters
-                val_unescaped = val_unescaped.replace("\ufffd", "")
-                try:
-                    uri = urlparse.urlparse(val_unescaped)
-                except ValueError:
-                    uri = None
-                    del attrs[attr]
-                if uri and uri.scheme:
-                    if uri.scheme not in self.allowed_protocols:
-                        del attrs[attr]
-                    if uri.scheme == 'data':
-                        m = data_content_type.match(uri.path)
-                        if not m:
-                            del attrs[attr]
-                        elif m.group('content_type') not in self.allowed_content_types:
-                            del attrs[attr]
-
-            for attr in self.svg_attr_val_allows_ref:
-                if attr in attrs:
-                    attrs[attr] = re.sub(r'url\s*\(\s*[^#\s][^)]+?\)',
-                                         ' ',
-                                         unescape(attrs[attr]))
-            if (token["name"] in self.svg_allow_local_href and
-                (namespaces['xlink'], 'href') in attrs and re.search(r'^\s*[^#\s].*',
-                                                                     attrs[(namespaces['xlink'], 'href')])):
-                del attrs[(namespaces['xlink'], 'href')]
-            if (None, 'style') in attrs:
-                attrs[(None, 'style')] = self.sanitize_css(attrs[(None, 'style')])
-            token["data"] = attrs
-        return token
-
-    def disallowed_token(self, token):
-        token_type = token["type"]
-        if token_type == "EndTag":
-            token["data"] = "</%s>" % token["name"]
-        elif token["data"]:
-            assert token_type in ("StartTag", "EmptyTag")
-            attrs = []
-            for (ns, name), v in token["data"].items():
-                attrs.append(' %s="%s"' % (name if ns is None else "%s:%s" % (prefixes[ns], name), escape(v)))
-            token["data"] = "<%s%s>" % (token["name"], ''.join(attrs))
-        else:
-            token["data"] = "<%s>" % token["name"]
-        if token.get("selfClosing"):
-            token["data"] = token["data"][:-1] + "/>"
-
-        token["type"] = "Characters"
-
-        del token["name"]
-        return token
-
-    def sanitize_css(self, style):
-        # disallow urls
-        style = re.compile(r'url\s*\(\s*[^\s)]+?\s*\)\s*').sub(' ', style)
-
-        # gauntlet
-        if not re.match(r"""^([:,;#%.\sa-zA-Z0-9!]|\w-\w|'[\s\w]+'|"[\s\w]+"|\([\d,\s]+\))*$""", style):
-            return ''
-        if not re.match(r"^\s*([-\w]+\s*:[^:;]*(;\s*|$))*$", style):
-            return ''
-
-        clean = []
-        for prop, value in re.findall(r"([-\w]+)\s*:\s*([^:;]*)", style):
-            if not value:
-                continue
-            if prop.lower() in self.allowed_css_properties:
-                clean.append(prop + ': ' + value + ';')
-            elif prop.split('-')[0].lower() in ['background', 'border', 'margin',
-                                                'padding']:
-                for keyword in value.split():
-                    if keyword not in self.allowed_css_keywords and \
-                            not re.match(r"^(#[0-9a-fA-F]+|rgb\(\d+%?,\d*%?,?\d*%?\)?|\d{0,2}\.?\d{0,2}(cm|em|ex|in|mm|pc|pt|px|%|,|\))?)$", keyword):  # noqa
-                        break
-                else:
-                    clean.append(prop + ': ' + value + ';')
-            elif prop.lower() in self.allowed_svg_properties:
-                clean.append(prop + ': ' + value + ';')
-
-        return ' '.join(clean)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/whitespace.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/whitespace.py
deleted file mode 100644
index 0d12584..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/filters/whitespace.py
+++ /dev/null
@@ -1,38 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-import re
-
-from . import base
-from ..constants import rcdataElements, spaceCharacters
-spaceCharacters = "".join(spaceCharacters)
-
-SPACES_REGEX = re.compile("[%s]+" % spaceCharacters)
-
-
-class Filter(base.Filter):
-    """Collapses whitespace except in pre, textarea, and script elements"""
-    spacePreserveElements = frozenset(["pre", "textarea"] + list(rcdataElements))
-
-    def __iter__(self):
-        preserve = 0
-        for token in base.Filter.__iter__(self):
-            type = token["type"]
-            if type == "StartTag" \
-                    and (preserve or token["name"] in self.spacePreserveElements):
-                preserve += 1
-
-            elif type == "EndTag" and preserve:
-                preserve -= 1
-
-            elif not preserve and type == "SpaceCharacters" and token["data"]:
-                # Test on token["data"] above to not introduce spaces where there were not
-                token["data"] = " "
-
-            elif not preserve and type == "Characters":
-                token["data"] = collapse_spaces(token["data"])
-
-            yield token
-
-
-def collapse_spaces(text):
-    return SPACES_REGEX.sub(' ', text)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/html5parser.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/html5parser.py
deleted file mode 100644
index ae41a13..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/html5parser.py
+++ /dev/null
@@ -1,2791 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-from pip._vendor.six import with_metaclass, viewkeys
-
-import types
-from collections import OrderedDict
-
-from . import _inputstream
-from . import _tokenizer
-
-from . import treebuilders
-from .treebuilders.base import Marker
-
-from . import _utils
-from .constants import (
-    spaceCharacters, asciiUpper2Lower,
-    specialElements, headingElements, cdataElements, rcdataElements,
-    tokenTypes, tagTokenTypes,
-    namespaces,
-    htmlIntegrationPointElements, mathmlTextIntegrationPointElements,
-    adjustForeignAttributes as adjustForeignAttributesMap,
-    adjustMathMLAttributes, adjustSVGAttributes,
-    E,
-    _ReparseException
-)
-
-
-def parse(doc, treebuilder="etree", namespaceHTMLElements=True, **kwargs):
-    """Parse an HTML document as a string or file-like object into a tree
-
-    :arg doc: the document to parse as a string or file-like object
-
-    :arg treebuilder: the treebuilder to use when parsing
-
-    :arg namespaceHTMLElements: whether or not to namespace HTML elements
-
-    :returns: parsed tree
-
-    Example:
-
-    >>> from html5lib.html5parser import parse
-    >>> parse('<html><body><p>This is a doc</p></body></html>')
-    <Element u'{http://www.w3.org/1999/xhtml}html' at 0x7feac4909db0>
-
-    """
-    tb = treebuilders.getTreeBuilder(treebuilder)
-    p = HTMLParser(tb, namespaceHTMLElements=namespaceHTMLElements)
-    return p.parse(doc, **kwargs)
-
-
-def parseFragment(doc, container="div", treebuilder="etree", namespaceHTMLElements=True, **kwargs):
-    """Parse an HTML fragment as a string or file-like object into a tree
-
-    :arg doc: the fragment to parse as a string or file-like object
-
-    :arg container: the container context to parse the fragment in
-
-    :arg treebuilder: the treebuilder to use when parsing
-
-    :arg namespaceHTMLElements: whether or not to namespace HTML elements
-
-    :returns: parsed tree
-
-    Example:
-
-    >>> from html5lib.html5libparser import parseFragment
-    >>> parseFragment('<b>this is a fragment</b>')
-    <Element u'DOCUMENT_FRAGMENT' at 0x7feac484b090>
-
-    """
-    tb = treebuilders.getTreeBuilder(treebuilder)
-    p = HTMLParser(tb, namespaceHTMLElements=namespaceHTMLElements)
-    return p.parseFragment(doc, container=container, **kwargs)
-
-
-def method_decorator_metaclass(function):
-    class Decorated(type):
-        def __new__(meta, classname, bases, classDict):
-            for attributeName, attribute in classDict.items():
-                if isinstance(attribute, types.FunctionType):
-                    attribute = function(attribute)
-
-                classDict[attributeName] = attribute
-            return type.__new__(meta, classname, bases, classDict)
-    return Decorated
-
-
-class HTMLParser(object):
-    """HTML parser
-
-    Generates a tree structure from a stream of (possibly malformed) HTML.
-
-    """
-
-    def __init__(self, tree=None, strict=False, namespaceHTMLElements=True, debug=False):
-        """
-        :arg tree: a treebuilder class controlling the type of tree that will be
-            returned. Built in treebuilders can be accessed through
-            html5lib.treebuilders.getTreeBuilder(treeType)
-
-        :arg strict: raise an exception when a parse error is encountered
-
-        :arg namespaceHTMLElements: whether or not to namespace HTML elements
-
-        :arg debug: whether or not to enable debug mode which logs things
-
-        Example:
-
-        >>> from html5lib.html5parser import HTMLParser
-        >>> parser = HTMLParser()                     # generates parser with etree builder
-        >>> parser = HTMLParser('lxml', strict=True)  # generates parser with lxml builder which is strict
-
-        """
-
-        # Raise an exception on the first error encountered
-        self.strict = strict
-
-        if tree is None:
-            tree = treebuilders.getTreeBuilder("etree")
-        self.tree = tree(namespaceHTMLElements)
-        self.errors = []
-
-        self.phases = dict([(name, cls(self, self.tree)) for name, cls in
-                            getPhases(debug).items()])
-
-    def _parse(self, stream, innerHTML=False, container="div", scripting=False, **kwargs):
-
-        self.innerHTMLMode = innerHTML
-        self.container = container
-        self.scripting = scripting
-        self.tokenizer = _tokenizer.HTMLTokenizer(stream, parser=self, **kwargs)
-        self.reset()
-
-        try:
-            self.mainLoop()
-        except _ReparseException:
-            self.reset()
-            self.mainLoop()
-
-    def reset(self):
-        self.tree.reset()
-        self.firstStartTag = False
-        self.errors = []
-        self.log = []  # only used with debug mode
-        # "quirks" / "limited quirks" / "no quirks"
-        self.compatMode = "no quirks"
-
-        if self.innerHTMLMode:
-            self.innerHTML = self.container.lower()
-
-            if self.innerHTML in cdataElements:
-                self.tokenizer.state = self.tokenizer.rcdataState
-            elif self.innerHTML in rcdataElements:
-                self.tokenizer.state = self.tokenizer.rawtextState
-            elif self.innerHTML == 'plaintext':
-                self.tokenizer.state = self.tokenizer.plaintextState
-            else:
-                # state already is data state
-                # self.tokenizer.state = self.tokenizer.dataState
-                pass
-            self.phase = self.phases["beforeHtml"]
-            self.phase.insertHtmlElement()
-            self.resetInsertionMode()
-        else:
-            self.innerHTML = False  # pylint:disable=redefined-variable-type
-            self.phase = self.phases["initial"]
-
-        self.lastPhase = None
-
-        self.beforeRCDataPhase = None
-
-        self.framesetOK = True
-
-    @property
-    def documentEncoding(self):
-        """Name of the character encoding that was used to decode the input stream, or
-        :obj:`None` if that is not determined yet
-
-        """
-        if not hasattr(self, 'tokenizer'):
-            return None
-        return self.tokenizer.stream.charEncoding[0].name
-
-    def isHTMLIntegrationPoint(self, element):
-        if (element.name == "annotation-xml" and
-                element.namespace == namespaces["mathml"]):
-            return ("encoding" in element.attributes and
-                    element.attributes["encoding"].translate(
-                        asciiUpper2Lower) in
-                    ("text/html", "application/xhtml+xml"))
-        else:
-            return (element.namespace, element.name) in htmlIntegrationPointElements
-
-    def isMathMLTextIntegrationPoint(self, element):
-        return (element.namespace, element.name) in mathmlTextIntegrationPointElements
-
-    def mainLoop(self):
-        CharactersToken = tokenTypes["Characters"]
-        SpaceCharactersToken = tokenTypes["SpaceCharacters"]
-        StartTagToken = tokenTypes["StartTag"]
-        EndTagToken = tokenTypes["EndTag"]
-        CommentToken = tokenTypes["Comment"]
-        DoctypeToken = tokenTypes["Doctype"]
-        ParseErrorToken = tokenTypes["ParseError"]
-
-        for token in self.normalizedTokens():
-            prev_token = None
-            new_token = token
-            while new_token is not None:
-                prev_token = new_token
-                currentNode = self.tree.openElements[-1] if self.tree.openElements else None
-                currentNodeNamespace = currentNode.namespace if currentNode else None
-                currentNodeName = currentNode.name if currentNode else None
-
-                type = new_token["type"]
-
-                if type == ParseErrorToken:
-                    self.parseError(new_token["data"], new_token.get("datavars", {}))
-                    new_token = None
-                else:
-                    if (len(self.tree.openElements) == 0 or
-                        currentNodeNamespace == self.tree.defaultNamespace or
-                        (self.isMathMLTextIntegrationPoint(currentNode) and
-                         ((type == StartTagToken and
-                           token["name"] not in frozenset(["mglyph", "malignmark"])) or
-                          type in (CharactersToken, SpaceCharactersToken))) or
-                        (currentNodeNamespace == namespaces["mathml"] and
-                         currentNodeName == "annotation-xml" and
-                         type == StartTagToken and
-                         token["name"] == "svg") or
-                        (self.isHTMLIntegrationPoint(currentNode) and
-                         type in (StartTagToken, CharactersToken, SpaceCharactersToken))):
-                        phase = self.phase
-                    else:
-                        phase = self.phases["inForeignContent"]
-
-                    if type == CharactersToken:
-                        new_token = phase.processCharacters(new_token)
-                    elif type == SpaceCharactersToken:
-                        new_token = phase.processSpaceCharacters(new_token)
-                    elif type == StartTagToken:
-                        new_token = phase.processStartTag(new_token)
-                    elif type == EndTagToken:
-                        new_token = phase.processEndTag(new_token)
-                    elif type == CommentToken:
-                        new_token = phase.processComment(new_token)
-                    elif type == DoctypeToken:
-                        new_token = phase.processDoctype(new_token)
-
-            if (type == StartTagToken and prev_token["selfClosing"] and
-                    not prev_token["selfClosingAcknowledged"]):
-                self.parseError("non-void-element-with-trailing-solidus",
-                                {"name": prev_token["name"]})
-
-        # When the loop finishes it's EOF
-        reprocess = True
-        phases = []
-        while reprocess:
-            phases.append(self.phase)
-            reprocess = self.phase.processEOF()
-            if reprocess:
-                assert self.phase not in phases
-
-    def normalizedTokens(self):
-        for token in self.tokenizer:
-            yield self.normalizeToken(token)
-
-    def parse(self, stream, *args, **kwargs):
-        """Parse a HTML document into a well-formed tree
-
-        :arg stream: a file-like object or string containing the HTML to be parsed
-
-            The optional encoding parameter must be a string that indicates
-            the encoding.  If specified, that encoding will be used,
-            regardless of any BOM or later declaration (such as in a meta
-            element).
-
-        :arg scripting: treat noscript elements as if JavaScript was turned on
-
-        :returns: parsed tree
-
-        Example:
-
-        >>> from html5lib.html5parser import HTMLParser
-        >>> parser = HTMLParser()
-        >>> parser.parse('<html><body><p>This is a doc</p></body></html>')
-        <Element u'{http://www.w3.org/1999/xhtml}html' at 0x7feac4909db0>
-
-        """
-        self._parse(stream, False, None, *args, **kwargs)
-        return self.tree.getDocument()
-
-    def parseFragment(self, stream, *args, **kwargs):
-        """Parse a HTML fragment into a well-formed tree fragment
-
-        :arg container: name of the element we're setting the innerHTML
-            property if set to None, default to 'div'
-
-        :arg stream: a file-like object or string containing the HTML to be parsed
-
-            The optional encoding parameter must be a string that indicates
-            the encoding.  If specified, that encoding will be used,
-            regardless of any BOM or later declaration (such as in a meta
-            element)
-
-        :arg scripting: treat noscript elements as if JavaScript was turned on
-
-        :returns: parsed tree
-
-        Example:
-
-        >>> from html5lib.html5libparser import HTMLParser
-        >>> parser = HTMLParser()
-        >>> parser.parseFragment('<b>this is a fragment</b>')
-        <Element u'DOCUMENT_FRAGMENT' at 0x7feac484b090>
-
-        """
-        self._parse(stream, True, *args, **kwargs)
-        return self.tree.getFragment()
-
-    def parseError(self, errorcode="XXX-undefined-error", datavars=None):
-        # XXX The idea is to make errorcode mandatory.
-        if datavars is None:
-            datavars = {}
-        self.errors.append((self.tokenizer.stream.position(), errorcode, datavars))
-        if self.strict:
-            raise ParseError(E[errorcode] % datavars)
-
-    def normalizeToken(self, token):
-        # HTML5 specific normalizations to the token stream
-        if token["type"] == tokenTypes["StartTag"]:
-            raw = token["data"]
-            token["data"] = OrderedDict(raw)
-            if len(raw) > len(token["data"]):
-                # we had some duplicated attribute, fix so first wins
-                token["data"].update(raw[::-1])
-
-        return token
-
-    def adjustMathMLAttributes(self, token):
-        adjust_attributes(token, adjustMathMLAttributes)
-
-    def adjustSVGAttributes(self, token):
-        adjust_attributes(token, adjustSVGAttributes)
-
-    def adjustForeignAttributes(self, token):
-        adjust_attributes(token, adjustForeignAttributesMap)
-
-    def reparseTokenNormal(self, token):
-        # pylint:disable=unused-argument
-        self.parser.phase()
-
-    def resetInsertionMode(self):
-        # The name of this method is mostly historical. (It's also used in the
-        # specification.)
-        last = False
-        newModes = {
-            "select": "inSelect",
-            "td": "inCell",
-            "th": "inCell",
-            "tr": "inRow",
-            "tbody": "inTableBody",
-            "thead": "inTableBody",
-            "tfoot": "inTableBody",
-            "caption": "inCaption",
-            "colgroup": "inColumnGroup",
-            "table": "inTable",
-            "head": "inBody",
-            "body": "inBody",
-            "frameset": "inFrameset",
-            "html": "beforeHead"
-        }
-        for node in self.tree.openElements[::-1]:
-            nodeName = node.name
-            new_phase = None
-            if node == self.tree.openElements[0]:
-                assert self.innerHTML
-                last = True
-                nodeName = self.innerHTML
-            # Check for conditions that should only happen in the innerHTML
-            # case
-            if nodeName in ("select", "colgroup", "head", "html"):
-                assert self.innerHTML
-
-            if not last and node.namespace != self.tree.defaultNamespace:
-                continue
-
-            if nodeName in newModes:
-                new_phase = self.phases[newModes[nodeName]]
-                break
-            elif last:
-                new_phase = self.phases["inBody"]
-                break
-
-        self.phase = new_phase
-
-    def parseRCDataRawtext(self, token, contentType):
-        # Generic RCDATA/RAWTEXT Parsing algorithm
-        assert contentType in ("RAWTEXT", "RCDATA")
-
-        self.tree.insertElement(token)
-
-        if contentType == "RAWTEXT":
-            self.tokenizer.state = self.tokenizer.rawtextState
-        else:
-            self.tokenizer.state = self.tokenizer.rcdataState
-
-        self.originalPhase = self.phase
-
-        self.phase = self.phases["text"]
-
-
-@_utils.memoize
-def getPhases(debug):
-    def log(function):
-        """Logger that records which phase processes each token"""
-        type_names = dict((value, key) for key, value in
-                          tokenTypes.items())
-
-        def wrapped(self, *args, **kwargs):
-            if function.__name__.startswith("process") and len(args) > 0:
-                token = args[0]
-                try:
-                    info = {"type": type_names[token['type']]}
-                except:
-                    raise
-                if token['type'] in tagTokenTypes:
-                    info["name"] = token['name']
-
-                self.parser.log.append((self.parser.tokenizer.state.__name__,
-                                        self.parser.phase.__class__.__name__,
-                                        self.__class__.__name__,
-                                        function.__name__,
-                                        info))
-                return function(self, *args, **kwargs)
-            else:
-                return function(self, *args, **kwargs)
-        return wrapped
-
-    def getMetaclass(use_metaclass, metaclass_func):
-        if use_metaclass:
-            return method_decorator_metaclass(metaclass_func)
-        else:
-            return type
-
-    # pylint:disable=unused-argument
-    class Phase(with_metaclass(getMetaclass(debug, log))):
-        """Base class for helper object that implements each phase of processing
-        """
-
-        def __init__(self, parser, tree):
-            self.parser = parser
-            self.tree = tree
-
-        def processEOF(self):
-            raise NotImplementedError
-
-        def processComment(self, token):
-            # For most phases the following is correct. Where it's not it will be
-            # overridden.
-            self.tree.insertComment(token, self.tree.openElements[-1])
-
-        def processDoctype(self, token):
-            self.parser.parseError("unexpected-doctype")
-
-        def processCharacters(self, token):
-            self.tree.insertText(token["data"])
-
-        def processSpaceCharacters(self, token):
-            self.tree.insertText(token["data"])
-
-        def processStartTag(self, token):
-            return self.startTagHandler[token["name"]](token)
-
-        def startTagHtml(self, token):
-            if not self.parser.firstStartTag and token["name"] == "html":
-                self.parser.parseError("non-html-root")
-            # XXX Need a check here to see if the first start tag token emitted is
-            # this token... If it's not, invoke self.parser.parseError().
-            for attr, value in token["data"].items():
-                if attr not in self.tree.openElements[0].attributes:
-                    self.tree.openElements[0].attributes[attr] = value
-            self.parser.firstStartTag = False
-
-        def processEndTag(self, token):
-            return self.endTagHandler[token["name"]](token)
-
-    class InitialPhase(Phase):
-        def processSpaceCharacters(self, token):
-            pass
-
-        def processComment(self, token):
-            self.tree.insertComment(token, self.tree.document)
-
-        def processDoctype(self, token):
-            name = token["name"]
-            publicId = token["publicId"]
-            systemId = token["systemId"]
-            correct = token["correct"]
-
-            if (name != "html" or publicId is not None or
-                    systemId is not None and systemId != "about:legacy-compat"):
-                self.parser.parseError("unknown-doctype")
-
-            if publicId is None:
-                publicId = ""
-
-            self.tree.insertDoctype(token)
-
-            if publicId != "":
-                publicId = publicId.translate(asciiUpper2Lower)
-
-            if (not correct or token["name"] != "html" or
-                    publicId.startswith(
-                        ("+//silmaril//dtd html pro v0r11 19970101//",
-                         "-//advasoft ltd//dtd html 3.0 aswedit + extensions//",
-                         "-//as//dtd html 3.0 aswedit + extensions//",
-                         "-//ietf//dtd html 2.0 level 1//",
-                         "-//ietf//dtd html 2.0 level 2//",
-                         "-//ietf//dtd html 2.0 strict level 1//",
-                         "-//ietf//dtd html 2.0 strict level 2//",
-                         "-//ietf//dtd html 2.0 strict//",
-                         "-//ietf//dtd html 2.0//",
-                         "-//ietf//dtd html 2.1e//",
-                         "-//ietf//dtd html 3.0//",
-                         "-//ietf//dtd html 3.2 final//",
-                         "-//ietf//dtd html 3.2//",
-                         "-//ietf//dtd html 3//",
-                         "-//ietf//dtd html level 0//",
-                         "-//ietf//dtd html level 1//",
-                         "-//ietf//dtd html level 2//",
-                         "-//ietf//dtd html level 3//",
-                         "-//ietf//dtd html strict level 0//",
-                         "-//ietf//dtd html strict level 1//",
-                         "-//ietf//dtd html strict level 2//",
-                         "-//ietf//dtd html strict level 3//",
-                         "-//ietf//dtd html strict//",
-                         "-//ietf//dtd html//",
-                         "-//metrius//dtd metrius presentational//",
-                         "-//microsoft//dtd internet explorer 2.0 html strict//",
-                         "-//microsoft//dtd internet explorer 2.0 html//",
-                         "-//microsoft//dtd internet explorer 2.0 tables//",
-                         "-//microsoft//dtd internet explorer 3.0 html strict//",
-                         "-//microsoft//dtd internet explorer 3.0 html//",
-                         "-//microsoft//dtd internet explorer 3.0 tables//",
-                         "-//netscape comm. corp.//dtd html//",
-                         "-//netscape comm. corp.//dtd strict html//",
-                         "-//o'reilly and associates//dtd html 2.0//",
-                         "-//o'reilly and associates//dtd html extended 1.0//",
-                         "-//o'reilly and associates//dtd html extended relaxed 1.0//",
-                         "-//softquad software//dtd hotmetal pro 6.0::19990601::extensions to html 4.0//",
-                         "-//softquad//dtd hotmetal pro 4.0::19971010::extensions to html 4.0//",
-                         "-//spyglass//dtd html 2.0 extended//",
-                         "-//sq//dtd html 2.0 hotmetal + extensions//",
-                         "-//sun microsystems corp.//dtd hotjava html//",
-                         "-//sun microsystems corp.//dtd hotjava strict html//",
-                         "-//w3c//dtd html 3 1995-03-24//",
-                         "-//w3c//dtd html 3.2 draft//",
-                         "-//w3c//dtd html 3.2 final//",
-                         "-//w3c//dtd html 3.2//",
-                         "-//w3c//dtd html 3.2s draft//",
-                         "-//w3c//dtd html 4.0 frameset//",
-                         "-//w3c//dtd html 4.0 transitional//",
-                         "-//w3c//dtd html experimental 19960712//",
-                         "-//w3c//dtd html experimental 970421//",
-                         "-//w3c//dtd w3 html//",
-                         "-//w3o//dtd w3 html 3.0//",
-                         "-//webtechs//dtd mozilla html 2.0//",
-                         "-//webtechs//dtd mozilla html//")) or
-                    publicId in ("-//w3o//dtd w3 html strict 3.0//en//",
-                                 "-/w3c/dtd html 4.0 transitional/en",
-                                 "html") or
-                    publicId.startswith(
-                        ("-//w3c//dtd html 4.01 frameset//",
-                         "-//w3c//dtd html 4.01 transitional//")) and
-                    systemId is None or
-                    systemId and systemId.lower() == "http://www.ibm.com/data/dtd/v11/ibmxhtml1-transitional.dtd"):
-                self.parser.compatMode = "quirks"
-            elif (publicId.startswith(
-                    ("-//w3c//dtd xhtml 1.0 frameset//",
-                     "-//w3c//dtd xhtml 1.0 transitional//")) or
-                  publicId.startswith(
-                      ("-//w3c//dtd html 4.01 frameset//",
-                       "-//w3c//dtd html 4.01 transitional//")) and
-                  systemId is not None):
-                self.parser.compatMode = "limited quirks"
-
-            self.parser.phase = self.parser.phases["beforeHtml"]
-
-        def anythingElse(self):
-            self.parser.compatMode = "quirks"
-            self.parser.phase = self.parser.phases["beforeHtml"]
-
-        def processCharacters(self, token):
-            self.parser.parseError("expected-doctype-but-got-chars")
-            self.anythingElse()
-            return token
-
-        def processStartTag(self, token):
-            self.parser.parseError("expected-doctype-but-got-start-tag",
-                                   {"name": token["name"]})
-            self.anythingElse()
-            return token
-
-        def processEndTag(self, token):
-            self.parser.parseError("expected-doctype-but-got-end-tag",
-                                   {"name": token["name"]})
-            self.anythingElse()
-            return token
-
-        def processEOF(self):
-            self.parser.parseError("expected-doctype-but-got-eof")
-            self.anythingElse()
-            return True
-
-    class BeforeHtmlPhase(Phase):
-        # helper methods
-        def insertHtmlElement(self):
-            self.tree.insertRoot(impliedTagToken("html", "StartTag"))
-            self.parser.phase = self.parser.phases["beforeHead"]
-
-        # other
-        def processEOF(self):
-            self.insertHtmlElement()
-            return True
-
-        def processComment(self, token):
-            self.tree.insertComment(token, self.tree.document)
-
-        def processSpaceCharacters(self, token):
-            pass
-
-        def processCharacters(self, token):
-            self.insertHtmlElement()
-            return token
-
-        def processStartTag(self, token):
-            if token["name"] == "html":
-                self.parser.firstStartTag = True
-            self.insertHtmlElement()
-            return token
-
-        def processEndTag(self, token):
-            if token["name"] not in ("head", "body", "html", "br"):
-                self.parser.parseError("unexpected-end-tag-before-html",
-                                       {"name": token["name"]})
-            else:
-                self.insertHtmlElement()
-                return token
-
-    class BeforeHeadPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("head", self.startTagHead)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                (("head", "body", "html", "br"), self.endTagImplyHead)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def processEOF(self):
-            self.startTagHead(impliedTagToken("head", "StartTag"))
-            return True
-
-        def processSpaceCharacters(self, token):
-            pass
-
-        def processCharacters(self, token):
-            self.startTagHead(impliedTagToken("head", "StartTag"))
-            return token
-
-        def startTagHtml(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagHead(self, token):
-            self.tree.insertElement(token)
-            self.tree.headPointer = self.tree.openElements[-1]
-            self.parser.phase = self.parser.phases["inHead"]
-
-        def startTagOther(self, token):
-            self.startTagHead(impliedTagToken("head", "StartTag"))
-            return token
-
-        def endTagImplyHead(self, token):
-            self.startTagHead(impliedTagToken("head", "StartTag"))
-            return token
-
-        def endTagOther(self, token):
-            self.parser.parseError("end-tag-after-implied-root",
-                                   {"name": token["name"]})
-
-    class InHeadPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("title", self.startTagTitle),
-                (("noframes", "style"), self.startTagNoFramesStyle),
-                ("noscript", self.startTagNoscript),
-                ("script", self.startTagScript),
-                (("base", "basefont", "bgsound", "command", "link"),
-                 self.startTagBaseLinkCommand),
-                ("meta", self.startTagMeta),
-                ("head", self.startTagHead)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("head", self.endTagHead),
-                (("br", "html", "body"), self.endTagHtmlBodyBr)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        # the real thing
-        def processEOF(self):
-            self.anythingElse()
-            return True
-
-        def processCharacters(self, token):
-            self.anythingElse()
-            return token
-
-        def startTagHtml(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagHead(self, token):
-            self.parser.parseError("two-heads-are-not-better-than-one")
-
-        def startTagBaseLinkCommand(self, token):
-            self.tree.insertElement(token)
-            self.tree.openElements.pop()
-            token["selfClosingAcknowledged"] = True
-
-        def startTagMeta(self, token):
-            self.tree.insertElement(token)
-            self.tree.openElements.pop()
-            token["selfClosingAcknowledged"] = True
-
-            attributes = token["data"]
-            if self.parser.tokenizer.stream.charEncoding[1] == "tentative":
-                if "charset" in attributes:
-                    self.parser.tokenizer.stream.changeEncoding(attributes["charset"])
-                elif ("content" in attributes and
-                      "http-equiv" in attributes and
-                      attributes["http-equiv"].lower() == "content-type"):
-                    # Encoding it as UTF-8 here is a hack, as really we should pass
-                    # the abstract Unicode string, and just use the
-                    # ContentAttrParser on that, but using UTF-8 allows all chars
-                    # to be encoded and as a ASCII-superset works.
-                    data = _inputstream.EncodingBytes(attributes["content"].encode("utf-8"))
-                    parser = _inputstream.ContentAttrParser(data)
-                    codec = parser.parse()
-                    self.parser.tokenizer.stream.changeEncoding(codec)
-
-        def startTagTitle(self, token):
-            self.parser.parseRCDataRawtext(token, "RCDATA")
-
-        def startTagNoFramesStyle(self, token):
-            # Need to decide whether to implement the scripting-disabled case
-            self.parser.parseRCDataRawtext(token, "RAWTEXT")
-
-        def startTagNoscript(self, token):
-            if self.parser.scripting:
-                self.parser.parseRCDataRawtext(token, "RAWTEXT")
-            else:
-                self.tree.insertElement(token)
-                self.parser.phase = self.parser.phases["inHeadNoscript"]
-
-        def startTagScript(self, token):
-            self.tree.insertElement(token)
-            self.parser.tokenizer.state = self.parser.tokenizer.scriptDataState
-            self.parser.originalPhase = self.parser.phase
-            self.parser.phase = self.parser.phases["text"]
-
-        def startTagOther(self, token):
-            self.anythingElse()
-            return token
-
-        def endTagHead(self, token):
-            node = self.parser.tree.openElements.pop()
-            assert node.name == "head", "Expected head got %s" % node.name
-            self.parser.phase = self.parser.phases["afterHead"]
-
-        def endTagHtmlBodyBr(self, token):
-            self.anythingElse()
-            return token
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-        def anythingElse(self):
-            self.endTagHead(impliedTagToken("head"))
-
-    class InHeadNoscriptPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                (("basefont", "bgsound", "link", "meta", "noframes", "style"), self.startTagBaseLinkCommand),
-                (("head", "noscript"), self.startTagHeadNoscript),
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("noscript", self.endTagNoscript),
-                ("br", self.endTagBr),
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def processEOF(self):
-            self.parser.parseError("eof-in-head-noscript")
-            self.anythingElse()
-            return True
-
-        def processComment(self, token):
-            return self.parser.phases["inHead"].processComment(token)
-
-        def processCharacters(self, token):
-            self.parser.parseError("char-in-head-noscript")
-            self.anythingElse()
-            return token
-
-        def processSpaceCharacters(self, token):
-            return self.parser.phases["inHead"].processSpaceCharacters(token)
-
-        def startTagHtml(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagBaseLinkCommand(self, token):
-            return self.parser.phases["inHead"].processStartTag(token)
-
-        def startTagHeadNoscript(self, token):
-            self.parser.parseError("unexpected-start-tag", {"name": token["name"]})
-
-        def startTagOther(self, token):
-            self.parser.parseError("unexpected-inhead-noscript-tag", {"name": token["name"]})
-            self.anythingElse()
-            return token
-
-        def endTagNoscript(self, token):
-            node = self.parser.tree.openElements.pop()
-            assert node.name == "noscript", "Expected noscript got %s" % node.name
-            self.parser.phase = self.parser.phases["inHead"]
-
-        def endTagBr(self, token):
-            self.parser.parseError("unexpected-inhead-noscript-tag", {"name": token["name"]})
-            self.anythingElse()
-            return token
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-        def anythingElse(self):
-            # Caller must raise parse error first!
-            self.endTagNoscript(impliedTagToken("noscript"))
-
-    class AfterHeadPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("body", self.startTagBody),
-                ("frameset", self.startTagFrameset),
-                (("base", "basefont", "bgsound", "link", "meta", "noframes", "script",
-                  "style", "title"),
-                 self.startTagFromHead),
-                ("head", self.startTagHead)
-            ])
-            self.startTagHandler.default = self.startTagOther
-            self.endTagHandler = _utils.MethodDispatcher([(("body", "html", "br"),
-                                                           self.endTagHtmlBodyBr)])
-            self.endTagHandler.default = self.endTagOther
-
-        def processEOF(self):
-            self.anythingElse()
-            return True
-
-        def processCharacters(self, token):
-            self.anythingElse()
-            return token
-
-        def startTagHtml(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagBody(self, token):
-            self.parser.framesetOK = False
-            self.tree.insertElement(token)
-            self.parser.phase = self.parser.phases["inBody"]
-
-        def startTagFrameset(self, token):
-            self.tree.insertElement(token)
-            self.parser.phase = self.parser.phases["inFrameset"]
-
-        def startTagFromHead(self, token):
-            self.parser.parseError("unexpected-start-tag-out-of-my-head",
-                                   {"name": token["name"]})
-            self.tree.openElements.append(self.tree.headPointer)
-            self.parser.phases["inHead"].processStartTag(token)
-            for node in self.tree.openElements[::-1]:
-                if node.name == "head":
-                    self.tree.openElements.remove(node)
-                    break
-
-        def startTagHead(self, token):
-            self.parser.parseError("unexpected-start-tag", {"name": token["name"]})
-
-        def startTagOther(self, token):
-            self.anythingElse()
-            return token
-
-        def endTagHtmlBodyBr(self, token):
-            self.anythingElse()
-            return token
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-        def anythingElse(self):
-            self.tree.insertElement(impliedTagToken("body", "StartTag"))
-            self.parser.phase = self.parser.phases["inBody"]
-            self.parser.framesetOK = True
-
-    class InBodyPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#parsing-main-inbody
-        # the really-really-really-very crazy mode
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            # Set this to the default handler
-            self.processSpaceCharacters = self.processSpaceCharactersNonPre
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                (("base", "basefont", "bgsound", "command", "link", "meta",
-                  "script", "style", "title"),
-                 self.startTagProcessInHead),
-                ("body", self.startTagBody),
-                ("frameset", self.startTagFrameset),
-                (("address", "article", "aside", "blockquote", "center", "details",
-                  "dir", "div", "dl", "fieldset", "figcaption", "figure",
-                  "footer", "header", "hgroup", "main", "menu", "nav", "ol", "p",
-                  "section", "summary", "ul"),
-                 self.startTagCloseP),
-                (headingElements, self.startTagHeading),
-                (("pre", "listing"), self.startTagPreListing),
-                ("form", self.startTagForm),
-                (("li", "dd", "dt"), self.startTagListItem),
-                ("plaintext", self.startTagPlaintext),
-                ("a", self.startTagA),
-                (("b", "big", "code", "em", "font", "i", "s", "small", "strike",
-                  "strong", "tt", "u"), self.startTagFormatting),
-                ("nobr", self.startTagNobr),
-                ("button", self.startTagButton),
-                (("applet", "marquee", "object"), self.startTagAppletMarqueeObject),
-                ("xmp", self.startTagXmp),
-                ("table", self.startTagTable),
-                (("area", "br", "embed", "img", "keygen", "wbr"),
-                 self.startTagVoidFormatting),
-                (("param", "source", "track"), self.startTagParamSource),
-                ("input", self.startTagInput),
-                ("hr", self.startTagHr),
-                ("image", self.startTagImage),
-                ("isindex", self.startTagIsIndex),
-                ("textarea", self.startTagTextarea),
-                ("iframe", self.startTagIFrame),
-                ("noscript", self.startTagNoscript),
-                (("noembed", "noframes"), self.startTagRawtext),
-                ("select", self.startTagSelect),
-                (("rp", "rt"), self.startTagRpRt),
-                (("option", "optgroup"), self.startTagOpt),
-                (("math"), self.startTagMath),
-                (("svg"), self.startTagSvg),
-                (("caption", "col", "colgroup", "frame", "head",
-                  "tbody", "td", "tfoot", "th", "thead",
-                  "tr"), self.startTagMisplaced)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("body", self.endTagBody),
-                ("html", self.endTagHtml),
-                (("address", "article", "aside", "blockquote", "button", "center",
-                  "details", "dialog", "dir", "div", "dl", "fieldset", "figcaption", "figure",
-                  "footer", "header", "hgroup", "listing", "main", "menu", "nav", "ol", "pre",
-                  "section", "summary", "ul"), self.endTagBlock),
-                ("form", self.endTagForm),
-                ("p", self.endTagP),
-                (("dd", "dt", "li"), self.endTagListItem),
-                (headingElements, self.endTagHeading),
-                (("a", "b", "big", "code", "em", "font", "i", "nobr", "s", "small",
-                  "strike", "strong", "tt", "u"), self.endTagFormatting),
-                (("applet", "marquee", "object"), self.endTagAppletMarqueeObject),
-                ("br", self.endTagBr),
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def isMatchingFormattingElement(self, node1, node2):
-            return (node1.name == node2.name and
-                    node1.namespace == node2.namespace and
-                    node1.attributes == node2.attributes)
-
-        # helper
-        def addFormattingElement(self, token):
-            self.tree.insertElement(token)
-            element = self.tree.openElements[-1]
-
-            matchingElements = []
-            for node in self.tree.activeFormattingElements[::-1]:
-                if node is Marker:
-                    break
-                elif self.isMatchingFormattingElement(node, element):
-                    matchingElements.append(node)
-
-            assert len(matchingElements) <= 3
-            if len(matchingElements) == 3:
-                self.tree.activeFormattingElements.remove(matchingElements[-1])
-            self.tree.activeFormattingElements.append(element)
-
-        # the real deal
-        def processEOF(self):
-            allowed_elements = frozenset(("dd", "dt", "li", "p", "tbody", "td",
-                                          "tfoot", "th", "thead", "tr", "body",
-                                          "html"))
-            for node in self.tree.openElements[::-1]:
-                if node.name not in allowed_elements:
-                    self.parser.parseError("expected-closing-tag-but-got-eof")
-                    break
-            # Stop parsing
-
-        def processSpaceCharactersDropNewline(self, token):
-            # Sometimes (start of <pre>, <listing>, and <textarea> blocks) we
-            # want to drop leading newlines
-            data = token["data"]
-            self.processSpaceCharacters = self.processSpaceCharactersNonPre
-            if (data.startswith("\n") and
-                self.tree.openElements[-1].name in ("pre", "listing", "textarea") and
-                    not self.tree.openElements[-1].hasContent()):
-                data = data[1:]
-            if data:
-                self.tree.reconstructActiveFormattingElements()
-                self.tree.insertText(data)
-
-        def processCharacters(self, token):
-            if token["data"] == "\u0000":
-                # The tokenizer should always emit null on its own
-                return
-            self.tree.reconstructActiveFormattingElements()
-            self.tree.insertText(token["data"])
-            # This must be bad for performance
-            if (self.parser.framesetOK and
-                any([char not in spaceCharacters
-                     for char in token["data"]])):
-                self.parser.framesetOK = False
-
-        def processSpaceCharactersNonPre(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.tree.insertText(token["data"])
-
-        def startTagProcessInHead(self, token):
-            return self.parser.phases["inHead"].processStartTag(token)
-
-        def startTagBody(self, token):
-            self.parser.parseError("unexpected-start-tag", {"name": "body"})
-            if (len(self.tree.openElements) == 1 or
-                    self.tree.openElements[1].name != "body"):
-                assert self.parser.innerHTML
-            else:
-                self.parser.framesetOK = False
-                for attr, value in token["data"].items():
-                    if attr not in self.tree.openElements[1].attributes:
-                        self.tree.openElements[1].attributes[attr] = value
-
-        def startTagFrameset(self, token):
-            self.parser.parseError("unexpected-start-tag", {"name": "frameset"})
-            if (len(self.tree.openElements) == 1 or self.tree.openElements[1].name != "body"):
-                assert self.parser.innerHTML
-            elif not self.parser.framesetOK:
-                pass
-            else:
-                if self.tree.openElements[1].parent:
-                    self.tree.openElements[1].parent.removeChild(self.tree.openElements[1])
-                while self.tree.openElements[-1].name != "html":
-                    self.tree.openElements.pop()
-                self.tree.insertElement(token)
-                self.parser.phase = self.parser.phases["inFrameset"]
-
-        def startTagCloseP(self, token):
-            if self.tree.elementInScope("p", variant="button"):
-                self.endTagP(impliedTagToken("p"))
-            self.tree.insertElement(token)
-
-        def startTagPreListing(self, token):
-            if self.tree.elementInScope("p", variant="button"):
-                self.endTagP(impliedTagToken("p"))
-            self.tree.insertElement(token)
-            self.parser.framesetOK = False
-            self.processSpaceCharacters = self.processSpaceCharactersDropNewline
-
-        def startTagForm(self, token):
-            if self.tree.formPointer:
-                self.parser.parseError("unexpected-start-tag", {"name": "form"})
-            else:
-                if self.tree.elementInScope("p", variant="button"):
-                    self.endTagP(impliedTagToken("p"))
-                self.tree.insertElement(token)
-                self.tree.formPointer = self.tree.openElements[-1]
-
-        def startTagListItem(self, token):
-            self.parser.framesetOK = False
-
-            stopNamesMap = {"li": ["li"],
-                            "dt": ["dt", "dd"],
-                            "dd": ["dt", "dd"]}
-            stopNames = stopNamesMap[token["name"]]
-            for node in reversed(self.tree.openElements):
-                if node.name in stopNames:
-                    self.parser.phase.processEndTag(
-                        impliedTagToken(node.name, "EndTag"))
-                    break
-                if (node.nameTuple in specialElements and
-                        node.name not in ("address", "div", "p")):
-                    break
-
-            if self.tree.elementInScope("p", variant="button"):
-                self.parser.phase.processEndTag(
-                    impliedTagToken("p", "EndTag"))
-
-            self.tree.insertElement(token)
-
-        def startTagPlaintext(self, token):
-            if self.tree.elementInScope("p", variant="button"):
-                self.endTagP(impliedTagToken("p"))
-            self.tree.insertElement(token)
-            self.parser.tokenizer.state = self.parser.tokenizer.plaintextState
-
-        def startTagHeading(self, token):
-            if self.tree.elementInScope("p", variant="button"):
-                self.endTagP(impliedTagToken("p"))
-            if self.tree.openElements[-1].name in headingElements:
-                self.parser.parseError("unexpected-start-tag", {"name": token["name"]})
-                self.tree.openElements.pop()
-            self.tree.insertElement(token)
-
-        def startTagA(self, token):
-            afeAElement = self.tree.elementInActiveFormattingElements("a")
-            if afeAElement:
-                self.parser.parseError("unexpected-start-tag-implies-end-tag",
-                                       {"startName": "a", "endName": "a"})
-                self.endTagFormatting(impliedTagToken("a"))
-                if afeAElement in self.tree.openElements:
-                    self.tree.openElements.remove(afeAElement)
-                if afeAElement in self.tree.activeFormattingElements:
-                    self.tree.activeFormattingElements.remove(afeAElement)
-            self.tree.reconstructActiveFormattingElements()
-            self.addFormattingElement(token)
-
-        def startTagFormatting(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.addFormattingElement(token)
-
-        def startTagNobr(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            if self.tree.elementInScope("nobr"):
-                self.parser.parseError("unexpected-start-tag-implies-end-tag",
-                                       {"startName": "nobr", "endName": "nobr"})
-                self.processEndTag(impliedTagToken("nobr"))
-                # XXX Need tests that trigger the following
-                self.tree.reconstructActiveFormattingElements()
-            self.addFormattingElement(token)
-
-        def startTagButton(self, token):
-            if self.tree.elementInScope("button"):
-                self.parser.parseError("unexpected-start-tag-implies-end-tag",
-                                       {"startName": "button", "endName": "button"})
-                self.processEndTag(impliedTagToken("button"))
-                return token
-            else:
-                self.tree.reconstructActiveFormattingElements()
-                self.tree.insertElement(token)
-                self.parser.framesetOK = False
-
-        def startTagAppletMarqueeObject(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.tree.insertElement(token)
-            self.tree.activeFormattingElements.append(Marker)
-            self.parser.framesetOK = False
-
-        def startTagXmp(self, token):
-            if self.tree.elementInScope("p", variant="button"):
-                self.endTagP(impliedTagToken("p"))
-            self.tree.reconstructActiveFormattingElements()
-            self.parser.framesetOK = False
-            self.parser.parseRCDataRawtext(token, "RAWTEXT")
-
-        def startTagTable(self, token):
-            if self.parser.compatMode != "quirks":
-                if self.tree.elementInScope("p", variant="button"):
-                    self.processEndTag(impliedTagToken("p"))
-            self.tree.insertElement(token)
-            self.parser.framesetOK = False
-            self.parser.phase = self.parser.phases["inTable"]
-
-        def startTagVoidFormatting(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.tree.insertElement(token)
-            self.tree.openElements.pop()
-            token["selfClosingAcknowledged"] = True
-            self.parser.framesetOK = False
-
-        def startTagInput(self, token):
-            framesetOK = self.parser.framesetOK
-            self.startTagVoidFormatting(token)
-            if ("type" in token["data"] and
-                    token["data"]["type"].translate(asciiUpper2Lower) == "hidden"):
-                # input type=hidden doesn't change framesetOK
-                self.parser.framesetOK = framesetOK
-
-        def startTagParamSource(self, token):
-            self.tree.insertElement(token)
-            self.tree.openElements.pop()
-            token["selfClosingAcknowledged"] = True
-
-        def startTagHr(self, token):
-            if self.tree.elementInScope("p", variant="button"):
-                self.endTagP(impliedTagToken("p"))
-            self.tree.insertElement(token)
-            self.tree.openElements.pop()
-            token["selfClosingAcknowledged"] = True
-            self.parser.framesetOK = False
-
-        def startTagImage(self, token):
-            # No really...
-            self.parser.parseError("unexpected-start-tag-treated-as",
-                                   {"originalName": "image", "newName": "img"})
-            self.processStartTag(impliedTagToken("img", "StartTag",
-                                                 attributes=token["data"],
-                                                 selfClosing=token["selfClosing"]))
-
-        def startTagIsIndex(self, token):
-            self.parser.parseError("deprecated-tag", {"name": "isindex"})
-            if self.tree.formPointer:
-                return
-            form_attrs = {}
-            if "action" in token["data"]:
-                form_attrs["action"] = token["data"]["action"]
-            self.processStartTag(impliedTagToken("form", "StartTag",
-                                                 attributes=form_attrs))
-            self.processStartTag(impliedTagToken("hr", "StartTag"))
-            self.processStartTag(impliedTagToken("label", "StartTag"))
-            # XXX Localization ...
-            if "prompt" in token["data"]:
-                prompt = token["data"]["prompt"]
-            else:
-                prompt = "This is a searchable index. Enter search keywords: "
-            self.processCharacters(
-                {"type": tokenTypes["Characters"], "data": prompt})
-            attributes = token["data"].copy()
-            if "action" in attributes:
-                del attributes["action"]
-            if "prompt" in attributes:
-                del attributes["prompt"]
-            attributes["name"] = "isindex"
-            self.processStartTag(impliedTagToken("input", "StartTag",
-                                                 attributes=attributes,
-                                                 selfClosing=token["selfClosing"]))
-            self.processEndTag(impliedTagToken("label"))
-            self.processStartTag(impliedTagToken("hr", "StartTag"))
-            self.processEndTag(impliedTagToken("form"))
-
-        def startTagTextarea(self, token):
-            self.tree.insertElement(token)
-            self.parser.tokenizer.state = self.parser.tokenizer.rcdataState
-            self.processSpaceCharacters = self.processSpaceCharactersDropNewline
-            self.parser.framesetOK = False
-
-        def startTagIFrame(self, token):
-            self.parser.framesetOK = False
-            self.startTagRawtext(token)
-
-        def startTagNoscript(self, token):
-            if self.parser.scripting:
-                self.startTagRawtext(token)
-            else:
-                self.startTagOther(token)
-
-        def startTagRawtext(self, token):
-            """iframe, noembed noframes, noscript(if scripting enabled)"""
-            self.parser.parseRCDataRawtext(token, "RAWTEXT")
-
-        def startTagOpt(self, token):
-            if self.tree.openElements[-1].name == "option":
-                self.parser.phase.processEndTag(impliedTagToken("option"))
-            self.tree.reconstructActiveFormattingElements()
-            self.parser.tree.insertElement(token)
-
-        def startTagSelect(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.tree.insertElement(token)
-            self.parser.framesetOK = False
-            if self.parser.phase in (self.parser.phases["inTable"],
-                                     self.parser.phases["inCaption"],
-                                     self.parser.phases["inColumnGroup"],
-                                     self.parser.phases["inTableBody"],
-                                     self.parser.phases["inRow"],
-                                     self.parser.phases["inCell"]):
-                self.parser.phase = self.parser.phases["inSelectInTable"]
-            else:
-                self.parser.phase = self.parser.phases["inSelect"]
-
-        def startTagRpRt(self, token):
-            if self.tree.elementInScope("ruby"):
-                self.tree.generateImpliedEndTags()
-                if self.tree.openElements[-1].name != "ruby":
-                    self.parser.parseError()
-            self.tree.insertElement(token)
-
-        def startTagMath(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.parser.adjustMathMLAttributes(token)
-            self.parser.adjustForeignAttributes(token)
-            token["namespace"] = namespaces["mathml"]
-            self.tree.insertElement(token)
-            # Need to get the parse error right for the case where the token
-            # has a namespace not equal to the xmlns attribute
-            if token["selfClosing"]:
-                self.tree.openElements.pop()
-                token["selfClosingAcknowledged"] = True
-
-        def startTagSvg(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.parser.adjustSVGAttributes(token)
-            self.parser.adjustForeignAttributes(token)
-            token["namespace"] = namespaces["svg"]
-            self.tree.insertElement(token)
-            # Need to get the parse error right for the case where the token
-            # has a namespace not equal to the xmlns attribute
-            if token["selfClosing"]:
-                self.tree.openElements.pop()
-                token["selfClosingAcknowledged"] = True
-
-        def startTagMisplaced(self, token):
-            """ Elements that should be children of other elements that have a
-            different insertion mode; here they are ignored
-            "caption", "col", "colgroup", "frame", "frameset", "head",
-            "option", "optgroup", "tbody", "td", "tfoot", "th", "thead",
-            "tr", "noscript"
-            """
-            self.parser.parseError("unexpected-start-tag-ignored", {"name": token["name"]})
-
-        def startTagOther(self, token):
-            self.tree.reconstructActiveFormattingElements()
-            self.tree.insertElement(token)
-
-        def endTagP(self, token):
-            if not self.tree.elementInScope("p", variant="button"):
-                self.startTagCloseP(impliedTagToken("p", "StartTag"))
-                self.parser.parseError("unexpected-end-tag", {"name": "p"})
-                self.endTagP(impliedTagToken("p", "EndTag"))
-            else:
-                self.tree.generateImpliedEndTags("p")
-                if self.tree.openElements[-1].name != "p":
-                    self.parser.parseError("unexpected-end-tag", {"name": "p"})
-                node = self.tree.openElements.pop()
-                while node.name != "p":
-                    node = self.tree.openElements.pop()
-
-        def endTagBody(self, token):
-            if not self.tree.elementInScope("body"):
-                self.parser.parseError()
-                return
-            elif self.tree.openElements[-1].name != "body":
-                for node in self.tree.openElements[2:]:
-                    if node.name not in frozenset(("dd", "dt", "li", "optgroup",
-                                                   "option", "p", "rp", "rt",
-                                                   "tbody", "td", "tfoot",
-                                                   "th", "thead", "tr", "body",
-                                                   "html")):
-                        # Not sure this is the correct name for the parse error
-                        self.parser.parseError(
-                            "expected-one-end-tag-but-got-another",
-                            {"gotName": "body", "expectedName": node.name})
-                        break
-            self.parser.phase = self.parser.phases["afterBody"]
-
-        def endTagHtml(self, token):
-            # We repeat the test for the body end tag token being ignored here
-            if self.tree.elementInScope("body"):
-                self.endTagBody(impliedTagToken("body"))
-                return token
-
-        def endTagBlock(self, token):
-            # Put us back in the right whitespace handling mode
-            if token["name"] == "pre":
-                self.processSpaceCharacters = self.processSpaceCharactersNonPre
-            inScope = self.tree.elementInScope(token["name"])
-            if inScope:
-                self.tree.generateImpliedEndTags()
-            if self.tree.openElements[-1].name != token["name"]:
-                self.parser.parseError("end-tag-too-early", {"name": token["name"]})
-            if inScope:
-                node = self.tree.openElements.pop()
-                while node.name != token["name"]:
-                    node = self.tree.openElements.pop()
-
-        def endTagForm(self, token):
-            node = self.tree.formPointer
-            self.tree.formPointer = None
-            if node is None or not self.tree.elementInScope(node):
-                self.parser.parseError("unexpected-end-tag",
-                                       {"name": "form"})
-            else:
-                self.tree.generateImpliedEndTags()
-                if self.tree.openElements[-1] != node:
-                    self.parser.parseError("end-tag-too-early-ignored",
-                                           {"name": "form"})
-                self.tree.openElements.remove(node)
-
-        def endTagListItem(self, token):
-            if token["name"] == "li":
-                variant = "list"
-            else:
-                variant = None
-            if not self.tree.elementInScope(token["name"], variant=variant):
-                self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-            else:
-                self.tree.generateImpliedEndTags(exclude=token["name"])
-                if self.tree.openElements[-1].name != token["name"]:
-                    self.parser.parseError(
-                        "end-tag-too-early",
-                        {"name": token["name"]})
-                node = self.tree.openElements.pop()
-                while node.name != token["name"]:
-                    node = self.tree.openElements.pop()
-
-        def endTagHeading(self, token):
-            for item in headingElements:
-                if self.tree.elementInScope(item):
-                    self.tree.generateImpliedEndTags()
-                    break
-            if self.tree.openElements[-1].name != token["name"]:
-                self.parser.parseError("end-tag-too-early", {"name": token["name"]})
-
-            for item in headingElements:
-                if self.tree.elementInScope(item):
-                    item = self.tree.openElements.pop()
-                    while item.name not in headingElements:
-                        item = self.tree.openElements.pop()
-                    break
-
-        def endTagFormatting(self, token):
-            """The much-feared adoption agency algorithm"""
-            # http://svn.whatwg.org/webapps/complete.html#adoptionAgency revision 7867
-            # XXX Better parseError messages appreciated.
-
-            # Step 1
-            outerLoopCounter = 0
-
-            # Step 2
-            while outerLoopCounter < 8:
-
-                # Step 3
-                outerLoopCounter += 1
-
-                # Step 4:
-
-                # Let the formatting element be the last element in
-                # the list of active formatting elements that:
-                # - is between the end of the list and the last scope
-                # marker in the list, if any, or the start of the list
-                # otherwise, and
-                # - has the same tag name as the token.
-                formattingElement = self.tree.elementInActiveFormattingElements(
-                    token["name"])
-                if (not formattingElement or
-                    (formattingElement in self.tree.openElements and
-                     not self.tree.elementInScope(formattingElement.name))):
-                    # If there is no such node, then abort these steps
-                    # and instead act as described in the "any other
-                    # end tag" entry below.
-                    self.endTagOther(token)
-                    return
-
-                # Otherwise, if there is such a node, but that node is
-                # not in the stack of open elements, then this is a
-                # parse error; remove the element from the list, and
-                # abort these steps.
-                elif formattingElement not in self.tree.openElements:
-                    self.parser.parseError("adoption-agency-1.2", {"name": token["name"]})
-                    self.tree.activeFormattingElements.remove(formattingElement)
-                    return
-
-                # Otherwise, if there is such a node, and that node is
-                # also in the stack of open elements, but the element
-                # is not in scope, then this is a parse error; ignore
-                # the token, and abort these steps.
-                elif not self.tree.elementInScope(formattingElement.name):
-                    self.parser.parseError("adoption-agency-4.4", {"name": token["name"]})
-                    return
-
-                # Otherwise, there is a formatting element and that
-                # element is in the stack and is in scope. If the
-                # element is not the current node, this is a parse
-                # error. In any case, proceed with the algorithm as
-                # written in the following steps.
-                else:
-                    if formattingElement != self.tree.openElements[-1]:
-                        self.parser.parseError("adoption-agency-1.3", {"name": token["name"]})
-
-                # Step 5:
-
-                # Let the furthest block be the topmost node in the
-                # stack of open elements that is lower in the stack
-                # than the formatting element, and is an element in
-                # the special category. There might not be one.
-                afeIndex = self.tree.openElements.index(formattingElement)
-                furthestBlock = None
-                for element in self.tree.openElements[afeIndex:]:
-                    if element.nameTuple in specialElements:
-                        furthestBlock = element
-                        break
-
-                # Step 6:
-
-                # If there is no furthest block, then the UA must
-                # first pop all the nodes from the bottom of the stack
-                # of open elements, from the current node up to and
-                # including the formatting element, then remove the
-                # formatting element from the list of active
-                # formatting elements, and finally abort these steps.
-                if furthestBlock is None:
-                    element = self.tree.openElements.pop()
-                    while element != formattingElement:
-                        element = self.tree.openElements.pop()
-                    self.tree.activeFormattingElements.remove(element)
-                    return
-
-                # Step 7
-                commonAncestor = self.tree.openElements[afeIndex - 1]
-
-                # Step 8:
-                # The bookmark is supposed to help us identify where to reinsert
-                # nodes in step 15. We have to ensure that we reinsert nodes after
-                # the node before the active formatting element. Note the bookmark
-                # can move in step 9.7
-                bookmark = self.tree.activeFormattingElements.index(formattingElement)
-
-                # Step 9
-                lastNode = node = furthestBlock
-                innerLoopCounter = 0
-
-                index = self.tree.openElements.index(node)
-                while innerLoopCounter < 3:
-                    innerLoopCounter += 1
-                    # Node is element before node in open elements
-                    index -= 1
-                    node = self.tree.openElements[index]
-                    if node not in self.tree.activeFormattingElements:
-                        self.tree.openElements.remove(node)
-                        continue
-                    # Step 9.6
-                    if node == formattingElement:
-                        break
-                    # Step 9.7
-                    if lastNode == furthestBlock:
-                        bookmark = self.tree.activeFormattingElements.index(node) + 1
-                    # Step 9.8
-                    clone = node.cloneNode()
-                    # Replace node with clone
-                    self.tree.activeFormattingElements[
-                        self.tree.activeFormattingElements.index(node)] = clone
-                    self.tree.openElements[
-                        self.tree.openElements.index(node)] = clone
-                    node = clone
-                    # Step 9.9
-                    # Remove lastNode from its parents, if any
-                    if lastNode.parent:
-                        lastNode.parent.removeChild(lastNode)
-                    node.appendChild(lastNode)
-                    # Step 9.10
-                    lastNode = node
-
-                # Step 10
-                # Foster parent lastNode if commonAncestor is a
-                # table, tbody, tfoot, thead, or tr we need to foster
-                # parent the lastNode
-                if lastNode.parent:
-                    lastNode.parent.removeChild(lastNode)
-
-                if commonAncestor.name in frozenset(("table", "tbody", "tfoot", "thead", "tr")):
-                    parent, insertBefore = self.tree.getTableMisnestedNodePosition()
-                    parent.insertBefore(lastNode, insertBefore)
-                else:
-                    commonAncestor.appendChild(lastNode)
-
-                # Step 11
-                clone = formattingElement.cloneNode()
-
-                # Step 12
-                furthestBlock.reparentChildren(clone)
-
-                # Step 13
-                furthestBlock.appendChild(clone)
-
-                # Step 14
-                self.tree.activeFormattingElements.remove(formattingElement)
-                self.tree.activeFormattingElements.insert(bookmark, clone)
-
-                # Step 15
-                self.tree.openElements.remove(formattingElement)
-                self.tree.openElements.insert(
-                    self.tree.openElements.index(furthestBlock) + 1, clone)
-
-        def endTagAppletMarqueeObject(self, token):
-            if self.tree.elementInScope(token["name"]):
-                self.tree.generateImpliedEndTags()
-            if self.tree.openElements[-1].name != token["name"]:
-                self.parser.parseError("end-tag-too-early", {"name": token["name"]})
-
-            if self.tree.elementInScope(token["name"]):
-                element = self.tree.openElements.pop()
-                while element.name != token["name"]:
-                    element = self.tree.openElements.pop()
-                self.tree.clearActiveFormattingElements()
-
-        def endTagBr(self, token):
-            self.parser.parseError("unexpected-end-tag-treated-as",
-                                   {"originalName": "br", "newName": "br element"})
-            self.tree.reconstructActiveFormattingElements()
-            self.tree.insertElement(impliedTagToken("br", "StartTag"))
-            self.tree.openElements.pop()
-
-        def endTagOther(self, token):
-            for node in self.tree.openElements[::-1]:
-                if node.name == token["name"]:
-                    self.tree.generateImpliedEndTags(exclude=token["name"])
-                    if self.tree.openElements[-1].name != token["name"]:
-                        self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-                    while self.tree.openElements.pop() != node:
-                        pass
-                    break
-                else:
-                    if node.nameTuple in specialElements:
-                        self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-                        break
-
-    class TextPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-            self.startTagHandler = _utils.MethodDispatcher([])
-            self.startTagHandler.default = self.startTagOther
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("script", self.endTagScript)])
-            self.endTagHandler.default = self.endTagOther
-
-        def processCharacters(self, token):
-            self.tree.insertText(token["data"])
-
-        def processEOF(self):
-            self.parser.parseError("expected-named-closing-tag-but-got-eof",
-                                   {"name": self.tree.openElements[-1].name})
-            self.tree.openElements.pop()
-            self.parser.phase = self.parser.originalPhase
-            return True
-
-        def startTagOther(self, token):
-            assert False, "Tried to process start tag %s in RCDATA/RAWTEXT mode" % token['name']
-
-        def endTagScript(self, token):
-            node = self.tree.openElements.pop()
-            assert node.name == "script"
-            self.parser.phase = self.parser.originalPhase
-            # The rest of this method is all stuff that only happens if
-            # document.write works
-
-        def endTagOther(self, token):
-            self.tree.openElements.pop()
-            self.parser.phase = self.parser.originalPhase
-
-    class InTablePhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-table
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("caption", self.startTagCaption),
-                ("colgroup", self.startTagColgroup),
-                ("col", self.startTagCol),
-                (("tbody", "tfoot", "thead"), self.startTagRowGroup),
-                (("td", "th", "tr"), self.startTagImplyTbody),
-                ("table", self.startTagTable),
-                (("style", "script"), self.startTagStyleScript),
-                ("input", self.startTagInput),
-                ("form", self.startTagForm)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("table", self.endTagTable),
-                (("body", "caption", "col", "colgroup", "html", "tbody", "td",
-                  "tfoot", "th", "thead", "tr"), self.endTagIgnore)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        # helper methods
-        def clearStackToTableContext(self):
-            # "clear the stack back to a table context"
-            while self.tree.openElements[-1].name not in ("table", "html"):
-                # self.parser.parseError("unexpected-implied-end-tag-in-table",
-                #  {"name":  self.tree.openElements[-1].name})
-                self.tree.openElements.pop()
-            # When the current node is <html> it's an innerHTML case
-
-        # processing methods
-        def processEOF(self):
-            if self.tree.openElements[-1].name != "html":
-                self.parser.parseError("eof-in-table")
-            else:
-                assert self.parser.innerHTML
-            # Stop parsing
-
-        def processSpaceCharacters(self, token):
-            originalPhase = self.parser.phase
-            self.parser.phase = self.parser.phases["inTableText"]
-            self.parser.phase.originalPhase = originalPhase
-            self.parser.phase.processSpaceCharacters(token)
-
-        def processCharacters(self, token):
-            originalPhase = self.parser.phase
-            self.parser.phase = self.parser.phases["inTableText"]
-            self.parser.phase.originalPhase = originalPhase
-            self.parser.phase.processCharacters(token)
-
-        def insertText(self, token):
-            # If we get here there must be at least one non-whitespace character
-            # Do the table magic!
-            self.tree.insertFromTable = True
-            self.parser.phases["inBody"].processCharacters(token)
-            self.tree.insertFromTable = False
-
-        def startTagCaption(self, token):
-            self.clearStackToTableContext()
-            self.tree.activeFormattingElements.append(Marker)
-            self.tree.insertElement(token)
-            self.parser.phase = self.parser.phases["inCaption"]
-
-        def startTagColgroup(self, token):
-            self.clearStackToTableContext()
-            self.tree.insertElement(token)
-            self.parser.phase = self.parser.phases["inColumnGroup"]
-
-        def startTagCol(self, token):
-            self.startTagColgroup(impliedTagToken("colgroup", "StartTag"))
-            return token
-
-        def startTagRowGroup(self, token):
-            self.clearStackToTableContext()
-            self.tree.insertElement(token)
-            self.parser.phase = self.parser.phases["inTableBody"]
-
-        def startTagImplyTbody(self, token):
-            self.startTagRowGroup(impliedTagToken("tbody", "StartTag"))
-            return token
-
-        def startTagTable(self, token):
-            self.parser.parseError("unexpected-start-tag-implies-end-tag",
-                                   {"startName": "table", "endName": "table"})
-            self.parser.phase.processEndTag(impliedTagToken("table"))
-            if not self.parser.innerHTML:
-                return token
-
-        def startTagStyleScript(self, token):
-            return self.parser.phases["inHead"].processStartTag(token)
-
-        def startTagInput(self, token):
-            if ("type" in token["data"] and
-                    token["data"]["type"].translate(asciiUpper2Lower) == "hidden"):
-                self.parser.parseError("unexpected-hidden-input-in-table")
-                self.tree.insertElement(token)
-                # XXX associate with form
-                self.tree.openElements.pop()
-            else:
-                self.startTagOther(token)
-
-        def startTagForm(self, token):
-            self.parser.parseError("unexpected-form-in-table")
-            if self.tree.formPointer is None:
-                self.tree.insertElement(token)
-                self.tree.formPointer = self.tree.openElements[-1]
-                self.tree.openElements.pop()
-
-        def startTagOther(self, token):
-            self.parser.parseError("unexpected-start-tag-implies-table-voodoo", {"name": token["name"]})
-            # Do the table magic!
-            self.tree.insertFromTable = True
-            self.parser.phases["inBody"].processStartTag(token)
-            self.tree.insertFromTable = False
-
-        def endTagTable(self, token):
-            if self.tree.elementInScope("table", variant="table"):
-                self.tree.generateImpliedEndTags()
-                if self.tree.openElements[-1].name != "table":
-                    self.parser.parseError("end-tag-too-early-named",
-                                           {"gotName": "table",
-                                            "expectedName": self.tree.openElements[-1].name})
-                while self.tree.openElements[-1].name != "table":
-                    self.tree.openElements.pop()
-                self.tree.openElements.pop()
-                self.parser.resetInsertionMode()
-            else:
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-
-        def endTagIgnore(self, token):
-            self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag-implies-table-voodoo", {"name": token["name"]})
-            # Do the table magic!
-            self.tree.insertFromTable = True
-            self.parser.phases["inBody"].processEndTag(token)
-            self.tree.insertFromTable = False
-
-    class InTableTextPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-            self.originalPhase = None
-            self.characterTokens = []
-
-        def flushCharacters(self):
-            data = "".join([item["data"] for item in self.characterTokens])
-            if any([item not in spaceCharacters for item in data]):
-                token = {"type": tokenTypes["Characters"], "data": data}
-                self.parser.phases["inTable"].insertText(token)
-            elif data:
-                self.tree.insertText(data)
-            self.characterTokens = []
-
-        def processComment(self, token):
-            self.flushCharacters()
-            self.parser.phase = self.originalPhase
-            return token
-
-        def processEOF(self):
-            self.flushCharacters()
-            self.parser.phase = self.originalPhase
-            return True
-
-        def processCharacters(self, token):
-            if token["data"] == "\u0000":
-                return
-            self.characterTokens.append(token)
-
-        def processSpaceCharacters(self, token):
-            # pretty sure we should never reach here
-            self.characterTokens.append(token)
-    #        assert False
-
-        def processStartTag(self, token):
-            self.flushCharacters()
-            self.parser.phase = self.originalPhase
-            return token
-
-        def processEndTag(self, token):
-            self.flushCharacters()
-            self.parser.phase = self.originalPhase
-            return token
-
-    class InCaptionPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-caption
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                (("caption", "col", "colgroup", "tbody", "td", "tfoot", "th",
-                  "thead", "tr"), self.startTagTableElement)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("caption", self.endTagCaption),
-                ("table", self.endTagTable),
-                (("body", "col", "colgroup", "html", "tbody", "td", "tfoot", "th",
-                  "thead", "tr"), self.endTagIgnore)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def ignoreEndTagCaption(self):
-            return not self.tree.elementInScope("caption", variant="table")
-
-        def processEOF(self):
-            self.parser.phases["inBody"].processEOF()
-
-        def processCharacters(self, token):
-            return self.parser.phases["inBody"].processCharacters(token)
-
-        def startTagTableElement(self, token):
-            self.parser.parseError()
-            # XXX Have to duplicate logic here to find out if the tag is ignored
-            ignoreEndTag = self.ignoreEndTagCaption()
-            self.parser.phase.processEndTag(impliedTagToken("caption"))
-            if not ignoreEndTag:
-                return token
-
-        def startTagOther(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def endTagCaption(self, token):
-            if not self.ignoreEndTagCaption():
-                # AT this code is quite similar to endTagTable in "InTable"
-                self.tree.generateImpliedEndTags()
-                if self.tree.openElements[-1].name != "caption":
-                    self.parser.parseError("expected-one-end-tag-but-got-another",
-                                           {"gotName": "caption",
-                                            "expectedName": self.tree.openElements[-1].name})
-                while self.tree.openElements[-1].name != "caption":
-                    self.tree.openElements.pop()
-                self.tree.openElements.pop()
-                self.tree.clearActiveFormattingElements()
-                self.parser.phase = self.parser.phases["inTable"]
-            else:
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-
-        def endTagTable(self, token):
-            self.parser.parseError()
-            ignoreEndTag = self.ignoreEndTagCaption()
-            self.parser.phase.processEndTag(impliedTagToken("caption"))
-            if not ignoreEndTag:
-                return token
-
-        def endTagIgnore(self, token):
-            self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-        def endTagOther(self, token):
-            return self.parser.phases["inBody"].processEndTag(token)
-
-    class InColumnGroupPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-column
-
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("col", self.startTagCol)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("colgroup", self.endTagColgroup),
-                ("col", self.endTagCol)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def ignoreEndTagColgroup(self):
-            return self.tree.openElements[-1].name == "html"
-
-        def processEOF(self):
-            if self.tree.openElements[-1].name == "html":
-                assert self.parser.innerHTML
-                return
-            else:
-                ignoreEndTag = self.ignoreEndTagColgroup()
-                self.endTagColgroup(impliedTagToken("colgroup"))
-                if not ignoreEndTag:
-                    return True
-
-        def processCharacters(self, token):
-            ignoreEndTag = self.ignoreEndTagColgroup()
-            self.endTagColgroup(impliedTagToken("colgroup"))
-            if not ignoreEndTag:
-                return token
-
-        def startTagCol(self, token):
-            self.tree.insertElement(token)
-            self.tree.openElements.pop()
-            token["selfClosingAcknowledged"] = True
-
-        def startTagOther(self, token):
-            ignoreEndTag = self.ignoreEndTagColgroup()
-            self.endTagColgroup(impliedTagToken("colgroup"))
-            if not ignoreEndTag:
-                return token
-
-        def endTagColgroup(self, token):
-            if self.ignoreEndTagColgroup():
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-            else:
-                self.tree.openElements.pop()
-                self.parser.phase = self.parser.phases["inTable"]
-
-        def endTagCol(self, token):
-            self.parser.parseError("no-end-tag", {"name": "col"})
-
-        def endTagOther(self, token):
-            ignoreEndTag = self.ignoreEndTagColgroup()
-            self.endTagColgroup(impliedTagToken("colgroup"))
-            if not ignoreEndTag:
-                return token
-
-    class InTableBodyPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-table0
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("tr", self.startTagTr),
-                (("td", "th"), self.startTagTableCell),
-                (("caption", "col", "colgroup", "tbody", "tfoot", "thead"),
-                 self.startTagTableOther)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                (("tbody", "tfoot", "thead"), self.endTagTableRowGroup),
-                ("table", self.endTagTable),
-                (("body", "caption", "col", "colgroup", "html", "td", "th",
-                  "tr"), self.endTagIgnore)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        # helper methods
-        def clearStackToTableBodyContext(self):
-            while self.tree.openElements[-1].name not in ("tbody", "tfoot",
-                                                          "thead", "html"):
-                # self.parser.parseError("unexpected-implied-end-tag-in-table",
-                #  {"name": self.tree.openElements[-1].name})
-                self.tree.openElements.pop()
-            if self.tree.openElements[-1].name == "html":
-                assert self.parser.innerHTML
-
-        # the rest
-        def processEOF(self):
-            self.parser.phases["inTable"].processEOF()
-
-        def processSpaceCharacters(self, token):
-            return self.parser.phases["inTable"].processSpaceCharacters(token)
-
-        def processCharacters(self, token):
-            return self.parser.phases["inTable"].processCharacters(token)
-
-        def startTagTr(self, token):
-            self.clearStackToTableBodyContext()
-            self.tree.insertElement(token)
-            self.parser.phase = self.parser.phases["inRow"]
-
-        def startTagTableCell(self, token):
-            self.parser.parseError("unexpected-cell-in-table-body",
-                                   {"name": token["name"]})
-            self.startTagTr(impliedTagToken("tr", "StartTag"))
-            return token
-
-        def startTagTableOther(self, token):
-            # XXX AT Any ideas on how to share this with endTagTable?
-            if (self.tree.elementInScope("tbody", variant="table") or
-                self.tree.elementInScope("thead", variant="table") or
-                    self.tree.elementInScope("tfoot", variant="table")):
-                self.clearStackToTableBodyContext()
-                self.endTagTableRowGroup(
-                    impliedTagToken(self.tree.openElements[-1].name))
-                return token
-            else:
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-
-        def startTagOther(self, token):
-            return self.parser.phases["inTable"].processStartTag(token)
-
-        def endTagTableRowGroup(self, token):
-            if self.tree.elementInScope(token["name"], variant="table"):
-                self.clearStackToTableBodyContext()
-                self.tree.openElements.pop()
-                self.parser.phase = self.parser.phases["inTable"]
-            else:
-                self.parser.parseError("unexpected-end-tag-in-table-body",
-                                       {"name": token["name"]})
-
-        def endTagTable(self, token):
-            if (self.tree.elementInScope("tbody", variant="table") or
-                self.tree.elementInScope("thead", variant="table") or
-                    self.tree.elementInScope("tfoot", variant="table")):
-                self.clearStackToTableBodyContext()
-                self.endTagTableRowGroup(
-                    impliedTagToken(self.tree.openElements[-1].name))
-                return token
-            else:
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-
-        def endTagIgnore(self, token):
-            self.parser.parseError("unexpected-end-tag-in-table-body",
-                                   {"name": token["name"]})
-
-        def endTagOther(self, token):
-            return self.parser.phases["inTable"].processEndTag(token)
-
-    class InRowPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-row
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                (("td", "th"), self.startTagTableCell),
-                (("caption", "col", "colgroup", "tbody", "tfoot", "thead",
-                  "tr"), self.startTagTableOther)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("tr", self.endTagTr),
-                ("table", self.endTagTable),
-                (("tbody", "tfoot", "thead"), self.endTagTableRowGroup),
-                (("body", "caption", "col", "colgroup", "html", "td", "th"),
-                 self.endTagIgnore)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        # helper methods (XXX unify this with other table helper methods)
-        def clearStackToTableRowContext(self):
-            while self.tree.openElements[-1].name not in ("tr", "html"):
-                self.parser.parseError("unexpected-implied-end-tag-in-table-row",
-                                       {"name": self.tree.openElements[-1].name})
-                self.tree.openElements.pop()
-
-        def ignoreEndTagTr(self):
-            return not self.tree.elementInScope("tr", variant="table")
-
-        # the rest
-        def processEOF(self):
-            self.parser.phases["inTable"].processEOF()
-
-        def processSpaceCharacters(self, token):
-            return self.parser.phases["inTable"].processSpaceCharacters(token)
-
-        def processCharacters(self, token):
-            return self.parser.phases["inTable"].processCharacters(token)
-
-        def startTagTableCell(self, token):
-            self.clearStackToTableRowContext()
-            self.tree.insertElement(token)
-            self.parser.phase = self.parser.phases["inCell"]
-            self.tree.activeFormattingElements.append(Marker)
-
-        def startTagTableOther(self, token):
-            ignoreEndTag = self.ignoreEndTagTr()
-            self.endTagTr(impliedTagToken("tr"))
-            # XXX how are we sure it's always ignored in the innerHTML case?
-            if not ignoreEndTag:
-                return token
-
-        def startTagOther(self, token):
-            return self.parser.phases["inTable"].processStartTag(token)
-
-        def endTagTr(self, token):
-            if not self.ignoreEndTagTr():
-                self.clearStackToTableRowContext()
-                self.tree.openElements.pop()
-                self.parser.phase = self.parser.phases["inTableBody"]
-            else:
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-
-        def endTagTable(self, token):
-            ignoreEndTag = self.ignoreEndTagTr()
-            self.endTagTr(impliedTagToken("tr"))
-            # Reprocess the current tag if the tr end tag was not ignored
-            # XXX how are we sure it's always ignored in the innerHTML case?
-            if not ignoreEndTag:
-                return token
-
-        def endTagTableRowGroup(self, token):
-            if self.tree.elementInScope(token["name"], variant="table"):
-                self.endTagTr(impliedTagToken("tr"))
-                return token
-            else:
-                self.parser.parseError()
-
-        def endTagIgnore(self, token):
-            self.parser.parseError("unexpected-end-tag-in-table-row",
-                                   {"name": token["name"]})
-
-        def endTagOther(self, token):
-            return self.parser.phases["inTable"].processEndTag(token)
-
-    class InCellPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-cell
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                (("caption", "col", "colgroup", "tbody", "td", "tfoot", "th",
-                  "thead", "tr"), self.startTagTableOther)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                (("td", "th"), self.endTagTableCell),
-                (("body", "caption", "col", "colgroup", "html"), self.endTagIgnore),
-                (("table", "tbody", "tfoot", "thead", "tr"), self.endTagImply)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        # helper
-        def closeCell(self):
-            if self.tree.elementInScope("td", variant="table"):
-                self.endTagTableCell(impliedTagToken("td"))
-            elif self.tree.elementInScope("th", variant="table"):
-                self.endTagTableCell(impliedTagToken("th"))
-
-        # the rest
-        def processEOF(self):
-            self.parser.phases["inBody"].processEOF()
-
-        def processCharacters(self, token):
-            return self.parser.phases["inBody"].processCharacters(token)
-
-        def startTagTableOther(self, token):
-            if (self.tree.elementInScope("td", variant="table") or
-                    self.tree.elementInScope("th", variant="table")):
-                self.closeCell()
-                return token
-            else:
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-
-        def startTagOther(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def endTagTableCell(self, token):
-            if self.tree.elementInScope(token["name"], variant="table"):
-                self.tree.generateImpliedEndTags(token["name"])
-                if self.tree.openElements[-1].name != token["name"]:
-                    self.parser.parseError("unexpected-cell-end-tag",
-                                           {"name": token["name"]})
-                    while True:
-                        node = self.tree.openElements.pop()
-                        if node.name == token["name"]:
-                            break
-                else:
-                    self.tree.openElements.pop()
-                self.tree.clearActiveFormattingElements()
-                self.parser.phase = self.parser.phases["inRow"]
-            else:
-                self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-        def endTagIgnore(self, token):
-            self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-        def endTagImply(self, token):
-            if self.tree.elementInScope(token["name"], variant="table"):
-                self.closeCell()
-                return token
-            else:
-                # sometimes innerHTML case
-                self.parser.parseError()
-
-        def endTagOther(self, token):
-            return self.parser.phases["inBody"].processEndTag(token)
-
-    class InSelectPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("option", self.startTagOption),
-                ("optgroup", self.startTagOptgroup),
-                ("select", self.startTagSelect),
-                (("input", "keygen", "textarea"), self.startTagInput),
-                ("script", self.startTagScript)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("option", self.endTagOption),
-                ("optgroup", self.endTagOptgroup),
-                ("select", self.endTagSelect)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-select
-        def processEOF(self):
-            if self.tree.openElements[-1].name != "html":
-                self.parser.parseError("eof-in-select")
-            else:
-                assert self.parser.innerHTML
-
-        def processCharacters(self, token):
-            if token["data"] == "\u0000":
-                return
-            self.tree.insertText(token["data"])
-
-        def startTagOption(self, token):
-            # We need to imply </option> if <option> is the current node.
-            if self.tree.openElements[-1].name == "option":
-                self.tree.openElements.pop()
-            self.tree.insertElement(token)
-
-        def startTagOptgroup(self, token):
-            if self.tree.openElements[-1].name == "option":
-                self.tree.openElements.pop()
-            if self.tree.openElements[-1].name == "optgroup":
-                self.tree.openElements.pop()
-            self.tree.insertElement(token)
-
-        def startTagSelect(self, token):
-            self.parser.parseError("unexpected-select-in-select")
-            self.endTagSelect(impliedTagToken("select"))
-
-        def startTagInput(self, token):
-            self.parser.parseError("unexpected-input-in-select")
-            if self.tree.elementInScope("select", variant="select"):
-                self.endTagSelect(impliedTagToken("select"))
-                return token
-            else:
-                assert self.parser.innerHTML
-
-        def startTagScript(self, token):
-            return self.parser.phases["inHead"].processStartTag(token)
-
-        def startTagOther(self, token):
-            self.parser.parseError("unexpected-start-tag-in-select",
-                                   {"name": token["name"]})
-
-        def endTagOption(self, token):
-            if self.tree.openElements[-1].name == "option":
-                self.tree.openElements.pop()
-            else:
-                self.parser.parseError("unexpected-end-tag-in-select",
-                                       {"name": "option"})
-
-        def endTagOptgroup(self, token):
-            # </optgroup> implicitly closes <option>
-            if (self.tree.openElements[-1].name == "option" and
-                    self.tree.openElements[-2].name == "optgroup"):
-                self.tree.openElements.pop()
-            # It also closes </optgroup>
-            if self.tree.openElements[-1].name == "optgroup":
-                self.tree.openElements.pop()
-            # But nothing else
-            else:
-                self.parser.parseError("unexpected-end-tag-in-select",
-                                       {"name": "optgroup"})
-
-        def endTagSelect(self, token):
-            if self.tree.elementInScope("select", variant="select"):
-                node = self.tree.openElements.pop()
-                while node.name != "select":
-                    node = self.tree.openElements.pop()
-                self.parser.resetInsertionMode()
-            else:
-                # innerHTML case
-                assert self.parser.innerHTML
-                self.parser.parseError()
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag-in-select",
-                                   {"name": token["name"]})
-
-    class InSelectInTablePhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                (("caption", "table", "tbody", "tfoot", "thead", "tr", "td", "th"),
-                 self.startTagTable)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                (("caption", "table", "tbody", "tfoot", "thead", "tr", "td", "th"),
-                 self.endTagTable)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def processEOF(self):
-            self.parser.phases["inSelect"].processEOF()
-
-        def processCharacters(self, token):
-            return self.parser.phases["inSelect"].processCharacters(token)
-
-        def startTagTable(self, token):
-            self.parser.parseError("unexpected-table-element-start-tag-in-select-in-table", {"name": token["name"]})
-            self.endTagOther(impliedTagToken("select"))
-            return token
-
-        def startTagOther(self, token):
-            return self.parser.phases["inSelect"].processStartTag(token)
-
-        def endTagTable(self, token):
-            self.parser.parseError("unexpected-table-element-end-tag-in-select-in-table", {"name": token["name"]})
-            if self.tree.elementInScope(token["name"], variant="table"):
-                self.endTagOther(impliedTagToken("select"))
-                return token
-
-        def endTagOther(self, token):
-            return self.parser.phases["inSelect"].processEndTag(token)
-
-    class InForeignContentPhase(Phase):
-        breakoutElements = frozenset(["b", "big", "blockquote", "body", "br",
-                                      "center", "code", "dd", "div", "dl", "dt",
-                                      "em", "embed", "h1", "h2", "h3",
-                                      "h4", "h5", "h6", "head", "hr", "i", "img",
-                                      "li", "listing", "menu", "meta", "nobr",
-                                      "ol", "p", "pre", "ruby", "s", "small",
-                                      "span", "strong", "strike", "sub", "sup",
-                                      "table", "tt", "u", "ul", "var"])
-
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-        def adjustSVGTagNames(self, token):
-            replacements = {"altglyph": "altGlyph",
-                            "altglyphdef": "altGlyphDef",
-                            "altglyphitem": "altGlyphItem",
-                            "animatecolor": "animateColor",
-                            "animatemotion": "animateMotion",
-                            "animatetransform": "animateTransform",
-                            "clippath": "clipPath",
-                            "feblend": "feBlend",
-                            "fecolormatrix": "feColorMatrix",
-                            "fecomponenttransfer": "feComponentTransfer",
-                            "fecomposite": "feComposite",
-                            "feconvolvematrix": "feConvolveMatrix",
-                            "fediffuselighting": "feDiffuseLighting",
-                            "fedisplacementmap": "feDisplacementMap",
-                            "fedistantlight": "feDistantLight",
-                            "feflood": "feFlood",
-                            "fefunca": "feFuncA",
-                            "fefuncb": "feFuncB",
-                            "fefuncg": "feFuncG",
-                            "fefuncr": "feFuncR",
-                            "fegaussianblur": "feGaussianBlur",
-                            "feimage": "feImage",
-                            "femerge": "feMerge",
-                            "femergenode": "feMergeNode",
-                            "femorphology": "feMorphology",
-                            "feoffset": "feOffset",
-                            "fepointlight": "fePointLight",
-                            "fespecularlighting": "feSpecularLighting",
-                            "fespotlight": "feSpotLight",
-                            "fetile": "feTile",
-                            "feturbulence": "feTurbulence",
-                            "foreignobject": "foreignObject",
-                            "glyphref": "glyphRef",
-                            "lineargradient": "linearGradient",
-                            "radialgradient": "radialGradient",
-                            "textpath": "textPath"}
-
-            if token["name"] in replacements:
-                token["name"] = replacements[token["name"]]
-
-        def processCharacters(self, token):
-            if token["data"] == "\u0000":
-                token["data"] = "\uFFFD"
-            elif (self.parser.framesetOK and
-                  any(char not in spaceCharacters for char in token["data"])):
-                self.parser.framesetOK = False
-            Phase.processCharacters(self, token)
-
-        def processStartTag(self, token):
-            currentNode = self.tree.openElements[-1]
-            if (token["name"] in self.breakoutElements or
-                (token["name"] == "font" and
-                 set(token["data"].keys()) & set(["color", "face", "size"]))):
-                self.parser.parseError("unexpected-html-element-in-foreign-content",
-                                       {"name": token["name"]})
-                while (self.tree.openElements[-1].namespace !=
-                       self.tree.defaultNamespace and
-                       not self.parser.isHTMLIntegrationPoint(self.tree.openElements[-1]) and
-                       not self.parser.isMathMLTextIntegrationPoint(self.tree.openElements[-1])):
-                    self.tree.openElements.pop()
-                return token
-
-            else:
-                if currentNode.namespace == namespaces["mathml"]:
-                    self.parser.adjustMathMLAttributes(token)
-                elif currentNode.namespace == namespaces["svg"]:
-                    self.adjustSVGTagNames(token)
-                    self.parser.adjustSVGAttributes(token)
-                self.parser.adjustForeignAttributes(token)
-                token["namespace"] = currentNode.namespace
-                self.tree.insertElement(token)
-                if token["selfClosing"]:
-                    self.tree.openElements.pop()
-                    token["selfClosingAcknowledged"] = True
-
-        def processEndTag(self, token):
-            nodeIndex = len(self.tree.openElements) - 1
-            node = self.tree.openElements[-1]
-            if node.name.translate(asciiUpper2Lower) != token["name"]:
-                self.parser.parseError("unexpected-end-tag", {"name": token["name"]})
-
-            while True:
-                if node.name.translate(asciiUpper2Lower) == token["name"]:
-                    # XXX this isn't in the spec but it seems necessary
-                    if self.parser.phase == self.parser.phases["inTableText"]:
-                        self.parser.phase.flushCharacters()
-                        self.parser.phase = self.parser.phase.originalPhase
-                    while self.tree.openElements.pop() != node:
-                        assert self.tree.openElements
-                    new_token = None
-                    break
-                nodeIndex -= 1
-
-                node = self.tree.openElements[nodeIndex]
-                if node.namespace != self.tree.defaultNamespace:
-                    continue
-                else:
-                    new_token = self.parser.phase.processEndTag(token)
-                    break
-            return new_token
-
-    class AfterBodyPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([("html", self.endTagHtml)])
-            self.endTagHandler.default = self.endTagOther
-
-        def processEOF(self):
-            # Stop parsing
-            pass
-
-        def processComment(self, token):
-            # This is needed because data is to be appended to the <html> element
-            # here and not to whatever is currently open.
-            self.tree.insertComment(token, self.tree.openElements[0])
-
-        def processCharacters(self, token):
-            self.parser.parseError("unexpected-char-after-body")
-            self.parser.phase = self.parser.phases["inBody"]
-            return token
-
-        def startTagHtml(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagOther(self, token):
-            self.parser.parseError("unexpected-start-tag-after-body",
-                                   {"name": token["name"]})
-            self.parser.phase = self.parser.phases["inBody"]
-            return token
-
-        def endTagHtml(self, name):
-            if self.parser.innerHTML:
-                self.parser.parseError("unexpected-end-tag-after-body-innerhtml")
-            else:
-                self.parser.phase = self.parser.phases["afterAfterBody"]
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag-after-body",
-                                   {"name": token["name"]})
-            self.parser.phase = self.parser.phases["inBody"]
-            return token
-
-    class InFramesetPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#in-frameset
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("frameset", self.startTagFrameset),
-                ("frame", self.startTagFrame),
-                ("noframes", self.startTagNoframes)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("frameset", self.endTagFrameset)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def processEOF(self):
-            if self.tree.openElements[-1].name != "html":
-                self.parser.parseError("eof-in-frameset")
-            else:
-                assert self.parser.innerHTML
-
-        def processCharacters(self, token):
-            self.parser.parseError("unexpected-char-in-frameset")
-
-        def startTagFrameset(self, token):
-            self.tree.insertElement(token)
-
-        def startTagFrame(self, token):
-            self.tree.insertElement(token)
-            self.tree.openElements.pop()
-
-        def startTagNoframes(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagOther(self, token):
-            self.parser.parseError("unexpected-start-tag-in-frameset",
-                                   {"name": token["name"]})
-
-        def endTagFrameset(self, token):
-            if self.tree.openElements[-1].name == "html":
-                # innerHTML case
-                self.parser.parseError("unexpected-frameset-in-frameset-innerhtml")
-            else:
-                self.tree.openElements.pop()
-            if (not self.parser.innerHTML and
-                    self.tree.openElements[-1].name != "frameset"):
-                # If we're not in innerHTML mode and the current node is not a
-                # "frameset" element (anymore) then switch.
-                self.parser.phase = self.parser.phases["afterFrameset"]
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag-in-frameset",
-                                   {"name": token["name"]})
-
-    class AfterFramesetPhase(Phase):
-        # http://www.whatwg.org/specs/web-apps/current-work/#after3
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("noframes", self.startTagNoframes)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-            self.endTagHandler = _utils.MethodDispatcher([
-                ("html", self.endTagHtml)
-            ])
-            self.endTagHandler.default = self.endTagOther
-
-        def processEOF(self):
-            # Stop parsing
-            pass
-
-        def processCharacters(self, token):
-            self.parser.parseError("unexpected-char-after-frameset")
-
-        def startTagNoframes(self, token):
-            return self.parser.phases["inHead"].processStartTag(token)
-
-        def startTagOther(self, token):
-            self.parser.parseError("unexpected-start-tag-after-frameset",
-                                   {"name": token["name"]})
-
-        def endTagHtml(self, token):
-            self.parser.phase = self.parser.phases["afterAfterFrameset"]
-
-        def endTagOther(self, token):
-            self.parser.parseError("unexpected-end-tag-after-frameset",
-                                   {"name": token["name"]})
-
-    class AfterAfterBodyPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-        def processEOF(self):
-            pass
-
-        def processComment(self, token):
-            self.tree.insertComment(token, self.tree.document)
-
-        def processSpaceCharacters(self, token):
-            return self.parser.phases["inBody"].processSpaceCharacters(token)
-
-        def processCharacters(self, token):
-            self.parser.parseError("expected-eof-but-got-char")
-            self.parser.phase = self.parser.phases["inBody"]
-            return token
-
-        def startTagHtml(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagOther(self, token):
-            self.parser.parseError("expected-eof-but-got-start-tag",
-                                   {"name": token["name"]})
-            self.parser.phase = self.parser.phases["inBody"]
-            return token
-
-        def processEndTag(self, token):
-            self.parser.parseError("expected-eof-but-got-end-tag",
-                                   {"name": token["name"]})
-            self.parser.phase = self.parser.phases["inBody"]
-            return token
-
-    class AfterAfterFramesetPhase(Phase):
-        def __init__(self, parser, tree):
-            Phase.__init__(self, parser, tree)
-
-            self.startTagHandler = _utils.MethodDispatcher([
-                ("html", self.startTagHtml),
-                ("noframes", self.startTagNoFrames)
-            ])
-            self.startTagHandler.default = self.startTagOther
-
-        def processEOF(self):
-            pass
-
-        def processComment(self, token):
-            self.tree.insertComment(token, self.tree.document)
-
-        def processSpaceCharacters(self, token):
-            return self.parser.phases["inBody"].processSpaceCharacters(token)
-
-        def processCharacters(self, token):
-            self.parser.parseError("expected-eof-but-got-char")
-
-        def startTagHtml(self, token):
-            return self.parser.phases["inBody"].processStartTag(token)
-
-        def startTagNoFrames(self, token):
-            return self.parser.phases["inHead"].processStartTag(token)
-
-        def startTagOther(self, token):
-            self.parser.parseError("expected-eof-but-got-start-tag",
-                                   {"name": token["name"]})
-
-        def processEndTag(self, token):
-            self.parser.parseError("expected-eof-but-got-end-tag",
-                                   {"name": token["name"]})
-    # pylint:enable=unused-argument
-
-    return {
-        "initial": InitialPhase,
-        "beforeHtml": BeforeHtmlPhase,
-        "beforeHead": BeforeHeadPhase,
-        "inHead": InHeadPhase,
-        "inHeadNoscript": InHeadNoscriptPhase,
-        "afterHead": AfterHeadPhase,
-        "inBody": InBodyPhase,
-        "text": TextPhase,
-        "inTable": InTablePhase,
-        "inTableText": InTableTextPhase,
-        "inCaption": InCaptionPhase,
-        "inColumnGroup": InColumnGroupPhase,
-        "inTableBody": InTableBodyPhase,
-        "inRow": InRowPhase,
-        "inCell": InCellPhase,
-        "inSelect": InSelectPhase,
-        "inSelectInTable": InSelectInTablePhase,
-        "inForeignContent": InForeignContentPhase,
-        "afterBody": AfterBodyPhase,
-        "inFrameset": InFramesetPhase,
-        "afterFrameset": AfterFramesetPhase,
-        "afterAfterBody": AfterAfterBodyPhase,
-        "afterAfterFrameset": AfterAfterFramesetPhase,
-        # XXX after after frameset
-    }
-
-
-def adjust_attributes(token, replacements):
-    needs_adjustment = viewkeys(token['data']) & viewkeys(replacements)
-    if needs_adjustment:
-        token['data'] = OrderedDict((replacements.get(k, k), v)
-                                    for k, v in token['data'].items())
-
-
-def impliedTagToken(name, type="EndTag", attributes=None,
-                    selfClosing=False):
-    if attributes is None:
-        attributes = {}
-    return {"type": tokenTypes[type], "name": name, "data": attributes,
-            "selfClosing": selfClosing}
-
-
-class ParseError(Exception):
-    """Error in parsed document"""
-    pass
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/serializer.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/serializer.py
deleted file mode 100644
index 53f4d44..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/serializer.py
+++ /dev/null
@@ -1,409 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-from pip._vendor.six import text_type
-
-import re
-
-from codecs import register_error, xmlcharrefreplace_errors
-
-from .constants import voidElements, booleanAttributes, spaceCharacters
-from .constants import rcdataElements, entities, xmlEntities
-from . import treewalkers, _utils
-from xml.sax.saxutils import escape
-
-_quoteAttributeSpecChars = "".join(spaceCharacters) + "\"'=<>`"
-_quoteAttributeSpec = re.compile("[" + _quoteAttributeSpecChars + "]")
-_quoteAttributeLegacy = re.compile("[" + _quoteAttributeSpecChars +
-                                   "\x00\x01\x02\x03\x04\x05\x06\x07\x08\t\n"
-                                   "\x0b\x0c\r\x0e\x0f\x10\x11\x12\x13\x14\x15"
-                                   "\x16\x17\x18\x19\x1a\x1b\x1c\x1d\x1e\x1f"
-                                   "\x20\x2f\x60\xa0\u1680\u180e\u180f\u2000"
-                                   "\u2001\u2002\u2003\u2004\u2005\u2006\u2007"
-                                   "\u2008\u2009\u200a\u2028\u2029\u202f\u205f"
-                                   "\u3000]")
-
-
-_encode_entity_map = {}
-_is_ucs4 = len("\U0010FFFF") == 1
-for k, v in list(entities.items()):
-    # skip multi-character entities
-    if ((_is_ucs4 and len(v) > 1) or
-            (not _is_ucs4 and len(v) > 2)):
-        continue
-    if v != "&":
-        if len(v) == 2:
-            v = _utils.surrogatePairToCodepoint(v)
-        else:
-            v = ord(v)
-        if v not in _encode_entity_map or k.islower():
-            # prefer &lt; over &LT; and similarly for &amp;, &gt;, etc.
-            _encode_entity_map[v] = k
-
-
-def htmlentityreplace_errors(exc):
-    if isinstance(exc, (UnicodeEncodeError, UnicodeTranslateError)):
-        res = []
-        codepoints = []
-        skip = False
-        for i, c in enumerate(exc.object[exc.start:exc.end]):
-            if skip:
-                skip = False
-                continue
-            index = i + exc.start
-            if _utils.isSurrogatePair(exc.object[index:min([exc.end, index + 2])]):
-                codepoint = _utils.surrogatePairToCodepoint(exc.object[index:index + 2])
-                skip = True
-            else:
-                codepoint = ord(c)
-            codepoints.append(codepoint)
-        for cp in codepoints:
-            e = _encode_entity_map.get(cp)
-            if e:
-                res.append("&")
-                res.append(e)
-                if not e.endswith(";"):
-                    res.append(";")
-            else:
-                res.append("&#x%s;" % (hex(cp)[2:]))
-        return ("".join(res), exc.end)
-    else:
-        return xmlcharrefreplace_errors(exc)
-
-
-register_error("htmlentityreplace", htmlentityreplace_errors)
-
-
-def serialize(input, tree="etree", encoding=None, **serializer_opts):
-    """Serializes the input token stream using the specified treewalker
-
-    :arg input: the token stream to serialize
-
-    :arg tree: the treewalker to use
-
-    :arg encoding: the encoding to use
-
-    :arg serializer_opts: any options to pass to the
-        :py:class:`html5lib.serializer.HTMLSerializer` that gets created
-
-    :returns: the tree serialized as a string
-
-    Example:
-
-    >>> from html5lib.html5parser import parse
-    >>> from html5lib.serializer import serialize
-    >>> token_stream = parse('<html><body><p>Hi!</p></body></html>')
-    >>> serialize(token_stream, omit_optional_tags=False)
-    '<html><head></head><body><p>Hi!</p></body></html>'
-
-    """
-    # XXX: Should we cache this?
-    walker = treewalkers.getTreeWalker(tree)
-    s = HTMLSerializer(**serializer_opts)
-    return s.render(walker(input), encoding)
-
-
-class HTMLSerializer(object):
-
-    # attribute quoting options
-    quote_attr_values = "legacy"  # be secure by default
-    quote_char = '"'
-    use_best_quote_char = True
-
-    # tag syntax options
-    omit_optional_tags = True
-    minimize_boolean_attributes = True
-    use_trailing_solidus = False
-    space_before_trailing_solidus = True
-
-    # escaping options
-    escape_lt_in_attrs = False
-    escape_rcdata = False
-    resolve_entities = True
-
-    # miscellaneous options
-    alphabetical_attributes = False
-    inject_meta_charset = True
-    strip_whitespace = False
-    sanitize = False
-
-    options = ("quote_attr_values", "quote_char", "use_best_quote_char",
-               "omit_optional_tags", "minimize_boolean_attributes",
-               "use_trailing_solidus", "space_before_trailing_solidus",
-               "escape_lt_in_attrs", "escape_rcdata", "resolve_entities",
-               "alphabetical_attributes", "inject_meta_charset",
-               "strip_whitespace", "sanitize")
-
-    def __init__(self, **kwargs):
-        """Initialize HTMLSerializer
-
-        :arg inject_meta_charset: Whether or not to inject the meta charset.
-
-            Defaults to ``True``.
-
-        :arg quote_attr_values: Whether to quote attribute values that don't
-            require quoting per legacy browser behavior (``"legacy"``), when
-            required by the standard (``"spec"``), or always (``"always"``).
-
-            Defaults to ``"legacy"``.
-
-        :arg quote_char: Use given quote character for attribute quoting.
-
-            Defaults to ``"`` which will use double quotes unless attribute
-            value contains a double quote, in which case single quotes are
-            used.
-
-        :arg escape_lt_in_attrs: Whether or not to escape ``<`` in attribute
-            values.
-
-            Defaults to ``False``.
-
-        :arg escape_rcdata: Whether to escape characters that need to be
-            escaped within normal elements within rcdata elements such as
-            style.
-
-            Defaults to ``False``.
-
-        :arg resolve_entities: Whether to resolve named character entities that
-            appear in the source tree. The XML predefined entities &lt; &gt;
-            &amp; &quot; &apos; are unaffected by this setting.
-
-            Defaults to ``True``.
-
-        :arg strip_whitespace: Whether to remove semantically meaningless
-            whitespace. (This compresses all whitespace to a single space
-            except within ``pre``.)
-
-            Defaults to ``False``.
-
-        :arg minimize_boolean_attributes: Shortens boolean attributes to give
-            just the attribute value, for example::
-
-              <input disabled="disabled">
-
-            becomes::
-
-              <input disabled>
-
-            Defaults to ``True``.
-
-        :arg use_trailing_solidus: Includes a close-tag slash at the end of the
-            start tag of void elements (empty elements whose end tag is
-            forbidden). E.g. ``<hr/>``.
-
-            Defaults to ``False``.
-
-        :arg space_before_trailing_solidus: Places a space immediately before
-            the closing slash in a tag using a trailing solidus. E.g.
-            ``<hr />``. Requires ``use_trailing_solidus=True``.
-
-            Defaults to ``True``.
-
-        :arg sanitize: Strip all unsafe or unknown constructs from output.
-            See :py:class:`html5lib.filters.sanitizer.Filter`.
-
-            Defaults to ``False``.
-
-        :arg omit_optional_tags: Omit start/end tags that are optional.
-
-            Defaults to ``True``.
-
-        :arg alphabetical_attributes: Reorder attributes to be in alphabetical order.
-
-            Defaults to ``False``.
-
-        """
-        unexpected_args = frozenset(kwargs) - frozenset(self.options)
-        if len(unexpected_args) > 0:
-            raise TypeError("__init__() got an unexpected keyword argument '%s'" % next(iter(unexpected_args)))
-        if 'quote_char' in kwargs:
-            self.use_best_quote_char = False
-        for attr in self.options:
-            setattr(self, attr, kwargs.get(attr, getattr(self, attr)))
-        self.errors = []
-        self.strict = False
-
-    def encode(self, string):
-        assert(isinstance(string, text_type))
-        if self.encoding:
-            return string.encode(self.encoding, "htmlentityreplace")
-        else:
-            return string
-
-    def encodeStrict(self, string):
-        assert(isinstance(string, text_type))
-        if self.encoding:
-            return string.encode(self.encoding, "strict")
-        else:
-            return string
-
-    def serialize(self, treewalker, encoding=None):
-        # pylint:disable=too-many-nested-blocks
-        self.encoding = encoding
-        in_cdata = False
-        self.errors = []
-
-        if encoding and self.inject_meta_charset:
-            from .filters.inject_meta_charset import Filter
-            treewalker = Filter(treewalker, encoding)
-        # Alphabetical attributes is here under the assumption that none of
-        # the later filters add or change order of attributes; it needs to be
-        # before the sanitizer so escaped elements come out correctly
-        if self.alphabetical_attributes:
-            from .filters.alphabeticalattributes import Filter
-            treewalker = Filter(treewalker)
-        # WhitespaceFilter should be used before OptionalTagFilter
-        # for maximum efficiently of this latter filter
-        if self.strip_whitespace:
-            from .filters.whitespace import Filter
-            treewalker = Filter(treewalker)
-        if self.sanitize:
-            from .filters.sanitizer import Filter
-            treewalker = Filter(treewalker)
-        if self.omit_optional_tags:
-            from .filters.optionaltags import Filter
-            treewalker = Filter(treewalker)
-
-        for token in treewalker:
-            type = token["type"]
-            if type == "Doctype":
-                doctype = "<!DOCTYPE %s" % token["name"]
-
-                if token["publicId"]:
-                    doctype += ' PUBLIC "%s"' % token["publicId"]
-                elif token["systemId"]:
-                    doctype += " SYSTEM"
-                if token["systemId"]:
-                    if token["systemId"].find('"') >= 0:
-                        if token["systemId"].find("'") >= 0:
-                            self.serializeError("System identifer contains both single and double quote characters")
-                        quote_char = "'"
-                    else:
-                        quote_char = '"'
-                    doctype += " %s%s%s" % (quote_char, token["systemId"], quote_char)
-
-                doctype += ">"
-                yield self.encodeStrict(doctype)
-
-            elif type in ("Characters", "SpaceCharacters"):
-                if type == "SpaceCharacters" or in_cdata:
-                    if in_cdata and token["data"].find("</") >= 0:
-                        self.serializeError("Unexpected </ in CDATA")
-                    yield self.encode(token["data"])
-                else:
-                    yield self.encode(escape(token["data"]))
-
-            elif type in ("StartTag", "EmptyTag"):
-                name = token["name"]
-                yield self.encodeStrict("<%s" % name)
-                if name in rcdataElements and not self.escape_rcdata:
-                    in_cdata = True
-                elif in_cdata:
-                    self.serializeError("Unexpected child element of a CDATA element")
-                for (_, attr_name), attr_value in token["data"].items():
-                    # TODO: Add namespace support here
-                    k = attr_name
-                    v = attr_value
-                    yield self.encodeStrict(' ')
-
-                    yield self.encodeStrict(k)
-                    if not self.minimize_boolean_attributes or \
-                        (k not in booleanAttributes.get(name, tuple()) and
-                         k not in booleanAttributes.get("", tuple())):
-                        yield self.encodeStrict("=")
-                        if self.quote_attr_values == "always" or len(v) == 0:
-                            quote_attr = True
-                        elif self.quote_attr_values == "spec":
-                            quote_attr = _quoteAttributeSpec.search(v) is not None
-                        elif self.quote_attr_values == "legacy":
-                            quote_attr = _quoteAttributeLegacy.search(v) is not None
-                        else:
-                            raise ValueError("quote_attr_values must be one of: "
-                                             "'always', 'spec', or 'legacy'")
-                        v = v.replace("&", "&amp;")
-                        if self.escape_lt_in_attrs:
-                            v = v.replace("<", "&lt;")
-                        if quote_attr:
-                            quote_char = self.quote_char
-                            if self.use_best_quote_char:
-                                if "'" in v and '"' not in v:
-                                    quote_char = '"'
-                                elif '"' in v and "'" not in v:
-                                    quote_char = "'"
-                            if quote_char == "'":
-                                v = v.replace("'", "&#39;")
-                            else:
-                                v = v.replace('"', "&quot;")
-                            yield self.encodeStrict(quote_char)
-                            yield self.encode(v)
-                            yield self.encodeStrict(quote_char)
-                        else:
-                            yield self.encode(v)
-                if name in voidElements and self.use_trailing_solidus:
-                    if self.space_before_trailing_solidus:
-                        yield self.encodeStrict(" /")
-                    else:
-                        yield self.encodeStrict("/")
-                yield self.encode(">")
-
-            elif type == "EndTag":
-                name = token["name"]
-                if name in rcdataElements:
-                    in_cdata = False
-                elif in_cdata:
-                    self.serializeError("Unexpected child element of a CDATA element")
-                yield self.encodeStrict("</%s>" % name)
-
-            elif type == "Comment":
-                data = token["data"]
-                if data.find("--") >= 0:
-                    self.serializeError("Comment contains --")
-                yield self.encodeStrict("<!--%s-->" % token["data"])
-
-            elif type == "Entity":
-                name = token["name"]
-                key = name + ";"
-                if key not in entities:
-                    self.serializeError("Entity %s not recognized" % name)
-                if self.resolve_entities and key not in xmlEntities:
-                    data = entities[key]
-                else:
-                    data = "&%s;" % name
-                yield self.encodeStrict(data)
-
-            else:
-                self.serializeError(token["data"])
-
-    def render(self, treewalker, encoding=None):
-        """Serializes the stream from the treewalker into a string
-
-        :arg treewalker: the treewalker to serialize
-
-        :arg encoding: the string encoding to use
-
-        :returns: the serialized tree
-
-        Example:
-
-        >>> from html5lib import parse, getTreeWalker
-        >>> from html5lib.serializer import HTMLSerializer
-        >>> token_stream = parse('<html><body>Hi!</body></html>')
-        >>> walker = getTreeWalker('etree')
-        >>> serializer = HTMLSerializer(omit_optional_tags=False)
-        >>> serializer.render(walker(token_stream))
-        '<html><head></head><body>Hi!</body></html>'
-
-        """
-        if encoding:
-            return b"".join(list(self.serialize(treewalker, encoding)))
-        else:
-            return "".join(list(self.serialize(treewalker)))
-
-    def serializeError(self, data="XXX ERROR MESSAGE NEEDED"):
-        # XXX The idea is to make data mandatory.
-        self.errors.append(data)
-        if self.strict:
-            raise SerializeError
-
-
-class SerializeError(Exception):
-    """Error in serialized tree"""
-    pass
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/__init__.py
deleted file mode 100644
index 7ef5959..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/__init__.py
+++ /dev/null
@@ -1,30 +0,0 @@
-"""Tree adapters let you convert from one tree structure to another
-
-Example:
-
-.. code-block:: python
-
-   from pip._vendor import html5lib
-   from pip._vendor.html5lib.treeadapters import genshi
-
-   doc = '<html><body>Hi!</body></html>'
-   treebuilder = html5lib.getTreeBuilder('etree')
-   parser = html5lib.HTMLParser(tree=treebuilder)
-   tree = parser.parse(doc)
-   TreeWalker = html5lib.getTreeWalker('etree')
-
-   genshi_tree = genshi.to_genshi(TreeWalker(tree))
-
-"""
-from __future__ import absolute_import, division, unicode_literals
-
-from . import sax
-
-__all__ = ["sax"]
-
-try:
-    from . import genshi  # noqa
-except ImportError:
-    pass
-else:
-    __all__.append("genshi")
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/genshi.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/genshi.py
deleted file mode 100644
index 61d5fb6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/genshi.py
+++ /dev/null
@@ -1,54 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from genshi.core import QName, Attrs
-from genshi.core import START, END, TEXT, COMMENT, DOCTYPE
-
-
-def to_genshi(walker):
-    """Convert a tree to a genshi tree
-
-    :arg walker: the treewalker to use to walk the tree to convert it
-
-    :returns: generator of genshi nodes
-
-    """
-    text = []
-    for token in walker:
-        type = token["type"]
-        if type in ("Characters", "SpaceCharacters"):
-            text.append(token["data"])
-        elif text:
-            yield TEXT, "".join(text), (None, -1, -1)
-            text = []
-
-        if type in ("StartTag", "EmptyTag"):
-            if token["namespace"]:
-                name = "{%s}%s" % (token["namespace"], token["name"])
-            else:
-                name = token["name"]
-            attrs = Attrs([(QName("{%s}%s" % attr if attr[0] is not None else attr[1]), value)
-                           for attr, value in token["data"].items()])
-            yield (START, (QName(name), attrs), (None, -1, -1))
-            if type == "EmptyTag":
-                type = "EndTag"
-
-        if type == "EndTag":
-            if token["namespace"]:
-                name = "{%s}%s" % (token["namespace"], token["name"])
-            else:
-                name = token["name"]
-
-            yield END, QName(name), (None, -1, -1)
-
-        elif type == "Comment":
-            yield COMMENT, token["data"], (None, -1, -1)
-
-        elif type == "Doctype":
-            yield DOCTYPE, (token["name"], token["publicId"],
-                            token["systemId"]), (None, -1, -1)
-
-        else:
-            pass  # FIXME: What to do?
-
-    if text:
-        yield TEXT, "".join(text), (None, -1, -1)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/sax.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/sax.py
deleted file mode 100644
index f4ccea5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treeadapters/sax.py
+++ /dev/null
@@ -1,50 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from xml.sax.xmlreader import AttributesNSImpl
-
-from ..constants import adjustForeignAttributes, unadjustForeignAttributes
-
-prefix_mapping = {}
-for prefix, localName, namespace in adjustForeignAttributes.values():
-    if prefix is not None:
-        prefix_mapping[prefix] = namespace
-
-
-def to_sax(walker, handler):
-    """Call SAX-like content handler based on treewalker walker
-
-    :arg walker: the treewalker to use to walk the tree to convert it
-
-    :arg handler: SAX handler to use
-
-    """
-    handler.startDocument()
-    for prefix, namespace in prefix_mapping.items():
-        handler.startPrefixMapping(prefix, namespace)
-
-    for token in walker:
-        type = token["type"]
-        if type == "Doctype":
-            continue
-        elif type in ("StartTag", "EmptyTag"):
-            attrs = AttributesNSImpl(token["data"],
-                                     unadjustForeignAttributes)
-            handler.startElementNS((token["namespace"], token["name"]),
-                                   token["name"],
-                                   attrs)
-            if type == "EmptyTag":
-                handler.endElementNS((token["namespace"], token["name"]),
-                                     token["name"])
-        elif type == "EndTag":
-            handler.endElementNS((token["namespace"], token["name"]),
-                                 token["name"])
-        elif type in ("Characters", "SpaceCharacters"):
-            handler.characters(token["data"])
-        elif type == "Comment":
-            pass
-        else:
-            assert False, "Unknown token type"
-
-    for prefix, namespace in prefix_mapping.items():
-        handler.endPrefixMapping(prefix)
-    handler.endDocument()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__init__.py
deleted file mode 100644
index d44447e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__init__.py
+++ /dev/null
@@ -1,88 +0,0 @@
-"""A collection of modules for building different kinds of trees from HTML
-documents.
-
-To create a treebuilder for a new type of tree, you need to do
-implement several things:
-
-1. A set of classes for various types of elements: Document, Doctype, Comment,
-   Element. These must implement the interface of ``base.treebuilders.Node``
-   (although comment nodes have a different signature for their constructor,
-   see ``treebuilders.etree.Comment``) Textual content may also be implemented
-   as another node type, or not, as your tree implementation requires.
-
-2. A treebuilder object (called ``TreeBuilder`` by convention) that inherits
-   from ``treebuilders.base.TreeBuilder``. This has 4 required attributes:
-
-   * ``documentClass`` - the class to use for the bottommost node of a document
-   * ``elementClass`` - the class to use for HTML Elements
-   * ``commentClass`` - the class to use for comments
-   * ``doctypeClass`` - the class to use for doctypes
-
-   It also has one required method:
-
-   * ``getDocument`` - Returns the root node of the complete document tree
-
-3. If you wish to run the unit tests, you must also create a ``testSerializer``
-   method on your treebuilder which accepts a node and returns a string
-   containing Node and its children serialized according to the format used in
-   the unittests
-
-"""
-
-from __future__ import absolute_import, division, unicode_literals
-
-from .._utils import default_etree
-
-treeBuilderCache = {}
-
-
-def getTreeBuilder(treeType, implementation=None, **kwargs):
-    """Get a TreeBuilder class for various types of trees with built-in support
-
-    :arg treeType: the name of the tree type required (case-insensitive). Supported
-        values are:
-
-        * "dom" - A generic builder for DOM implementations, defaulting to a
-          xml.dom.minidom based implementation.
-        * "etree" - A generic builder for tree implementations exposing an
-          ElementTree-like interface, defaulting to xml.etree.cElementTree if
-          available and xml.etree.ElementTree if not.
-        * "lxml" - A etree-based builder for lxml.etree, handling limitations
-          of lxml's implementation.
-
-    :arg implementation: (Currently applies to the "etree" and "dom" tree
-        types). A module implementing the tree type e.g. xml.etree.ElementTree
-        or xml.etree.cElementTree.
-
-    :arg kwargs: Any additional options to pass to the TreeBuilder when
-        creating it.
-
-    Example:
-
-    >>> from html5lib.treebuilders import getTreeBuilder
-    >>> builder = getTreeBuilder('etree')
-
-    """
-
-    treeType = treeType.lower()
-    if treeType not in treeBuilderCache:
-        if treeType == "dom":
-            from . import dom
-            # Come up with a sane default (pref. from the stdlib)
-            if implementation is None:
-                from xml.dom import minidom
-                implementation = minidom
-            # NEVER cache here, caching is done in the dom submodule
-            return dom.getDomModule(implementation, **kwargs).TreeBuilder
-        elif treeType == "lxml":
-            from . import etree_lxml
-            treeBuilderCache[treeType] = etree_lxml.TreeBuilder
-        elif treeType == "etree":
-            from . import etree
-            if implementation is None:
-                implementation = default_etree
-            # NEVER cache here, caching is done in the etree submodule
-            return etree.getETreeModule(implementation, **kwargs).TreeBuilder
-        else:
-            raise ValueError("""Unrecognised treebuilder "%s" """ % treeType)
-    return treeBuilderCache.get(treeType)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index dad249d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/base.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/base.cpython-37.pyc
deleted file mode 100644
index 6262068..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/base.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/etree.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/etree.cpython-37.pyc
deleted file mode 100644
index 160968d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/__pycache__/etree.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/base.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/base.py
deleted file mode 100644
index 73973db..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/base.py
+++ /dev/null
@@ -1,417 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-from pip._vendor.six import text_type
-
-from ..constants import scopingElements, tableInsertModeElements, namespaces
-
-# The scope markers are inserted when entering object elements,
-# marquees, table cells, and table captions, and are used to prevent formatting
-# from "leaking" into tables, object elements, and marquees.
-Marker = None
-
-listElementsMap = {
-    None: (frozenset(scopingElements), False),
-    "button": (frozenset(scopingElements | set([(namespaces["html"], "button")])), False),
-    "list": (frozenset(scopingElements | set([(namespaces["html"], "ol"),
-                                              (namespaces["html"], "ul")])), False),
-    "table": (frozenset([(namespaces["html"], "html"),
-                         (namespaces["html"], "table")]), False),
-    "select": (frozenset([(namespaces["html"], "optgroup"),
-                          (namespaces["html"], "option")]), True)
-}
-
-
-class Node(object):
-    """Represents an item in the tree"""
-    def __init__(self, name):
-        """Creates a Node
-
-        :arg name: The tag name associated with the node
-
-        """
-        # The tag name assocaited with the node
-        self.name = name
-        # The parent of the current node (or None for the document node)
-        self.parent = None
-        # The value of the current node (applies to text nodes and comments)
-        self.value = None
-        # A dict holding name -> value pairs for attributes of the node
-        self.attributes = {}
-        # A list of child nodes of the current node. This must include all
-        # elements but not necessarily other node types.
-        self.childNodes = []
-        # A list of miscellaneous flags that can be set on the node.
-        self._flags = []
-
-    def __str__(self):
-        attributesStr = " ".join(["%s=\"%s\"" % (name, value)
-                                  for name, value in
-                                  self.attributes.items()])
-        if attributesStr:
-            return "<%s %s>" % (self.name, attributesStr)
-        else:
-            return "<%s>" % (self.name)
-
-    def __repr__(self):
-        return "<%s>" % (self.name)
-
-    def appendChild(self, node):
-        """Insert node as a child of the current node
-
-        :arg node: the node to insert
-
-        """
-        raise NotImplementedError
-
-    def insertText(self, data, insertBefore=None):
-        """Insert data as text in the current node, positioned before the
-        start of node insertBefore or to the end of the node's text.
-
-        :arg data: the data to insert
-
-        :arg insertBefore: True if you want to insert the text before the node
-            and False if you want to insert it after the node
-
-        """
-        raise NotImplementedError
-
-    def insertBefore(self, node, refNode):
-        """Insert node as a child of the current node, before refNode in the
-        list of child nodes. Raises ValueError if refNode is not a child of
-        the current node
-
-        :arg node: the node to insert
-
-        :arg refNode: the child node to insert the node before
-
-        """
-        raise NotImplementedError
-
-    def removeChild(self, node):
-        """Remove node from the children of the current node
-
-        :arg node: the child node to remove
-
-        """
-        raise NotImplementedError
-
-    def reparentChildren(self, newParent):
-        """Move all the children of the current node to newParent.
-        This is needed so that trees that don't store text as nodes move the
-        text in the correct way
-
-        :arg newParent: the node to move all this node's children to
-
-        """
-        # XXX - should this method be made more general?
-        for child in self.childNodes:
-            newParent.appendChild(child)
-        self.childNodes = []
-
-    def cloneNode(self):
-        """Return a shallow copy of the current node i.e. a node with the same
-        name and attributes but with no parent or child nodes
-        """
-        raise NotImplementedError
-
-    def hasContent(self):
-        """Return true if the node has children or text, false otherwise
-        """
-        raise NotImplementedError
-
-
-class ActiveFormattingElements(list):
-    def append(self, node):
-        equalCount = 0
-        if node != Marker:
-            for element in self[::-1]:
-                if element == Marker:
-                    break
-                if self.nodesEqual(element, node):
-                    equalCount += 1
-                if equalCount == 3:
-                    self.remove(element)
-                    break
-        list.append(self, node)
-
-    def nodesEqual(self, node1, node2):
-        if not node1.nameTuple == node2.nameTuple:
-            return False
-
-        if not node1.attributes == node2.attributes:
-            return False
-
-        return True
-
-
-class TreeBuilder(object):
-    """Base treebuilder implementation
-
-    * documentClass - the class to use for the bottommost node of a document
-    * elementClass - the class to use for HTML Elements
-    * commentClass - the class to use for comments
-    * doctypeClass - the class to use for doctypes
-
-    """
-    # pylint:disable=not-callable
-
-    # Document class
-    documentClass = None
-
-    # The class to use for creating a node
-    elementClass = None
-
-    # The class to use for creating comments
-    commentClass = None
-
-    # The class to use for creating doctypes
-    doctypeClass = None
-
-    # Fragment class
-    fragmentClass = None
-
-    def __init__(self, namespaceHTMLElements):
-        """Create a TreeBuilder
-
-        :arg namespaceHTMLElements: whether or not to namespace HTML elements
-
-        """
-        if namespaceHTMLElements:
-            self.defaultNamespace = "http://www.w3.org/1999/xhtml"
-        else:
-            self.defaultNamespace = None
-        self.reset()
-
-    def reset(self):
-        self.openElements = []
-        self.activeFormattingElements = ActiveFormattingElements()
-
-        # XXX - rename these to headElement, formElement
-        self.headPointer = None
-        self.formPointer = None
-
-        self.insertFromTable = False
-
-        self.document = self.documentClass()
-
-    def elementInScope(self, target, variant=None):
-
-        # If we pass a node in we match that. if we pass a string
-        # match any node with that name
-        exactNode = hasattr(target, "nameTuple")
-        if not exactNode:
-            if isinstance(target, text_type):
-                target = (namespaces["html"], target)
-            assert isinstance(target, tuple)
-
-        listElements, invert = listElementsMap[variant]
-
-        for node in reversed(self.openElements):
-            if exactNode and node == target:
-                return True
-            elif not exactNode and node.nameTuple == target:
-                return True
-            elif (invert ^ (node.nameTuple in listElements)):
-                return False
-
-        assert False  # We should never reach this point
-
-    def reconstructActiveFormattingElements(self):
-        # Within this algorithm the order of steps described in the
-        # specification is not quite the same as the order of steps in the
-        # code. It should still do the same though.
-
-        # Step 1: stop the algorithm when there's nothing to do.
-        if not self.activeFormattingElements:
-            return
-
-        # Step 2 and step 3: we start with the last element. So i is -1.
-        i = len(self.activeFormattingElements) - 1
-        entry = self.activeFormattingElements[i]
-        if entry == Marker or entry in self.openElements:
-            return
-
-        # Step 6
-        while entry != Marker and entry not in self.openElements:
-            if i == 0:
-                # This will be reset to 0 below
-                i = -1
-                break
-            i -= 1
-            # Step 5: let entry be one earlier in the list.
-            entry = self.activeFormattingElements[i]
-
-        while True:
-            # Step 7
-            i += 1
-
-            # Step 8
-            entry = self.activeFormattingElements[i]
-            clone = entry.cloneNode()  # Mainly to get a new copy of the attributes
-
-            # Step 9
-            element = self.insertElement({"type": "StartTag",
-                                          "name": clone.name,
-                                          "namespace": clone.namespace,
-                                          "data": clone.attributes})
-
-            # Step 10
-            self.activeFormattingElements[i] = element
-
-            # Step 11
-            if element == self.activeFormattingElements[-1]:
-                break
-
-    def clearActiveFormattingElements(self):
-        entry = self.activeFormattingElements.pop()
-        while self.activeFormattingElements and entry != Marker:
-            entry = self.activeFormattingElements.pop()
-
-    def elementInActiveFormattingElements(self, name):
-        """Check if an element exists between the end of the active
-        formatting elements and the last marker. If it does, return it, else
-        return false"""
-
-        for item in self.activeFormattingElements[::-1]:
-            # Check for Marker first because if it's a Marker it doesn't have a
-            # name attribute.
-            if item == Marker:
-                break
-            elif item.name == name:
-                return item
-        return False
-
-    def insertRoot(self, token):
-        element = self.createElement(token)
-        self.openElements.append(element)
-        self.document.appendChild(element)
-
-    def insertDoctype(self, token):
-        name = token["name"]
-        publicId = token["publicId"]
-        systemId = token["systemId"]
-
-        doctype = self.doctypeClass(name, publicId, systemId)
-        self.document.appendChild(doctype)
-
-    def insertComment(self, token, parent=None):
-        if parent is None:
-            parent = self.openElements[-1]
-        parent.appendChild(self.commentClass(token["data"]))
-
-    def createElement(self, token):
-        """Create an element but don't insert it anywhere"""
-        name = token["name"]
-        namespace = token.get("namespace", self.defaultNamespace)
-        element = self.elementClass(name, namespace)
-        element.attributes = token["data"]
-        return element
-
-    def _getInsertFromTable(self):
-        return self._insertFromTable
-
-    def _setInsertFromTable(self, value):
-        """Switch the function used to insert an element from the
-        normal one to the misnested table one and back again"""
-        self._insertFromTable = value
-        if value:
-            self.insertElement = self.insertElementTable
-        else:
-            self.insertElement = self.insertElementNormal
-
-    insertFromTable = property(_getInsertFromTable, _setInsertFromTable)
-
-    def insertElementNormal(self, token):
-        name = token["name"]
-        assert isinstance(name, text_type), "Element %s not unicode" % name
-        namespace = token.get("namespace", self.defaultNamespace)
-        element = self.elementClass(name, namespace)
-        element.attributes = token["data"]
-        self.openElements[-1].appendChild(element)
-        self.openElements.append(element)
-        return element
-
-    def insertElementTable(self, token):
-        """Create an element and insert it into the tree"""
-        element = self.createElement(token)
-        if self.openElements[-1].name not in tableInsertModeElements:
-            return self.insertElementNormal(token)
-        else:
-            # We should be in the InTable mode. This means we want to do
-            # special magic element rearranging
-            parent, insertBefore = self.getTableMisnestedNodePosition()
-            if insertBefore is None:
-                parent.appendChild(element)
-            else:
-                parent.insertBefore(element, insertBefore)
-            self.openElements.append(element)
-        return element
-
-    def insertText(self, data, parent=None):
-        """Insert text data."""
-        if parent is None:
-            parent = self.openElements[-1]
-
-        if (not self.insertFromTable or (self.insertFromTable and
-                                         self.openElements[-1].name
-                                         not in tableInsertModeElements)):
-            parent.insertText(data)
-        else:
-            # We should be in the InTable mode. This means we want to do
-            # special magic element rearranging
-            parent, insertBefore = self.getTableMisnestedNodePosition()
-            parent.insertText(data, insertBefore)
-
-    def getTableMisnestedNodePosition(self):
-        """Get the foster parent element, and sibling to insert before
-        (or None) when inserting a misnested table node"""
-        # The foster parent element is the one which comes before the most
-        # recently opened table element
-        # XXX - this is really inelegant
-        lastTable = None
-        fosterParent = None
-        insertBefore = None
-        for elm in self.openElements[::-1]:
-            if elm.name == "table":
-                lastTable = elm
-                break
-        if lastTable:
-            # XXX - we should really check that this parent is actually a
-            # node here
-            if lastTable.parent:
-                fosterParent = lastTable.parent
-                insertBefore = lastTable
-            else:
-                fosterParent = self.openElements[
-                    self.openElements.index(lastTable) - 1]
-        else:
-            fosterParent = self.openElements[0]
-        return fosterParent, insertBefore
-
-    def generateImpliedEndTags(self, exclude=None):
-        name = self.openElements[-1].name
-        # XXX td, th and tr are not actually needed
-        if (name in frozenset(("dd", "dt", "li", "option", "optgroup", "p", "rp", "rt")) and
-                name != exclude):
-            self.openElements.pop()
-            # XXX This is not entirely what the specification says. We should
-            # investigate it more closely.
-            self.generateImpliedEndTags(exclude)
-
-    def getDocument(self):
-        """Return the final tree"""
-        return self.document
-
-    def getFragment(self):
-        """Return the final fragment"""
-        # assert self.innerHTML
-        fragment = self.fragmentClass()
-        self.openElements[0].reparentChildren(fragment)
-        return fragment
-
-    def testSerializer(self, node):
-        """Serialize the subtree of node in the format required by unit tests
-
-        :arg node: the node from which to start serializing
-
-        """
-        raise NotImplementedError
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/dom.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/dom.py
deleted file mode 100644
index dcfac22..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/dom.py
+++ /dev/null
@@ -1,236 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-
-from collections import MutableMapping
-from xml.dom import minidom, Node
-import weakref
-
-from . import base
-from .. import constants
-from ..constants import namespaces
-from .._utils import moduleFactoryFactory
-
-
-def getDomBuilder(DomImplementation):
-    Dom = DomImplementation
-
-    class AttrList(MutableMapping):
-        def __init__(self, element):
-            self.element = element
-
-        def __iter__(self):
-            return iter(self.element.attributes.keys())
-
-        def __setitem__(self, name, value):
-            if isinstance(name, tuple):
-                raise NotImplementedError
-            else:
-                attr = self.element.ownerDocument.createAttribute(name)
-                attr.value = value
-                self.element.attributes[name] = attr
-
-        def __len__(self):
-            return len(self.element.attributes)
-
-        def items(self):
-            return list(self.element.attributes.items())
-
-        def values(self):
-            return list(self.element.attributes.values())
-
-        def __getitem__(self, name):
-            if isinstance(name, tuple):
-                raise NotImplementedError
-            else:
-                return self.element.attributes[name].value
-
-        def __delitem__(self, name):
-            if isinstance(name, tuple):
-                raise NotImplementedError
-            else:
-                del self.element.attributes[name]
-
-    class NodeBuilder(base.Node):
-        def __init__(self, element):
-            base.Node.__init__(self, element.nodeName)
-            self.element = element
-
-        namespace = property(lambda self: hasattr(self.element, "namespaceURI") and
-                             self.element.namespaceURI or None)
-
-        def appendChild(self, node):
-            node.parent = self
-            self.element.appendChild(node.element)
-
-        def insertText(self, data, insertBefore=None):
-            text = self.element.ownerDocument.createTextNode(data)
-            if insertBefore:
-                self.element.insertBefore(text, insertBefore.element)
-            else:
-                self.element.appendChild(text)
-
-        def insertBefore(self, node, refNode):
-            self.element.insertBefore(node.element, refNode.element)
-            node.parent = self
-
-        def removeChild(self, node):
-            if node.element.parentNode == self.element:
-                self.element.removeChild(node.element)
-            node.parent = None
-
-        def reparentChildren(self, newParent):
-            while self.element.hasChildNodes():
-                child = self.element.firstChild
-                self.element.removeChild(child)
-                newParent.element.appendChild(child)
-            self.childNodes = []
-
-        def getAttributes(self):
-            return AttrList(self.element)
-
-        def setAttributes(self, attributes):
-            if attributes:
-                for name, value in list(attributes.items()):
-                    if isinstance(name, tuple):
-                        if name[0] is not None:
-                            qualifiedName = (name[0] + ":" + name[1])
-                        else:
-                            qualifiedName = name[1]
-                        self.element.setAttributeNS(name[2], qualifiedName,
-                                                    value)
-                    else:
-                        self.element.setAttribute(
-                            name, value)
-        attributes = property(getAttributes, setAttributes)
-
-        def cloneNode(self):
-            return NodeBuilder(self.element.cloneNode(False))
-
-        def hasContent(self):
-            return self.element.hasChildNodes()
-
-        def getNameTuple(self):
-            if self.namespace is None:
-                return namespaces["html"], self.name
-            else:
-                return self.namespace, self.name
-
-        nameTuple = property(getNameTuple)
-
-    class TreeBuilder(base.TreeBuilder):  # pylint:disable=unused-variable
-        def documentClass(self):
-            self.dom = Dom.getDOMImplementation().createDocument(None, None, None)
-            return weakref.proxy(self)
-
-        def insertDoctype(self, token):
-            name = token["name"]
-            publicId = token["publicId"]
-            systemId = token["systemId"]
-
-            domimpl = Dom.getDOMImplementation()
-            doctype = domimpl.createDocumentType(name, publicId, systemId)
-            self.document.appendChild(NodeBuilder(doctype))
-            if Dom == minidom:
-                doctype.ownerDocument = self.dom
-
-        def elementClass(self, name, namespace=None):
-            if namespace is None and self.defaultNamespace is None:
-                node = self.dom.createElement(name)
-            else:
-                node = self.dom.createElementNS(namespace, name)
-
-            return NodeBuilder(node)
-
-        def commentClass(self, data):
-            return NodeBuilder(self.dom.createComment(data))
-
-        def fragmentClass(self):
-            return NodeBuilder(self.dom.createDocumentFragment())
-
-        def appendChild(self, node):
-            self.dom.appendChild(node.element)
-
-        def testSerializer(self, element):
-            return testSerializer(element)
-
-        def getDocument(self):
-            return self.dom
-
-        def getFragment(self):
-            return base.TreeBuilder.getFragment(self).element
-
-        def insertText(self, data, parent=None):
-            data = data
-            if parent != self:
-                base.TreeBuilder.insertText(self, data, parent)
-            else:
-                # HACK: allow text nodes as children of the document node
-                if hasattr(self.dom, '_child_node_types'):
-                    # pylint:disable=protected-access
-                    if Node.TEXT_NODE not in self.dom._child_node_types:
-                        self.dom._child_node_types = list(self.dom._child_node_types)
-                        self.dom._child_node_types.append(Node.TEXT_NODE)
-                self.dom.appendChild(self.dom.createTextNode(data))
-
-        implementation = DomImplementation
-        name = None
-
-    def testSerializer(element):
-        element.normalize()
-        rv = []
-
-        def serializeElement(element, indent=0):
-            if element.nodeType == Node.DOCUMENT_TYPE_NODE:
-                if element.name:
-                    if element.publicId or element.systemId:
-                        publicId = element.publicId or ""
-                        systemId = element.systemId or ""
-                        rv.append("""|%s<!DOCTYPE %s "%s" "%s">""" %
-                                  (' ' * indent, element.name, publicId, systemId))
-                    else:
-                        rv.append("|%s<!DOCTYPE %s>" % (' ' * indent, element.name))
-                else:
-                    rv.append("|%s<!DOCTYPE >" % (' ' * indent,))
-            elif element.nodeType == Node.DOCUMENT_NODE:
-                rv.append("#document")
-            elif element.nodeType == Node.DOCUMENT_FRAGMENT_NODE:
-                rv.append("#document-fragment")
-            elif element.nodeType == Node.COMMENT_NODE:
-                rv.append("|%s<!-- %s -->" % (' ' * indent, element.nodeValue))
-            elif element.nodeType == Node.TEXT_NODE:
-                rv.append("|%s\"%s\"" % (' ' * indent, element.nodeValue))
-            else:
-                if (hasattr(element, "namespaceURI") and
-                        element.namespaceURI is not None):
-                    name = "%s %s" % (constants.prefixes[element.namespaceURI],
-                                      element.nodeName)
-                else:
-                    name = element.nodeName
-                rv.append("|%s<%s>" % (' ' * indent, name))
-                if element.hasAttributes():
-                    attributes = []
-                    for i in range(len(element.attributes)):
-                        attr = element.attributes.item(i)
-                        name = attr.nodeName
-                        value = attr.value
-                        ns = attr.namespaceURI
-                        if ns:
-                            name = "%s %s" % (constants.prefixes[ns], attr.localName)
-                        else:
-                            name = attr.nodeName
-                        attributes.append((name, value))
-
-                    for name, value in sorted(attributes):
-                        rv.append('|%s%s="%s"' % (' ' * (indent + 2), name, value))
-            indent += 2
-            for child in element.childNodes:
-                serializeElement(child, indent)
-        serializeElement(element, 0)
-
-        return "\n".join(rv)
-
-    return locals()
-
-
-# The actual means to get a module!
-getDomModule = moduleFactoryFactory(getDomBuilder)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/etree.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/etree.py
deleted file mode 100644
index 0dedf44..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/etree.py
+++ /dev/null
@@ -1,340 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-# pylint:disable=protected-access
-
-from pip._vendor.six import text_type
-
-import re
-
-from . import base
-from .. import _ihatexml
-from .. import constants
-from ..constants import namespaces
-from .._utils import moduleFactoryFactory
-
-tag_regexp = re.compile("{([^}]*)}(.*)")
-
-
-def getETreeBuilder(ElementTreeImplementation, fullTree=False):
-    ElementTree = ElementTreeImplementation
-    ElementTreeCommentType = ElementTree.Comment("asd").tag
-
-    class Element(base.Node):
-        def __init__(self, name, namespace=None):
-            self._name = name
-            self._namespace = namespace
-            self._element = ElementTree.Element(self._getETreeTag(name,
-                                                                  namespace))
-            if namespace is None:
-                self.nameTuple = namespaces["html"], self._name
-            else:
-                self.nameTuple = self._namespace, self._name
-            self.parent = None
-            self._childNodes = []
-            self._flags = []
-
-        def _getETreeTag(self, name, namespace):
-            if namespace is None:
-                etree_tag = name
-            else:
-                etree_tag = "{%s}%s" % (namespace, name)
-            return etree_tag
-
-        def _setName(self, name):
-            self._name = name
-            self._element.tag = self._getETreeTag(self._name, self._namespace)
-
-        def _getName(self):
-            return self._name
-
-        name = property(_getName, _setName)
-
-        def _setNamespace(self, namespace):
-            self._namespace = namespace
-            self._element.tag = self._getETreeTag(self._name, self._namespace)
-
-        def _getNamespace(self):
-            return self._namespace
-
-        namespace = property(_getNamespace, _setNamespace)
-
-        def _getAttributes(self):
-            return self._element.attrib
-
-        def _setAttributes(self, attributes):
-            # Delete existing attributes first
-            # XXX - there may be a better way to do this...
-            for key in list(self._element.attrib.keys()):
-                del self._element.attrib[key]
-            for key, value in attributes.items():
-                if isinstance(key, tuple):
-                    name = "{%s}%s" % (key[2], key[1])
-                else:
-                    name = key
-                self._element.set(name, value)
-
-        attributes = property(_getAttributes, _setAttributes)
-
-        def _getChildNodes(self):
-            return self._childNodes
-
-        def _setChildNodes(self, value):
-            del self._element[:]
-            self._childNodes = []
-            for element in value:
-                self.insertChild(element)
-
-        childNodes = property(_getChildNodes, _setChildNodes)
-
-        def hasContent(self):
-            """Return true if the node has children or text"""
-            return bool(self._element.text or len(self._element))
-
-        def appendChild(self, node):
-            self._childNodes.append(node)
-            self._element.append(node._element)
-            node.parent = self
-
-        def insertBefore(self, node, refNode):
-            index = list(self._element).index(refNode._element)
-            self._element.insert(index, node._element)
-            node.parent = self
-
-        def removeChild(self, node):
-            self._childNodes.remove(node)
-            self._element.remove(node._element)
-            node.parent = None
-
-        def insertText(self, data, insertBefore=None):
-            if not(len(self._element)):
-                if not self._element.text:
-                    self._element.text = ""
-                self._element.text += data
-            elif insertBefore is None:
-                # Insert the text as the tail of the last child element
-                if not self._element[-1].tail:
-                    self._element[-1].tail = ""
-                self._element[-1].tail += data
-            else:
-                # Insert the text before the specified node
-                children = list(self._element)
-                index = children.index(insertBefore._element)
-                if index > 0:
-                    if not self._element[index - 1].tail:
-                        self._element[index - 1].tail = ""
-                    self._element[index - 1].tail += data
-                else:
-                    if not self._element.text:
-                        self._element.text = ""
-                    self._element.text += data
-
-        def cloneNode(self):
-            element = type(self)(self.name, self.namespace)
-            for name, value in self.attributes.items():
-                element.attributes[name] = value
-            return element
-
-        def reparentChildren(self, newParent):
-            if newParent.childNodes:
-                newParent.childNodes[-1]._element.tail += self._element.text
-            else:
-                if not newParent._element.text:
-                    newParent._element.text = ""
-                if self._element.text is not None:
-                    newParent._element.text += self._element.text
-            self._element.text = ""
-            base.Node.reparentChildren(self, newParent)
-
-    class Comment(Element):
-        def __init__(self, data):
-            # Use the superclass constructor to set all properties on the
-            # wrapper element
-            self._element = ElementTree.Comment(data)
-            self.parent = None
-            self._childNodes = []
-            self._flags = []
-
-        def _getData(self):
-            return self._element.text
-
-        def _setData(self, value):
-            self._element.text = value
-
-        data = property(_getData, _setData)
-
-    class DocumentType(Element):
-        def __init__(self, name, publicId, systemId):
-            Element.__init__(self, "<!DOCTYPE>")
-            self._element.text = name
-            self.publicId = publicId
-            self.systemId = systemId
-
-        def _getPublicId(self):
-            return self._element.get("publicId", "")
-
-        def _setPublicId(self, value):
-            if value is not None:
-                self._element.set("publicId", value)
-
-        publicId = property(_getPublicId, _setPublicId)
-
-        def _getSystemId(self):
-            return self._element.get("systemId", "")
-
-        def _setSystemId(self, value):
-            if value is not None:
-                self._element.set("systemId", value)
-
-        systemId = property(_getSystemId, _setSystemId)
-
-    class Document(Element):
-        def __init__(self):
-            Element.__init__(self, "DOCUMENT_ROOT")
-
-    class DocumentFragment(Element):
-        def __init__(self):
-            Element.__init__(self, "DOCUMENT_FRAGMENT")
-
-    def testSerializer(element):
-        rv = []
-
-        def serializeElement(element, indent=0):
-            if not(hasattr(element, "tag")):
-                element = element.getroot()
-            if element.tag == "<!DOCTYPE>":
-                if element.get("publicId") or element.get("systemId"):
-                    publicId = element.get("publicId") or ""
-                    systemId = element.get("systemId") or ""
-                    rv.append("""<!DOCTYPE %s "%s" "%s">""" %
-                              (element.text, publicId, systemId))
-                else:
-                    rv.append("<!DOCTYPE %s>" % (element.text,))
-            elif element.tag == "DOCUMENT_ROOT":
-                rv.append("#document")
-                if element.text is not None:
-                    rv.append("|%s\"%s\"" % (' ' * (indent + 2), element.text))
-                if element.tail is not None:
-                    raise TypeError("Document node cannot have tail")
-                if hasattr(element, "attrib") and len(element.attrib):
-                    raise TypeError("Document node cannot have attributes")
-            elif element.tag == ElementTreeCommentType:
-                rv.append("|%s<!-- %s -->" % (' ' * indent, element.text))
-            else:
-                assert isinstance(element.tag, text_type), \
-                    "Expected unicode, got %s, %s" % (type(element.tag), element.tag)
-                nsmatch = tag_regexp.match(element.tag)
-
-                if nsmatch is None:
-                    name = element.tag
-                else:
-                    ns, name = nsmatch.groups()
-                    prefix = constants.prefixes[ns]
-                    name = "%s %s" % (prefix, name)
-                rv.append("|%s<%s>" % (' ' * indent, name))
-
-                if hasattr(element, "attrib"):
-                    attributes = []
-                    for name, value in element.attrib.items():
-                        nsmatch = tag_regexp.match(name)
-                        if nsmatch is not None:
-                            ns, name = nsmatch.groups()
-                            prefix = constants.prefixes[ns]
-                            attr_string = "%s %s" % (prefix, name)
-                        else:
-                            attr_string = name
-                        attributes.append((attr_string, value))
-
-                    for name, value in sorted(attributes):
-                        rv.append('|%s%s="%s"' % (' ' * (indent + 2), name, value))
-                if element.text:
-                    rv.append("|%s\"%s\"" % (' ' * (indent + 2), element.text))
-            indent += 2
-            for child in element:
-                serializeElement(child, indent)
-            if element.tail:
-                rv.append("|%s\"%s\"" % (' ' * (indent - 2), element.tail))
-        serializeElement(element, 0)
-
-        return "\n".join(rv)
-
-    def tostring(element):  # pylint:disable=unused-variable
-        """Serialize an element and its child nodes to a string"""
-        rv = []
-        filter = _ihatexml.InfosetFilter()
-
-        def serializeElement(element):
-            if isinstance(element, ElementTree.ElementTree):
-                element = element.getroot()
-
-            if element.tag == "<!DOCTYPE>":
-                if element.get("publicId") or element.get("systemId"):
-                    publicId = element.get("publicId") or ""
-                    systemId = element.get("systemId") or ""
-                    rv.append("""<!DOCTYPE %s PUBLIC "%s" "%s">""" %
-                              (element.text, publicId, systemId))
-                else:
-                    rv.append("<!DOCTYPE %s>" % (element.text,))
-            elif element.tag == "DOCUMENT_ROOT":
-                if element.text is not None:
-                    rv.append(element.text)
-                if element.tail is not None:
-                    raise TypeError("Document node cannot have tail")
-                if hasattr(element, "attrib") and len(element.attrib):
-                    raise TypeError("Document node cannot have attributes")
-
-                for child in element:
-                    serializeElement(child)
-
-            elif element.tag == ElementTreeCommentType:
-                rv.append("<!--%s-->" % (element.text,))
-            else:
-                # This is assumed to be an ordinary element
-                if not element.attrib:
-                    rv.append("<%s>" % (filter.fromXmlName(element.tag),))
-                else:
-                    attr = " ".join(["%s=\"%s\"" % (
-                        filter.fromXmlName(name), value)
-                        for name, value in element.attrib.items()])
-                    rv.append("<%s %s>" % (element.tag, attr))
-                if element.text:
-                    rv.append(element.text)
-
-                for child in element:
-                    serializeElement(child)
-
-                rv.append("</%s>" % (element.tag,))
-
-            if element.tail:
-                rv.append(element.tail)
-
-        serializeElement(element)
-
-        return "".join(rv)
-
-    class TreeBuilder(base.TreeBuilder):  # pylint:disable=unused-variable
-        documentClass = Document
-        doctypeClass = DocumentType
-        elementClass = Element
-        commentClass = Comment
-        fragmentClass = DocumentFragment
-        implementation = ElementTreeImplementation
-
-        def testSerializer(self, element):
-            return testSerializer(element)
-
-        def getDocument(self):
-            if fullTree:
-                return self.document._element
-            else:
-                if self.defaultNamespace is not None:
-                    return self.document._element.find(
-                        "{%s}html" % self.defaultNamespace)
-                else:
-                    return self.document._element.find("html")
-
-        def getFragment(self):
-            return base.TreeBuilder.getFragment(self)._element
-
-    return locals()
-
-
-getETreeModule = moduleFactoryFactory(getETreeBuilder)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/etree_lxml.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/etree_lxml.py
deleted file mode 100644
index ca12a99..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treebuilders/etree_lxml.py
+++ /dev/null
@@ -1,366 +0,0 @@
-"""Module for supporting the lxml.etree library. The idea here is to use as much
-of the native library as possible, without using fragile hacks like custom element
-names that break between releases. The downside of this is that we cannot represent
-all possible trees; specifically the following are known to cause problems:
-
-Text or comments as siblings of the root element
-Docypes with no name
-
-When any of these things occur, we emit a DataLossWarning
-"""
-
-from __future__ import absolute_import, division, unicode_literals
-# pylint:disable=protected-access
-
-import warnings
-import re
-import sys
-
-from . import base
-from ..constants import DataLossWarning
-from .. import constants
-from . import etree as etree_builders
-from .. import _ihatexml
-
-import lxml.etree as etree
-
-
-fullTree = True
-tag_regexp = re.compile("{([^}]*)}(.*)")
-
-comment_type = etree.Comment("asd").tag
-
-
-class DocumentType(object):
-    def __init__(self, name, publicId, systemId):
-        self.name = name
-        self.publicId = publicId
-        self.systemId = systemId
-
-
-class Document(object):
-    def __init__(self):
-        self._elementTree = None
-        self._childNodes = []
-
-    def appendChild(self, element):
-        self._elementTree.getroot().addnext(element._element)
-
-    def _getChildNodes(self):
-        return self._childNodes
-
-    childNodes = property(_getChildNodes)
-
-
-def testSerializer(element):
-    rv = []
-    infosetFilter = _ihatexml.InfosetFilter(preventDoubleDashComments=True)
-
-    def serializeElement(element, indent=0):
-        if not hasattr(element, "tag"):
-            if hasattr(element, "getroot"):
-                # Full tree case
-                rv.append("#document")
-                if element.docinfo.internalDTD:
-                    if not (element.docinfo.public_id or
-                            element.docinfo.system_url):
-                        dtd_str = "<!DOCTYPE %s>" % element.docinfo.root_name
-                    else:
-                        dtd_str = """<!DOCTYPE %s "%s" "%s">""" % (
-                            element.docinfo.root_name,
-                            element.docinfo.public_id,
-                            element.docinfo.system_url)
-                    rv.append("|%s%s" % (' ' * (indent + 2), dtd_str))
-                next_element = element.getroot()
-                while next_element.getprevious() is not None:
-                    next_element = next_element.getprevious()
-                while next_element is not None:
-                    serializeElement(next_element, indent + 2)
-                    next_element = next_element.getnext()
-            elif isinstance(element, str) or isinstance(element, bytes):
-                # Text in a fragment
-                assert isinstance(element, str) or sys.version_info[0] == 2
-                rv.append("|%s\"%s\"" % (' ' * indent, element))
-            else:
-                # Fragment case
-                rv.append("#document-fragment")
-                for next_element in element:
-                    serializeElement(next_element, indent + 2)
-        elif element.tag == comment_type:
-            rv.append("|%s<!-- %s -->" % (' ' * indent, element.text))
-            if hasattr(element, "tail") and element.tail:
-                rv.append("|%s\"%s\"" % (' ' * indent, element.tail))
-        else:
-            assert isinstance(element, etree._Element)
-            nsmatch = etree_builders.tag_regexp.match(element.tag)
-            if nsmatch is not None:
-                ns = nsmatch.group(1)
-                tag = nsmatch.group(2)
-                prefix = constants.prefixes[ns]
-                rv.append("|%s<%s %s>" % (' ' * indent, prefix,
-                                          infosetFilter.fromXmlName(tag)))
-            else:
-                rv.append("|%s<%s>" % (' ' * indent,
-                                       infosetFilter.fromXmlName(element.tag)))
-
-            if hasattr(element, "attrib"):
-                attributes = []
-                for name, value in element.attrib.items():
-                    nsmatch = tag_regexp.match(name)
-                    if nsmatch is not None:
-                        ns, name = nsmatch.groups()
-                        name = infosetFilter.fromXmlName(name)
-                        prefix = constants.prefixes[ns]
-                        attr_string = "%s %s" % (prefix, name)
-                    else:
-                        attr_string = infosetFilter.fromXmlName(name)
-                    attributes.append((attr_string, value))
-
-                for name, value in sorted(attributes):
-                    rv.append('|%s%s="%s"' % (' ' * (indent + 2), name, value))
-
-            if element.text:
-                rv.append("|%s\"%s\"" % (' ' * (indent + 2), element.text))
-            indent += 2
-            for child in element:
-                serializeElement(child, indent)
-            if hasattr(element, "tail") and element.tail:
-                rv.append("|%s\"%s\"" % (' ' * (indent - 2), element.tail))
-    serializeElement(element, 0)
-
-    return "\n".join(rv)
-
-
-def tostring(element):
-    """Serialize an element and its child nodes to a string"""
-    rv = []
-
-    def serializeElement(element):
-        if not hasattr(element, "tag"):
-            if element.docinfo.internalDTD:
-                if element.docinfo.doctype:
-                    dtd_str = element.docinfo.doctype
-                else:
-                    dtd_str = "<!DOCTYPE %s>" % element.docinfo.root_name
-                rv.append(dtd_str)
-            serializeElement(element.getroot())
-
-        elif element.tag == comment_type:
-            rv.append("<!--%s-->" % (element.text,))
-
-        else:
-            # This is assumed to be an ordinary element
-            if not element.attrib:
-                rv.append("<%s>" % (element.tag,))
-            else:
-                attr = " ".join(["%s=\"%s\"" % (name, value)
-                                 for name, value in element.attrib.items()])
-                rv.append("<%s %s>" % (element.tag, attr))
-            if element.text:
-                rv.append(element.text)
-
-            for child in element:
-                serializeElement(child)
-
-            rv.append("</%s>" % (element.tag,))
-
-        if hasattr(element, "tail") and element.tail:
-            rv.append(element.tail)
-
-    serializeElement(element)
-
-    return "".join(rv)
-
-
-class TreeBuilder(base.TreeBuilder):
-    documentClass = Document
-    doctypeClass = DocumentType
-    elementClass = None
-    commentClass = None
-    fragmentClass = Document
-    implementation = etree
-
-    def __init__(self, namespaceHTMLElements, fullTree=False):
-        builder = etree_builders.getETreeModule(etree, fullTree=fullTree)
-        infosetFilter = self.infosetFilter = _ihatexml.InfosetFilter(preventDoubleDashComments=True)
-        self.namespaceHTMLElements = namespaceHTMLElements
-
-        class Attributes(dict):
-            def __init__(self, element, value=None):
-                if value is None:
-                    value = {}
-                self._element = element
-                dict.__init__(self, value)  # pylint:disable=non-parent-init-called
-                for key, value in self.items():
-                    if isinstance(key, tuple):
-                        name = "{%s}%s" % (key[2], infosetFilter.coerceAttribute(key[1]))
-                    else:
-                        name = infosetFilter.coerceAttribute(key)
-                    self._element._element.attrib[name] = value
-
-            def __setitem__(self, key, value):
-                dict.__setitem__(self, key, value)
-                if isinstance(key, tuple):
-                    name = "{%s}%s" % (key[2], infosetFilter.coerceAttribute(key[1]))
-                else:
-                    name = infosetFilter.coerceAttribute(key)
-                self._element._element.attrib[name] = value
-
-        class Element(builder.Element):
-            def __init__(self, name, namespace):
-                name = infosetFilter.coerceElement(name)
-                builder.Element.__init__(self, name, namespace=namespace)
-                self._attributes = Attributes(self)
-
-            def _setName(self, name):
-                self._name = infosetFilter.coerceElement(name)
-                self._element.tag = self._getETreeTag(
-                    self._name, self._namespace)
-
-            def _getName(self):
-                return infosetFilter.fromXmlName(self._name)
-
-            name = property(_getName, _setName)
-
-            def _getAttributes(self):
-                return self._attributes
-
-            def _setAttributes(self, attributes):
-                self._attributes = Attributes(self, attributes)
-
-            attributes = property(_getAttributes, _setAttributes)
-
-            def insertText(self, data, insertBefore=None):
-                data = infosetFilter.coerceCharacters(data)
-                builder.Element.insertText(self, data, insertBefore)
-
-            def appendChild(self, child):
-                builder.Element.appendChild(self, child)
-
-        class Comment(builder.Comment):
-            def __init__(self, data):
-                data = infosetFilter.coerceComment(data)
-                builder.Comment.__init__(self, data)
-
-            def _setData(self, data):
-                data = infosetFilter.coerceComment(data)
-                self._element.text = data
-
-            def _getData(self):
-                return self._element.text
-
-            data = property(_getData, _setData)
-
-        self.elementClass = Element
-        self.commentClass = Comment
-        # self.fragmentClass = builder.DocumentFragment
-        base.TreeBuilder.__init__(self, namespaceHTMLElements)
-
-    def reset(self):
-        base.TreeBuilder.reset(self)
-        self.insertComment = self.insertCommentInitial
-        self.initial_comments = []
-        self.doctype = None
-
-    def testSerializer(self, element):
-        return testSerializer(element)
-
-    def getDocument(self):
-        if fullTree:
-            return self.document._elementTree
-        else:
-            return self.document._elementTree.getroot()
-
-    def getFragment(self):
-        fragment = []
-        element = self.openElements[0]._element
-        if element.text:
-            fragment.append(element.text)
-        fragment.extend(list(element))
-        if element.tail:
-            fragment.append(element.tail)
-        return fragment
-
-    def insertDoctype(self, token):
-        name = token["name"]
-        publicId = token["publicId"]
-        systemId = token["systemId"]
-
-        if not name:
-            warnings.warn("lxml cannot represent empty doctype", DataLossWarning)
-            self.doctype = None
-        else:
-            coercedName = self.infosetFilter.coerceElement(name)
-            if coercedName != name:
-                warnings.warn("lxml cannot represent non-xml doctype", DataLossWarning)
-
-            doctype = self.doctypeClass(coercedName, publicId, systemId)
-            self.doctype = doctype
-
-    def insertCommentInitial(self, data, parent=None):
-        assert parent is None or parent is self.document
-        assert self.document._elementTree is None
-        self.initial_comments.append(data)
-
-    def insertCommentMain(self, data, parent=None):
-        if (parent == self.document and
-                self.document._elementTree.getroot()[-1].tag == comment_type):
-            warnings.warn("lxml cannot represent adjacent comments beyond the root elements", DataLossWarning)
-        super(TreeBuilder, self).insertComment(data, parent)
-
-    def insertRoot(self, token):
-        # Because of the way libxml2 works, it doesn't seem to be possible to
-        # alter information like the doctype after the tree has been parsed.
-        # Therefore we need to use the built-in parser to create our initial
-        # tree, after which we can add elements like normal
-        docStr = ""
-        if self.doctype:
-            assert self.doctype.name
-            docStr += "<!DOCTYPE %s" % self.doctype.name
-            if (self.doctype.publicId is not None or
-                    self.doctype.systemId is not None):
-                docStr += (' PUBLIC "%s" ' %
-                           (self.infosetFilter.coercePubid(self.doctype.publicId or "")))
-                if self.doctype.systemId:
-                    sysid = self.doctype.systemId
-                    if sysid.find("'") >= 0 and sysid.find('"') >= 0:
-                        warnings.warn("DOCTYPE system cannot contain single and double quotes", DataLossWarning)
-                        sysid = sysid.replace("'", 'U00027')
-                    if sysid.find("'") >= 0:
-                        docStr += '"%s"' % sysid
-                    else:
-                        docStr += "'%s'" % sysid
-                else:
-                    docStr += "''"
-            docStr += ">"
-            if self.doctype.name != token["name"]:
-                warnings.warn("lxml cannot represent doctype with a different name to the root element", DataLossWarning)
-        docStr += "<THIS_SHOULD_NEVER_APPEAR_PUBLICLY/>"
-        root = etree.fromstring(docStr)
-
-        # Append the initial comments:
-        for comment_token in self.initial_comments:
-            comment = self.commentClass(comment_token["data"])
-            root.addprevious(comment._element)
-
-        # Create the root document and add the ElementTree to it
-        self.document = self.documentClass()
-        self.document._elementTree = root.getroottree()
-
-        # Give the root element the right name
-        name = token["name"]
-        namespace = token.get("namespace", self.defaultNamespace)
-        if namespace is None:
-            etree_tag = name
-        else:
-            etree_tag = "{%s}%s" % (namespace, name)
-        root.tag = etree_tag
-
-        # Add the root element to the internal child/open data structures
-        root_element = self.elementClass(name, namespace)
-        root_element._element = root
-        self.document._childNodes.append(root_element)
-        self.openElements.append(root_element)
-
-        # Reset to the default insert comment function
-        self.insertComment = self.insertCommentMain
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/__init__.py
deleted file mode 100644
index 9bec207..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/__init__.py
+++ /dev/null
@@ -1,154 +0,0 @@
-"""A collection of modules for iterating through different kinds of
-tree, generating tokens identical to those produced by the tokenizer
-module.
-
-To create a tree walker for a new type of tree, you need to do
-implement a tree walker object (called TreeWalker by convention) that
-implements a 'serialize' method taking a tree as sole argument and
-returning an iterator generating tokens.
-"""
-
-from __future__ import absolute_import, division, unicode_literals
-
-from .. import constants
-from .._utils import default_etree
-
-__all__ = ["getTreeWalker", "pprint"]
-
-treeWalkerCache = {}
-
-
-def getTreeWalker(treeType, implementation=None, **kwargs):
-    """Get a TreeWalker class for various types of tree with built-in support
-
-    :arg str treeType: the name of the tree type required (case-insensitive).
-        Supported values are:
-
-        * "dom": The xml.dom.minidom DOM implementation
-        * "etree": A generic walker for tree implementations exposing an
-          elementtree-like interface (known to work with ElementTree,
-          cElementTree and lxml.etree).
-        * "lxml": Optimized walker for lxml.etree
-        * "genshi": a Genshi stream
-
-    :arg implementation: A module implementing the tree type e.g.
-        xml.etree.ElementTree or cElementTree (Currently applies to the "etree"
-        tree type only).
-
-    :arg kwargs: keyword arguments passed to the etree walker--for other
-        walkers, this has no effect
-
-    :returns: a TreeWalker class
-
-    """
-
-    treeType = treeType.lower()
-    if treeType not in treeWalkerCache:
-        if treeType == "dom":
-            from . import dom
-            treeWalkerCache[treeType] = dom.TreeWalker
-        elif treeType == "genshi":
-            from . import genshi
-            treeWalkerCache[treeType] = genshi.TreeWalker
-        elif treeType == "lxml":
-            from . import etree_lxml
-            treeWalkerCache[treeType] = etree_lxml.TreeWalker
-        elif treeType == "etree":
-            from . import etree
-            if implementation is None:
-                implementation = default_etree
-            # XXX: NEVER cache here, caching is done in the etree submodule
-            return etree.getETreeModule(implementation, **kwargs).TreeWalker
-    return treeWalkerCache.get(treeType)
-
-
-def concatenateCharacterTokens(tokens):
-    pendingCharacters = []
-    for token in tokens:
-        type = token["type"]
-        if type in ("Characters", "SpaceCharacters"):
-            pendingCharacters.append(token["data"])
-        else:
-            if pendingCharacters:
-                yield {"type": "Characters", "data": "".join(pendingCharacters)}
-                pendingCharacters = []
-            yield token
-    if pendingCharacters:
-        yield {"type": "Characters", "data": "".join(pendingCharacters)}
-
-
-def pprint(walker):
-    """Pretty printer for tree walkers
-
-    Takes a TreeWalker instance and pretty prints the output of walking the tree.
-
-    :arg walker: a TreeWalker instance
-
-    """
-    output = []
-    indent = 0
-    for token in concatenateCharacterTokens(walker):
-        type = token["type"]
-        if type in ("StartTag", "EmptyTag"):
-            # tag name
-            if token["namespace"] and token["namespace"] != constants.namespaces["html"]:
-                if token["namespace"] in constants.prefixes:
-                    ns = constants.prefixes[token["namespace"]]
-                else:
-                    ns = token["namespace"]
-                name = "%s %s" % (ns, token["name"])
-            else:
-                name = token["name"]
-            output.append("%s<%s>" % (" " * indent, name))
-            indent += 2
-            # attributes (sorted for consistent ordering)
-            attrs = token["data"]
-            for (namespace, localname), value in sorted(attrs.items()):
-                if namespace:
-                    if namespace in constants.prefixes:
-                        ns = constants.prefixes[namespace]
-                    else:
-                        ns = namespace
-                    name = "%s %s" % (ns, localname)
-                else:
-                    name = localname
-                output.append("%s%s=\"%s\"" % (" " * indent, name, value))
-            # self-closing
-            if type == "EmptyTag":
-                indent -= 2
-
-        elif type == "EndTag":
-            indent -= 2
-
-        elif type == "Comment":
-            output.append("%s<!-- %s -->" % (" " * indent, token["data"]))
-
-        elif type == "Doctype":
-            if token["name"]:
-                if token["publicId"]:
-                    output.append("""%s<!DOCTYPE %s "%s" "%s">""" %
-                                  (" " * indent,
-                                   token["name"],
-                                   token["publicId"],
-                                   token["systemId"] if token["systemId"] else ""))
-                elif token["systemId"]:
-                    output.append("""%s<!DOCTYPE %s "" "%s">""" %
-                                  (" " * indent,
-                                   token["name"],
-                                   token["systemId"]))
-                else:
-                    output.append("%s<!DOCTYPE %s>" % (" " * indent,
-                                                       token["name"]))
-            else:
-                output.append("%s<!DOCTYPE >" % (" " * indent,))
-
-        elif type == "Characters":
-            output.append("%s\"%s\"" % (" " * indent, token["data"]))
-
-        elif type == "SpaceCharacters":
-            assert False, "concatenateCharacterTokens should have got rid of all Space tokens"
-
-        else:
-            raise ValueError("Unknown token type, %s" % type)
-
-    return "\n".join(output)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 7330be3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/base.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/base.py
deleted file mode 100644
index 80c474c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/base.py
+++ /dev/null
@@ -1,252 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from xml.dom import Node
-from ..constants import namespaces, voidElements, spaceCharacters
-
-__all__ = ["DOCUMENT", "DOCTYPE", "TEXT", "ELEMENT", "COMMENT", "ENTITY", "UNKNOWN",
-           "TreeWalker", "NonRecursiveTreeWalker"]
-
-DOCUMENT = Node.DOCUMENT_NODE
-DOCTYPE = Node.DOCUMENT_TYPE_NODE
-TEXT = Node.TEXT_NODE
-ELEMENT = Node.ELEMENT_NODE
-COMMENT = Node.COMMENT_NODE
-ENTITY = Node.ENTITY_NODE
-UNKNOWN = "<#UNKNOWN#>"
-
-spaceCharacters = "".join(spaceCharacters)
-
-
-class TreeWalker(object):
-    """Walks a tree yielding tokens
-
-    Tokens are dicts that all have a ``type`` field specifying the type of the
-    token.
-
-    """
-    def __init__(self, tree):
-        """Creates a TreeWalker
-
-        :arg tree: the tree to walk
-
-        """
-        self.tree = tree
-
-    def __iter__(self):
-        raise NotImplementedError
-
-    def error(self, msg):
-        """Generates an error token with the given message
-
-        :arg msg: the error message
-
-        :returns: SerializeError token
-
-        """
-        return {"type": "SerializeError", "data": msg}
-
-    def emptyTag(self, namespace, name, attrs, hasChildren=False):
-        """Generates an EmptyTag token
-
-        :arg namespace: the namespace of the token--can be ``None``
-
-        :arg name: the name of the element
-
-        :arg attrs: the attributes of the element as a dict
-
-        :arg hasChildren: whether or not to yield a SerializationError because
-            this tag shouldn't have children
-
-        :returns: EmptyTag token
-
-        """
-        yield {"type": "EmptyTag", "name": name,
-               "namespace": namespace,
-               "data": attrs}
-        if hasChildren:
-            yield self.error("Void element has children")
-
-    def startTag(self, namespace, name, attrs):
-        """Generates a StartTag token
-
-        :arg namespace: the namespace of the token--can be ``None``
-
-        :arg name: the name of the element
-
-        :arg attrs: the attributes of the element as a dict
-
-        :returns: StartTag token
-
-        """
-        return {"type": "StartTag",
-                "name": name,
-                "namespace": namespace,
-                "data": attrs}
-
-    def endTag(self, namespace, name):
-        """Generates an EndTag token
-
-        :arg namespace: the namespace of the token--can be ``None``
-
-        :arg name: the name of the element
-
-        :returns: EndTag token
-
-        """
-        return {"type": "EndTag",
-                "name": name,
-                "namespace": namespace}
-
-    def text(self, data):
-        """Generates SpaceCharacters and Characters tokens
-
-        Depending on what's in the data, this generates one or more
-        ``SpaceCharacters`` and ``Characters`` tokens.
-
-        For example:
-
-            >>> from html5lib.treewalkers.base import TreeWalker
-            >>> # Give it an empty tree just so it instantiates
-            >>> walker = TreeWalker([])
-            >>> list(walker.text(''))
-            []
-            >>> list(walker.text('  '))
-            [{u'data': '  ', u'type': u'SpaceCharacters'}]
-            >>> list(walker.text(' abc '))  # doctest: +NORMALIZE_WHITESPACE
-            [{u'data': ' ', u'type': u'SpaceCharacters'},
-            {u'data': u'abc', u'type': u'Characters'},
-            {u'data': u' ', u'type': u'SpaceCharacters'}]
-
-        :arg data: the text data
-
-        :returns: one or more ``SpaceCharacters`` and ``Characters`` tokens
-
-        """
-        data = data
-        middle = data.lstrip(spaceCharacters)
-        left = data[:len(data) - len(middle)]
-        if left:
-            yield {"type": "SpaceCharacters", "data": left}
-        data = middle
-        middle = data.rstrip(spaceCharacters)
-        right = data[len(middle):]
-        if middle:
-            yield {"type": "Characters", "data": middle}
-        if right:
-            yield {"type": "SpaceCharacters", "data": right}
-
-    def comment(self, data):
-        """Generates a Comment token
-
-        :arg data: the comment
-
-        :returns: Comment token
-
-        """
-        return {"type": "Comment", "data": data}
-
-    def doctype(self, name, publicId=None, systemId=None):
-        """Generates a Doctype token
-
-        :arg name:
-
-        :arg publicId:
-
-        :arg systemId:
-
-        :returns: the Doctype token
-
-        """
-        return {"type": "Doctype",
-                "name": name,
-                "publicId": publicId,
-                "systemId": systemId}
-
-    def entity(self, name):
-        """Generates an Entity token
-
-        :arg name: the entity name
-
-        :returns: an Entity token
-
-        """
-        return {"type": "Entity", "name": name}
-
-    def unknown(self, nodeType):
-        """Handles unknown node types"""
-        return self.error("Unknown node type: " + nodeType)
-
-
-class NonRecursiveTreeWalker(TreeWalker):
-    def getNodeDetails(self, node):
-        raise NotImplementedError
-
-    def getFirstChild(self, node):
-        raise NotImplementedError
-
-    def getNextSibling(self, node):
-        raise NotImplementedError
-
-    def getParentNode(self, node):
-        raise NotImplementedError
-
-    def __iter__(self):
-        currentNode = self.tree
-        while currentNode is not None:
-            details = self.getNodeDetails(currentNode)
-            type, details = details[0], details[1:]
-            hasChildren = False
-
-            if type == DOCTYPE:
-                yield self.doctype(*details)
-
-            elif type == TEXT:
-                for token in self.text(*details):
-                    yield token
-
-            elif type == ELEMENT:
-                namespace, name, attributes, hasChildren = details
-                if (not namespace or namespace == namespaces["html"]) and name in voidElements:
-                    for token in self.emptyTag(namespace, name, attributes,
-                                               hasChildren):
-                        yield token
-                    hasChildren = False
-                else:
-                    yield self.startTag(namespace, name, attributes)
-
-            elif type == COMMENT:
-                yield self.comment(details[0])
-
-            elif type == ENTITY:
-                yield self.entity(details[0])
-
-            elif type == DOCUMENT:
-                hasChildren = True
-
-            else:
-                yield self.unknown(details[0])
-
-            if hasChildren:
-                firstChild = self.getFirstChild(currentNode)
-            else:
-                firstChild = None
-
-            if firstChild is not None:
-                currentNode = firstChild
-            else:
-                while currentNode is not None:
-                    details = self.getNodeDetails(currentNode)
-                    type, details = details[0], details[1:]
-                    if type == ELEMENT:
-                        namespace, name, attributes, hasChildren = details
-                        if (namespace and namespace != namespaces["html"]) or name not in voidElements:
-                            yield self.endTag(namespace, name)
-                    if self.tree is currentNode:
-                        currentNode = None
-                        break
-                    nextSibling = self.getNextSibling(currentNode)
-                    if nextSibling is not None:
-                        currentNode = nextSibling
-                        break
-                    else:
-                        currentNode = self.getParentNode(currentNode)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/dom.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/dom.py
deleted file mode 100644
index b0c89b0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/dom.py
+++ /dev/null
@@ -1,43 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from xml.dom import Node
-
-from . import base
-
-
-class TreeWalker(base.NonRecursiveTreeWalker):
-    def getNodeDetails(self, node):
-        if node.nodeType == Node.DOCUMENT_TYPE_NODE:
-            return base.DOCTYPE, node.name, node.publicId, node.systemId
-
-        elif node.nodeType in (Node.TEXT_NODE, Node.CDATA_SECTION_NODE):
-            return base.TEXT, node.nodeValue
-
-        elif node.nodeType == Node.ELEMENT_NODE:
-            attrs = {}
-            for attr in list(node.attributes.keys()):
-                attr = node.getAttributeNode(attr)
-                if attr.namespaceURI:
-                    attrs[(attr.namespaceURI, attr.localName)] = attr.value
-                else:
-                    attrs[(None, attr.name)] = attr.value
-            return (base.ELEMENT, node.namespaceURI, node.nodeName,
-                    attrs, node.hasChildNodes())
-
-        elif node.nodeType == Node.COMMENT_NODE:
-            return base.COMMENT, node.nodeValue
-
-        elif node.nodeType in (Node.DOCUMENT_NODE, Node.DOCUMENT_FRAGMENT_NODE):
-            return (base.DOCUMENT,)
-
-        else:
-            return base.UNKNOWN, node.nodeType
-
-    def getFirstChild(self, node):
-        return node.firstChild
-
-    def getNextSibling(self, node):
-        return node.nextSibling
-
-    def getParentNode(self, node):
-        return node.parentNode
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/etree.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/etree.py
deleted file mode 100644
index 95fc0c1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/etree.py
+++ /dev/null
@@ -1,130 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from collections import OrderedDict
-import re
-
-from pip._vendor.six import string_types
-
-from . import base
-from .._utils import moduleFactoryFactory
-
-tag_regexp = re.compile("{([^}]*)}(.*)")
-
-
-def getETreeBuilder(ElementTreeImplementation):
-    ElementTree = ElementTreeImplementation
-    ElementTreeCommentType = ElementTree.Comment("asd").tag
-
-    class TreeWalker(base.NonRecursiveTreeWalker):  # pylint:disable=unused-variable
-        """Given the particular ElementTree representation, this implementation,
-        to avoid using recursion, returns "nodes" as tuples with the following
-        content:
-
-        1. The current element
-
-        2. The index of the element relative to its parent
-
-        3. A stack of ancestor elements
-
-        4. A flag "text", "tail" or None to indicate if the current node is a
-           text node; either the text or tail of the current element (1)
-        """
-        def getNodeDetails(self, node):
-            if isinstance(node, tuple):  # It might be the root Element
-                elt, _, _, flag = node
-                if flag in ("text", "tail"):
-                    return base.TEXT, getattr(elt, flag)
-                else:
-                    node = elt
-
-            if not(hasattr(node, "tag")):
-                node = node.getroot()
-
-            if node.tag in ("DOCUMENT_ROOT", "DOCUMENT_FRAGMENT"):
-                return (base.DOCUMENT,)
-
-            elif node.tag == "<!DOCTYPE>":
-                return (base.DOCTYPE, node.text,
-                        node.get("publicId"), node.get("systemId"))
-
-            elif node.tag == ElementTreeCommentType:
-                return base.COMMENT, node.text
-
-            else:
-                assert isinstance(node.tag, string_types), type(node.tag)
-                # This is assumed to be an ordinary element
-                match = tag_regexp.match(node.tag)
-                if match:
-                    namespace, tag = match.groups()
-                else:
-                    namespace = None
-                    tag = node.tag
-                attrs = OrderedDict()
-                for name, value in list(node.attrib.items()):
-                    match = tag_regexp.match(name)
-                    if match:
-                        attrs[(match.group(1), match.group(2))] = value
-                    else:
-                        attrs[(None, name)] = value
-                return (base.ELEMENT, namespace, tag,
-                        attrs, len(node) or node.text)
-
-        def getFirstChild(self, node):
-            if isinstance(node, tuple):
-                element, key, parents, flag = node
-            else:
-                element, key, parents, flag = node, None, [], None
-
-            if flag in ("text", "tail"):
-                return None
-            else:
-                if element.text:
-                    return element, key, parents, "text"
-                elif len(element):
-                    parents.append(element)
-                    return element[0], 0, parents, None
-                else:
-                    return None
-
-        def getNextSibling(self, node):
-            if isinstance(node, tuple):
-                element, key, parents, flag = node
-            else:
-                return None
-
-            if flag == "text":
-                if len(element):
-                    parents.append(element)
-                    return element[0], 0, parents, None
-                else:
-                    return None
-            else:
-                if element.tail and flag != "tail":
-                    return element, key, parents, "tail"
-                elif key < len(parents[-1]) - 1:
-                    return parents[-1][key + 1], key + 1, parents, None
-                else:
-                    return None
-
-        def getParentNode(self, node):
-            if isinstance(node, tuple):
-                element, key, parents, flag = node
-            else:
-                return None
-
-            if flag == "text":
-                if not parents:
-                    return element
-                else:
-                    return element, key, parents, None
-            else:
-                parent = parents.pop()
-                if not parents:
-                    return parent
-                else:
-                    assert list(parents[-1]).count(parent) == 1
-                    return parent, list(parents[-1]).index(parent), parents, None
-
-    return locals()
-
-getETreeModule = moduleFactoryFactory(getETreeBuilder)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/etree_lxml.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/etree_lxml.py
deleted file mode 100644
index e81ddf3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/etree_lxml.py
+++ /dev/null
@@ -1,213 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-from pip._vendor.six import text_type
-
-from lxml import etree
-from ..treebuilders.etree import tag_regexp
-
-from . import base
-
-from .. import _ihatexml
-
-
-def ensure_str(s):
-    if s is None:
-        return None
-    elif isinstance(s, text_type):
-        return s
-    else:
-        return s.decode("ascii", "strict")
-
-
-class Root(object):
-    def __init__(self, et):
-        self.elementtree = et
-        self.children = []
-
-        try:
-            if et.docinfo.internalDTD:
-                self.children.append(Doctype(self,
-                                             ensure_str(et.docinfo.root_name),
-                                             ensure_str(et.docinfo.public_id),
-                                             ensure_str(et.docinfo.system_url)))
-        except AttributeError:
-            pass
-
-        try:
-            node = et.getroot()
-        except AttributeError:
-            node = et
-
-        while node.getprevious() is not None:
-            node = node.getprevious()
-        while node is not None:
-            self.children.append(node)
-            node = node.getnext()
-
-        self.text = None
-        self.tail = None
-
-    def __getitem__(self, key):
-        return self.children[key]
-
-    def getnext(self):
-        return None
-
-    def __len__(self):
-        return 1
-
-
-class Doctype(object):
-    def __init__(self, root_node, name, public_id, system_id):
-        self.root_node = root_node
-        self.name = name
-        self.public_id = public_id
-        self.system_id = system_id
-
-        self.text = None
-        self.tail = None
-
-    def getnext(self):
-        return self.root_node.children[1]
-
-
-class FragmentRoot(Root):
-    def __init__(self, children):
-        self.children = [FragmentWrapper(self, child) for child in children]
-        self.text = self.tail = None
-
-    def getnext(self):
-        return None
-
-
-class FragmentWrapper(object):
-    def __init__(self, fragment_root, obj):
-        self.root_node = fragment_root
-        self.obj = obj
-        if hasattr(self.obj, 'text'):
-            self.text = ensure_str(self.obj.text)
-        else:
-            self.text = None
-        if hasattr(self.obj, 'tail'):
-            self.tail = ensure_str(self.obj.tail)
-        else:
-            self.tail = None
-
-    def __getattr__(self, name):
-        return getattr(self.obj, name)
-
-    def getnext(self):
-        siblings = self.root_node.children
-        idx = siblings.index(self)
-        if idx < len(siblings) - 1:
-            return siblings[idx + 1]
-        else:
-            return None
-
-    def __getitem__(self, key):
-        return self.obj[key]
-
-    def __bool__(self):
-        return bool(self.obj)
-
-    def getparent(self):
-        return None
-
-    def __str__(self):
-        return str(self.obj)
-
-    def __unicode__(self):
-        return str(self.obj)
-
-    def __len__(self):
-        return len(self.obj)
-
-
-class TreeWalker(base.NonRecursiveTreeWalker):
-    def __init__(self, tree):
-        # pylint:disable=redefined-variable-type
-        if isinstance(tree, list):
-            self.fragmentChildren = set(tree)
-            tree = FragmentRoot(tree)
-        else:
-            self.fragmentChildren = set()
-            tree = Root(tree)
-        base.NonRecursiveTreeWalker.__init__(self, tree)
-        self.filter = _ihatexml.InfosetFilter()
-
-    def getNodeDetails(self, node):
-        if isinstance(node, tuple):  # Text node
-            node, key = node
-            assert key in ("text", "tail"), "Text nodes are text or tail, found %s" % key
-            return base.TEXT, ensure_str(getattr(node, key))
-
-        elif isinstance(node, Root):
-            return (base.DOCUMENT,)
-
-        elif isinstance(node, Doctype):
-            return base.DOCTYPE, node.name, node.public_id, node.system_id
-
-        elif isinstance(node, FragmentWrapper) and not hasattr(node, "tag"):
-            return base.TEXT, ensure_str(node.obj)
-
-        elif node.tag == etree.Comment:
-            return base.COMMENT, ensure_str(node.text)
-
-        elif node.tag == etree.Entity:
-            return base.ENTITY, ensure_str(node.text)[1:-1]  # strip &;
-
-        else:
-            # This is assumed to be an ordinary element
-            match = tag_regexp.match(ensure_str(node.tag))
-            if match:
-                namespace, tag = match.groups()
-            else:
-                namespace = None
-                tag = ensure_str(node.tag)
-            attrs = {}
-            for name, value in list(node.attrib.items()):
-                name = ensure_str(name)
-                value = ensure_str(value)
-                match = tag_regexp.match(name)
-                if match:
-                    attrs[(match.group(1), match.group(2))] = value
-                else:
-                    attrs[(None, name)] = value
-            return (base.ELEMENT, namespace, self.filter.fromXmlName(tag),
-                    attrs, len(node) > 0 or node.text)
-
-    def getFirstChild(self, node):
-        assert not isinstance(node, tuple), "Text nodes have no children"
-
-        assert len(node) or node.text, "Node has no children"
-        if node.text:
-            return (node, "text")
-        else:
-            return node[0]
-
-    def getNextSibling(self, node):
-        if isinstance(node, tuple):  # Text node
-            node, key = node
-            assert key in ("text", "tail"), "Text nodes are text or tail, found %s" % key
-            if key == "text":
-                # XXX: we cannot use a "bool(node) and node[0] or None" construct here
-                # because node[0] might evaluate to False if it has no child element
-                if len(node):
-                    return node[0]
-                else:
-                    return None
-            else:  # tail
-                return node.getnext()
-
-        return (node, "tail") if node.tail else node.getnext()
-
-    def getParentNode(self, node):
-        if isinstance(node, tuple):  # Text node
-            node, key = node
-            assert key in ("text", "tail"), "Text nodes are text or tail, found %s" % key
-            if key == "text":
-                return node
-            # else: fallback to "normal" processing
-        elif node in self.fragmentChildren:
-            return None
-
-        return node.getparent()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/genshi.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/genshi.py
deleted file mode 100644
index 7483be2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/html5lib/treewalkers/genshi.py
+++ /dev/null
@@ -1,69 +0,0 @@
-from __future__ import absolute_import, division, unicode_literals
-
-from genshi.core import QName
-from genshi.core import START, END, XML_NAMESPACE, DOCTYPE, TEXT
-from genshi.core import START_NS, END_NS, START_CDATA, END_CDATA, PI, COMMENT
-
-from . import base
-
-from ..constants import voidElements, namespaces
-
-
-class TreeWalker(base.TreeWalker):
-    def __iter__(self):
-        # Buffer the events so we can pass in the following one
-        previous = None
-        for event in self.tree:
-            if previous is not None:
-                for token in self.tokens(previous, event):
-                    yield token
-            previous = event
-
-        # Don't forget the final event!
-        if previous is not None:
-            for token in self.tokens(previous, None):
-                yield token
-
-    def tokens(self, event, next):
-        kind, data, _ = event
-        if kind == START:
-            tag, attribs = data
-            name = tag.localname
-            namespace = tag.namespace
-            converted_attribs = {}
-            for k, v in attribs:
-                if isinstance(k, QName):
-                    converted_attribs[(k.namespace, k.localname)] = v
-                else:
-                    converted_attribs[(None, k)] = v
-
-            if namespace == namespaces["html"] and name in voidElements:
-                for token in self.emptyTag(namespace, name, converted_attribs,
-                                           not next or next[0] != END or
-                                           next[1] != tag):
-                    yield token
-            else:
-                yield self.startTag(namespace, name, converted_attribs)
-
-        elif kind == END:
-            name = data.localname
-            namespace = data.namespace
-            if namespace != namespaces["html"] or name not in voidElements:
-                yield self.endTag(namespace, name)
-
-        elif kind == COMMENT:
-            yield self.comment(data)
-
-        elif kind == TEXT:
-            for token in self.text(data):
-                yield token
-
-        elif kind == DOCTYPE:
-            yield self.doctype(*data)
-
-        elif kind in (XML_NAMESPACE, DOCTYPE, START_NS, END_NS,
-                      START_CDATA, END_CDATA, PI):
-            pass
-
-        else:
-            yield self.unknown(kind)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__init__.py
deleted file mode 100644
index 847bf93..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__init__.py
+++ /dev/null
@@ -1,2 +0,0 @@
-from .package_data import __version__
-from .core import *
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index a1d0411..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/core.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/core.cpython-37.pyc
deleted file mode 100644
index 963fb5f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/core.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/idnadata.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/idnadata.cpython-37.pyc
deleted file mode 100644
index c83ef17..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/idnadata.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/intranges.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/intranges.cpython-37.pyc
deleted file mode 100644
index 0d54126..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/intranges.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/package_data.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/package_data.cpython-37.pyc
deleted file mode 100644
index 5b4d3cc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/__pycache__/package_data.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/codec.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/codec.py
deleted file mode 100644
index 98c65ea..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/codec.py
+++ /dev/null
@@ -1,118 +0,0 @@
-from .core import encode, decode, alabel, ulabel, IDNAError
-import codecs
-import re
-
-_unicode_dots_re = re.compile(u'[\u002e\u3002\uff0e\uff61]')
-
-class Codec(codecs.Codec):
-
-    def encode(self, data, errors='strict'):
-
-        if errors != 'strict':
-            raise IDNAError("Unsupported error handling \"{0}\"".format(errors))
-
-        if not data:
-            return "", 0
-
-        return encode(data), len(data)
-
-    def decode(self, data, errors='strict'):
-
-        if errors != 'strict':
-            raise IDNAError("Unsupported error handling \"{0}\"".format(errors))
-
-        if not data:
-            return u"", 0
-
-        return decode(data), len(data)
-
-class IncrementalEncoder(codecs.BufferedIncrementalEncoder):
-    def _buffer_encode(self, data, errors, final):
-        if errors != 'strict':
-            raise IDNAError("Unsupported error handling \"{0}\"".format(errors))
-
-        if not data:
-            return ("", 0)
-
-        labels = _unicode_dots_re.split(data)
-        trailing_dot = u''
-        if labels:
-            if not labels[-1]:
-                trailing_dot = '.'
-                del labels[-1]
-            elif not final:
-                # Keep potentially unfinished label until the next call
-                del labels[-1]
-                if labels:
-                    trailing_dot = '.'
-
-        result = []
-        size = 0
-        for label in labels:
-            result.append(alabel(label))
-            if size:
-                size += 1
-            size += len(label)
-
-        # Join with U+002E
-        result = ".".join(result) + trailing_dot
-        size += len(trailing_dot)
-        return (result, size)
-
-class IncrementalDecoder(codecs.BufferedIncrementalDecoder):
-    def _buffer_decode(self, data, errors, final):
-        if errors != 'strict':
-            raise IDNAError("Unsupported error handling \"{0}\"".format(errors))
-
-        if not data:
-            return (u"", 0)
-
-        # IDNA allows decoding to operate on Unicode strings, too.
-        if isinstance(data, unicode):
-            labels = _unicode_dots_re.split(data)
-        else:
-            # Must be ASCII string
-            data = str(data)
-            unicode(data, "ascii")
-            labels = data.split(".")
-
-        trailing_dot = u''
-        if labels:
-            if not labels[-1]:
-                trailing_dot = u'.'
-                del labels[-1]
-            elif not final:
-                # Keep potentially unfinished label until the next call
-                del labels[-1]
-                if labels:
-                    trailing_dot = u'.'
-
-        result = []
-        size = 0
-        for label in labels:
-            result.append(ulabel(label))
-            if size:
-                size += 1
-            size += len(label)
-
-        result = u".".join(result) + trailing_dot
-        size += len(trailing_dot)
-        return (result, size)
-
-
-class StreamWriter(Codec, codecs.StreamWriter):
-    pass
-
-class StreamReader(Codec, codecs.StreamReader):
-    pass
-
-def getregentry():
-    return codecs.CodecInfo(
-        name='idna',
-        encode=Codec().encode,
-        decode=Codec().decode,
-        incrementalencoder=IncrementalEncoder,
-        incrementaldecoder=IncrementalDecoder,
-        streamwriter=StreamWriter,
-        streamreader=StreamReader,
-    )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/compat.py
deleted file mode 100644
index 4d47f33..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/compat.py
+++ /dev/null
@@ -1,12 +0,0 @@
-from .core import *
-from .codec import *
-
-def ToASCII(label):
-    return encode(label)
-
-def ToUnicode(label):
-    return decode(label)
-
-def nameprep(s):
-    raise NotImplementedError("IDNA 2008 does not utilise nameprep protocol")
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/core.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/core.py
deleted file mode 100644
index 104624a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/core.py
+++ /dev/null
@@ -1,396 +0,0 @@
-from . import idnadata
-import bisect
-import unicodedata
-import re
-import sys
-from .intranges import intranges_contain
-
-_virama_combining_class = 9
-_alabel_prefix = b'xn--'
-_unicode_dots_re = re.compile(u'[\u002e\u3002\uff0e\uff61]')
-
-if sys.version_info[0] == 3:
-    unicode = str
-    unichr = chr
-
-class IDNAError(UnicodeError):
-    """ Base exception for all IDNA-encoding related problems """
-    pass
-
-
-class IDNABidiError(IDNAError):
-    """ Exception when bidirectional requirements are not satisfied """
-    pass
-
-
-class InvalidCodepoint(IDNAError):
-    """ Exception when a disallowed or unallocated codepoint is used """
-    pass
-
-
-class InvalidCodepointContext(IDNAError):
-    """ Exception when the codepoint is not valid in the context it is used """
-    pass
-
-
-def _combining_class(cp):
-    v = unicodedata.combining(unichr(cp))
-    if v == 0:
-        if not unicodedata.name(unichr(cp)):
-            raise ValueError("Unknown character in unicodedata")
-    return v
-
-def _is_script(cp, script):
-    return intranges_contain(ord(cp), idnadata.scripts[script])
-
-def _punycode(s):
-    return s.encode('punycode')
-
-def _unot(s):
-    return 'U+{0:04X}'.format(s)
-
-
-def valid_label_length(label):
-
-    if len(label) > 63:
-        return False
-    return True
-
-
-def valid_string_length(label, trailing_dot):
-
-    if len(label) > (254 if trailing_dot else 253):
-        return False
-    return True
-
-
-def check_bidi(label, check_ltr=False):
-
-    # Bidi rules should only be applied if string contains RTL characters
-    bidi_label = False
-    for (idx, cp) in enumerate(label, 1):
-        direction = unicodedata.bidirectional(cp)
-        if direction == '':
-            # String likely comes from a newer version of Unicode
-            raise IDNABidiError('Unknown directionality in label {0} at position {1}'.format(repr(label), idx))
-        if direction in ['R', 'AL', 'AN']:
-            bidi_label = True
-    if not bidi_label and not check_ltr:
-        return True
-
-    # Bidi rule 1
-    direction = unicodedata.bidirectional(label[0])
-    if direction in ['R', 'AL']:
-        rtl = True
-    elif direction == 'L':
-        rtl = False
-    else:
-        raise IDNABidiError('First codepoint in label {0} must be directionality L, R or AL'.format(repr(label)))
-
-    valid_ending = False
-    number_type = False
-    for (idx, cp) in enumerate(label, 1):
-        direction = unicodedata.bidirectional(cp)
-
-        if rtl:
-            # Bidi rule 2
-            if not direction in ['R', 'AL', 'AN', 'EN', 'ES', 'CS', 'ET', 'ON', 'BN', 'NSM']:
-                raise IDNABidiError('Invalid direction for codepoint at position {0} in a right-to-left label'.format(idx))
-            # Bidi rule 3
-            if direction in ['R', 'AL', 'EN', 'AN']:
-                valid_ending = True
-            elif direction != 'NSM':
-                valid_ending = False
-            # Bidi rule 4
-            if direction in ['AN', 'EN']:
-                if not number_type:
-                    number_type = direction
-                else:
-                    if number_type != direction:
-                        raise IDNABidiError('Can not mix numeral types in a right-to-left label')
-        else:
-            # Bidi rule 5
-            if not direction in ['L', 'EN', 'ES', 'CS', 'ET', 'ON', 'BN', 'NSM']:
-                raise IDNABidiError('Invalid direction for codepoint at position {0} in a left-to-right label'.format(idx))
-            # Bidi rule 6
-            if direction in ['L', 'EN']:
-                valid_ending = True
-            elif direction != 'NSM':
-                valid_ending = False
-
-    if not valid_ending:
-        raise IDNABidiError('Label ends with illegal codepoint directionality')
-
-    return True
-
-
-def check_initial_combiner(label):
-
-    if unicodedata.category(label[0])[0] == 'M':
-        raise IDNAError('Label begins with an illegal combining character')
-    return True
-
-
-def check_hyphen_ok(label):
-
-    if label[2:4] == '--':
-        raise IDNAError('Label has disallowed hyphens in 3rd and 4th position')
-    if label[0] == '-' or label[-1] == '-':
-        raise IDNAError('Label must not start or end with a hyphen')
-    return True
-
-
-def check_nfc(label):
-
-    if unicodedata.normalize('NFC', label) != label:
-        raise IDNAError('Label must be in Normalization Form C')
-
-
-def valid_contextj(label, pos):
-
-    cp_value = ord(label[pos])
-
-    if cp_value == 0x200c:
-
-        if pos > 0:
-            if _combining_class(ord(label[pos - 1])) == _virama_combining_class:
-                return True
-
-        ok = False
-        for i in range(pos-1, -1, -1):
-            joining_type = idnadata.joining_types.get(ord(label[i]))
-            if joining_type == ord('T'):
-                continue
-            if joining_type in [ord('L'), ord('D')]:
-                ok = True
-                break
-
-        if not ok:
-            return False
-
-        ok = False
-        for i in range(pos+1, len(label)):
-            joining_type = idnadata.joining_types.get(ord(label[i]))
-            if joining_type == ord('T'):
-                continue
-            if joining_type in [ord('R'), ord('D')]:
-                ok = True
-                break
-        return ok
-
-    if cp_value == 0x200d:
-
-        if pos > 0:
-            if _combining_class(ord(label[pos - 1])) == _virama_combining_class:
-                return True
-        return False
-
-    else:
-
-        return False
-
-
-def valid_contexto(label, pos, exception=False):
-
-    cp_value = ord(label[pos])
-
-    if cp_value == 0x00b7:
-        if 0 < pos < len(label)-1:
-            if ord(label[pos - 1]) == 0x006c and ord(label[pos + 1]) == 0x006c:
-                return True
-        return False
-
-    elif cp_value == 0x0375:
-        if pos < len(label)-1 and len(label) > 1:
-            return _is_script(label[pos + 1], 'Greek')
-        return False
-
-    elif cp_value == 0x05f3 or cp_value == 0x05f4:
-        if pos > 0:
-            return _is_script(label[pos - 1], 'Hebrew')
-        return False
-
-    elif cp_value == 0x30fb:
-        for cp in label:
-            if cp == u'\u30fb':
-                continue
-            if _is_script(cp, 'Hiragana') or _is_script(cp, 'Katakana') or _is_script(cp, 'Han'):
-                return True
-        return False
-
-    elif 0x660 <= cp_value <= 0x669:
-        for cp in label:
-            if 0x6f0 <= ord(cp) <= 0x06f9:
-                return False
-        return True
-
-    elif 0x6f0 <= cp_value <= 0x6f9:
-        for cp in label:
-            if 0x660 <= ord(cp) <= 0x0669:
-                return False
-        return True
-
-
-def check_label(label):
-
-    if isinstance(label, (bytes, bytearray)):
-        label = label.decode('utf-8')
-    if len(label) == 0:
-        raise IDNAError('Empty Label')
-
-    check_nfc(label)
-    check_hyphen_ok(label)
-    check_initial_combiner(label)
-
-    for (pos, cp) in enumerate(label):
-        cp_value = ord(cp)
-        if intranges_contain(cp_value, idnadata.codepoint_classes['PVALID']):
-            continue
-        elif intranges_contain(cp_value, idnadata.codepoint_classes['CONTEXTJ']):
-            try:
-                if not valid_contextj(label, pos):
-                    raise InvalidCodepointContext('Joiner {0} not allowed at position {1} in {2}'.format(
-                        _unot(cp_value), pos+1, repr(label)))
-            except ValueError:
-                raise IDNAError('Unknown codepoint adjacent to joiner {0} at position {1} in {2}'.format(
-                    _unot(cp_value), pos+1, repr(label)))
-        elif intranges_contain(cp_value, idnadata.codepoint_classes['CONTEXTO']):
-            if not valid_contexto(label, pos):
-                raise InvalidCodepointContext('Codepoint {0} not allowed at position {1} in {2}'.format(_unot(cp_value), pos+1, repr(label)))
-        else:
-            raise InvalidCodepoint('Codepoint {0} at position {1} of {2} not allowed'.format(_unot(cp_value), pos+1, repr(label)))
-
-    check_bidi(label)
-
-
-def alabel(label):
-
-    try:
-        label = label.encode('ascii')
-        ulabel(label)
-        if not valid_label_length(label):
-            raise IDNAError('Label too long')
-        return label
-    except UnicodeEncodeError:
-        pass
-
-    if not label:
-        raise IDNAError('No Input')
-
-    label = unicode(label)
-    check_label(label)
-    label = _punycode(label)
-    label = _alabel_prefix + label
-
-    if not valid_label_length(label):
-        raise IDNAError('Label too long')
-
-    return label
-
-
-def ulabel(label):
-
-    if not isinstance(label, (bytes, bytearray)):
-        try:
-            label = label.encode('ascii')
-        except UnicodeEncodeError:
-            check_label(label)
-            return label
-
-    label = label.lower()
-    if label.startswith(_alabel_prefix):
-        label = label[len(_alabel_prefix):]
-    else:
-        check_label(label)
-        return label.decode('ascii')
-
-    label = label.decode('punycode')
-    check_label(label)
-    return label
-
-
-def uts46_remap(domain, std3_rules=True, transitional=False):
-    """Re-map the characters in the string according to UTS46 processing."""
-    from .uts46data import uts46data
-    output = u""
-    try:
-        for pos, char in enumerate(domain):
-            code_point = ord(char)
-            uts46row = uts46data[code_point if code_point < 256 else
-                bisect.bisect_left(uts46data, (code_point, "Z")) - 1]
-            status = uts46row[1]
-            replacement = uts46row[2] if len(uts46row) == 3 else None
-            if (status == "V" or
-                    (status == "D" and not transitional) or
-                    (status == "3" and not std3_rules and replacement is None)):
-                output += char
-            elif replacement is not None and (status == "M" or
-                    (status == "3" and not std3_rules) or
-                    (status == "D" and transitional)):
-                output += replacement
-            elif status != "I":
-                raise IndexError()
-        return unicodedata.normalize("NFC", output)
-    except IndexError:
-        raise InvalidCodepoint(
-            "Codepoint {0} not allowed at position {1} in {2}".format(
-            _unot(code_point), pos + 1, repr(domain)))
-
-
-def encode(s, strict=False, uts46=False, std3_rules=False, transitional=False):
-
-    if isinstance(s, (bytes, bytearray)):
-        s = s.decode("ascii")
-    if uts46:
-        s = uts46_remap(s, std3_rules, transitional)
-    trailing_dot = False
-    result = []
-    if strict:
-        labels = s.split('.')
-    else:
-        labels = _unicode_dots_re.split(s)
-    if not labels or labels == ['']:
-        raise IDNAError('Empty domain')
-    if labels[-1] == '':
-        del labels[-1]
-        trailing_dot = True
-    for label in labels:
-        s = alabel(label)
-        if s:
-            result.append(s)
-        else:
-            raise IDNAError('Empty label')
-    if trailing_dot:
-        result.append(b'')
-    s = b'.'.join(result)
-    if not valid_string_length(s, trailing_dot):
-        raise IDNAError('Domain too long')
-    return s
-
-
-def decode(s, strict=False, uts46=False, std3_rules=False):
-
-    if isinstance(s, (bytes, bytearray)):
-        s = s.decode("ascii")
-    if uts46:
-        s = uts46_remap(s, std3_rules, False)
-    trailing_dot = False
-    result = []
-    if not strict:
-        labels = _unicode_dots_re.split(s)
-    else:
-        labels = s.split(u'.')
-    if not labels or labels == ['']:
-        raise IDNAError('Empty domain')
-    if not labels[-1]:
-        del labels[-1]
-        trailing_dot = True
-    for label in labels:
-        s = ulabel(label)
-        if s:
-            result.append(s)
-        else:
-            raise IDNAError('Empty label')
-    if trailing_dot:
-        result.append(u'')
-    return u'.'.join(result)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/idnadata.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/idnadata.py
deleted file mode 100644
index a80c959..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/idnadata.py
+++ /dev/null
@@ -1,1979 +0,0 @@
-# This file is automatically generated by tools/idna-data
-
-__version__ = "11.0.0"
-scripts = {
-    'Greek': (
-        0x37000000374,
-        0x37500000378,
-        0x37a0000037e,
-        0x37f00000380,
-        0x38400000385,
-        0x38600000387,
-        0x3880000038b,
-        0x38c0000038d,
-        0x38e000003a2,
-        0x3a3000003e2,
-        0x3f000000400,
-        0x1d2600001d2b,
-        0x1d5d00001d62,
-        0x1d6600001d6b,
-        0x1dbf00001dc0,
-        0x1f0000001f16,
-        0x1f1800001f1e,
-        0x1f2000001f46,
-        0x1f4800001f4e,
-        0x1f5000001f58,
-        0x1f5900001f5a,
-        0x1f5b00001f5c,
-        0x1f5d00001f5e,
-        0x1f5f00001f7e,
-        0x1f8000001fb5,
-        0x1fb600001fc5,
-        0x1fc600001fd4,
-        0x1fd600001fdc,
-        0x1fdd00001ff0,
-        0x1ff200001ff5,
-        0x1ff600001fff,
-        0x212600002127,
-        0xab650000ab66,
-        0x101400001018f,
-        0x101a0000101a1,
-        0x1d2000001d246,
-    ),
-    'Han': (
-        0x2e8000002e9a,
-        0x2e9b00002ef4,
-        0x2f0000002fd6,
-        0x300500003006,
-        0x300700003008,
-        0x30210000302a,
-        0x30380000303c,
-        0x340000004db6,
-        0x4e0000009ff0,
-        0xf9000000fa6e,
-        0xfa700000fada,
-        0x200000002a6d7,
-        0x2a7000002b735,
-        0x2b7400002b81e,
-        0x2b8200002cea2,
-        0x2ceb00002ebe1,
-        0x2f8000002fa1e,
-    ),
-    'Hebrew': (
-        0x591000005c8,
-        0x5d0000005eb,
-        0x5ef000005f5,
-        0xfb1d0000fb37,
-        0xfb380000fb3d,
-        0xfb3e0000fb3f,
-        0xfb400000fb42,
-        0xfb430000fb45,
-        0xfb460000fb50,
-    ),
-    'Hiragana': (
-        0x304100003097,
-        0x309d000030a0,
-        0x1b0010001b11f,
-        0x1f2000001f201,
-    ),
-    'Katakana': (
-        0x30a1000030fb,
-        0x30fd00003100,
-        0x31f000003200,
-        0x32d0000032ff,
-        0x330000003358,
-        0xff660000ff70,
-        0xff710000ff9e,
-        0x1b0000001b001,
-    ),
-}
-joining_types = {
-    0x600: 85,
-    0x601: 85,
-    0x602: 85,
-    0x603: 85,
-    0x604: 85,
-    0x605: 85,
-    0x608: 85,
-    0x60b: 85,
-    0x620: 68,
-    0x621: 85,
-    0x622: 82,
-    0x623: 82,
-    0x624: 82,
-    0x625: 82,
-    0x626: 68,
-    0x627: 82,
-    0x628: 68,
-    0x629: 82,
-    0x62a: 68,
-    0x62b: 68,
-    0x62c: 68,
-    0x62d: 68,
-    0x62e: 68,
-    0x62f: 82,
-    0x630: 82,
-    0x631: 82,
-    0x632: 82,
-    0x633: 68,
-    0x634: 68,
-    0x635: 68,
-    0x636: 68,
-    0x637: 68,
-    0x638: 68,
-    0x639: 68,
-    0x63a: 68,
-    0x63b: 68,
-    0x63c: 68,
-    0x63d: 68,
-    0x63e: 68,
-    0x63f: 68,
-    0x640: 67,
-    0x641: 68,
-    0x642: 68,
-    0x643: 68,
-    0x644: 68,
-    0x645: 68,
-    0x646: 68,
-    0x647: 68,
-    0x648: 82,
-    0x649: 68,
-    0x64a: 68,
-    0x66e: 68,
-    0x66f: 68,
-    0x671: 82,
-    0x672: 82,
-    0x673: 82,
-    0x674: 85,
-    0x675: 82,
-    0x676: 82,
-    0x677: 82,
-    0x678: 68,
-    0x679: 68,
-    0x67a: 68,
-    0x67b: 68,
-    0x67c: 68,
-    0x67d: 68,
-    0x67e: 68,
-    0x67f: 68,
-    0x680: 68,
-    0x681: 68,
-    0x682: 68,
-    0x683: 68,
-    0x684: 68,
-    0x685: 68,
-    0x686: 68,
-    0x687: 68,
-    0x688: 82,
-    0x689: 82,
-    0x68a: 82,
-    0x68b: 82,
-    0x68c: 82,
-    0x68d: 82,
-    0x68e: 82,
-    0x68f: 82,
-    0x690: 82,
-    0x691: 82,
-    0x692: 82,
-    0x693: 82,
-    0x694: 82,
-    0x695: 82,
-    0x696: 82,
-    0x697: 82,
-    0x698: 82,
-    0x699: 82,
-    0x69a: 68,
-    0x69b: 68,
-    0x69c: 68,
-    0x69d: 68,
-    0x69e: 68,
-    0x69f: 68,
-    0x6a0: 68,
-    0x6a1: 68,
-    0x6a2: 68,
-    0x6a3: 68,
-    0x6a4: 68,
-    0x6a5: 68,
-    0x6a6: 68,
-    0x6a7: 68,
-    0x6a8: 68,
-    0x6a9: 68,
-    0x6aa: 68,
-    0x6ab: 68,
-    0x6ac: 68,
-    0x6ad: 68,
-    0x6ae: 68,
-    0x6af: 68,
-    0x6b0: 68,
-    0x6b1: 68,
-    0x6b2: 68,
-    0x6b3: 68,
-    0x6b4: 68,
-    0x6b5: 68,
-    0x6b6: 68,
-    0x6b7: 68,
-    0x6b8: 68,
-    0x6b9: 68,
-    0x6ba: 68,
-    0x6bb: 68,
-    0x6bc: 68,
-    0x6bd: 68,
-    0x6be: 68,
-    0x6bf: 68,
-    0x6c0: 82,
-    0x6c1: 68,
-    0x6c2: 68,
-    0x6c3: 82,
-    0x6c4: 82,
-    0x6c5: 82,
-    0x6c6: 82,
-    0x6c7: 82,
-    0x6c8: 82,
-    0x6c9: 82,
-    0x6ca: 82,
-    0x6cb: 82,
-    0x6cc: 68,
-    0x6cd: 82,
-    0x6ce: 68,
-    0x6cf: 82,
-    0x6d0: 68,
-    0x6d1: 68,
-    0x6d2: 82,
-    0x6d3: 82,
-    0x6d5: 82,
-    0x6dd: 85,
-    0x6ee: 82,
-    0x6ef: 82,
-    0x6fa: 68,
-    0x6fb: 68,
-    0x6fc: 68,
-    0x6ff: 68,
-    0x70f: 84,
-    0x710: 82,
-    0x712: 68,
-    0x713: 68,
-    0x714: 68,
-    0x715: 82,
-    0x716: 82,
-    0x717: 82,
-    0x718: 82,
-    0x719: 82,
-    0x71a: 68,
-    0x71b: 68,
-    0x71c: 68,
-    0x71d: 68,
-    0x71e: 82,
-    0x71f: 68,
-    0x720: 68,
-    0x721: 68,
-    0x722: 68,
-    0x723: 68,
-    0x724: 68,
-    0x725: 68,
-    0x726: 68,
-    0x727: 68,
-    0x728: 82,
-    0x729: 68,
-    0x72a: 82,
-    0x72b: 68,
-    0x72c: 82,
-    0x72d: 68,
-    0x72e: 68,
-    0x72f: 82,
-    0x74d: 82,
-    0x74e: 68,
-    0x74f: 68,
-    0x750: 68,
-    0x751: 68,
-    0x752: 68,
-    0x753: 68,
-    0x754: 68,
-    0x755: 68,
-    0x756: 68,
-    0x757: 68,
-    0x758: 68,
-    0x759: 82,
-    0x75a: 82,
-    0x75b: 82,
-    0x75c: 68,
-    0x75d: 68,
-    0x75e: 68,
-    0x75f: 68,
-    0x760: 68,
-    0x761: 68,
-    0x762: 68,
-    0x763: 68,
-    0x764: 68,
-    0x765: 68,
-    0x766: 68,
-    0x767: 68,
-    0x768: 68,
-    0x769: 68,
-    0x76a: 68,
-    0x76b: 82,
-    0x76c: 82,
-    0x76d: 68,
-    0x76e: 68,
-    0x76f: 68,
-    0x770: 68,
-    0x771: 82,
-    0x772: 68,
-    0x773: 82,
-    0x774: 82,
-    0x775: 68,
-    0x776: 68,
-    0x777: 68,
-    0x778: 82,
-    0x779: 82,
-    0x77a: 68,
-    0x77b: 68,
-    0x77c: 68,
-    0x77d: 68,
-    0x77e: 68,
-    0x77f: 68,
-    0x7ca: 68,
-    0x7cb: 68,
-    0x7cc: 68,
-    0x7cd: 68,
-    0x7ce: 68,
-    0x7cf: 68,
-    0x7d0: 68,
-    0x7d1: 68,
-    0x7d2: 68,
-    0x7d3: 68,
-    0x7d4: 68,
-    0x7d5: 68,
-    0x7d6: 68,
-    0x7d7: 68,
-    0x7d8: 68,
-    0x7d9: 68,
-    0x7da: 68,
-    0x7db: 68,
-    0x7dc: 68,
-    0x7dd: 68,
-    0x7de: 68,
-    0x7df: 68,
-    0x7e0: 68,
-    0x7e1: 68,
-    0x7e2: 68,
-    0x7e3: 68,
-    0x7e4: 68,
-    0x7e5: 68,
-    0x7e6: 68,
-    0x7e7: 68,
-    0x7e8: 68,
-    0x7e9: 68,
-    0x7ea: 68,
-    0x7fa: 67,
-    0x840: 82,
-    0x841: 68,
-    0x842: 68,
-    0x843: 68,
-    0x844: 68,
-    0x845: 68,
-    0x846: 82,
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/intranges.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/intranges.py
deleted file mode 100644
index fa8a735..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/intranges.py
+++ /dev/null
@@ -1,53 +0,0 @@
-"""
-Given a list of integers, made up of (hopefully) a small number of long runs
-of consecutive integers, compute a representation of the form
-((start1, end1), (start2, end2) ...). Then answer the question "was x present
-in the original list?" in time O(log(# runs)).
-"""
-
-import bisect
-
-def intranges_from_list(list_):
-    """Represent a list of integers as a sequence of ranges:
-    ((start_0, end_0), (start_1, end_1), ...), such that the original
-    integers are exactly those x such that start_i <= x < end_i for some i.
-
-    Ranges are encoded as single integers (start << 32 | end), not as tuples.
-    """
-
-    sorted_list = sorted(list_)
-    ranges = []
-    last_write = -1
-    for i in range(len(sorted_list)):
-        if i+1 < len(sorted_list):
-            if sorted_list[i] == sorted_list[i+1]-1:
-                continue
-        current_range = sorted_list[last_write+1:i+1]
-        ranges.append(_encode_range(current_range[0], current_range[-1] + 1))
-        last_write = i
-
-    return tuple(ranges)
-
-def _encode_range(start, end):
-    return (start << 32) | end
-
-def _decode_range(r):
-    return (r >> 32), (r & ((1 << 32) - 1))
-
-
-def intranges_contain(int_, ranges):
-    """Determine if `int_` falls into one of the ranges in `ranges`."""
-    tuple_ = _encode_range(int_, 0)
-    pos = bisect.bisect_left(ranges, tuple_)
-    # we could be immediately ahead of a tuple (start, end)
-    # with start < int_ <= end
-    if pos > 0:
-        left, right = _decode_range(ranges[pos-1])
-        if left <= int_ < right:
-            return True
-    # or we could be immediately behind a tuple (int_, end)
-    if pos < len(ranges):
-        left, _ = _decode_range(ranges[pos])
-        if left == int_:
-            return True
-    return False
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/package_data.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/package_data.py
deleted file mode 100644
index 257e898..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/package_data.py
+++ /dev/null
@@ -1,2 +0,0 @@
-__version__ = '2.8'
-
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/uts46data.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/uts46data.py
deleted file mode 100644
index a68ed4c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/idna/uts46data.py
+++ /dev/null
@@ -1,8205 +0,0 @@
-# This file is automatically generated by tools/idna-data
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-
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diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/ipaddress.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/ipaddress.py
deleted file mode 100644
index f2d0766..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/ipaddress.py
+++ /dev/null
@@ -1,2419 +0,0 @@
-# Copyright 2007 Google Inc.
-#  Licensed to PSF under a Contributor Agreement.
-
-"""A fast, lightweight IPv4/IPv6 manipulation library in Python.
-
-This library is used to create/poke/manipulate IPv4 and IPv6 addresses
-and networks.
-
-"""
-
-from __future__ import unicode_literals
-
-
-import itertools
-import struct
-
-__version__ = '1.0.22'
-
-# Compatibility functions
-_compat_int_types = (int,)
-try:
-    _compat_int_types = (int, long)
-except NameError:
-    pass
-try:
-    _compat_str = unicode
-except NameError:
-    _compat_str = str
-    assert bytes != str
-if b'\0'[0] == 0:  # Python 3 semantics
-    def _compat_bytes_to_byte_vals(byt):
-        return byt
-else:
-    def _compat_bytes_to_byte_vals(byt):
-        return [struct.unpack(b'!B', b)[0] for b in byt]
-try:
-    _compat_int_from_byte_vals = int.from_bytes
-except AttributeError:
-    def _compat_int_from_byte_vals(bytvals, endianess):
-        assert endianess == 'big'
-        res = 0
-        for bv in bytvals:
-            assert isinstance(bv, _compat_int_types)
-            res = (res << 8) + bv
-        return res
-
-
-def _compat_to_bytes(intval, length, endianess):
-    assert isinstance(intval, _compat_int_types)
-    assert endianess == 'big'
-    if length == 4:
-        if intval < 0 or intval >= 2 ** 32:
-            raise struct.error("integer out of range for 'I' format code")
-        return struct.pack(b'!I', intval)
-    elif length == 16:
-        if intval < 0 or intval >= 2 ** 128:
-            raise struct.error("integer out of range for 'QQ' format code")
-        return struct.pack(b'!QQ', intval >> 64, intval & 0xffffffffffffffff)
-    else:
-        raise NotImplementedError()
-
-
-if hasattr(int, 'bit_length'):
-    # Not int.bit_length , since that won't work in 2.7 where long exists
-    def _compat_bit_length(i):
-        return i.bit_length()
-else:
-    def _compat_bit_length(i):
-        for res in itertools.count():
-            if i >> res == 0:
-                return res
-
-
-def _compat_range(start, end, step=1):
-    assert step > 0
-    i = start
-    while i < end:
-        yield i
-        i += step
-
-
-class _TotalOrderingMixin(object):
-    __slots__ = ()
-
-    # Helper that derives the other comparison operations from
-    # __lt__ and __eq__
-    # We avoid functools.total_ordering because it doesn't handle
-    # NotImplemented correctly yet (http://bugs.python.org/issue10042)
-    def __eq__(self, other):
-        raise NotImplementedError
-
-    def __ne__(self, other):
-        equal = self.__eq__(other)
-        if equal is NotImplemented:
-            return NotImplemented
-        return not equal
-
-    def __lt__(self, other):
-        raise NotImplementedError
-
-    def __le__(self, other):
-        less = self.__lt__(other)
-        if less is NotImplemented or not less:
-            return self.__eq__(other)
-        return less
-
-    def __gt__(self, other):
-        less = self.__lt__(other)
-        if less is NotImplemented:
-            return NotImplemented
-        equal = self.__eq__(other)
-        if equal is NotImplemented:
-            return NotImplemented
-        return not (less or equal)
-
-    def __ge__(self, other):
-        less = self.__lt__(other)
-        if less is NotImplemented:
-            return NotImplemented
-        return not less
-
-
-IPV4LENGTH = 32
-IPV6LENGTH = 128
-
-
-class AddressValueError(ValueError):
-    """A Value Error related to the address."""
-
-
-class NetmaskValueError(ValueError):
-    """A Value Error related to the netmask."""
-
-
-def ip_address(address):
-    """Take an IP string/int and return an object of the correct type.
-
-    Args:
-        address: A string or integer, the IP address.  Either IPv4 or
-          IPv6 addresses may be supplied; integers less than 2**32 will
-          be considered to be IPv4 by default.
-
-    Returns:
-        An IPv4Address or IPv6Address object.
-
-    Raises:
-        ValueError: if the *address* passed isn't either a v4 or a v6
-          address
-
-    """
-    try:
-        return IPv4Address(address)
-    except (AddressValueError, NetmaskValueError):
-        pass
-
-    try:
-        return IPv6Address(address)
-    except (AddressValueError, NetmaskValueError):
-        pass
-
-    if isinstance(address, bytes):
-        raise AddressValueError(
-            '%r does not appear to be an IPv4 or IPv6 address. '
-            'Did you pass in a bytes (str in Python 2) instead of'
-            ' a unicode object?' % address)
-
-    raise ValueError('%r does not appear to be an IPv4 or IPv6 address' %
-                     address)
-
-
-def ip_network(address, strict=True):
-    """Take an IP string/int and return an object of the correct type.
-
-    Args:
-        address: A string or integer, the IP network.  Either IPv4 or
-          IPv6 networks may be supplied; integers less than 2**32 will
-          be considered to be IPv4 by default.
-
-    Returns:
-        An IPv4Network or IPv6Network object.
-
-    Raises:
-        ValueError: if the string passed isn't either a v4 or a v6
-          address. Or if the network has host bits set.
-
-    """
-    try:
-        return IPv4Network(address, strict)
-    except (AddressValueError, NetmaskValueError):
-        pass
-
-    try:
-        return IPv6Network(address, strict)
-    except (AddressValueError, NetmaskValueError):
-        pass
-
-    if isinstance(address, bytes):
-        raise AddressValueError(
-            '%r does not appear to be an IPv4 or IPv6 network. '
-            'Did you pass in a bytes (str in Python 2) instead of'
-            ' a unicode object?' % address)
-
-    raise ValueError('%r does not appear to be an IPv4 or IPv6 network' %
-                     address)
-
-
-def ip_interface(address):
-    """Take an IP string/int and return an object of the correct type.
-
-    Args:
-        address: A string or integer, the IP address.  Either IPv4 or
-          IPv6 addresses may be supplied; integers less than 2**32 will
-          be considered to be IPv4 by default.
-
-    Returns:
-        An IPv4Interface or IPv6Interface object.
-
-    Raises:
-        ValueError: if the string passed isn't either a v4 or a v6
-          address.
-
-    Notes:
-        The IPv?Interface classes describe an Address on a particular
-        Network, so they're basically a combination of both the Address
-        and Network classes.
-
-    """
-    try:
-        return IPv4Interface(address)
-    except (AddressValueError, NetmaskValueError):
-        pass
-
-    try:
-        return IPv6Interface(address)
-    except (AddressValueError, NetmaskValueError):
-        pass
-
-    raise ValueError('%r does not appear to be an IPv4 or IPv6 interface' %
-                     address)
-
-
-def v4_int_to_packed(address):
-    """Represent an address as 4 packed bytes in network (big-endian) order.
-
-    Args:
-        address: An integer representation of an IPv4 IP address.
-
-    Returns:
-        The integer address packed as 4 bytes in network (big-endian) order.
-
-    Raises:
-        ValueError: If the integer is negative or too large to be an
-          IPv4 IP address.
-
-    """
-    try:
-        return _compat_to_bytes(address, 4, 'big')
-    except (struct.error, OverflowError):
-        raise ValueError("Address negative or too large for IPv4")
-
-
-def v6_int_to_packed(address):
-    """Represent an address as 16 packed bytes in network (big-endian) order.
-
-    Args:
-        address: An integer representation of an IPv6 IP address.
-
-    Returns:
-        The integer address packed as 16 bytes in network (big-endian) order.
-
-    """
-    try:
-        return _compat_to_bytes(address, 16, 'big')
-    except (struct.error, OverflowError):
-        raise ValueError("Address negative or too large for IPv6")
-
-
-def _split_optional_netmask(address):
-    """Helper to split the netmask and raise AddressValueError if needed"""
-    addr = _compat_str(address).split('/')
-    if len(addr) > 2:
-        raise AddressValueError("Only one '/' permitted in %r" % address)
-    return addr
-
-
-def _find_address_range(addresses):
-    """Find a sequence of sorted deduplicated IPv#Address.
-
-    Args:
-        addresses: a list of IPv#Address objects.
-
-    Yields:
-        A tuple containing the first and last IP addresses in the sequence.
-
-    """
-    it = iter(addresses)
-    first = last = next(it)
-    for ip in it:
-        if ip._ip != last._ip + 1:
-            yield first, last
-            first = ip
-        last = ip
-    yield first, last
-
-
-def _count_righthand_zero_bits(number, bits):
-    """Count the number of zero bits on the right hand side.
-
-    Args:
-        number: an integer.
-        bits: maximum number of bits to count.
-
-    Returns:
-        The number of zero bits on the right hand side of the number.
-
-    """
-    if number == 0:
-        return bits
-    return min(bits, _compat_bit_length(~number & (number - 1)))
-
-
-def summarize_address_range(first, last):
-    """Summarize a network range given the first and last IP addresses.
-
-    Example:
-        >>> list(summarize_address_range(IPv4Address('192.0.2.0'),
-        ...                              IPv4Address('192.0.2.130')))
-        ...                                #doctest: +NORMALIZE_WHITESPACE
-        [IPv4Network('192.0.2.0/25'), IPv4Network('192.0.2.128/31'),
-         IPv4Network('192.0.2.130/32')]
-
-    Args:
-        first: the first IPv4Address or IPv6Address in the range.
-        last: the last IPv4Address or IPv6Address in the range.
-
-    Returns:
-        An iterator of the summarized IPv(4|6) network objects.
-
-    Raise:
-        TypeError:
-            If the first and last objects are not IP addresses.
-            If the first and last objects are not the same version.
-        ValueError:
-            If the last object is not greater than the first.
-            If the version of the first address is not 4 or 6.
-
-    """
-    if (not (isinstance(first, _BaseAddress) and
-             isinstance(last, _BaseAddress))):
-        raise TypeError('first and last must be IP addresses, not networks')
-    if first.version != last.version:
-        raise TypeError("%s and %s are not of the same version" % (
-                        first, last))
-    if first > last:
-        raise ValueError('last IP address must be greater than first')
-
-    if first.version == 4:
-        ip = IPv4Network
-    elif first.version == 6:
-        ip = IPv6Network
-    else:
-        raise ValueError('unknown IP version')
-
-    ip_bits = first._max_prefixlen
-    first_int = first._ip
-    last_int = last._ip
-    while first_int <= last_int:
-        nbits = min(_count_righthand_zero_bits(first_int, ip_bits),
-                    _compat_bit_length(last_int - first_int + 1) - 1)
-        net = ip((first_int, ip_bits - nbits))
-        yield net
-        first_int += 1 << nbits
-        if first_int - 1 == ip._ALL_ONES:
-            break
-
-
-def _collapse_addresses_internal(addresses):
-    """Loops through the addresses, collapsing concurrent netblocks.
-
-    Example:
-
-        ip1 = IPv4Network('192.0.2.0/26')
-        ip2 = IPv4Network('192.0.2.64/26')
-        ip3 = IPv4Network('192.0.2.128/26')
-        ip4 = IPv4Network('192.0.2.192/26')
-
-        _collapse_addresses_internal([ip1, ip2, ip3, ip4]) ->
-          [IPv4Network('192.0.2.0/24')]
-
-        This shouldn't be called directly; it is called via
-          collapse_addresses([]).
-
-    Args:
-        addresses: A list of IPv4Network's or IPv6Network's
-
-    Returns:
-        A list of IPv4Network's or IPv6Network's depending on what we were
-        passed.
-
-    """
-    # First merge
-    to_merge = list(addresses)
-    subnets = {}
-    while to_merge:
-        net = to_merge.pop()
-        supernet = net.supernet()
-        existing = subnets.get(supernet)
-        if existing is None:
-            subnets[supernet] = net
-        elif existing != net:
-            # Merge consecutive subnets
-            del subnets[supernet]
-            to_merge.append(supernet)
-    # Then iterate over resulting networks, skipping subsumed subnets
-    last = None
-    for net in sorted(subnets.values()):
-        if last is not None:
-            # Since they are sorted,
-            # last.network_address <= net.network_address is a given.
-            if last.broadcast_address >= net.broadcast_address:
-                continue
-        yield net
-        last = net
-
-
-def collapse_addresses(addresses):
-    """Collapse a list of IP objects.
-
-    Example:
-        collapse_addresses([IPv4Network('192.0.2.0/25'),
-                            IPv4Network('192.0.2.128/25')]) ->
-                           [IPv4Network('192.0.2.0/24')]
-
-    Args:
-        addresses: An iterator of IPv4Network or IPv6Network objects.
-
-    Returns:
-        An iterator of the collapsed IPv(4|6)Network objects.
-
-    Raises:
-        TypeError: If passed a list of mixed version objects.
-
-    """
-    addrs = []
-    ips = []
-    nets = []
-
-    # split IP addresses and networks
-    for ip in addresses:
-        if isinstance(ip, _BaseAddress):
-            if ips and ips[-1]._version != ip._version:
-                raise TypeError("%s and %s are not of the same version" % (
-                                ip, ips[-1]))
-            ips.append(ip)
-        elif ip._prefixlen == ip._max_prefixlen:
-            if ips and ips[-1]._version != ip._version:
-                raise TypeError("%s and %s are not of the same version" % (
-                                ip, ips[-1]))
-            try:
-                ips.append(ip.ip)
-            except AttributeError:
-                ips.append(ip.network_address)
-        else:
-            if nets and nets[-1]._version != ip._version:
-                raise TypeError("%s and %s are not of the same version" % (
-                                ip, nets[-1]))
-            nets.append(ip)
-
-    # sort and dedup
-    ips = sorted(set(ips))
-
-    # find consecutive address ranges in the sorted sequence and summarize them
-    if ips:
-        for first, last in _find_address_range(ips):
-            addrs.extend(summarize_address_range(first, last))
-
-    return _collapse_addresses_internal(addrs + nets)
-
-
-def get_mixed_type_key(obj):
-    """Return a key suitable for sorting between networks and addresses.
-
-    Address and Network objects are not sortable by default; they're
-    fundamentally different so the expression
-
-        IPv4Address('192.0.2.0') <= IPv4Network('192.0.2.0/24')
-
-    doesn't make any sense.  There are some times however, where you may wish
-    to have ipaddress sort these for you anyway. If you need to do this, you
-    can use this function as the key= argument to sorted().
-
-    Args:
-      obj: either a Network or Address object.
-    Returns:
-      appropriate key.
-
-    """
-    if isinstance(obj, _BaseNetwork):
-        return obj._get_networks_key()
-    elif isinstance(obj, _BaseAddress):
-        return obj._get_address_key()
-    return NotImplemented
-
-
-class _IPAddressBase(_TotalOrderingMixin):
-
-    """The mother class."""
-
-    __slots__ = ()
-
-    @property
-    def exploded(self):
-        """Return the longhand version of the IP address as a string."""
-        return self._explode_shorthand_ip_string()
-
-    @property
-    def compressed(self):
-        """Return the shorthand version of the IP address as a string."""
-        return _compat_str(self)
-
-    @property
-    def reverse_pointer(self):
-        """The name of the reverse DNS pointer for the IP address, e.g.:
-            >>> ipaddress.ip_address("127.0.0.1").reverse_pointer
-            '1.0.0.127.in-addr.arpa'
-            >>> ipaddress.ip_address("2001:db8::1").reverse_pointer
-            '1.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.0.8.b.d.0.1.0.0.2.ip6.arpa'
-
-        """
-        return self._reverse_pointer()
-
-    @property
-    def version(self):
-        msg = '%200s has no version specified' % (type(self),)
-        raise NotImplementedError(msg)
-
-    def _check_int_address(self, address):
-        if address < 0:
-            msg = "%d (< 0) is not permitted as an IPv%d address"
-            raise AddressValueError(msg % (address, self._version))
-        if address > self._ALL_ONES:
-            msg = "%d (>= 2**%d) is not permitted as an IPv%d address"
-            raise AddressValueError(msg % (address, self._max_prefixlen,
-                                           self._version))
-
-    def _check_packed_address(self, address, expected_len):
-        address_len = len(address)
-        if address_len != expected_len:
-            msg = (
-                '%r (len %d != %d) is not permitted as an IPv%d address. '
-                'Did you pass in a bytes (str in Python 2) instead of'
-                ' a unicode object?')
-            raise AddressValueError(msg % (address, address_len,
-                                           expected_len, self._version))
-
-    @classmethod
-    def _ip_int_from_prefix(cls, prefixlen):
-        """Turn the prefix length into a bitwise netmask
-
-        Args:
-            prefixlen: An integer, the prefix length.
-
-        Returns:
-            An integer.
-
-        """
-        return cls._ALL_ONES ^ (cls._ALL_ONES >> prefixlen)
-
-    @classmethod
-    def _prefix_from_ip_int(cls, ip_int):
-        """Return prefix length from the bitwise netmask.
-
-        Args:
-            ip_int: An integer, the netmask in expanded bitwise format
-
-        Returns:
-            An integer, the prefix length.
-
-        Raises:
-            ValueError: If the input intermingles zeroes & ones
-        """
-        trailing_zeroes = _count_righthand_zero_bits(ip_int,
-                                                     cls._max_prefixlen)
-        prefixlen = cls._max_prefixlen - trailing_zeroes
-        leading_ones = ip_int >> trailing_zeroes
-        all_ones = (1 << prefixlen) - 1
-        if leading_ones != all_ones:
-            byteslen = cls._max_prefixlen // 8
-            details = _compat_to_bytes(ip_int, byteslen, 'big')
-            msg = 'Netmask pattern %r mixes zeroes & ones'
-            raise ValueError(msg % details)
-        return prefixlen
-
-    @classmethod
-    def _report_invalid_netmask(cls, netmask_str):
-        msg = '%r is not a valid netmask' % netmask_str
-        raise NetmaskValueError(msg)
-
-    @classmethod
-    def _prefix_from_prefix_string(cls, prefixlen_str):
-        """Return prefix length from a numeric string
-
-        Args:
-            prefixlen_str: The string to be converted
-
-        Returns:
-            An integer, the prefix length.
-
-        Raises:
-            NetmaskValueError: If the input is not a valid netmask
-        """
-        # int allows a leading +/- as well as surrounding whitespace,
-        # so we ensure that isn't the case
-        if not _BaseV4._DECIMAL_DIGITS.issuperset(prefixlen_str):
-            cls._report_invalid_netmask(prefixlen_str)
-        try:
-            prefixlen = int(prefixlen_str)
-        except ValueError:
-            cls._report_invalid_netmask(prefixlen_str)
-        if not (0 <= prefixlen <= cls._max_prefixlen):
-            cls._report_invalid_netmask(prefixlen_str)
-        return prefixlen
-
-    @classmethod
-    def _prefix_from_ip_string(cls, ip_str):
-        """Turn a netmask/hostmask string into a prefix length
-
-        Args:
-            ip_str: The netmask/hostmask to be converted
-
-        Returns:
-            An integer, the prefix length.
-
-        Raises:
-            NetmaskValueError: If the input is not a valid netmask/hostmask
-        """
-        # Parse the netmask/hostmask like an IP address.
-        try:
-            ip_int = cls._ip_int_from_string(ip_str)
-        except AddressValueError:
-            cls._report_invalid_netmask(ip_str)
-
-        # Try matching a netmask (this would be /1*0*/ as a bitwise regexp).
-        # Note that the two ambiguous cases (all-ones and all-zeroes) are
-        # treated as netmasks.
-        try:
-            return cls._prefix_from_ip_int(ip_int)
-        except ValueError:
-            pass
-
-        # Invert the bits, and try matching a /0+1+/ hostmask instead.
-        ip_int ^= cls._ALL_ONES
-        try:
-            return cls._prefix_from_ip_int(ip_int)
-        except ValueError:
-            cls._report_invalid_netmask(ip_str)
-
-    def __reduce__(self):
-        return self.__class__, (_compat_str(self),)
-
-
-class _BaseAddress(_IPAddressBase):
-
-    """A generic IP object.
-
-    This IP class contains the version independent methods which are
-    used by single IP addresses.
-    """
-
-    __slots__ = ()
-
-    def __int__(self):
-        return self._ip
-
-    def __eq__(self, other):
-        try:
-            return (self._ip == other._ip and
-                    self._version == other._version)
-        except AttributeError:
-            return NotImplemented
-
-    def __lt__(self, other):
-        if not isinstance(other, _IPAddressBase):
-            return NotImplemented
-        if not isinstance(other, _BaseAddress):
-            raise TypeError('%s and %s are not of the same type' % (
-                self, other))
-        if self._version != other._version:
-            raise TypeError('%s and %s are not of the same version' % (
-                self, other))
-        if self._ip != other._ip:
-            return self._ip < other._ip
-        return False
-
-    # Shorthand for Integer addition and subtraction. This is not
-    # meant to ever support addition/subtraction of addresses.
-    def __add__(self, other):
-        if not isinstance(other, _compat_int_types):
-            return NotImplemented
-        return self.__class__(int(self) + other)
-
-    def __sub__(self, other):
-        if not isinstance(other, _compat_int_types):
-            return NotImplemented
-        return self.__class__(int(self) - other)
-
-    def __repr__(self):
-        return '%s(%r)' % (self.__class__.__name__, _compat_str(self))
-
-    def __str__(self):
-        return _compat_str(self._string_from_ip_int(self._ip))
-
-    def __hash__(self):
-        return hash(hex(int(self._ip)))
-
-    def _get_address_key(self):
-        return (self._version, self)
-
-    def __reduce__(self):
-        return self.__class__, (self._ip,)
-
-
-class _BaseNetwork(_IPAddressBase):
-
-    """A generic IP network object.
-
-    This IP class contains the version independent methods which are
-    used by networks.
-
-    """
-    def __init__(self, address):
-        self._cache = {}
-
-    def __repr__(self):
-        return '%s(%r)' % (self.__class__.__name__, _compat_str(self))
-
-    def __str__(self):
-        return '%s/%d' % (self.network_address, self.prefixlen)
-
-    def hosts(self):
-        """Generate Iterator over usable hosts in a network.
-
-        This is like __iter__ except it doesn't return the network
-        or broadcast addresses.
-
-        """
-        network = int(self.network_address)
-        broadcast = int(self.broadcast_address)
-        for x in _compat_range(network + 1, broadcast):
-            yield self._address_class(x)
-
-    def __iter__(self):
-        network = int(self.network_address)
-        broadcast = int(self.broadcast_address)
-        for x in _compat_range(network, broadcast + 1):
-            yield self._address_class(x)
-
-    def __getitem__(self, n):
-        network = int(self.network_address)
-        broadcast = int(self.broadcast_address)
-        if n >= 0:
-            if network + n > broadcast:
-                raise IndexError('address out of range')
-            return self._address_class(network + n)
-        else:
-            n += 1
-            if broadcast + n < network:
-                raise IndexError('address out of range')
-            return self._address_class(broadcast + n)
-
-    def __lt__(self, other):
-        if not isinstance(other, _IPAddressBase):
-            return NotImplemented
-        if not isinstance(other, _BaseNetwork):
-            raise TypeError('%s and %s are not of the same type' % (
-                            self, other))
-        if self._version != other._version:
-            raise TypeError('%s and %s are not of the same version' % (
-                            self, other))
-        if self.network_address != other.network_address:
-            return self.network_address < other.network_address
-        if self.netmask != other.netmask:
-            return self.netmask < other.netmask
-        return False
-
-    def __eq__(self, other):
-        try:
-            return (self._version == other._version and
-                    self.network_address == other.network_address and
-                    int(self.netmask) == int(other.netmask))
-        except AttributeError:
-            return NotImplemented
-
-    def __hash__(self):
-        return hash(int(self.network_address) ^ int(self.netmask))
-
-    def __contains__(self, other):
-        # always false if one is v4 and the other is v6.
-        if self._version != other._version:
-            return False
-        # dealing with another network.
-        if isinstance(other, _BaseNetwork):
-            return False
-        # dealing with another address
-        else:
-            # address
-            return (int(self.network_address) <= int(other._ip) <=
-                    int(self.broadcast_address))
-
-    def overlaps(self, other):
-        """Tell if self is partly contained in other."""
-        return self.network_address in other or (
-            self.broadcast_address in other or (
-                other.network_address in self or (
-                    other.broadcast_address in self)))
-
-    @property
-    def broadcast_address(self):
-        x = self._cache.get('broadcast_address')
-        if x is None:
-            x = self._address_class(int(self.network_address) |
-                                    int(self.hostmask))
-            self._cache['broadcast_address'] = x
-        return x
-
-    @property
-    def hostmask(self):
-        x = self._cache.get('hostmask')
-        if x is None:
-            x = self._address_class(int(self.netmask) ^ self._ALL_ONES)
-            self._cache['hostmask'] = x
-        return x
-
-    @property
-    def with_prefixlen(self):
-        return '%s/%d' % (self.network_address, self._prefixlen)
-
-    @property
-    def with_netmask(self):
-        return '%s/%s' % (self.network_address, self.netmask)
-
-    @property
-    def with_hostmask(self):
-        return '%s/%s' % (self.network_address, self.hostmask)
-
-    @property
-    def num_addresses(self):
-        """Number of hosts in the current subnet."""
-        return int(self.broadcast_address) - int(self.network_address) + 1
-
-    @property
-    def _address_class(self):
-        # Returning bare address objects (rather than interfaces) allows for
-        # more consistent behaviour across the network address, broadcast
-        # address and individual host addresses.
-        msg = '%200s has no associated address class' % (type(self),)
-        raise NotImplementedError(msg)
-
-    @property
-    def prefixlen(self):
-        return self._prefixlen
-
-    def address_exclude(self, other):
-        """Remove an address from a larger block.
-
-        For example:
-
-            addr1 = ip_network('192.0.2.0/28')
-            addr2 = ip_network('192.0.2.1/32')
-            list(addr1.address_exclude(addr2)) =
-                [IPv4Network('192.0.2.0/32'), IPv4Network('192.0.2.2/31'),
-                 IPv4Network('192.0.2.4/30'), IPv4Network('192.0.2.8/29')]
-
-        or IPv6:
-
-            addr1 = ip_network('2001:db8::1/32')
-            addr2 = ip_network('2001:db8::1/128')
-            list(addr1.address_exclude(addr2)) =
-                [ip_network('2001:db8::1/128'),
-                 ip_network('2001:db8::2/127'),
-                 ip_network('2001:db8::4/126'),
-                 ip_network('2001:db8::8/125'),
-                 ...
-                 ip_network('2001:db8:8000::/33')]
-
-        Args:
-            other: An IPv4Network or IPv6Network object of the same type.
-
-        Returns:
-            An iterator of the IPv(4|6)Network objects which is self
-            minus other.
-
-        Raises:
-            TypeError: If self and other are of differing address
-              versions, or if other is not a network object.
-            ValueError: If other is not completely contained by self.
-
-        """
-        if not self._version == other._version:
-            raise TypeError("%s and %s are not of the same version" % (
-                            self, other))
-
-        if not isinstance(other, _BaseNetwork):
-            raise TypeError("%s is not a network object" % other)
-
-        if not other.subnet_of(self):
-            raise ValueError('%s not contained in %s' % (other, self))
-        if other == self:
-            return
-
-        # Make sure we're comparing the network of other.
-        other = other.__class__('%s/%s' % (other.network_address,
-                                           other.prefixlen))
-
-        s1, s2 = self.subnets()
-        while s1 != other and s2 != other:
-            if other.subnet_of(s1):
-                yield s2
-                s1, s2 = s1.subnets()
-            elif other.subnet_of(s2):
-                yield s1
-                s1, s2 = s2.subnets()
-            else:
-                # If we got here, there's a bug somewhere.
-                raise AssertionError('Error performing exclusion: '
-                                     's1: %s s2: %s other: %s' %
-                                     (s1, s2, other))
-        if s1 == other:
-            yield s2
-        elif s2 == other:
-            yield s1
-        else:
-            # If we got here, there's a bug somewhere.
-            raise AssertionError('Error performing exclusion: '
-                                 's1: %s s2: %s other: %s' %
-                                 (s1, s2, other))
-
-    def compare_networks(self, other):
-        """Compare two IP objects.
-
-        This is only concerned about the comparison of the integer
-        representation of the network addresses.  This means that the
-        host bits aren't considered at all in this method.  If you want
-        to compare host bits, you can easily enough do a
-        'HostA._ip < HostB._ip'
-
-        Args:
-            other: An IP object.
-
-        Returns:
-            If the IP versions of self and other are the same, returns:
-
-            -1 if self < other:
-              eg: IPv4Network('192.0.2.0/25') < IPv4Network('192.0.2.128/25')
-              IPv6Network('2001:db8::1000/124') <
-                  IPv6Network('2001:db8::2000/124')
-            0 if self == other
-              eg: IPv4Network('192.0.2.0/24') == IPv4Network('192.0.2.0/24')
-              IPv6Network('2001:db8::1000/124') ==
-                  IPv6Network('2001:db8::1000/124')
-            1 if self > other
-              eg: IPv4Network('192.0.2.128/25') > IPv4Network('192.0.2.0/25')
-                  IPv6Network('2001:db8::2000/124') >
-                      IPv6Network('2001:db8::1000/124')
-
-          Raises:
-              TypeError if the IP versions are different.
-
-        """
-        # does this need to raise a ValueError?
-        if self._version != other._version:
-            raise TypeError('%s and %s are not of the same type' % (
-                            self, other))
-        # self._version == other._version below here:
-        if self.network_address < other.network_address:
-            return -1
-        if self.network_address > other.network_address:
-            return 1
-        # self.network_address == other.network_address below here:
-        if self.netmask < other.netmask:
-            return -1
-        if self.netmask > other.netmask:
-            return 1
-        return 0
-
-    def _get_networks_key(self):
-        """Network-only key function.
-
-        Returns an object that identifies this address' network and
-        netmask. This function is a suitable "key" argument for sorted()
-        and list.sort().
-
-        """
-        return (self._version, self.network_address, self.netmask)
-
-    def subnets(self, prefixlen_diff=1, new_prefix=None):
-        """The subnets which join to make the current subnet.
-
-        In the case that self contains only one IP
-        (self._prefixlen == 32 for IPv4 or self._prefixlen == 128
-        for IPv6), yield an iterator with just ourself.
-
-        Args:
-            prefixlen_diff: An integer, the amount the prefix length
-              should be increased by. This should not be set if
-              new_prefix is also set.
-            new_prefix: The desired new prefix length. This must be a
-              larger number (smaller prefix) than the existing prefix.
-              This should not be set if prefixlen_diff is also set.
-
-        Returns:
-            An iterator of IPv(4|6) objects.
-
-        Raises:
-            ValueError: The prefixlen_diff is too small or too large.
-                OR
-            prefixlen_diff and new_prefix are both set or new_prefix
-              is a smaller number than the current prefix (smaller
-              number means a larger network)
-
-        """
-        if self._prefixlen == self._max_prefixlen:
-            yield self
-            return
-
-        if new_prefix is not None:
-            if new_prefix < self._prefixlen:
-                raise ValueError('new prefix must be longer')
-            if prefixlen_diff != 1:
-                raise ValueError('cannot set prefixlen_diff and new_prefix')
-            prefixlen_diff = new_prefix - self._prefixlen
-
-        if prefixlen_diff < 0:
-            raise ValueError('prefix length diff must be > 0')
-        new_prefixlen = self._prefixlen + prefixlen_diff
-
-        if new_prefixlen > self._max_prefixlen:
-            raise ValueError(
-                'prefix length diff %d is invalid for netblock %s' % (
-                    new_prefixlen, self))
-
-        start = int(self.network_address)
-        end = int(self.broadcast_address) + 1
-        step = (int(self.hostmask) + 1) >> prefixlen_diff
-        for new_addr in _compat_range(start, end, step):
-            current = self.__class__((new_addr, new_prefixlen))
-            yield current
-
-    def supernet(self, prefixlen_diff=1, new_prefix=None):
-        """The supernet containing the current network.
-
-        Args:
-            prefixlen_diff: An integer, the amount the prefix length of
-              the network should be decreased by.  For example, given a
-              /24 network and a prefixlen_diff of 3, a supernet with a
-              /21 netmask is returned.
-
-        Returns:
-            An IPv4 network object.
-
-        Raises:
-            ValueError: If self.prefixlen - prefixlen_diff < 0. I.e., you have
-              a negative prefix length.
-                OR
-            If prefixlen_diff and new_prefix are both set or new_prefix is a
-              larger number than the current prefix (larger number means a
-              smaller network)
-
-        """
-        if self._prefixlen == 0:
-            return self
-
-        if new_prefix is not None:
-            if new_prefix > self._prefixlen:
-                raise ValueError('new prefix must be shorter')
-            if prefixlen_diff != 1:
-                raise ValueError('cannot set prefixlen_diff and new_prefix')
-            prefixlen_diff = self._prefixlen - new_prefix
-
-        new_prefixlen = self.prefixlen - prefixlen_diff
-        if new_prefixlen < 0:
-            raise ValueError(
-                'current prefixlen is %d, cannot have a prefixlen_diff of %d' %
-                (self.prefixlen, prefixlen_diff))
-        return self.__class__((
-            int(self.network_address) & (int(self.netmask) << prefixlen_diff),
-            new_prefixlen))
-
-    @property
-    def is_multicast(self):
-        """Test if the address is reserved for multicast use.
-
-        Returns:
-            A boolean, True if the address is a multicast address.
-            See RFC 2373 2.7 for details.
-
-        """
-        return (self.network_address.is_multicast and
-                self.broadcast_address.is_multicast)
-
-    @staticmethod
-    def _is_subnet_of(a, b):
-        try:
-            # Always false if one is v4 and the other is v6.
-            if a._version != b._version:
-                raise TypeError("%s and %s are not of the same version" (a, b))
-            return (b.network_address <= a.network_address and
-                    b.broadcast_address >= a.broadcast_address)
-        except AttributeError:
-            raise TypeError("Unable to test subnet containment "
-                            "between %s and %s" % (a, b))
-
-    def subnet_of(self, other):
-        """Return True if this network is a subnet of other."""
-        return self._is_subnet_of(self, other)
-
-    def supernet_of(self, other):
-        """Return True if this network is a supernet of other."""
-        return self._is_subnet_of(other, self)
-
-    @property
-    def is_reserved(self):
-        """Test if the address is otherwise IETF reserved.
-
-        Returns:
-            A boolean, True if the address is within one of the
-            reserved IPv6 Network ranges.
-
-        """
-        return (self.network_address.is_reserved and
-                self.broadcast_address.is_reserved)
-
-    @property
-    def is_link_local(self):
-        """Test if the address is reserved for link-local.
-
-        Returns:
-            A boolean, True if the address is reserved per RFC 4291.
-
-        """
-        return (self.network_address.is_link_local and
-                self.broadcast_address.is_link_local)
-
-    @property
-    def is_private(self):
-        """Test if this address is allocated for private networks.
-
-        Returns:
-            A boolean, True if the address is reserved per
-            iana-ipv4-special-registry or iana-ipv6-special-registry.
-
-        """
-        return (self.network_address.is_private and
-                self.broadcast_address.is_private)
-
-    @property
-    def is_global(self):
-        """Test if this address is allocated for public networks.
-
-        Returns:
-            A boolean, True if the address is not reserved per
-            iana-ipv4-special-registry or iana-ipv6-special-registry.
-
-        """
-        return not self.is_private
-
-    @property
-    def is_unspecified(self):
-        """Test if the address is unspecified.
-
-        Returns:
-            A boolean, True if this is the unspecified address as defined in
-            RFC 2373 2.5.2.
-
-        """
-        return (self.network_address.is_unspecified and
-                self.broadcast_address.is_unspecified)
-
-    @property
-    def is_loopback(self):
-        """Test if the address is a loopback address.
-
-        Returns:
-            A boolean, True if the address is a loopback address as defined in
-            RFC 2373 2.5.3.
-
-        """
-        return (self.network_address.is_loopback and
-                self.broadcast_address.is_loopback)
-
-
-class _BaseV4(object):
-
-    """Base IPv4 object.
-
-    The following methods are used by IPv4 objects in both single IP
-    addresses and networks.
-
-    """
-
-    __slots__ = ()
-    _version = 4
-    # Equivalent to 255.255.255.255 or 32 bits of 1's.
-    _ALL_ONES = (2 ** IPV4LENGTH) - 1
-    _DECIMAL_DIGITS = frozenset('0123456789')
-
-    # the valid octets for host and netmasks. only useful for IPv4.
-    _valid_mask_octets = frozenset([255, 254, 252, 248, 240, 224, 192, 128, 0])
-
-    _max_prefixlen = IPV4LENGTH
-    # There are only a handful of valid v4 netmasks, so we cache them all
-    # when constructed (see _make_netmask()).
-    _netmask_cache = {}
-
-    def _explode_shorthand_ip_string(self):
-        return _compat_str(self)
-
-    @classmethod
-    def _make_netmask(cls, arg):
-        """Make a (netmask, prefix_len) tuple from the given argument.
-
-        Argument can be:
-        - an integer (the prefix length)
-        - a string representing the prefix length (e.g. "24")
-        - a string representing the prefix netmask (e.g. "255.255.255.0")
-        """
-        if arg not in cls._netmask_cache:
-            if isinstance(arg, _compat_int_types):
-                prefixlen = arg
-            else:
-                try:
-                    # Check for a netmask in prefix length form
-                    prefixlen = cls._prefix_from_prefix_string(arg)
-                except NetmaskValueError:
-                    # Check for a netmask or hostmask in dotted-quad form.
-                    # This may raise NetmaskValueError.
-                    prefixlen = cls._prefix_from_ip_string(arg)
-            netmask = IPv4Address(cls._ip_int_from_prefix(prefixlen))
-            cls._netmask_cache[arg] = netmask, prefixlen
-        return cls._netmask_cache[arg]
-
-    @classmethod
-    def _ip_int_from_string(cls, ip_str):
-        """Turn the given IP string into an integer for comparison.
-
-        Args:
-            ip_str: A string, the IP ip_str.
-
-        Returns:
-            The IP ip_str as an integer.
-
-        Raises:
-            AddressValueError: if ip_str isn't a valid IPv4 Address.
-
-        """
-        if not ip_str:
-            raise AddressValueError('Address cannot be empty')
-
-        octets = ip_str.split('.')
-        if len(octets) != 4:
-            raise AddressValueError("Expected 4 octets in %r" % ip_str)
-
-        try:
-            return _compat_int_from_byte_vals(
-                map(cls._parse_octet, octets), 'big')
-        except ValueError as exc:
-            raise AddressValueError("%s in %r" % (exc, ip_str))
-
-    @classmethod
-    def _parse_octet(cls, octet_str):
-        """Convert a decimal octet into an integer.
-
-        Args:
-            octet_str: A string, the number to parse.
-
-        Returns:
-            The octet as an integer.
-
-        Raises:
-            ValueError: if the octet isn't strictly a decimal from [0..255].
-
-        """
-        if not octet_str:
-            raise ValueError("Empty octet not permitted")
-        # Whitelist the characters, since int() allows a lot of bizarre stuff.
-        if not cls._DECIMAL_DIGITS.issuperset(octet_str):
-            msg = "Only decimal digits permitted in %r"
-            raise ValueError(msg % octet_str)
-        # We do the length check second, since the invalid character error
-        # is likely to be more informative for the user
-        if len(octet_str) > 3:
-            msg = "At most 3 characters permitted in %r"
-            raise ValueError(msg % octet_str)
-        # Convert to integer (we know digits are legal)
-        octet_int = int(octet_str, 10)
-        # Any octets that look like they *might* be written in octal,
-        # and which don't look exactly the same in both octal and
-        # decimal are rejected as ambiguous
-        if octet_int > 7 and octet_str[0] == '0':
-            msg = "Ambiguous (octal/decimal) value in %r not permitted"
-            raise ValueError(msg % octet_str)
-        if octet_int > 255:
-            raise ValueError("Octet %d (> 255) not permitted" % octet_int)
-        return octet_int
-
-    @classmethod
-    def _string_from_ip_int(cls, ip_int):
-        """Turns a 32-bit integer into dotted decimal notation.
-
-        Args:
-            ip_int: An integer, the IP address.
-
-        Returns:
-            The IP address as a string in dotted decimal notation.
-
-        """
-        return '.'.join(_compat_str(struct.unpack(b'!B', b)[0]
-                                    if isinstance(b, bytes)
-                                    else b)
-                        for b in _compat_to_bytes(ip_int, 4, 'big'))
-
-    def _is_hostmask(self, ip_str):
-        """Test if the IP string is a hostmask (rather than a netmask).
-
-        Args:
-            ip_str: A string, the potential hostmask.
-
-        Returns:
-            A boolean, True if the IP string is a hostmask.
-
-        """
-        bits = ip_str.split('.')
-        try:
-            parts = [x for x in map(int, bits) if x in self._valid_mask_octets]
-        except ValueError:
-            return False
-        if len(parts) != len(bits):
-            return False
-        if parts[0] < parts[-1]:
-            return True
-        return False
-
-    def _reverse_pointer(self):
-        """Return the reverse DNS pointer name for the IPv4 address.
-
-        This implements the method described in RFC1035 3.5.
-
-        """
-        reverse_octets = _compat_str(self).split('.')[::-1]
-        return '.'.join(reverse_octets) + '.in-addr.arpa'
-
-    @property
-    def max_prefixlen(self):
-        return self._max_prefixlen
-
-    @property
-    def version(self):
-        return self._version
-
-
-class IPv4Address(_BaseV4, _BaseAddress):
-
-    """Represent and manipulate single IPv4 Addresses."""
-
-    __slots__ = ('_ip', '__weakref__')
-
-    def __init__(self, address):
-
-        """
-        Args:
-            address: A string or integer representing the IP
-
-              Additionally, an integer can be passed, so
-              IPv4Address('192.0.2.1') == IPv4Address(3221225985).
-              or, more generally
-              IPv4Address(int(IPv4Address('192.0.2.1'))) ==
-                IPv4Address('192.0.2.1')
-
-        Raises:
-            AddressValueError: If ipaddress isn't a valid IPv4 address.
-
-        """
-        # Efficient constructor from integer.
-        if isinstance(address, _compat_int_types):
-            self._check_int_address(address)
-            self._ip = address
-            return
-
-        # Constructing from a packed address
-        if isinstance(address, bytes):
-            self._check_packed_address(address, 4)
-            bvs = _compat_bytes_to_byte_vals(address)
-            self._ip = _compat_int_from_byte_vals(bvs, 'big')
-            return
-
-        # Assume input argument to be string or any object representation
-        # which converts into a formatted IP string.
-        addr_str = _compat_str(address)
-        if '/' in addr_str:
-            raise AddressValueError("Unexpected '/' in %r" % address)
-        self._ip = self._ip_int_from_string(addr_str)
-
-    @property
-    def packed(self):
-        """The binary representation of this address."""
-        return v4_int_to_packed(self._ip)
-
-    @property
-    def is_reserved(self):
-        """Test if the address is otherwise IETF reserved.
-
-         Returns:
-             A boolean, True if the address is within the
-             reserved IPv4 Network range.
-
-        """
-        return self in self._constants._reserved_network
-
-    @property
-    def is_private(self):
-        """Test if this address is allocated for private networks.
-
-        Returns:
-            A boolean, True if the address is reserved per
-            iana-ipv4-special-registry.
-
-        """
-        return any(self in net for net in self._constants._private_networks)
-
-    @property
-    def is_global(self):
-        return (
-            self not in self._constants._public_network and
-            not self.is_private)
-
-    @property
-    def is_multicast(self):
-        """Test if the address is reserved for multicast use.
-
-        Returns:
-            A boolean, True if the address is multicast.
-            See RFC 3171 for details.
-
-        """
-        return self in self._constants._multicast_network
-
-    @property
-    def is_unspecified(self):
-        """Test if the address is unspecified.
-
-        Returns:
-            A boolean, True if this is the unspecified address as defined in
-            RFC 5735 3.
-
-        """
-        return self == self._constants._unspecified_address
-
-    @property
-    def is_loopback(self):
-        """Test if the address is a loopback address.
-
-        Returns:
-            A boolean, True if the address is a loopback per RFC 3330.
-
-        """
-        return self in self._constants._loopback_network
-
-    @property
-    def is_link_local(self):
-        """Test if the address is reserved for link-local.
-
-        Returns:
-            A boolean, True if the address is link-local per RFC 3927.
-
-        """
-        return self in self._constants._linklocal_network
-
-
-class IPv4Interface(IPv4Address):
-
-    def __init__(self, address):
-        if isinstance(address, (bytes, _compat_int_types)):
-            IPv4Address.__init__(self, address)
-            self.network = IPv4Network(self._ip)
-            self._prefixlen = self._max_prefixlen
-            return
-
-        if isinstance(address, tuple):
-            IPv4Address.__init__(self, address[0])
-            if len(address) > 1:
-                self._prefixlen = int(address[1])
-            else:
-                self._prefixlen = self._max_prefixlen
-
-            self.network = IPv4Network(address, strict=False)
-            self.netmask = self.network.netmask
-            self.hostmask = self.network.hostmask
-            return
-
-        addr = _split_optional_netmask(address)
-        IPv4Address.__init__(self, addr[0])
-
-        self.network = IPv4Network(address, strict=False)
-        self._prefixlen = self.network._prefixlen
-
-        self.netmask = self.network.netmask
-        self.hostmask = self.network.hostmask
-
-    def __str__(self):
-        return '%s/%d' % (self._string_from_ip_int(self._ip),
-                          self.network.prefixlen)
-
-    def __eq__(self, other):
-        address_equal = IPv4Address.__eq__(self, other)
-        if not address_equal or address_equal is NotImplemented:
-            return address_equal
-        try:
-            return self.network == other.network
-        except AttributeError:
-            # An interface with an associated network is NOT the
-            # same as an unassociated address. That's why the hash
-            # takes the extra info into account.
-            return False
-
-    def __lt__(self, other):
-        address_less = IPv4Address.__lt__(self, other)
-        if address_less is NotImplemented:
-            return NotImplemented
-        try:
-            return (self.network < other.network or
-                    self.network == other.network and address_less)
-        except AttributeError:
-            # We *do* allow addresses and interfaces to be sorted. The
-            # unassociated address is considered less than all interfaces.
-            return False
-
-    def __hash__(self):
-        return self._ip ^ self._prefixlen ^ int(self.network.network_address)
-
-    __reduce__ = _IPAddressBase.__reduce__
-
-    @property
-    def ip(self):
-        return IPv4Address(self._ip)
-
-    @property
-    def with_prefixlen(self):
-        return '%s/%s' % (self._string_from_ip_int(self._ip),
-                          self._prefixlen)
-
-    @property
-    def with_netmask(self):
-        return '%s/%s' % (self._string_from_ip_int(self._ip),
-                          self.netmask)
-
-    @property
-    def with_hostmask(self):
-        return '%s/%s' % (self._string_from_ip_int(self._ip),
-                          self.hostmask)
-
-
-class IPv4Network(_BaseV4, _BaseNetwork):
-
-    """This class represents and manipulates 32-bit IPv4 network + addresses..
-
-    Attributes: [examples for IPv4Network('192.0.2.0/27')]
-        .network_address: IPv4Address('192.0.2.0')
-        .hostmask: IPv4Address('0.0.0.31')
-        .broadcast_address: IPv4Address('192.0.2.32')
-        .netmask: IPv4Address('255.255.255.224')
-        .prefixlen: 27
-
-    """
-    # Class to use when creating address objects
-    _address_class = IPv4Address
-
-    def __init__(self, address, strict=True):
-
-        """Instantiate a new IPv4 network object.
-
-        Args:
-            address: A string or integer representing the IP [& network].
-              '192.0.2.0/24'
-              '192.0.2.0/255.255.255.0'
-              '192.0.0.2/0.0.0.255'
-              are all functionally the same in IPv4. Similarly,
-              '192.0.2.1'
-              '192.0.2.1/255.255.255.255'
-              '192.0.2.1/32'
-              are also functionally equivalent. That is to say, failing to
-              provide a subnetmask will create an object with a mask of /32.
-
-              If the mask (portion after the / in the argument) is given in
-              dotted quad form, it is treated as a netmask if it starts with a
-              non-zero field (e.g. /255.0.0.0 == /8) and as a hostmask if it
-              starts with a zero field (e.g. 0.255.255.255 == /8), with the
-              single exception of an all-zero mask which is treated as a
-              netmask == /0. If no mask is given, a default of /32 is used.
-
-              Additionally, an integer can be passed, so
-              IPv4Network('192.0.2.1') == IPv4Network(3221225985)
-              or, more generally
-              IPv4Interface(int(IPv4Interface('192.0.2.1'))) ==
-                IPv4Interface('192.0.2.1')
-
-        Raises:
-            AddressValueError: If ipaddress isn't a valid IPv4 address.
-            NetmaskValueError: If the netmask isn't valid for
-              an IPv4 address.
-            ValueError: If strict is True and a network address is not
-              supplied.
-
-        """
-        _BaseNetwork.__init__(self, address)
-
-        # Constructing from a packed address or integer
-        if isinstance(address, (_compat_int_types, bytes)):
-            self.network_address = IPv4Address(address)
-            self.netmask, self._prefixlen = self._make_netmask(
-                self._max_prefixlen)
-            # fixme: address/network test here.
-            return
-
-        if isinstance(address, tuple):
-            if len(address) > 1:
-                arg = address[1]
-            else:
-                # We weren't given an address[1]
-                arg = self._max_prefixlen
-            self.network_address = IPv4Address(address[0])
-            self.netmask, self._prefixlen = self._make_netmask(arg)
-            packed = int(self.network_address)
-            if packed & int(self.netmask) != packed:
-                if strict:
-                    raise ValueError('%s has host bits set' % self)
-                else:
-                    self.network_address = IPv4Address(packed &
-                                                       int(self.netmask))
-            return
-
-        # Assume input argument to be string or any object representation
-        # which converts into a formatted IP prefix string.
-        addr = _split_optional_netmask(address)
-        self.network_address = IPv4Address(self._ip_int_from_string(addr[0]))
-
-        if len(addr) == 2:
-            arg = addr[1]
-        else:
-            arg = self._max_prefixlen
-        self.netmask, self._prefixlen = self._make_netmask(arg)
-
-        if strict:
-            if (IPv4Address(int(self.network_address) & int(self.netmask)) !=
-                    self.network_address):
-                raise ValueError('%s has host bits set' % self)
-        self.network_address = IPv4Address(int(self.network_address) &
-                                           int(self.netmask))
-
-        if self._prefixlen == (self._max_prefixlen - 1):
-            self.hosts = self.__iter__
-
-    @property
-    def is_global(self):
-        """Test if this address is allocated for public networks.
-
-        Returns:
-            A boolean, True if the address is not reserved per
-            iana-ipv4-special-registry.
-
-        """
-        return (not (self.network_address in IPv4Network('100.64.0.0/10') and
-                self.broadcast_address in IPv4Network('100.64.0.0/10')) and
-                not self.is_private)
-
-
-class _IPv4Constants(object):
-
-    _linklocal_network = IPv4Network('169.254.0.0/16')
-
-    _loopback_network = IPv4Network('127.0.0.0/8')
-
-    _multicast_network = IPv4Network('224.0.0.0/4')
-
-    _public_network = IPv4Network('100.64.0.0/10')
-
-    _private_networks = [
-        IPv4Network('0.0.0.0/8'),
-        IPv4Network('10.0.0.0/8'),
-        IPv4Network('127.0.0.0/8'),
-        IPv4Network('169.254.0.0/16'),
-        IPv4Network('172.16.0.0/12'),
-        IPv4Network('192.0.0.0/29'),
-        IPv4Network('192.0.0.170/31'),
-        IPv4Network('192.0.2.0/24'),
-        IPv4Network('192.168.0.0/16'),
-        IPv4Network('198.18.0.0/15'),
-        IPv4Network('198.51.100.0/24'),
-        IPv4Network('203.0.113.0/24'),
-        IPv4Network('240.0.0.0/4'),
-        IPv4Network('255.255.255.255/32'),
-    ]
-
-    _reserved_network = IPv4Network('240.0.0.0/4')
-
-    _unspecified_address = IPv4Address('0.0.0.0')
-
-
-IPv4Address._constants = _IPv4Constants
-
-
-class _BaseV6(object):
-
-    """Base IPv6 object.
-
-    The following methods are used by IPv6 objects in both single IP
-    addresses and networks.
-
-    """
-
-    __slots__ = ()
-    _version = 6
-    _ALL_ONES = (2 ** IPV6LENGTH) - 1
-    _HEXTET_COUNT = 8
-    _HEX_DIGITS = frozenset('0123456789ABCDEFabcdef')
-    _max_prefixlen = IPV6LENGTH
-
-    # There are only a bunch of valid v6 netmasks, so we cache them all
-    # when constructed (see _make_netmask()).
-    _netmask_cache = {}
-
-    @classmethod
-    def _make_netmask(cls, arg):
-        """Make a (netmask, prefix_len) tuple from the given argument.
-
-        Argument can be:
-        - an integer (the prefix length)
-        - a string representing the prefix length (e.g. "24")
-        - a string representing the prefix netmask (e.g. "255.255.255.0")
-        """
-        if arg not in cls._netmask_cache:
-            if isinstance(arg, _compat_int_types):
-                prefixlen = arg
-            else:
-                prefixlen = cls._prefix_from_prefix_string(arg)
-            netmask = IPv6Address(cls._ip_int_from_prefix(prefixlen))
-            cls._netmask_cache[arg] = netmask, prefixlen
-        return cls._netmask_cache[arg]
-
-    @classmethod
-    def _ip_int_from_string(cls, ip_str):
-        """Turn an IPv6 ip_str into an integer.
-
-        Args:
-            ip_str: A string, the IPv6 ip_str.
-
-        Returns:
-            An int, the IPv6 address
-
-        Raises:
-            AddressValueError: if ip_str isn't a valid IPv6 Address.
-
-        """
-        if not ip_str:
-            raise AddressValueError('Address cannot be empty')
-
-        parts = ip_str.split(':')
-
-        # An IPv6 address needs at least 2 colons (3 parts).
-        _min_parts = 3
-        if len(parts) < _min_parts:
-            msg = "At least %d parts expected in %r" % (_min_parts, ip_str)
-            raise AddressValueError(msg)
-
-        # If the address has an IPv4-style suffix, convert it to hexadecimal.
-        if '.' in parts[-1]:
-            try:
-                ipv4_int = IPv4Address(parts.pop())._ip
-            except AddressValueError as exc:
-                raise AddressValueError("%s in %r" % (exc, ip_str))
-            parts.append('%x' % ((ipv4_int >> 16) & 0xFFFF))
-            parts.append('%x' % (ipv4_int & 0xFFFF))
-
-        # An IPv6 address can't have more than 8 colons (9 parts).
-        # The extra colon comes from using the "::" notation for a single
-        # leading or trailing zero part.
-        _max_parts = cls._HEXTET_COUNT + 1
-        if len(parts) > _max_parts:
-            msg = "At most %d colons permitted in %r" % (
-                _max_parts - 1, ip_str)
-            raise AddressValueError(msg)
-
-        # Disregarding the endpoints, find '::' with nothing in between.
-        # This indicates that a run of zeroes has been skipped.
-        skip_index = None
-        for i in _compat_range(1, len(parts) - 1):
-            if not parts[i]:
-                if skip_index is not None:
-                    # Can't have more than one '::'
-                    msg = "At most one '::' permitted in %r" % ip_str
-                    raise AddressValueError(msg)
-                skip_index = i
-
-        # parts_hi is the number of parts to copy from above/before the '::'
-        # parts_lo is the number of parts to copy from below/after the '::'
-        if skip_index is not None:
-            # If we found a '::', then check if it also covers the endpoints.
-            parts_hi = skip_index
-            parts_lo = len(parts) - skip_index - 1
-            if not parts[0]:
-                parts_hi -= 1
-                if parts_hi:
-                    msg = "Leading ':' only permitted as part of '::' in %r"
-                    raise AddressValueError(msg % ip_str)  # ^: requires ^::
-            if not parts[-1]:
-                parts_lo -= 1
-                if parts_lo:
-                    msg = "Trailing ':' only permitted as part of '::' in %r"
-                    raise AddressValueError(msg % ip_str)  # :$ requires ::$
-            parts_skipped = cls._HEXTET_COUNT - (parts_hi + parts_lo)
-            if parts_skipped < 1:
-                msg = "Expected at most %d other parts with '::' in %r"
-                raise AddressValueError(msg % (cls._HEXTET_COUNT - 1, ip_str))
-        else:
-            # Otherwise, allocate the entire address to parts_hi.  The
-            # endpoints could still be empty, but _parse_hextet() will check
-            # for that.
-            if len(parts) != cls._HEXTET_COUNT:
-                msg = "Exactly %d parts expected without '::' in %r"
-                raise AddressValueError(msg % (cls._HEXTET_COUNT, ip_str))
-            if not parts[0]:
-                msg = "Leading ':' only permitted as part of '::' in %r"
-                raise AddressValueError(msg % ip_str)  # ^: requires ^::
-            if not parts[-1]:
-                msg = "Trailing ':' only permitted as part of '::' in %r"
-                raise AddressValueError(msg % ip_str)  # :$ requires ::$
-            parts_hi = len(parts)
-            parts_lo = 0
-            parts_skipped = 0
-
-        try:
-            # Now, parse the hextets into a 128-bit integer.
-            ip_int = 0
-            for i in range(parts_hi):
-                ip_int <<= 16
-                ip_int |= cls._parse_hextet(parts[i])
-            ip_int <<= 16 * parts_skipped
-            for i in range(-parts_lo, 0):
-                ip_int <<= 16
-                ip_int |= cls._parse_hextet(parts[i])
-            return ip_int
-        except ValueError as exc:
-            raise AddressValueError("%s in %r" % (exc, ip_str))
-
-    @classmethod
-    def _parse_hextet(cls, hextet_str):
-        """Convert an IPv6 hextet string into an integer.
-
-        Args:
-            hextet_str: A string, the number to parse.
-
-        Returns:
-            The hextet as an integer.
-
-        Raises:
-            ValueError: if the input isn't strictly a hex number from
-              [0..FFFF].
-
-        """
-        # Whitelist the characters, since int() allows a lot of bizarre stuff.
-        if not cls._HEX_DIGITS.issuperset(hextet_str):
-            raise ValueError("Only hex digits permitted in %r" % hextet_str)
-        # We do the length check second, since the invalid character error
-        # is likely to be more informative for the user
-        if len(hextet_str) > 4:
-            msg = "At most 4 characters permitted in %r"
-            raise ValueError(msg % hextet_str)
-        # Length check means we can skip checking the integer value
-        return int(hextet_str, 16)
-
-    @classmethod
-    def _compress_hextets(cls, hextets):
-        """Compresses a list of hextets.
-
-        Compresses a list of strings, replacing the longest continuous
-        sequence of "0" in the list with "" and adding empty strings at
-        the beginning or at the end of the string such that subsequently
-        calling ":".join(hextets) will produce the compressed version of
-        the IPv6 address.
-
-        Args:
-            hextets: A list of strings, the hextets to compress.
-
-        Returns:
-            A list of strings.
-
-        """
-        best_doublecolon_start = -1
-        best_doublecolon_len = 0
-        doublecolon_start = -1
-        doublecolon_len = 0
-        for index, hextet in enumerate(hextets):
-            if hextet == '0':
-                doublecolon_len += 1
-                if doublecolon_start == -1:
-                    # Start of a sequence of zeros.
-                    doublecolon_start = index
-                if doublecolon_len > best_doublecolon_len:
-                    # This is the longest sequence of zeros so far.
-                    best_doublecolon_len = doublecolon_len
-                    best_doublecolon_start = doublecolon_start
-            else:
-                doublecolon_len = 0
-                doublecolon_start = -1
-
-        if best_doublecolon_len > 1:
-            best_doublecolon_end = (best_doublecolon_start +
-                                    best_doublecolon_len)
-            # For zeros at the end of the address.
-            if best_doublecolon_end == len(hextets):
-                hextets += ['']
-            hextets[best_doublecolon_start:best_doublecolon_end] = ['']
-            # For zeros at the beginning of the address.
-            if best_doublecolon_start == 0:
-                hextets = [''] + hextets
-
-        return hextets
-
-    @classmethod
-    def _string_from_ip_int(cls, ip_int=None):
-        """Turns a 128-bit integer into hexadecimal notation.
-
-        Args:
-            ip_int: An integer, the IP address.
-
-        Returns:
-            A string, the hexadecimal representation of the address.
-
-        Raises:
-            ValueError: The address is bigger than 128 bits of all ones.
-
-        """
-        if ip_int is None:
-            ip_int = int(cls._ip)
-
-        if ip_int > cls._ALL_ONES:
-            raise ValueError('IPv6 address is too large')
-
-        hex_str = '%032x' % ip_int
-        hextets = ['%x' % int(hex_str[x:x + 4], 16) for x in range(0, 32, 4)]
-
-        hextets = cls._compress_hextets(hextets)
-        return ':'.join(hextets)
-
-    def _explode_shorthand_ip_string(self):
-        """Expand a shortened IPv6 address.
-
-        Args:
-            ip_str: A string, the IPv6 address.
-
-        Returns:
-            A string, the expanded IPv6 address.
-
-        """
-        if isinstance(self, IPv6Network):
-            ip_str = _compat_str(self.network_address)
-        elif isinstance(self, IPv6Interface):
-            ip_str = _compat_str(self.ip)
-        else:
-            ip_str = _compat_str(self)
-
-        ip_int = self._ip_int_from_string(ip_str)
-        hex_str = '%032x' % ip_int
-        parts = [hex_str[x:x + 4] for x in range(0, 32, 4)]
-        if isinstance(self, (_BaseNetwork, IPv6Interface)):
-            return '%s/%d' % (':'.join(parts), self._prefixlen)
-        return ':'.join(parts)
-
-    def _reverse_pointer(self):
-        """Return the reverse DNS pointer name for the IPv6 address.
-
-        This implements the method described in RFC3596 2.5.
-
-        """
-        reverse_chars = self.exploded[::-1].replace(':', '')
-        return '.'.join(reverse_chars) + '.ip6.arpa'
-
-    @property
-    def max_prefixlen(self):
-        return self._max_prefixlen
-
-    @property
-    def version(self):
-        return self._version
-
-
-class IPv6Address(_BaseV6, _BaseAddress):
-
-    """Represent and manipulate single IPv6 Addresses."""
-
-    __slots__ = ('_ip', '__weakref__')
-
-    def __init__(self, address):
-        """Instantiate a new IPv6 address object.
-
-        Args:
-            address: A string or integer representing the IP
-
-              Additionally, an integer can be passed, so
-              IPv6Address('2001:db8::') ==
-                IPv6Address(42540766411282592856903984951653826560)
-              or, more generally
-              IPv6Address(int(IPv6Address('2001:db8::'))) ==
-                IPv6Address('2001:db8::')
-
-        Raises:
-            AddressValueError: If address isn't a valid IPv6 address.
-
-        """
-        # Efficient constructor from integer.
-        if isinstance(address, _compat_int_types):
-            self._check_int_address(address)
-            self._ip = address
-            return
-
-        # Constructing from a packed address
-        if isinstance(address, bytes):
-            self._check_packed_address(address, 16)
-            bvs = _compat_bytes_to_byte_vals(address)
-            self._ip = _compat_int_from_byte_vals(bvs, 'big')
-            return
-
-        # Assume input argument to be string or any object representation
-        # which converts into a formatted IP string.
-        addr_str = _compat_str(address)
-        if '/' in addr_str:
-            raise AddressValueError("Unexpected '/' in %r" % address)
-        self._ip = self._ip_int_from_string(addr_str)
-
-    @property
-    def packed(self):
-        """The binary representation of this address."""
-        return v6_int_to_packed(self._ip)
-
-    @property
-    def is_multicast(self):
-        """Test if the address is reserved for multicast use.
-
-        Returns:
-            A boolean, True if the address is a multicast address.
-            See RFC 2373 2.7 for details.
-
-        """
-        return self in self._constants._multicast_network
-
-    @property
-    def is_reserved(self):
-        """Test if the address is otherwise IETF reserved.
-
-        Returns:
-            A boolean, True if the address is within one of the
-            reserved IPv6 Network ranges.
-
-        """
-        return any(self in x for x in self._constants._reserved_networks)
-
-    @property
-    def is_link_local(self):
-        """Test if the address is reserved for link-local.
-
-        Returns:
-            A boolean, True if the address is reserved per RFC 4291.
-
-        """
-        return self in self._constants._linklocal_network
-
-    @property
-    def is_site_local(self):
-        """Test if the address is reserved for site-local.
-
-        Note that the site-local address space has been deprecated by RFC 3879.
-        Use is_private to test if this address is in the space of unique local
-        addresses as defined by RFC 4193.
-
-        Returns:
-            A boolean, True if the address is reserved per RFC 3513 2.5.6.
-
-        """
-        return self in self._constants._sitelocal_network
-
-    @property
-    def is_private(self):
-        """Test if this address is allocated for private networks.
-
-        Returns:
-            A boolean, True if the address is reserved per
-            iana-ipv6-special-registry.
-
-        """
-        return any(self in net for net in self._constants._private_networks)
-
-    @property
-    def is_global(self):
-        """Test if this address is allocated for public networks.
-
-        Returns:
-            A boolean, true if the address is not reserved per
-            iana-ipv6-special-registry.
-
-        """
-        return not self.is_private
-
-    @property
-    def is_unspecified(self):
-        """Test if the address is unspecified.
-
-        Returns:
-            A boolean, True if this is the unspecified address as defined in
-            RFC 2373 2.5.2.
-
-        """
-        return self._ip == 0
-
-    @property
-    def is_loopback(self):
-        """Test if the address is a loopback address.
-
-        Returns:
-            A boolean, True if the address is a loopback address as defined in
-            RFC 2373 2.5.3.
-
-        """
-        return self._ip == 1
-
-    @property
-    def ipv4_mapped(self):
-        """Return the IPv4 mapped address.
-
-        Returns:
-            If the IPv6 address is a v4 mapped address, return the
-            IPv4 mapped address. Return None otherwise.
-
-        """
-        if (self._ip >> 32) != 0xFFFF:
-            return None
-        return IPv4Address(self._ip & 0xFFFFFFFF)
-
-    @property
-    def teredo(self):
-        """Tuple of embedded teredo IPs.
-
-        Returns:
-            Tuple of the (server, client) IPs or None if the address
-            doesn't appear to be a teredo address (doesn't start with
-            2001::/32)
-
-        """
-        if (self._ip >> 96) != 0x20010000:
-            return None
-        return (IPv4Address((self._ip >> 64) & 0xFFFFFFFF),
-                IPv4Address(~self._ip & 0xFFFFFFFF))
-
-    @property
-    def sixtofour(self):
-        """Return the IPv4 6to4 embedded address.
-
-        Returns:
-            The IPv4 6to4-embedded address if present or None if the
-            address doesn't appear to contain a 6to4 embedded address.
-
-        """
-        if (self._ip >> 112) != 0x2002:
-            return None
-        return IPv4Address((self._ip >> 80) & 0xFFFFFFFF)
-
-
-class IPv6Interface(IPv6Address):
-
-    def __init__(self, address):
-        if isinstance(address, (bytes, _compat_int_types)):
-            IPv6Address.__init__(self, address)
-            self.network = IPv6Network(self._ip)
-            self._prefixlen = self._max_prefixlen
-            return
-        if isinstance(address, tuple):
-            IPv6Address.__init__(self, address[0])
-            if len(address) > 1:
-                self._prefixlen = int(address[1])
-            else:
-                self._prefixlen = self._max_prefixlen
-            self.network = IPv6Network(address, strict=False)
-            self.netmask = self.network.netmask
-            self.hostmask = self.network.hostmask
-            return
-
-        addr = _split_optional_netmask(address)
-        IPv6Address.__init__(self, addr[0])
-        self.network = IPv6Network(address, strict=False)
-        self.netmask = self.network.netmask
-        self._prefixlen = self.network._prefixlen
-        self.hostmask = self.network.hostmask
-
-    def __str__(self):
-        return '%s/%d' % (self._string_from_ip_int(self._ip),
-                          self.network.prefixlen)
-
-    def __eq__(self, other):
-        address_equal = IPv6Address.__eq__(self, other)
-        if not address_equal or address_equal is NotImplemented:
-            return address_equal
-        try:
-            return self.network == other.network
-        except AttributeError:
-            # An interface with an associated network is NOT the
-            # same as an unassociated address. That's why the hash
-            # takes the extra info into account.
-            return False
-
-    def __lt__(self, other):
-        address_less = IPv6Address.__lt__(self, other)
-        if address_less is NotImplemented:
-            return NotImplemented
-        try:
-            return (self.network < other.network or
-                    self.network == other.network and address_less)
-        except AttributeError:
-            # We *do* allow addresses and interfaces to be sorted. The
-            # unassociated address is considered less than all interfaces.
-            return False
-
-    def __hash__(self):
-        return self._ip ^ self._prefixlen ^ int(self.network.network_address)
-
-    __reduce__ = _IPAddressBase.__reduce__
-
-    @property
-    def ip(self):
-        return IPv6Address(self._ip)
-
-    @property
-    def with_prefixlen(self):
-        return '%s/%s' % (self._string_from_ip_int(self._ip),
-                          self._prefixlen)
-
-    @property
-    def with_netmask(self):
-        return '%s/%s' % (self._string_from_ip_int(self._ip),
-                          self.netmask)
-
-    @property
-    def with_hostmask(self):
-        return '%s/%s' % (self._string_from_ip_int(self._ip),
-                          self.hostmask)
-
-    @property
-    def is_unspecified(self):
-        return self._ip == 0 and self.network.is_unspecified
-
-    @property
-    def is_loopback(self):
-        return self._ip == 1 and self.network.is_loopback
-
-
-class IPv6Network(_BaseV6, _BaseNetwork):
-
-    """This class represents and manipulates 128-bit IPv6 networks.
-
-    Attributes: [examples for IPv6('2001:db8::1000/124')]
-        .network_address: IPv6Address('2001:db8::1000')
-        .hostmask: IPv6Address('::f')
-        .broadcast_address: IPv6Address('2001:db8::100f')
-        .netmask: IPv6Address('ffff:ffff:ffff:ffff:ffff:ffff:ffff:fff0')
-        .prefixlen: 124
-
-    """
-
-    # Class to use when creating address objects
-    _address_class = IPv6Address
-
-    def __init__(self, address, strict=True):
-        """Instantiate a new IPv6 Network object.
-
-        Args:
-            address: A string or integer representing the IPv6 network or the
-              IP and prefix/netmask.
-              '2001:db8::/128'
-              '2001:db8:0000:0000:0000:0000:0000:0000/128'
-              '2001:db8::'
-              are all functionally the same in IPv6.  That is to say,
-              failing to provide a subnetmask will create an object with
-              a mask of /128.
-
-              Additionally, an integer can be passed, so
-              IPv6Network('2001:db8::') ==
-                IPv6Network(42540766411282592856903984951653826560)
-              or, more generally
-              IPv6Network(int(IPv6Network('2001:db8::'))) ==
-                IPv6Network('2001:db8::')
-
-            strict: A boolean. If true, ensure that we have been passed
-              A true network address, eg, 2001:db8::1000/124 and not an
-              IP address on a network, eg, 2001:db8::1/124.
-
-        Raises:
-            AddressValueError: If address isn't a valid IPv6 address.
-            NetmaskValueError: If the netmask isn't valid for
-              an IPv6 address.
-            ValueError: If strict was True and a network address was not
-              supplied.
-
-        """
-        _BaseNetwork.__init__(self, address)
-
-        # Efficient constructor from integer or packed address
-        if isinstance(address, (bytes, _compat_int_types)):
-            self.network_address = IPv6Address(address)
-            self.netmask, self._prefixlen = self._make_netmask(
-                self._max_prefixlen)
-            return
-
-        if isinstance(address, tuple):
-            if len(address) > 1:
-                arg = address[1]
-            else:
-                arg = self._max_prefixlen
-            self.netmask, self._prefixlen = self._make_netmask(arg)
-            self.network_address = IPv6Address(address[0])
-            packed = int(self.network_address)
-            if packed & int(self.netmask) != packed:
-                if strict:
-                    raise ValueError('%s has host bits set' % self)
-                else:
-                    self.network_address = IPv6Address(packed &
-                                                       int(self.netmask))
-            return
-
-        # Assume input argument to be string or any object representation
-        # which converts into a formatted IP prefix string.
-        addr = _split_optional_netmask(address)
-
-        self.network_address = IPv6Address(self._ip_int_from_string(addr[0]))
-
-        if len(addr) == 2:
-            arg = addr[1]
-        else:
-            arg = self._max_prefixlen
-        self.netmask, self._prefixlen = self._make_netmask(arg)
-
-        if strict:
-            if (IPv6Address(int(self.network_address) & int(self.netmask)) !=
-                    self.network_address):
-                raise ValueError('%s has host bits set' % self)
-        self.network_address = IPv6Address(int(self.network_address) &
-                                           int(self.netmask))
-
-        if self._prefixlen == (self._max_prefixlen - 1):
-            self.hosts = self.__iter__
-
-    def hosts(self):
-        """Generate Iterator over usable hosts in a network.
-
-          This is like __iter__ except it doesn't return the
-          Subnet-Router anycast address.
-
-        """
-        network = int(self.network_address)
-        broadcast = int(self.broadcast_address)
-        for x in _compat_range(network + 1, broadcast + 1):
-            yield self._address_class(x)
-
-    @property
-    def is_site_local(self):
-        """Test if the address is reserved for site-local.
-
-        Note that the site-local address space has been deprecated by RFC 3879.
-        Use is_private to test if this address is in the space of unique local
-        addresses as defined by RFC 4193.
-
-        Returns:
-            A boolean, True if the address is reserved per RFC 3513 2.5.6.
-
-        """
-        return (self.network_address.is_site_local and
-                self.broadcast_address.is_site_local)
-
-
-class _IPv6Constants(object):
-
-    _linklocal_network = IPv6Network('fe80::/10')
-
-    _multicast_network = IPv6Network('ff00::/8')
-
-    _private_networks = [
-        IPv6Network('::1/128'),
-        IPv6Network('::/128'),
-        IPv6Network('::ffff:0:0/96'),
-        IPv6Network('100::/64'),
-        IPv6Network('2001::/23'),
-        IPv6Network('2001:2::/48'),
-        IPv6Network('2001:db8::/32'),
-        IPv6Network('2001:10::/28'),
-        IPv6Network('fc00::/7'),
-        IPv6Network('fe80::/10'),
-    ]
-
-    _reserved_networks = [
-        IPv6Network('::/8'), IPv6Network('100::/8'),
-        IPv6Network('200::/7'), IPv6Network('400::/6'),
-        IPv6Network('800::/5'), IPv6Network('1000::/4'),
-        IPv6Network('4000::/3'), IPv6Network('6000::/3'),
-        IPv6Network('8000::/3'), IPv6Network('A000::/3'),
-        IPv6Network('C000::/3'), IPv6Network('E000::/4'),
-        IPv6Network('F000::/5'), IPv6Network('F800::/6'),
-        IPv6Network('FE00::/9'),
-    ]
-
-    _sitelocal_network = IPv6Network('fec0::/10')
-
-
-IPv6Address._constants = _IPv6Constants
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__init__.py
deleted file mode 100644
index a6f44a5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__init__.py
+++ /dev/null
@@ -1,347 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-lockfile.py - Platform-independent advisory file locks.
-
-Requires Python 2.5 unless you apply 2.4.diff
-Locking is done on a per-thread basis instead of a per-process basis.
-
-Usage:
-
->>> lock = LockFile('somefile')
->>> try:
-...     lock.acquire()
-... except AlreadyLocked:
-...     print 'somefile', 'is locked already.'
-... except LockFailed:
-...     print 'somefile', 'can\\'t be locked.'
-... else:
-...     print 'got lock'
-got lock
->>> print lock.is_locked()
-True
->>> lock.release()
-
->>> lock = LockFile('somefile')
->>> print lock.is_locked()
-False
->>> with lock:
-...    print lock.is_locked()
-True
->>> print lock.is_locked()
-False
-
->>> lock = LockFile('somefile')
->>> # It is okay to lock twice from the same thread...
->>> with lock:
-...     lock.acquire()
-...
->>> # Though no counter is kept, so you can't unlock multiple times...
->>> print lock.is_locked()
-False
-
-Exceptions:
-
-    Error - base class for other exceptions
-        LockError - base class for all locking exceptions
-            AlreadyLocked - Another thread or process already holds the lock
-            LockFailed - Lock failed for some other reason
-        UnlockError - base class for all unlocking exceptions
-            AlreadyUnlocked - File was not locked.
-            NotMyLock - File was locked but not by the current thread/process
-"""
-
-from __future__ import absolute_import
-
-import functools
-import os
-import socket
-import threading
-import warnings
-
-# Work with PEP8 and non-PEP8 versions of threading module.
-if not hasattr(threading, "current_thread"):
-    threading.current_thread = threading.currentThread
-if not hasattr(threading.Thread, "get_name"):
-    threading.Thread.get_name = threading.Thread.getName
-
-__all__ = ['Error', 'LockError', 'LockTimeout', 'AlreadyLocked',
-           'LockFailed', 'UnlockError', 'NotLocked', 'NotMyLock',
-           'LinkFileLock', 'MkdirFileLock', 'SQLiteFileLock',
-           'LockBase', 'locked']
-
-
-class Error(Exception):
-    """
-    Base class for other exceptions.
-
-    >>> try:
-    ...   raise Error
-    ... except Exception:
-    ...   pass
-    """
-    pass
-
-
-class LockError(Error):
-    """
-    Base class for error arising from attempts to acquire the lock.
-
-    >>> try:
-    ...   raise LockError
-    ... except Error:
-    ...   pass
-    """
-    pass
-
-
-class LockTimeout(LockError):
-    """Raised when lock creation fails within a user-defined period of time.
-
-    >>> try:
-    ...   raise LockTimeout
-    ... except LockError:
-    ...   pass
-    """
-    pass
-
-
-class AlreadyLocked(LockError):
-    """Some other thread/process is locking the file.
-
-    >>> try:
-    ...   raise AlreadyLocked
-    ... except LockError:
-    ...   pass
-    """
-    pass
-
-
-class LockFailed(LockError):
-    """Lock file creation failed for some other reason.
-
-    >>> try:
-    ...   raise LockFailed
-    ... except LockError:
-    ...   pass
-    """
-    pass
-
-
-class UnlockError(Error):
-    """
-    Base class for errors arising from attempts to release the lock.
-
-    >>> try:
-    ...   raise UnlockError
-    ... except Error:
-    ...   pass
-    """
-    pass
-
-
-class NotLocked(UnlockError):
-    """Raised when an attempt is made to unlock an unlocked file.
-
-    >>> try:
-    ...   raise NotLocked
-    ... except UnlockError:
-    ...   pass
-    """
-    pass
-
-
-class NotMyLock(UnlockError):
-    """Raised when an attempt is made to unlock a file someone else locked.
-
-    >>> try:
-    ...   raise NotMyLock
-    ... except UnlockError:
-    ...   pass
-    """
-    pass
-
-
-class _SharedBase(object):
-    def __init__(self, path):
-        self.path = path
-
-    def acquire(self, timeout=None):
-        """
-        Acquire the lock.
-
-        * If timeout is omitted (or None), wait forever trying to lock the
-          file.
-
-        * If timeout > 0, try to acquire the lock for that many seconds.  If
-          the lock period expires and the file is still locked, raise
-          LockTimeout.
-
-        * If timeout <= 0, raise AlreadyLocked immediately if the file is
-          already locked.
-        """
-        raise NotImplemented("implement in subclass")
-
-    def release(self):
-        """
-        Release the lock.
-
-        If the file is not locked, raise NotLocked.
-        """
-        raise NotImplemented("implement in subclass")
-
-    def __enter__(self):
-        """
-        Context manager support.
-        """
-        self.acquire()
-        return self
-
-    def __exit__(self, *_exc):
-        """
-        Context manager support.
-        """
-        self.release()
-
-    def __repr__(self):
-        return "<%s: %r>" % (self.__class__.__name__, self.path)
-
-
-class LockBase(_SharedBase):
-    """Base class for platform-specific lock classes."""
-    def __init__(self, path, threaded=True, timeout=None):
-        """
-        >>> lock = LockBase('somefile')
-        >>> lock = LockBase('somefile', threaded=False)
-        """
-        super(LockBase, self).__init__(path)
-        self.lock_file = os.path.abspath(path) + ".lock"
-        self.hostname = socket.gethostname()
-        self.pid = os.getpid()
-        if threaded:
-            t = threading.current_thread()
-            # Thread objects in Python 2.4 and earlier do not have ident
-            # attrs.  Worm around that.
-            ident = getattr(t, "ident", hash(t))
-            self.tname = "-%x" % (ident & 0xffffffff)
-        else:
-            self.tname = ""
-        dirname = os.path.dirname(self.lock_file)
-
-        # unique name is mostly about the current process, but must
-        # also contain the path -- otherwise, two adjacent locked
-        # files conflict (one file gets locked, creating lock-file and
-        # unique file, the other one gets locked, creating lock-file
-        # and overwriting the already existing lock-file, then one
-        # gets unlocked, deleting both lock-file and unique file,
-        # finally the last lock errors out upon releasing.
-        self.unique_name = os.path.join(dirname,
-                                        "%s%s.%s%s" % (self.hostname,
-                                                       self.tname,
-                                                       self.pid,
-                                                       hash(self.path)))
-        self.timeout = timeout
-
-    def is_locked(self):
-        """
-        Tell whether or not the file is locked.
-        """
-        raise NotImplemented("implement in subclass")
-
-    def i_am_locking(self):
-        """
-        Return True if this object is locking the file.
-        """
-        raise NotImplemented("implement in subclass")
-
-    def break_lock(self):
-        """
-        Remove a lock.  Useful if a locking thread failed to unlock.
-        """
-        raise NotImplemented("implement in subclass")
-
-    def __repr__(self):
-        return "<%s: %r -- %r>" % (self.__class__.__name__, self.unique_name,
-                                   self.path)
-
-
-def _fl_helper(cls, mod, *args, **kwds):
-    warnings.warn("Import from %s module instead of lockfile package" % mod,
-                  DeprecationWarning, stacklevel=2)
-    # This is a bit funky, but it's only for awhile.  The way the unit tests
-    # are constructed this function winds up as an unbound method, so it
-    # actually takes three args, not two.  We want to toss out self.
-    if not isinstance(args[0], str):
-        # We are testing, avoid the first arg
-        args = args[1:]
-    if len(args) == 1 and not kwds:
-        kwds["threaded"] = True
-    return cls(*args, **kwds)
-
-
-def LinkFileLock(*args, **kwds):
-    """Factory function provided for backwards compatibility.
-
-    Do not use in new code.  Instead, import LinkLockFile from the
-    lockfile.linklockfile module.
-    """
-    from . import linklockfile
-    return _fl_helper(linklockfile.LinkLockFile, "lockfile.linklockfile",
-                      *args, **kwds)
-
-
-def MkdirFileLock(*args, **kwds):
-    """Factory function provided for backwards compatibility.
-
-    Do not use in new code.  Instead, import MkdirLockFile from the
-    lockfile.mkdirlockfile module.
-    """
-    from . import mkdirlockfile
-    return _fl_helper(mkdirlockfile.MkdirLockFile, "lockfile.mkdirlockfile",
-                      *args, **kwds)
-
-
-def SQLiteFileLock(*args, **kwds):
-    """Factory function provided for backwards compatibility.
-
-    Do not use in new code.  Instead, import SQLiteLockFile from the
-    lockfile.mkdirlockfile module.
-    """
-    from . import sqlitelockfile
-    return _fl_helper(sqlitelockfile.SQLiteLockFile, "lockfile.sqlitelockfile",
-                      *args, **kwds)
-
-
-def locked(path, timeout=None):
-    """Decorator which enables locks for decorated function.
-
-    Arguments:
-     - path: path for lockfile.
-     - timeout (optional): Timeout for acquiring lock.
-
-     Usage:
-         @locked('/var/run/myname', timeout=0)
-         def myname(...):
-             ...
-    """
-    def decor(func):
-        @functools.wraps(func)
-        def wrapper(*args, **kwargs):
-            lock = FileLock(path, timeout=timeout)
-            lock.acquire()
-            try:
-                return func(*args, **kwargs)
-            finally:
-                lock.release()
-        return wrapper
-    return decor
-
-
-if hasattr(os, "link"):
-    from . import linklockfile as _llf
-    LockFile = _llf.LinkLockFile
-else:
-    from . import mkdirlockfile as _mlf
-    LockFile = _mlf.MkdirLockFile
-
-FileLock = LockFile
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 418c6af..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/linklockfile.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/linklockfile.cpython-37.pyc
deleted file mode 100644
index 7c5c820..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/linklockfile.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/mkdirlockfile.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/mkdirlockfile.cpython-37.pyc
deleted file mode 100644
index 1984697..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/__pycache__/mkdirlockfile.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/linklockfile.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/linklockfile.py
deleted file mode 100644
index 2ca9be0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/linklockfile.py
+++ /dev/null
@@ -1,73 +0,0 @@
-from __future__ import absolute_import
-
-import time
-import os
-
-from . import (LockBase, LockFailed, NotLocked, NotMyLock, LockTimeout,
-               AlreadyLocked)
-
-
-class LinkLockFile(LockBase):
-    """Lock access to a file using atomic property of link(2).
-
-    >>> lock = LinkLockFile('somefile')
-    >>> lock = LinkLockFile('somefile', threaded=False)
-    """
-
-    def acquire(self, timeout=None):
-        try:
-            open(self.unique_name, "wb").close()
-        except IOError:
-            raise LockFailed("failed to create %s" % self.unique_name)
-
-        timeout = timeout if timeout is not None else self.timeout
-        end_time = time.time()
-        if timeout is not None and timeout > 0:
-            end_time += timeout
-
-        while True:
-            # Try and create a hard link to it.
-            try:
-                os.link(self.unique_name, self.lock_file)
-            except OSError:
-                # Link creation failed.  Maybe we've double-locked?
-                nlinks = os.stat(self.unique_name).st_nlink
-                if nlinks == 2:
-                    # The original link plus the one I created == 2.  We're
-                    # good to go.
-                    return
-                else:
-                    # Otherwise the lock creation failed.
-                    if timeout is not None and time.time() > end_time:
-                        os.unlink(self.unique_name)
-                        if timeout > 0:
-                            raise LockTimeout("Timeout waiting to acquire"
-                                              " lock for %s" %
-                                              self.path)
-                        else:
-                            raise AlreadyLocked("%s is already locked" %
-                                                self.path)
-                    time.sleep(timeout is not None and timeout / 10 or 0.1)
-            else:
-                # Link creation succeeded.  We're good to go.
-                return
-
-    def release(self):
-        if not self.is_locked():
-            raise NotLocked("%s is not locked" % self.path)
-        elif not os.path.exists(self.unique_name):
-            raise NotMyLock("%s is locked, but not by me" % self.path)
-        os.unlink(self.unique_name)
-        os.unlink(self.lock_file)
-
-    def is_locked(self):
-        return os.path.exists(self.lock_file)
-
-    def i_am_locking(self):
-        return (self.is_locked() and
-                os.path.exists(self.unique_name) and
-                os.stat(self.unique_name).st_nlink == 2)
-
-    def break_lock(self):
-        if os.path.exists(self.lock_file):
-            os.unlink(self.lock_file)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/mkdirlockfile.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/mkdirlockfile.py
deleted file mode 100644
index 05a8c96..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/mkdirlockfile.py
+++ /dev/null
@@ -1,84 +0,0 @@
-from __future__ import absolute_import, division
-
-import time
-import os
-import sys
-import errno
-
-from . import (LockBase, LockFailed, NotLocked, NotMyLock, LockTimeout,
-               AlreadyLocked)
-
-
-class MkdirLockFile(LockBase):
-    """Lock file by creating a directory."""
-    def __init__(self, path, threaded=True, timeout=None):
-        """
-        >>> lock = MkdirLockFile('somefile')
-        >>> lock = MkdirLockFile('somefile', threaded=False)
-        """
-        LockBase.__init__(self, path, threaded, timeout)
-        # Lock file itself is a directory.  Place the unique file name into
-        # it.
-        self.unique_name = os.path.join(self.lock_file,
-                                        "%s.%s%s" % (self.hostname,
-                                                     self.tname,
-                                                     self.pid))
-
-    def acquire(self, timeout=None):
-        timeout = timeout if timeout is not None else self.timeout
-        end_time = time.time()
-        if timeout is not None and timeout > 0:
-            end_time += timeout
-
-        if timeout is None:
-            wait = 0.1
-        else:
-            wait = max(0, timeout / 10)
-
-        while True:
-            try:
-                os.mkdir(self.lock_file)
-            except OSError:
-                err = sys.exc_info()[1]
-                if err.errno == errno.EEXIST:
-                    # Already locked.
-                    if os.path.exists(self.unique_name):
-                        # Already locked by me.
-                        return
-                    if timeout is not None and time.time() > end_time:
-                        if timeout > 0:
-                            raise LockTimeout("Timeout waiting to acquire"
-                                              " lock for %s" %
-                                              self.path)
-                        else:
-                            # Someone else has the lock.
-                            raise AlreadyLocked("%s is already locked" %
-                                                self.path)
-                    time.sleep(wait)
-                else:
-                    # Couldn't create the lock for some other reason
-                    raise LockFailed("failed to create %s" % self.lock_file)
-            else:
-                open(self.unique_name, "wb").close()
-                return
-
-    def release(self):
-        if not self.is_locked():
-            raise NotLocked("%s is not locked" % self.path)
-        elif not os.path.exists(self.unique_name):
-            raise NotMyLock("%s is locked, but not by me" % self.path)
-        os.unlink(self.unique_name)
-        os.rmdir(self.lock_file)
-
-    def is_locked(self):
-        return os.path.exists(self.lock_file)
-
-    def i_am_locking(self):
-        return (self.is_locked() and
-                os.path.exists(self.unique_name))
-
-    def break_lock(self):
-        if os.path.exists(self.lock_file):
-            for name in os.listdir(self.lock_file):
-                os.unlink(os.path.join(self.lock_file, name))
-            os.rmdir(self.lock_file)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/pidlockfile.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/pidlockfile.py
deleted file mode 100644
index 069e85b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/pidlockfile.py
+++ /dev/null
@@ -1,190 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# pidlockfile.py
-#
-# Copyright © 2008–2009 Ben Finney <ben+python@benfinney.id.au>
-#
-# This is free software: you may copy, modify, and/or distribute this work
-# under the terms of the Python Software Foundation License, version 2 or
-# later as published by the Python Software Foundation.
-# No warranty expressed or implied. See the file LICENSE.PSF-2 for details.
-
-""" Lockfile behaviour implemented via Unix PID files.
-    """
-
-from __future__ import absolute_import
-
-import errno
-import os
-import time
-
-from . import (LockBase, AlreadyLocked, LockFailed, NotLocked, NotMyLock,
-               LockTimeout)
-
-
-class PIDLockFile(LockBase):
-    """ Lockfile implemented as a Unix PID file.
-
-    The lock file is a normal file named by the attribute `path`.
-    A lock's PID file contains a single line of text, containing
-    the process ID (PID) of the process that acquired the lock.
-
-    >>> lock = PIDLockFile('somefile')
-    >>> lock = PIDLockFile('somefile')
-    """
-
-    def __init__(self, path, threaded=False, timeout=None):
-        # pid lockfiles don't support threaded operation, so always force
-        # False as the threaded arg.
-        LockBase.__init__(self, path, False, timeout)
-        self.unique_name = self.path
-
-    def read_pid(self):
-        """ Get the PID from the lock file.
-            """
-        return read_pid_from_pidfile(self.path)
-
-    def is_locked(self):
-        """ Test if the lock is currently held.
-
-            The lock is held if the PID file for this lock exists.
-
-            """
-        return os.path.exists(self.path)
-
-    def i_am_locking(self):
-        """ Test if the lock is held by the current process.
-
-        Returns ``True`` if the current process ID matches the
-        number stored in the PID file.
-        """
-        return self.is_locked() and os.getpid() == self.read_pid()
-
-    def acquire(self, timeout=None):
-        """ Acquire the lock.
-
-        Creates the PID file for this lock, or raises an error if
-        the lock could not be acquired.
-        """
-
-        timeout = timeout if timeout is not None else self.timeout
-        end_time = time.time()
-        if timeout is not None and timeout > 0:
-            end_time += timeout
-
-        while True:
-            try:
-                write_pid_to_pidfile(self.path)
-            except OSError as exc:
-                if exc.errno == errno.EEXIST:
-                    # The lock creation failed.  Maybe sleep a bit.
-                    if time.time() > end_time:
-                        if timeout is not None and timeout > 0:
-                            raise LockTimeout("Timeout waiting to acquire"
-                                              " lock for %s" %
-                                              self.path)
-                        else:
-                            raise AlreadyLocked("%s is already locked" %
-                                                self.path)
-                    time.sleep(timeout is not None and timeout / 10 or 0.1)
-                else:
-                    raise LockFailed("failed to create %s" % self.path)
-            else:
-                return
-
-    def release(self):
-        """ Release the lock.
-
-            Removes the PID file to release the lock, or raises an
-            error if the current process does not hold the lock.
-
-            """
-        if not self.is_locked():
-            raise NotLocked("%s is not locked" % self.path)
-        if not self.i_am_locking():
-            raise NotMyLock("%s is locked, but not by me" % self.path)
-        remove_existing_pidfile(self.path)
-
-    def break_lock(self):
-        """ Break an existing lock.
-
-            Removes the PID file if it already exists, otherwise does
-            nothing.
-
-            """
-        remove_existing_pidfile(self.path)
-
-
-def read_pid_from_pidfile(pidfile_path):
-    """ Read the PID recorded in the named PID file.
-
-        Read and return the numeric PID recorded as text in the named
-        PID file. If the PID file cannot be read, or if the content is
-        not a valid PID, return ``None``.
-
-        """
-    pid = None
-    try:
-        pidfile = open(pidfile_path, 'r')
-    except IOError:
-        pass
-    else:
-        # According to the FHS 2.3 section on PID files in /var/run:
-        #
-        #   The file must consist of the process identifier in
-        #   ASCII-encoded decimal, followed by a newline character.
-        #
-        #   Programs that read PID files should be somewhat flexible
-        #   in what they accept; i.e., they should ignore extra
-        #   whitespace, leading zeroes, absence of the trailing
-        #   newline, or additional lines in the PID file.
-
-        line = pidfile.readline().strip()
-        try:
-            pid = int(line)
-        except ValueError:
-            pass
-        pidfile.close()
-
-    return pid
-
-
-def write_pid_to_pidfile(pidfile_path):
-    """ Write the PID in the named PID file.
-
-        Get the numeric process ID (“PID”) of the current process
-        and write it to the named file as a line of text.
-
-        """
-    open_flags = (os.O_CREAT | os.O_EXCL | os.O_WRONLY)
-    open_mode = 0o644
-    pidfile_fd = os.open(pidfile_path, open_flags, open_mode)
-    pidfile = os.fdopen(pidfile_fd, 'w')
-
-    # According to the FHS 2.3 section on PID files in /var/run:
-    #
-    #   The file must consist of the process identifier in
-    #   ASCII-encoded decimal, followed by a newline character. For
-    #   example, if crond was process number 25, /var/run/crond.pid
-    #   would contain three characters: two, five, and newline.
-
-    pid = os.getpid()
-    pidfile.write("%s\n" % pid)
-    pidfile.close()
-
-
-def remove_existing_pidfile(pidfile_path):
-    """ Remove the named PID file if it exists.
-
-        Removing a PID file that doesn't already exist puts us in the
-        desired state, so we ignore the condition if the file does not
-        exist.
-
-        """
-    try:
-        os.remove(pidfile_path)
-    except OSError as exc:
-        if exc.errno == errno.ENOENT:
-            pass
-        else:
-            raise
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/sqlitelockfile.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/sqlitelockfile.py
deleted file mode 100644
index f997e24..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/sqlitelockfile.py
+++ /dev/null
@@ -1,156 +0,0 @@
-from __future__ import absolute_import, division
-
-import time
-import os
-
-try:
-    unicode
-except NameError:
-    unicode = str
-
-from . import LockBase, NotLocked, NotMyLock, LockTimeout, AlreadyLocked
-
-
-class SQLiteLockFile(LockBase):
-    "Demonstrate SQL-based locking."
-
-    testdb = None
-
-    def __init__(self, path, threaded=True, timeout=None):
-        """
-        >>> lock = SQLiteLockFile('somefile')
-        >>> lock = SQLiteLockFile('somefile', threaded=False)
-        """
-        LockBase.__init__(self, path, threaded, timeout)
-        self.lock_file = unicode(self.lock_file)
-        self.unique_name = unicode(self.unique_name)
-
-        if SQLiteLockFile.testdb is None:
-            import tempfile
-            _fd, testdb = tempfile.mkstemp()
-            os.close(_fd)
-            os.unlink(testdb)
-            del _fd, tempfile
-            SQLiteLockFile.testdb = testdb
-
-        import sqlite3
-        self.connection = sqlite3.connect(SQLiteLockFile.testdb)
-
-        c = self.connection.cursor()
-        try:
-            c.execute("create table locks"
-                      "("
-                      "   lock_file varchar(32),"
-                      "   unique_name varchar(32)"
-                      ")")
-        except sqlite3.OperationalError:
-            pass
-        else:
-            self.connection.commit()
-            import atexit
-            atexit.register(os.unlink, SQLiteLockFile.testdb)
-
-    def acquire(self, timeout=None):
-        timeout = timeout if timeout is not None else self.timeout
-        end_time = time.time()
-        if timeout is not None and timeout > 0:
-            end_time += timeout
-
-        if timeout is None:
-            wait = 0.1
-        elif timeout <= 0:
-            wait = 0
-        else:
-            wait = timeout / 10
-
-        cursor = self.connection.cursor()
-
-        while True:
-            if not self.is_locked():
-                # Not locked.  Try to lock it.
-                cursor.execute("insert into locks"
-                               "  (lock_file, unique_name)"
-                               "  values"
-                               "  (?, ?)",
-                               (self.lock_file, self.unique_name))
-                self.connection.commit()
-
-                # Check to see if we are the only lock holder.
-                cursor.execute("select * from locks"
-                               "  where unique_name = ?",
-                               (self.unique_name,))
-                rows = cursor.fetchall()
-                if len(rows) > 1:
-                    # Nope.  Someone else got there.  Remove our lock.
-                    cursor.execute("delete from locks"
-                                   "  where unique_name = ?",
-                                   (self.unique_name,))
-                    self.connection.commit()
-                else:
-                    # Yup.  We're done, so go home.
-                    return
-            else:
-                # Check to see if we are the only lock holder.
-                cursor.execute("select * from locks"
-                               "  where unique_name = ?",
-                               (self.unique_name,))
-                rows = cursor.fetchall()
-                if len(rows) == 1:
-                    # We're the locker, so go home.
-                    return
-
-            # Maybe we should wait a bit longer.
-            if timeout is not None and time.time() > end_time:
-                if timeout > 0:
-                    # No more waiting.
-                    raise LockTimeout("Timeout waiting to acquire"
-                                      " lock for %s" %
-                                      self.path)
-                else:
-                    # Someone else has the lock and we are impatient..
-                    raise AlreadyLocked("%s is already locked" % self.path)
-
-            # Well, okay.  We'll give it a bit longer.
-            time.sleep(wait)
-
-    def release(self):
-        if not self.is_locked():
-            raise NotLocked("%s is not locked" % self.path)
-        if not self.i_am_locking():
-            raise NotMyLock("%s is locked, but not by me (by %s)" %
-                            (self.unique_name, self._who_is_locking()))
-        cursor = self.connection.cursor()
-        cursor.execute("delete from locks"
-                       "  where unique_name = ?",
-                       (self.unique_name,))
-        self.connection.commit()
-
-    def _who_is_locking(self):
-        cursor = self.connection.cursor()
-        cursor.execute("select unique_name from locks"
-                       "  where lock_file = ?",
-                       (self.lock_file,))
-        return cursor.fetchone()[0]
-
-    def is_locked(self):
-        cursor = self.connection.cursor()
-        cursor.execute("select * from locks"
-                       "  where lock_file = ?",
-                       (self.lock_file,))
-        rows = cursor.fetchall()
-        return not not rows
-
-    def i_am_locking(self):
-        cursor = self.connection.cursor()
-        cursor.execute("select * from locks"
-                       "  where lock_file = ?"
-                       "    and unique_name = ?",
-                       (self.lock_file, self.unique_name))
-        return not not cursor.fetchall()
-
-    def break_lock(self):
-        cursor = self.connection.cursor()
-        cursor.execute("delete from locks"
-                       "  where lock_file = ?",
-                       (self.lock_file,))
-        self.connection.commit()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/symlinklockfile.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/symlinklockfile.py
deleted file mode 100644
index 23b41f5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/lockfile/symlinklockfile.py
+++ /dev/null
@@ -1,70 +0,0 @@
-from __future__ import absolute_import
-
-import os
-import time
-
-from . import (LockBase, NotLocked, NotMyLock, LockTimeout,
-               AlreadyLocked)
-
-
-class SymlinkLockFile(LockBase):
-    """Lock access to a file using symlink(2)."""
-
-    def __init__(self, path, threaded=True, timeout=None):
-        # super(SymlinkLockFile).__init(...)
-        LockBase.__init__(self, path, threaded, timeout)
-        # split it back!
-        self.unique_name = os.path.split(self.unique_name)[1]
-
-    def acquire(self, timeout=None):
-        # Hopefully unnecessary for symlink.
-        # try:
-        #     open(self.unique_name, "wb").close()
-        # except IOError:
-        #     raise LockFailed("failed to create %s" % self.unique_name)
-        timeout = timeout if timeout is not None else self.timeout
-        end_time = time.time()
-        if timeout is not None and timeout > 0:
-            end_time += timeout
-
-        while True:
-            # Try and create a symbolic link to it.
-            try:
-                os.symlink(self.unique_name, self.lock_file)
-            except OSError:
-                # Link creation failed.  Maybe we've double-locked?
-                if self.i_am_locking():
-                    # Linked to out unique name. Proceed.
-                    return
-                else:
-                    # Otherwise the lock creation failed.
-                    if timeout is not None and time.time() > end_time:
-                        if timeout > 0:
-                            raise LockTimeout("Timeout waiting to acquire"
-                                              " lock for %s" %
-                                              self.path)
-                        else:
-                            raise AlreadyLocked("%s is already locked" %
-                                                self.path)
-                    time.sleep(timeout / 10 if timeout is not None else 0.1)
-            else:
-                # Link creation succeeded.  We're good to go.
-                return
-
-    def release(self):
-        if not self.is_locked():
-            raise NotLocked("%s is not locked" % self.path)
-        elif not self.i_am_locking():
-            raise NotMyLock("%s is locked, but not by me" % self.path)
-        os.unlink(self.lock_file)
-
-    def is_locked(self):
-        return os.path.islink(self.lock_file)
-
-    def i_am_locking(self):
-        return (os.path.islink(self.lock_file)
-                and os.readlink(self.lock_file) == self.unique_name)
-
-    def break_lock(self):
-        if os.path.islink(self.lock_file):  # exists && link
-            os.unlink(self.lock_file)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__init__.py
deleted file mode 100644
index 2afca5a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__init__.py
+++ /dev/null
@@ -1,66 +0,0 @@
-# coding: utf-8
-from pip._vendor.msgpack._version import version
-from pip._vendor.msgpack.exceptions import *
-
-from collections import namedtuple
-
-
-class ExtType(namedtuple('ExtType', 'code data')):
-    """ExtType represents ext type in msgpack."""
-    def __new__(cls, code, data):
-        if not isinstance(code, int):
-            raise TypeError("code must be int")
-        if not isinstance(data, bytes):
-            raise TypeError("data must be bytes")
-        if not 0 <= code <= 127:
-            raise ValueError("code must be 0~127")
-        return super(ExtType, cls).__new__(cls, code, data)
-
-
-import os
-if os.environ.get('MSGPACK_PUREPYTHON'):
-    from pip._vendor.msgpack.fallback import Packer, unpackb, Unpacker
-else:
-    try:
-        from pip._vendor.msgpack._packer import Packer
-        from pip._vendor.msgpack._unpacker import unpackb, Unpacker
-    except ImportError:
-        from pip._vendor.msgpack.fallback import Packer, unpackb, Unpacker
-
-
-def pack(o, stream, **kwargs):
-    """
-    Pack object `o` and write it to `stream`
-
-    See :class:`Packer` for options.
-    """
-    packer = Packer(**kwargs)
-    stream.write(packer.pack(o))
-
-
-def packb(o, **kwargs):
-    """
-    Pack object `o` and return packed bytes
-
-    See :class:`Packer` for options.
-    """
-    return Packer(**kwargs).pack(o)
-
-
-def unpack(stream, **kwargs):
-    """
-    Unpack an object from `stream`.
-
-    Raises `ExtraData` when `stream` contains extra bytes.
-    See :class:`Unpacker` for options.
-    """
-    data = stream.read()
-    return unpackb(data, **kwargs)
-
-
-# alias for compatibility to simplejson/marshal/pickle.
-load = unpack
-loads = unpackb
-
-dump = pack
-dumps = packb
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 5a04b77..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/_version.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/_version.cpython-37.pyc
deleted file mode 100644
index db58f9d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/_version.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/exceptions.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/exceptions.cpython-37.pyc
deleted file mode 100644
index f5f0908..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/exceptions.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/fallback.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/fallback.cpython-37.pyc
deleted file mode 100644
index b0d2505..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/__pycache__/fallback.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/_version.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/_version.py
deleted file mode 100644
index d28f0de..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/_version.py
+++ /dev/null
@@ -1 +0,0 @@
-version = (0, 5, 6)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/exceptions.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/exceptions.py
deleted file mode 100644
index 9766881..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/exceptions.py
+++ /dev/null
@@ -1,41 +0,0 @@
-class UnpackException(Exception):
-    """Deprecated.  Use Exception instead to catch all exception during unpacking."""
-
-
-class BufferFull(UnpackException):
-    pass
-
-
-class OutOfData(UnpackException):
-    pass
-
-
-class UnpackValueError(UnpackException, ValueError):
-    """Deprecated.  Use ValueError instead."""
-
-
-class ExtraData(UnpackValueError):
-    def __init__(self, unpacked, extra):
-        self.unpacked = unpacked
-        self.extra = extra
-
-    def __str__(self):
-        return "unpack(b) received extra data."
-
-
-class PackException(Exception):
-    """Deprecated.  Use Exception instead to catch all exception during packing."""
-
-
-class PackValueError(PackException, ValueError):
-    """PackValueError is raised when type of input data is supported but it's value is unsupported.
-
-    Deprecated.  Use ValueError instead.
-    """
-
-
-class PackOverflowError(PackValueError, OverflowError):
-    """PackOverflowError is raised when integer value is out of range of msgpack support [-2**31, 2**32).
-
-    Deprecated.  Use ValueError instead.
-    """
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/fallback.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/fallback.py
deleted file mode 100644
index 9418421..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/msgpack/fallback.py
+++ /dev/null
@@ -1,977 +0,0 @@
-"""Fallback pure Python implementation of msgpack"""
-
-import sys
-import struct
-import warnings
-
-if sys.version_info[0] == 3:
-    PY3 = True
-    int_types = int
-    Unicode = str
-    xrange = range
-    def dict_iteritems(d):
-        return d.items()
-else:
-    PY3 = False
-    int_types = (int, long)
-    Unicode = unicode
-    def dict_iteritems(d):
-        return d.iteritems()
-
-
-if hasattr(sys, 'pypy_version_info'):
-    # cStringIO is slow on PyPy, StringIO is faster.  However: PyPy's own
-    # StringBuilder is fastest.
-    from __pypy__ import newlist_hint
-    try:
-        from __pypy__.builders import BytesBuilder as StringBuilder
-    except ImportError:
-        from __pypy__.builders import StringBuilder
-    USING_STRINGBUILDER = True
-    class StringIO(object):
-        def __init__(self, s=b''):
-            if s:
-                self.builder = StringBuilder(len(s))
-                self.builder.append(s)
-            else:
-                self.builder = StringBuilder()
-        def write(self, s):
-            if isinstance(s, memoryview):
-                s = s.tobytes()
-            elif isinstance(s, bytearray):
-                s = bytes(s)
-            self.builder.append(s)
-        def getvalue(self):
-            return self.builder.build()
-else:
-    USING_STRINGBUILDER = False
-    from io import BytesIO as StringIO
-    newlist_hint = lambda size: []
-
-
-from pip._vendor.msgpack.exceptions import (
-    BufferFull,
-    OutOfData,
-    UnpackValueError,
-    PackValueError,
-    PackOverflowError,
-    ExtraData)
-
-from pip._vendor.msgpack import ExtType
-
-
-EX_SKIP                 = 0
-EX_CONSTRUCT            = 1
-EX_READ_ARRAY_HEADER    = 2
-EX_READ_MAP_HEADER      = 3
-
-TYPE_IMMEDIATE          = 0
-TYPE_ARRAY              = 1
-TYPE_MAP                = 2
-TYPE_RAW                = 3
-TYPE_BIN                = 4
-TYPE_EXT                = 5
-
-DEFAULT_RECURSE_LIMIT = 511
-
-
-def _check_type_strict(obj, t, type=type, tuple=tuple):
-    if type(t) is tuple:
-        return type(obj) in t
-    else:
-        return type(obj) is t
-
-
-def _get_data_from_buffer(obj):
-    try:
-        view = memoryview(obj)
-    except TypeError:
-        # try to use legacy buffer protocol if 2.7, otherwise re-raise
-        if not PY3:
-            view = memoryview(buffer(obj))
-            warnings.warn("using old buffer interface to unpack %s; "
-                          "this leads to unpacking errors if slicing is used and "
-                          "will be removed in a future version" % type(obj),
-                          RuntimeWarning)
-        else:
-            raise
-    if view.itemsize != 1:
-        raise ValueError("cannot unpack from multi-byte object")
-    return view
-
-
-def unpack(stream, **kwargs):
-    warnings.warn(
-        "Direct calling implementation's unpack() is deprecated, Use msgpack.unpack() or unpackb() instead.",
-        PendingDeprecationWarning)
-    data = stream.read()
-    return unpackb(data, **kwargs)
-
-
-def unpackb(packed, **kwargs):
-    """
-    Unpack an object from `packed`.
-
-    Raises `ExtraData` when `packed` contains extra bytes.
-    See :class:`Unpacker` for options.
-    """
-    unpacker = Unpacker(None, **kwargs)
-    unpacker.feed(packed)
-    try:
-        ret = unpacker._unpack()
-    except OutOfData:
-        raise UnpackValueError("Data is not enough.")
-    if unpacker._got_extradata():
-        raise ExtraData(ret, unpacker._get_extradata())
-    return ret
-
-
-class Unpacker(object):
-    """Streaming unpacker.
-
-    arguments:
-
-    :param file_like:
-        File-like object having `.read(n)` method.
-        If specified, unpacker reads serialized data from it and :meth:`feed()` is not usable.
-
-    :param int read_size:
-        Used as `file_like.read(read_size)`. (default: `min(16*1024, max_buffer_size)`)
-
-    :param bool use_list:
-        If true, unpack msgpack array to Python list.
-        Otherwise, unpack to Python tuple. (default: True)
-
-    :param bool raw:
-        If true, unpack msgpack raw to Python bytes (default).
-        Otherwise, unpack to Python str (or unicode on Python 2) by decoding
-        with UTF-8 encoding (recommended).
-        Currently, the default is true, but it will be changed to false in
-        near future.  So you must specify it explicitly for keeping backward
-        compatibility.
-
-        *encoding* option which is deprecated overrides this option.
-
-    :param callable object_hook:
-        When specified, it should be callable.
-        Unpacker calls it with a dict argument after unpacking msgpack map.
-        (See also simplejson)
-
-    :param callable object_pairs_hook:
-        When specified, it should be callable.
-        Unpacker calls it with a list of key-value pairs after unpacking msgpack map.
-        (See also simplejson)
-
-    :param str encoding:
-        Encoding used for decoding msgpack raw.
-        If it is None (default), msgpack raw is deserialized to Python bytes.
-
-    :param str unicode_errors:
-        (deprecated) Used for decoding msgpack raw with *encoding*.
-        (default: `'strict'`)
-
-    :param int max_buffer_size:
-        Limits size of data waiting unpacked.  0 means system's INT_MAX (default).
-        Raises `BufferFull` exception when it is insufficient.
-        You should set this parameter when unpacking data from untrusted source.
-
-    :param int max_str_len:
-        Limits max length of str. (default: 2**31-1)
-
-    :param int max_bin_len:
-        Limits max length of bin. (default: 2**31-1)
-
-    :param int max_array_len:
-        Limits max length of array. (default: 2**31-1)
-
-    :param int max_map_len:
-        Limits max length of map. (default: 2**31-1)
-
-
-    example of streaming deserialize from file-like object::
-
-        unpacker = Unpacker(file_like, raw=False)
-        for o in unpacker:
-            process(o)
-
-    example of streaming deserialize from socket::
-
-        unpacker = Unpacker(raw=False)
-        while True:
-            buf = sock.recv(1024**2)
-            if not buf:
-                break
-            unpacker.feed(buf)
-            for o in unpacker:
-                process(o)
-    """
-
-    def __init__(self, file_like=None, read_size=0, use_list=True, raw=True,
-                 object_hook=None, object_pairs_hook=None, list_hook=None,
-                 encoding=None, unicode_errors=None, max_buffer_size=0,
-                 ext_hook=ExtType,
-                 max_str_len=2147483647, # 2**32-1
-                 max_bin_len=2147483647,
-                 max_array_len=2147483647,
-                 max_map_len=2147483647,
-                 max_ext_len=2147483647):
-
-        if encoding is not None:
-            warnings.warn(
-                "encoding is deprecated, Use raw=False instead.",
-                PendingDeprecationWarning)
-
-        if unicode_errors is None:
-            unicode_errors = 'strict'
-
-        if file_like is None:
-            self._feeding = True
-        else:
-            if not callable(file_like.read):
-                raise TypeError("`file_like.read` must be callable")
-            self.file_like = file_like
-            self._feeding = False
-
-        #: array of bytes fed.
-        self._buffer = bytearray()
-        # Some very old pythons don't support `struct.unpack_from()` with a
-        # `bytearray`. So we wrap it in a `buffer()` there.
-        if sys.version_info < (2, 7, 6):
-            self._buffer_view = buffer(self._buffer)
-        else:
-            self._buffer_view = self._buffer
-        #: Which position we currently reads
-        self._buff_i = 0
-
-        # When Unpacker is used as an iterable, between the calls to next(),
-        # the buffer is not "consumed" completely, for efficiency sake.
-        # Instead, it is done sloppily.  To make sure we raise BufferFull at
-        # the correct moments, we have to keep track of how sloppy we were.
-        # Furthermore, when the buffer is incomplete (that is: in the case
-        # we raise an OutOfData) we need to rollback the buffer to the correct
-        # state, which _buf_checkpoint records.
-        self._buf_checkpoint = 0
-
-        self._max_buffer_size = max_buffer_size or 2**31-1
-        if read_size > self._max_buffer_size:
-            raise ValueError("read_size must be smaller than max_buffer_size")
-        self._read_size = read_size or min(self._max_buffer_size, 16*1024)
-        self._raw = bool(raw)
-        self._encoding = encoding
-        self._unicode_errors = unicode_errors
-        self._use_list = use_list
-        self._list_hook = list_hook
-        self._object_hook = object_hook
-        self._object_pairs_hook = object_pairs_hook
-        self._ext_hook = ext_hook
-        self._max_str_len = max_str_len
-        self._max_bin_len = max_bin_len
-        self._max_array_len = max_array_len
-        self._max_map_len = max_map_len
-        self._max_ext_len = max_ext_len
-        self._stream_offset = 0
-
-        if list_hook is not None and not callable(list_hook):
-            raise TypeError('`list_hook` is not callable')
-        if object_hook is not None and not callable(object_hook):
-            raise TypeError('`object_hook` is not callable')
-        if object_pairs_hook is not None and not callable(object_pairs_hook):
-            raise TypeError('`object_pairs_hook` is not callable')
-        if object_hook is not None and object_pairs_hook is not None:
-            raise TypeError("object_pairs_hook and object_hook are mutually "
-                            "exclusive")
-        if not callable(ext_hook):
-            raise TypeError("`ext_hook` is not callable")
-
-    def feed(self, next_bytes):
-        assert self._feeding
-        view = _get_data_from_buffer(next_bytes)
-        if (len(self._buffer) - self._buff_i + len(view) > self._max_buffer_size):
-            raise BufferFull
-
-        # Strip buffer before checkpoint before reading file.
-        if self._buf_checkpoint > 0:
-            del self._buffer[:self._buf_checkpoint]
-            self._buff_i -= self._buf_checkpoint
-            self._buf_checkpoint = 0
-
-        self._buffer += view
-
-    def _consume(self):
-        """ Gets rid of the used parts of the buffer. """
-        self._stream_offset += self._buff_i - self._buf_checkpoint
-        self._buf_checkpoint = self._buff_i
-
-    def _got_extradata(self):
-        return self._buff_i < len(self._buffer)
-
-    def _get_extradata(self):
-        return self._buffer[self._buff_i:]
-
-    def read_bytes(self, n):
-        return self._read(n)
-
-    def _read(self, n):
-        # (int) -> bytearray
-        self._reserve(n)
-        i = self._buff_i
-        self._buff_i = i+n
-        return self._buffer[i:i+n]
-
-    def _reserve(self, n):
-        remain_bytes = len(self._buffer) - self._buff_i - n
-
-        # Fast path: buffer has n bytes already
-        if remain_bytes >= 0:
-            return
-
-        if self._feeding:
-            self._buff_i = self._buf_checkpoint
-            raise OutOfData
-
-        # Strip buffer before checkpoint before reading file.
-        if self._buf_checkpoint > 0:
-            del self._buffer[:self._buf_checkpoint]
-            self._buff_i -= self._buf_checkpoint
-            self._buf_checkpoint = 0
-
-        # Read from file
-        remain_bytes = -remain_bytes
-        while remain_bytes > 0:
-            to_read_bytes = max(self._read_size, remain_bytes)
-            read_data = self.file_like.read(to_read_bytes)
-            if not read_data:
-                break
-            assert isinstance(read_data, bytes)
-            self._buffer += read_data
-            remain_bytes -= len(read_data)
-
-        if len(self._buffer) < n + self._buff_i:
-            self._buff_i = 0  # rollback
-            raise OutOfData
-
-    def _read_header(self, execute=EX_CONSTRUCT):
-        typ = TYPE_IMMEDIATE
-        n = 0
-        obj = None
-        self._reserve(1)
-        b = self._buffer[self._buff_i]
-        self._buff_i += 1
-        if b & 0b10000000 == 0:
-            obj = b
-        elif b & 0b11100000 == 0b11100000:
-            obj = -1 - (b ^ 0xff)
-        elif b & 0b11100000 == 0b10100000:
-            n = b & 0b00011111
-            typ = TYPE_RAW
-            if n > self._max_str_len:
-                raise UnpackValueError("%s exceeds max_str_len(%s)", n, self._max_str_len)
-            obj = self._read(n)
-        elif b & 0b11110000 == 0b10010000:
-            n = b & 0b00001111
-            typ = TYPE_ARRAY
-            if n > self._max_array_len:
-                raise UnpackValueError("%s exceeds max_array_len(%s)", n, self._max_array_len)
-        elif b & 0b11110000 == 0b10000000:
-            n = b & 0b00001111
-            typ = TYPE_MAP
-            if n > self._max_map_len:
-                raise UnpackValueError("%s exceeds max_map_len(%s)", n, self._max_map_len)
-        elif b == 0xc0:
-            obj = None
-        elif b == 0xc2:
-            obj = False
-        elif b == 0xc3:
-            obj = True
-        elif b == 0xc4:
-            typ = TYPE_BIN
-            self._reserve(1)
-            n = self._buffer[self._buff_i]
-            self._buff_i += 1
-            if n > self._max_bin_len:
-                raise UnpackValueError("%s exceeds max_bin_len(%s)" % (n, self._max_bin_len))
-            obj = self._read(n)
-        elif b == 0xc5:
-            typ = TYPE_BIN
-            self._reserve(2)
-            n = struct.unpack_from(">H", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 2
-            if n > self._max_bin_len:
-                raise UnpackValueError("%s exceeds max_bin_len(%s)" % (n, self._max_bin_len))
-            obj = self._read(n)
-        elif b == 0xc6:
-            typ = TYPE_BIN
-            self._reserve(4)
-            n = struct.unpack_from(">I", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 4
-            if n > self._max_bin_len:
-                raise UnpackValueError("%s exceeds max_bin_len(%s)" % (n, self._max_bin_len))
-            obj = self._read(n)
-        elif b == 0xc7:  # ext 8
-            typ = TYPE_EXT
-            self._reserve(2)
-            L, n = struct.unpack_from('Bb', self._buffer_view, self._buff_i)
-            self._buff_i += 2
-            if L > self._max_ext_len:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (L, self._max_ext_len))
-            obj = self._read(L)
-        elif b == 0xc8:  # ext 16
-            typ = TYPE_EXT
-            self._reserve(3)
-            L, n = struct.unpack_from('>Hb', self._buffer_view, self._buff_i)
-            self._buff_i += 3
-            if L > self._max_ext_len:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (L, self._max_ext_len))
-            obj = self._read(L)
-        elif b == 0xc9:  # ext 32
-            typ = TYPE_EXT
-            self._reserve(5)
-            L, n = struct.unpack_from('>Ib', self._buffer_view, self._buff_i)
-            self._buff_i += 5
-            if L > self._max_ext_len:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (L, self._max_ext_len))
-            obj = self._read(L)
-        elif b == 0xca:
-            self._reserve(4)
-            obj = struct.unpack_from(">f", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 4
-        elif b == 0xcb:
-            self._reserve(8)
-            obj = struct.unpack_from(">d", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 8
-        elif b == 0xcc:
-            self._reserve(1)
-            obj = self._buffer[self._buff_i]
-            self._buff_i += 1
-        elif b == 0xcd:
-            self._reserve(2)
-            obj = struct.unpack_from(">H", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 2
-        elif b == 0xce:
-            self._reserve(4)
-            obj = struct.unpack_from(">I", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 4
-        elif b == 0xcf:
-            self._reserve(8)
-            obj = struct.unpack_from(">Q", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 8
-        elif b == 0xd0:
-            self._reserve(1)
-            obj = struct.unpack_from("b", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 1
-        elif b == 0xd1:
-            self._reserve(2)
-            obj = struct.unpack_from(">h", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 2
-        elif b == 0xd2:
-            self._reserve(4)
-            obj = struct.unpack_from(">i", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 4
-        elif b == 0xd3:
-            self._reserve(8)
-            obj = struct.unpack_from(">q", self._buffer_view, self._buff_i)[0]
-            self._buff_i += 8
-        elif b == 0xd4:  # fixext 1
-            typ = TYPE_EXT
-            if self._max_ext_len < 1:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (1, self._max_ext_len))
-            self._reserve(2)
-            n, obj = struct.unpack_from("b1s", self._buffer_view, self._buff_i)
-            self._buff_i += 2
-        elif b == 0xd5:  # fixext 2
-            typ = TYPE_EXT
-            if self._max_ext_len < 2:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (2, self._max_ext_len))
-            self._reserve(3)
-            n, obj = struct.unpack_from("b2s", self._buffer_view, self._buff_i)
-            self._buff_i += 3
-        elif b == 0xd6:  # fixext 4
-            typ = TYPE_EXT
-            if self._max_ext_len < 4:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (4, self._max_ext_len))
-            self._reserve(5)
-            n, obj = struct.unpack_from("b4s", self._buffer_view, self._buff_i)
-            self._buff_i += 5
-        elif b == 0xd7:  # fixext 8
-            typ = TYPE_EXT
-            if self._max_ext_len < 8:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (8, self._max_ext_len))
-            self._reserve(9)
-            n, obj = struct.unpack_from("b8s", self._buffer_view, self._buff_i)
-            self._buff_i += 9
-        elif b == 0xd8:  # fixext 16
-            typ = TYPE_EXT
-            if self._max_ext_len < 16:
-                raise UnpackValueError("%s exceeds max_ext_len(%s)" % (16, self._max_ext_len))
-            self._reserve(17)
-            n, obj = struct.unpack_from("b16s", self._buffer_view, self._buff_i)
-            self._buff_i += 17
-        elif b == 0xd9:
-            typ = TYPE_RAW
-            self._reserve(1)
-            n = self._buffer[self._buff_i]
-            self._buff_i += 1
-            if n > self._max_str_len:
-                raise UnpackValueError("%s exceeds max_str_len(%s)", n, self._max_str_len)
-            obj = self._read(n)
-        elif b == 0xda:
-            typ = TYPE_RAW
-            self._reserve(2)
-            n, = struct.unpack_from(">H", self._buffer_view, self._buff_i)
-            self._buff_i += 2
-            if n > self._max_str_len:
-                raise UnpackValueError("%s exceeds max_str_len(%s)", n, self._max_str_len)
-            obj = self._read(n)
-        elif b == 0xdb:
-            typ = TYPE_RAW
-            self._reserve(4)
-            n, = struct.unpack_from(">I", self._buffer_view, self._buff_i)
-            self._buff_i += 4
-            if n > self._max_str_len:
-                raise UnpackValueError("%s exceeds max_str_len(%s)", n, self._max_str_len)
-            obj = self._read(n)
-        elif b == 0xdc:
-            typ = TYPE_ARRAY
-            self._reserve(2)
-            n, = struct.unpack_from(">H", self._buffer_view, self._buff_i)
-            self._buff_i += 2
-            if n > self._max_array_len:
-                raise UnpackValueError("%s exceeds max_array_len(%s)", n, self._max_array_len)
-        elif b == 0xdd:
-            typ = TYPE_ARRAY
-            self._reserve(4)
-            n, = struct.unpack_from(">I", self._buffer_view, self._buff_i)
-            self._buff_i += 4
-            if n > self._max_array_len:
-                raise UnpackValueError("%s exceeds max_array_len(%s)", n, self._max_array_len)
-        elif b == 0xde:
-            self._reserve(2)
-            n, = struct.unpack_from(">H", self._buffer_view, self._buff_i)
-            self._buff_i += 2
-            if n > self._max_map_len:
-                raise UnpackValueError("%s exceeds max_map_len(%s)", n, self._max_map_len)
-            typ = TYPE_MAP
-        elif b == 0xdf:
-            self._reserve(4)
-            n, = struct.unpack_from(">I", self._buffer_view, self._buff_i)
-            self._buff_i += 4
-            if n > self._max_map_len:
-                raise UnpackValueError("%s exceeds max_map_len(%s)", n, self._max_map_len)
-            typ = TYPE_MAP
-        else:
-            raise UnpackValueError("Unknown header: 0x%x" % b)
-        return typ, n, obj
-
-    def _unpack(self, execute=EX_CONSTRUCT):
-        typ, n, obj = self._read_header(execute)
-
-        if execute == EX_READ_ARRAY_HEADER:
-            if typ != TYPE_ARRAY:
-                raise UnpackValueError("Expected array")
-            return n
-        if execute == EX_READ_MAP_HEADER:
-            if typ != TYPE_MAP:
-                raise UnpackValueError("Expected map")
-            return n
-        # TODO should we eliminate the recursion?
-        if typ == TYPE_ARRAY:
-            if execute == EX_SKIP:
-                for i in xrange(n):
-                    # TODO check whether we need to call `list_hook`
-                    self._unpack(EX_SKIP)
-                return
-            ret = newlist_hint(n)
-            for i in xrange(n):
-                ret.append(self._unpack(EX_CONSTRUCT))
-            if self._list_hook is not None:
-                ret = self._list_hook(ret)
-            # TODO is the interaction between `list_hook` and `use_list` ok?
-            return ret if self._use_list else tuple(ret)
-        if typ == TYPE_MAP:
-            if execute == EX_SKIP:
-                for i in xrange(n):
-                    # TODO check whether we need to call hooks
-                    self._unpack(EX_SKIP)
-                    self._unpack(EX_SKIP)
-                return
-            if self._object_pairs_hook is not None:
-                ret = self._object_pairs_hook(
-                    (self._unpack(EX_CONSTRUCT),
-                     self._unpack(EX_CONSTRUCT))
-                    for _ in xrange(n))
-            else:
-                ret = {}
-                for _ in xrange(n):
-                    key = self._unpack(EX_CONSTRUCT)
-                    ret[key] = self._unpack(EX_CONSTRUCT)
-                if self._object_hook is not None:
-                    ret = self._object_hook(ret)
-            return ret
-        if execute == EX_SKIP:
-            return
-        if typ == TYPE_RAW:
-            if self._encoding is not None:
-                obj = obj.decode(self._encoding, self._unicode_errors)
-            elif self._raw:
-                obj = bytes(obj)
-            else:
-                obj = obj.decode('utf_8')
-            return obj
-        if typ == TYPE_EXT:
-            return self._ext_hook(n, bytes(obj))
-        if typ == TYPE_BIN:
-            return bytes(obj)
-        assert typ == TYPE_IMMEDIATE
-        return obj
-
-    def __iter__(self):
-        return self
-
-    def __next__(self):
-        try:
-            ret = self._unpack(EX_CONSTRUCT)
-            self._consume()
-            return ret
-        except OutOfData:
-            self._consume()
-            raise StopIteration
-
-    next = __next__
-
-    def skip(self, write_bytes=None):
-        self._unpack(EX_SKIP)
-        if write_bytes is not None:
-            warnings.warn("`write_bytes` option is deprecated.  Use `.tell()` instead.", DeprecationWarning)
-            write_bytes(self._buffer[self._buf_checkpoint:self._buff_i])
-        self._consume()
-
-    def unpack(self, write_bytes=None):
-        ret = self._unpack(EX_CONSTRUCT)
-        if write_bytes is not None:
-            warnings.warn("`write_bytes` option is deprecated.  Use `.tell()` instead.", DeprecationWarning)
-            write_bytes(self._buffer[self._buf_checkpoint:self._buff_i])
-        self._consume()
-        return ret
-
-    def read_array_header(self, write_bytes=None):
-        ret = self._unpack(EX_READ_ARRAY_HEADER)
-        if write_bytes is not None:
-            warnings.warn("`write_bytes` option is deprecated.  Use `.tell()` instead.", DeprecationWarning)
-            write_bytes(self._buffer[self._buf_checkpoint:self._buff_i])
-        self._consume()
-        return ret
-
-    def read_map_header(self, write_bytes=None):
-        ret = self._unpack(EX_READ_MAP_HEADER)
-        if write_bytes is not None:
-            warnings.warn("`write_bytes` option is deprecated.  Use `.tell()` instead.", DeprecationWarning)
-            write_bytes(self._buffer[self._buf_checkpoint:self._buff_i])
-        self._consume()
-        return ret
-
-    def tell(self):
-        return self._stream_offset
-
-
-class Packer(object):
-    """
-    MessagePack Packer
-
-    usage:
-
-        packer = Packer()
-        astream.write(packer.pack(a))
-        astream.write(packer.pack(b))
-
-    Packer's constructor has some keyword arguments:
-
-    :param callable default:
-        Convert user type to builtin type that Packer supports.
-        See also simplejson's document.
-
-    :param bool use_single_float:
-        Use single precision float type for float. (default: False)
-
-    :param bool autoreset:
-        Reset buffer after each pack and return its content as `bytes`. (default: True).
-        If set this to false, use `bytes()` to get content and `.reset()` to clear buffer.
-
-    :param bool use_bin_type:
-        Use bin type introduced in msgpack spec 2.0 for bytes.
-        It also enables str8 type for unicode.
-
-    :param bool strict_types:
-        If set to true, types will be checked to be exact. Derived classes
-        from serializeable types will not be serialized and will be
-        treated as unsupported type and forwarded to default.
-        Additionally tuples will not be serialized as lists.
-        This is useful when trying to implement accurate serialization
-        for python types.
-
-    :param str encoding:
-        (deprecated) Convert unicode to bytes with this encoding. (default: 'utf-8')
-
-    :param str unicode_errors:
-        Error handler for encoding unicode. (default: 'strict')
-    """
-    def __init__(self, default=None, encoding=None, unicode_errors=None,
-                 use_single_float=False, autoreset=True, use_bin_type=False,
-                 strict_types=False):
-        if encoding is None:
-            encoding = 'utf_8'
-        else:
-            warnings.warn(
-                "encoding is deprecated, Use raw=False instead.",
-                PendingDeprecationWarning)
-
-        if unicode_errors is None:
-            unicode_errors = 'strict'
-
-        self._strict_types = strict_types
-        self._use_float = use_single_float
-        self._autoreset = autoreset
-        self._use_bin_type = use_bin_type
-        self._encoding = encoding
-        self._unicode_errors = unicode_errors
-        self._buffer = StringIO()
-        if default is not None:
-            if not callable(default):
-                raise TypeError("default must be callable")
-        self._default = default
-
-    def _pack(self, obj, nest_limit=DEFAULT_RECURSE_LIMIT,
-              check=isinstance, check_type_strict=_check_type_strict):
-        default_used = False
-        if self._strict_types:
-            check = check_type_strict
-            list_types = list
-        else:
-            list_types = (list, tuple)
-        while True:
-            if nest_limit < 0:
-                raise PackValueError("recursion limit exceeded")
-            if obj is None:
-                return self._buffer.write(b"\xc0")
-            if check(obj, bool):
-                if obj:
-                    return self._buffer.write(b"\xc3")
-                return self._buffer.write(b"\xc2")
-            if check(obj, int_types):
-                if 0 <= obj < 0x80:
-                    return self._buffer.write(struct.pack("B", obj))
-                if -0x20 <= obj < 0:
-                    return self._buffer.write(struct.pack("b", obj))
-                if 0x80 <= obj <= 0xff:
-                    return self._buffer.write(struct.pack("BB", 0xcc, obj))
-                if -0x80 <= obj < 0:
-                    return self._buffer.write(struct.pack(">Bb", 0xd0, obj))
-                if 0xff < obj <= 0xffff:
-                    return self._buffer.write(struct.pack(">BH", 0xcd, obj))
-                if -0x8000 <= obj < -0x80:
-                    return self._buffer.write(struct.pack(">Bh", 0xd1, obj))
-                if 0xffff < obj <= 0xffffffff:
-                    return self._buffer.write(struct.pack(">BI", 0xce, obj))
-                if -0x80000000 <= obj < -0x8000:
-                    return self._buffer.write(struct.pack(">Bi", 0xd2, obj))
-                if 0xffffffff < obj <= 0xffffffffffffffff:
-                    return self._buffer.write(struct.pack(">BQ", 0xcf, obj))
-                if -0x8000000000000000 <= obj < -0x80000000:
-                    return self._buffer.write(struct.pack(">Bq", 0xd3, obj))
-                if not default_used and self._default is not None:
-                    obj = self._default(obj)
-                    default_used = True
-                    continue
-                raise PackOverflowError("Integer value out of range")
-            if check(obj, (bytes, bytearray)):
-                n = len(obj)
-                if n >= 2**32:
-                    raise PackValueError("%s is too large" % type(obj).__name__)
-                self._pack_bin_header(n)
-                return self._buffer.write(obj)
-            if check(obj, Unicode):
-                if self._encoding is None:
-                    raise TypeError(
-                        "Can't encode unicode string: "
-                        "no encoding is specified")
-                obj = obj.encode(self._encoding, self._unicode_errors)
-                n = len(obj)
-                if n >= 2**32:
-                    raise PackValueError("String is too large")
-                self._pack_raw_header(n)
-                return self._buffer.write(obj)
-            if check(obj, memoryview):
-                n = len(obj) * obj.itemsize
-                if n >= 2**32:
-                    raise PackValueError("Memoryview is too large")
-                self._pack_bin_header(n)
-                return self._buffer.write(obj)
-            if check(obj, float):
-                if self._use_float:
-                    return self._buffer.write(struct.pack(">Bf", 0xca, obj))
-                return self._buffer.write(struct.pack(">Bd", 0xcb, obj))
-            if check(obj, ExtType):
-                code = obj.code
-                data = obj.data
-                assert isinstance(code, int)
-                assert isinstance(data, bytes)
-                L = len(data)
-                if L == 1:
-                    self._buffer.write(b'\xd4')
-                elif L == 2:
-                    self._buffer.write(b'\xd5')
-                elif L == 4:
-                    self._buffer.write(b'\xd6')
-                elif L == 8:
-                    self._buffer.write(b'\xd7')
-                elif L == 16:
-                    self._buffer.write(b'\xd8')
-                elif L <= 0xff:
-                    self._buffer.write(struct.pack(">BB", 0xc7, L))
-                elif L <= 0xffff:
-                    self._buffer.write(struct.pack(">BH", 0xc8, L))
-                else:
-                    self._buffer.write(struct.pack(">BI", 0xc9, L))
-                self._buffer.write(struct.pack("b", code))
-                self._buffer.write(data)
-                return
-            if check(obj, list_types):
-                n = len(obj)
-                self._pack_array_header(n)
-                for i in xrange(n):
-                    self._pack(obj[i], nest_limit - 1)
-                return
-            if check(obj, dict):
-                return self._pack_map_pairs(len(obj), dict_iteritems(obj),
-                                               nest_limit - 1)
-            if not default_used and self._default is not None:
-                obj = self._default(obj)
-                default_used = 1
-                continue
-            raise TypeError("Cannot serialize %r" % (obj, ))
-
-    def pack(self, obj):
-        try:
-            self._pack(obj)
-        except:
-            self._buffer = StringIO()  # force reset
-            raise
-        ret = self._buffer.getvalue()
-        if self._autoreset:
-            self._buffer = StringIO()
-        elif USING_STRINGBUILDER:
-            self._buffer = StringIO(ret)
-        return ret
-
-    def pack_map_pairs(self, pairs):
-        self._pack_map_pairs(len(pairs), pairs)
-        ret = self._buffer.getvalue()
-        if self._autoreset:
-            self._buffer = StringIO()
-        elif USING_STRINGBUILDER:
-            self._buffer = StringIO(ret)
-        return ret
-
-    def pack_array_header(self, n):
-        if n >= 2**32:
-            raise PackValueError
-        self._pack_array_header(n)
-        ret = self._buffer.getvalue()
-        if self._autoreset:
-            self._buffer = StringIO()
-        elif USING_STRINGBUILDER:
-            self._buffer = StringIO(ret)
-        return ret
-
-    def pack_map_header(self, n):
-        if n >= 2**32:
-            raise PackValueError
-        self._pack_map_header(n)
-        ret = self._buffer.getvalue()
-        if self._autoreset:
-            self._buffer = StringIO()
-        elif USING_STRINGBUILDER:
-            self._buffer = StringIO(ret)
-        return ret
-
-    def pack_ext_type(self, typecode, data):
-        if not isinstance(typecode, int):
-            raise TypeError("typecode must have int type.")
-        if not 0 <= typecode <= 127:
-            raise ValueError("typecode should be 0-127")
-        if not isinstance(data, bytes):
-            raise TypeError("data must have bytes type")
-        L = len(data)
-        if L > 0xffffffff:
-            raise PackValueError("Too large data")
-        if L == 1:
-            self._buffer.write(b'\xd4')
-        elif L == 2:
-            self._buffer.write(b'\xd5')
-        elif L == 4:
-            self._buffer.write(b'\xd6')
-        elif L == 8:
-            self._buffer.write(b'\xd7')
-        elif L == 16:
-            self._buffer.write(b'\xd8')
-        elif L <= 0xff:
-            self._buffer.write(b'\xc7' + struct.pack('B', L))
-        elif L <= 0xffff:
-            self._buffer.write(b'\xc8' + struct.pack('>H', L))
-        else:
-            self._buffer.write(b'\xc9' + struct.pack('>I', L))
-        self._buffer.write(struct.pack('B', typecode))
-        self._buffer.write(data)
-
-    def _pack_array_header(self, n):
-        if n <= 0x0f:
-            return self._buffer.write(struct.pack('B', 0x90 + n))
-        if n <= 0xffff:
-            return self._buffer.write(struct.pack(">BH", 0xdc, n))
-        if n <= 0xffffffff:
-            return self._buffer.write(struct.pack(">BI", 0xdd, n))
-        raise PackValueError("Array is too large")
-
-    def _pack_map_header(self, n):
-        if n <= 0x0f:
-            return self._buffer.write(struct.pack('B', 0x80 + n))
-        if n <= 0xffff:
-            return self._buffer.write(struct.pack(">BH", 0xde, n))
-        if n <= 0xffffffff:
-            return self._buffer.write(struct.pack(">BI", 0xdf, n))
-        raise PackValueError("Dict is too large")
-
-    def _pack_map_pairs(self, n, pairs, nest_limit=DEFAULT_RECURSE_LIMIT):
-        self._pack_map_header(n)
-        for (k, v) in pairs:
-            self._pack(k, nest_limit - 1)
-            self._pack(v, nest_limit - 1)
-
-    def _pack_raw_header(self, n):
-        if n <= 0x1f:
-            self._buffer.write(struct.pack('B', 0xa0 + n))
-        elif self._use_bin_type and n <= 0xff:
-            self._buffer.write(struct.pack('>BB', 0xd9, n))
-        elif n <= 0xffff:
-            self._buffer.write(struct.pack(">BH", 0xda, n))
-        elif n <= 0xffffffff:
-            self._buffer.write(struct.pack(">BI", 0xdb, n))
-        else:
-            raise PackValueError('Raw is too large')
-
-    def _pack_bin_header(self, n):
-        if not self._use_bin_type:
-            return self._pack_raw_header(n)
-        elif n <= 0xff:
-            return self._buffer.write(struct.pack('>BB', 0xc4, n))
-        elif n <= 0xffff:
-            return self._buffer.write(struct.pack(">BH", 0xc5, n))
-        elif n <= 0xffffffff:
-            return self._buffer.write(struct.pack(">BI", 0xc6, n))
-        else:
-            raise PackValueError('Bin is too large')
-
-    def bytes(self):
-        return self._buffer.getvalue()
-
-    def reset(self):
-        self._buffer = StringIO()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__about__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__about__.py
deleted file mode 100644
index 7481c9e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__about__.py
+++ /dev/null
@@ -1,27 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-__all__ = [
-    "__title__",
-    "__summary__",
-    "__uri__",
-    "__version__",
-    "__author__",
-    "__email__",
-    "__license__",
-    "__copyright__",
-]
-
-__title__ = "packaging"
-__summary__ = "Core utilities for Python packages"
-__uri__ = "https://github.com/pypa/packaging"
-
-__version__ = "19.0"
-
-__author__ = "Donald Stufft and individual contributors"
-__email__ = "donald@stufft.io"
-
-__license__ = "BSD or Apache License, Version 2.0"
-__copyright__ = "Copyright 2014-2019 %s" % __author__
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__init__.py
deleted file mode 100644
index a0cf67d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__init__.py
+++ /dev/null
@@ -1,26 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-from .__about__ import (
-    __author__,
-    __copyright__,
-    __email__,
-    __license__,
-    __summary__,
-    __title__,
-    __uri__,
-    __version__,
-)
-
-__all__ = [
-    "__title__",
-    "__summary__",
-    "__uri__",
-    "__version__",
-    "__author__",
-    "__email__",
-    "__license__",
-    "__copyright__",
-]
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/__about__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/__about__.cpython-37.pyc
deleted file mode 100644
index 29ea00f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/__about__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 887ce3f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/_compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/_compat.cpython-37.pyc
deleted file mode 100644
index a9d0d37..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/_compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/_structures.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/_structures.cpython-37.pyc
deleted file mode 100644
index 9136b76..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/_structures.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/markers.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/markers.cpython-37.pyc
deleted file mode 100644
index 7b78e61..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/markers.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/requirements.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/requirements.cpython-37.pyc
deleted file mode 100644
index 1fccbed..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/requirements.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/specifiers.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/specifiers.cpython-37.pyc
deleted file mode 100644
index 5b7bd84..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/specifiers.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index d68ec3e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/version.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/version.cpython-37.pyc
deleted file mode 100644
index c7b9e23..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/__pycache__/version.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/_compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/_compat.py
deleted file mode 100644
index 25da473..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/_compat.py
+++ /dev/null
@@ -1,31 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-import sys
-
-
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-
-# flake8: noqa
-
-if PY3:
-    string_types = (str,)
-else:
-    string_types = (basestring,)
-
-
-def with_metaclass(meta, *bases):
-    """
-    Create a base class with a metaclass.
-    """
-    # This requires a bit of explanation: the basic idea is to make a dummy
-    # metaclass for one level of class instantiation that replaces itself with
-    # the actual metaclass.
-    class metaclass(meta):
-        def __new__(cls, name, this_bases, d):
-            return meta(name, bases, d)
-
-    return type.__new__(metaclass, "temporary_class", (), {})
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/_structures.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/_structures.py
deleted file mode 100644
index 68dcca6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/_structures.py
+++ /dev/null
@@ -1,68 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-
-class Infinity(object):
-    def __repr__(self):
-        return "Infinity"
-
-    def __hash__(self):
-        return hash(repr(self))
-
-    def __lt__(self, other):
-        return False
-
-    def __le__(self, other):
-        return False
-
-    def __eq__(self, other):
-        return isinstance(other, self.__class__)
-
-    def __ne__(self, other):
-        return not isinstance(other, self.__class__)
-
-    def __gt__(self, other):
-        return True
-
-    def __ge__(self, other):
-        return True
-
-    def __neg__(self):
-        return NegativeInfinity
-
-
-Infinity = Infinity()
-
-
-class NegativeInfinity(object):
-    def __repr__(self):
-        return "-Infinity"
-
-    def __hash__(self):
-        return hash(repr(self))
-
-    def __lt__(self, other):
-        return True
-
-    def __le__(self, other):
-        return True
-
-    def __eq__(self, other):
-        return isinstance(other, self.__class__)
-
-    def __ne__(self, other):
-        return not isinstance(other, self.__class__)
-
-    def __gt__(self, other):
-        return False
-
-    def __ge__(self, other):
-        return False
-
-    def __neg__(self):
-        return Infinity
-
-
-NegativeInfinity = NegativeInfinity()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/markers.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/markers.py
deleted file mode 100644
index 5482476..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/markers.py
+++ /dev/null
@@ -1,296 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-import operator
-import os
-import platform
-import sys
-
-from pip._vendor.pyparsing import ParseException, ParseResults, stringStart, stringEnd
-from pip._vendor.pyparsing import ZeroOrMore, Group, Forward, QuotedString
-from pip._vendor.pyparsing import Literal as L  # noqa
-
-from ._compat import string_types
-from .specifiers import Specifier, InvalidSpecifier
-
-
-__all__ = [
-    "InvalidMarker",
-    "UndefinedComparison",
-    "UndefinedEnvironmentName",
-    "Marker",
-    "default_environment",
-]
-
-
-class InvalidMarker(ValueError):
-    """
-    An invalid marker was found, users should refer to PEP 508.
-    """
-
-
-class UndefinedComparison(ValueError):
-    """
-    An invalid operation was attempted on a value that doesn't support it.
-    """
-
-
-class UndefinedEnvironmentName(ValueError):
-    """
-    A name was attempted to be used that does not exist inside of the
-    environment.
-    """
-
-
-class Node(object):
-    def __init__(self, value):
-        self.value = value
-
-    def __str__(self):
-        return str(self.value)
-
-    def __repr__(self):
-        return "<{0}({1!r})>".format(self.__class__.__name__, str(self))
-
-    def serialize(self):
-        raise NotImplementedError
-
-
-class Variable(Node):
-    def serialize(self):
-        return str(self)
-
-
-class Value(Node):
-    def serialize(self):
-        return '"{0}"'.format(self)
-
-
-class Op(Node):
-    def serialize(self):
-        return str(self)
-
-
-VARIABLE = (
-    L("implementation_version")
-    | L("platform_python_implementation")
-    | L("implementation_name")
-    | L("python_full_version")
-    | L("platform_release")
-    | L("platform_version")
-    | L("platform_machine")
-    | L("platform_system")
-    | L("python_version")
-    | L("sys_platform")
-    | L("os_name")
-    | L("os.name")
-    | L("sys.platform")  # PEP-345
-    | L("platform.version")  # PEP-345
-    | L("platform.machine")  # PEP-345
-    | L("platform.python_implementation")  # PEP-345
-    | L("python_implementation")  # PEP-345
-    | L("extra")  # undocumented setuptools legacy
-)
-ALIASES = {
-    "os.name": "os_name",
-    "sys.platform": "sys_platform",
-    "platform.version": "platform_version",
-    "platform.machine": "platform_machine",
-    "platform.python_implementation": "platform_python_implementation",
-    "python_implementation": "platform_python_implementation",
-}
-VARIABLE.setParseAction(lambda s, l, t: Variable(ALIASES.get(t[0], t[0])))
-
-VERSION_CMP = (
-    L("===") | L("==") | L(">=") | L("<=") | L("!=") | L("~=") | L(">") | L("<")
-)
-
-MARKER_OP = VERSION_CMP | L("not in") | L("in")
-MARKER_OP.setParseAction(lambda s, l, t: Op(t[0]))
-
-MARKER_VALUE = QuotedString("'") | QuotedString('"')
-MARKER_VALUE.setParseAction(lambda s, l, t: Value(t[0]))
-
-BOOLOP = L("and") | L("or")
-
-MARKER_VAR = VARIABLE | MARKER_VALUE
-
-MARKER_ITEM = Group(MARKER_VAR + MARKER_OP + MARKER_VAR)
-MARKER_ITEM.setParseAction(lambda s, l, t: tuple(t[0]))
-
-LPAREN = L("(").suppress()
-RPAREN = L(")").suppress()
-
-MARKER_EXPR = Forward()
-MARKER_ATOM = MARKER_ITEM | Group(LPAREN + MARKER_EXPR + RPAREN)
-MARKER_EXPR << MARKER_ATOM + ZeroOrMore(BOOLOP + MARKER_EXPR)
-
-MARKER = stringStart + MARKER_EXPR + stringEnd
-
-
-def _coerce_parse_result(results):
-    if isinstance(results, ParseResults):
-        return [_coerce_parse_result(i) for i in results]
-    else:
-        return results
-
-
-def _format_marker(marker, first=True):
-    assert isinstance(marker, (list, tuple, string_types))
-
-    # Sometimes we have a structure like [[...]] which is a single item list
-    # where the single item is itself it's own list. In that case we want skip
-    # the rest of this function so that we don't get extraneous () on the
-    # outside.
-    if (
-        isinstance(marker, list)
-        and len(marker) == 1
-        and isinstance(marker[0], (list, tuple))
-    ):
-        return _format_marker(marker[0])
-
-    if isinstance(marker, list):
-        inner = (_format_marker(m, first=False) for m in marker)
-        if first:
-            return " ".join(inner)
-        else:
-            return "(" + " ".join(inner) + ")"
-    elif isinstance(marker, tuple):
-        return " ".join([m.serialize() for m in marker])
-    else:
-        return marker
-
-
-_operators = {
-    "in": lambda lhs, rhs: lhs in rhs,
-    "not in": lambda lhs, rhs: lhs not in rhs,
-    "<": operator.lt,
-    "<=": operator.le,
-    "==": operator.eq,
-    "!=": operator.ne,
-    ">=": operator.ge,
-    ">": operator.gt,
-}
-
-
-def _eval_op(lhs, op, rhs):
-    try:
-        spec = Specifier("".join([op.serialize(), rhs]))
-    except InvalidSpecifier:
-        pass
-    else:
-        return spec.contains(lhs)
-
-    oper = _operators.get(op.serialize())
-    if oper is None:
-        raise UndefinedComparison(
-            "Undefined {0!r} on {1!r} and {2!r}.".format(op, lhs, rhs)
-        )
-
-    return oper(lhs, rhs)
-
-
-_undefined = object()
-
-
-def _get_env(environment, name):
-    value = environment.get(name, _undefined)
-
-    if value is _undefined:
-        raise UndefinedEnvironmentName(
-            "{0!r} does not exist in evaluation environment.".format(name)
-        )
-
-    return value
-
-
-def _evaluate_markers(markers, environment):
-    groups = [[]]
-
-    for marker in markers:
-        assert isinstance(marker, (list, tuple, string_types))
-
-        if isinstance(marker, list):
-            groups[-1].append(_evaluate_markers(marker, environment))
-        elif isinstance(marker, tuple):
-            lhs, op, rhs = marker
-
-            if isinstance(lhs, Variable):
-                lhs_value = _get_env(environment, lhs.value)
-                rhs_value = rhs.value
-            else:
-                lhs_value = lhs.value
-                rhs_value = _get_env(environment, rhs.value)
-
-            groups[-1].append(_eval_op(lhs_value, op, rhs_value))
-        else:
-            assert marker in ["and", "or"]
-            if marker == "or":
-                groups.append([])
-
-    return any(all(item) for item in groups)
-
-
-def format_full_version(info):
-    version = "{0.major}.{0.minor}.{0.micro}".format(info)
-    kind = info.releaselevel
-    if kind != "final":
-        version += kind[0] + str(info.serial)
-    return version
-
-
-def default_environment():
-    if hasattr(sys, "implementation"):
-        iver = format_full_version(sys.implementation.version)
-        implementation_name = sys.implementation.name
-    else:
-        iver = "0"
-        implementation_name = ""
-
-    return {
-        "implementation_name": implementation_name,
-        "implementation_version": iver,
-        "os_name": os.name,
-        "platform_machine": platform.machine(),
-        "platform_release": platform.release(),
-        "platform_system": platform.system(),
-        "platform_version": platform.version(),
-        "python_full_version": platform.python_version(),
-        "platform_python_implementation": platform.python_implementation(),
-        "python_version": platform.python_version()[:3],
-        "sys_platform": sys.platform,
-    }
-
-
-class Marker(object):
-    def __init__(self, marker):
-        try:
-            self._markers = _coerce_parse_result(MARKER.parseString(marker))
-        except ParseException as e:
-            err_str = "Invalid marker: {0!r}, parse error at {1!r}".format(
-                marker, marker[e.loc : e.loc + 8]
-            )
-            raise InvalidMarker(err_str)
-
-    def __str__(self):
-        return _format_marker(self._markers)
-
-    def __repr__(self):
-        return "<Marker({0!r})>".format(str(self))
-
-    def evaluate(self, environment=None):
-        """Evaluate a marker.
-
-        Return the boolean from evaluating the given marker against the
-        environment. environment is an optional argument to override all or
-        part of the determined environment.
-
-        The environment is determined from the current Python process.
-        """
-        current_environment = default_environment()
-        if environment is not None:
-            current_environment.update(environment)
-
-        return _evaluate_markers(self._markers, current_environment)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/requirements.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/requirements.py
deleted file mode 100644
index dbc5f11..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/requirements.py
+++ /dev/null
@@ -1,138 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-import string
-import re
-
-from pip._vendor.pyparsing import stringStart, stringEnd, originalTextFor, ParseException
-from pip._vendor.pyparsing import ZeroOrMore, Word, Optional, Regex, Combine
-from pip._vendor.pyparsing import Literal as L  # noqa
-from pip._vendor.six.moves.urllib import parse as urlparse
-
-from .markers import MARKER_EXPR, Marker
-from .specifiers import LegacySpecifier, Specifier, SpecifierSet
-
-
-class InvalidRequirement(ValueError):
-    """
-    An invalid requirement was found, users should refer to PEP 508.
-    """
-
-
-ALPHANUM = Word(string.ascii_letters + string.digits)
-
-LBRACKET = L("[").suppress()
-RBRACKET = L("]").suppress()
-LPAREN = L("(").suppress()
-RPAREN = L(")").suppress()
-COMMA = L(",").suppress()
-SEMICOLON = L(";").suppress()
-AT = L("@").suppress()
-
-PUNCTUATION = Word("-_.")
-IDENTIFIER_END = ALPHANUM | (ZeroOrMore(PUNCTUATION) + ALPHANUM)
-IDENTIFIER = Combine(ALPHANUM + ZeroOrMore(IDENTIFIER_END))
-
-NAME = IDENTIFIER("name")
-EXTRA = IDENTIFIER
-
-URI = Regex(r"[^ ]+")("url")
-URL = AT + URI
-
-EXTRAS_LIST = EXTRA + ZeroOrMore(COMMA + EXTRA)
-EXTRAS = (LBRACKET + Optional(EXTRAS_LIST) + RBRACKET)("extras")
-
-VERSION_PEP440 = Regex(Specifier._regex_str, re.VERBOSE | re.IGNORECASE)
-VERSION_LEGACY = Regex(LegacySpecifier._regex_str, re.VERBOSE | re.IGNORECASE)
-
-VERSION_ONE = VERSION_PEP440 ^ VERSION_LEGACY
-VERSION_MANY = Combine(
-    VERSION_ONE + ZeroOrMore(COMMA + VERSION_ONE), joinString=",", adjacent=False
-)("_raw_spec")
-_VERSION_SPEC = Optional(((LPAREN + VERSION_MANY + RPAREN) | VERSION_MANY))
-_VERSION_SPEC.setParseAction(lambda s, l, t: t._raw_spec or "")
-
-VERSION_SPEC = originalTextFor(_VERSION_SPEC)("specifier")
-VERSION_SPEC.setParseAction(lambda s, l, t: t[1])
-
-MARKER_EXPR = originalTextFor(MARKER_EXPR())("marker")
-MARKER_EXPR.setParseAction(
-    lambda s, l, t: Marker(s[t._original_start : t._original_end])
-)
-MARKER_SEPARATOR = SEMICOLON
-MARKER = MARKER_SEPARATOR + MARKER_EXPR
-
-VERSION_AND_MARKER = VERSION_SPEC + Optional(MARKER)
-URL_AND_MARKER = URL + Optional(MARKER)
-
-NAMED_REQUIREMENT = NAME + Optional(EXTRAS) + (URL_AND_MARKER | VERSION_AND_MARKER)
-
-REQUIREMENT = stringStart + NAMED_REQUIREMENT + stringEnd
-# pyparsing isn't thread safe during initialization, so we do it eagerly, see
-# issue #104
-REQUIREMENT.parseString("x[]")
-
-
-class Requirement(object):
-    """Parse a requirement.
-
-    Parse a given requirement string into its parts, such as name, specifier,
-    URL, and extras. Raises InvalidRequirement on a badly-formed requirement
-    string.
-    """
-
-    # TODO: Can we test whether something is contained within a requirement?
-    #       If so how do we do that? Do we need to test against the _name_ of
-    #       the thing as well as the version? What about the markers?
-    # TODO: Can we normalize the name and extra name?
-
-    def __init__(self, requirement_string):
-        try:
-            req = REQUIREMENT.parseString(requirement_string)
-        except ParseException as e:
-            raise InvalidRequirement(
-                'Parse error at "{0!r}": {1}'.format(
-                    requirement_string[e.loc : e.loc + 8], e.msg
-                )
-            )
-
-        self.name = req.name
-        if req.url:
-            parsed_url = urlparse.urlparse(req.url)
-            if parsed_url.scheme == "file":
-                if urlparse.urlunparse(parsed_url) != req.url:
-                    raise InvalidRequirement("Invalid URL given")
-            elif not (parsed_url.scheme and parsed_url.netloc) or (
-                not parsed_url.scheme and not parsed_url.netloc
-            ):
-                raise InvalidRequirement("Invalid URL: {0}".format(req.url))
-            self.url = req.url
-        else:
-            self.url = None
-        self.extras = set(req.extras.asList() if req.extras else [])
-        self.specifier = SpecifierSet(req.specifier)
-        self.marker = req.marker if req.marker else None
-
-    def __str__(self):
-        parts = [self.name]
-
-        if self.extras:
-            parts.append("[{0}]".format(",".join(sorted(self.extras))))
-
-        if self.specifier:
-            parts.append(str(self.specifier))
-
-        if self.url:
-            parts.append("@ {0}".format(self.url))
-            if self.marker:
-                parts.append(" ")
-
-        if self.marker:
-            parts.append("; {0}".format(self.marker))
-
-        return "".join(parts)
-
-    def __repr__(self):
-        return "<Requirement({0!r})>".format(str(self))
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/specifiers.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/specifiers.py
deleted file mode 100644
index 743576a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/specifiers.py
+++ /dev/null
@@ -1,749 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-import abc
-import functools
-import itertools
-import re
-
-from ._compat import string_types, with_metaclass
-from .version import Version, LegacyVersion, parse
-
-
-class InvalidSpecifier(ValueError):
-    """
-    An invalid specifier was found, users should refer to PEP 440.
-    """
-
-
-class BaseSpecifier(with_metaclass(abc.ABCMeta, object)):
-    @abc.abstractmethod
-    def __str__(self):
-        """
-        Returns the str representation of this Specifier like object. This
-        should be representative of the Specifier itself.
-        """
-
-    @abc.abstractmethod
-    def __hash__(self):
-        """
-        Returns a hash value for this Specifier like object.
-        """
-
-    @abc.abstractmethod
-    def __eq__(self, other):
-        """
-        Returns a boolean representing whether or not the two Specifier like
-        objects are equal.
-        """
-
-    @abc.abstractmethod
-    def __ne__(self, other):
-        """
-        Returns a boolean representing whether or not the two Specifier like
-        objects are not equal.
-        """
-
-    @abc.abstractproperty
-    def prereleases(self):
-        """
-        Returns whether or not pre-releases as a whole are allowed by this
-        specifier.
-        """
-
-    @prereleases.setter
-    def prereleases(self, value):
-        """
-        Sets whether or not pre-releases as a whole are allowed by this
-        specifier.
-        """
-
-    @abc.abstractmethod
-    def contains(self, item, prereleases=None):
-        """
-        Determines if the given item is contained within this specifier.
-        """
-
-    @abc.abstractmethod
-    def filter(self, iterable, prereleases=None):
-        """
-        Takes an iterable of items and filters them so that only items which
-        are contained within this specifier are allowed in it.
-        """
-
-
-class _IndividualSpecifier(BaseSpecifier):
-
-    _operators = {}
-
-    def __init__(self, spec="", prereleases=None):
-        match = self._regex.search(spec)
-        if not match:
-            raise InvalidSpecifier("Invalid specifier: '{0}'".format(spec))
-
-        self._spec = (match.group("operator").strip(), match.group("version").strip())
-
-        # Store whether or not this Specifier should accept prereleases
-        self._prereleases = prereleases
-
-    def __repr__(self):
-        pre = (
-            ", prereleases={0!r}".format(self.prereleases)
-            if self._prereleases is not None
-            else ""
-        )
-
-        return "<{0}({1!r}{2})>".format(self.__class__.__name__, str(self), pre)
-
-    def __str__(self):
-        return "{0}{1}".format(*self._spec)
-
-    def __hash__(self):
-        return hash(self._spec)
-
-    def __eq__(self, other):
-        if isinstance(other, string_types):
-            try:
-                other = self.__class__(other)
-            except InvalidSpecifier:
-                return NotImplemented
-        elif not isinstance(other, self.__class__):
-            return NotImplemented
-
-        return self._spec == other._spec
-
-    def __ne__(self, other):
-        if isinstance(other, string_types):
-            try:
-                other = self.__class__(other)
-            except InvalidSpecifier:
-                return NotImplemented
-        elif not isinstance(other, self.__class__):
-            return NotImplemented
-
-        return self._spec != other._spec
-
-    def _get_operator(self, op):
-        return getattr(self, "_compare_{0}".format(self._operators[op]))
-
-    def _coerce_version(self, version):
-        if not isinstance(version, (LegacyVersion, Version)):
-            version = parse(version)
-        return version
-
-    @property
-    def operator(self):
-        return self._spec[0]
-
-    @property
-    def version(self):
-        return self._spec[1]
-
-    @property
-    def prereleases(self):
-        return self._prereleases
-
-    @prereleases.setter
-    def prereleases(self, value):
-        self._prereleases = value
-
-    def __contains__(self, item):
-        return self.contains(item)
-
-    def contains(self, item, prereleases=None):
-        # Determine if prereleases are to be allowed or not.
-        if prereleases is None:
-            prereleases = self.prereleases
-
-        # Normalize item to a Version or LegacyVersion, this allows us to have
-        # a shortcut for ``"2.0" in Specifier(">=2")
-        item = self._coerce_version(item)
-
-        # Determine if we should be supporting prereleases in this specifier
-        # or not, if we do not support prereleases than we can short circuit
-        # logic if this version is a prereleases.
-        if item.is_prerelease and not prereleases:
-            return False
-
-        # Actually do the comparison to determine if this item is contained
-        # within this Specifier or not.
-        return self._get_operator(self.operator)(item, self.version)
-
-    def filter(self, iterable, prereleases=None):
-        yielded = False
-        found_prereleases = []
-
-        kw = {"prereleases": prereleases if prereleases is not None else True}
-
-        # Attempt to iterate over all the values in the iterable and if any of
-        # them match, yield them.
-        for version in iterable:
-            parsed_version = self._coerce_version(version)
-
-            if self.contains(parsed_version, **kw):
-                # If our version is a prerelease, and we were not set to allow
-                # prereleases, then we'll store it for later incase nothing
-                # else matches this specifier.
-                if parsed_version.is_prerelease and not (
-                    prereleases or self.prereleases
-                ):
-                    found_prereleases.append(version)
-                # Either this is not a prerelease, or we should have been
-                # accepting prereleases from the beginning.
-                else:
-                    yielded = True
-                    yield version
-
-        # Now that we've iterated over everything, determine if we've yielded
-        # any values, and if we have not and we have any prereleases stored up
-        # then we will go ahead and yield the prereleases.
-        if not yielded and found_prereleases:
-            for version in found_prereleases:
-                yield version
-
-
-class LegacySpecifier(_IndividualSpecifier):
-
-    _regex_str = r"""
-        (?P<operator>(==|!=|<=|>=|<|>))
-        \s*
-        (?P<version>
-            [^,;\s)]* # Since this is a "legacy" specifier, and the version
-                      # string can be just about anything, we match everything
-                      # except for whitespace, a semi-colon for marker support,
-                      # a closing paren since versions can be enclosed in
-                      # them, and a comma since it's a version separator.
-        )
-        """
-
-    _regex = re.compile(r"^\s*" + _regex_str + r"\s*$", re.VERBOSE | re.IGNORECASE)
-
-    _operators = {
-        "==": "equal",
-        "!=": "not_equal",
-        "<=": "less_than_equal",
-        ">=": "greater_than_equal",
-        "<": "less_than",
-        ">": "greater_than",
-    }
-
-    def _coerce_version(self, version):
-        if not isinstance(version, LegacyVersion):
-            version = LegacyVersion(str(version))
-        return version
-
-    def _compare_equal(self, prospective, spec):
-        return prospective == self._coerce_version(spec)
-
-    def _compare_not_equal(self, prospective, spec):
-        return prospective != self._coerce_version(spec)
-
-    def _compare_less_than_equal(self, prospective, spec):
-        return prospective <= self._coerce_version(spec)
-
-    def _compare_greater_than_equal(self, prospective, spec):
-        return prospective >= self._coerce_version(spec)
-
-    def _compare_less_than(self, prospective, spec):
-        return prospective < self._coerce_version(spec)
-
-    def _compare_greater_than(self, prospective, spec):
-        return prospective > self._coerce_version(spec)
-
-
-def _require_version_compare(fn):
-    @functools.wraps(fn)
-    def wrapped(self, prospective, spec):
-        if not isinstance(prospective, Version):
-            return False
-        return fn(self, prospective, spec)
-
-    return wrapped
-
-
-class Specifier(_IndividualSpecifier):
-
-    _regex_str = r"""
-        (?P<operator>(~=|==|!=|<=|>=|<|>|===))
-        (?P<version>
-            (?:
-                # The identity operators allow for an escape hatch that will
-                # do an exact string match of the version you wish to install.
-                # This will not be parsed by PEP 440 and we cannot determine
-                # any semantic meaning from it. This operator is discouraged
-                # but included entirely as an escape hatch.
-                (?<====)  # Only match for the identity operator
-                \s*
-                [^\s]*    # We just match everything, except for whitespace
-                          # since we are only testing for strict identity.
-            )
-            |
-            (?:
-                # The (non)equality operators allow for wild card and local
-                # versions to be specified so we have to define these two
-                # operators separately to enable that.
-                (?<===|!=)            # Only match for equals and not equals
-
-                \s*
-                v?
-                (?:[0-9]+!)?          # epoch
-                [0-9]+(?:\.[0-9]+)*   # release
-                (?:                   # pre release
-                    [-_\.]?
-                    (a|b|c|rc|alpha|beta|pre|preview)
-                    [-_\.]?
-                    [0-9]*
-                )?
-                (?:                   # post release
-                    (?:-[0-9]+)|(?:[-_\.]?(post|rev|r)[-_\.]?[0-9]*)
-                )?
-
-                # You cannot use a wild card and a dev or local version
-                # together so group them with a | and make them optional.
-                (?:
-                    (?:[-_\.]?dev[-_\.]?[0-9]*)?         # dev release
-                    (?:\+[a-z0-9]+(?:[-_\.][a-z0-9]+)*)? # local
-                    |
-                    \.\*  # Wild card syntax of .*
-                )?
-            )
-            |
-            (?:
-                # The compatible operator requires at least two digits in the
-                # release segment.
-                (?<=~=)               # Only match for the compatible operator
-
-                \s*
-                v?
-                (?:[0-9]+!)?          # epoch
-                [0-9]+(?:\.[0-9]+)+   # release  (We have a + instead of a *)
-                (?:                   # pre release
-                    [-_\.]?
-                    (a|b|c|rc|alpha|beta|pre|preview)
-                    [-_\.]?
-                    [0-9]*
-                )?
-                (?:                                   # post release
-                    (?:-[0-9]+)|(?:[-_\.]?(post|rev|r)[-_\.]?[0-9]*)
-                )?
-                (?:[-_\.]?dev[-_\.]?[0-9]*)?          # dev release
-            )
-            |
-            (?:
-                # All other operators only allow a sub set of what the
-                # (non)equality operators do. Specifically they do not allow
-                # local versions to be specified nor do they allow the prefix
-                # matching wild cards.
-                (?<!==|!=|~=)         # We have special cases for these
-                                      # operators so we want to make sure they
-                                      # don't match here.
-
-                \s*
-                v?
-                (?:[0-9]+!)?          # epoch
-                [0-9]+(?:\.[0-9]+)*   # release
-                (?:                   # pre release
-                    [-_\.]?
-                    (a|b|c|rc|alpha|beta|pre|preview)
-                    [-_\.]?
-                    [0-9]*
-                )?
-                (?:                                   # post release
-                    (?:-[0-9]+)|(?:[-_\.]?(post|rev|r)[-_\.]?[0-9]*)
-                )?
-                (?:[-_\.]?dev[-_\.]?[0-9]*)?          # dev release
-            )
-        )
-        """
-
-    _regex = re.compile(r"^\s*" + _regex_str + r"\s*$", re.VERBOSE | re.IGNORECASE)
-
-    _operators = {
-        "~=": "compatible",
-        "==": "equal",
-        "!=": "not_equal",
-        "<=": "less_than_equal",
-        ">=": "greater_than_equal",
-        "<": "less_than",
-        ">": "greater_than",
-        "===": "arbitrary",
-    }
-
-    @_require_version_compare
-    def _compare_compatible(self, prospective, spec):
-        # Compatible releases have an equivalent combination of >= and ==. That
-        # is that ~=2.2 is equivalent to >=2.2,==2.*. This allows us to
-        # implement this in terms of the other specifiers instead of
-        # implementing it ourselves. The only thing we need to do is construct
-        # the other specifiers.
-
-        # We want everything but the last item in the version, but we want to
-        # ignore post and dev releases and we want to treat the pre-release as
-        # it's own separate segment.
-        prefix = ".".join(
-            list(
-                itertools.takewhile(
-                    lambda x: (not x.startswith("post") and not x.startswith("dev")),
-                    _version_split(spec),
-                )
-            )[:-1]
-        )
-
-        # Add the prefix notation to the end of our string
-        prefix += ".*"
-
-        return self._get_operator(">=")(prospective, spec) and self._get_operator("==")(
-            prospective, prefix
-        )
-
-    @_require_version_compare
-    def _compare_equal(self, prospective, spec):
-        # We need special logic to handle prefix matching
-        if spec.endswith(".*"):
-            # In the case of prefix matching we want to ignore local segment.
-            prospective = Version(prospective.public)
-            # Split the spec out by dots, and pretend that there is an implicit
-            # dot in between a release segment and a pre-release segment.
-            spec = _version_split(spec[:-2])  # Remove the trailing .*
-
-            # Split the prospective version out by dots, and pretend that there
-            # is an implicit dot in between a release segment and a pre-release
-            # segment.
-            prospective = _version_split(str(prospective))
-
-            # Shorten the prospective version to be the same length as the spec
-            # so that we can determine if the specifier is a prefix of the
-            # prospective version or not.
-            prospective = prospective[: len(spec)]
-
-            # Pad out our two sides with zeros so that they both equal the same
-            # length.
-            spec, prospective = _pad_version(spec, prospective)
-        else:
-            # Convert our spec string into a Version
-            spec = Version(spec)
-
-            # If the specifier does not have a local segment, then we want to
-            # act as if the prospective version also does not have a local
-            # segment.
-            if not spec.local:
-                prospective = Version(prospective.public)
-
-        return prospective == spec
-
-    @_require_version_compare
-    def _compare_not_equal(self, prospective, spec):
-        return not self._compare_equal(prospective, spec)
-
-    @_require_version_compare
-    def _compare_less_than_equal(self, prospective, spec):
-        return prospective <= Version(spec)
-
-    @_require_version_compare
-    def _compare_greater_than_equal(self, prospective, spec):
-        return prospective >= Version(spec)
-
-    @_require_version_compare
-    def _compare_less_than(self, prospective, spec):
-        # Convert our spec to a Version instance, since we'll want to work with
-        # it as a version.
-        spec = Version(spec)
-
-        # Check to see if the prospective version is less than the spec
-        # version. If it's not we can short circuit and just return False now
-        # instead of doing extra unneeded work.
-        if not prospective < spec:
-            return False
-
-        # This special case is here so that, unless the specifier itself
-        # includes is a pre-release version, that we do not accept pre-release
-        # versions for the version mentioned in the specifier (e.g. <3.1 should
-        # not match 3.1.dev0, but should match 3.0.dev0).
-        if not spec.is_prerelease and prospective.is_prerelease:
-            if Version(prospective.base_version) == Version(spec.base_version):
-                return False
-
-        # If we've gotten to here, it means that prospective version is both
-        # less than the spec version *and* it's not a pre-release of the same
-        # version in the spec.
-        return True
-
-    @_require_version_compare
-    def _compare_greater_than(self, prospective, spec):
-        # Convert our spec to a Version instance, since we'll want to work with
-        # it as a version.
-        spec = Version(spec)
-
-        # Check to see if the prospective version is greater than the spec
-        # version. If it's not we can short circuit and just return False now
-        # instead of doing extra unneeded work.
-        if not prospective > spec:
-            return False
-
-        # This special case is here so that, unless the specifier itself
-        # includes is a post-release version, that we do not accept
-        # post-release versions for the version mentioned in the specifier
-        # (e.g. >3.1 should not match 3.0.post0, but should match 3.2.post0).
-        if not spec.is_postrelease and prospective.is_postrelease:
-            if Version(prospective.base_version) == Version(spec.base_version):
-                return False
-
-        # Ensure that we do not allow a local version of the version mentioned
-        # in the specifier, which is technically greater than, to match.
-        if prospective.local is not None:
-            if Version(prospective.base_version) == Version(spec.base_version):
-                return False
-
-        # If we've gotten to here, it means that prospective version is both
-        # greater than the spec version *and* it's not a pre-release of the
-        # same version in the spec.
-        return True
-
-    def _compare_arbitrary(self, prospective, spec):
-        return str(prospective).lower() == str(spec).lower()
-
-    @property
-    def prereleases(self):
-        # If there is an explicit prereleases set for this, then we'll just
-        # blindly use that.
-        if self._prereleases is not None:
-            return self._prereleases
-
-        # Look at all of our specifiers and determine if they are inclusive
-        # operators, and if they are if they are including an explicit
-        # prerelease.
-        operator, version = self._spec
-        if operator in ["==", ">=", "<=", "~=", "==="]:
-            # The == specifier can include a trailing .*, if it does we
-            # want to remove before parsing.
-            if operator == "==" and version.endswith(".*"):
-                version = version[:-2]
-
-            # Parse the version, and if it is a pre-release than this
-            # specifier allows pre-releases.
-            if parse(version).is_prerelease:
-                return True
-
-        return False
-
-    @prereleases.setter
-    def prereleases(self, value):
-        self._prereleases = value
-
-
-_prefix_regex = re.compile(r"^([0-9]+)((?:a|b|c|rc)[0-9]+)$")
-
-
-def _version_split(version):
-    result = []
-    for item in version.split("."):
-        match = _prefix_regex.search(item)
-        if match:
-            result.extend(match.groups())
-        else:
-            result.append(item)
-    return result
-
-
-def _pad_version(left, right):
-    left_split, right_split = [], []
-
-    # Get the release segment of our versions
-    left_split.append(list(itertools.takewhile(lambda x: x.isdigit(), left)))
-    right_split.append(list(itertools.takewhile(lambda x: x.isdigit(), right)))
-
-    # Get the rest of our versions
-    left_split.append(left[len(left_split[0]) :])
-    right_split.append(right[len(right_split[0]) :])
-
-    # Insert our padding
-    left_split.insert(1, ["0"] * max(0, len(right_split[0]) - len(left_split[0])))
-    right_split.insert(1, ["0"] * max(0, len(left_split[0]) - len(right_split[0])))
-
-    return (list(itertools.chain(*left_split)), list(itertools.chain(*right_split)))
-
-
-class SpecifierSet(BaseSpecifier):
-    def __init__(self, specifiers="", prereleases=None):
-        # Split on , to break each indidivual specifier into it's own item, and
-        # strip each item to remove leading/trailing whitespace.
-        specifiers = [s.strip() for s in specifiers.split(",") if s.strip()]
-
-        # Parsed each individual specifier, attempting first to make it a
-        # Specifier and falling back to a LegacySpecifier.
-        parsed = set()
-        for specifier in specifiers:
-            try:
-                parsed.add(Specifier(specifier))
-            except InvalidSpecifier:
-                parsed.add(LegacySpecifier(specifier))
-
-        # Turn our parsed specifiers into a frozen set and save them for later.
-        self._specs = frozenset(parsed)
-
-        # Store our prereleases value so we can use it later to determine if
-        # we accept prereleases or not.
-        self._prereleases = prereleases
-
-    def __repr__(self):
-        pre = (
-            ", prereleases={0!r}".format(self.prereleases)
-            if self._prereleases is not None
-            else ""
-        )
-
-        return "<SpecifierSet({0!r}{1})>".format(str(self), pre)
-
-    def __str__(self):
-        return ",".join(sorted(str(s) for s in self._specs))
-
-    def __hash__(self):
-        return hash(self._specs)
-
-    def __and__(self, other):
-        if isinstance(other, string_types):
-            other = SpecifierSet(other)
-        elif not isinstance(other, SpecifierSet):
-            return NotImplemented
-
-        specifier = SpecifierSet()
-        specifier._specs = frozenset(self._specs | other._specs)
-
-        if self._prereleases is None and other._prereleases is not None:
-            specifier._prereleases = other._prereleases
-        elif self._prereleases is not None and other._prereleases is None:
-            specifier._prereleases = self._prereleases
-        elif self._prereleases == other._prereleases:
-            specifier._prereleases = self._prereleases
-        else:
-            raise ValueError(
-                "Cannot combine SpecifierSets with True and False prerelease "
-                "overrides."
-            )
-
-        return specifier
-
-    def __eq__(self, other):
-        if isinstance(other, string_types):
-            other = SpecifierSet(other)
-        elif isinstance(other, _IndividualSpecifier):
-            other = SpecifierSet(str(other))
-        elif not isinstance(other, SpecifierSet):
-            return NotImplemented
-
-        return self._specs == other._specs
-
-    def __ne__(self, other):
-        if isinstance(other, string_types):
-            other = SpecifierSet(other)
-        elif isinstance(other, _IndividualSpecifier):
-            other = SpecifierSet(str(other))
-        elif not isinstance(other, SpecifierSet):
-            return NotImplemented
-
-        return self._specs != other._specs
-
-    def __len__(self):
-        return len(self._specs)
-
-    def __iter__(self):
-        return iter(self._specs)
-
-    @property
-    def prereleases(self):
-        # If we have been given an explicit prerelease modifier, then we'll
-        # pass that through here.
-        if self._prereleases is not None:
-            return self._prereleases
-
-        # If we don't have any specifiers, and we don't have a forced value,
-        # then we'll just return None since we don't know if this should have
-        # pre-releases or not.
-        if not self._specs:
-            return None
-
-        # Otherwise we'll see if any of the given specifiers accept
-        # prereleases, if any of them do we'll return True, otherwise False.
-        return any(s.prereleases for s in self._specs)
-
-    @prereleases.setter
-    def prereleases(self, value):
-        self._prereleases = value
-
-    def __contains__(self, item):
-        return self.contains(item)
-
-    def contains(self, item, prereleases=None):
-        # Ensure that our item is a Version or LegacyVersion instance.
-        if not isinstance(item, (LegacyVersion, Version)):
-            item = parse(item)
-
-        # Determine if we're forcing a prerelease or not, if we're not forcing
-        # one for this particular filter call, then we'll use whatever the
-        # SpecifierSet thinks for whether or not we should support prereleases.
-        if prereleases is None:
-            prereleases = self.prereleases
-
-        # We can determine if we're going to allow pre-releases by looking to
-        # see if any of the underlying items supports them. If none of them do
-        # and this item is a pre-release then we do not allow it and we can
-        # short circuit that here.
-        # Note: This means that 1.0.dev1 would not be contained in something
-        #       like >=1.0.devabc however it would be in >=1.0.debabc,>0.0.dev0
-        if not prereleases and item.is_prerelease:
-            return False
-
-        # We simply dispatch to the underlying specs here to make sure that the
-        # given version is contained within all of them.
-        # Note: This use of all() here means that an empty set of specifiers
-        #       will always return True, this is an explicit design decision.
-        return all(s.contains(item, prereleases=prereleases) for s in self._specs)
-
-    def filter(self, iterable, prereleases=None):
-        # Determine if we're forcing a prerelease or not, if we're not forcing
-        # one for this particular filter call, then we'll use whatever the
-        # SpecifierSet thinks for whether or not we should support prereleases.
-        if prereleases is None:
-            prereleases = self.prereleases
-
-        # If we have any specifiers, then we want to wrap our iterable in the
-        # filter method for each one, this will act as a logical AND amongst
-        # each specifier.
-        if self._specs:
-            for spec in self._specs:
-                iterable = spec.filter(iterable, prereleases=bool(prereleases))
-            return iterable
-        # If we do not have any specifiers, then we need to have a rough filter
-        # which will filter out any pre-releases, unless there are no final
-        # releases, and which will filter out LegacyVersion in general.
-        else:
-            filtered = []
-            found_prereleases = []
-
-            for item in iterable:
-                # Ensure that we some kind of Version class for this item.
-                if not isinstance(item, (LegacyVersion, Version)):
-                    parsed_version = parse(item)
-                else:
-                    parsed_version = item
-
-                # Filter out any item which is parsed as a LegacyVersion
-                if isinstance(parsed_version, LegacyVersion):
-                    continue
-
-                # Store any item which is a pre-release for later unless we've
-                # already found a final version or we are accepting prereleases
-                if parsed_version.is_prerelease and not prereleases:
-                    if not filtered:
-                        found_prereleases.append(item)
-                else:
-                    filtered.append(item)
-
-            # If we've found no items except for pre-releases, then we'll go
-            # ahead and use the pre-releases
-            if not filtered and found_prereleases and prereleases is None:
-                return found_prereleases
-
-            return filtered
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/utils.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/utils.py
deleted file mode 100644
index 8841878..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/utils.py
+++ /dev/null
@@ -1,57 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-import re
-
-from .version import InvalidVersion, Version
-
-
-_canonicalize_regex = re.compile(r"[-_.]+")
-
-
-def canonicalize_name(name):
-    # This is taken from PEP 503.
-    return _canonicalize_regex.sub("-", name).lower()
-
-
-def canonicalize_version(version):
-    """
-    This is very similar to Version.__str__, but has one subtle differences
-    with the way it handles the release segment.
-    """
-
-    try:
-        version = Version(version)
-    except InvalidVersion:
-        # Legacy versions cannot be normalized
-        return version
-
-    parts = []
-
-    # Epoch
-    if version.epoch != 0:
-        parts.append("{0}!".format(version.epoch))
-
-    # Release segment
-    # NB: This strips trailing '.0's to normalize
-    parts.append(re.sub(r"(\.0)+$", "", ".".join(str(x) for x in version.release)))
-
-    # Pre-release
-    if version.pre is not None:
-        parts.append("".join(str(x) for x in version.pre))
-
-    # Post-release
-    if version.post is not None:
-        parts.append(".post{0}".format(version.post))
-
-    # Development release
-    if version.dev is not None:
-        parts.append(".dev{0}".format(version.dev))
-
-    # Local version segment
-    if version.local is not None:
-        parts.append("+{0}".format(version.local))
-
-    return "".join(parts)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/version.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/version.py
deleted file mode 100644
index 95157a1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/packaging/version.py
+++ /dev/null
@@ -1,420 +0,0 @@
-# This file is dual licensed under the terms of the Apache License, Version
-# 2.0, and the BSD License. See the LICENSE file in the root of this repository
-# for complete details.
-from __future__ import absolute_import, division, print_function
-
-import collections
-import itertools
-import re
-
-from ._structures import Infinity
-
-
-__all__ = ["parse", "Version", "LegacyVersion", "InvalidVersion", "VERSION_PATTERN"]
-
-
-_Version = collections.namedtuple(
-    "_Version", ["epoch", "release", "dev", "pre", "post", "local"]
-)
-
-
-def parse(version):
-    """
-    Parse the given version string and return either a :class:`Version` object
-    or a :class:`LegacyVersion` object depending on if the given version is
-    a valid PEP 440 version or a legacy version.
-    """
-    try:
-        return Version(version)
-    except InvalidVersion:
-        return LegacyVersion(version)
-
-
-class InvalidVersion(ValueError):
-    """
-    An invalid version was found, users should refer to PEP 440.
-    """
-
-
-class _BaseVersion(object):
-    def __hash__(self):
-        return hash(self._key)
-
-    def __lt__(self, other):
-        return self._compare(other, lambda s, o: s < o)
-
-    def __le__(self, other):
-        return self._compare(other, lambda s, o: s <= o)
-
-    def __eq__(self, other):
-        return self._compare(other, lambda s, o: s == o)
-
-    def __ge__(self, other):
-        return self._compare(other, lambda s, o: s >= o)
-
-    def __gt__(self, other):
-        return self._compare(other, lambda s, o: s > o)
-
-    def __ne__(self, other):
-        return self._compare(other, lambda s, o: s != o)
-
-    def _compare(self, other, method):
-        if not isinstance(other, _BaseVersion):
-            return NotImplemented
-
-        return method(self._key, other._key)
-
-
-class LegacyVersion(_BaseVersion):
-    def __init__(self, version):
-        self._version = str(version)
-        self._key = _legacy_cmpkey(self._version)
-
-    def __str__(self):
-        return self._version
-
-    def __repr__(self):
-        return "<LegacyVersion({0})>".format(repr(str(self)))
-
-    @property
-    def public(self):
-        return self._version
-
-    @property
-    def base_version(self):
-        return self._version
-
-    @property
-    def epoch(self):
-        return -1
-
-    @property
-    def release(self):
-        return None
-
-    @property
-    def pre(self):
-        return None
-
-    @property
-    def post(self):
-        return None
-
-    @property
-    def dev(self):
-        return None
-
-    @property
-    def local(self):
-        return None
-
-    @property
-    def is_prerelease(self):
-        return False
-
-    @property
-    def is_postrelease(self):
-        return False
-
-    @property
-    def is_devrelease(self):
-        return False
-
-
-_legacy_version_component_re = re.compile(r"(\d+ | [a-z]+ | \.| -)", re.VERBOSE)
-
-_legacy_version_replacement_map = {
-    "pre": "c",
-    "preview": "c",
-    "-": "final-",
-    "rc": "c",
-    "dev": "@",
-}
-
-
-def _parse_version_parts(s):
-    for part in _legacy_version_component_re.split(s):
-        part = _legacy_version_replacement_map.get(part, part)
-
-        if not part or part == ".":
-            continue
-
-        if part[:1] in "0123456789":
-            # pad for numeric comparison
-            yield part.zfill(8)
-        else:
-            yield "*" + part
-
-    # ensure that alpha/beta/candidate are before final
-    yield "*final"
-
-
-def _legacy_cmpkey(version):
-    # We hardcode an epoch of -1 here. A PEP 440 version can only have a epoch
-    # greater than or equal to 0. This will effectively put the LegacyVersion,
-    # which uses the defacto standard originally implemented by setuptools,
-    # as before all PEP 440 versions.
-    epoch = -1
-
-    # This scheme is taken from pkg_resources.parse_version setuptools prior to
-    # it's adoption of the packaging library.
-    parts = []
-    for part in _parse_version_parts(version.lower()):
-        if part.startswith("*"):
-            # remove "-" before a prerelease tag
-            if part < "*final":
-                while parts and parts[-1] == "*final-":
-                    parts.pop()
-
-            # remove trailing zeros from each series of numeric parts
-            while parts and parts[-1] == "00000000":
-                parts.pop()
-
-        parts.append(part)
-    parts = tuple(parts)
-
-    return epoch, parts
-
-
-# Deliberately not anchored to the start and end of the string, to make it
-# easier for 3rd party code to reuse
-VERSION_PATTERN = r"""
-    v?
-    (?:
-        (?:(?P<epoch>[0-9]+)!)?                           # epoch
-        (?P<release>[0-9]+(?:\.[0-9]+)*)                  # release segment
-        (?P<pre>                                          # pre-release
-            [-_\.]?
-            (?P<pre_l>(a|b|c|rc|alpha|beta|pre|preview))
-            [-_\.]?
-            (?P<pre_n>[0-9]+)?
-        )?
-        (?P<post>                                         # post release
-            (?:-(?P<post_n1>[0-9]+))
-            |
-            (?:
-                [-_\.]?
-                (?P<post_l>post|rev|r)
-                [-_\.]?
-                (?P<post_n2>[0-9]+)?
-            )
-        )?
-        (?P<dev>                                          # dev release
-            [-_\.]?
-            (?P<dev_l>dev)
-            [-_\.]?
-            (?P<dev_n>[0-9]+)?
-        )?
-    )
-    (?:\+(?P<local>[a-z0-9]+(?:[-_\.][a-z0-9]+)*))?       # local version
-"""
-
-
-class Version(_BaseVersion):
-
-    _regex = re.compile(r"^\s*" + VERSION_PATTERN + r"\s*$", re.VERBOSE | re.IGNORECASE)
-
-    def __init__(self, version):
-        # Validate the version and parse it into pieces
-        match = self._regex.search(version)
-        if not match:
-            raise InvalidVersion("Invalid version: '{0}'".format(version))
-
-        # Store the parsed out pieces of the version
-        self._version = _Version(
-            epoch=int(match.group("epoch")) if match.group("epoch") else 0,
-            release=tuple(int(i) for i in match.group("release").split(".")),
-            pre=_parse_letter_version(match.group("pre_l"), match.group("pre_n")),
-            post=_parse_letter_version(
-                match.group("post_l"), match.group("post_n1") or match.group("post_n2")
-            ),
-            dev=_parse_letter_version(match.group("dev_l"), match.group("dev_n")),
-            local=_parse_local_version(match.group("local")),
-        )
-
-        # Generate a key which will be used for sorting
-        self._key = _cmpkey(
-            self._version.epoch,
-            self._version.release,
-            self._version.pre,
-            self._version.post,
-            self._version.dev,
-            self._version.local,
-        )
-
-    def __repr__(self):
-        return "<Version({0})>".format(repr(str(self)))
-
-    def __str__(self):
-        parts = []
-
-        # Epoch
-        if self.epoch != 0:
-            parts.append("{0}!".format(self.epoch))
-
-        # Release segment
-        parts.append(".".join(str(x) for x in self.release))
-
-        # Pre-release
-        if self.pre is not None:
-            parts.append("".join(str(x) for x in self.pre))
-
-        # Post-release
-        if self.post is not None:
-            parts.append(".post{0}".format(self.post))
-
-        # Development release
-        if self.dev is not None:
-            parts.append(".dev{0}".format(self.dev))
-
-        # Local version segment
-        if self.local is not None:
-            parts.append("+{0}".format(self.local))
-
-        return "".join(parts)
-
-    @property
-    def epoch(self):
-        return self._version.epoch
-
-    @property
-    def release(self):
-        return self._version.release
-
-    @property
-    def pre(self):
-        return self._version.pre
-
-    @property
-    def post(self):
-        return self._version.post[1] if self._version.post else None
-
-    @property
-    def dev(self):
-        return self._version.dev[1] if self._version.dev else None
-
-    @property
-    def local(self):
-        if self._version.local:
-            return ".".join(str(x) for x in self._version.local)
-        else:
-            return None
-
-    @property
-    def public(self):
-        return str(self).split("+", 1)[0]
-
-    @property
-    def base_version(self):
-        parts = []
-
-        # Epoch
-        if self.epoch != 0:
-            parts.append("{0}!".format(self.epoch))
-
-        # Release segment
-        parts.append(".".join(str(x) for x in self.release))
-
-        return "".join(parts)
-
-    @property
-    def is_prerelease(self):
-        return self.dev is not None or self.pre is not None
-
-    @property
-    def is_postrelease(self):
-        return self.post is not None
-
-    @property
-    def is_devrelease(self):
-        return self.dev is not None
-
-
-def _parse_letter_version(letter, number):
-    if letter:
-        # We consider there to be an implicit 0 in a pre-release if there is
-        # not a numeral associated with it.
-        if number is None:
-            number = 0
-
-        # We normalize any letters to their lower case form
-        letter = letter.lower()
-
-        # We consider some words to be alternate spellings of other words and
-        # in those cases we want to normalize the spellings to our preferred
-        # spelling.
-        if letter == "alpha":
-            letter = "a"
-        elif letter == "beta":
-            letter = "b"
-        elif letter in ["c", "pre", "preview"]:
-            letter = "rc"
-        elif letter in ["rev", "r"]:
-            letter = "post"
-
-        return letter, int(number)
-    if not letter and number:
-        # We assume if we are given a number, but we are not given a letter
-        # then this is using the implicit post release syntax (e.g. 1.0-1)
-        letter = "post"
-
-        return letter, int(number)
-
-
-_local_version_separators = re.compile(r"[\._-]")
-
-
-def _parse_local_version(local):
-    """
-    Takes a string like abc.1.twelve and turns it into ("abc", 1, "twelve").
-    """
-    if local is not None:
-        return tuple(
-            part.lower() if not part.isdigit() else int(part)
-            for part in _local_version_separators.split(local)
-        )
-
-
-def _cmpkey(epoch, release, pre, post, dev, local):
-    # When we compare a release version, we want to compare it with all of the
-    # trailing zeros removed. So we'll use a reverse the list, drop all the now
-    # leading zeros until we come to something non zero, then take the rest
-    # re-reverse it back into the correct order and make it a tuple and use
-    # that for our sorting key.
-    release = tuple(
-        reversed(list(itertools.dropwhile(lambda x: x == 0, reversed(release))))
-    )
-
-    # We need to "trick" the sorting algorithm to put 1.0.dev0 before 1.0a0.
-    # We'll do this by abusing the pre segment, but we _only_ want to do this
-    # if there is not a pre or a post segment. If we have one of those then
-    # the normal sorting rules will handle this case correctly.
-    if pre is None and post is None and dev is not None:
-        pre = -Infinity
-    # Versions without a pre-release (except as noted above) should sort after
-    # those with one.
-    elif pre is None:
-        pre = Infinity
-
-    # Versions without a post segment should sort before those with one.
-    if post is None:
-        post = -Infinity
-
-    # Versions without a development segment should sort after those with one.
-    if dev is None:
-        dev = Infinity
-
-    if local is None:
-        # Versions without a local segment should sort before those with one.
-        local = -Infinity
-    else:
-        # Versions with a local segment need that segment parsed to implement
-        # the sorting rules in PEP440.
-        # - Alpha numeric segments sort before numeric segments
-        # - Alpha numeric segments sort lexicographically
-        # - Numeric segments sort numerically
-        # - Shorter versions sort before longer versions when the prefixes
-        #   match exactly
-        local = tuple((i, "") if isinstance(i, int) else (-Infinity, i) for i in local)
-
-    return epoch, release, pre, post, dev, local
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__init__.py
deleted file mode 100644
index 9c1a098..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__init__.py
+++ /dev/null
@@ -1,4 +0,0 @@
-"""Wrappers to build Python packages using PEP 517 hooks
-"""
-
-__version__ = '0.5.0'
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 40d05aa..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/compat.cpython-37.pyc
deleted file mode 100644
index a1d9d4f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/wrappers.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/wrappers.cpython-37.pyc
deleted file mode 100644
index b56c6e4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/__pycache__/wrappers.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/_in_process.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/_in_process.py
deleted file mode 100644
index d6524b6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/_in_process.py
+++ /dev/null
@@ -1,207 +0,0 @@
-"""This is invoked in a subprocess to call the build backend hooks.
-
-It expects:
-- Command line args: hook_name, control_dir
-- Environment variable: PEP517_BUILD_BACKEND=entry.point:spec
-- control_dir/input.json:
-  - {"kwargs": {...}}
-
-Results:
-- control_dir/output.json
-  - {"return_val": ...}
-"""
-from glob import glob
-from importlib import import_module
-import os
-from os.path import join as pjoin
-import re
-import shutil
-import sys
-
-# This is run as a script, not a module, so it can't do a relative import
-import compat
-
-
-class BackendUnavailable(Exception):
-    """Raised if we cannot import the backend"""
-
-
-def _build_backend():
-    """Find and load the build backend"""
-    ep = os.environ['PEP517_BUILD_BACKEND']
-    mod_path, _, obj_path = ep.partition(':')
-    try:
-        obj = import_module(mod_path)
-    except ImportError:
-        raise BackendUnavailable
-    if obj_path:
-        for path_part in obj_path.split('.'):
-            obj = getattr(obj, path_part)
-    return obj
-
-
-def get_requires_for_build_wheel(config_settings):
-    """Invoke the optional get_requires_for_build_wheel hook
-
-    Returns [] if the hook is not defined.
-    """
-    backend = _build_backend()
-    try:
-        hook = backend.get_requires_for_build_wheel
-    except AttributeError:
-        return []
-    else:
-        return hook(config_settings)
-
-
-def prepare_metadata_for_build_wheel(metadata_directory, config_settings):
-    """Invoke optional prepare_metadata_for_build_wheel
-
-    Implements a fallback by building a wheel if the hook isn't defined.
-    """
-    backend = _build_backend()
-    try:
-        hook = backend.prepare_metadata_for_build_wheel
-    except AttributeError:
-        return _get_wheel_metadata_from_wheel(backend, metadata_directory,
-                                              config_settings)
-    else:
-        return hook(metadata_directory, config_settings)
-
-
-WHEEL_BUILT_MARKER = 'PEP517_ALREADY_BUILT_WHEEL'
-
-
-def _dist_info_files(whl_zip):
-    """Identify the .dist-info folder inside a wheel ZipFile."""
-    res = []
-    for path in whl_zip.namelist():
-        m = re.match(r'[^/\\]+-[^/\\]+\.dist-info/', path)
-        if m:
-            res.append(path)
-    if res:
-        return res
-    raise Exception("No .dist-info folder found in wheel")
-
-
-def _get_wheel_metadata_from_wheel(
-        backend, metadata_directory, config_settings):
-    """Build a wheel and extract the metadata from it.
-
-    Fallback for when the build backend does not
-    define the 'get_wheel_metadata' hook.
-    """
-    from zipfile import ZipFile
-    whl_basename = backend.build_wheel(metadata_directory, config_settings)
-    with open(os.path.join(metadata_directory, WHEEL_BUILT_MARKER), 'wb'):
-        pass  # Touch marker file
-
-    whl_file = os.path.join(metadata_directory, whl_basename)
-    with ZipFile(whl_file) as zipf:
-        dist_info = _dist_info_files(zipf)
-        zipf.extractall(path=metadata_directory, members=dist_info)
-    return dist_info[0].split('/')[0]
-
-
-def _find_already_built_wheel(metadata_directory):
-    """Check for a wheel already built during the get_wheel_metadata hook.
-    """
-    if not metadata_directory:
-        return None
-    metadata_parent = os.path.dirname(metadata_directory)
-    if not os.path.isfile(pjoin(metadata_parent, WHEEL_BUILT_MARKER)):
-        return None
-
-    whl_files = glob(os.path.join(metadata_parent, '*.whl'))
-    if not whl_files:
-        print('Found wheel built marker, but no .whl files')
-        return None
-    if len(whl_files) > 1:
-        print('Found multiple .whl files; unspecified behaviour. '
-              'Will call build_wheel.')
-        return None
-
-    # Exactly one .whl file
-    return whl_files[0]
-
-
-def build_wheel(wheel_directory, config_settings, metadata_directory=None):
-    """Invoke the mandatory build_wheel hook.
-
-    If a wheel was already built in the
-    prepare_metadata_for_build_wheel fallback, this
-    will copy it rather than rebuilding the wheel.
-    """
-    prebuilt_whl = _find_already_built_wheel(metadata_directory)
-    if prebuilt_whl:
-        shutil.copy2(prebuilt_whl, wheel_directory)
-        return os.path.basename(prebuilt_whl)
-
-    return _build_backend().build_wheel(wheel_directory, config_settings,
-                                        metadata_directory)
-
-
-def get_requires_for_build_sdist(config_settings):
-    """Invoke the optional get_requires_for_build_wheel hook
-
-    Returns [] if the hook is not defined.
-    """
-    backend = _build_backend()
-    try:
-        hook = backend.get_requires_for_build_sdist
-    except AttributeError:
-        return []
-    else:
-        return hook(config_settings)
-
-
-class _DummyException(Exception):
-    """Nothing should ever raise this exception"""
-
-
-class GotUnsupportedOperation(Exception):
-    """For internal use when backend raises UnsupportedOperation"""
-
-
-def build_sdist(sdist_directory, config_settings):
-    """Invoke the mandatory build_sdist hook."""
-    backend = _build_backend()
-    try:
-        return backend.build_sdist(sdist_directory, config_settings)
-    except getattr(backend, 'UnsupportedOperation', _DummyException):
-        raise GotUnsupportedOperation
-
-
-HOOK_NAMES = {
-    'get_requires_for_build_wheel',
-    'prepare_metadata_for_build_wheel',
-    'build_wheel',
-    'get_requires_for_build_sdist',
-    'build_sdist',
-}
-
-
-def main():
-    if len(sys.argv) < 3:
-        sys.exit("Needs args: hook_name, control_dir")
-    hook_name = sys.argv[1]
-    control_dir = sys.argv[2]
-    if hook_name not in HOOK_NAMES:
-        sys.exit("Unknown hook: %s" % hook_name)
-    hook = globals()[hook_name]
-
-    hook_input = compat.read_json(pjoin(control_dir, 'input.json'))
-
-    json_out = {'unsupported': False, 'return_val': None}
-    try:
-        json_out['return_val'] = hook(**hook_input['kwargs'])
-    except BackendUnavailable:
-        json_out['no_backend'] = True
-    except GotUnsupportedOperation:
-        json_out['unsupported'] = True
-
-    compat.write_json(json_out, pjoin(control_dir, 'output.json'), indent=2)
-
-
-if __name__ == '__main__':
-    main()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/build.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/build.py
deleted file mode 100644
index ac6c949..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/build.py
+++ /dev/null
@@ -1,108 +0,0 @@
-"""Build a project using PEP 517 hooks.
-"""
-import argparse
-import logging
-import os
-import contextlib
-from pip._vendor import pytoml
-import shutil
-import errno
-import tempfile
-
-from .envbuild import BuildEnvironment
-from .wrappers import Pep517HookCaller
-
-log = logging.getLogger(__name__)
-
-
-@contextlib.contextmanager
-def tempdir():
-    td = tempfile.mkdtemp()
-    try:
-        yield td
-    finally:
-        shutil.rmtree(td)
-
-
-def _do_build(hooks, env, dist, dest):
-    get_requires_name = 'get_requires_for_build_{dist}'.format(**locals())
-    get_requires = getattr(hooks, get_requires_name)
-    reqs = get_requires({})
-    log.info('Got build requires: %s', reqs)
-
-    env.pip_install(reqs)
-    log.info('Installed dynamic build dependencies')
-
-    with tempdir() as td:
-        log.info('Trying to build %s in %s', dist, td)
-        build_name = 'build_{dist}'.format(**locals())
-        build = getattr(hooks, build_name)
-        filename = build(td, {})
-        source = os.path.join(td, filename)
-        shutil.move(source, os.path.join(dest, os.path.basename(filename)))
-
-
-def mkdir_p(*args, **kwargs):
-    """Like `mkdir`, but does not raise an exception if the
-    directory already exists.
-    """
-    try:
-        return os.mkdir(*args, **kwargs)
-    except OSError as exc:
-        if exc.errno != errno.EEXIST:
-            raise
-
-
-def build(source_dir, dist, dest=None):
-    pyproject = os.path.join(source_dir, 'pyproject.toml')
-    dest = os.path.join(source_dir, dest or 'dist')
-    mkdir_p(dest)
-
-    with open(pyproject) as f:
-        pyproject_data = pytoml.load(f)
-    # Ensure the mandatory data can be loaded
-    buildsys = pyproject_data['build-system']
-    requires = buildsys['requires']
-    backend = buildsys['build-backend']
-
-    hooks = Pep517HookCaller(source_dir, backend)
-
-    with BuildEnvironment() as env:
-        env.pip_install(requires)
-        _do_build(hooks, env, dist, dest)
-
-
-parser = argparse.ArgumentParser()
-parser.add_argument(
-    'source_dir',
-    help="A directory containing pyproject.toml",
-)
-parser.add_argument(
-    '--binary', '-b',
-    action='store_true',
-    default=False,
-)
-parser.add_argument(
-    '--source', '-s',
-    action='store_true',
-    default=False,
-)
-parser.add_argument(
-    '--out-dir', '-o',
-    help="Destination in which to save the builds relative to source dir",
-)
-
-
-def main(args):
-    # determine which dists to build
-    dists = list(filter(None, (
-        'sdist' if args.source or not args.binary else None,
-        'wheel' if args.binary or not args.source else None,
-    )))
-
-    for dist in dists:
-        build(args.source_dir, dist, args.out_dir)
-
-
-if __name__ == '__main__':
-    main(parser.parse_args())
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/check.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/check.py
deleted file mode 100644
index f4cdc6b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/check.py
+++ /dev/null
@@ -1,202 +0,0 @@
-"""Check a project and backend by attempting to build using PEP 517 hooks.
-"""
-import argparse
-import logging
-import os
-from os.path import isfile, join as pjoin
-from pip._vendor.pytoml import TomlError, load as toml_load
-import shutil
-from subprocess import CalledProcessError
-import sys
-import tarfile
-from tempfile import mkdtemp
-import zipfile
-
-from .colorlog import enable_colourful_output
-from .envbuild import BuildEnvironment
-from .wrappers import Pep517HookCaller
-
-log = logging.getLogger(__name__)
-
-
-def check_build_sdist(hooks, build_sys_requires):
-    with BuildEnvironment() as env:
-        try:
-            env.pip_install(build_sys_requires)
-            log.info('Installed static build dependencies')
-        except CalledProcessError:
-            log.error('Failed to install static build dependencies')
-            return False
-
-        try:
-            reqs = hooks.get_requires_for_build_sdist({})
-            log.info('Got build requires: %s', reqs)
-        except Exception:
-            log.error('Failure in get_requires_for_build_sdist', exc_info=True)
-            return False
-
-        try:
-            env.pip_install(reqs)
-            log.info('Installed dynamic build dependencies')
-        except CalledProcessError:
-            log.error('Failed to install dynamic build dependencies')
-            return False
-
-        td = mkdtemp()
-        log.info('Trying to build sdist in %s', td)
-        try:
-            try:
-                filename = hooks.build_sdist(td, {})
-                log.info('build_sdist returned %r', filename)
-            except Exception:
-                log.info('Failure in build_sdist', exc_info=True)
-                return False
-
-            if not filename.endswith('.tar.gz'):
-                log.error(
-                    "Filename %s doesn't have .tar.gz extension", filename)
-                return False
-
-            path = pjoin(td, filename)
-            if isfile(path):
-                log.info("Output file %s exists", path)
-            else:
-                log.error("Output file %s does not exist", path)
-                return False
-
-            if tarfile.is_tarfile(path):
-                log.info("Output file is a tar file")
-            else:
-                log.error("Output file is not a tar file")
-                return False
-
-        finally:
-            shutil.rmtree(td)
-
-        return True
-
-
-def check_build_wheel(hooks, build_sys_requires):
-    with BuildEnvironment() as env:
-        try:
-            env.pip_install(build_sys_requires)
-            log.info('Installed static build dependencies')
-        except CalledProcessError:
-            log.error('Failed to install static build dependencies')
-            return False
-
-        try:
-            reqs = hooks.get_requires_for_build_wheel({})
-            log.info('Got build requires: %s', reqs)
-        except Exception:
-            log.error('Failure in get_requires_for_build_sdist', exc_info=True)
-            return False
-
-        try:
-            env.pip_install(reqs)
-            log.info('Installed dynamic build dependencies')
-        except CalledProcessError:
-            log.error('Failed to install dynamic build dependencies')
-            return False
-
-        td = mkdtemp()
-        log.info('Trying to build wheel in %s', td)
-        try:
-            try:
-                filename = hooks.build_wheel(td, {})
-                log.info('build_wheel returned %r', filename)
-            except Exception:
-                log.info('Failure in build_wheel', exc_info=True)
-                return False
-
-            if not filename.endswith('.whl'):
-                log.error("Filename %s doesn't have .whl extension", filename)
-                return False
-
-            path = pjoin(td, filename)
-            if isfile(path):
-                log.info("Output file %s exists", path)
-            else:
-                log.error("Output file %s does not exist", path)
-                return False
-
-            if zipfile.is_zipfile(path):
-                log.info("Output file is a zip file")
-            else:
-                log.error("Output file is not a zip file")
-                return False
-
-        finally:
-            shutil.rmtree(td)
-
-        return True
-
-
-def check(source_dir):
-    pyproject = pjoin(source_dir, 'pyproject.toml')
-    if isfile(pyproject):
-        log.info('Found pyproject.toml')
-    else:
-        log.error('Missing pyproject.toml')
-        return False
-
-    try:
-        with open(pyproject) as f:
-            pyproject_data = toml_load(f)
-        # Ensure the mandatory data can be loaded
-        buildsys = pyproject_data['build-system']
-        requires = buildsys['requires']
-        backend = buildsys['build-backend']
-        log.info('Loaded pyproject.toml')
-    except (TomlError, KeyError):
-        log.error("Invalid pyproject.toml", exc_info=True)
-        return False
-
-    hooks = Pep517HookCaller(source_dir, backend)
-
-    sdist_ok = check_build_sdist(hooks, requires)
-    wheel_ok = check_build_wheel(hooks, requires)
-
-    if not sdist_ok:
-        log.warning('Sdist checks failed; scroll up to see')
-    if not wheel_ok:
-        log.warning('Wheel checks failed')
-
-    return sdist_ok
-
-
-def main(argv=None):
-    ap = argparse.ArgumentParser()
-    ap.add_argument(
-        'source_dir',
-        help="A directory containing pyproject.toml")
-    args = ap.parse_args(argv)
-
-    enable_colourful_output()
-
-    ok = check(args.source_dir)
-
-    if ok:
-        print(ansi('Checks passed', 'green'))
-    else:
-        print(ansi('Checks failed', 'red'))
-        sys.exit(1)
-
-
-ansi_codes = {
-    'reset': '\x1b[0m',
-    'bold': '\x1b[1m',
-    'red': '\x1b[31m',
-    'green': '\x1b[32m',
-}
-
-
-def ansi(s, attr):
-    if os.name != 'nt' and sys.stdout.isatty():
-        return ansi_codes[attr] + str(s) + ansi_codes['reset']
-    else:
-        return str(s)
-
-
-if __name__ == '__main__':
-    main()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/colorlog.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/colorlog.py
deleted file mode 100644
index 69c8a59..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/colorlog.py
+++ /dev/null
@@ -1,115 +0,0 @@
-"""Nicer log formatting with colours.
-
-Code copied from Tornado, Apache licensed.
-"""
-# Copyright 2012 Facebook
-#
-# Licensed under the Apache License, Version 2.0 (the "License"); you may
-# not use this file except in compliance with the License. You may obtain
-# a copy of the License at
-#
-# http://www.apache.org/licenses/LICENSE-2.0
-#
-# Unless required by applicable law or agreed to in writing, software
-# distributed under the License is distributed on an "AS IS" BASIS, WITHOUT
-# WARRANTIES OR CONDITIONS OF ANY KIND, either express or implied. See the
-# License for the specific language governing permissions and limitations
-# under the License.
-
-import logging
-import sys
-
-try:
-    import curses
-except ImportError:
-    curses = None
-
-
-def _stderr_supports_color():
-    color = False
-    if curses and hasattr(sys.stderr, 'isatty') and sys.stderr.isatty():
-        try:
-            curses.setupterm()
-            if curses.tigetnum("colors") > 0:
-                color = True
-        except Exception:
-            pass
-    return color
-
-
-class LogFormatter(logging.Formatter):
-    """Log formatter with colour support
-    """
-    DEFAULT_COLORS = {
-        logging.INFO: 2,  # Green
-        logging.WARNING: 3,  # Yellow
-        logging.ERROR: 1,  # Red
-        logging.CRITICAL: 1,
-    }
-
-    def __init__(self, color=True, datefmt=None):
-        r"""
-        :arg bool color: Enables color support.
-        :arg string fmt: Log message format.
-        It will be applied to the attributes dict of log records. The
-        text between ``%(color)s`` and ``%(end_color)s`` will be colored
-        depending on the level if color support is on.
-        :arg dict colors: color mappings from logging level to terminal color
-        code
-        :arg string datefmt: Datetime format.
-        Used for formatting ``(asctime)`` placeholder in ``prefix_fmt``.
-        .. versionchanged:: 3.2
-        Added ``fmt`` and ``datefmt`` arguments.
-        """
-        logging.Formatter.__init__(self, datefmt=datefmt)
-        self._colors = {}
-        if color and _stderr_supports_color():
-            # The curses module has some str/bytes confusion in
-            # python3. Until version 3.2.3, most methods return
-            # bytes, but only accept strings. In addition, we want to
-            # output these strings with the logging module, which
-            # works with unicode strings. The explicit calls to
-            # unicode() below are harmless in python2 but will do the
-            # right conversion in python 3.
-            fg_color = (curses.tigetstr("setaf") or
-                        curses.tigetstr("setf") or "")
-            if (3, 0) < sys.version_info < (3, 2, 3):
-                fg_color = str(fg_color, "ascii")
-
-            for levelno, code in self.DEFAULT_COLORS.items():
-                self._colors[levelno] = str(
-                    curses.tparm(fg_color, code), "ascii")
-            self._normal = str(curses.tigetstr("sgr0"), "ascii")
-
-            scr = curses.initscr()
-            self.termwidth = scr.getmaxyx()[1]
-            curses.endwin()
-        else:
-            self._normal = ''
-            # Default width is usually 80, but too wide is
-            # worse than too narrow
-            self.termwidth = 70
-
-    def formatMessage(self, record):
-        mlen = len(record.message)
-        right_text = '{initial}-{name}'.format(initial=record.levelname[0],
-                                               name=record.name)
-        if mlen + len(right_text) < self.termwidth:
-            space = ' ' * (self.termwidth - (mlen + len(right_text)))
-        else:
-            space = '  '
-
-        if record.levelno in self._colors:
-            start_color = self._colors[record.levelno]
-            end_color = self._normal
-        else:
-            start_color = end_color = ''
-
-        return record.message + space + start_color + right_text + end_color
-
-
-def enable_colourful_output(level=logging.INFO):
-    handler = logging.StreamHandler()
-    handler.setFormatter(LogFormatter())
-    logging.root.addHandler(handler)
-    logging.root.setLevel(level)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/compat.py
deleted file mode 100644
index 01c66fc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/compat.py
+++ /dev/null
@@ -1,23 +0,0 @@
-"""Handle reading and writing JSON in UTF-8, on Python 3 and 2."""
-import json
-import sys
-
-if sys.version_info[0] >= 3:
-    # Python 3
-    def write_json(obj, path, **kwargs):
-        with open(path, 'w', encoding='utf-8') as f:
-            json.dump(obj, f, **kwargs)
-
-    def read_json(path):
-        with open(path, 'r', encoding='utf-8') as f:
-            return json.load(f)
-
-else:
-    # Python 2
-    def write_json(obj, path, **kwargs):
-        with open(path, 'wb') as f:
-            json.dump(obj, f, encoding='utf-8', **kwargs)
-
-    def read_json(path):
-        with open(path, 'rb') as f:
-            return json.load(f)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/envbuild.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/envbuild.py
deleted file mode 100644
index f7ac5f4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/envbuild.py
+++ /dev/null
@@ -1,158 +0,0 @@
-"""Build wheels/sdists by installing build deps to a temporary environment.
-"""
-
-import os
-import logging
-from pip._vendor import pytoml
-import shutil
-from subprocess import check_call
-import sys
-from sysconfig import get_paths
-from tempfile import mkdtemp
-
-from .wrappers import Pep517HookCaller
-
-log = logging.getLogger(__name__)
-
-
-def _load_pyproject(source_dir):
-    with open(os.path.join(source_dir, 'pyproject.toml')) as f:
-        pyproject_data = pytoml.load(f)
-    buildsys = pyproject_data['build-system']
-    return buildsys['requires'], buildsys['build-backend']
-
-
-class BuildEnvironment(object):
-    """Context manager to install build deps in a simple temporary environment
-
-    Based on code I wrote for pip, which is MIT licensed.
-    """
-    # Copyright (c) 2008-2016 The pip developers (see AUTHORS.txt file)
-    #
-    # Permission is hereby granted, free of charge, to any person obtaining
-    # a copy of this software and associated documentation files (the
-    # "Software"), to deal in the Software without restriction, including
-    # without limitation the rights to use, copy, modify, merge, publish,
-    # distribute, sublicense, and/or sell copies of the Software, and to
-    # permit persons to whom the Software is furnished to do so, subject to
-    # the following conditions:
-    #
-    # The above copyright notice and this permission notice shall be
-    # included in all copies or substantial portions of the Software.
-    #
-    # THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND,
-    # EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF
-    # MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND
-    # NONINFRINGEMENT. IN NO EVENT SHALL THE AUTHORS OR COPYRIGHT HOLDERS BE
-    # LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION
-    # OF CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION
-    # WITH THE SOFTWARE OR THE USE OR OTHER DEALINGS IN THE SOFTWARE.
-
-    path = None
-
-    def __init__(self, cleanup=True):
-        self._cleanup = cleanup
-
-    def __enter__(self):
-        self.path = mkdtemp(prefix='pep517-build-env-')
-        log.info('Temporary build environment: %s', self.path)
-
-        self.save_path = os.environ.get('PATH', None)
-        self.save_pythonpath = os.environ.get('PYTHONPATH', None)
-
-        install_scheme = 'nt' if (os.name == 'nt') else 'posix_prefix'
-        install_dirs = get_paths(install_scheme, vars={
-            'base': self.path,
-            'platbase': self.path,
-        })
-
-        scripts = install_dirs['scripts']
-        if self.save_path:
-            os.environ['PATH'] = scripts + os.pathsep + self.save_path
-        else:
-            os.environ['PATH'] = scripts + os.pathsep + os.defpath
-
-        if install_dirs['purelib'] == install_dirs['platlib']:
-            lib_dirs = install_dirs['purelib']
-        else:
-            lib_dirs = install_dirs['purelib'] + os.pathsep + \
-                install_dirs['platlib']
-        if self.save_pythonpath:
-            os.environ['PYTHONPATH'] = lib_dirs + os.pathsep + \
-                self.save_pythonpath
-        else:
-            os.environ['PYTHONPATH'] = lib_dirs
-
-        return self
-
-    def pip_install(self, reqs):
-        """Install dependencies into this env by calling pip in a subprocess"""
-        if not reqs:
-            return
-        log.info('Calling pip to install %s', reqs)
-        check_call([
-            sys.executable, '-m', 'pip', 'install', '--ignore-installed',
-            '--prefix', self.path] + list(reqs))
-
-    def __exit__(self, exc_type, exc_val, exc_tb):
-        needs_cleanup = (
-            self._cleanup and
-            self.path is not None and
-            os.path.isdir(self.path)
-        )
-        if needs_cleanup:
-            shutil.rmtree(self.path)
-
-        if self.save_path is None:
-            os.environ.pop('PATH', None)
-        else:
-            os.environ['PATH'] = self.save_path
-
-        if self.save_pythonpath is None:
-            os.environ.pop('PYTHONPATH', None)
-        else:
-            os.environ['PYTHONPATH'] = self.save_pythonpath
-
-
-def build_wheel(source_dir, wheel_dir, config_settings=None):
-    """Build a wheel from a source directory using PEP 517 hooks.
-
-    :param str source_dir: Source directory containing pyproject.toml
-    :param str wheel_dir: Target directory to create wheel in
-    :param dict config_settings: Options to pass to build backend
-
-    This is a blocking function which will run pip in a subprocess to install
-    build requirements.
-    """
-    if config_settings is None:
-        config_settings = {}
-    requires, backend = _load_pyproject(source_dir)
-    hooks = Pep517HookCaller(source_dir, backend)
-
-    with BuildEnvironment() as env:
-        env.pip_install(requires)
-        reqs = hooks.get_requires_for_build_wheel(config_settings)
-        env.pip_install(reqs)
-        return hooks.build_wheel(wheel_dir, config_settings)
-
-
-def build_sdist(source_dir, sdist_dir, config_settings=None):
-    """Build an sdist from a source directory using PEP 517 hooks.
-
-    :param str source_dir: Source directory containing pyproject.toml
-    :param str sdist_dir: Target directory to place sdist in
-    :param dict config_settings: Options to pass to build backend
-
-    This is a blocking function which will run pip in a subprocess to install
-    build requirements.
-    """
-    if config_settings is None:
-        config_settings = {}
-    requires, backend = _load_pyproject(source_dir)
-    hooks = Pep517HookCaller(source_dir, backend)
-
-    with BuildEnvironment() as env:
-        env.pip_install(requires)
-        reqs = hooks.get_requires_for_build_sdist(config_settings)
-        env.pip_install(reqs)
-        return hooks.build_sdist(sdist_dir, config_settings)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/wrappers.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/wrappers.py
deleted file mode 100644
index b14b899..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pep517/wrappers.py
+++ /dev/null
@@ -1,163 +0,0 @@
-from contextlib import contextmanager
-import os
-from os.path import dirname, abspath, join as pjoin
-import shutil
-from subprocess import check_call
-import sys
-from tempfile import mkdtemp
-
-from . import compat
-
-_in_proc_script = pjoin(dirname(abspath(__file__)), '_in_process.py')
-
-
-@contextmanager
-def tempdir():
-    td = mkdtemp()
-    try:
-        yield td
-    finally:
-        shutil.rmtree(td)
-
-
-class BackendUnavailable(Exception):
-    """Will be raised if the backend cannot be imported in the hook process."""
-
-
-class UnsupportedOperation(Exception):
-    """May be raised by build_sdist if the backend indicates that it can't."""
-
-
-def default_subprocess_runner(cmd, cwd=None, extra_environ=None):
-    """The default method of calling the wrapper subprocess."""
-    env = os.environ.copy()
-    if extra_environ:
-        env.update(extra_environ)
-
-    check_call(cmd, cwd=cwd, env=env)
-
-
-class Pep517HookCaller(object):
-    """A wrapper around a source directory to be built with a PEP 517 backend.
-
-    source_dir : The path to the source directory, containing pyproject.toml.
-    backend : The build backend spec, as per PEP 517, from pyproject.toml.
-    """
-    def __init__(self, source_dir, build_backend):
-        self.source_dir = abspath(source_dir)
-        self.build_backend = build_backend
-        self._subprocess_runner = default_subprocess_runner
-
-    # TODO: Is this over-engineered? Maybe frontends only need to
-    #       set this when creating the wrapper, not on every call.
-    @contextmanager
-    def subprocess_runner(self, runner):
-        prev = self._subprocess_runner
-        self._subprocess_runner = runner
-        yield
-        self._subprocess_runner = prev
-
-    def get_requires_for_build_wheel(self, config_settings=None):
-        """Identify packages required for building a wheel
-
-        Returns a list of dependency specifications, e.g.:
-            ["wheel >= 0.25", "setuptools"]
-
-        This does not include requirements specified in pyproject.toml.
-        It returns the result of calling the equivalently named hook in a
-        subprocess.
-        """
-        return self._call_hook('get_requires_for_build_wheel', {
-            'config_settings': config_settings
-        })
-
-    def prepare_metadata_for_build_wheel(
-            self, metadata_directory, config_settings=None):
-        """Prepare a *.dist-info folder with metadata for this project.
-
-        Returns the name of the newly created folder.
-
-        If the build backend defines a hook with this name, it will be called
-        in a subprocess. If not, the backend will be asked to build a wheel,
-        and the dist-info extracted from that.
-        """
-        return self._call_hook('prepare_metadata_for_build_wheel', {
-            'metadata_directory': abspath(metadata_directory),
-            'config_settings': config_settings,
-        })
-
-    def build_wheel(
-            self, wheel_directory, config_settings=None,
-            metadata_directory=None):
-        """Build a wheel from this project.
-
-        Returns the name of the newly created file.
-
-        In general, this will call the 'build_wheel' hook in the backend.
-        However, if that was previously called by
-        'prepare_metadata_for_build_wheel', and the same metadata_directory is
-        used, the previously built wheel will be copied to wheel_directory.
-        """
-        if metadata_directory is not None:
-            metadata_directory = abspath(metadata_directory)
-        return self._call_hook('build_wheel', {
-            'wheel_directory': abspath(wheel_directory),
-            'config_settings': config_settings,
-            'metadata_directory': metadata_directory,
-        })
-
-    def get_requires_for_build_sdist(self, config_settings=None):
-        """Identify packages required for building a wheel
-
-        Returns a list of dependency specifications, e.g.:
-            ["setuptools >= 26"]
-
-        This does not include requirements specified in pyproject.toml.
-        It returns the result of calling the equivalently named hook in a
-        subprocess.
-        """
-        return self._call_hook('get_requires_for_build_sdist', {
-            'config_settings': config_settings
-        })
-
-    def build_sdist(self, sdist_directory, config_settings=None):
-        """Build an sdist from this project.
-
-        Returns the name of the newly created file.
-
-        This calls the 'build_sdist' backend hook in a subprocess.
-        """
-        return self._call_hook('build_sdist', {
-            'sdist_directory': abspath(sdist_directory),
-            'config_settings': config_settings,
-        })
-
-    def _call_hook(self, hook_name, kwargs):
-        # On Python 2, pytoml returns Unicode values (which is correct) but the
-        # environment passed to check_call needs to contain string values. We
-        # convert here by encoding using ASCII (the backend can only contain
-        # letters, digits and _, . and : characters, and will be used as a
-        # Python identifier, so non-ASCII content is wrong on Python 2 in
-        # any case).
-        if sys.version_info[0] == 2:
-            build_backend = self.build_backend.encode('ASCII')
-        else:
-            build_backend = self.build_backend
-
-        with tempdir() as td:
-            compat.write_json({'kwargs': kwargs}, pjoin(td, 'input.json'),
-                              indent=2)
-
-            # Run the hook in a subprocess
-            self._subprocess_runner(
-                [sys.executable, _in_proc_script, hook_name, td],
-                cwd=self.source_dir,
-                extra_environ={'PEP517_BUILD_BACKEND': build_backend}
-            )
-
-            data = compat.read_json(pjoin(td, 'output.json'))
-            if data.get('unsupported'):
-                raise UnsupportedOperation
-            if data.get('no_backend'):
-                raise BackendUnavailable
-            return data['return_val']
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__init__.py
deleted file mode 100644
index 9c4fd8e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__init__.py
+++ /dev/null
@@ -1,3171 +0,0 @@
-# coding: utf-8
-"""
-Package resource API
---------------------
-
-A resource is a logical file contained within a package, or a logical
-subdirectory thereof.  The package resource API expects resource names
-to have their path parts separated with ``/``, *not* whatever the local
-path separator is.  Do not use os.path operations to manipulate resource
-names being passed into the API.
-
-The package resource API is designed to work with normal filesystem packages,
-.egg files, and unpacked .egg files.  It can also work in a limited way with
-.zip files and with custom PEP 302 loaders that support the ``get_data()``
-method.
-"""
-
-from __future__ import absolute_import
-
-import sys
-import os
-import io
-import time
-import re
-import types
-import zipfile
-import zipimport
-import warnings
-import stat
-import functools
-import pkgutil
-import operator
-import platform
-import collections
-import plistlib
-import email.parser
-import errno
-import tempfile
-import textwrap
-import itertools
-import inspect
-from pkgutil import get_importer
-
-try:
-    import _imp
-except ImportError:
-    # Python 3.2 compatibility
-    import imp as _imp
-
-try:
-    FileExistsError
-except NameError:
-    FileExistsError = OSError
-
-from pip._vendor import six
-from pip._vendor.six.moves import urllib, map, filter
-
-# capture these to bypass sandboxing
-from os import utime
-try:
-    from os import mkdir, rename, unlink
-    WRITE_SUPPORT = True
-except ImportError:
-    # no write support, probably under GAE
-    WRITE_SUPPORT = False
-
-from os import open as os_open
-from os.path import isdir, split
-
-try:
-    import importlib.machinery as importlib_machinery
-    # access attribute to force import under delayed import mechanisms.
-    importlib_machinery.__name__
-except ImportError:
-    importlib_machinery = None
-
-from . import py31compat
-from pip._vendor import appdirs
-from pip._vendor import packaging
-__import__('pip._vendor.packaging.version')
-__import__('pip._vendor.packaging.specifiers')
-__import__('pip._vendor.packaging.requirements')
-__import__('pip._vendor.packaging.markers')
-
-
-__metaclass__ = type
-
-
-if (3, 0) < sys.version_info < (3, 4):
-    raise RuntimeError("Python 3.4 or later is required")
-
-if six.PY2:
-    # Those builtin exceptions are only defined in Python 3
-    PermissionError = None
-    NotADirectoryError = None
-
-# declare some globals that will be defined later to
-# satisfy the linters.
-require = None
-working_set = None
-add_activation_listener = None
-resources_stream = None
-cleanup_resources = None
-resource_dir = None
-resource_stream = None
-set_extraction_path = None
-resource_isdir = None
-resource_string = None
-iter_entry_points = None
-resource_listdir = None
-resource_filename = None
-resource_exists = None
-_distribution_finders = None
-_namespace_handlers = None
-_namespace_packages = None
-
-
-class PEP440Warning(RuntimeWarning):
-    """
-    Used when there is an issue with a version or specifier not complying with
-    PEP 440.
-    """
-
-
-def parse_version(v):
-    try:
-        return packaging.version.Version(v)
-    except packaging.version.InvalidVersion:
-        return packaging.version.LegacyVersion(v)
-
-
-_state_vars = {}
-
-
-def _declare_state(vartype, **kw):
-    globals().update(kw)
-    _state_vars.update(dict.fromkeys(kw, vartype))
-
-
-def __getstate__():
-    state = {}
-    g = globals()
-    for k, v in _state_vars.items():
-        state[k] = g['_sget_' + v](g[k])
-    return state
-
-
-def __setstate__(state):
-    g = globals()
-    for k, v in state.items():
-        g['_sset_' + _state_vars[k]](k, g[k], v)
-    return state
-
-
-def _sget_dict(val):
-    return val.copy()
-
-
-def _sset_dict(key, ob, state):
-    ob.clear()
-    ob.update(state)
-
-
-def _sget_object(val):
-    return val.__getstate__()
-
-
-def _sset_object(key, ob, state):
-    ob.__setstate__(state)
-
-
-_sget_none = _sset_none = lambda *args: None
-
-
-def get_supported_platform():
-    """Return this platform's maximum compatible version.
-
-    distutils.util.get_platform() normally reports the minimum version
-    of Mac OS X that would be required to *use* extensions produced by
-    distutils.  But what we want when checking compatibility is to know the
-    version of Mac OS X that we are *running*.  To allow usage of packages that
-    explicitly require a newer version of Mac OS X, we must also know the
-    current version of the OS.
-
-    If this condition occurs for any other platform with a version in its
-    platform strings, this function should be extended accordingly.
-    """
-    plat = get_build_platform()
-    m = macosVersionString.match(plat)
-    if m is not None and sys.platform == "darwin":
-        try:
-            plat = 'macosx-%s-%s' % ('.'.join(_macosx_vers()[:2]), m.group(3))
-        except ValueError:
-            # not Mac OS X
-            pass
-    return plat
-
-
-__all__ = [
-    # Basic resource access and distribution/entry point discovery
-    'require', 'run_script', 'get_provider', 'get_distribution',
-    'load_entry_point', 'get_entry_map', 'get_entry_info',
-    'iter_entry_points',
-    'resource_string', 'resource_stream', 'resource_filename',
-    'resource_listdir', 'resource_exists', 'resource_isdir',
-
-    # Environmental control
-    'declare_namespace', 'working_set', 'add_activation_listener',
-    'find_distributions', 'set_extraction_path', 'cleanup_resources',
-    'get_default_cache',
-
-    # Primary implementation classes
-    'Environment', 'WorkingSet', 'ResourceManager',
-    'Distribution', 'Requirement', 'EntryPoint',
-
-    # Exceptions
-    'ResolutionError', 'VersionConflict', 'DistributionNotFound',
-    'UnknownExtra', 'ExtractionError',
-
-    # Warnings
-    'PEP440Warning',
-
-    # Parsing functions and string utilities
-    'parse_requirements', 'parse_version', 'safe_name', 'safe_version',
-    'get_platform', 'compatible_platforms', 'yield_lines', 'split_sections',
-    'safe_extra', 'to_filename', 'invalid_marker', 'evaluate_marker',
-
-    # filesystem utilities
-    'ensure_directory', 'normalize_path',
-
-    # Distribution "precedence" constants
-    'EGG_DIST', 'BINARY_DIST', 'SOURCE_DIST', 'CHECKOUT_DIST', 'DEVELOP_DIST',
-
-    # "Provider" interfaces, implementations, and registration/lookup APIs
-    'IMetadataProvider', 'IResourceProvider', 'FileMetadata',
-    'PathMetadata', 'EggMetadata', 'EmptyProvider', 'empty_provider',
-    'NullProvider', 'EggProvider', 'DefaultProvider', 'ZipProvider',
-    'register_finder', 'register_namespace_handler', 'register_loader_type',
-    'fixup_namespace_packages', 'get_importer',
-
-    # Warnings
-    'PkgResourcesDeprecationWarning',
-
-    # Deprecated/backward compatibility only
-    'run_main', 'AvailableDistributions',
-]
-
-
-class ResolutionError(Exception):
-    """Abstract base for dependency resolution errors"""
-
-    def __repr__(self):
-        return self.__class__.__name__ + repr(self.args)
-
-
-class VersionConflict(ResolutionError):
-    """
-    An already-installed version conflicts with the requested version.
-
-    Should be initialized with the installed Distribution and the requested
-    Requirement.
-    """
-
-    _template = "{self.dist} is installed but {self.req} is required"
-
-    @property
-    def dist(self):
-        return self.args[0]
-
-    @property
-    def req(self):
-        return self.args[1]
-
-    def report(self):
-        return self._template.format(**locals())
-
-    def with_context(self, required_by):
-        """
-        If required_by is non-empty, return a version of self that is a
-        ContextualVersionConflict.
-        """
-        if not required_by:
-            return self
-        args = self.args + (required_by,)
-        return ContextualVersionConflict(*args)
-
-
-class ContextualVersionConflict(VersionConflict):
-    """
-    A VersionConflict that accepts a third parameter, the set of the
-    requirements that required the installed Distribution.
-    """
-
-    _template = VersionConflict._template + ' by {self.required_by}'
-
-    @property
-    def required_by(self):
-        return self.args[2]
-
-
-class DistributionNotFound(ResolutionError):
-    """A requested distribution was not found"""
-
-    _template = ("The '{self.req}' distribution was not found "
-                 "and is required by {self.requirers_str}")
-
-    @property
-    def req(self):
-        return self.args[0]
-
-    @property
-    def requirers(self):
-        return self.args[1]
-
-    @property
-    def requirers_str(self):
-        if not self.requirers:
-            return 'the application'
-        return ', '.join(self.requirers)
-
-    def report(self):
-        return self._template.format(**locals())
-
-    def __str__(self):
-        return self.report()
-
-
-class UnknownExtra(ResolutionError):
-    """Distribution doesn't have an "extra feature" of the given name"""
-
-
-_provider_factories = {}
-
-PY_MAJOR = sys.version[:3]
-EGG_DIST = 3
-BINARY_DIST = 2
-SOURCE_DIST = 1
-CHECKOUT_DIST = 0
-DEVELOP_DIST = -1
-
-
-def register_loader_type(loader_type, provider_factory):
-    """Register `provider_factory` to make providers for `loader_type`
-
-    `loader_type` is the type or class of a PEP 302 ``module.__loader__``,
-    and `provider_factory` is a function that, passed a *module* object,
-    returns an ``IResourceProvider`` for that module.
-    """
-    _provider_factories[loader_type] = provider_factory
-
-
-def get_provider(moduleOrReq):
-    """Return an IResourceProvider for the named module or requirement"""
-    if isinstance(moduleOrReq, Requirement):
-        return working_set.find(moduleOrReq) or require(str(moduleOrReq))[0]
-    try:
-        module = sys.modules[moduleOrReq]
-    except KeyError:
-        __import__(moduleOrReq)
-        module = sys.modules[moduleOrReq]
-    loader = getattr(module, '__loader__', None)
-    return _find_adapter(_provider_factories, loader)(module)
-
-
-def _macosx_vers(_cache=[]):
-    if not _cache:
-        version = platform.mac_ver()[0]
-        # fallback for MacPorts
-        if version == '':
-            plist = '/System/Library/CoreServices/SystemVersion.plist'
-            if os.path.exists(plist):
-                if hasattr(plistlib, 'readPlist'):
-                    plist_content = plistlib.readPlist(plist)
-                    if 'ProductVersion' in plist_content:
-                        version = plist_content['ProductVersion']
-
-        _cache.append(version.split('.'))
-    return _cache[0]
-
-
-def _macosx_arch(machine):
-    return {'PowerPC': 'ppc', 'Power_Macintosh': 'ppc'}.get(machine, machine)
-
-
-def get_build_platform():
-    """Return this platform's string for platform-specific distributions
-
-    XXX Currently this is the same as ``distutils.util.get_platform()``, but it
-    needs some hacks for Linux and Mac OS X.
-    """
-    from sysconfig import get_platform
-
-    plat = get_platform()
-    if sys.platform == "darwin" and not plat.startswith('macosx-'):
-        try:
-            version = _macosx_vers()
-            machine = os.uname()[4].replace(" ", "_")
-            return "macosx-%d.%d-%s" % (
-                int(version[0]), int(version[1]),
-                _macosx_arch(machine),
-            )
-        except ValueError:
-            # if someone is running a non-Mac darwin system, this will fall
-            # through to the default implementation
-            pass
-    return plat
-
-
-macosVersionString = re.compile(r"macosx-(\d+)\.(\d+)-(.*)")
-darwinVersionString = re.compile(r"darwin-(\d+)\.(\d+)\.(\d+)-(.*)")
-# XXX backward compat
-get_platform = get_build_platform
-
-
-def compatible_platforms(provided, required):
-    """Can code for the `provided` platform run on the `required` platform?
-
-    Returns true if either platform is ``None``, or the platforms are equal.
-
-    XXX Needs compatibility checks for Linux and other unixy OSes.
-    """
-    if provided is None or required is None or provided == required:
-        # easy case
-        return True
-
-    # Mac OS X special cases
-    reqMac = macosVersionString.match(required)
-    if reqMac:
-        provMac = macosVersionString.match(provided)
-
-        # is this a Mac package?
-        if not provMac:
-            # this is backwards compatibility for packages built before
-            # setuptools 0.6. All packages built after this point will
-            # use the new macosx designation.
-            provDarwin = darwinVersionString.match(provided)
-            if provDarwin:
-                dversion = int(provDarwin.group(1))
-                macosversion = "%s.%s" % (reqMac.group(1), reqMac.group(2))
-                if dversion == 7 and macosversion >= "10.3" or \
-                        dversion == 8 and macosversion >= "10.4":
-                    return True
-            # egg isn't macosx or legacy darwin
-            return False
-
-        # are they the same major version and machine type?
-        if provMac.group(1) != reqMac.group(1) or \
-                provMac.group(3) != reqMac.group(3):
-            return False
-
-        # is the required OS major update >= the provided one?
-        if int(provMac.group(2)) > int(reqMac.group(2)):
-            return False
-
-        return True
-
-    # XXX Linux and other platforms' special cases should go here
-    return False
-
-
-def run_script(dist_spec, script_name):
-    """Locate distribution `dist_spec` and run its `script_name` script"""
-    ns = sys._getframe(1).f_globals
-    name = ns['__name__']
-    ns.clear()
-    ns['__name__'] = name
-    require(dist_spec)[0].run_script(script_name, ns)
-
-
-# backward compatibility
-run_main = run_script
-
-
-def get_distribution(dist):
-    """Return a current distribution object for a Requirement or string"""
-    if isinstance(dist, six.string_types):
-        dist = Requirement.parse(dist)
-    if isinstance(dist, Requirement):
-        dist = get_provider(dist)
-    if not isinstance(dist, Distribution):
-        raise TypeError("Expected string, Requirement, or Distribution", dist)
-    return dist
-
-
-def load_entry_point(dist, group, name):
-    """Return `name` entry point of `group` for `dist` or raise ImportError"""
-    return get_distribution(dist).load_entry_point(group, name)
-
-
-def get_entry_map(dist, group=None):
-    """Return the entry point map for `group`, or the full entry map"""
-    return get_distribution(dist).get_entry_map(group)
-
-
-def get_entry_info(dist, group, name):
-    """Return the EntryPoint object for `group`+`name`, or ``None``"""
-    return get_distribution(dist).get_entry_info(group, name)
-
-
-class IMetadataProvider:
-    def has_metadata(name):
-        """Does the package's distribution contain the named metadata?"""
-
-    def get_metadata(name):
-        """The named metadata resource as a string"""
-
-    def get_metadata_lines(name):
-        """Yield named metadata resource as list of non-blank non-comment lines
-
-       Leading and trailing whitespace is stripped from each line, and lines
-       with ``#`` as the first non-blank character are omitted."""
-
-    def metadata_isdir(name):
-        """Is the named metadata a directory?  (like ``os.path.isdir()``)"""
-
-    def metadata_listdir(name):
-        """List of metadata names in the directory (like ``os.listdir()``)"""
-
-    def run_script(script_name, namespace):
-        """Execute the named script in the supplied namespace dictionary"""
-
-
-class IResourceProvider(IMetadataProvider):
-    """An object that provides access to package resources"""
-
-    def get_resource_filename(manager, resource_name):
-        """Return a true filesystem path for `resource_name`
-
-        `manager` must be an ``IResourceManager``"""
-
-    def get_resource_stream(manager, resource_name):
-        """Return a readable file-like object for `resource_name`
-
-        `manager` must be an ``IResourceManager``"""
-
-    def get_resource_string(manager, resource_name):
-        """Return a string containing the contents of `resource_name`
-
-        `manager` must be an ``IResourceManager``"""
-
-    def has_resource(resource_name):
-        """Does the package contain the named resource?"""
-
-    def resource_isdir(resource_name):
-        """Is the named resource a directory?  (like ``os.path.isdir()``)"""
-
-    def resource_listdir(resource_name):
-        """List of resource names in the directory (like ``os.listdir()``)"""
-
-
-class WorkingSet:
-    """A collection of active distributions on sys.path (or a similar list)"""
-
-    def __init__(self, entries=None):
-        """Create working set from list of path entries (default=sys.path)"""
-        self.entries = []
-        self.entry_keys = {}
-        self.by_key = {}
-        self.callbacks = []
-
-        if entries is None:
-            entries = sys.path
-
-        for entry in entries:
-            self.add_entry(entry)
-
-    @classmethod
-    def _build_master(cls):
-        """
-        Prepare the master working set.
-        """
-        ws = cls()
-        try:
-            from __main__ import __requires__
-        except ImportError:
-            # The main program does not list any requirements
-            return ws
-
-        # ensure the requirements are met
-        try:
-            ws.require(__requires__)
-        except VersionConflict:
-            return cls._build_from_requirements(__requires__)
-
-        return ws
-
-    @classmethod
-    def _build_from_requirements(cls, req_spec):
-        """
-        Build a working set from a requirement spec. Rewrites sys.path.
-        """
-        # try it without defaults already on sys.path
-        # by starting with an empty path
-        ws = cls([])
-        reqs = parse_requirements(req_spec)
-        dists = ws.resolve(reqs, Environment())
-        for dist in dists:
-            ws.add(dist)
-
-        # add any missing entries from sys.path
-        for entry in sys.path:
-            if entry not in ws.entries:
-                ws.add_entry(entry)
-
-        # then copy back to sys.path
-        sys.path[:] = ws.entries
-        return ws
-
-    def add_entry(self, entry):
-        """Add a path item to ``.entries``, finding any distributions on it
-
-        ``find_distributions(entry, True)`` is used to find distributions
-        corresponding to the path entry, and they are added.  `entry` is
-        always appended to ``.entries``, even if it is already present.
-        (This is because ``sys.path`` can contain the same value more than
-        once, and the ``.entries`` of the ``sys.path`` WorkingSet should always
-        equal ``sys.path``.)
-        """
-        self.entry_keys.setdefault(entry, [])
-        self.entries.append(entry)
-        for dist in find_distributions(entry, True):
-            self.add(dist, entry, False)
-
-    def __contains__(self, dist):
-        """True if `dist` is the active distribution for its project"""
-        return self.by_key.get(dist.key) == dist
-
-    def find(self, req):
-        """Find a distribution matching requirement `req`
-
-        If there is an active distribution for the requested project, this
-        returns it as long as it meets the version requirement specified by
-        `req`.  But, if there is an active distribution for the project and it
-        does *not* meet the `req` requirement, ``VersionConflict`` is raised.
-        If there is no active distribution for the requested project, ``None``
-        is returned.
-        """
-        dist = self.by_key.get(req.key)
-        if dist is not None and dist not in req:
-            # XXX add more info
-            raise VersionConflict(dist, req)
-        return dist
-
-    def iter_entry_points(self, group, name=None):
-        """Yield entry point objects from `group` matching `name`
-
-        If `name` is None, yields all entry points in `group` from all
-        distributions in the working set, otherwise only ones matching
-        both `group` and `name` are yielded (in distribution order).
-        """
-        return (
-            entry
-            for dist in self
-            for entry in dist.get_entry_map(group).values()
-            if name is None or name == entry.name
-        )
-
-    def run_script(self, requires, script_name):
-        """Locate distribution for `requires` and run `script_name` script"""
-        ns = sys._getframe(1).f_globals
-        name = ns['__name__']
-        ns.clear()
-        ns['__name__'] = name
-        self.require(requires)[0].run_script(script_name, ns)
-
-    def __iter__(self):
-        """Yield distributions for non-duplicate projects in the working set
-
-        The yield order is the order in which the items' path entries were
-        added to the working set.
-        """
-        seen = {}
-        for item in self.entries:
-            if item not in self.entry_keys:
-                # workaround a cache issue
-                continue
-
-            for key in self.entry_keys[item]:
-                if key not in seen:
-                    seen[key] = 1
-                    yield self.by_key[key]
-
-    def add(self, dist, entry=None, insert=True, replace=False):
-        """Add `dist` to working set, associated with `entry`
-
-        If `entry` is unspecified, it defaults to the ``.location`` of `dist`.
-        On exit from this routine, `entry` is added to the end of the working
-        set's ``.entries`` (if it wasn't already present).
-
-        `dist` is only added to the working set if it's for a project that
-        doesn't already have a distribution in the set, unless `replace=True`.
-        If it's added, any callbacks registered with the ``subscribe()`` method
-        will be called.
-        """
-        if insert:
-            dist.insert_on(self.entries, entry, replace=replace)
-
-        if entry is None:
-            entry = dist.location
-        keys = self.entry_keys.setdefault(entry, [])
-        keys2 = self.entry_keys.setdefault(dist.location, [])
-        if not replace and dist.key in self.by_key:
-            # ignore hidden distros
-            return
-
-        self.by_key[dist.key] = dist
-        if dist.key not in keys:
-            keys.append(dist.key)
-        if dist.key not in keys2:
-            keys2.append(dist.key)
-        self._added_new(dist)
-
-    def resolve(self, requirements, env=None, installer=None,
-                replace_conflicting=False, extras=None):
-        """List all distributions needed to (recursively) meet `requirements`
-
-        `requirements` must be a sequence of ``Requirement`` objects.  `env`,
-        if supplied, should be an ``Environment`` instance.  If
-        not supplied, it defaults to all distributions available within any
-        entry or distribution in the working set.  `installer`, if supplied,
-        will be invoked with each requirement that cannot be met by an
-        already-installed distribution; it should return a ``Distribution`` or
-        ``None``.
-
-        Unless `replace_conflicting=True`, raises a VersionConflict exception
-        if
-        any requirements are found on the path that have the correct name but
-        the wrong version.  Otherwise, if an `installer` is supplied it will be
-        invoked to obtain the correct version of the requirement and activate
-        it.
-
-        `extras` is a list of the extras to be used with these requirements.
-        This is important because extra requirements may look like `my_req;
-        extra = "my_extra"`, which would otherwise be interpreted as a purely
-        optional requirement.  Instead, we want to be able to assert that these
-        requirements are truly required.
-        """
-
-        # set up the stack
-        requirements = list(requirements)[::-1]
-        # set of processed requirements
-        processed = {}
-        # key -> dist
-        best = {}
-        to_activate = []
-
-        req_extras = _ReqExtras()
-
-        # Mapping of requirement to set of distributions that required it;
-        # useful for reporting info about conflicts.
-        required_by = collections.defaultdict(set)
-
-        while requirements:
-            # process dependencies breadth-first
-            req = requirements.pop(0)
-            if req in processed:
-                # Ignore cyclic or redundant dependencies
-                continue
-
-            if not req_extras.markers_pass(req, extras):
-                continue
-
-            dist = best.get(req.key)
-            if dist is None:
-                # Find the best distribution and add it to the map
-                dist = self.by_key.get(req.key)
-                if dist is None or (dist not in req and replace_conflicting):
-                    ws = self
-                    if env is None:
-                        if dist is None:
-                            env = Environment(self.entries)
-                        else:
-                            # Use an empty environment and workingset to avoid
-                            # any further conflicts with the conflicting
-                            # distribution
-                            env = Environment([])
-                            ws = WorkingSet([])
-                    dist = best[req.key] = env.best_match(
-                        req, ws, installer,
-                        replace_conflicting=replace_conflicting
-                    )
-                    if dist is None:
-                        requirers = required_by.get(req, None)
-                        raise DistributionNotFound(req, requirers)
-                to_activate.append(dist)
-            if dist not in req:
-                # Oops, the "best" so far conflicts with a dependency
-                dependent_req = required_by[req]
-                raise VersionConflict(dist, req).with_context(dependent_req)
-
-            # push the new requirements onto the stack
-            new_requirements = dist.requires(req.extras)[::-1]
-            requirements.extend(new_requirements)
-
-            # Register the new requirements needed by req
-            for new_requirement in new_requirements:
-                required_by[new_requirement].add(req.project_name)
-                req_extras[new_requirement] = req.extras
-
-            processed[req] = True
-
-        # return list of distros to activate
-        return to_activate
-
-    def find_plugins(
-            self, plugin_env, full_env=None, installer=None, fallback=True):
-        """Find all activatable distributions in `plugin_env`
-
-        Example usage::
-
-            distributions, errors = working_set.find_plugins(
-                Environment(plugin_dirlist)
-            )
-            # add plugins+libs to sys.path
-            map(working_set.add, distributions)
-            # display errors
-            print('Could not load', errors)
-
-        The `plugin_env` should be an ``Environment`` instance that contains
-        only distributions that are in the project's "plugin directory" or
-        directories. The `full_env`, if supplied, should be an ``Environment``
-        contains all currently-available distributions.  If `full_env` is not
-        supplied, one is created automatically from the ``WorkingSet`` this
-        method is called on, which will typically mean that every directory on
-        ``sys.path`` will be scanned for distributions.
-
-        `installer` is a standard installer callback as used by the
-        ``resolve()`` method. The `fallback` flag indicates whether we should
-        attempt to resolve older versions of a plugin if the newest version
-        cannot be resolved.
-
-        This method returns a 2-tuple: (`distributions`, `error_info`), where
-        `distributions` is a list of the distributions found in `plugin_env`
-        that were loadable, along with any other distributions that are needed
-        to resolve their dependencies.  `error_info` is a dictionary mapping
-        unloadable plugin distributions to an exception instance describing the
-        error that occurred. Usually this will be a ``DistributionNotFound`` or
-        ``VersionConflict`` instance.
-        """
-
-        plugin_projects = list(plugin_env)
-        # scan project names in alphabetic order
-        plugin_projects.sort()
-
-        error_info = {}
-        distributions = {}
-
-        if full_env is None:
-            env = Environment(self.entries)
-            env += plugin_env
-        else:
-            env = full_env + plugin_env
-
-        shadow_set = self.__class__([])
-        # put all our entries in shadow_set
-        list(map(shadow_set.add, self))
-
-        for project_name in plugin_projects:
-
-            for dist in plugin_env[project_name]:
-
-                req = [dist.as_requirement()]
-
-                try:
-                    resolvees = shadow_set.resolve(req, env, installer)
-
-                except ResolutionError as v:
-                    # save error info
-                    error_info[dist] = v
-                    if fallback:
-                        # try the next older version of project
-                        continue
-                    else:
-                        # give up on this project, keep going
-                        break
-
-                else:
-                    list(map(shadow_set.add, resolvees))
-                    distributions.update(dict.fromkeys(resolvees))
-
-                    # success, no need to try any more versions of this project
-                    break
-
-        distributions = list(distributions)
-        distributions.sort()
-
-        return distributions, error_info
-
-    def require(self, *requirements):
-        """Ensure that distributions matching `requirements` are activated
-
-        `requirements` must be a string or a (possibly-nested) sequence
-        thereof, specifying the distributions and versions required.  The
-        return value is a sequence of the distributions that needed to be
-        activated to fulfill the requirements; all relevant distributions are
-        included, even if they were already activated in this working set.
-        """
-        needed = self.resolve(parse_requirements(requirements))
-
-        for dist in needed:
-            self.add(dist)
-
-        return needed
-
-    def subscribe(self, callback, existing=True):
-        """Invoke `callback` for all distributions
-
-        If `existing=True` (default),
-        call on all existing ones, as well.
-        """
-        if callback in self.callbacks:
-            return
-        self.callbacks.append(callback)
-        if not existing:
-            return
-        for dist in self:
-            callback(dist)
-
-    def _added_new(self, dist):
-        for callback in self.callbacks:
-            callback(dist)
-
-    def __getstate__(self):
-        return (
-            self.entries[:], self.entry_keys.copy(), self.by_key.copy(),
-            self.callbacks[:]
-        )
-
-    def __setstate__(self, e_k_b_c):
-        entries, keys, by_key, callbacks = e_k_b_c
-        self.entries = entries[:]
-        self.entry_keys = keys.copy()
-        self.by_key = by_key.copy()
-        self.callbacks = callbacks[:]
-
-
-class _ReqExtras(dict):
-    """
-    Map each requirement to the extras that demanded it.
-    """
-
-    def markers_pass(self, req, extras=None):
-        """
-        Evaluate markers for req against each extra that
-        demanded it.
-
-        Return False if the req has a marker and fails
-        evaluation. Otherwise, return True.
-        """
-        extra_evals = (
-            req.marker.evaluate({'extra': extra})
-            for extra in self.get(req, ()) + (extras or (None,))
-        )
-        return not req.marker or any(extra_evals)
-
-
-class Environment:
-    """Searchable snapshot of distributions on a search path"""
-
-    def __init__(
-            self, search_path=None, platform=get_supported_platform(),
-            python=PY_MAJOR):
-        """Snapshot distributions available on a search path
-
-        Any distributions found on `search_path` are added to the environment.
-        `search_path` should be a sequence of ``sys.path`` items.  If not
-        supplied, ``sys.path`` is used.
-
-        `platform` is an optional string specifying the name of the platform
-        that platform-specific distributions must be compatible with.  If
-        unspecified, it defaults to the current platform.  `python` is an
-        optional string naming the desired version of Python (e.g. ``'3.6'``);
-        it defaults to the current version.
-
-        You may explicitly set `platform` (and/or `python`) to ``None`` if you
-        wish to map *all* distributions, not just those compatible with the
-        running platform or Python version.
-        """
-        self._distmap = {}
-        self.platform = platform
-        self.python = python
-        self.scan(search_path)
-
-    def can_add(self, dist):
-        """Is distribution `dist` acceptable for this environment?
-
-        The distribution must match the platform and python version
-        requirements specified when this environment was created, or False
-        is returned.
-        """
-        py_compat = (
-            self.python is None
-            or dist.py_version is None
-            or dist.py_version == self.python
-        )
-        return py_compat and compatible_platforms(dist.platform, self.platform)
-
-    def remove(self, dist):
-        """Remove `dist` from the environment"""
-        self._distmap[dist.key].remove(dist)
-
-    def scan(self, search_path=None):
-        """Scan `search_path` for distributions usable in this environment
-
-        Any distributions found are added to the environment.
-        `search_path` should be a sequence of ``sys.path`` items.  If not
-        supplied, ``sys.path`` is used.  Only distributions conforming to
-        the platform/python version defined at initialization are added.
-        """
-        if search_path is None:
-            search_path = sys.path
-
-        for item in search_path:
-            for dist in find_distributions(item):
-                self.add(dist)
-
-    def __getitem__(self, project_name):
-        """Return a newest-to-oldest list of distributions for `project_name`
-
-        Uses case-insensitive `project_name` comparison, assuming all the
-        project's distributions use their project's name converted to all
-        lowercase as their key.
-
-        """
-        distribution_key = project_name.lower()
-        return self._distmap.get(distribution_key, [])
-
-    def add(self, dist):
-        """Add `dist` if we ``can_add()`` it and it has not already been added
-        """
-        if self.can_add(dist) and dist.has_version():
-            dists = self._distmap.setdefault(dist.key, [])
-            if dist not in dists:
-                dists.append(dist)
-                dists.sort(key=operator.attrgetter('hashcmp'), reverse=True)
-
-    def best_match(
-            self, req, working_set, installer=None, replace_conflicting=False):
-        """Find distribution best matching `req` and usable on `working_set`
-
-        This calls the ``find(req)`` method of the `working_set` to see if a
-        suitable distribution is already active.  (This may raise
-        ``VersionConflict`` if an unsuitable version of the project is already
-        active in the specified `working_set`.)  If a suitable distribution
-        isn't active, this method returns the newest distribution in the
-        environment that meets the ``Requirement`` in `req`.  If no suitable
-        distribution is found, and `installer` is supplied, then the result of
-        calling the environment's ``obtain(req, installer)`` method will be
-        returned.
-        """
-        try:
-            dist = working_set.find(req)
-        except VersionConflict:
-            if not replace_conflicting:
-                raise
-            dist = None
-        if dist is not None:
-            return dist
-        for dist in self[req.key]:
-            if dist in req:
-                return dist
-        # try to download/install
-        return self.obtain(req, installer)
-
-    def obtain(self, requirement, installer=None):
-        """Obtain a distribution matching `requirement` (e.g. via download)
-
-        Obtain a distro that matches requirement (e.g. via download).  In the
-        base ``Environment`` class, this routine just returns
-        ``installer(requirement)``, unless `installer` is None, in which case
-        None is returned instead.  This method is a hook that allows subclasses
-        to attempt other ways of obtaining a distribution before falling back
-        to the `installer` argument."""
-        if installer is not None:
-            return installer(requirement)
-
-    def __iter__(self):
-        """Yield the unique project names of the available distributions"""
-        for key in self._distmap.keys():
-            if self[key]:
-                yield key
-
-    def __iadd__(self, other):
-        """In-place addition of a distribution or environment"""
-        if isinstance(other, Distribution):
-            self.add(other)
-        elif isinstance(other, Environment):
-            for project in other:
-                for dist in other[project]:
-                    self.add(dist)
-        else:
-            raise TypeError("Can't add %r to environment" % (other,))
-        return self
-
-    def __add__(self, other):
-        """Add an environment or distribution to an environment"""
-        new = self.__class__([], platform=None, python=None)
-        for env in self, other:
-            new += env
-        return new
-
-
-# XXX backward compatibility
-AvailableDistributions = Environment
-
-
-class ExtractionError(RuntimeError):
-    """An error occurred extracting a resource
-
-    The following attributes are available from instances of this exception:
-
-    manager
-        The resource manager that raised this exception
-
-    cache_path
-        The base directory for resource extraction
-
-    original_error
-        The exception instance that caused extraction to fail
-    """
-
-
-class ResourceManager:
-    """Manage resource extraction and packages"""
-    extraction_path = None
-
-    def __init__(self):
-        self.cached_files = {}
-
-    def resource_exists(self, package_or_requirement, resource_name):
-        """Does the named resource exist?"""
-        return get_provider(package_or_requirement).has_resource(resource_name)
-
-    def resource_isdir(self, package_or_requirement, resource_name):
-        """Is the named resource an existing directory?"""
-        return get_provider(package_or_requirement).resource_isdir(
-            resource_name
-        )
-
-    def resource_filename(self, package_or_requirement, resource_name):
-        """Return a true filesystem path for specified resource"""
-        return get_provider(package_or_requirement).get_resource_filename(
-            self, resource_name
-        )
-
-    def resource_stream(self, package_or_requirement, resource_name):
-        """Return a readable file-like object for specified resource"""
-        return get_provider(package_or_requirement).get_resource_stream(
-            self, resource_name
-        )
-
-    def resource_string(self, package_or_requirement, resource_name):
-        """Return specified resource as a string"""
-        return get_provider(package_or_requirement).get_resource_string(
-            self, resource_name
-        )
-
-    def resource_listdir(self, package_or_requirement, resource_name):
-        """List the contents of the named resource directory"""
-        return get_provider(package_or_requirement).resource_listdir(
-            resource_name
-        )
-
-    def extraction_error(self):
-        """Give an error message for problems extracting file(s)"""
-
-        old_exc = sys.exc_info()[1]
-        cache_path = self.extraction_path or get_default_cache()
-
-        tmpl = textwrap.dedent("""
-            Can't extract file(s) to egg cache
-
-            The following error occurred while trying to extract file(s)
-            to the Python egg cache:
-
-              {old_exc}
-
-            The Python egg cache directory is currently set to:
-
-              {cache_path}
-
-            Perhaps your account does not have write access to this directory?
-            You can change the cache directory by setting the PYTHON_EGG_CACHE
-            environment variable to point to an accessible directory.
-            """).lstrip()
-        err = ExtractionError(tmpl.format(**locals()))
-        err.manager = self
-        err.cache_path = cache_path
-        err.original_error = old_exc
-        raise err
-
-    def get_cache_path(self, archive_name, names=()):
-        """Return absolute location in cache for `archive_name` and `names`
-
-        The parent directory of the resulting path will be created if it does
-        not already exist.  `archive_name` should be the base filename of the
-        enclosing egg (which may not be the name of the enclosing zipfile!),
-        including its ".egg" extension.  `names`, if provided, should be a
-        sequence of path name parts "under" the egg's extraction location.
-
-        This method should only be called by resource providers that need to
-        obtain an extraction location, and only for names they intend to
-        extract, as it tracks the generated names for possible cleanup later.
-        """
-        extract_path = self.extraction_path or get_default_cache()
-        target_path = os.path.join(extract_path, archive_name + '-tmp', *names)
-        try:
-            _bypass_ensure_directory(target_path)
-        except Exception:
-            self.extraction_error()
-
-        self._warn_unsafe_extraction_path(extract_path)
-
-        self.cached_files[target_path] = 1
-        return target_path
-
-    @staticmethod
-    def _warn_unsafe_extraction_path(path):
-        """
-        If the default extraction path is overridden and set to an insecure
-        location, such as /tmp, it opens up an opportunity for an attacker to
-        replace an extracted file with an unauthorized payload. Warn the user
-        if a known insecure location is used.
-
-        See Distribute #375 for more details.
-        """
-        if os.name == 'nt' and not path.startswith(os.environ['windir']):
-            # On Windows, permissions are generally restrictive by default
-            #  and temp directories are not writable by other users, so
-            #  bypass the warning.
-            return
-        mode = os.stat(path).st_mode
-        if mode & stat.S_IWOTH or mode & stat.S_IWGRP:
-            msg = (
-                "%s is writable by group/others and vulnerable to attack "
-                "when "
-                "used with get_resource_filename. Consider a more secure "
-                "location (set with .set_extraction_path or the "
-                "PYTHON_EGG_CACHE environment variable)." % path
-            )
-            warnings.warn(msg, UserWarning)
-
-    def postprocess(self, tempname, filename):
-        """Perform any platform-specific postprocessing of `tempname`
-
-        This is where Mac header rewrites should be done; other platforms don't
-        have anything special they should do.
-
-        Resource providers should call this method ONLY after successfully
-        extracting a compressed resource.  They must NOT call it on resources
-        that are already in the filesystem.
-
-        `tempname` is the current (temporary) name of the file, and `filename`
-        is the name it will be renamed to by the caller after this routine
-        returns.
-        """
-
-        if os.name == 'posix':
-            # Make the resource executable
-            mode = ((os.stat(tempname).st_mode) | 0o555) & 0o7777
-            os.chmod(tempname, mode)
-
-    def set_extraction_path(self, path):
-        """Set the base path where resources will be extracted to, if needed.
-
-        If you do not call this routine before any extractions take place, the
-        path defaults to the return value of ``get_default_cache()``.  (Which
-        is based on the ``PYTHON_EGG_CACHE`` environment variable, with various
-        platform-specific fallbacks.  See that routine's documentation for more
-        details.)
-
-        Resources are extracted to subdirectories of this path based upon
-        information given by the ``IResourceProvider``.  You may set this to a
-        temporary directory, but then you must call ``cleanup_resources()`` to
-        delete the extracted files when done.  There is no guarantee that
-        ``cleanup_resources()`` will be able to remove all extracted files.
-
-        (Note: you may not change the extraction path for a given resource
-        manager once resources have been extracted, unless you first call
-        ``cleanup_resources()``.)
-        """
-        if self.cached_files:
-            raise ValueError(
-                "Can't change extraction path, files already extracted"
-            )
-
-        self.extraction_path = path
-
-    def cleanup_resources(self, force=False):
-        """
-        Delete all extracted resource files and directories, returning a list
-        of the file and directory names that could not be successfully removed.
-        This function does not have any concurrency protection, so it should
-        generally only be called when the extraction path is a temporary
-        directory exclusive to a single process.  This method is not
-        automatically called; you must call it explicitly or register it as an
-        ``atexit`` function if you wish to ensure cleanup of a temporary
-        directory used for extractions.
-        """
-        # XXX
-
-
-def get_default_cache():
-    """
-    Return the ``PYTHON_EGG_CACHE`` environment variable
-    or a platform-relevant user cache dir for an app
-    named "Python-Eggs".
-    """
-    return (
-        os.environ.get('PYTHON_EGG_CACHE')
-        or appdirs.user_cache_dir(appname='Python-Eggs')
-    )
-
-
-def safe_name(name):
-    """Convert an arbitrary string to a standard distribution name
-
-    Any runs of non-alphanumeric/. characters are replaced with a single '-'.
-    """
-    return re.sub('[^A-Za-z0-9.]+', '-', name)
-
-
-def safe_version(version):
-    """
-    Convert an arbitrary string to a standard version string
-    """
-    try:
-        # normalize the version
-        return str(packaging.version.Version(version))
-    except packaging.version.InvalidVersion:
-        version = version.replace(' ', '.')
-        return re.sub('[^A-Za-z0-9.]+', '-', version)
-
-
-def safe_extra(extra):
-    """Convert an arbitrary string to a standard 'extra' name
-
-    Any runs of non-alphanumeric characters are replaced with a single '_',
-    and the result is always lowercased.
-    """
-    return re.sub('[^A-Za-z0-9.-]+', '_', extra).lower()
-
-
-def to_filename(name):
-    """Convert a project or version name to its filename-escaped form
-
-    Any '-' characters are currently replaced with '_'.
-    """
-    return name.replace('-', '_')
-
-
-def invalid_marker(text):
-    """
-    Validate text as a PEP 508 environment marker; return an exception
-    if invalid or False otherwise.
-    """
-    try:
-        evaluate_marker(text)
-    except SyntaxError as e:
-        e.filename = None
-        e.lineno = None
-        return e
-    return False
-
-
-def evaluate_marker(text, extra=None):
-    """
-    Evaluate a PEP 508 environment marker.
-    Return a boolean indicating the marker result in this environment.
-    Raise SyntaxError if marker is invalid.
-
-    This implementation uses the 'pyparsing' module.
-    """
-    try:
-        marker = packaging.markers.Marker(text)
-        return marker.evaluate()
-    except packaging.markers.InvalidMarker as e:
-        raise SyntaxError(e)
-
-
-class NullProvider:
-    """Try to implement resources and metadata for arbitrary PEP 302 loaders"""
-
-    egg_name = None
-    egg_info = None
-    loader = None
-
-    def __init__(self, module):
-        self.loader = getattr(module, '__loader__', None)
-        self.module_path = os.path.dirname(getattr(module, '__file__', ''))
-
-    def get_resource_filename(self, manager, resource_name):
-        return self._fn(self.module_path, resource_name)
-
-    def get_resource_stream(self, manager, resource_name):
-        return io.BytesIO(self.get_resource_string(manager, resource_name))
-
-    def get_resource_string(self, manager, resource_name):
-        return self._get(self._fn(self.module_path, resource_name))
-
-    def has_resource(self, resource_name):
-        return self._has(self._fn(self.module_path, resource_name))
-
-    def has_metadata(self, name):
-        return self.egg_info and self._has(self._fn(self.egg_info, name))
-
-    def get_metadata(self, name):
-        if not self.egg_info:
-            return ""
-        value = self._get(self._fn(self.egg_info, name))
-        return value.decode('utf-8') if six.PY3 else value
-
-    def get_metadata_lines(self, name):
-        return yield_lines(self.get_metadata(name))
-
-    def resource_isdir(self, resource_name):
-        return self._isdir(self._fn(self.module_path, resource_name))
-
-    def metadata_isdir(self, name):
-        return self.egg_info and self._isdir(self._fn(self.egg_info, name))
-
-    def resource_listdir(self, resource_name):
-        return self._listdir(self._fn(self.module_path, resource_name))
-
-    def metadata_listdir(self, name):
-        if self.egg_info:
-            return self._listdir(self._fn(self.egg_info, name))
-        return []
-
-    def run_script(self, script_name, namespace):
-        script = 'scripts/' + script_name
-        if not self.has_metadata(script):
-            raise ResolutionError(
-                "Script {script!r} not found in metadata at {self.egg_info!r}"
-                .format(**locals()),
-            )
-        script_text = self.get_metadata(script).replace('\r\n', '\n')
-        script_text = script_text.replace('\r', '\n')
-        script_filename = self._fn(self.egg_info, script)
-        namespace['__file__'] = script_filename
-        if os.path.exists(script_filename):
-            source = open(script_filename).read()
-            code = compile(source, script_filename, 'exec')
-            exec(code, namespace, namespace)
-        else:
-            from linecache import cache
-            cache[script_filename] = (
-                len(script_text), 0, script_text.split('\n'), script_filename
-            )
-            script_code = compile(script_text, script_filename, 'exec')
-            exec(script_code, namespace, namespace)
-
-    def _has(self, path):
-        raise NotImplementedError(
-            "Can't perform this operation for unregistered loader type"
-        )
-
-    def _isdir(self, path):
-        raise NotImplementedError(
-            "Can't perform this operation for unregistered loader type"
-        )
-
-    def _listdir(self, path):
-        raise NotImplementedError(
-            "Can't perform this operation for unregistered loader type"
-        )
-
-    def _fn(self, base, resource_name):
-        if resource_name:
-            return os.path.join(base, *resource_name.split('/'))
-        return base
-
-    def _get(self, path):
-        if hasattr(self.loader, 'get_data'):
-            return self.loader.get_data(path)
-        raise NotImplementedError(
-            "Can't perform this operation for loaders without 'get_data()'"
-        )
-
-
-register_loader_type(object, NullProvider)
-
-
-class EggProvider(NullProvider):
-    """Provider based on a virtual filesystem"""
-
-    def __init__(self, module):
-        NullProvider.__init__(self, module)
-        self._setup_prefix()
-
-    def _setup_prefix(self):
-        # we assume here that our metadata may be nested inside a "basket"
-        # of multiple eggs; that's why we use module_path instead of .archive
-        path = self.module_path
-        old = None
-        while path != old:
-            if _is_egg_path(path):
-                self.egg_name = os.path.basename(path)
-                self.egg_info = os.path.join(path, 'EGG-INFO')
-                self.egg_root = path
-                break
-            old = path
-            path, base = os.path.split(path)
-
-
-class DefaultProvider(EggProvider):
-    """Provides access to package resources in the filesystem"""
-
-    def _has(self, path):
-        return os.path.exists(path)
-
-    def _isdir(self, path):
-        return os.path.isdir(path)
-
-    def _listdir(self, path):
-        return os.listdir(path)
-
-    def get_resource_stream(self, manager, resource_name):
-        return open(self._fn(self.module_path, resource_name), 'rb')
-
-    def _get(self, path):
-        with open(path, 'rb') as stream:
-            return stream.read()
-
-    @classmethod
-    def _register(cls):
-        loader_names = 'SourceFileLoader', 'SourcelessFileLoader',
-        for name in loader_names:
-            loader_cls = getattr(importlib_machinery, name, type(None))
-            register_loader_type(loader_cls, cls)
-
-
-DefaultProvider._register()
-
-
-class EmptyProvider(NullProvider):
-    """Provider that returns nothing for all requests"""
-
-    module_path = None
-
-    _isdir = _has = lambda self, path: False
-
-    def _get(self, path):
-        return ''
-
-    def _listdir(self, path):
-        return []
-
-    def __init__(self):
-        pass
-
-
-empty_provider = EmptyProvider()
-
-
-class ZipManifests(dict):
-    """
-    zip manifest builder
-    """
-
-    @classmethod
-    def build(cls, path):
-        """
-        Build a dictionary similar to the zipimport directory
-        caches, except instead of tuples, store ZipInfo objects.
-
-        Use a platform-specific path separator (os.sep) for the path keys
-        for compatibility with pypy on Windows.
-        """
-        with zipfile.ZipFile(path) as zfile:
-            items = (
-                (
-                    name.replace('/', os.sep),
-                    zfile.getinfo(name),
-                )
-                for name in zfile.namelist()
-            )
-            return dict(items)
-
-    load = build
-
-
-class MemoizedZipManifests(ZipManifests):
-    """
-    Memoized zipfile manifests.
-    """
-    manifest_mod = collections.namedtuple('manifest_mod', 'manifest mtime')
-
-    def load(self, path):
-        """
-        Load a manifest at path or return a suitable manifest already loaded.
-        """
-        path = os.path.normpath(path)
-        mtime = os.stat(path).st_mtime
-
-        if path not in self or self[path].mtime != mtime:
-            manifest = self.build(path)
-            self[path] = self.manifest_mod(manifest, mtime)
-
-        return self[path].manifest
-
-
-class ZipProvider(EggProvider):
-    """Resource support for zips and eggs"""
-
-    eagers = None
-    _zip_manifests = MemoizedZipManifests()
-
-    def __init__(self, module):
-        EggProvider.__init__(self, module)
-        self.zip_pre = self.loader.archive + os.sep
-
-    def _zipinfo_name(self, fspath):
-        # Convert a virtual filename (full path to file) into a zipfile subpath
-        # usable with the zipimport directory cache for our target archive
-        fspath = fspath.rstrip(os.sep)
-        if fspath == self.loader.archive:
-            return ''
-        if fspath.startswith(self.zip_pre):
-            return fspath[len(self.zip_pre):]
-        raise AssertionError(
-            "%s is not a subpath of %s" % (fspath, self.zip_pre)
-        )
-
-    def _parts(self, zip_path):
-        # Convert a zipfile subpath into an egg-relative path part list.
-        # pseudo-fs path
-        fspath = self.zip_pre + zip_path
-        if fspath.startswith(self.egg_root + os.sep):
-            return fspath[len(self.egg_root) + 1:].split(os.sep)
-        raise AssertionError(
-            "%s is not a subpath of %s" % (fspath, self.egg_root)
-        )
-
-    @property
-    def zipinfo(self):
-        return self._zip_manifests.load(self.loader.archive)
-
-    def get_resource_filename(self, manager, resource_name):
-        if not self.egg_name:
-            raise NotImplementedError(
-                "resource_filename() only supported for .egg, not .zip"
-            )
-        # no need to lock for extraction, since we use temp names
-        zip_path = self._resource_to_zip(resource_name)
-        eagers = self._get_eager_resources()
-        if '/'.join(self._parts(zip_path)) in eagers:
-            for name in eagers:
-                self._extract_resource(manager, self._eager_to_zip(name))
-        return self._extract_resource(manager, zip_path)
-
-    @staticmethod
-    def _get_date_and_size(zip_stat):
-        size = zip_stat.file_size
-        # ymdhms+wday, yday, dst
-        date_time = zip_stat.date_time + (0, 0, -1)
-        # 1980 offset already done
-        timestamp = time.mktime(date_time)
-        return timestamp, size
-
-    def _extract_resource(self, manager, zip_path):
-
-        if zip_path in self._index():
-            for name in self._index()[zip_path]:
-                last = self._extract_resource(
-                    manager, os.path.join(zip_path, name)
-                )
-            # return the extracted directory name
-            return os.path.dirname(last)
-
-        timestamp, size = self._get_date_and_size(self.zipinfo[zip_path])
-
-        if not WRITE_SUPPORT:
-            raise IOError('"os.rename" and "os.unlink" are not supported '
-                          'on this platform')
-        try:
-
-            real_path = manager.get_cache_path(
-                self.egg_name, self._parts(zip_path)
-            )
-
-            if self._is_current(real_path, zip_path):
-                return real_path
-
-            outf, tmpnam = _mkstemp(
-                ".$extract",
-                dir=os.path.dirname(real_path),
-            )
-            os.write(outf, self.loader.get_data(zip_path))
-            os.close(outf)
-            utime(tmpnam, (timestamp, timestamp))
-            manager.postprocess(tmpnam, real_path)
-
-            try:
-                rename(tmpnam, real_path)
-
-            except os.error:
-                if os.path.isfile(real_path):
-                    if self._is_current(real_path, zip_path):
-                        # the file became current since it was checked above,
-                        #  so proceed.
-                        return real_path
-                    # Windows, del old file and retry
-                    elif os.name == 'nt':
-                        unlink(real_path)
-                        rename(tmpnam, real_path)
-                        return real_path
-                raise
-
-        except os.error:
-            # report a user-friendly error
-            manager.extraction_error()
-
-        return real_path
-
-    def _is_current(self, file_path, zip_path):
-        """
-        Return True if the file_path is current for this zip_path
-        """
-        timestamp, size = self._get_date_and_size(self.zipinfo[zip_path])
-        if not os.path.isfile(file_path):
-            return False
-        stat = os.stat(file_path)
-        if stat.st_size != size or stat.st_mtime != timestamp:
-            return False
-        # check that the contents match
-        zip_contents = self.loader.get_data(zip_path)
-        with open(file_path, 'rb') as f:
-            file_contents = f.read()
-        return zip_contents == file_contents
-
-    def _get_eager_resources(self):
-        if self.eagers is None:
-            eagers = []
-            for name in ('native_libs.txt', 'eager_resources.txt'):
-                if self.has_metadata(name):
-                    eagers.extend(self.get_metadata_lines(name))
-            self.eagers = eagers
-        return self.eagers
-
-    def _index(self):
-        try:
-            return self._dirindex
-        except AttributeError:
-            ind = {}
-            for path in self.zipinfo:
-                parts = path.split(os.sep)
-                while parts:
-                    parent = os.sep.join(parts[:-1])
-                    if parent in ind:
-                        ind[parent].append(parts[-1])
-                        break
-                    else:
-                        ind[parent] = [parts.pop()]
-            self._dirindex = ind
-            return ind
-
-    def _has(self, fspath):
-        zip_path = self._zipinfo_name(fspath)
-        return zip_path in self.zipinfo or zip_path in self._index()
-
-    def _isdir(self, fspath):
-        return self._zipinfo_name(fspath) in self._index()
-
-    def _listdir(self, fspath):
-        return list(self._index().get(self._zipinfo_name(fspath), ()))
-
-    def _eager_to_zip(self, resource_name):
-        return self._zipinfo_name(self._fn(self.egg_root, resource_name))
-
-    def _resource_to_zip(self, resource_name):
-        return self._zipinfo_name(self._fn(self.module_path, resource_name))
-
-
-register_loader_type(zipimport.zipimporter, ZipProvider)
-
-
-class FileMetadata(EmptyProvider):
-    """Metadata handler for standalone PKG-INFO files
-
-    Usage::
-
-        metadata = FileMetadata("/path/to/PKG-INFO")
-
-    This provider rejects all data and metadata requests except for PKG-INFO,
-    which is treated as existing, and will be the contents of the file at
-    the provided location.
-    """
-
-    def __init__(self, path):
-        self.path = path
-
-    def has_metadata(self, name):
-        return name == 'PKG-INFO' and os.path.isfile(self.path)
-
-    def get_metadata(self, name):
-        if name != 'PKG-INFO':
-            raise KeyError("No metadata except PKG-INFO is available")
-
-        with io.open(self.path, encoding='utf-8', errors="replace") as f:
-            metadata = f.read()
-        self._warn_on_replacement(metadata)
-        return metadata
-
-    def _warn_on_replacement(self, metadata):
-        # Python 2.7 compat for: replacement_char = '�'
-        replacement_char = b'\xef\xbf\xbd'.decode('utf-8')
-        if replacement_char in metadata:
-            tmpl = "{self.path} could not be properly decoded in UTF-8"
-            msg = tmpl.format(**locals())
-            warnings.warn(msg)
-
-    def get_metadata_lines(self, name):
-        return yield_lines(self.get_metadata(name))
-
-
-class PathMetadata(DefaultProvider):
-    """Metadata provider for egg directories
-
-    Usage::
-
-        # Development eggs:
-
-        egg_info = "/path/to/PackageName.egg-info"
-        base_dir = os.path.dirname(egg_info)
-        metadata = PathMetadata(base_dir, egg_info)
-        dist_name = os.path.splitext(os.path.basename(egg_info))[0]
-        dist = Distribution(basedir, project_name=dist_name, metadata=metadata)
-
-        # Unpacked egg directories:
-
-        egg_path = "/path/to/PackageName-ver-pyver-etc.egg"
-        metadata = PathMetadata(egg_path, os.path.join(egg_path,'EGG-INFO'))
-        dist = Distribution.from_filename(egg_path, metadata=metadata)
-    """
-
-    def __init__(self, path, egg_info):
-        self.module_path = path
-        self.egg_info = egg_info
-
-
-class EggMetadata(ZipProvider):
-    """Metadata provider for .egg files"""
-
-    def __init__(self, importer):
-        """Create a metadata provider from a zipimporter"""
-
-        self.zip_pre = importer.archive + os.sep
-        self.loader = importer
-        if importer.prefix:
-            self.module_path = os.path.join(importer.archive, importer.prefix)
-        else:
-            self.module_path = importer.archive
-        self._setup_prefix()
-
-
-_declare_state('dict', _distribution_finders={})
-
-
-def register_finder(importer_type, distribution_finder):
-    """Register `distribution_finder` to find distributions in sys.path items
-
-    `importer_type` is the type or class of a PEP 302 "Importer" (sys.path item
-    handler), and `distribution_finder` is a callable that, passed a path
-    item and the importer instance, yields ``Distribution`` instances found on
-    that path item.  See ``pkg_resources.find_on_path`` for an example."""
-    _distribution_finders[importer_type] = distribution_finder
-
-
-def find_distributions(path_item, only=False):
-    """Yield distributions accessible via `path_item`"""
-    importer = get_importer(path_item)
-    finder = _find_adapter(_distribution_finders, importer)
-    return finder(importer, path_item, only)
-
-
-def find_eggs_in_zip(importer, path_item, only=False):
-    """
-    Find eggs in zip files; possibly multiple nested eggs.
-    """
-    if importer.archive.endswith('.whl'):
-        # wheels are not supported with this finder
-        # they don't have PKG-INFO metadata, and won't ever contain eggs
-        return
-    metadata = EggMetadata(importer)
-    if metadata.has_metadata('PKG-INFO'):
-        yield Distribution.from_filename(path_item, metadata=metadata)
-    if only:
-        # don't yield nested distros
-        return
-    for subitem in metadata.resource_listdir('/'):
-        if _is_egg_path(subitem):
-            subpath = os.path.join(path_item, subitem)
-            dists = find_eggs_in_zip(zipimport.zipimporter(subpath), subpath)
-            for dist in dists:
-                yield dist
-        elif subitem.lower().endswith('.dist-info'):
-            subpath = os.path.join(path_item, subitem)
-            submeta = EggMetadata(zipimport.zipimporter(subpath))
-            submeta.egg_info = subpath
-            yield Distribution.from_location(path_item, subitem, submeta)
-
-
-register_finder(zipimport.zipimporter, find_eggs_in_zip)
-
-
-def find_nothing(importer, path_item, only=False):
-    return ()
-
-
-register_finder(object, find_nothing)
-
-
-def _by_version_descending(names):
-    """
-    Given a list of filenames, return them in descending order
-    by version number.
-
-    >>> names = 'bar', 'foo', 'Python-2.7.10.egg', 'Python-2.7.2.egg'
-    >>> _by_version_descending(names)
-    ['Python-2.7.10.egg', 'Python-2.7.2.egg', 'foo', 'bar']
-    >>> names = 'Setuptools-1.2.3b1.egg', 'Setuptools-1.2.3.egg'
-    >>> _by_version_descending(names)
-    ['Setuptools-1.2.3.egg', 'Setuptools-1.2.3b1.egg']
-    >>> names = 'Setuptools-1.2.3b1.egg', 'Setuptools-1.2.3.post1.egg'
-    >>> _by_version_descending(names)
-    ['Setuptools-1.2.3.post1.egg', 'Setuptools-1.2.3b1.egg']
-    """
-    def _by_version(name):
-        """
-        Parse each component of the filename
-        """
-        name, ext = os.path.splitext(name)
-        parts = itertools.chain(name.split('-'), [ext])
-        return [packaging.version.parse(part) for part in parts]
-
-    return sorted(names, key=_by_version, reverse=True)
-
-
-def find_on_path(importer, path_item, only=False):
-    """Yield distributions accessible on a sys.path directory"""
-    path_item = _normalize_cached(path_item)
-
-    if _is_unpacked_egg(path_item):
-        yield Distribution.from_filename(
-            path_item, metadata=PathMetadata(
-                path_item, os.path.join(path_item, 'EGG-INFO')
-            )
-        )
-        return
-
-    entries = safe_listdir(path_item)
-
-    # for performance, before sorting by version,
-    # screen entries for only those that will yield
-    # distributions
-    filtered = (
-        entry
-        for entry in entries
-        if dist_factory(path_item, entry, only)
-    )
-
-    # scan for .egg and .egg-info in directory
-    path_item_entries = _by_version_descending(filtered)
-    for entry in path_item_entries:
-        fullpath = os.path.join(path_item, entry)
-        factory = dist_factory(path_item, entry, only)
-        for dist in factory(fullpath):
-            yield dist
-
-
-def dist_factory(path_item, entry, only):
-    """
-    Return a dist_factory for a path_item and entry
-    """
-    lower = entry.lower()
-    is_meta = any(map(lower.endswith, ('.egg-info', '.dist-info')))
-    return (
-        distributions_from_metadata
-        if is_meta else
-        find_distributions
-        if not only and _is_egg_path(entry) else
-        resolve_egg_link
-        if not only and lower.endswith('.egg-link') else
-        NoDists()
-    )
-
-
-class NoDists:
-    """
-    >>> bool(NoDists())
-    False
-
-    >>> list(NoDists()('anything'))
-    []
-    """
-    def __bool__(self):
-        return False
-    if six.PY2:
-        __nonzero__ = __bool__
-
-    def __call__(self, fullpath):
-        return iter(())
-
-
-def safe_listdir(path):
-    """
-    Attempt to list contents of path, but suppress some exceptions.
-    """
-    try:
-        return os.listdir(path)
-    except (PermissionError, NotADirectoryError):
-        pass
-    except OSError as e:
-        # Ignore the directory if does not exist, not a directory or
-        # permission denied
-        ignorable = (
-            e.errno in (errno.ENOTDIR, errno.EACCES, errno.ENOENT)
-            # Python 2 on Windows needs to be handled this way :(
-            or getattr(e, "winerror", None) == 267
-        )
-        if not ignorable:
-            raise
-    return ()
-
-
-def distributions_from_metadata(path):
-    root = os.path.dirname(path)
-    if os.path.isdir(path):
-        if len(os.listdir(path)) == 0:
-            # empty metadata dir; skip
-            return
-        metadata = PathMetadata(root, path)
-    else:
-        metadata = FileMetadata(path)
-    entry = os.path.basename(path)
-    yield Distribution.from_location(
-        root, entry, metadata, precedence=DEVELOP_DIST,
-    )
-
-
-def non_empty_lines(path):
-    """
-    Yield non-empty lines from file at path
-    """
-    with open(path) as f:
-        for line in f:
-            line = line.strip()
-            if line:
-                yield line
-
-
-def resolve_egg_link(path):
-    """
-    Given a path to an .egg-link, resolve distributions
-    present in the referenced path.
-    """
-    referenced_paths = non_empty_lines(path)
-    resolved_paths = (
-        os.path.join(os.path.dirname(path), ref)
-        for ref in referenced_paths
-    )
-    dist_groups = map(find_distributions, resolved_paths)
-    return next(dist_groups, ())
-
-
-register_finder(pkgutil.ImpImporter, find_on_path)
-
-if hasattr(importlib_machinery, 'FileFinder'):
-    register_finder(importlib_machinery.FileFinder, find_on_path)
-
-_declare_state('dict', _namespace_handlers={})
-_declare_state('dict', _namespace_packages={})
-
-
-def register_namespace_handler(importer_type, namespace_handler):
-    """Register `namespace_handler` to declare namespace packages
-
-    `importer_type` is the type or class of a PEP 302 "Importer" (sys.path item
-    handler), and `namespace_handler` is a callable like this::
-
-        def namespace_handler(importer, path_entry, moduleName, module):
-            # return a path_entry to use for child packages
-
-    Namespace handlers are only called if the importer object has already
-    agreed that it can handle the relevant path item, and they should only
-    return a subpath if the module __path__ does not already contain an
-    equivalent subpath.  For an example namespace handler, see
-    ``pkg_resources.file_ns_handler``.
-    """
-    _namespace_handlers[importer_type] = namespace_handler
-
-
-def _handle_ns(packageName, path_item):
-    """Ensure that named package includes a subpath of path_item (if needed)"""
-
-    importer = get_importer(path_item)
-    if importer is None:
-        return None
-
-    # capture warnings due to #1111
-    with warnings.catch_warnings():
-        warnings.simplefilter("ignore")
-        loader = importer.find_module(packageName)
-
-    if loader is None:
-        return None
-    module = sys.modules.get(packageName)
-    if module is None:
-        module = sys.modules[packageName] = types.ModuleType(packageName)
-        module.__path__ = []
-        _set_parent_ns(packageName)
-    elif not hasattr(module, '__path__'):
-        raise TypeError("Not a package:", packageName)
-    handler = _find_adapter(_namespace_handlers, importer)
-    subpath = handler(importer, path_item, packageName, module)
-    if subpath is not None:
-        path = module.__path__
-        path.append(subpath)
-        loader.load_module(packageName)
-        _rebuild_mod_path(path, packageName, module)
-    return subpath
-
-
-def _rebuild_mod_path(orig_path, package_name, module):
-    """
-    Rebuild module.__path__ ensuring that all entries are ordered
-    corresponding to their sys.path order
-    """
-    sys_path = [_normalize_cached(p) for p in sys.path]
-
-    def safe_sys_path_index(entry):
-        """
-        Workaround for #520 and #513.
-        """
-        try:
-            return sys_path.index(entry)
-        except ValueError:
-            return float('inf')
-
-    def position_in_sys_path(path):
-        """
-        Return the ordinal of the path based on its position in sys.path
-        """
-        path_parts = path.split(os.sep)
-        module_parts = package_name.count('.') + 1
-        parts = path_parts[:-module_parts]
-        return safe_sys_path_index(_normalize_cached(os.sep.join(parts)))
-
-    new_path = sorted(orig_path, key=position_in_sys_path)
-    new_path = [_normalize_cached(p) for p in new_path]
-
-    if isinstance(module.__path__, list):
-        module.__path__[:] = new_path
-    else:
-        module.__path__ = new_path
-
-
-def declare_namespace(packageName):
-    """Declare that package 'packageName' is a namespace package"""
-
-    _imp.acquire_lock()
-    try:
-        if packageName in _namespace_packages:
-            return
-
-        path = sys.path
-        parent, _, _ = packageName.rpartition('.')
-
-        if parent:
-            declare_namespace(parent)
-            if parent not in _namespace_packages:
-                __import__(parent)
-            try:
-                path = sys.modules[parent].__path__
-            except AttributeError:
-                raise TypeError("Not a package:", parent)
-
-        # Track what packages are namespaces, so when new path items are added,
-        # they can be updated
-        _namespace_packages.setdefault(parent or None, []).append(packageName)
-        _namespace_packages.setdefault(packageName, [])
-
-        for path_item in path:
-            # Ensure all the parent's path items are reflected in the child,
-            # if they apply
-            _handle_ns(packageName, path_item)
-
-    finally:
-        _imp.release_lock()
-
-
-def fixup_namespace_packages(path_item, parent=None):
-    """Ensure that previously-declared namespace packages include path_item"""
-    _imp.acquire_lock()
-    try:
-        for package in _namespace_packages.get(parent, ()):
-            subpath = _handle_ns(package, path_item)
-            if subpath:
-                fixup_namespace_packages(subpath, package)
-    finally:
-        _imp.release_lock()
-
-
-def file_ns_handler(importer, path_item, packageName, module):
-    """Compute an ns-package subpath for a filesystem or zipfile importer"""
-
-    subpath = os.path.join(path_item, packageName.split('.')[-1])
-    normalized = _normalize_cached(subpath)
-    for item in module.__path__:
-        if _normalize_cached(item) == normalized:
-            break
-    else:
-        # Only return the path if it's not already there
-        return subpath
-
-
-register_namespace_handler(pkgutil.ImpImporter, file_ns_handler)
-register_namespace_handler(zipimport.zipimporter, file_ns_handler)
-
-if hasattr(importlib_machinery, 'FileFinder'):
-    register_namespace_handler(importlib_machinery.FileFinder, file_ns_handler)
-
-
-def null_ns_handler(importer, path_item, packageName, module):
-    return None
-
-
-register_namespace_handler(object, null_ns_handler)
-
-
-def normalize_path(filename):
-    """Normalize a file/dir name for comparison purposes"""
-    return os.path.normcase(os.path.realpath(os.path.normpath(_cygwin_patch(filename))))
-
-
-def _cygwin_patch(filename):  # pragma: nocover
-    """
-    Contrary to POSIX 2008, on Cygwin, getcwd (3) contains
-    symlink components. Using
-    os.path.abspath() works around this limitation. A fix in os.getcwd()
-    would probably better, in Cygwin even more so, except
-    that this seems to be by design...
-    """
-    return os.path.abspath(filename) if sys.platform == 'cygwin' else filename
-
-
-def _normalize_cached(filename, _cache={}):
-    try:
-        return _cache[filename]
-    except KeyError:
-        _cache[filename] = result = normalize_path(filename)
-        return result
-
-
-def _is_egg_path(path):
-    """
-    Determine if given path appears to be an egg.
-    """
-    return path.lower().endswith('.egg')
-
-
-def _is_unpacked_egg(path):
-    """
-    Determine if given path appears to be an unpacked egg.
-    """
-    return (
-        _is_egg_path(path) and
-        os.path.isfile(os.path.join(path, 'EGG-INFO', 'PKG-INFO'))
-    )
-
-
-def _set_parent_ns(packageName):
-    parts = packageName.split('.')
-    name = parts.pop()
-    if parts:
-        parent = '.'.join(parts)
-        setattr(sys.modules[parent], name, sys.modules[packageName])
-
-
-def yield_lines(strs):
-    """Yield non-empty/non-comment lines of a string or sequence"""
-    if isinstance(strs, six.string_types):
-        for s in strs.splitlines():
-            s = s.strip()
-            # skip blank lines/comments
-            if s and not s.startswith('#'):
-                yield s
-    else:
-        for ss in strs:
-            for s in yield_lines(ss):
-                yield s
-
-
-MODULE = re.compile(r"\w+(\.\w+)*$").match
-EGG_NAME = re.compile(
-    r"""
-    (?P<name>[^-]+) (
-        -(?P<ver>[^-]+) (
-            -py(?P<pyver>[^-]+) (
-                -(?P<plat>.+)
-            )?
-        )?
-    )?
-    """,
-    re.VERBOSE | re.IGNORECASE,
-).match
-
-
-class EntryPoint:
-    """Object representing an advertised importable object"""
-
-    def __init__(self, name, module_name, attrs=(), extras=(), dist=None):
-        if not MODULE(module_name):
-            raise ValueError("Invalid module name", module_name)
-        self.name = name
-        self.module_name = module_name
-        self.attrs = tuple(attrs)
-        self.extras = tuple(extras)
-        self.dist = dist
-
-    def __str__(self):
-        s = "%s = %s" % (self.name, self.module_name)
-        if self.attrs:
-            s += ':' + '.'.join(self.attrs)
-        if self.extras:
-            s += ' [%s]' % ','.join(self.extras)
-        return s
-
-    def __repr__(self):
-        return "EntryPoint.parse(%r)" % str(self)
-
-    def load(self, require=True, *args, **kwargs):
-        """
-        Require packages for this EntryPoint, then resolve it.
-        """
-        if not require or args or kwargs:
-            warnings.warn(
-                "Parameters to load are deprecated.  Call .resolve and "
-                ".require separately.",
-                PkgResourcesDeprecationWarning,
-                stacklevel=2,
-            )
-        if require:
-            self.require(*args, **kwargs)
-        return self.resolve()
-
-    def resolve(self):
-        """
-        Resolve the entry point from its module and attrs.
-        """
-        module = __import__(self.module_name, fromlist=['__name__'], level=0)
-        try:
-            return functools.reduce(getattr, self.attrs, module)
-        except AttributeError as exc:
-            raise ImportError(str(exc))
-
-    def require(self, env=None, installer=None):
-        if self.extras and not self.dist:
-            raise UnknownExtra("Can't require() without a distribution", self)
-
-        # Get the requirements for this entry point with all its extras and
-        # then resolve them. We have to pass `extras` along when resolving so
-        # that the working set knows what extras we want. Otherwise, for
-        # dist-info distributions, the working set will assume that the
-        # requirements for that extra are purely optional and skip over them.
-        reqs = self.dist.requires(self.extras)
-        items = working_set.resolve(reqs, env, installer, extras=self.extras)
-        list(map(working_set.add, items))
-
-    pattern = re.compile(
-        r'\s*'
-        r'(?P<name>.+?)\s*'
-        r'=\s*'
-        r'(?P<module>[\w.]+)\s*'
-        r'(:\s*(?P<attr>[\w.]+))?\s*'
-        r'(?P<extras>\[.*\])?\s*$'
-    )
-
-    @classmethod
-    def parse(cls, src, dist=None):
-        """Parse a single entry point from string `src`
-
-        Entry point syntax follows the form::
-
-            name = some.module:some.attr [extra1, extra2]
-
-        The entry name and module name are required, but the ``:attrs`` and
-        ``[extras]`` parts are optional
-        """
-        m = cls.pattern.match(src)
-        if not m:
-            msg = "EntryPoint must be in 'name=module:attrs [extras]' format"
-            raise ValueError(msg, src)
-        res = m.groupdict()
-        extras = cls._parse_extras(res['extras'])
-        attrs = res['attr'].split('.') if res['attr'] else ()
-        return cls(res['name'], res['module'], attrs, extras, dist)
-
-    @classmethod
-    def _parse_extras(cls, extras_spec):
-        if not extras_spec:
-            return ()
-        req = Requirement.parse('x' + extras_spec)
-        if req.specs:
-            raise ValueError()
-        return req.extras
-
-    @classmethod
-    def parse_group(cls, group, lines, dist=None):
-        """Parse an entry point group"""
-        if not MODULE(group):
-            raise ValueError("Invalid group name", group)
-        this = {}
-        for line in yield_lines(lines):
-            ep = cls.parse(line, dist)
-            if ep.name in this:
-                raise ValueError("Duplicate entry point", group, ep.name)
-            this[ep.name] = ep
-        return this
-
-    @classmethod
-    def parse_map(cls, data, dist=None):
-        """Parse a map of entry point groups"""
-        if isinstance(data, dict):
-            data = data.items()
-        else:
-            data = split_sections(data)
-        maps = {}
-        for group, lines in data:
-            if group is None:
-                if not lines:
-                    continue
-                raise ValueError("Entry points must be listed in groups")
-            group = group.strip()
-            if group in maps:
-                raise ValueError("Duplicate group name", group)
-            maps[group] = cls.parse_group(group, lines, dist)
-        return maps
-
-
-def _remove_md5_fragment(location):
-    if not location:
-        return ''
-    parsed = urllib.parse.urlparse(location)
-    if parsed[-1].startswith('md5='):
-        return urllib.parse.urlunparse(parsed[:-1] + ('',))
-    return location
-
-
-def _version_from_file(lines):
-    """
-    Given an iterable of lines from a Metadata file, return
-    the value of the Version field, if present, or None otherwise.
-    """
-    def is_version_line(line):
-        return line.lower().startswith('version:')
-    version_lines = filter(is_version_line, lines)
-    line = next(iter(version_lines), '')
-    _, _, value = line.partition(':')
-    return safe_version(value.strip()) or None
-
-
-class Distribution:
-    """Wrap an actual or potential sys.path entry w/metadata"""
-    PKG_INFO = 'PKG-INFO'
-
-    def __init__(
-            self, location=None, metadata=None, project_name=None,
-            version=None, py_version=PY_MAJOR, platform=None,
-            precedence=EGG_DIST):
-        self.project_name = safe_name(project_name or 'Unknown')
-        if version is not None:
-            self._version = safe_version(version)
-        self.py_version = py_version
-        self.platform = platform
-        self.location = location
-        self.precedence = precedence
-        self._provider = metadata or empty_provider
-
-    @classmethod
-    def from_location(cls, location, basename, metadata=None, **kw):
-        project_name, version, py_version, platform = [None] * 4
-        basename, ext = os.path.splitext(basename)
-        if ext.lower() in _distributionImpl:
-            cls = _distributionImpl[ext.lower()]
-
-            match = EGG_NAME(basename)
-            if match:
-                project_name, version, py_version, platform = match.group(
-                    'name', 'ver', 'pyver', 'plat'
-                )
-        return cls(
-            location, metadata, project_name=project_name, version=version,
-            py_version=py_version, platform=platform, **kw
-        )._reload_version()
-
-    def _reload_version(self):
-        return self
-
-    @property
-    def hashcmp(self):
-        return (
-            self.parsed_version,
-            self.precedence,
-            self.key,
-            _remove_md5_fragment(self.location),
-            self.py_version or '',
-            self.platform or '',
-        )
-
-    def __hash__(self):
-        return hash(self.hashcmp)
-
-    def __lt__(self, other):
-        return self.hashcmp < other.hashcmp
-
-    def __le__(self, other):
-        return self.hashcmp <= other.hashcmp
-
-    def __gt__(self, other):
-        return self.hashcmp > other.hashcmp
-
-    def __ge__(self, other):
-        return self.hashcmp >= other.hashcmp
-
-    def __eq__(self, other):
-        if not isinstance(other, self.__class__):
-            # It's not a Distribution, so they are not equal
-            return False
-        return self.hashcmp == other.hashcmp
-
-    def __ne__(self, other):
-        return not self == other
-
-    # These properties have to be lazy so that we don't have to load any
-    # metadata until/unless it's actually needed.  (i.e., some distributions
-    # may not know their name or version without loading PKG-INFO)
-
-    @property
-    def key(self):
-        try:
-            return self._key
-        except AttributeError:
-            self._key = key = self.project_name.lower()
-            return key
-
-    @property
-    def parsed_version(self):
-        if not hasattr(self, "_parsed_version"):
-            self._parsed_version = parse_version(self.version)
-
-        return self._parsed_version
-
-    def _warn_legacy_version(self):
-        LV = packaging.version.LegacyVersion
-        is_legacy = isinstance(self._parsed_version, LV)
-        if not is_legacy:
-            return
-
-        # While an empty version is technically a legacy version and
-        # is not a valid PEP 440 version, it's also unlikely to
-        # actually come from someone and instead it is more likely that
-        # it comes from setuptools attempting to parse a filename and
-        # including it in the list. So for that we'll gate this warning
-        # on if the version is anything at all or not.
-        if not self.version:
-            return
-
-        tmpl = textwrap.dedent("""
-            '{project_name} ({version})' is being parsed as a legacy,
-            non PEP 440,
-            version. You may find odd behavior and sort order.
-            In particular it will be sorted as less than 0.0. It
-            is recommended to migrate to PEP 440 compatible
-            versions.
-            """).strip().replace('\n', ' ')
-
-        warnings.warn(tmpl.format(**vars(self)), PEP440Warning)
-
-    @property
-    def version(self):
-        try:
-            return self._version
-        except AttributeError:
-            version = _version_from_file(self._get_metadata(self.PKG_INFO))
-            if version is None:
-                tmpl = "Missing 'Version:' header and/or %s file"
-                raise ValueError(tmpl % self.PKG_INFO, self)
-            return version
-
-    @property
-    def _dep_map(self):
-        """
-        A map of extra to its list of (direct) requirements
-        for this distribution, including the null extra.
-        """
-        try:
-            return self.__dep_map
-        except AttributeError:
-            self.__dep_map = self._filter_extras(self._build_dep_map())
-        return self.__dep_map
-
-    @staticmethod
-    def _filter_extras(dm):
-        """
-        Given a mapping of extras to dependencies, strip off
-        environment markers and filter out any dependencies
-        not matching the markers.
-        """
-        for extra in list(filter(None, dm)):
-            new_extra = extra
-            reqs = dm.pop(extra)
-            new_extra, _, marker = extra.partition(':')
-            fails_marker = marker and (
-                invalid_marker(marker)
-                or not evaluate_marker(marker)
-            )
-            if fails_marker:
-                reqs = []
-            new_extra = safe_extra(new_extra) or None
-
-            dm.setdefault(new_extra, []).extend(reqs)
-        return dm
-
-    def _build_dep_map(self):
-        dm = {}
-        for name in 'requires.txt', 'depends.txt':
-            for extra, reqs in split_sections(self._get_metadata(name)):
-                dm.setdefault(extra, []).extend(parse_requirements(reqs))
-        return dm
-
-    def requires(self, extras=()):
-        """List of Requirements needed for this distro if `extras` are used"""
-        dm = self._dep_map
-        deps = []
-        deps.extend(dm.get(None, ()))
-        for ext in extras:
-            try:
-                deps.extend(dm[safe_extra(ext)])
-            except KeyError:
-                raise UnknownExtra(
-                    "%s has no such extra feature %r" % (self, ext)
-                )
-        return deps
-
-    def _get_metadata(self, name):
-        if self.has_metadata(name):
-            for line in self.get_metadata_lines(name):
-                yield line
-
-    def activate(self, path=None, replace=False):
-        """Ensure distribution is importable on `path` (default=sys.path)"""
-        if path is None:
-            path = sys.path
-        self.insert_on(path, replace=replace)
-        if path is sys.path:
-            fixup_namespace_packages(self.location)
-            for pkg in self._get_metadata('namespace_packages.txt'):
-                if pkg in sys.modules:
-                    declare_namespace(pkg)
-
-    def egg_name(self):
-        """Return what this distribution's standard .egg filename should be"""
-        filename = "%s-%s-py%s" % (
-            to_filename(self.project_name), to_filename(self.version),
-            self.py_version or PY_MAJOR
-        )
-
-        if self.platform:
-            filename += '-' + self.platform
-        return filename
-
-    def __repr__(self):
-        if self.location:
-            return "%s (%s)" % (self, self.location)
-        else:
-            return str(self)
-
-    def __str__(self):
-        try:
-            version = getattr(self, 'version', None)
-        except ValueError:
-            version = None
-        version = version or "[unknown version]"
-        return "%s %s" % (self.project_name, version)
-
-    def __getattr__(self, attr):
-        """Delegate all unrecognized public attributes to .metadata provider"""
-        if attr.startswith('_'):
-            raise AttributeError(attr)
-        return getattr(self._provider, attr)
-
-    def __dir__(self):
-        return list(
-            set(super(Distribution, self).__dir__())
-            | set(
-                attr for attr in self._provider.__dir__()
-                if not attr.startswith('_')
-            )
-        )
-
-    if not hasattr(object, '__dir__'):
-        # python 2.7 not supported
-        del __dir__
-
-    @classmethod
-    def from_filename(cls, filename, metadata=None, **kw):
-        return cls.from_location(
-            _normalize_cached(filename), os.path.basename(filename), metadata,
-            **kw
-        )
-
-    def as_requirement(self):
-        """Return a ``Requirement`` that matches this distribution exactly"""
-        if isinstance(self.parsed_version, packaging.version.Version):
-            spec = "%s==%s" % (self.project_name, self.parsed_version)
-        else:
-            spec = "%s===%s" % (self.project_name, self.parsed_version)
-
-        return Requirement.parse(spec)
-
-    def load_entry_point(self, group, name):
-        """Return the `name` entry point of `group` or raise ImportError"""
-        ep = self.get_entry_info(group, name)
-        if ep is None:
-            raise ImportError("Entry point %r not found" % ((group, name),))
-        return ep.load()
-
-    def get_entry_map(self, group=None):
-        """Return the entry point map for `group`, or the full entry map"""
-        try:
-            ep_map = self._ep_map
-        except AttributeError:
-            ep_map = self._ep_map = EntryPoint.parse_map(
-                self._get_metadata('entry_points.txt'), self
-            )
-        if group is not None:
-            return ep_map.get(group, {})
-        return ep_map
-
-    def get_entry_info(self, group, name):
-        """Return the EntryPoint object for `group`+`name`, or ``None``"""
-        return self.get_entry_map(group).get(name)
-
-    def insert_on(self, path, loc=None, replace=False):
-        """Ensure self.location is on path
-
-        If replace=False (default):
-            - If location is already in path anywhere, do nothing.
-            - Else:
-              - If it's an egg and its parent directory is on path,
-                insert just ahead of the parent.
-              - Else: add to the end of path.
-        If replace=True:
-            - If location is already on path anywhere (not eggs)
-              or higher priority than its parent (eggs)
-              do nothing.
-            - Else:
-              - If it's an egg and its parent directory is on path,
-                insert just ahead of the parent,
-                removing any lower-priority entries.
-              - Else: add it to the front of path.
-        """
-
-        loc = loc or self.location
-        if not loc:
-            return
-
-        nloc = _normalize_cached(loc)
-        bdir = os.path.dirname(nloc)
-        npath = [(p and _normalize_cached(p) or p) for p in path]
-
-        for p, item in enumerate(npath):
-            if item == nloc:
-                if replace:
-                    break
-                else:
-                    # don't modify path (even removing duplicates) if
-                    # found and not replace
-                    return
-            elif item == bdir and self.precedence == EGG_DIST:
-                # if it's an .egg, give it precedence over its directory
-                # UNLESS it's already been added to sys.path and replace=False
-                if (not replace) and nloc in npath[p:]:
-                    return
-                if path is sys.path:
-                    self.check_version_conflict()
-                path.insert(p, loc)
-                npath.insert(p, nloc)
-                break
-        else:
-            if path is sys.path:
-                self.check_version_conflict()
-            if replace:
-                path.insert(0, loc)
-            else:
-                path.append(loc)
-            return
-
-        # p is the spot where we found or inserted loc; now remove duplicates
-        while True:
-            try:
-                np = npath.index(nloc, p + 1)
-            except ValueError:
-                break
-            else:
-                del npath[np], path[np]
-                # ha!
-                p = np
-
-        return
-
-    def check_version_conflict(self):
-        if self.key == 'setuptools':
-            # ignore the inevitable setuptools self-conflicts  :(
-            return
-
-        nsp = dict.fromkeys(self._get_metadata('namespace_packages.txt'))
-        loc = normalize_path(self.location)
-        for modname in self._get_metadata('top_level.txt'):
-            if (modname not in sys.modules or modname in nsp
-                    or modname in _namespace_packages):
-                continue
-            if modname in ('pkg_resources', 'setuptools', 'site'):
-                continue
-            fn = getattr(sys.modules[modname], '__file__', None)
-            if fn and (normalize_path(fn).startswith(loc) or
-                       fn.startswith(self.location)):
-                continue
-            issue_warning(
-                "Module %s was already imported from %s, but %s is being added"
-                " to sys.path" % (modname, fn, self.location),
-            )
-
-    def has_version(self):
-        try:
-            self.version
-        except ValueError:
-            issue_warning("Unbuilt egg for " + repr(self))
-            return False
-        return True
-
-    def clone(self, **kw):
-        """Copy this distribution, substituting in any changed keyword args"""
-        names = 'project_name version py_version platform location precedence'
-        for attr in names.split():
-            kw.setdefault(attr, getattr(self, attr, None))
-        kw.setdefault('metadata', self._provider)
-        return self.__class__(**kw)
-
-    @property
-    def extras(self):
-        return [dep for dep in self._dep_map if dep]
-
-
-class EggInfoDistribution(Distribution):
-    def _reload_version(self):
-        """
-        Packages installed by distutils (e.g. numpy or scipy),
-        which uses an old safe_version, and so
-        their version numbers can get mangled when
-        converted to filenames (e.g., 1.11.0.dev0+2329eae to
-        1.11.0.dev0_2329eae). These distributions will not be
-        parsed properly
-        downstream by Distribution and safe_version, so
-        take an extra step and try to get the version number from
-        the metadata file itself instead of the filename.
-        """
-        md_version = _version_from_file(self._get_metadata(self.PKG_INFO))
-        if md_version:
-            self._version = md_version
-        return self
-
-
-class DistInfoDistribution(Distribution):
-    """
-    Wrap an actual or potential sys.path entry
-    w/metadata, .dist-info style.
-    """
-    PKG_INFO = 'METADATA'
-    EQEQ = re.compile(r"([\(,])\s*(\d.*?)\s*([,\)])")
-
-    @property
-    def _parsed_pkg_info(self):
-        """Parse and cache metadata"""
-        try:
-            return self._pkg_info
-        except AttributeError:
-            metadata = self.get_metadata(self.PKG_INFO)
-            self._pkg_info = email.parser.Parser().parsestr(metadata)
-            return self._pkg_info
-
-    @property
-    def _dep_map(self):
-        try:
-            return self.__dep_map
-        except AttributeError:
-            self.__dep_map = self._compute_dependencies()
-            return self.__dep_map
-
-    def _compute_dependencies(self):
-        """Recompute this distribution's dependencies."""
-        dm = self.__dep_map = {None: []}
-
-        reqs = []
-        # Including any condition expressions
-        for req in self._parsed_pkg_info.get_all('Requires-Dist') or []:
-            reqs.extend(parse_requirements(req))
-
-        def reqs_for_extra(extra):
-            for req in reqs:
-                if not req.marker or req.marker.evaluate({'extra': extra}):
-                    yield req
-
-        common = frozenset(reqs_for_extra(None))
-        dm[None].extend(common)
-
-        for extra in self._parsed_pkg_info.get_all('Provides-Extra') or []:
-            s_extra = safe_extra(extra.strip())
-            dm[s_extra] = list(frozenset(reqs_for_extra(extra)) - common)
-
-        return dm
-
-
-_distributionImpl = {
-    '.egg': Distribution,
-    '.egg-info': EggInfoDistribution,
-    '.dist-info': DistInfoDistribution,
-}
-
-
-def issue_warning(*args, **kw):
-    level = 1
-    g = globals()
-    try:
-        # find the first stack frame that is *not* code in
-        # the pkg_resources module, to use for the warning
-        while sys._getframe(level).f_globals is g:
-            level += 1
-    except ValueError:
-        pass
-    warnings.warn(stacklevel=level + 1, *args, **kw)
-
-
-class RequirementParseError(ValueError):
-    def __str__(self):
-        return ' '.join(self.args)
-
-
-def parse_requirements(strs):
-    """Yield ``Requirement`` objects for each specification in `strs`
-
-    `strs` must be a string, or a (possibly-nested) iterable thereof.
-    """
-    # create a steppable iterator, so we can handle \-continuations
-    lines = iter(yield_lines(strs))
-
-    for line in lines:
-        # Drop comments -- a hash without a space may be in a URL.
-        if ' #' in line:
-            line = line[:line.find(' #')]
-        # If there is a line continuation, drop it, and append the next line.
-        if line.endswith('\\'):
-            line = line[:-2].strip()
-            try:
-                line += next(lines)
-            except StopIteration:
-                return
-        yield Requirement(line)
-
-
-class Requirement(packaging.requirements.Requirement):
-    def __init__(self, requirement_string):
-        """DO NOT CALL THIS UNDOCUMENTED METHOD; use Requirement.parse()!"""
-        try:
-            super(Requirement, self).__init__(requirement_string)
-        except packaging.requirements.InvalidRequirement as e:
-            raise RequirementParseError(str(e))
-        self.unsafe_name = self.name
-        project_name = safe_name(self.name)
-        self.project_name, self.key = project_name, project_name.lower()
-        self.specs = [
-            (spec.operator, spec.version) for spec in self.specifier]
-        self.extras = tuple(map(safe_extra, self.extras))
-        self.hashCmp = (
-            self.key,
-            self.specifier,
-            frozenset(self.extras),
-            str(self.marker) if self.marker else None,
-        )
-        self.__hash = hash(self.hashCmp)
-
-    def __eq__(self, other):
-        return (
-            isinstance(other, Requirement) and
-            self.hashCmp == other.hashCmp
-        )
-
-    def __ne__(self, other):
-        return not self == other
-
-    def __contains__(self, item):
-        if isinstance(item, Distribution):
-            if item.key != self.key:
-                return False
-
-            item = item.version
-
-        # Allow prereleases always in order to match the previous behavior of
-        # this method. In the future this should be smarter and follow PEP 440
-        # more accurately.
-        return self.specifier.contains(item, prereleases=True)
-
-    def __hash__(self):
-        return self.__hash
-
-    def __repr__(self):
-        return "Requirement.parse(%r)" % str(self)
-
-    @staticmethod
-    def parse(s):
-        req, = parse_requirements(s)
-        return req
-
-
-def _always_object(classes):
-    """
-    Ensure object appears in the mro even
-    for old-style classes.
-    """
-    if object not in classes:
-        return classes + (object,)
-    return classes
-
-
-def _find_adapter(registry, ob):
-    """Return an adapter factory for `ob` from `registry`"""
-    types = _always_object(inspect.getmro(getattr(ob, '__class__', type(ob))))
-    for t in types:
-        if t in registry:
-            return registry[t]
-
-
-def ensure_directory(path):
-    """Ensure that the parent directory of `path` exists"""
-    dirname = os.path.dirname(path)
-    py31compat.makedirs(dirname, exist_ok=True)
-
-
-def _bypass_ensure_directory(path):
-    """Sandbox-bypassing version of ensure_directory()"""
-    if not WRITE_SUPPORT:
-        raise IOError('"os.mkdir" not supported on this platform.')
-    dirname, filename = split(path)
-    if dirname and filename and not isdir(dirname):
-        _bypass_ensure_directory(dirname)
-        try:
-            mkdir(dirname, 0o755)
-        except FileExistsError:
-            pass
-
-
-def split_sections(s):
-    """Split a string or iterable thereof into (section, content) pairs
-
-    Each ``section`` is a stripped version of the section header ("[section]")
-    and each ``content`` is a list of stripped lines excluding blank lines and
-    comment-only lines.  If there are any such lines before the first section
-    header, they're returned in a first ``section`` of ``None``.
-    """
-    section = None
-    content = []
-    for line in yield_lines(s):
-        if line.startswith("["):
-            if line.endswith("]"):
-                if section or content:
-                    yield section, content
-                section = line[1:-1].strip()
-                content = []
-            else:
-                raise ValueError("Invalid section heading", line)
-        else:
-            content.append(line)
-
-    # wrap up last segment
-    yield section, content
-
-
-def _mkstemp(*args, **kw):
-    old_open = os.open
-    try:
-        # temporarily bypass sandboxing
-        os.open = os_open
-        return tempfile.mkstemp(*args, **kw)
-    finally:
-        # and then put it back
-        os.open = old_open
-
-
-# Silence the PEP440Warning by default, so that end users don't get hit by it
-# randomly just because they use pkg_resources. We want to append the rule
-# because we want earlier uses of filterwarnings to take precedence over this
-# one.
-warnings.filterwarnings("ignore", category=PEP440Warning, append=True)
-
-
-# from jaraco.functools 1.3
-def _call_aside(f, *args, **kwargs):
-    f(*args, **kwargs)
-    return f
-
-
-@_call_aside
-def _initialize(g=globals()):
-    "Set up global resource manager (deliberately not state-saved)"
-    manager = ResourceManager()
-    g['_manager'] = manager
-    g.update(
-        (name, getattr(manager, name))
-        for name in dir(manager)
-        if not name.startswith('_')
-    )
-
-
-@_call_aside
-def _initialize_master_working_set():
-    """
-    Prepare the master working set and make the ``require()``
-    API available.
-
-    This function has explicit effects on the global state
-    of pkg_resources. It is intended to be invoked once at
-    the initialization of this module.
-
-    Invocation by other packages is unsupported and done
-    at their own risk.
-    """
-    working_set = WorkingSet._build_master()
-    _declare_state('object', working_set=working_set)
-
-    require = working_set.require
-    iter_entry_points = working_set.iter_entry_points
-    add_activation_listener = working_set.subscribe
-    run_script = working_set.run_script
-    # backward compatibility
-    run_main = run_script
-    # Activate all distributions already on sys.path with replace=False and
-    # ensure that all distributions added to the working set in the future
-    # (e.g. by calling ``require()``) will get activated as well,
-    # with higher priority (replace=True).
-    tuple(
-        dist.activate(replace=False)
-        for dist in working_set
-    )
-    add_activation_listener(
-        lambda dist: dist.activate(replace=True),
-        existing=False,
-    )
-    working_set.entries = []
-    # match order
-    list(map(working_set.add_entry, sys.path))
-    globals().update(locals())
-
-class PkgResourcesDeprecationWarning(Warning):
-    """
-    Base class for warning about deprecations in ``pkg_resources``
-
-    This class is not derived from ``DeprecationWarning``, and as such is
-    visible by default.
-    """
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 132792d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__pycache__/py31compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__pycache__/py31compat.cpython-37.pyc
deleted file mode 100644
index f17a185..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/__pycache__/py31compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/py31compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/py31compat.py
deleted file mode 100644
index a2d3007..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pkg_resources/py31compat.py
+++ /dev/null
@@ -1,23 +0,0 @@
-import os
-import errno
-import sys
-
-from pip._vendor import six
-
-
-def _makedirs_31(path, exist_ok=False):
-    try:
-        os.makedirs(path)
-    except OSError as exc:
-        if not exist_ok or exc.errno != errno.EEXIST:
-            raise
-
-
-# rely on compatibility behavior until mode considerations
-#  and exists_ok considerations are disentangled.
-# See https://github.com/pypa/setuptools/pull/1083#issuecomment-315168663
-needs_makedirs = (
-    six.PY2 or
-    (3, 4) <= sys.version_info < (3, 4, 1)
-)
-makedirs = _makedirs_31 if needs_makedirs else os.makedirs
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__init__.py
deleted file mode 100644
index a41f65d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__init__.py
+++ /dev/null
@@ -1,127 +0,0 @@
-# Copyright (c) 2012 Giorgos Verigakis <verigak@gmail.com>
-#
-# Permission to use, copy, modify, and distribute this software for any
-# purpose with or without fee is hereby granted, provided that the above
-# copyright notice and this permission notice appear in all copies.
-#
-# THE SOFTWARE IS PROVIDED "AS IS" AND THE AUTHOR DISCLAIMS ALL WARRANTIES
-# WITH REGARD TO THIS SOFTWARE INCLUDING ALL IMPLIED WARRANTIES OF
-# MERCHANTABILITY AND FITNESS. IN NO EVENT SHALL THE AUTHOR BE LIABLE FOR
-# ANY SPECIAL, DIRECT, INDIRECT, OR CONSEQUENTIAL DAMAGES OR ANY DAMAGES
-# WHATSOEVER RESULTING FROM LOSS OF USE, DATA OR PROFITS, WHETHER IN AN
-# ACTION OF CONTRACT, NEGLIGENCE OR OTHER TORTIOUS ACTION, ARISING OUT OF
-# OR IN CONNECTION WITH THE USE OR PERFORMANCE OF THIS SOFTWARE.
-
-from __future__ import division
-
-from collections import deque
-from datetime import timedelta
-from math import ceil
-from sys import stderr
-from time import time
-
-
-__version__ = '1.4'
-
-
-class Infinite(object):
-    file = stderr
-    sma_window = 10         # Simple Moving Average window
-
-    def __init__(self, *args, **kwargs):
-        self.index = 0
-        self.start_ts = time()
-        self.avg = 0
-        self._ts = self.start_ts
-        self._xput = deque(maxlen=self.sma_window)
-        for key, val in kwargs.items():
-            setattr(self, key, val)
-
-    def __getitem__(self, key):
-        if key.startswith('_'):
-            return None
-        return getattr(self, key, None)
-
-    @property
-    def elapsed(self):
-        return int(time() - self.start_ts)
-
-    @property
-    def elapsed_td(self):
-        return timedelta(seconds=self.elapsed)
-
-    def update_avg(self, n, dt):
-        if n > 0:
-            self._xput.append(dt / n)
-            self.avg = sum(self._xput) / len(self._xput)
-
-    def update(self):
-        pass
-
-    def start(self):
-        pass
-
-    def finish(self):
-        pass
-
-    def next(self, n=1):
-        now = time()
-        dt = now - self._ts
-        self.update_avg(n, dt)
-        self._ts = now
-        self.index = self.index + n
-        self.update()
-
-    def iter(self, it):
-        try:
-            for x in it:
-                yield x
-                self.next()
-        finally:
-            self.finish()
-
-
-class Progress(Infinite):
-    def __init__(self, *args, **kwargs):
-        super(Progress, self).__init__(*args, **kwargs)
-        self.max = kwargs.get('max', 100)
-
-    @property
-    def eta(self):
-        return int(ceil(self.avg * self.remaining))
-
-    @property
-    def eta_td(self):
-        return timedelta(seconds=self.eta)
-
-    @property
-    def percent(self):
-        return self.progress * 100
-
-    @property
-    def progress(self):
-        return min(1, self.index / self.max)
-
-    @property
-    def remaining(self):
-        return max(self.max - self.index, 0)
-
-    def start(self):
-        self.update()
-
-    def goto(self, index):
-        incr = index - self.index
-        self.next(incr)
-
-    def iter(self, it):
-        try:
-            self.max = len(it)
-        except TypeError:
-            pass
-
-        try:
-            for x in it:
-                yield x
-                self.next()
-        finally:
-            self.finish()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 59b3fbe..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/bar.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/bar.cpython-37.pyc
deleted file mode 100644
index e3c2e89..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/bar.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/helpers.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/helpers.cpython-37.pyc
deleted file mode 100644
index 89d26eb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/helpers.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/spinner.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/spinner.cpython-37.pyc
deleted file mode 100644
index 3f01f3b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/__pycache__/spinner.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/bar.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/bar.py
deleted file mode 100644
index 025e61c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/bar.py
+++ /dev/null
@@ -1,94 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Copyright (c) 2012 Giorgos Verigakis <verigak@gmail.com>
-#
-# Permission to use, copy, modify, and distribute this software for any
-# purpose with or without fee is hereby granted, provided that the above
-# copyright notice and this permission notice appear in all copies.
-#
-# THE SOFTWARE IS PROVIDED "AS IS" AND THE AUTHOR DISCLAIMS ALL WARRANTIES
-# WITH REGARD TO THIS SOFTWARE INCLUDING ALL IMPLIED WARRANTIES OF
-# MERCHANTABILITY AND FITNESS. IN NO EVENT SHALL THE AUTHOR BE LIABLE FOR
-# ANY SPECIAL, DIRECT, INDIRECT, OR CONSEQUENTIAL DAMAGES OR ANY DAMAGES
-# WHATSOEVER RESULTING FROM LOSS OF USE, DATA OR PROFITS, WHETHER IN AN
-# ACTION OF CONTRACT, NEGLIGENCE OR OTHER TORTIOUS ACTION, ARISING OUT OF
-# OR IN CONNECTION WITH THE USE OR PERFORMANCE OF THIS SOFTWARE.
-
-from __future__ import unicode_literals
-
-import sys
-
-from . import Progress
-from .helpers import WritelnMixin
-
-
-class Bar(WritelnMixin, Progress):
-    width = 32
-    message = ''
-    suffix = '%(index)d/%(max)d'
-    bar_prefix = ' |'
-    bar_suffix = '| '
-    empty_fill = ' '
-    fill = '#'
-    hide_cursor = True
-
-    def update(self):
-        filled_length = int(self.width * self.progress)
-        empty_length = self.width - filled_length
-
-        message = self.message % self
-        bar = self.fill * filled_length
-        empty = self.empty_fill * empty_length
-        suffix = self.suffix % self
-        line = ''.join([message, self.bar_prefix, bar, empty, self.bar_suffix,
-                        suffix])
-        self.writeln(line)
-
-
-class ChargingBar(Bar):
-    suffix = '%(percent)d%%'
-    bar_prefix = ' '
-    bar_suffix = ' '
-    empty_fill = '∙'
-    fill = '█'
-
-
-class FillingSquaresBar(ChargingBar):
-    empty_fill = '▢'
-    fill = '▣'
-
-
-class FillingCirclesBar(ChargingBar):
-    empty_fill = '◯'
-    fill = '◉'
-
-
-class IncrementalBar(Bar):
-    if sys.platform.startswith('win'):
-        phases = (u' ', u'▌', u'█')
-    else:
-        phases = (' ', '▏', '▎', '▍', '▌', '▋', '▊', '▉', '█')
-
-    def update(self):
-        nphases = len(self.phases)
-        filled_len = self.width * self.progress
-        nfull = int(filled_len)                      # Number of full chars
-        phase = int((filled_len - nfull) * nphases)  # Phase of last char
-        nempty = self.width - nfull                  # Number of empty chars
-
-        message = self.message % self
-        bar = self.phases[-1] * nfull
-        current = self.phases[phase] if phase > 0 else ''
-        empty = self.empty_fill * max(0, nempty - len(current))
-        suffix = self.suffix % self
-        line = ''.join([message, self.bar_prefix, bar, current, empty,
-                        self.bar_suffix, suffix])
-        self.writeln(line)
-
-
-class PixelBar(IncrementalBar):
-    phases = ('⡀', '⡄', '⡆', '⡇', '⣇', '⣧', '⣷', '⣿')
-
-
-class ShadyBar(IncrementalBar):
-    phases = (' ', '░', '▒', '▓', '█')
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/counter.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/counter.py
deleted file mode 100644
index 6b45a1e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/counter.py
+++ /dev/null
@@ -1,48 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Copyright (c) 2012 Giorgos Verigakis <verigak@gmail.com>
-#
-# Permission to use, copy, modify, and distribute this software for any
-# purpose with or without fee is hereby granted, provided that the above
-# copyright notice and this permission notice appear in all copies.
-#
-# THE SOFTWARE IS PROVIDED "AS IS" AND THE AUTHOR DISCLAIMS ALL WARRANTIES
-# WITH REGARD TO THIS SOFTWARE INCLUDING ALL IMPLIED WARRANTIES OF
-# MERCHANTABILITY AND FITNESS. IN NO EVENT SHALL THE AUTHOR BE LIABLE FOR
-# ANY SPECIAL, DIRECT, INDIRECT, OR CONSEQUENTIAL DAMAGES OR ANY DAMAGES
-# WHATSOEVER RESULTING FROM LOSS OF USE, DATA OR PROFITS, WHETHER IN AN
-# ACTION OF CONTRACT, NEGLIGENCE OR OTHER TORTIOUS ACTION, ARISING OUT OF
-# OR IN CONNECTION WITH THE USE OR PERFORMANCE OF THIS SOFTWARE.
-
-from __future__ import unicode_literals
-from . import Infinite, Progress
-from .helpers import WriteMixin
-
-
-class Counter(WriteMixin, Infinite):
-    message = ''
-    hide_cursor = True
-
-    def update(self):
-        self.write(str(self.index))
-
-
-class Countdown(WriteMixin, Progress):
-    hide_cursor = True
-
-    def update(self):
-        self.write(str(self.remaining))
-
-
-class Stack(WriteMixin, Progress):
-    phases = (' ', '▁', '▂', '▃', '▄', '▅', '▆', '▇', '█')
-    hide_cursor = True
-
-    def update(self):
-        nphases = len(self.phases)
-        i = min(nphases - 1, int(self.progress * nphases))
-        self.write(self.phases[i])
-
-
-class Pie(Stack):
-    phases = ('○', '◔', '◑', '◕', '●')
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/helpers.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/helpers.py
deleted file mode 100644
index 0cde44e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/helpers.py
+++ /dev/null
@@ -1,91 +0,0 @@
-# Copyright (c) 2012 Giorgos Verigakis <verigak@gmail.com>
-#
-# Permission to use, copy, modify, and distribute this software for any
-# purpose with or without fee is hereby granted, provided that the above
-# copyright notice and this permission notice appear in all copies.
-#
-# THE SOFTWARE IS PROVIDED "AS IS" AND THE AUTHOR DISCLAIMS ALL WARRANTIES
-# WITH REGARD TO THIS SOFTWARE INCLUDING ALL IMPLIED WARRANTIES OF
-# MERCHANTABILITY AND FITNESS. IN NO EVENT SHALL THE AUTHOR BE LIABLE FOR
-# ANY SPECIAL, DIRECT, INDIRECT, OR CONSEQUENTIAL DAMAGES OR ANY DAMAGES
-# WHATSOEVER RESULTING FROM LOSS OF USE, DATA OR PROFITS, WHETHER IN AN
-# ACTION OF CONTRACT, NEGLIGENCE OR OTHER TORTIOUS ACTION, ARISING OUT OF
-# OR IN CONNECTION WITH THE USE OR PERFORMANCE OF THIS SOFTWARE.
-
-from __future__ import print_function
-
-
-HIDE_CURSOR = '\x1b[?25l'
-SHOW_CURSOR = '\x1b[?25h'
-
-
-class WriteMixin(object):
-    hide_cursor = False
-
-    def __init__(self, message=None, **kwargs):
-        super(WriteMixin, self).__init__(**kwargs)
-        self._width = 0
-        if message:
-            self.message = message
-
-        if self.file and self.file.isatty():
-            if self.hide_cursor:
-                print(HIDE_CURSOR, end='', file=self.file)
-            print(self.message, end='', file=self.file)
-            self.file.flush()
-
-    def write(self, s):
-        if self.file and self.file.isatty():
-            b = '\b' * self._width
-            c = s.ljust(self._width)
-            print(b + c, end='', file=self.file)
-            self._width = max(self._width, len(s))
-            self.file.flush()
-
-    def finish(self):
-        if self.file and self.file.isatty() and self.hide_cursor:
-            print(SHOW_CURSOR, end='', file=self.file)
-
-
-class WritelnMixin(object):
-    hide_cursor = False
-
-    def __init__(self, message=None, **kwargs):
-        super(WritelnMixin, self).__init__(**kwargs)
-        if message:
-            self.message = message
-
-        if self.file and self.file.isatty() and self.hide_cursor:
-            print(HIDE_CURSOR, end='', file=self.file)
-
-    def clearln(self):
-        if self.file and self.file.isatty():
-            print('\r\x1b[K', end='', file=self.file)
-
-    def writeln(self, line):
-        if self.file and self.file.isatty():
-            self.clearln()
-            print(line, end='', file=self.file)
-            self.file.flush()
-
-    def finish(self):
-        if self.file and self.file.isatty():
-            print(file=self.file)
-            if self.hide_cursor:
-                print(SHOW_CURSOR, end='', file=self.file)
-
-
-from signal import signal, SIGINT
-from sys import exit
-
-
-class SigIntMixin(object):
-    """Registers a signal handler that calls finish on SIGINT"""
-
-    def __init__(self, *args, **kwargs):
-        super(SigIntMixin, self).__init__(*args, **kwargs)
-        signal(SIGINT, self._sigint_handler)
-
-    def _sigint_handler(self, signum, frame):
-        self.finish()
-        exit(0)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/spinner.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/spinner.py
deleted file mode 100644
index 464c7b2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/progress/spinner.py
+++ /dev/null
@@ -1,44 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Copyright (c) 2012 Giorgos Verigakis <verigak@gmail.com>
-#
-# Permission to use, copy, modify, and distribute this software for any
-# purpose with or without fee is hereby granted, provided that the above
-# copyright notice and this permission notice appear in all copies.
-#
-# THE SOFTWARE IS PROVIDED "AS IS" AND THE AUTHOR DISCLAIMS ALL WARRANTIES
-# WITH REGARD TO THIS SOFTWARE INCLUDING ALL IMPLIED WARRANTIES OF
-# MERCHANTABILITY AND FITNESS. IN NO EVENT SHALL THE AUTHOR BE LIABLE FOR
-# ANY SPECIAL, DIRECT, INDIRECT, OR CONSEQUENTIAL DAMAGES OR ANY DAMAGES
-# WHATSOEVER RESULTING FROM LOSS OF USE, DATA OR PROFITS, WHETHER IN AN
-# ACTION OF CONTRACT, NEGLIGENCE OR OTHER TORTIOUS ACTION, ARISING OUT OF
-# OR IN CONNECTION WITH THE USE OR PERFORMANCE OF THIS SOFTWARE.
-
-from __future__ import unicode_literals
-from . import Infinite
-from .helpers import WriteMixin
-
-
-class Spinner(WriteMixin, Infinite):
-    message = ''
-    phases = ('-', '\\', '|', '/')
-    hide_cursor = True
-
-    def update(self):
-        i = self.index % len(self.phases)
-        self.write(self.phases[i])
-
-
-class PieSpinner(Spinner):
-    phases = ['◷', '◶', '◵', '◴']
-
-
-class MoonSpinner(Spinner):
-    phases = ['◑', '◒', '◐', '◓']
-
-
-class LineSpinner(Spinner):
-    phases = ['⎺', '⎻', '⎼', '⎽', '⎼', '⎻']
-
-class PixelSpinner(Spinner):
-    phases = ['⣾','⣷', '⣯', '⣟', '⡿', '⢿', '⣻', '⣽']
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pyparsing.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pyparsing.py
deleted file mode 100644
index bea4d9c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pyparsing.py
+++ /dev/null
@@ -1,6452 +0,0 @@
-#-*- coding: utf-8 -*-
-# module pyparsing.py
-#
-# Copyright (c) 2003-2019  Paul T. McGuire
-#
-# Permission is hereby granted, free of charge, to any person obtaining
-# a copy of this software and associated documentation files (the
-# "Software"), to deal in the Software without restriction, including
-# without limitation the rights to use, copy, modify, merge, publish,
-# distribute, sublicense, and/or sell copies of the Software, and to
-# permit persons to whom the Software is furnished to do so, subject to
-# the following conditions:
-#
-# The above copyright notice and this permission notice shall be
-# included in all copies or substantial portions of the Software.
-#
-# THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND,
-# EXPRESS OR IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF
-# MERCHANTABILITY, FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT.
-# IN NO EVENT SHALL THE AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY
-# CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER IN AN ACTION OF CONTRACT,
-# TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE
-# SOFTWARE OR THE USE OR OTHER DEALINGS IN THE SOFTWARE.
-#
-
-__doc__ = \
-"""
-pyparsing module - Classes and methods to define and execute parsing grammars
-=============================================================================
-
-The pyparsing module is an alternative approach to creating and
-executing simple grammars, vs. the traditional lex/yacc approach, or the
-use of regular expressions.  With pyparsing, you don't need to learn
-a new syntax for defining grammars or matching expressions - the parsing
-module provides a library of classes that you use to construct the
-grammar directly in Python.
-
-Here is a program to parse "Hello, World!" (or any greeting of the form
-``"<salutation>, <addressee>!"``), built up using :class:`Word`,
-:class:`Literal`, and :class:`And` elements
-(the :class:`'+'<ParserElement.__add__>` operators create :class:`And` expressions,
-and the strings are auto-converted to :class:`Literal` expressions)::
-
-    from pip._vendor.pyparsing import Word, alphas
-
-    # define grammar of a greeting
-    greet = Word(alphas) + "," + Word(alphas) + "!"
-
-    hello = "Hello, World!"
-    print (hello, "->", greet.parseString(hello))
-
-The program outputs the following::
-
-    Hello, World! -> ['Hello', ',', 'World', '!']
-
-The Python representation of the grammar is quite readable, owing to the
-self-explanatory class names, and the use of '+', '|' and '^' operators.
-
-The :class:`ParseResults` object returned from
-:class:`ParserElement.parseString` can be
-accessed as a nested list, a dictionary, or an object with named
-attributes.
-
-The pyparsing module handles some of the problems that are typically
-vexing when writing text parsers:
-
-  - extra or missing whitespace (the above program will also handle
-    "Hello,World!", "Hello  ,  World  !", etc.)
-  - quoted strings
-  - embedded comments
-
-
-Getting Started -
------------------
-Visit the classes :class:`ParserElement` and :class:`ParseResults` to
-see the base classes that most other pyparsing
-classes inherit from. Use the docstrings for examples of how to:
-
- - construct literal match expressions from :class:`Literal` and
-   :class:`CaselessLiteral` classes
- - construct character word-group expressions using the :class:`Word`
-   class
- - see how to create repetitive expressions using :class:`ZeroOrMore`
-   and :class:`OneOrMore` classes
- - use :class:`'+'<And>`, :class:`'|'<MatchFirst>`, :class:`'^'<Or>`,
-   and :class:`'&'<Each>` operators to combine simple expressions into
-   more complex ones
- - associate names with your parsed results using
-   :class:`ParserElement.setResultsName`
- - find some helpful expression short-cuts like :class:`delimitedList`
-   and :class:`oneOf`
- - find more useful common expressions in the :class:`pyparsing_common`
-   namespace class
-"""
-
-__version__ = "2.3.1"
-__versionTime__ = "09 Jan 2019 23:26 UTC"
-__author__ = "Paul McGuire <ptmcg@users.sourceforge.net>"
-
-import string
-from weakref import ref as wkref
-import copy
-import sys
-import warnings
-import re
-import sre_constants
-import collections
-import pprint
-import traceback
-import types
-from datetime import datetime
-
-try:
-    # Python 3
-    from itertools import filterfalse
-except ImportError:
-    from itertools import ifilterfalse as filterfalse
-
-try:
-    from _thread import RLock
-except ImportError:
-    from threading import RLock
-
-try:
-    # Python 3
-    from collections.abc import Iterable
-    from collections.abc import MutableMapping
-except ImportError:
-    # Python 2.7
-    from collections import Iterable
-    from collections import MutableMapping
-
-try:
-    from collections import OrderedDict as _OrderedDict
-except ImportError:
-    try:
-        from ordereddict import OrderedDict as _OrderedDict
-    except ImportError:
-        _OrderedDict = None
-
-try:
-    from types import SimpleNamespace
-except ImportError:
-    class SimpleNamespace: pass
-
-
-#~ sys.stderr.write( "testing pyparsing module, version %s, %s\n" % (__version__,__versionTime__ ) )
-
-__all__ = [
-'And', 'CaselessKeyword', 'CaselessLiteral', 'CharsNotIn', 'Combine', 'Dict', 'Each', 'Empty',
-'FollowedBy', 'Forward', 'GoToColumn', 'Group', 'Keyword', 'LineEnd', 'LineStart', 'Literal',
-'PrecededBy', 'MatchFirst', 'NoMatch', 'NotAny', 'OneOrMore', 'OnlyOnce', 'Optional', 'Or',
-'ParseBaseException', 'ParseElementEnhance', 'ParseException', 'ParseExpression', 'ParseFatalException',
-'ParseResults', 'ParseSyntaxException', 'ParserElement', 'QuotedString', 'RecursiveGrammarException',
-'Regex', 'SkipTo', 'StringEnd', 'StringStart', 'Suppress', 'Token', 'TokenConverter',
-'White', 'Word', 'WordEnd', 'WordStart', 'ZeroOrMore', 'Char',
-'alphanums', 'alphas', 'alphas8bit', 'anyCloseTag', 'anyOpenTag', 'cStyleComment', 'col',
-'commaSeparatedList', 'commonHTMLEntity', 'countedArray', 'cppStyleComment', 'dblQuotedString',
-'dblSlashComment', 'delimitedList', 'dictOf', 'downcaseTokens', 'empty', 'hexnums',
-'htmlComment', 'javaStyleComment', 'line', 'lineEnd', 'lineStart', 'lineno',
-'makeHTMLTags', 'makeXMLTags', 'matchOnlyAtCol', 'matchPreviousExpr', 'matchPreviousLiteral',
-'nestedExpr', 'nullDebugAction', 'nums', 'oneOf', 'opAssoc', 'operatorPrecedence', 'printables',
-'punc8bit', 'pythonStyleComment', 'quotedString', 'removeQuotes', 'replaceHTMLEntity',
-'replaceWith', 'restOfLine', 'sglQuotedString', 'srange', 'stringEnd',
-'stringStart', 'traceParseAction', 'unicodeString', 'upcaseTokens', 'withAttribute',
-'indentedBlock', 'originalTextFor', 'ungroup', 'infixNotation','locatedExpr', 'withClass',
-'CloseMatch', 'tokenMap', 'pyparsing_common', 'pyparsing_unicode', 'unicode_set',
-]
-
-system_version = tuple(sys.version_info)[:3]
-PY_3 = system_version[0] == 3
-if PY_3:
-    _MAX_INT = sys.maxsize
-    basestring = str
-    unichr = chr
-    unicode = str
-    _ustr = str
-
-    # build list of single arg builtins, that can be used as parse actions
-    singleArgBuiltins = [sum, len, sorted, reversed, list, tuple, set, any, all, min, max]
-
-else:
-    _MAX_INT = sys.maxint
-    range = xrange
-
-    def _ustr(obj):
-        """Drop-in replacement for str(obj) that tries to be Unicode
-        friendly. It first tries str(obj). If that fails with
-        a UnicodeEncodeError, then it tries unicode(obj). It then
-        < returns the unicode object | encodes it with the default
-        encoding | ... >.
-        """
-        if isinstance(obj,unicode):
-            return obj
-
-        try:
-            # If this works, then _ustr(obj) has the same behaviour as str(obj), so
-            # it won't break any existing code.
-            return str(obj)
-
-        except UnicodeEncodeError:
-            # Else encode it
-            ret = unicode(obj).encode(sys.getdefaultencoding(), 'xmlcharrefreplace')
-            xmlcharref = Regex(r'&#\d+;')
-            xmlcharref.setParseAction(lambda t: '\\u' + hex(int(t[0][2:-1]))[2:])
-            return xmlcharref.transformString(ret)
-
-    # build list of single arg builtins, tolerant of Python version, that can be used as parse actions
-    singleArgBuiltins = []
-    import __builtin__
-    for fname in "sum len sorted reversed list tuple set any all min max".split():
-        try:
-            singleArgBuiltins.append(getattr(__builtin__,fname))
-        except AttributeError:
-            continue
-
-_generatorType = type((y for y in range(1)))
-
-def _xml_escape(data):
-    """Escape &, <, >, ", ', etc. in a string of data."""
-
-    # ampersand must be replaced first
-    from_symbols = '&><"\''
-    to_symbols = ('&'+s+';' for s in "amp gt lt quot apos".split())
-    for from_,to_ in zip(from_symbols, to_symbols):
-        data = data.replace(from_, to_)
-    return data
-
-alphas     = string.ascii_uppercase + string.ascii_lowercase
-nums       = "0123456789"
-hexnums    = nums + "ABCDEFabcdef"
-alphanums  = alphas + nums
-_bslash    = chr(92)
-printables = "".join(c for c in string.printable if c not in string.whitespace)
-
-class ParseBaseException(Exception):
-    """base exception class for all parsing runtime exceptions"""
-    # Performance tuning: we construct a *lot* of these, so keep this
-    # constructor as small and fast as possible
-    def __init__( self, pstr, loc=0, msg=None, elem=None ):
-        self.loc = loc
-        if msg is None:
-            self.msg = pstr
-            self.pstr = ""
-        else:
-            self.msg = msg
-            self.pstr = pstr
-        self.parserElement = elem
-        self.args = (pstr, loc, msg)
-
-    @classmethod
-    def _from_exception(cls, pe):
-        """
-        internal factory method to simplify creating one type of ParseException
-        from another - avoids having __init__ signature conflicts among subclasses
-        """
-        return cls(pe.pstr, pe.loc, pe.msg, pe.parserElement)
-
-    def __getattr__( self, aname ):
-        """supported attributes by name are:
-           - lineno - returns the line number of the exception text
-           - col - returns the column number of the exception text
-           - line - returns the line containing the exception text
-        """
-        if( aname == "lineno" ):
-            return lineno( self.loc, self.pstr )
-        elif( aname in ("col", "column") ):
-            return col( self.loc, self.pstr )
-        elif( aname == "line" ):
-            return line( self.loc, self.pstr )
-        else:
-            raise AttributeError(aname)
-
-    def __str__( self ):
-        return "%s (at char %d), (line:%d, col:%d)" % \
-                ( self.msg, self.loc, self.lineno, self.column )
-    def __repr__( self ):
-        return _ustr(self)
-    def markInputline( self, markerString = ">!<" ):
-        """Extracts the exception line from the input string, and marks
-           the location of the exception with a special symbol.
-        """
-        line_str = self.line
-        line_column = self.column - 1
-        if markerString:
-            line_str = "".join((line_str[:line_column],
-                                markerString, line_str[line_column:]))
-        return line_str.strip()
-    def __dir__(self):
-        return "lineno col line".split() + dir(type(self))
-
-class ParseException(ParseBaseException):
-    """
-    Exception thrown when parse expressions don't match class;
-    supported attributes by name are:
-    - lineno - returns the line number of the exception text
-    - col - returns the column number of the exception text
-    - line - returns the line containing the exception text
-
-    Example::
-
-        try:
-            Word(nums).setName("integer").parseString("ABC")
-        except ParseException as pe:
-            print(pe)
-            print("column: {}".format(pe.col))
-
-    prints::
-
-       Expected integer (at char 0), (line:1, col:1)
-        column: 1
-
-    """
-
-    @staticmethod
-    def explain(exc, depth=16):
-        """
-        Method to take an exception and translate the Python internal traceback into a list
-        of the pyparsing expressions that caused the exception to be raised.
-
-        Parameters:
-
-         - exc - exception raised during parsing (need not be a ParseException, in support
-           of Python exceptions that might be raised in a parse action)
-         - depth (default=16) - number of levels back in the stack trace to list expression
-           and function names; if None, the full stack trace names will be listed; if 0, only
-           the failing input line, marker, and exception string will be shown
-
-        Returns a multi-line string listing the ParserElements and/or function names in the
-        exception's stack trace.
-
-        Note: the diagnostic output will include string representations of the expressions
-        that failed to parse. These representations will be more helpful if you use `setName` to
-        give identifiable names to your expressions. Otherwise they will use the default string
-        forms, which may be cryptic to read.
-
-        explain() is only supported under Python 3.
-        """
-        import inspect
-
-        if depth is None:
-            depth = sys.getrecursionlimit()
-        ret = []
-        if isinstance(exc, ParseBaseException):
-            ret.append(exc.line)
-            ret.append(' ' * (exc.col - 1) + '^')
-        ret.append("{0}: {1}".format(type(exc).__name__, exc))
-
-        if depth > 0:
-            callers = inspect.getinnerframes(exc.__traceback__, context=depth)
-            seen = set()
-            for i, ff in enumerate(callers[-depth:]):
-                frm = ff.frame
-
-                f_self = frm.f_locals.get('self', None)
-                if isinstance(f_self, ParserElement):
-                    if frm.f_code.co_name not in ('parseImpl', '_parseNoCache'):
-                        continue
-                    if f_self in seen:
-                        continue
-                    seen.add(f_self)
-
-                    self_type = type(f_self)
-                    ret.append("{0}.{1} - {2}".format(self_type.__module__,
-                                                      self_type.__name__,
-                                                      f_self))
-                elif f_self is not None:
-                    self_type = type(f_self)
-                    ret.append("{0}.{1}".format(self_type.__module__,
-                                                self_type.__name__))
-                else:
-                    code = frm.f_code
-                    if code.co_name in ('wrapper', '<module>'):
-                        continue
-
-                    ret.append("{0}".format(code.co_name))
-
-                depth -= 1
-                if not depth:
-                    break
-
-        return '\n'.join(ret)
-
-
-class ParseFatalException(ParseBaseException):
-    """user-throwable exception thrown when inconsistent parse content
-       is found; stops all parsing immediately"""
-    pass
-
-class ParseSyntaxException(ParseFatalException):
-    """just like :class:`ParseFatalException`, but thrown internally
-    when an :class:`ErrorStop<And._ErrorStop>` ('-' operator) indicates
-    that parsing is to stop immediately because an unbacktrackable
-    syntax error has been found.
-    """
-    pass
-
-#~ class ReparseException(ParseBaseException):
-    #~ """Experimental class - parse actions can raise this exception to cause
-       #~ pyparsing to reparse the input string:
-        #~ - with a modified input string, and/or
-        #~ - with a modified start location
-       #~ Set the values of the ReparseException in the constructor, and raise the
-       #~ exception in a parse action to cause pyparsing to use the new string/location.
-       #~ Setting the values as None causes no change to be made.
-       #~ """
-    #~ def __init_( self, newstring, restartLoc ):
-        #~ self.newParseText = newstring
-        #~ self.reparseLoc = restartLoc
-
-class RecursiveGrammarException(Exception):
-    """exception thrown by :class:`ParserElement.validate` if the
-    grammar could be improperly recursive
-    """
-    def __init__( self, parseElementList ):
-        self.parseElementTrace = parseElementList
-
-    def __str__( self ):
-        return "RecursiveGrammarException: %s" % self.parseElementTrace
-
-class _ParseResultsWithOffset(object):
-    def __init__(self,p1,p2):
-        self.tup = (p1,p2)
-    def __getitem__(self,i):
-        return self.tup[i]
-    def __repr__(self):
-        return repr(self.tup[0])
-    def setOffset(self,i):
-        self.tup = (self.tup[0],i)
-
-class ParseResults(object):
-    """Structured parse results, to provide multiple means of access to
-    the parsed data:
-
-       - as a list (``len(results)``)
-       - by list index (``results[0], results[1]``, etc.)
-       - by attribute (``results.<resultsName>`` - see :class:`ParserElement.setResultsName`)
-
-    Example::
-
-        integer = Word(nums)
-        date_str = (integer.setResultsName("year") + '/'
-                        + integer.setResultsName("month") + '/'
-                        + integer.setResultsName("day"))
-        # equivalent form:
-        # date_str = integer("year") + '/' + integer("month") + '/' + integer("day")
-
-        # parseString returns a ParseResults object
-        result = date_str.parseString("1999/12/31")
-
-        def test(s, fn=repr):
-            print("%s -> %s" % (s, fn(eval(s))))
-        test("list(result)")
-        test("result[0]")
-        test("result['month']")
-        test("result.day")
-        test("'month' in result")
-        test("'minutes' in result")
-        test("result.dump()", str)
-
-    prints::
-
-        list(result) -> ['1999', '/', '12', '/', '31']
-        result[0] -> '1999'
-        result['month'] -> '12'
-        result.day -> '31'
-        'month' in result -> True
-        'minutes' in result -> False
-        result.dump() -> ['1999', '/', '12', '/', '31']
-        - day: 31
-        - month: 12
-        - year: 1999
-    """
-    def __new__(cls, toklist=None, name=None, asList=True, modal=True ):
-        if isinstance(toklist, cls):
-            return toklist
-        retobj = object.__new__(cls)
-        retobj.__doinit = True
-        return retobj
-
-    # Performance tuning: we construct a *lot* of these, so keep this
-    # constructor as small and fast as possible
-    def __init__( self, toklist=None, name=None, asList=True, modal=True, isinstance=isinstance ):
-        if self.__doinit:
-            self.__doinit = False
-            self.__name = None
-            self.__parent = None
-            self.__accumNames = {}
-            self.__asList = asList
-            self.__modal = modal
-            if toklist is None:
-                toklist = []
-            if isinstance(toklist, list):
-                self.__toklist = toklist[:]
-            elif isinstance(toklist, _generatorType):
-                self.__toklist = list(toklist)
-            else:
-                self.__toklist = [toklist]
-            self.__tokdict = dict()
-
-        if name is not None and name:
-            if not modal:
-                self.__accumNames[name] = 0
-            if isinstance(name,int):
-                name = _ustr(name) # will always return a str, but use _ustr for consistency
-            self.__name = name
-            if not (isinstance(toklist, (type(None), basestring, list)) and toklist in (None,'',[])):
-                if isinstance(toklist,basestring):
-                    toklist = [ toklist ]
-                if asList:
-                    if isinstance(toklist,ParseResults):
-                        self[name] = _ParseResultsWithOffset(ParseResults(toklist.__toklist), 0)
-                    else:
-                        self[name] = _ParseResultsWithOffset(ParseResults(toklist[0]),0)
-                    self[name].__name = name
-                else:
-                    try:
-                        self[name] = toklist[0]
-                    except (KeyError,TypeError,IndexError):
-                        self[name] = toklist
-
-    def __getitem__( self, i ):
-        if isinstance( i, (int,slice) ):
-            return self.__toklist[i]
-        else:
-            if i not in self.__accumNames:
-                return self.__tokdict[i][-1][0]
-            else:
-                return ParseResults([ v[0] for v in self.__tokdict[i] ])
-
-    def __setitem__( self, k, v, isinstance=isinstance ):
-        if isinstance(v,_ParseResultsWithOffset):
-            self.__tokdict[k] = self.__tokdict.get(k,list()) + [v]
-            sub = v[0]
-        elif isinstance(k,(int,slice)):
-            self.__toklist[k] = v
-            sub = v
-        else:
-            self.__tokdict[k] = self.__tokdict.get(k,list()) + [_ParseResultsWithOffset(v,0)]
-            sub = v
-        if isinstance(sub,ParseResults):
-            sub.__parent = wkref(self)
-
-    def __delitem__( self, i ):
-        if isinstance(i,(int,slice)):
-            mylen = len( self.__toklist )
-            del self.__toklist[i]
-
-            # convert int to slice
-            if isinstance(i, int):
-                if i < 0:
-                    i += mylen
-                i = slice(i, i+1)
-            # get removed indices
-            removed = list(range(*i.indices(mylen)))
-            removed.reverse()
-            # fixup indices in token dictionary
-            for name,occurrences in self.__tokdict.items():
-                for j in removed:
-                    for k, (value, position) in enumerate(occurrences):
-                        occurrences[k] = _ParseResultsWithOffset(value, position - (position > j))
-        else:
-            del self.__tokdict[i]
-
-    def __contains__( self, k ):
-        return k in self.__tokdict
-
-    def __len__( self ): return len( self.__toklist )
-    def __bool__(self): return ( not not self.__toklist )
-    __nonzero__ = __bool__
-    def __iter__( self ): return iter( self.__toklist )
-    def __reversed__( self ): return iter( self.__toklist[::-1] )
-    def _iterkeys( self ):
-        if hasattr(self.__tokdict, "iterkeys"):
-            return self.__tokdict.iterkeys()
-        else:
-            return iter(self.__tokdict)
-
-    def _itervalues( self ):
-        return (self[k] for k in self._iterkeys())
-
-    def _iteritems( self ):
-        return ((k, self[k]) for k in self._iterkeys())
-
-    if PY_3:
-        keys = _iterkeys
-        """Returns an iterator of all named result keys."""
-
-        values = _itervalues
-        """Returns an iterator of all named result values."""
-
-        items = _iteritems
-        """Returns an iterator of all named result key-value tuples."""
-
-    else:
-        iterkeys = _iterkeys
-        """Returns an iterator of all named result keys (Python 2.x only)."""
-
-        itervalues = _itervalues
-        """Returns an iterator of all named result values (Python 2.x only)."""
-
-        iteritems = _iteritems
-        """Returns an iterator of all named result key-value tuples (Python 2.x only)."""
-
-        def keys( self ):
-            """Returns all named result keys (as a list in Python 2.x, as an iterator in Python 3.x)."""
-            return list(self.iterkeys())
-
-        def values( self ):
-            """Returns all named result values (as a list in Python 2.x, as an iterator in Python 3.x)."""
-            return list(self.itervalues())
-
-        def items( self ):
-            """Returns all named result key-values (as a list of tuples in Python 2.x, as an iterator in Python 3.x)."""
-            return list(self.iteritems())
-
-    def haskeys( self ):
-        """Since keys() returns an iterator, this method is helpful in bypassing
-           code that looks for the existence of any defined results names."""
-        return bool(self.__tokdict)
-
-    def pop( self, *args, **kwargs):
-        """
-        Removes and returns item at specified index (default= ``last``).
-        Supports both ``list`` and ``dict`` semantics for ``pop()``. If
-        passed no argument or an integer argument, it will use ``list``
-        semantics and pop tokens from the list of parsed tokens. If passed
-        a non-integer argument (most likely a string), it will use ``dict``
-        semantics and pop the corresponding value from any defined results
-        names. A second default return value argument is supported, just as in
-        ``dict.pop()``.
-
-        Example::
-
-            def remove_first(tokens):
-                tokens.pop(0)
-            print(OneOrMore(Word(nums)).parseString("0 123 321")) # -> ['0', '123', '321']
-            print(OneOrMore(Word(nums)).addParseAction(remove_first).parseString("0 123 321")) # -> ['123', '321']
-
-            label = Word(alphas)
-            patt = label("LABEL") + OneOrMore(Word(nums))
-            print(patt.parseString("AAB 123 321").dump())
-
-            # Use pop() in a parse action to remove named result (note that corresponding value is not
-            # removed from list form of results)
-            def remove_LABEL(tokens):
-                tokens.pop("LABEL")
-                return tokens
-            patt.addParseAction(remove_LABEL)
-            print(patt.parseString("AAB 123 321").dump())
-
-        prints::
-
-            ['AAB', '123', '321']
-            - LABEL: AAB
-
-            ['AAB', '123', '321']
-        """
-        if not args:
-            args = [-1]
-        for k,v in kwargs.items():
-            if k == 'default':
-                args = (args[0], v)
-            else:
-                raise TypeError("pop() got an unexpected keyword argument '%s'" % k)
-        if (isinstance(args[0], int) or
-                        len(args) == 1 or
-                        args[0] in self):
-            index = args[0]
-            ret = self[index]
-            del self[index]
-            return ret
-        else:
-            defaultvalue = args[1]
-            return defaultvalue
-
-    def get(self, key, defaultValue=None):
-        """
-        Returns named result matching the given key, or if there is no
-        such name, then returns the given ``defaultValue`` or ``None`` if no
-        ``defaultValue`` is specified.
-
-        Similar to ``dict.get()``.
-
-        Example::
-
-            integer = Word(nums)
-            date_str = integer("year") + '/' + integer("month") + '/' + integer("day")
-
-            result = date_str.parseString("1999/12/31")
-            print(result.get("year")) # -> '1999'
-            print(result.get("hour", "not specified")) # -> 'not specified'
-            print(result.get("hour")) # -> None
-        """
-        if key in self:
-            return self[key]
-        else:
-            return defaultValue
-
-    def insert( self, index, insStr ):
-        """
-        Inserts new element at location index in the list of parsed tokens.
-
-        Similar to ``list.insert()``.
-
-        Example::
-
-            print(OneOrMore(Word(nums)).parseString("0 123 321")) # -> ['0', '123', '321']
-
-            # use a parse action to insert the parse location in the front of the parsed results
-            def insert_locn(locn, tokens):
-                tokens.insert(0, locn)
-            print(OneOrMore(Word(nums)).addParseAction(insert_locn).parseString("0 123 321")) # -> [0, '0', '123', '321']
-        """
-        self.__toklist.insert(index, insStr)
-        # fixup indices in token dictionary
-        for name,occurrences in self.__tokdict.items():
-            for k, (value, position) in enumerate(occurrences):
-                occurrences[k] = _ParseResultsWithOffset(value, position + (position > index))
-
-    def append( self, item ):
-        """
-        Add single element to end of ParseResults list of elements.
-
-        Example::
-
-            print(OneOrMore(Word(nums)).parseString("0 123 321")) # -> ['0', '123', '321']
-
-            # use a parse action to compute the sum of the parsed integers, and add it to the end
-            def append_sum(tokens):
-                tokens.append(sum(map(int, tokens)))
-            print(OneOrMore(Word(nums)).addParseAction(append_sum).parseString("0 123 321")) # -> ['0', '123', '321', 444]
-        """
-        self.__toklist.append(item)
-
-    def extend( self, itemseq ):
-        """
-        Add sequence of elements to end of ParseResults list of elements.
-
-        Example::
-
-            patt = OneOrMore(Word(alphas))
-
-            # use a parse action to append the reverse of the matched strings, to make a palindrome
-            def make_palindrome(tokens):
-                tokens.extend(reversed([t[::-1] for t in tokens]))
-                return ''.join(tokens)
-            print(patt.addParseAction(make_palindrome).parseString("lskdj sdlkjf lksd")) # -> 'lskdjsdlkjflksddsklfjkldsjdksl'
-        """
-        if isinstance(itemseq, ParseResults):
-            self += itemseq
-        else:
-            self.__toklist.extend(itemseq)
-
-    def clear( self ):
-        """
-        Clear all elements and results names.
-        """
-        del self.__toklist[:]
-        self.__tokdict.clear()
-
-    def __getattr__( self, name ):
-        try:
-            return self[name]
-        except KeyError:
-            return ""
-
-        if name in self.__tokdict:
-            if name not in self.__accumNames:
-                return self.__tokdict[name][-1][0]
-            else:
-                return ParseResults([ v[0] for v in self.__tokdict[name] ])
-        else:
-            return ""
-
-    def __add__( self, other ):
-        ret = self.copy()
-        ret += other
-        return ret
-
-    def __iadd__( self, other ):
-        if other.__tokdict:
-            offset = len(self.__toklist)
-            addoffset = lambda a: offset if a<0 else a+offset
-            otheritems = other.__tokdict.items()
-            otherdictitems = [(k, _ParseResultsWithOffset(v[0],addoffset(v[1])) )
-                                for (k,vlist) in otheritems for v in vlist]
-            for k,v in otherdictitems:
-                self[k] = v
-                if isinstance(v[0],ParseResults):
-                    v[0].__parent = wkref(self)
-
-        self.__toklist += other.__toklist
-        self.__accumNames.update( other.__accumNames )
-        return self
-
-    def __radd__(self, other):
-        if isinstance(other,int) and other == 0:
-            # useful for merging many ParseResults using sum() builtin
-            return self.copy()
-        else:
-            # this may raise a TypeError - so be it
-            return other + self
-
-    def __repr__( self ):
-        return "(%s, %s)" % ( repr( self.__toklist ), repr( self.__tokdict ) )
-
-    def __str__( self ):
-        return '[' + ', '.join(_ustr(i) if isinstance(i, ParseResults) else repr(i) for i in self.__toklist) + ']'
-
-    def _asStringList( self, sep='' ):
-        out = []
-        for item in self.__toklist:
-            if out and sep:
-                out.append(sep)
-            if isinstance( item, ParseResults ):
-                out += item._asStringList()
-            else:
-                out.append( _ustr(item) )
-        return out
-
-    def asList( self ):
-        """
-        Returns the parse results as a nested list of matching tokens, all converted to strings.
-
-        Example::
-
-            patt = OneOrMore(Word(alphas))
-            result = patt.parseString("sldkj lsdkj sldkj")
-            # even though the result prints in string-like form, it is actually a pyparsing ParseResults
-            print(type(result), result) # -> <class 'pyparsing.ParseResults'> ['sldkj', 'lsdkj', 'sldkj']
-
-            # Use asList() to create an actual list
-            result_list = result.asList()
-            print(type(result_list), result_list) # -> <class 'list'> ['sldkj', 'lsdkj', 'sldkj']
-        """
-        return [res.asList() if isinstance(res,ParseResults) else res for res in self.__toklist]
-
-    def asDict( self ):
-        """
-        Returns the named parse results as a nested dictionary.
-
-        Example::
-
-            integer = Word(nums)
-            date_str = integer("year") + '/' + integer("month") + '/' + integer("day")
-
-            result = date_str.parseString('12/31/1999')
-            print(type(result), repr(result)) # -> <class 'pyparsing.ParseResults'> (['12', '/', '31', '/', '1999'], {'day': [('1999', 4)], 'year': [('12', 0)], 'month': [('31', 2)]})
-
-            result_dict = result.asDict()
-            print(type(result_dict), repr(result_dict)) # -> <class 'dict'> {'day': '1999', 'year': '12', 'month': '31'}
-
-            # even though a ParseResults supports dict-like access, sometime you just need to have a dict
-            import json
-            print(json.dumps(result)) # -> Exception: TypeError: ... is not JSON serializable
-            print(json.dumps(result.asDict())) # -> {"month": "31", "day": "1999", "year": "12"}
-        """
-        if PY_3:
-            item_fn = self.items
-        else:
-            item_fn = self.iteritems
-
-        def toItem(obj):
-            if isinstance(obj, ParseResults):
-                if obj.haskeys():
-                    return obj.asDict()
-                else:
-                    return [toItem(v) for v in obj]
-            else:
-                return obj
-
-        return dict((k,toItem(v)) for k,v in item_fn())
-
-    def copy( self ):
-        """
-        Returns a new copy of a :class:`ParseResults` object.
-        """
-        ret = ParseResults( self.__toklist )
-        ret.__tokdict = dict(self.__tokdict.items())
-        ret.__parent = self.__parent
-        ret.__accumNames.update( self.__accumNames )
-        ret.__name = self.__name
-        return ret
-
-    def asXML( self, doctag=None, namedItemsOnly=False, indent="", formatted=True ):
-        """
-        (Deprecated) Returns the parse results as XML. Tags are created for tokens and lists that have defined results names.
-        """
-        nl = "\n"
-        out = []
-        namedItems = dict((v[1],k) for (k,vlist) in self.__tokdict.items()
-                                                            for v in vlist)
-        nextLevelIndent = indent + "  "
-
-        # collapse out indents if formatting is not desired
-        if not formatted:
-            indent = ""
-            nextLevelIndent = ""
-            nl = ""
-
-        selfTag = None
-        if doctag is not None:
-            selfTag = doctag
-        else:
-            if self.__name:
-                selfTag = self.__name
-
-        if not selfTag:
-            if namedItemsOnly:
-                return ""
-            else:
-                selfTag = "ITEM"
-
-        out += [ nl, indent, "<", selfTag, ">" ]
-
-        for i,res in enumerate(self.__toklist):
-            if isinstance(res,ParseResults):
-                if i in namedItems:
-                    out += [ res.asXML(namedItems[i],
-                                        namedItemsOnly and doctag is None,
-                                        nextLevelIndent,
-                                        formatted)]
-                else:
-                    out += [ res.asXML(None,
-                                        namedItemsOnly and doctag is None,
-                                        nextLevelIndent,
-                                        formatted)]
-            else:
-                # individual token, see if there is a name for it
-                resTag = None
-                if i in namedItems:
-                    resTag = namedItems[i]
-                if not resTag:
-                    if namedItemsOnly:
-                        continue
-                    else:
-                        resTag = "ITEM"
-                xmlBodyText = _xml_escape(_ustr(res))
-                out += [ nl, nextLevelIndent, "<", resTag, ">",
-                                                xmlBodyText,
-                                                "</", resTag, ">" ]
-
-        out += [ nl, indent, "</", selfTag, ">" ]
-        return "".join(out)
-
-    def __lookup(self,sub):
-        for k,vlist in self.__tokdict.items():
-            for v,loc in vlist:
-                if sub is v:
-                    return k
-        return None
-
-    def getName(self):
-        r"""
-        Returns the results name for this token expression. Useful when several
-        different expressions might match at a particular location.
-
-        Example::
-
-            integer = Word(nums)
-            ssn_expr = Regex(r"\d\d\d-\d\d-\d\d\d\d")
-            house_number_expr = Suppress('#') + Word(nums, alphanums)
-            user_data = (Group(house_number_expr)("house_number")
-                        | Group(ssn_expr)("ssn")
-                        | Group(integer)("age"))
-            user_info = OneOrMore(user_data)
-
-            result = user_info.parseString("22 111-22-3333 #221B")
-            for item in result:
-                print(item.getName(), ':', item[0])
-
-        prints::
-
-            age : 22
-            ssn : 111-22-3333
-            house_number : 221B
-        """
-        if self.__name:
-            return self.__name
-        elif self.__parent:
-            par = self.__parent()
-            if par:
-                return par.__lookup(self)
-            else:
-                return None
-        elif (len(self) == 1 and
-               len(self.__tokdict) == 1 and
-               next(iter(self.__tokdict.values()))[0][1] in (0,-1)):
-            return next(iter(self.__tokdict.keys()))
-        else:
-            return None
-
-    def dump(self, indent='', depth=0, full=True):
-        """
-        Diagnostic method for listing out the contents of
-        a :class:`ParseResults`. Accepts an optional ``indent`` argument so
-        that this string can be embedded in a nested display of other data.
-
-        Example::
-
-            integer = Word(nums)
-            date_str = integer("year") + '/' + integer("month") + '/' + integer("day")
-
-            result = date_str.parseString('12/31/1999')
-            print(result.dump())
-
-        prints::
-
-            ['12', '/', '31', '/', '1999']
-            - day: 1999
-            - month: 31
-            - year: 12
-        """
-        out = []
-        NL = '\n'
-        out.append( indent+_ustr(self.asList()) )
-        if full:
-            if self.haskeys():
-                items = sorted((str(k), v) for k,v in self.items())
-                for k,v in items:
-                    if out:
-                        out.append(NL)
-                    out.append( "%s%s- %s: " % (indent,('  '*depth), k) )
-                    if isinstance(v,ParseResults):
-                        if v:
-                            out.append( v.dump(indent,depth+1) )
-                        else:
-                            out.append(_ustr(v))
-                    else:
-                        out.append(repr(v))
-            elif any(isinstance(vv,ParseResults) for vv in self):
-                v = self
-                for i,vv in enumerate(v):
-                    if isinstance(vv,ParseResults):
-                        out.append("\n%s%s[%d]:\n%s%s%s" % (indent,('  '*(depth)),i,indent,('  '*(depth+1)),vv.dump(indent,depth+1) ))
-                    else:
-                        out.append("\n%s%s[%d]:\n%s%s%s" % (indent,('  '*(depth)),i,indent,('  '*(depth+1)),_ustr(vv)))
-
-        return "".join(out)
-
-    def pprint(self, *args, **kwargs):
-        """
-        Pretty-printer for parsed results as a list, using the
-        `pprint <https://docs.python.org/3/library/pprint.html>`_ module.
-        Accepts additional positional or keyword args as defined for
-        `pprint.pprint <https://docs.python.org/3/library/pprint.html#pprint.pprint>`_ .
-
-        Example::
-
-            ident = Word(alphas, alphanums)
-            num = Word(nums)
-            func = Forward()
-            term = ident | num | Group('(' + func + ')')
-            func <<= ident + Group(Optional(delimitedList(term)))
-            result = func.parseString("fna a,b,(fnb c,d,200),100")
-            result.pprint(width=40)
-
-        prints::
-
-            ['fna',
-             ['a',
-              'b',
-              ['(', 'fnb', ['c', 'd', '200'], ')'],
-              '100']]
-        """
-        pprint.pprint(self.asList(), *args, **kwargs)
-
-    # add support for pickle protocol
-    def __getstate__(self):
-        return ( self.__toklist,
-                 ( self.__tokdict.copy(),
-                   self.__parent is not None and self.__parent() or None,
-                   self.__accumNames,
-                   self.__name ) )
-
-    def __setstate__(self,state):
-        self.__toklist = state[0]
-        (self.__tokdict,
-         par,
-         inAccumNames,
-         self.__name) = state[1]
-        self.__accumNames = {}
-        self.__accumNames.update(inAccumNames)
-        if par is not None:
-            self.__parent = wkref(par)
-        else:
-            self.__parent = None
-
-    def __getnewargs__(self):
-        return self.__toklist, self.__name, self.__asList, self.__modal
-
-    def __dir__(self):
-        return (dir(type(self)) + list(self.keys()))
-
-MutableMapping.register(ParseResults)
-
-def col (loc,strg):
-    """Returns current column within a string, counting newlines as line separators.
-   The first column is number 1.
-
-   Note: the default parsing behavior is to expand tabs in the input string
-   before starting the parsing process.  See
-   :class:`ParserElement.parseString` for more
-   information on parsing strings containing ``<TAB>`` s, and suggested
-   methods to maintain a consistent view of the parsed string, the parse
-   location, and line and column positions within the parsed string.
-   """
-    s = strg
-    return 1 if 0<loc<len(s) and s[loc-1] == '\n' else loc - s.rfind("\n", 0, loc)
-
-def lineno(loc,strg):
-    """Returns current line number within a string, counting newlines as line separators.
-    The first line is number 1.
-
-    Note - the default parsing behavior is to expand tabs in the input string
-    before starting the parsing process.  See :class:`ParserElement.parseString`
-    for more information on parsing strings containing ``<TAB>`` s, and
-    suggested methods to maintain a consistent view of the parsed string, the
-    parse location, and line and column positions within the parsed string.
-    """
-    return strg.count("\n",0,loc) + 1
-
-def line( loc, strg ):
-    """Returns the line of text containing loc within a string, counting newlines as line separators.
-       """
-    lastCR = strg.rfind("\n", 0, loc)
-    nextCR = strg.find("\n", loc)
-    if nextCR >= 0:
-        return strg[lastCR+1:nextCR]
-    else:
-        return strg[lastCR+1:]
-
-def _defaultStartDebugAction( instring, loc, expr ):
-    print (("Match " + _ustr(expr) + " at loc " + _ustr(loc) + "(%d,%d)" % ( lineno(loc,instring), col(loc,instring) )))
-
-def _defaultSuccessDebugAction( instring, startloc, endloc, expr, toks ):
-    print ("Matched " + _ustr(expr) + " -> " + str(toks.asList()))
-
-def _defaultExceptionDebugAction( instring, loc, expr, exc ):
-    print ("Exception raised:" + _ustr(exc))
-
-def nullDebugAction(*args):
-    """'Do-nothing' debug action, to suppress debugging output during parsing."""
-    pass
-
-# Only works on Python 3.x - nonlocal is toxic to Python 2 installs
-#~ 'decorator to trim function calls to match the arity of the target'
-#~ def _trim_arity(func, maxargs=3):
-    #~ if func in singleArgBuiltins:
-        #~ return lambda s,l,t: func(t)
-    #~ limit = 0
-    #~ foundArity = False
-    #~ def wrapper(*args):
-        #~ nonlocal limit,foundArity
-        #~ while 1:
-            #~ try:
-                #~ ret = func(*args[limit:])
-                #~ foundArity = True
-                #~ return ret
-            #~ except TypeError:
-                #~ if limit == maxargs or foundArity:
-                    #~ raise
-                #~ limit += 1
-                #~ continue
-    #~ return wrapper
-
-# this version is Python 2.x-3.x cross-compatible
-'decorator to trim function calls to match the arity of the target'
-def _trim_arity(func, maxargs=2):
-    if func in singleArgBuiltins:
-        return lambda s,l,t: func(t)
-    limit = [0]
-    foundArity = [False]
-
-    # traceback return data structure changed in Py3.5 - normalize back to plain tuples
-    if system_version[:2] >= (3,5):
-        def extract_stack(limit=0):
-            # special handling for Python 3.5.0 - extra deep call stack by 1
-            offset = -3 if system_version == (3,5,0) else -2
-            frame_summary = traceback.extract_stack(limit=-offset+limit-1)[offset]
-            return [frame_summary[:2]]
-        def extract_tb(tb, limit=0):
-            frames = traceback.extract_tb(tb, limit=limit)
-            frame_summary = frames[-1]
-            return [frame_summary[:2]]
-    else:
-        extract_stack = traceback.extract_stack
-        extract_tb = traceback.extract_tb
-
-    # synthesize what would be returned by traceback.extract_stack at the call to
-    # user's parse action 'func', so that we don't incur call penalty at parse time
-
-    LINE_DIFF = 6
-    # IF ANY CODE CHANGES, EVEN JUST COMMENTS OR BLANK LINES, BETWEEN THE NEXT LINE AND
-    # THE CALL TO FUNC INSIDE WRAPPER, LINE_DIFF MUST BE MODIFIED!!!!
-    this_line = extract_stack(limit=2)[-1]
-    pa_call_line_synth = (this_line[0], this_line[1]+LINE_DIFF)
-
-    def wrapper(*args):
-        while 1:
-            try:
-                ret = func(*args[limit[0]:])
-                foundArity[0] = True
-                return ret
-            except TypeError:
-                # re-raise TypeErrors if they did not come from our arity testing
-                if foundArity[0]:
-                    raise
-                else:
-                    try:
-                        tb = sys.exc_info()[-1]
-                        if not extract_tb(tb, limit=2)[-1][:2] == pa_call_line_synth:
-                            raise
-                    finally:
-                        del tb
-
-                if limit[0] <= maxargs:
-                    limit[0] += 1
-                    continue
-                raise
-
-    # copy func name to wrapper for sensible debug output
-    func_name = "<parse action>"
-    try:
-        func_name = getattr(func, '__name__',
-                            getattr(func, '__class__').__name__)
-    except Exception:
-        func_name = str(func)
-    wrapper.__name__ = func_name
-
-    return wrapper
-
-class ParserElement(object):
-    """Abstract base level parser element class."""
-    DEFAULT_WHITE_CHARS = " \n\t\r"
-    verbose_stacktrace = False
-
-    @staticmethod
-    def setDefaultWhitespaceChars( chars ):
-        r"""
-        Overrides the default whitespace chars
-
-        Example::
-
-            # default whitespace chars are space, <TAB> and newline
-            OneOrMore(Word(alphas)).parseString("abc def\nghi jkl")  # -> ['abc', 'def', 'ghi', 'jkl']
-
-            # change to just treat newline as significant
-            ParserElement.setDefaultWhitespaceChars(" \t")
-            OneOrMore(Word(alphas)).parseString("abc def\nghi jkl")  # -> ['abc', 'def']
-        """
-        ParserElement.DEFAULT_WHITE_CHARS = chars
-
-    @staticmethod
-    def inlineLiteralsUsing(cls):
-        """
-        Set class to be used for inclusion of string literals into a parser.
-
-        Example::
-
-            # default literal class used is Literal
-            integer = Word(nums)
-            date_str = integer("year") + '/' + integer("month") + '/' + integer("day")
-
-            date_str.parseString("1999/12/31")  # -> ['1999', '/', '12', '/', '31']
-
-
-            # change to Suppress
-            ParserElement.inlineLiteralsUsing(Suppress)
-            date_str = integer("year") + '/' + integer("month") + '/' + integer("day")
-
-            date_str.parseString("1999/12/31")  # -> ['1999', '12', '31']
-        """
-        ParserElement._literalStringClass = cls
-
-    def __init__( self, savelist=False ):
-        self.parseAction = list()
-        self.failAction = None
-        #~ self.name = "<unknown>"  # don't define self.name, let subclasses try/except upcall
-        self.strRepr = None
-        self.resultsName = None
-        self.saveAsList = savelist
-        self.skipWhitespace = True
-        self.whiteChars = set(ParserElement.DEFAULT_WHITE_CHARS)
-        self.copyDefaultWhiteChars = True
-        self.mayReturnEmpty = False # used when checking for left-recursion
-        self.keepTabs = False
-        self.ignoreExprs = list()
-        self.debug = False
-        self.streamlined = False
-        self.mayIndexError = True # used to optimize exception handling for subclasses that don't advance parse index
-        self.errmsg = ""
-        self.modalResults = True # used to mark results names as modal (report only last) or cumulative (list all)
-        self.debugActions = ( None, None, None ) #custom debug actions
-        self.re = None
-        self.callPreparse = True # used to avoid redundant calls to preParse
-        self.callDuringTry = False
-
-    def copy( self ):
-        """
-        Make a copy of this :class:`ParserElement`.  Useful for defining
-        different parse actions for the same parsing pattern, using copies of
-        the original parse element.
-
-        Example::
-
-            integer = Word(nums).setParseAction(lambda toks: int(toks[0]))
-            integerK = integer.copy().addParseAction(lambda toks: toks[0]*1024) + Suppress("K")
-            integerM = integer.copy().addParseAction(lambda toks: toks[0]*1024*1024) + Suppress("M")
-
-            print(OneOrMore(integerK | integerM | integer).parseString("5K 100 640K 256M"))
-
-        prints::
-
-            [5120, 100, 655360, 268435456]
-
-        Equivalent form of ``expr.copy()`` is just ``expr()``::
-
-            integerM = integer().addParseAction(lambda toks: toks[0]*1024*1024) + Suppress("M")
-        """
-        cpy = copy.copy( self )
-        cpy.parseAction = self.parseAction[:]
-        cpy.ignoreExprs = self.ignoreExprs[:]
-        if self.copyDefaultWhiteChars:
-            cpy.whiteChars = ParserElement.DEFAULT_WHITE_CHARS
-        return cpy
-
-    def setName( self, name ):
-        """
-        Define name for this expression, makes debugging and exception messages clearer.
-
-        Example::
-
-            Word(nums).parseString("ABC")  # -> Exception: Expected W:(0123...) (at char 0), (line:1, col:1)
-            Word(nums).setName("integer").parseString("ABC")  # -> Exception: Expected integer (at char 0), (line:1, col:1)
-        """
-        self.name = name
-        self.errmsg = "Expected " + self.name
-        if hasattr(self,"exception"):
-            self.exception.msg = self.errmsg
-        return self
-
-    def setResultsName( self, name, listAllMatches=False ):
-        """
-        Define name for referencing matching tokens as a nested attribute
-        of the returned parse results.
-        NOTE: this returns a *copy* of the original :class:`ParserElement` object;
-        this is so that the client can define a basic element, such as an
-        integer, and reference it in multiple places with different names.
-
-        You can also set results names using the abbreviated syntax,
-        ``expr("name")`` in place of ``expr.setResultsName("name")``
-        - see :class:`__call__`.
-
-        Example::
-
-            date_str = (integer.setResultsName("year") + '/'
-                        + integer.setResultsName("month") + '/'
-                        + integer.setResultsName("day"))
-
-            # equivalent form:
-            date_str = integer("year") + '/' + integer("month") + '/' + integer("day")
-        """
-        newself = self.copy()
-        if name.endswith("*"):
-            name = name[:-1]
-            listAllMatches=True
-        newself.resultsName = name
-        newself.modalResults = not listAllMatches
-        return newself
-
-    def setBreak(self,breakFlag = True):
-        """Method to invoke the Python pdb debugger when this element is
-           about to be parsed. Set ``breakFlag`` to True to enable, False to
-           disable.
-        """
-        if breakFlag:
-            _parseMethod = self._parse
-            def breaker(instring, loc, doActions=True, callPreParse=True):
-                import pdb
-                pdb.set_trace()
-                return _parseMethod( instring, loc, doActions, callPreParse )
-            breaker._originalParseMethod = _parseMethod
-            self._parse = breaker
-        else:
-            if hasattr(self._parse,"_originalParseMethod"):
-                self._parse = self._parse._originalParseMethod
-        return self
-
-    def setParseAction( self, *fns, **kwargs ):
-        """
-        Define one or more actions to perform when successfully matching parse element definition.
-        Parse action fn is a callable method with 0-3 arguments, called as ``fn(s,loc,toks)`` ,
-        ``fn(loc,toks)`` , ``fn(toks)`` , or just ``fn()`` , where:
-
-        - s   = the original string being parsed (see note below)
-        - loc = the location of the matching substring
-        - toks = a list of the matched tokens, packaged as a :class:`ParseResults` object
-
-        If the functions in fns modify the tokens, they can return them as the return
-        value from fn, and the modified list of tokens will replace the original.
-        Otherwise, fn does not need to return any value.
-
-        Optional keyword arguments:
-        - callDuringTry = (default= ``False`` ) indicate if parse action should be run during lookaheads and alternate testing
-
-        Note: the default parsing behavior is to expand tabs in the input string
-        before starting the parsing process.  See :class:`parseString for more
-        information on parsing strings containing ``<TAB>`` s, and suggested
-        methods to maintain a consistent view of the parsed string, the parse
-        location, and line and column positions within the parsed string.
-
-        Example::
-
-            integer = Word(nums)
-            date_str = integer + '/' + integer + '/' + integer
-
-            date_str.parseString("1999/12/31")  # -> ['1999', '/', '12', '/', '31']
-
-            # use parse action to convert to ints at parse time
-            integer = Word(nums).setParseAction(lambda toks: int(toks[0]))
-            date_str = integer + '/' + integer + '/' + integer
-
-            # note that integer fields are now ints, not strings
-            date_str.parseString("1999/12/31")  # -> [1999, '/', 12, '/', 31]
-        """
-        self.parseAction = list(map(_trim_arity, list(fns)))
-        self.callDuringTry = kwargs.get("callDuringTry", False)
-        return self
-
-    def addParseAction( self, *fns, **kwargs ):
-        """
-        Add one or more parse actions to expression's list of parse actions. See :class:`setParseAction`.
-
-        See examples in :class:`copy`.
-        """
-        self.parseAction += list(map(_trim_arity, list(fns)))
-        self.callDuringTry = self.callDuringTry or kwargs.get("callDuringTry", False)
-        return self
-
-    def addCondition(self, *fns, **kwargs):
-        """Add a boolean predicate function to expression's list of parse actions. See
-        :class:`setParseAction` for function call signatures. Unlike ``setParseAction``,
-        functions passed to ``addCondition`` need to return boolean success/fail of the condition.
-
-        Optional keyword arguments:
-        - message = define a custom message to be used in the raised exception
-        - fatal   = if True, will raise ParseFatalException to stop parsing immediately; otherwise will raise ParseException
-
-        Example::
-
-            integer = Word(nums).setParseAction(lambda toks: int(toks[0]))
-            year_int = integer.copy()
-            year_int.addCondition(lambda toks: toks[0] >= 2000, message="Only support years 2000 and later")
-            date_str = year_int + '/' + integer + '/' + integer
-
-            result = date_str.parseString("1999/12/31")  # -> Exception: Only support years 2000 and later (at char 0), (line:1, col:1)
-        """
-        msg = kwargs.get("message", "failed user-defined condition")
-        exc_type = ParseFatalException if kwargs.get("fatal", False) else ParseException
-        for fn in fns:
-            fn = _trim_arity(fn)
-            def pa(s,l,t):
-                if not bool(fn(s,l,t)):
-                    raise exc_type(s,l,msg)
-            self.parseAction.append(pa)
-        self.callDuringTry = self.callDuringTry or kwargs.get("callDuringTry", False)
-        return self
-
-    def setFailAction( self, fn ):
-        """Define action to perform if parsing fails at this expression.
-           Fail acton fn is a callable function that takes the arguments
-           ``fn(s,loc,expr,err)`` where:
-           - s = string being parsed
-           - loc = location where expression match was attempted and failed
-           - expr = the parse expression that failed
-           - err = the exception thrown
-           The function returns no value.  It may throw :class:`ParseFatalException`
-           if it is desired to stop parsing immediately."""
-        self.failAction = fn
-        return self
-
-    def _skipIgnorables( self, instring, loc ):
-        exprsFound = True
-        while exprsFound:
-            exprsFound = False
-            for e in self.ignoreExprs:
-                try:
-                    while 1:
-                        loc,dummy = e._parse( instring, loc )
-                        exprsFound = True
-                except ParseException:
-                    pass
-        return loc
-
-    def preParse( self, instring, loc ):
-        if self.ignoreExprs:
-            loc = self._skipIgnorables( instring, loc )
-
-        if self.skipWhitespace:
-            wt = self.whiteChars
-            instrlen = len(instring)
-            while loc < instrlen and instring[loc] in wt:
-                loc += 1
-
-        return loc
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        return loc, []
-
-    def postParse( self, instring, loc, tokenlist ):
-        return tokenlist
-
-    #~ @profile
-    def _parseNoCache( self, instring, loc, doActions=True, callPreParse=True ):
-        debugging = ( self.debug ) #and doActions )
-
-        if debugging or self.failAction:
-            #~ print ("Match",self,"at loc",loc,"(%d,%d)" % ( lineno(loc,instring), col(loc,instring) ))
-            if (self.debugActions[0] ):
-                self.debugActions[0]( instring, loc, self )
-            if callPreParse and self.callPreparse:
-                preloc = self.preParse( instring, loc )
-            else:
-                preloc = loc
-            tokensStart = preloc
-            try:
-                try:
-                    loc,tokens = self.parseImpl( instring, preloc, doActions )
-                except IndexError:
-                    raise ParseException( instring, len(instring), self.errmsg, self )
-            except ParseBaseException as err:
-                #~ print ("Exception raised:", err)
-                if self.debugActions[2]:
-                    self.debugActions[2]( instring, tokensStart, self, err )
-                if self.failAction:
-                    self.failAction( instring, tokensStart, self, err )
-                raise
-        else:
-            if callPreParse and self.callPreparse:
-                preloc = self.preParse( instring, loc )
-            else:
-                preloc = loc
-            tokensStart = preloc
-            if self.mayIndexError or preloc >= len(instring):
-                try:
-                    loc,tokens = self.parseImpl( instring, preloc, doActions )
-                except IndexError:
-                    raise ParseException( instring, len(instring), self.errmsg, self )
-            else:
-                loc,tokens = self.parseImpl( instring, preloc, doActions )
-
-        tokens = self.postParse( instring, loc, tokens )
-
-        retTokens = ParseResults( tokens, self.resultsName, asList=self.saveAsList, modal=self.modalResults )
-        if self.parseAction and (doActions or self.callDuringTry):
-            if debugging:
-                try:
-                    for fn in self.parseAction:
-                        try:
-                            tokens = fn( instring, tokensStart, retTokens )
-                        except IndexError as parse_action_exc:
-                            exc = ParseException("exception raised in parse action")
-                            exc.__cause__ = parse_action_exc
-                            raise exc
-
-                        if tokens is not None and tokens is not retTokens:
-                            retTokens = ParseResults( tokens,
-                                                      self.resultsName,
-                                                      asList=self.saveAsList and isinstance(tokens,(ParseResults,list)),
-                                                      modal=self.modalResults )
-                except ParseBaseException as err:
-                    #~ print "Exception raised in user parse action:", err
-                    if (self.debugActions[2] ):
-                        self.debugActions[2]( instring, tokensStart, self, err )
-                    raise
-            else:
-                for fn in self.parseAction:
-                    try:
-                        tokens = fn( instring, tokensStart, retTokens )
-                    except IndexError as parse_action_exc:
-                        exc = ParseException("exception raised in parse action")
-                        exc.__cause__ = parse_action_exc
-                        raise exc
-
-                    if tokens is not None and tokens is not retTokens:
-                        retTokens = ParseResults( tokens,
-                                                  self.resultsName,
-                                                  asList=self.saveAsList and isinstance(tokens,(ParseResults,list)),
-                                                  modal=self.modalResults )
-        if debugging:
-            #~ print ("Matched",self,"->",retTokens.asList())
-            if (self.debugActions[1] ):
-                self.debugActions[1]( instring, tokensStart, loc, self, retTokens )
-
-        return loc, retTokens
-
-    def tryParse( self, instring, loc ):
-        try:
-            return self._parse( instring, loc, doActions=False )[0]
-        except ParseFatalException:
-            raise ParseException( instring, loc, self.errmsg, self)
-
-    def canParseNext(self, instring, loc):
-        try:
-            self.tryParse(instring, loc)
-        except (ParseException, IndexError):
-            return False
-        else:
-            return True
-
-    class _UnboundedCache(object):
-        def __init__(self):
-            cache = {}
-            self.not_in_cache = not_in_cache = object()
-
-            def get(self, key):
-                return cache.get(key, not_in_cache)
-
-            def set(self, key, value):
-                cache[key] = value
-
-            def clear(self):
-                cache.clear()
-
-            def cache_len(self):
-                return len(cache)
-
-            self.get = types.MethodType(get, self)
-            self.set = types.MethodType(set, self)
-            self.clear = types.MethodType(clear, self)
-            self.__len__ = types.MethodType(cache_len, self)
-
-    if _OrderedDict is not None:
-        class _FifoCache(object):
-            def __init__(self, size):
-                self.not_in_cache = not_in_cache = object()
-
-                cache = _OrderedDict()
-
-                def get(self, key):
-                    return cache.get(key, not_in_cache)
-
-                def set(self, key, value):
-                    cache[key] = value
-                    while len(cache) > size:
-                        try:
-                            cache.popitem(False)
-                        except KeyError:
-                            pass
-
-                def clear(self):
-                    cache.clear()
-
-                def cache_len(self):
-                    return len(cache)
-
-                self.get = types.MethodType(get, self)
-                self.set = types.MethodType(set, self)
-                self.clear = types.MethodType(clear, self)
-                self.__len__ = types.MethodType(cache_len, self)
-
-    else:
-        class _FifoCache(object):
-            def __init__(self, size):
-                self.not_in_cache = not_in_cache = object()
-
-                cache = {}
-                key_fifo = collections.deque([], size)
-
-                def get(self, key):
-                    return cache.get(key, not_in_cache)
-
-                def set(self, key, value):
-                    cache[key] = value
-                    while len(key_fifo) > size:
-                        cache.pop(key_fifo.popleft(), None)
-                    key_fifo.append(key)
-
-                def clear(self):
-                    cache.clear()
-                    key_fifo.clear()
-
-                def cache_len(self):
-                    return len(cache)
-
-                self.get = types.MethodType(get, self)
-                self.set = types.MethodType(set, self)
-                self.clear = types.MethodType(clear, self)
-                self.__len__ = types.MethodType(cache_len, self)
-
-    # argument cache for optimizing repeated calls when backtracking through recursive expressions
-    packrat_cache = {} # this is set later by enabledPackrat(); this is here so that resetCache() doesn't fail
-    packrat_cache_lock = RLock()
-    packrat_cache_stats = [0, 0]
-
-    # this method gets repeatedly called during backtracking with the same arguments -
-    # we can cache these arguments and save ourselves the trouble of re-parsing the contained expression
-    def _parseCache( self, instring, loc, doActions=True, callPreParse=True ):
-        HIT, MISS = 0, 1
-        lookup = (self, instring, loc, callPreParse, doActions)
-        with ParserElement.packrat_cache_lock:
-            cache = ParserElement.packrat_cache
-            value = cache.get(lookup)
-            if value is cache.not_in_cache:
-                ParserElement.packrat_cache_stats[MISS] += 1
-                try:
-                    value = self._parseNoCache(instring, loc, doActions, callPreParse)
-                except ParseBaseException as pe:
-                    # cache a copy of the exception, without the traceback
-                    cache.set(lookup, pe.__class__(*pe.args))
-                    raise
-                else:
-                    cache.set(lookup, (value[0], value[1].copy()))
-                    return value
-            else:
-                ParserElement.packrat_cache_stats[HIT] += 1
-                if isinstance(value, Exception):
-                    raise value
-                return (value[0], value[1].copy())
-
-    _parse = _parseNoCache
-
-    @staticmethod
-    def resetCache():
-        ParserElement.packrat_cache.clear()
-        ParserElement.packrat_cache_stats[:] = [0] * len(ParserElement.packrat_cache_stats)
-
-    _packratEnabled = False
-    @staticmethod
-    def enablePackrat(cache_size_limit=128):
-        """Enables "packrat" parsing, which adds memoizing to the parsing logic.
-           Repeated parse attempts at the same string location (which happens
-           often in many complex grammars) can immediately return a cached value,
-           instead of re-executing parsing/validating code.  Memoizing is done of
-           both valid results and parsing exceptions.
-
-           Parameters:
-
-           - cache_size_limit - (default= ``128``) - if an integer value is provided
-             will limit the size of the packrat cache; if None is passed, then
-             the cache size will be unbounded; if 0 is passed, the cache will
-             be effectively disabled.
-
-           This speedup may break existing programs that use parse actions that
-           have side-effects.  For this reason, packrat parsing is disabled when
-           you first import pyparsing.  To activate the packrat feature, your
-           program must call the class method :class:`ParserElement.enablePackrat`.
-           For best results, call ``enablePackrat()`` immediately after
-           importing pyparsing.
-
-           Example::
-
-               from pip._vendor import pyparsing
-               pyparsing.ParserElement.enablePackrat()
-        """
-        if not ParserElement._packratEnabled:
-            ParserElement._packratEnabled = True
-            if cache_size_limit is None:
-                ParserElement.packrat_cache = ParserElement._UnboundedCache()
-            else:
-                ParserElement.packrat_cache = ParserElement._FifoCache(cache_size_limit)
-            ParserElement._parse = ParserElement._parseCache
-
-    def parseString( self, instring, parseAll=False ):
-        """
-        Execute the parse expression with the given string.
-        This is the main interface to the client code, once the complete
-        expression has been built.
-
-        If you want the grammar to require that the entire input string be
-        successfully parsed, then set ``parseAll`` to True (equivalent to ending
-        the grammar with ``StringEnd()``).
-
-        Note: ``parseString`` implicitly calls ``expandtabs()`` on the input string,
-        in order to report proper column numbers in parse actions.
-        If the input string contains tabs and
-        the grammar uses parse actions that use the ``loc`` argument to index into the
-        string being parsed, you can ensure you have a consistent view of the input
-        string by:
-
-        - calling ``parseWithTabs`` on your grammar before calling ``parseString``
-          (see :class:`parseWithTabs`)
-        - define your parse action using the full ``(s,loc,toks)`` signature, and
-          reference the input string using the parse action's ``s`` argument
-        - explictly expand the tabs in your input string before calling
-          ``parseString``
-
-        Example::
-
-            Word('a').parseString('aaaaabaaa')  # -> ['aaaaa']
-            Word('a').parseString('aaaaabaaa', parseAll=True)  # -> Exception: Expected end of text
-        """
-        ParserElement.resetCache()
-        if not self.streamlined:
-            self.streamline()
-            #~ self.saveAsList = True
-        for e in self.ignoreExprs:
-            e.streamline()
-        if not self.keepTabs:
-            instring = instring.expandtabs()
-        try:
-            loc, tokens = self._parse( instring, 0 )
-            if parseAll:
-                loc = self.preParse( instring, loc )
-                se = Empty() + StringEnd()
-                se._parse( instring, loc )
-        except ParseBaseException as exc:
-            if ParserElement.verbose_stacktrace:
-                raise
-            else:
-                # catch and re-raise exception from here, clears out pyparsing internal stack trace
-                raise exc
-        else:
-            return tokens
-
-    def scanString( self, instring, maxMatches=_MAX_INT, overlap=False ):
-        """
-        Scan the input string for expression matches.  Each match will return the
-        matching tokens, start location, and end location.  May be called with optional
-        ``maxMatches`` argument, to clip scanning after 'n' matches are found.  If
-        ``overlap`` is specified, then overlapping matches will be reported.
-
-        Note that the start and end locations are reported relative to the string
-        being parsed.  See :class:`parseString` for more information on parsing
-        strings with embedded tabs.
-
-        Example::
-
-            source = "sldjf123lsdjjkf345sldkjf879lkjsfd987"
-            print(source)
-            for tokens,start,end in Word(alphas).scanString(source):
-                print(' '*start + '^'*(end-start))
-                print(' '*start + tokens[0])
-
-        prints::
-
-            sldjf123lsdjjkf345sldkjf879lkjsfd987
-            ^^^^^
-            sldjf
-                    ^^^^^^^
-                    lsdjjkf
-                              ^^^^^^
-                              sldkjf
-                                       ^^^^^^
-                                       lkjsfd
-        """
-        if not self.streamlined:
-            self.streamline()
-        for e in self.ignoreExprs:
-            e.streamline()
-
-        if not self.keepTabs:
-            instring = _ustr(instring).expandtabs()
-        instrlen = len(instring)
-        loc = 0
-        preparseFn = self.preParse
-        parseFn = self._parse
-        ParserElement.resetCache()
-        matches = 0
-        try:
-            while loc <= instrlen and matches < maxMatches:
-                try:
-                    preloc = preparseFn( instring, loc )
-                    nextLoc,tokens = parseFn( instring, preloc, callPreParse=False )
-                except ParseException:
-                    loc = preloc+1
-                else:
-                    if nextLoc > loc:
-                        matches += 1
-                        yield tokens, preloc, nextLoc
-                        if overlap:
-                            nextloc = preparseFn( instring, loc )
-                            if nextloc > loc:
-                                loc = nextLoc
-                            else:
-                                loc += 1
-                        else:
-                            loc = nextLoc
-                    else:
-                        loc = preloc+1
-        except ParseBaseException as exc:
-            if ParserElement.verbose_stacktrace:
-                raise
-            else:
-                # catch and re-raise exception from here, clears out pyparsing internal stack trace
-                raise exc
-
-    def transformString( self, instring ):
-        """
-        Extension to :class:`scanString`, to modify matching text with modified tokens that may
-        be returned from a parse action.  To use ``transformString``, define a grammar and
-        attach a parse action to it that modifies the returned token list.
-        Invoking ``transformString()`` on a target string will then scan for matches,
-        and replace the matched text patterns according to the logic in the parse
-        action.  ``transformString()`` returns the resulting transformed string.
-
-        Example::
-
-            wd = Word(alphas)
-            wd.setParseAction(lambda toks: toks[0].title())
-
-            print(wd.transformString("now is the winter of our discontent made glorious summer by this sun of york."))
-
-        prints::
-
-            Now Is The Winter Of Our Discontent Made Glorious Summer By This Sun Of York.
-        """
-        out = []
-        lastE = 0
-        # force preservation of <TAB>s, to minimize unwanted transformation of string, and to
-        # keep string locs straight between transformString and scanString
-        self.keepTabs = True
-        try:
-            for t,s,e in self.scanString( instring ):
-                out.append( instring[lastE:s] )
-                if t:
-                    if isinstance(t,ParseResults):
-                        out += t.asList()
-                    elif isinstance(t,list):
-                        out += t
-                    else:
-                        out.append(t)
-                lastE = e
-            out.append(instring[lastE:])
-            out = [o for o in out if o]
-            return "".join(map(_ustr,_flatten(out)))
-        except ParseBaseException as exc:
-            if ParserElement.verbose_stacktrace:
-                raise
-            else:
-                # catch and re-raise exception from here, clears out pyparsing internal stack trace
-                raise exc
-
-    def searchString( self, instring, maxMatches=_MAX_INT ):
-        """
-        Another extension to :class:`scanString`, simplifying the access to the tokens found
-        to match the given parse expression.  May be called with optional
-        ``maxMatches`` argument, to clip searching after 'n' matches are found.
-
-        Example::
-
-            # a capitalized word starts with an uppercase letter, followed by zero or more lowercase letters
-            cap_word = Word(alphas.upper(), alphas.lower())
-
-            print(cap_word.searchString("More than Iron, more than Lead, more than Gold I need Electricity"))
-
-            # the sum() builtin can be used to merge results into a single ParseResults object
-            print(sum(cap_word.searchString("More than Iron, more than Lead, more than Gold I need Electricity")))
-
-        prints::
-
-            [['More'], ['Iron'], ['Lead'], ['Gold'], ['I'], ['Electricity']]
-            ['More', 'Iron', 'Lead', 'Gold', 'I', 'Electricity']
-        """
-        try:
-            return ParseResults([ t for t,s,e in self.scanString( instring, maxMatches ) ])
-        except ParseBaseException as exc:
-            if ParserElement.verbose_stacktrace:
-                raise
-            else:
-                # catch and re-raise exception from here, clears out pyparsing internal stack trace
-                raise exc
-
-    def split(self, instring, maxsplit=_MAX_INT, includeSeparators=False):
-        """
-        Generator method to split a string using the given expression as a separator.
-        May be called with optional ``maxsplit`` argument, to limit the number of splits;
-        and the optional ``includeSeparators`` argument (default= ``False``), if the separating
-        matching text should be included in the split results.
-
-        Example::
-
-            punc = oneOf(list(".,;:/-!?"))
-            print(list(punc.split("This, this?, this sentence, is badly punctuated!")))
-
-        prints::
-
-            ['This', ' this', '', ' this sentence', ' is badly punctuated', '']
-        """
-        splits = 0
-        last = 0
-        for t,s,e in self.scanString(instring, maxMatches=maxsplit):
-            yield instring[last:s]
-            if includeSeparators:
-                yield t[0]
-            last = e
-        yield instring[last:]
-
-    def __add__(self, other ):
-        """
-        Implementation of + operator - returns :class:`And`. Adding strings to a ParserElement
-        converts them to :class:`Literal`s by default.
-
-        Example::
-
-            greet = Word(alphas) + "," + Word(alphas) + "!"
-            hello = "Hello, World!"
-            print (hello, "->", greet.parseString(hello))
-
-        prints::
-
-            Hello, World! -> ['Hello', ',', 'World', '!']
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return And( [ self, other ] )
-
-    def __radd__(self, other ):
-        """
-        Implementation of + operator when left operand is not a :class:`ParserElement`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return other + self
-
-    def __sub__(self, other):
-        """
-        Implementation of - operator, returns :class:`And` with error stop
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return self + And._ErrorStop() + other
-
-    def __rsub__(self, other ):
-        """
-        Implementation of - operator when left operand is not a :class:`ParserElement`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return other - self
-
-    def __mul__(self,other):
-        """
-        Implementation of * operator, allows use of ``expr * 3`` in place of
-        ``expr + expr + expr``.  Expressions may also me multiplied by a 2-integer
-        tuple, similar to ``{min,max}`` multipliers in regular expressions.  Tuples
-        may also include ``None`` as in:
-         - ``expr*(n,None)`` or ``expr*(n,)`` is equivalent
-              to ``expr*n + ZeroOrMore(expr)``
-              (read as "at least n instances of ``expr``")
-         - ``expr*(None,n)`` is equivalent to ``expr*(0,n)``
-              (read as "0 to n instances of ``expr``")
-         - ``expr*(None,None)`` is equivalent to ``ZeroOrMore(expr)``
-         - ``expr*(1,None)`` is equivalent to ``OneOrMore(expr)``
-
-        Note that ``expr*(None,n)`` does not raise an exception if
-        more than n exprs exist in the input stream; that is,
-        ``expr*(None,n)`` does not enforce a maximum number of expr
-        occurrences.  If this behavior is desired, then write
-        ``expr*(None,n) + ~expr``
-        """
-        if isinstance(other,int):
-            minElements, optElements = other,0
-        elif isinstance(other,tuple):
-            other = (other + (None, None))[:2]
-            if other[0] is None:
-                other = (0, other[1])
-            if isinstance(other[0],int) and other[1] is None:
-                if other[0] == 0:
-                    return ZeroOrMore(self)
-                if other[0] == 1:
-                    return OneOrMore(self)
-                else:
-                    return self*other[0] + ZeroOrMore(self)
-            elif isinstance(other[0],int) and isinstance(other[1],int):
-                minElements, optElements = other
-                optElements -= minElements
-            else:
-                raise TypeError("cannot multiply 'ParserElement' and ('%s','%s') objects", type(other[0]),type(other[1]))
-        else:
-            raise TypeError("cannot multiply 'ParserElement' and '%s' objects", type(other))
-
-        if minElements < 0:
-            raise ValueError("cannot multiply ParserElement by negative value")
-        if optElements < 0:
-            raise ValueError("second tuple value must be greater or equal to first tuple value")
-        if minElements == optElements == 0:
-            raise ValueError("cannot multiply ParserElement by 0 or (0,0)")
-
-        if (optElements):
-            def makeOptionalList(n):
-                if n>1:
-                    return Optional(self + makeOptionalList(n-1))
-                else:
-                    return Optional(self)
-            if minElements:
-                if minElements == 1:
-                    ret = self + makeOptionalList(optElements)
-                else:
-                    ret = And([self]*minElements) + makeOptionalList(optElements)
-            else:
-                ret = makeOptionalList(optElements)
-        else:
-            if minElements == 1:
-                ret = self
-            else:
-                ret = And([self]*minElements)
-        return ret
-
-    def __rmul__(self, other):
-        return self.__mul__(other)
-
-    def __or__(self, other ):
-        """
-        Implementation of | operator - returns :class:`MatchFirst`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return MatchFirst( [ self, other ] )
-
-    def __ror__(self, other ):
-        """
-        Implementation of | operator when left operand is not a :class:`ParserElement`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return other | self
-
-    def __xor__(self, other ):
-        """
-        Implementation of ^ operator - returns :class:`Or`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return Or( [ self, other ] )
-
-    def __rxor__(self, other ):
-        """
-        Implementation of ^ operator when left operand is not a :class:`ParserElement`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return other ^ self
-
-    def __and__(self, other ):
-        """
-        Implementation of & operator - returns :class:`Each`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return Each( [ self, other ] )
-
-    def __rand__(self, other ):
-        """
-        Implementation of & operator when left operand is not a :class:`ParserElement`
-        """
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        if not isinstance( other, ParserElement ):
-            warnings.warn("Cannot combine element of type %s with ParserElement" % type(other),
-                    SyntaxWarning, stacklevel=2)
-            return None
-        return other & self
-
-    def __invert__( self ):
-        """
-        Implementation of ~ operator - returns :class:`NotAny`
-        """
-        return NotAny( self )
-
-    def __call__(self, name=None):
-        """
-        Shortcut for :class:`setResultsName`, with ``listAllMatches=False``.
-
-        If ``name`` is given with a trailing ``'*'`` character, then ``listAllMatches`` will be
-        passed as ``True``.
-
-        If ``name` is omitted, same as calling :class:`copy`.
-
-        Example::
-
-            # these are equivalent
-            userdata = Word(alphas).setResultsName("name") + Word(nums+"-").setResultsName("socsecno")
-            userdata = Word(alphas)("name") + Word(nums+"-")("socsecno")
-        """
-        if name is not None:
-            return self.setResultsName(name)
-        else:
-            return self.copy()
-
-    def suppress( self ):
-        """
-        Suppresses the output of this :class:`ParserElement`; useful to keep punctuation from
-        cluttering up returned output.
-        """
-        return Suppress( self )
-
-    def leaveWhitespace( self ):
-        """
-        Disables the skipping of whitespace before matching the characters in the
-        :class:`ParserElement`'s defined pattern.  This is normally only used internally by
-        the pyparsing module, but may be needed in some whitespace-sensitive grammars.
-        """
-        self.skipWhitespace = False
-        return self
-
-    def setWhitespaceChars( self, chars ):
-        """
-        Overrides the default whitespace chars
-        """
-        self.skipWhitespace = True
-        self.whiteChars = chars
-        self.copyDefaultWhiteChars = False
-        return self
-
-    def parseWithTabs( self ):
-        """
-        Overrides default behavior to expand ``<TAB>``s to spaces before parsing the input string.
-        Must be called before ``parseString`` when the input grammar contains elements that
-        match ``<TAB>`` characters.
-        """
-        self.keepTabs = True
-        return self
-
-    def ignore( self, other ):
-        """
-        Define expression to be ignored (e.g., comments) while doing pattern
-        matching; may be called repeatedly, to define multiple comment or other
-        ignorable patterns.
-
-        Example::
-
-            patt = OneOrMore(Word(alphas))
-            patt.parseString('ablaj /* comment */ lskjd') # -> ['ablaj']
-
-            patt.ignore(cStyleComment)
-            patt.parseString('ablaj /* comment */ lskjd') # -> ['ablaj', 'lskjd']
-        """
-        if isinstance(other, basestring):
-            other = Suppress(other)
-
-        if isinstance( other, Suppress ):
-            if other not in self.ignoreExprs:
-                self.ignoreExprs.append(other)
-        else:
-            self.ignoreExprs.append( Suppress( other.copy() ) )
-        return self
-
-    def setDebugActions( self, startAction, successAction, exceptionAction ):
-        """
-        Enable display of debugging messages while doing pattern matching.
-        """
-        self.debugActions = (startAction or _defaultStartDebugAction,
-                             successAction or _defaultSuccessDebugAction,
-                             exceptionAction or _defaultExceptionDebugAction)
-        self.debug = True
-        return self
-
-    def setDebug( self, flag=True ):
-        """
-        Enable display of debugging messages while doing pattern matching.
-        Set ``flag`` to True to enable, False to disable.
-
-        Example::
-
-            wd = Word(alphas).setName("alphaword")
-            integer = Word(nums).setName("numword")
-            term = wd | integer
-
-            # turn on debugging for wd
-            wd.setDebug()
-
-            OneOrMore(term).parseString("abc 123 xyz 890")
-
-        prints::
-
-            Match alphaword at loc 0(1,1)
-            Matched alphaword -> ['abc']
-            Match alphaword at loc 3(1,4)
-            Exception raised:Expected alphaword (at char 4), (line:1, col:5)
-            Match alphaword at loc 7(1,8)
-            Matched alphaword -> ['xyz']
-            Match alphaword at loc 11(1,12)
-            Exception raised:Expected alphaword (at char 12), (line:1, col:13)
-            Match alphaword at loc 15(1,16)
-            Exception raised:Expected alphaword (at char 15), (line:1, col:16)
-
-        The output shown is that produced by the default debug actions - custom debug actions can be
-        specified using :class:`setDebugActions`. Prior to attempting
-        to match the ``wd`` expression, the debugging message ``"Match <exprname> at loc <n>(<line>,<col>)"``
-        is shown. Then if the parse succeeds, a ``"Matched"`` message is shown, or an ``"Exception raised"``
-        message is shown. Also note the use of :class:`setName` to assign a human-readable name to the expression,
-        which makes debugging and exception messages easier to understand - for instance, the default
-        name created for the :class:`Word` expression without calling ``setName`` is ``"W:(ABCD...)"``.
-        """
-        if flag:
-            self.setDebugActions( _defaultStartDebugAction, _defaultSuccessDebugAction, _defaultExceptionDebugAction )
-        else:
-            self.debug = False
-        return self
-
-    def __str__( self ):
-        return self.name
-
-    def __repr__( self ):
-        return _ustr(self)
-
-    def streamline( self ):
-        self.streamlined = True
-        self.strRepr = None
-        return self
-
-    def checkRecursion( self, parseElementList ):
-        pass
-
-    def validate( self, validateTrace=[] ):
-        """
-        Check defined expressions for valid structure, check for infinite recursive definitions.
-        """
-        self.checkRecursion( [] )
-
-    def parseFile( self, file_or_filename, parseAll=False ):
-        """
-        Execute the parse expression on the given file or filename.
-        If a filename is specified (instead of a file object),
-        the entire file is opened, read, and closed before parsing.
-        """
-        try:
-            file_contents = file_or_filename.read()
-        except AttributeError:
-            with open(file_or_filename, "r") as f:
-                file_contents = f.read()
-        try:
-            return self.parseString(file_contents, parseAll)
-        except ParseBaseException as exc:
-            if ParserElement.verbose_stacktrace:
-                raise
-            else:
-                # catch and re-raise exception from here, clears out pyparsing internal stack trace
-                raise exc
-
-    def __eq__(self,other):
-        if isinstance(other, ParserElement):
-            return self is other or vars(self) == vars(other)
-        elif isinstance(other, basestring):
-            return self.matches(other)
-        else:
-            return super(ParserElement,self)==other
-
-    def __ne__(self,other):
-        return not (self == other)
-
-    def __hash__(self):
-        return hash(id(self))
-
-    def __req__(self,other):
-        return self == other
-
-    def __rne__(self,other):
-        return not (self == other)
-
-    def matches(self, testString, parseAll=True):
-        """
-        Method for quick testing of a parser against a test string. Good for simple
-        inline microtests of sub expressions while building up larger parser.
-
-        Parameters:
-         - testString - to test against this expression for a match
-         - parseAll - (default= ``True``) - flag to pass to :class:`parseString` when running tests
-
-        Example::
-
-            expr = Word(nums)
-            assert expr.matches("100")
-        """
-        try:
-            self.parseString(_ustr(testString), parseAll=parseAll)
-            return True
-        except ParseBaseException:
-            return False
-
-    def runTests(self, tests, parseAll=True, comment='#',
-                 fullDump=True, printResults=True, failureTests=False, postParse=None):
-        """
-        Execute the parse expression on a series of test strings, showing each
-        test, the parsed results or where the parse failed. Quick and easy way to
-        run a parse expression against a list of sample strings.
-
-        Parameters:
-         - tests - a list of separate test strings, or a multiline string of test strings
-         - parseAll - (default= ``True``) - flag to pass to :class:`parseString` when running tests
-         - comment - (default= ``'#'``) - expression for indicating embedded comments in the test
-              string; pass None to disable comment filtering
-         - fullDump - (default= ``True``) - dump results as list followed by results names in nested outline;
-              if False, only dump nested list
-         - printResults - (default= ``True``) prints test output to stdout
-         - failureTests - (default= ``False``) indicates if these tests are expected to fail parsing
-         - postParse - (default= ``None``) optional callback for successful parse results; called as
-              `fn(test_string, parse_results)` and returns a string to be added to the test output
-
-        Returns: a (success, results) tuple, where success indicates that all tests succeeded
-        (or failed if ``failureTests`` is True), and the results contain a list of lines of each
-        test's output
-
-        Example::
-
-            number_expr = pyparsing_common.number.copy()
-
-            result = number_expr.runTests('''
-                # unsigned integer
-                100
-                # negative integer
-                -100
-                # float with scientific notation
-                6.02e23
-                # integer with scientific notation
-                1e-12
-                ''')
-            print("Success" if result[0] else "Failed!")
-
-            result = number_expr.runTests('''
-                # stray character
-                100Z
-                # missing leading digit before '.'
-                -.100
-                # too many '.'
-                3.14.159
-                ''', failureTests=True)
-            print("Success" if result[0] else "Failed!")
-
-        prints::
-
-            # unsigned integer
-            100
-            [100]
-
-            # negative integer
-            -100
-            [-100]
-
-            # float with scientific notation
-            6.02e23
-            [6.02e+23]
-
-            # integer with scientific notation
-            1e-12
-            [1e-12]
-
-            Success
-
-            # stray character
-            100Z
-               ^
-            FAIL: Expected end of text (at char 3), (line:1, col:4)
-
-            # missing leading digit before '.'
-            -.100
-            ^
-            FAIL: Expected {real number with scientific notation | real number | signed integer} (at char 0), (line:1, col:1)
-
-            # too many '.'
-            3.14.159
-                ^
-            FAIL: Expected end of text (at char 4), (line:1, col:5)
-
-            Success
-
-        Each test string must be on a single line. If you want to test a string that spans multiple
-        lines, create a test like this::
-
-            expr.runTest(r"this is a test\\n of strings that spans \\n 3 lines")
-
-        (Note that this is a raw string literal, you must include the leading 'r'.)
-        """
-        if isinstance(tests, basestring):
-            tests = list(map(str.strip, tests.rstrip().splitlines()))
-        if isinstance(comment, basestring):
-            comment = Literal(comment)
-        allResults = []
-        comments = []
-        success = True
-        for t in tests:
-            if comment is not None and comment.matches(t, False) or comments and not t:
-                comments.append(t)
-                continue
-            if not t:
-                continue
-            out = ['\n'.join(comments), t]
-            comments = []
-            try:
-                # convert newline marks to actual newlines, and strip leading BOM if present
-                t = t.replace(r'\n','\n').lstrip('\ufeff')
-                result = self.parseString(t, parseAll=parseAll)
-                out.append(result.dump(full=fullDump))
-                success = success and not failureTests
-                if postParse is not None:
-                    try:
-                        pp_value = postParse(t, result)
-                        if pp_value is not None:
-                            out.append(str(pp_value))
-                    except Exception as e:
-                        out.append("{0} failed: {1}: {2}".format(postParse.__name__, type(e).__name__, e))
-            except ParseBaseException as pe:
-                fatal = "(FATAL)" if isinstance(pe, ParseFatalException) else ""
-                if '\n' in t:
-                    out.append(line(pe.loc, t))
-                    out.append(' '*(col(pe.loc,t)-1) + '^' + fatal)
-                else:
-                    out.append(' '*pe.loc + '^' + fatal)
-                out.append("FAIL: " + str(pe))
-                success = success and failureTests
-                result = pe
-            except Exception as exc:
-                out.append("FAIL-EXCEPTION: " + str(exc))
-                success = success and failureTests
-                result = exc
-
-            if printResults:
-                if fullDump:
-                    out.append('')
-                print('\n'.join(out))
-
-            allResults.append((t, result))
-
-        return success, allResults
-
-
-class Token(ParserElement):
-    """Abstract :class:`ParserElement` subclass, for defining atomic
-    matching patterns.
-    """
-    def __init__( self ):
-        super(Token,self).__init__( savelist=False )
-
-
-class Empty(Token):
-    """An empty token, will always match.
-    """
-    def __init__( self ):
-        super(Empty,self).__init__()
-        self.name = "Empty"
-        self.mayReturnEmpty = True
-        self.mayIndexError = False
-
-
-class NoMatch(Token):
-    """A token that will never match.
-    """
-    def __init__( self ):
-        super(NoMatch,self).__init__()
-        self.name = "NoMatch"
-        self.mayReturnEmpty = True
-        self.mayIndexError = False
-        self.errmsg = "Unmatchable token"
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        raise ParseException(instring, loc, self.errmsg, self)
-
-
-class Literal(Token):
-    """Token to exactly match a specified string.
-
-    Example::
-
-        Literal('blah').parseString('blah')  # -> ['blah']
-        Literal('blah').parseString('blahfooblah')  # -> ['blah']
-        Literal('blah').parseString('bla')  # -> Exception: Expected "blah"
-
-    For case-insensitive matching, use :class:`CaselessLiteral`.
-
-    For keyword matching (force word break before and after the matched string),
-    use :class:`Keyword` or :class:`CaselessKeyword`.
-    """
-    def __init__( self, matchString ):
-        super(Literal,self).__init__()
-        self.match = matchString
-        self.matchLen = len(matchString)
-        try:
-            self.firstMatchChar = matchString[0]
-        except IndexError:
-            warnings.warn("null string passed to Literal; use Empty() instead",
-                            SyntaxWarning, stacklevel=2)
-            self.__class__ = Empty
-        self.name = '"%s"' % _ustr(self.match)
-        self.errmsg = "Expected " + self.name
-        self.mayReturnEmpty = False
-        self.mayIndexError = False
-
-    # Performance tuning: this routine gets called a *lot*
-    # if this is a single character match string  and the first character matches,
-    # short-circuit as quickly as possible, and avoid calling startswith
-    #~ @profile
-    def parseImpl( self, instring, loc, doActions=True ):
-        if (instring[loc] == self.firstMatchChar and
-            (self.matchLen==1 or instring.startswith(self.match,loc)) ):
-            return loc+self.matchLen, self.match
-        raise ParseException(instring, loc, self.errmsg, self)
-_L = Literal
-ParserElement._literalStringClass = Literal
-
-class Keyword(Token):
-    """Token to exactly match a specified string as a keyword, that is,
-    it must be immediately followed by a non-keyword character.  Compare
-    with :class:`Literal`:
-
-     - ``Literal("if")`` will match the leading ``'if'`` in
-       ``'ifAndOnlyIf'``.
-     - ``Keyword("if")`` will not; it will only match the leading
-       ``'if'`` in ``'if x=1'``, or ``'if(y==2)'``
-
-    Accepts two optional constructor arguments in addition to the
-    keyword string:
-
-     - ``identChars`` is a string of characters that would be valid
-       identifier characters, defaulting to all alphanumerics + "_" and
-       "$"
-     - ``caseless`` allows case-insensitive matching, default is ``False``.
-
-    Example::
-
-        Keyword("start").parseString("start")  # -> ['start']
-        Keyword("start").parseString("starting")  # -> Exception
-
-    For case-insensitive matching, use :class:`CaselessKeyword`.
-    """
-    DEFAULT_KEYWORD_CHARS = alphanums+"_$"
-
-    def __init__( self, matchString, identChars=None, caseless=False ):
-        super(Keyword,self).__init__()
-        if identChars is None:
-            identChars = Keyword.DEFAULT_KEYWORD_CHARS
-        self.match = matchString
-        self.matchLen = len(matchString)
-        try:
-            self.firstMatchChar = matchString[0]
-        except IndexError:
-            warnings.warn("null string passed to Keyword; use Empty() instead",
-                            SyntaxWarning, stacklevel=2)
-        self.name = '"%s"' % self.match
-        self.errmsg = "Expected " + self.name
-        self.mayReturnEmpty = False
-        self.mayIndexError = False
-        self.caseless = caseless
-        if caseless:
-            self.caselessmatch = matchString.upper()
-            identChars = identChars.upper()
-        self.identChars = set(identChars)
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if self.caseless:
-            if ( (instring[ loc:loc+self.matchLen ].upper() == self.caselessmatch) and
-                 (loc >= len(instring)-self.matchLen or instring[loc+self.matchLen].upper() not in self.identChars) and
-                 (loc == 0 or instring[loc-1].upper() not in self.identChars) ):
-                return loc+self.matchLen, self.match
-        else:
-            if (instring[loc] == self.firstMatchChar and
-                (self.matchLen==1 or instring.startswith(self.match,loc)) and
-                (loc >= len(instring)-self.matchLen or instring[loc+self.matchLen] not in self.identChars) and
-                (loc == 0 or instring[loc-1] not in self.identChars) ):
-                return loc+self.matchLen, self.match
-        raise ParseException(instring, loc, self.errmsg, self)
-
-    def copy(self):
-        c = super(Keyword,self).copy()
-        c.identChars = Keyword.DEFAULT_KEYWORD_CHARS
-        return c
-
-    @staticmethod
-    def setDefaultKeywordChars( chars ):
-        """Overrides the default Keyword chars
-        """
-        Keyword.DEFAULT_KEYWORD_CHARS = chars
-
-class CaselessLiteral(Literal):
-    """Token to match a specified string, ignoring case of letters.
-    Note: the matched results will always be in the case of the given
-    match string, NOT the case of the input text.
-
-    Example::
-
-        OneOrMore(CaselessLiteral("CMD")).parseString("cmd CMD Cmd10") # -> ['CMD', 'CMD', 'CMD']
-
-    (Contrast with example for :class:`CaselessKeyword`.)
-    """
-    def __init__( self, matchString ):
-        super(CaselessLiteral,self).__init__( matchString.upper() )
-        # Preserve the defining literal.
-        self.returnString = matchString
-        self.name = "'%s'" % self.returnString
-        self.errmsg = "Expected " + self.name
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if instring[ loc:loc+self.matchLen ].upper() == self.match:
-            return loc+self.matchLen, self.returnString
-        raise ParseException(instring, loc, self.errmsg, self)
-
-class CaselessKeyword(Keyword):
-    """
-    Caseless version of :class:`Keyword`.
-
-    Example::
-
-        OneOrMore(CaselessKeyword("CMD")).parseString("cmd CMD Cmd10") # -> ['CMD', 'CMD']
-
-    (Contrast with example for :class:`CaselessLiteral`.)
-    """
-    def __init__( self, matchString, identChars=None ):
-        super(CaselessKeyword,self).__init__( matchString, identChars, caseless=True )
-
-class CloseMatch(Token):
-    """A variation on :class:`Literal` which matches "close" matches,
-    that is, strings with at most 'n' mismatching characters.
-    :class:`CloseMatch` takes parameters:
-
-     - ``match_string`` - string to be matched
-     - ``maxMismatches`` - (``default=1``) maximum number of
-       mismatches allowed to count as a match
-
-    The results from a successful parse will contain the matched text
-    from the input string and the following named results:
-
-     - ``mismatches`` - a list of the positions within the
-       match_string where mismatches were found
-     - ``original`` - the original match_string used to compare
-       against the input string
-
-    If ``mismatches`` is an empty list, then the match was an exact
-    match.
-
-    Example::
-
-        patt = CloseMatch("ATCATCGAATGGA")
-        patt.parseString("ATCATCGAAXGGA") # -> (['ATCATCGAAXGGA'], {'mismatches': [[9]], 'original': ['ATCATCGAATGGA']})
-        patt.parseString("ATCAXCGAAXGGA") # -> Exception: Expected 'ATCATCGAATGGA' (with up to 1 mismatches) (at char 0), (line:1, col:1)
-
-        # exact match
-        patt.parseString("ATCATCGAATGGA") # -> (['ATCATCGAATGGA'], {'mismatches': [[]], 'original': ['ATCATCGAATGGA']})
-
-        # close match allowing up to 2 mismatches
-        patt = CloseMatch("ATCATCGAATGGA", maxMismatches=2)
-        patt.parseString("ATCAXCGAAXGGA") # -> (['ATCAXCGAAXGGA'], {'mismatches': [[4, 9]], 'original': ['ATCATCGAATGGA']})
-    """
-    def __init__(self, match_string, maxMismatches=1):
-        super(CloseMatch,self).__init__()
-        self.name = match_string
-        self.match_string = match_string
-        self.maxMismatches = maxMismatches
-        self.errmsg = "Expected %r (with up to %d mismatches)" % (self.match_string, self.maxMismatches)
-        self.mayIndexError = False
-        self.mayReturnEmpty = False
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        start = loc
-        instrlen = len(instring)
-        maxloc = start + len(self.match_string)
-
-        if maxloc <= instrlen:
-            match_string = self.match_string
-            match_stringloc = 0
-            mismatches = []
-            maxMismatches = self.maxMismatches
-
-            for match_stringloc,s_m in enumerate(zip(instring[loc:maxloc], self.match_string)):
-                src,mat = s_m
-                if src != mat:
-                    mismatches.append(match_stringloc)
-                    if len(mismatches) > maxMismatches:
-                        break
-            else:
-                loc = match_stringloc + 1
-                results = ParseResults([instring[start:loc]])
-                results['original'] = self.match_string
-                results['mismatches'] = mismatches
-                return loc, results
-
-        raise ParseException(instring, loc, self.errmsg, self)
-
-
-class Word(Token):
-    """Token for matching words composed of allowed character sets.
-    Defined with string containing all allowed initial characters, an
-    optional string containing allowed body characters (if omitted,
-    defaults to the initial character set), and an optional minimum,
-    maximum, and/or exact length.  The default value for ``min`` is
-    1 (a minimum value < 1 is not valid); the default values for
-    ``max`` and ``exact`` are 0, meaning no maximum or exact
-    length restriction. An optional ``excludeChars`` parameter can
-    list characters that might be found in the input ``bodyChars``
-    string; useful to define a word of all printables except for one or
-    two characters, for instance.
-
-    :class:`srange` is useful for defining custom character set strings
-    for defining ``Word`` expressions, using range notation from
-    regular expression character sets.
-
-    A common mistake is to use :class:`Word` to match a specific literal
-    string, as in ``Word("Address")``. Remember that :class:`Word`
-    uses the string argument to define *sets* of matchable characters.
-    This expression would match "Add", "AAA", "dAred", or any other word
-    made up of the characters 'A', 'd', 'r', 'e', and 's'. To match an
-    exact literal string, use :class:`Literal` or :class:`Keyword`.
-
-    pyparsing includes helper strings for building Words:
-
-     - :class:`alphas`
-     - :class:`nums`
-     - :class:`alphanums`
-     - :class:`hexnums`
-     - :class:`alphas8bit` (alphabetic characters in ASCII range 128-255
-       - accented, tilded, umlauted, etc.)
-     - :class:`punc8bit` (non-alphabetic characters in ASCII range
-       128-255 - currency, symbols, superscripts, diacriticals, etc.)
-     - :class:`printables` (any non-whitespace character)
-
-    Example::
-
-        # a word composed of digits
-        integer = Word(nums) # equivalent to Word("0123456789") or Word(srange("0-9"))
-
-        # a word with a leading capital, and zero or more lowercase
-        capital_word = Word(alphas.upper(), alphas.lower())
-
-        # hostnames are alphanumeric, with leading alpha, and '-'
-        hostname = Word(alphas, alphanums+'-')
-
-        # roman numeral (not a strict parser, accepts invalid mix of characters)
-        roman = Word("IVXLCDM")
-
-        # any string of non-whitespace characters, except for ','
-        csv_value = Word(printables, excludeChars=",")
-    """
-    def __init__( self, initChars, bodyChars=None, min=1, max=0, exact=0, asKeyword=False, excludeChars=None ):
-        super(Word,self).__init__()
-        if excludeChars:
-            initChars = ''.join(c for c in initChars if c not in excludeChars)
-            if bodyChars:
-                bodyChars = ''.join(c for c in bodyChars if c not in excludeChars)
-        self.initCharsOrig = initChars
-        self.initChars = set(initChars)
-        if bodyChars :
-            self.bodyCharsOrig = bodyChars
-            self.bodyChars = set(bodyChars)
-        else:
-            self.bodyCharsOrig = initChars
-            self.bodyChars = set(initChars)
-
-        self.maxSpecified = max > 0
-
-        if min < 1:
-            raise ValueError("cannot specify a minimum length < 1; use Optional(Word()) if zero-length word is permitted")
-
-        self.minLen = min
-
-        if max > 0:
-            self.maxLen = max
-        else:
-            self.maxLen = _MAX_INT
-
-        if exact > 0:
-            self.maxLen = exact
-            self.minLen = exact
-
-        self.name = _ustr(self)
-        self.errmsg = "Expected " + self.name
-        self.mayIndexError = False
-        self.asKeyword = asKeyword
-
-        if ' ' not in self.initCharsOrig+self.bodyCharsOrig and (min==1 and max==0 and exact==0):
-            if self.bodyCharsOrig == self.initCharsOrig:
-                self.reString = "[%s]+" % _escapeRegexRangeChars(self.initCharsOrig)
-            elif len(self.initCharsOrig) == 1:
-                self.reString = "%s[%s]*" % \
-                                      (re.escape(self.initCharsOrig),
-                                      _escapeRegexRangeChars(self.bodyCharsOrig),)
-            else:
-                self.reString = "[%s][%s]*" % \
-                                      (_escapeRegexRangeChars(self.initCharsOrig),
-                                      _escapeRegexRangeChars(self.bodyCharsOrig),)
-            if self.asKeyword:
-                self.reString = r"\b"+self.reString+r"\b"
-            try:
-                self.re = re.compile( self.reString )
-            except Exception:
-                self.re = None
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if self.re:
-            result = self.re.match(instring,loc)
-            if not result:
-                raise ParseException(instring, loc, self.errmsg, self)
-
-            loc = result.end()
-            return loc, result.group()
-
-        if not(instring[ loc ] in self.initChars):
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        start = loc
-        loc += 1
-        instrlen = len(instring)
-        bodychars = self.bodyChars
-        maxloc = start + self.maxLen
-        maxloc = min( maxloc, instrlen )
-        while loc < maxloc and instring[loc] in bodychars:
-            loc += 1
-
-        throwException = False
-        if loc - start < self.minLen:
-            throwException = True
-        if self.maxSpecified and loc < instrlen and instring[loc] in bodychars:
-            throwException = True
-        if self.asKeyword:
-            if (start>0 and instring[start-1] in bodychars) or (loc<instrlen and instring[loc] in bodychars):
-                throwException = True
-
-        if throwException:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        return loc, instring[start:loc]
-
-    def __str__( self ):
-        try:
-            return super(Word,self).__str__()
-        except Exception:
-            pass
-
-
-        if self.strRepr is None:
-
-            def charsAsStr(s):
-                if len(s)>4:
-                    return s[:4]+"..."
-                else:
-                    return s
-
-            if ( self.initCharsOrig != self.bodyCharsOrig ):
-                self.strRepr = "W:(%s,%s)" % ( charsAsStr(self.initCharsOrig), charsAsStr(self.bodyCharsOrig) )
-            else:
-                self.strRepr = "W:(%s)" % charsAsStr(self.initCharsOrig)
-
-        return self.strRepr
-
-
-class Char(Word):
-    """A short-cut class for defining ``Word(characters, exact=1)``,
-    when defining a match of any single character in a string of
-    characters.
-    """
-    def __init__(self, charset):
-        super(Char, self).__init__(charset, exact=1)
-        self.reString = "[%s]" % _escapeRegexRangeChars(self.initCharsOrig)
-        self.re = re.compile( self.reString )
-
-
-class Regex(Token):
-    r"""Token for matching strings that match a given regular
-    expression. Defined with string specifying the regular expression in
-    a form recognized by the stdlib Python  `re module <https://docs.python.org/3/library/re.html>`_.
-    If the given regex contains named groups (defined using ``(?P<name>...)``),
-    these will be preserved as named parse results.
-
-    Example::
-
-        realnum = Regex(r"[+-]?\d+\.\d*")
-        date = Regex(r'(?P<year>\d{4})-(?P<month>\d\d?)-(?P<day>\d\d?)')
-        # ref: https://stackoverflow.com/questions/267399/how-do-you-match-only-valid-roman-numerals-with-a-regular-expression
-        roman = Regex(r"M{0,4}(CM|CD|D?{0,3})(XC|XL|L?X{0,3})(IX|IV|V?I{0,3})")
-    """
-    compiledREtype = type(re.compile("[A-Z]"))
-    def __init__( self, pattern, flags=0, asGroupList=False, asMatch=False):
-        """The parameters ``pattern`` and ``flags`` are passed
-        to the ``re.compile()`` function as-is. See the Python
-        `re module <https://docs.python.org/3/library/re.html>`_ module for an
-        explanation of the acceptable patterns and flags.
-        """
-        super(Regex,self).__init__()
-
-        if isinstance(pattern, basestring):
-            if not pattern:
-                warnings.warn("null string passed to Regex; use Empty() instead",
-                        SyntaxWarning, stacklevel=2)
-
-            self.pattern = pattern
-            self.flags = flags
-
-            try:
-                self.re = re.compile(self.pattern, self.flags)
-                self.reString = self.pattern
-            except sre_constants.error:
-                warnings.warn("invalid pattern (%s) passed to Regex" % pattern,
-                    SyntaxWarning, stacklevel=2)
-                raise
-
-        elif isinstance(pattern, Regex.compiledREtype):
-            self.re = pattern
-            self.pattern = \
-            self.reString = str(pattern)
-            self.flags = flags
-
-        else:
-            raise ValueError("Regex may only be constructed with a string or a compiled RE object")
-
-        self.name = _ustr(self)
-        self.errmsg = "Expected " + self.name
-        self.mayIndexError = False
-        self.mayReturnEmpty = True
-        self.asGroupList = asGroupList
-        self.asMatch = asMatch
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        result = self.re.match(instring,loc)
-        if not result:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        loc = result.end()
-        if self.asMatch:
-            ret = result
-        elif self.asGroupList:
-            ret = result.groups()
-        else:
-            ret = ParseResults(result.group())
-            d = result.groupdict()
-            if d:
-                for k, v in d.items():
-                    ret[k] = v
-        return loc,ret
-
-    def __str__( self ):
-        try:
-            return super(Regex,self).__str__()
-        except Exception:
-            pass
-
-        if self.strRepr is None:
-            self.strRepr = "Re:(%s)" % repr(self.pattern)
-
-        return self.strRepr
-
-    def sub(self, repl):
-        """
-        Return Regex with an attached parse action to transform the parsed
-        result as if called using `re.sub(expr, repl, string) <https://docs.python.org/3/library/re.html#re.sub>`_.
-
-        Example::
-
-            make_html = Regex(r"(\w+):(.*?):").sub(r"<\1>\2</\1>")
-            print(make_html.transformString("h1:main title:"))
-            # prints "<h1>main title</h1>"
-        """
-        if self.asGroupList:
-            warnings.warn("cannot use sub() with Regex(asGroupList=True)",
-                           SyntaxWarning, stacklevel=2)
-            raise SyntaxError()
-
-        if self.asMatch and callable(repl):
-            warnings.warn("cannot use sub() with a callable with Regex(asMatch=True)",
-                           SyntaxWarning, stacklevel=2)
-            raise SyntaxError()
-
-        if self.asMatch:
-            def pa(tokens):
-                return tokens[0].expand(repl)
-        else:
-            def pa(tokens):
-                return self.re.sub(repl, tokens[0])
-        return self.addParseAction(pa)
-
-class QuotedString(Token):
-    r"""
-    Token for matching strings that are delimited by quoting characters.
-
-    Defined with the following parameters:
-
-        - quoteChar - string of one or more characters defining the
-          quote delimiting string
-        - escChar - character to escape quotes, typically backslash
-          (default= ``None`` )
-        - escQuote - special quote sequence to escape an embedded quote
-          string (such as SQL's ``""`` to escape an embedded ``"``)
-          (default= ``None`` )
-        - multiline - boolean indicating whether quotes can span
-          multiple lines (default= ``False`` )
-        - unquoteResults - boolean indicating whether the matched text
-          should be unquoted (default= ``True`` )
-        - endQuoteChar - string of one or more characters defining the
-          end of the quote delimited string (default= ``None``  => same as
-          quoteChar)
-        - convertWhitespaceEscapes - convert escaped whitespace
-          (``'\t'``, ``'\n'``, etc.) to actual whitespace
-          (default= ``True`` )
-
-    Example::
-
-        qs = QuotedString('"')
-        print(qs.searchString('lsjdf "This is the quote" sldjf'))
-        complex_qs = QuotedString('{{', endQuoteChar='}}')
-        print(complex_qs.searchString('lsjdf {{This is the "quote"}} sldjf'))
-        sql_qs = QuotedString('"', escQuote='""')
-        print(sql_qs.searchString('lsjdf "This is the quote with ""embedded"" quotes" sldjf'))
-
-    prints::
-
-        [['This is the quote']]
-        [['This is the "quote"']]
-        [['This is the quote with "embedded" quotes']]
-    """
-    def __init__( self, quoteChar, escChar=None, escQuote=None, multiline=False, unquoteResults=True, endQuoteChar=None, convertWhitespaceEscapes=True):
-        super(QuotedString,self).__init__()
-
-        # remove white space from quote chars - wont work anyway
-        quoteChar = quoteChar.strip()
-        if not quoteChar:
-            warnings.warn("quoteChar cannot be the empty string",SyntaxWarning,stacklevel=2)
-            raise SyntaxError()
-
-        if endQuoteChar is None:
-            endQuoteChar = quoteChar
-        else:
-            endQuoteChar = endQuoteChar.strip()
-            if not endQuoteChar:
-                warnings.warn("endQuoteChar cannot be the empty string",SyntaxWarning,stacklevel=2)
-                raise SyntaxError()
-
-        self.quoteChar = quoteChar
-        self.quoteCharLen = len(quoteChar)
-        self.firstQuoteChar = quoteChar[0]
-        self.endQuoteChar = endQuoteChar
-        self.endQuoteCharLen = len(endQuoteChar)
-        self.escChar = escChar
-        self.escQuote = escQuote
-        self.unquoteResults = unquoteResults
-        self.convertWhitespaceEscapes = convertWhitespaceEscapes
-
-        if multiline:
-            self.flags = re.MULTILINE | re.DOTALL
-            self.pattern = r'%s(?:[^%s%s]' % \
-                ( re.escape(self.quoteChar),
-                  _escapeRegexRangeChars(self.endQuoteChar[0]),
-                  (escChar is not None and _escapeRegexRangeChars(escChar) or '') )
-        else:
-            self.flags = 0
-            self.pattern = r'%s(?:[^%s\n\r%s]' % \
-                ( re.escape(self.quoteChar),
-                  _escapeRegexRangeChars(self.endQuoteChar[0]),
-                  (escChar is not None and _escapeRegexRangeChars(escChar) or '') )
-        if len(self.endQuoteChar) > 1:
-            self.pattern += (
-                '|(?:' + ')|(?:'.join("%s[^%s]" % (re.escape(self.endQuoteChar[:i]),
-                                               _escapeRegexRangeChars(self.endQuoteChar[i]))
-                                    for i in range(len(self.endQuoteChar)-1,0,-1)) + ')'
-                )
-        if escQuote:
-            self.pattern += (r'|(?:%s)' % re.escape(escQuote))
-        if escChar:
-            self.pattern += (r'|(?:%s.)' % re.escape(escChar))
-            self.escCharReplacePattern = re.escape(self.escChar)+"(.)"
-        self.pattern += (r')*%s' % re.escape(self.endQuoteChar))
-
-        try:
-            self.re = re.compile(self.pattern, self.flags)
-            self.reString = self.pattern
-        except sre_constants.error:
-            warnings.warn("invalid pattern (%s) passed to Regex" % self.pattern,
-                SyntaxWarning, stacklevel=2)
-            raise
-
-        self.name = _ustr(self)
-        self.errmsg = "Expected " + self.name
-        self.mayIndexError = False
-        self.mayReturnEmpty = True
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        result = instring[loc] == self.firstQuoteChar and self.re.match(instring,loc) or None
-        if not result:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        loc = result.end()
-        ret = result.group()
-
-        if self.unquoteResults:
-
-            # strip off quotes
-            ret = ret[self.quoteCharLen:-self.endQuoteCharLen]
-
-            if isinstance(ret,basestring):
-                # replace escaped whitespace
-                if '\\' in ret and self.convertWhitespaceEscapes:
-                    ws_map = {
-                        r'\t' : '\t',
-                        r'\n' : '\n',
-                        r'\f' : '\f',
-                        r'\r' : '\r',
-                    }
-                    for wslit,wschar in ws_map.items():
-                        ret = ret.replace(wslit, wschar)
-
-                # replace escaped characters
-                if self.escChar:
-                    ret = re.sub(self.escCharReplacePattern, r"\g<1>", ret)
-
-                # replace escaped quotes
-                if self.escQuote:
-                    ret = ret.replace(self.escQuote, self.endQuoteChar)
-
-        return loc, ret
-
-    def __str__( self ):
-        try:
-            return super(QuotedString,self).__str__()
-        except Exception:
-            pass
-
-        if self.strRepr is None:
-            self.strRepr = "quoted string, starting with %s ending with %s" % (self.quoteChar, self.endQuoteChar)
-
-        return self.strRepr
-
-
-class CharsNotIn(Token):
-    """Token for matching words composed of characters *not* in a given
-    set (will include whitespace in matched characters if not listed in
-    the provided exclusion set - see example). Defined with string
-    containing all disallowed characters, and an optional minimum,
-    maximum, and/or exact length.  The default value for ``min`` is
-    1 (a minimum value < 1 is not valid); the default values for
-    ``max`` and ``exact`` are 0, meaning no maximum or exact
-    length restriction.
-
-    Example::
-
-        # define a comma-separated-value as anything that is not a ','
-        csv_value = CharsNotIn(',')
-        print(delimitedList(csv_value).parseString("dkls,lsdkjf,s12 34,@!#,213"))
-
-    prints::
-
-        ['dkls', 'lsdkjf', 's12 34', '@!#', '213']
-    """
-    def __init__( self, notChars, min=1, max=0, exact=0 ):
-        super(CharsNotIn,self).__init__()
-        self.skipWhitespace = False
-        self.notChars = notChars
-
-        if min < 1:
-            raise ValueError(
-                "cannot specify a minimum length < 1; use " +
-                "Optional(CharsNotIn()) if zero-length char group is permitted")
-
-        self.minLen = min
-
-        if max > 0:
-            self.maxLen = max
-        else:
-            self.maxLen = _MAX_INT
-
-        if exact > 0:
-            self.maxLen = exact
-            self.minLen = exact
-
-        self.name = _ustr(self)
-        self.errmsg = "Expected " + self.name
-        self.mayReturnEmpty = ( self.minLen == 0 )
-        self.mayIndexError = False
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if instring[loc] in self.notChars:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        start = loc
-        loc += 1
-        notchars = self.notChars
-        maxlen = min( start+self.maxLen, len(instring) )
-        while loc < maxlen and \
-              (instring[loc] not in notchars):
-            loc += 1
-
-        if loc - start < self.minLen:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        return loc, instring[start:loc]
-
-    def __str__( self ):
-        try:
-            return super(CharsNotIn, self).__str__()
-        except Exception:
-            pass
-
-        if self.strRepr is None:
-            if len(self.notChars) > 4:
-                self.strRepr = "!W:(%s...)" % self.notChars[:4]
-            else:
-                self.strRepr = "!W:(%s)" % self.notChars
-
-        return self.strRepr
-
-class White(Token):
-    """Special matching class for matching whitespace.  Normally,
-    whitespace is ignored by pyparsing grammars.  This class is included
-    when some whitespace structures are significant.  Define with
-    a string containing the whitespace characters to be matched; default
-    is ``" \\t\\r\\n"``.  Also takes optional ``min``,
-    ``max``, and ``exact`` arguments, as defined for the
-    :class:`Word` class.
-    """
-    whiteStrs = {
-        ' ' : '<SP>',
-        '\t': '<TAB>',
-        '\n': '<LF>',
-        '\r': '<CR>',
-        '\f': '<FF>',
-        'u\00A0': '<NBSP>',
-        'u\1680': '<OGHAM_SPACE_MARK>',
-        'u\180E': '<MONGOLIAN_VOWEL_SEPARATOR>',
-        'u\2000': '<EN_QUAD>',
-        'u\2001': '<EM_QUAD>',
-        'u\2002': '<EN_SPACE>',
-        'u\2003': '<EM_SPACE>',
-        'u\2004': '<THREE-PER-EM_SPACE>',
-        'u\2005': '<FOUR-PER-EM_SPACE>',
-        'u\2006': '<SIX-PER-EM_SPACE>',
-        'u\2007': '<FIGURE_SPACE>',
-        'u\2008': '<PUNCTUATION_SPACE>',
-        'u\2009': '<THIN_SPACE>',
-        'u\200A': '<HAIR_SPACE>',
-        'u\200B': '<ZERO_WIDTH_SPACE>',
-        'u\202F': '<NNBSP>',
-        'u\205F': '<MMSP>',
-        'u\3000': '<IDEOGRAPHIC_SPACE>',
-        }
-    def __init__(self, ws=" \t\r\n", min=1, max=0, exact=0):
-        super(White,self).__init__()
-        self.matchWhite = ws
-        self.setWhitespaceChars( "".join(c for c in self.whiteChars if c not in self.matchWhite) )
-        #~ self.leaveWhitespace()
-        self.name = ("".join(White.whiteStrs[c] for c in self.matchWhite))
-        self.mayReturnEmpty = True
-        self.errmsg = "Expected " + self.name
-
-        self.minLen = min
-
-        if max > 0:
-            self.maxLen = max
-        else:
-            self.maxLen = _MAX_INT
-
-        if exact > 0:
-            self.maxLen = exact
-            self.minLen = exact
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if not(instring[ loc ] in self.matchWhite):
-            raise ParseException(instring, loc, self.errmsg, self)
-        start = loc
-        loc += 1
-        maxloc = start + self.maxLen
-        maxloc = min( maxloc, len(instring) )
-        while loc < maxloc and instring[loc] in self.matchWhite:
-            loc += 1
-
-        if loc - start < self.minLen:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        return loc, instring[start:loc]
-
-
-class _PositionToken(Token):
-    def __init__( self ):
-        super(_PositionToken,self).__init__()
-        self.name=self.__class__.__name__
-        self.mayReturnEmpty = True
-        self.mayIndexError = False
-
-class GoToColumn(_PositionToken):
-    """Token to advance to a specific column of input text; useful for
-    tabular report scraping.
-    """
-    def __init__( self, colno ):
-        super(GoToColumn,self).__init__()
-        self.col = colno
-
-    def preParse( self, instring, loc ):
-        if col(loc,instring) != self.col:
-            instrlen = len(instring)
-            if self.ignoreExprs:
-                loc = self._skipIgnorables( instring, loc )
-            while loc < instrlen and instring[loc].isspace() and col( loc, instring ) != self.col :
-                loc += 1
-        return loc
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        thiscol = col( loc, instring )
-        if thiscol > self.col:
-            raise ParseException( instring, loc, "Text not in expected column", self )
-        newloc = loc + self.col - thiscol
-        ret = instring[ loc: newloc ]
-        return newloc, ret
-
-
-class LineStart(_PositionToken):
-    """Matches if current position is at the beginning of a line within
-    the parse string
-
-    Example::
-
-        test = '''\
-        AAA this line
-        AAA and this line
-          AAA but not this one
-        B AAA and definitely not this one
-        '''
-
-        for t in (LineStart() + 'AAA' + restOfLine).searchString(test):
-            print(t)
-
-    prints::
-
-        ['AAA', ' this line']
-        ['AAA', ' and this line']
-
-    """
-    def __init__( self ):
-        super(LineStart,self).__init__()
-        self.errmsg = "Expected start of line"
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if col(loc, instring) == 1:
-            return loc, []
-        raise ParseException(instring, loc, self.errmsg, self)
-
-class LineEnd(_PositionToken):
-    """Matches if current position is at the end of a line within the
-    parse string
-    """
-    def __init__( self ):
-        super(LineEnd,self).__init__()
-        self.setWhitespaceChars( ParserElement.DEFAULT_WHITE_CHARS.replace("\n","") )
-        self.errmsg = "Expected end of line"
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if loc<len(instring):
-            if instring[loc] == "\n":
-                return loc+1, "\n"
-            else:
-                raise ParseException(instring, loc, self.errmsg, self)
-        elif loc == len(instring):
-            return loc+1, []
-        else:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-class StringStart(_PositionToken):
-    """Matches if current position is at the beginning of the parse
-    string
-    """
-    def __init__( self ):
-        super(StringStart,self).__init__()
-        self.errmsg = "Expected start of text"
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if loc != 0:
-            # see if entire string up to here is just whitespace and ignoreables
-            if loc != self.preParse( instring, 0 ):
-                raise ParseException(instring, loc, self.errmsg, self)
-        return loc, []
-
-class StringEnd(_PositionToken):
-    """Matches if current position is at the end of the parse string
-    """
-    def __init__( self ):
-        super(StringEnd,self).__init__()
-        self.errmsg = "Expected end of text"
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if loc < len(instring):
-            raise ParseException(instring, loc, self.errmsg, self)
-        elif loc == len(instring):
-            return loc+1, []
-        elif loc > len(instring):
-            return loc, []
-        else:
-            raise ParseException(instring, loc, self.errmsg, self)
-
-class WordStart(_PositionToken):
-    """Matches if the current position is at the beginning of a Word,
-    and is not preceded by any character in a given set of
-    ``wordChars`` (default= ``printables``). To emulate the
-    ``\b`` behavior of regular expressions, use
-    ``WordStart(alphanums)``. ``WordStart`` will also match at
-    the beginning of the string being parsed, or at the beginning of
-    a line.
-    """
-    def __init__(self, wordChars = printables):
-        super(WordStart,self).__init__()
-        self.wordChars = set(wordChars)
-        self.errmsg = "Not at the start of a word"
-
-    def parseImpl(self, instring, loc, doActions=True ):
-        if loc != 0:
-            if (instring[loc-1] in self.wordChars or
-                instring[loc] not in self.wordChars):
-                raise ParseException(instring, loc, self.errmsg, self)
-        return loc, []
-
-class WordEnd(_PositionToken):
-    """Matches if the current position is at the end of a Word, and is
-    not followed by any character in a given set of ``wordChars``
-    (default= ``printables``). To emulate the ``\b`` behavior of
-    regular expressions, use ``WordEnd(alphanums)``. ``WordEnd``
-    will also match at the end of the string being parsed, or at the end
-    of a line.
-    """
-    def __init__(self, wordChars = printables):
-        super(WordEnd,self).__init__()
-        self.wordChars = set(wordChars)
-        self.skipWhitespace = False
-        self.errmsg = "Not at the end of a word"
-
-    def parseImpl(self, instring, loc, doActions=True ):
-        instrlen = len(instring)
-        if instrlen>0 and loc<instrlen:
-            if (instring[loc] in self.wordChars or
-                instring[loc-1] not in self.wordChars):
-                raise ParseException(instring, loc, self.errmsg, self)
-        return loc, []
-
-
-class ParseExpression(ParserElement):
-    """Abstract subclass of ParserElement, for combining and
-    post-processing parsed tokens.
-    """
-    def __init__( self, exprs, savelist = False ):
-        super(ParseExpression,self).__init__(savelist)
-        if isinstance( exprs, _generatorType ):
-            exprs = list(exprs)
-
-        if isinstance( exprs, basestring ):
-            self.exprs = [ ParserElement._literalStringClass( exprs ) ]
-        elif isinstance( exprs, Iterable ):
-            exprs = list(exprs)
-            # if sequence of strings provided, wrap with Literal
-            if all(isinstance(expr, basestring) for expr in exprs):
-                exprs = map(ParserElement._literalStringClass, exprs)
-            self.exprs = list(exprs)
-        else:
-            try:
-                self.exprs = list( exprs )
-            except TypeError:
-                self.exprs = [ exprs ]
-        self.callPreparse = False
-
-    def __getitem__( self, i ):
-        return self.exprs[i]
-
-    def append( self, other ):
-        self.exprs.append( other )
-        self.strRepr = None
-        return self
-
-    def leaveWhitespace( self ):
-        """Extends ``leaveWhitespace`` defined in base class, and also invokes ``leaveWhitespace`` on
-           all contained expressions."""
-        self.skipWhitespace = False
-        self.exprs = [ e.copy() for e in self.exprs ]
-        for e in self.exprs:
-            e.leaveWhitespace()
-        return self
-
-    def ignore( self, other ):
-        if isinstance( other, Suppress ):
-            if other not in self.ignoreExprs:
-                super( ParseExpression, self).ignore( other )
-                for e in self.exprs:
-                    e.ignore( self.ignoreExprs[-1] )
-        else:
-            super( ParseExpression, self).ignore( other )
-            for e in self.exprs:
-                e.ignore( self.ignoreExprs[-1] )
-        return self
-
-    def __str__( self ):
-        try:
-            return super(ParseExpression,self).__str__()
-        except Exception:
-            pass
-
-        if self.strRepr is None:
-            self.strRepr = "%s:(%s)" % ( self.__class__.__name__, _ustr(self.exprs) )
-        return self.strRepr
-
-    def streamline( self ):
-        super(ParseExpression,self).streamline()
-
-        for e in self.exprs:
-            e.streamline()
-
-        # collapse nested And's of the form And( And( And( a,b), c), d) to And( a,b,c,d )
-        # but only if there are no parse actions or resultsNames on the nested And's
-        # (likewise for Or's and MatchFirst's)
-        if ( len(self.exprs) == 2 ):
-            other = self.exprs[0]
-            if ( isinstance( other, self.__class__ ) and
-                  not(other.parseAction) and
-                  other.resultsName is None and
-                  not other.debug ):
-                self.exprs = other.exprs[:] + [ self.exprs[1] ]
-                self.strRepr = None
-                self.mayReturnEmpty |= other.mayReturnEmpty
-                self.mayIndexError  |= other.mayIndexError
-
-            other = self.exprs[-1]
-            if ( isinstance( other, self.__class__ ) and
-                  not(other.parseAction) and
-                  other.resultsName is None and
-                  not other.debug ):
-                self.exprs = self.exprs[:-1] + other.exprs[:]
-                self.strRepr = None
-                self.mayReturnEmpty |= other.mayReturnEmpty
-                self.mayIndexError  |= other.mayIndexError
-
-        self.errmsg = "Expected " + _ustr(self)
-
-        return self
-
-    def setResultsName( self, name, listAllMatches=False ):
-        ret = super(ParseExpression,self).setResultsName(name,listAllMatches)
-        return ret
-
-    def validate( self, validateTrace=[] ):
-        tmp = validateTrace[:]+[self]
-        for e in self.exprs:
-            e.validate(tmp)
-        self.checkRecursion( [] )
-
-    def copy(self):
-        ret = super(ParseExpression,self).copy()
-        ret.exprs = [e.copy() for e in self.exprs]
-        return ret
-
-class And(ParseExpression):
-    """
-    Requires all given :class:`ParseExpression` s to be found in the given order.
-    Expressions may be separated by whitespace.
-    May be constructed using the ``'+'`` operator.
-    May also be constructed using the ``'-'`` operator, which will
-    suppress backtracking.
-
-    Example::
-
-        integer = Word(nums)
-        name_expr = OneOrMore(Word(alphas))
-
-        expr = And([integer("id"),name_expr("name"),integer("age")])
-        # more easily written as:
-        expr = integer("id") + name_expr("name") + integer("age")
-    """
-
-    class _ErrorStop(Empty):
-        def __init__(self, *args, **kwargs):
-            super(And._ErrorStop,self).__init__(*args, **kwargs)
-            self.name = '-'
-            self.leaveWhitespace()
-
-    def __init__( self, exprs, savelist = True ):
-        super(And,self).__init__(exprs, savelist)
-        self.mayReturnEmpty = all(e.mayReturnEmpty for e in self.exprs)
-        self.setWhitespaceChars( self.exprs[0].whiteChars )
-        self.skipWhitespace = self.exprs[0].skipWhitespace
-        self.callPreparse = True
-
-    def streamline(self):
-        super(And, self).streamline()
-        self.mayReturnEmpty = all(e.mayReturnEmpty for e in self.exprs)
-        return self
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        # pass False as last arg to _parse for first element, since we already
-        # pre-parsed the string as part of our And pre-parsing
-        loc, resultlist = self.exprs[0]._parse( instring, loc, doActions, callPreParse=False )
-        errorStop = False
-        for e in self.exprs[1:]:
-            if isinstance(e, And._ErrorStop):
-                errorStop = True
-                continue
-            if errorStop:
-                try:
-                    loc, exprtokens = e._parse( instring, loc, doActions )
-                except ParseSyntaxException:
-                    raise
-                except ParseBaseException as pe:
-                    pe.__traceback__ = None
-                    raise ParseSyntaxException._from_exception(pe)
-                except IndexError:
-                    raise ParseSyntaxException(instring, len(instring), self.errmsg, self)
-            else:
-                loc, exprtokens = e._parse( instring, loc, doActions )
-            if exprtokens or exprtokens.haskeys():
-                resultlist += exprtokens
-        return loc, resultlist
-
-    def __iadd__(self, other ):
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        return self.append( other ) #And( [ self, other ] )
-
-    def checkRecursion( self, parseElementList ):
-        subRecCheckList = parseElementList[:] + [ self ]
-        for e in self.exprs:
-            e.checkRecursion( subRecCheckList )
-            if not e.mayReturnEmpty:
-                break
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "{" + " ".join(_ustr(e) for e in self.exprs) + "}"
-
-        return self.strRepr
-
-
-class Or(ParseExpression):
-    """Requires that at least one :class:`ParseExpression` is found. If
-    two expressions match, the expression that matches the longest
-    string will be used. May be constructed using the ``'^'``
-    operator.
-
-    Example::
-
-        # construct Or using '^' operator
-
-        number = Word(nums) ^ Combine(Word(nums) + '.' + Word(nums))
-        print(number.searchString("123 3.1416 789"))
-
-    prints::
-
-        [['123'], ['3.1416'], ['789']]
-    """
-    def __init__( self, exprs, savelist = False ):
-        super(Or,self).__init__(exprs, savelist)
-        if self.exprs:
-            self.mayReturnEmpty = any(e.mayReturnEmpty for e in self.exprs)
-        else:
-            self.mayReturnEmpty = True
-
-    def streamline(self):
-        super(Or, self).streamline()
-        self.saveAsList = any(e.saveAsList for e in self.exprs)
-        return self
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        maxExcLoc = -1
-        maxException = None
-        matches = []
-        for e in self.exprs:
-            try:
-                loc2 = e.tryParse( instring, loc )
-            except ParseException as err:
-                err.__traceback__ = None
-                if err.loc > maxExcLoc:
-                    maxException = err
-                    maxExcLoc = err.loc
-            except IndexError:
-                if len(instring) > maxExcLoc:
-                    maxException = ParseException(instring,len(instring),e.errmsg,self)
-                    maxExcLoc = len(instring)
-            else:
-                # save match among all matches, to retry longest to shortest
-                matches.append((loc2, e))
-
-        if matches:
-            matches.sort(key=lambda x: -x[0])
-            for _,e in matches:
-                try:
-                    return e._parse( instring, loc, doActions )
-                except ParseException as err:
-                    err.__traceback__ = None
-                    if err.loc > maxExcLoc:
-                        maxException = err
-                        maxExcLoc = err.loc
-
-        if maxException is not None:
-            maxException.msg = self.errmsg
-            raise maxException
-        else:
-            raise ParseException(instring, loc, "no defined alternatives to match", self)
-
-
-    def __ixor__(self, other ):
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        return self.append( other ) #Or( [ self, other ] )
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "{" + " ^ ".join(_ustr(e) for e in self.exprs) + "}"
-
-        return self.strRepr
-
-    def checkRecursion( self, parseElementList ):
-        subRecCheckList = parseElementList[:] + [ self ]
-        for e in self.exprs:
-            e.checkRecursion( subRecCheckList )
-
-
-class MatchFirst(ParseExpression):
-    """Requires that at least one :class:`ParseExpression` is found. If
-    two expressions match, the first one listed is the one that will
-    match. May be constructed using the ``'|'`` operator.
-
-    Example::
-
-        # construct MatchFirst using '|' operator
-
-        # watch the order of expressions to match
-        number = Word(nums) | Combine(Word(nums) + '.' + Word(nums))
-        print(number.searchString("123 3.1416 789")) #  Fail! -> [['123'], ['3'], ['1416'], ['789']]
-
-        # put more selective expression first
-        number = Combine(Word(nums) + '.' + Word(nums)) | Word(nums)
-        print(number.searchString("123 3.1416 789")) #  Better -> [['123'], ['3.1416'], ['789']]
-    """
-    def __init__( self, exprs, savelist = False ):
-        super(MatchFirst,self).__init__(exprs, savelist)
-        if self.exprs:
-            self.mayReturnEmpty = any(e.mayReturnEmpty for e in self.exprs)
-            # self.saveAsList = any(e.saveAsList for e in self.exprs)
-        else:
-            self.mayReturnEmpty = True
-
-    def streamline(self):
-        super(MatchFirst, self).streamline()
-        self.saveAsList = any(e.saveAsList for e in self.exprs)
-        return self
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        maxExcLoc = -1
-        maxException = None
-        for e in self.exprs:
-            try:
-                ret = e._parse( instring, loc, doActions )
-                return ret
-            except ParseException as err:
-                if err.loc > maxExcLoc:
-                    maxException = err
-                    maxExcLoc = err.loc
-            except IndexError:
-                if len(instring) > maxExcLoc:
-                    maxException = ParseException(instring,len(instring),e.errmsg,self)
-                    maxExcLoc = len(instring)
-
-        # only got here if no expression matched, raise exception for match that made it the furthest
-        else:
-            if maxException is not None:
-                maxException.msg = self.errmsg
-                raise maxException
-            else:
-                raise ParseException(instring, loc, "no defined alternatives to match", self)
-
-    def __ior__(self, other ):
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass( other )
-        return self.append( other ) #MatchFirst( [ self, other ] )
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "{" + " | ".join(_ustr(e) for e in self.exprs) + "}"
-
-        return self.strRepr
-
-    def checkRecursion( self, parseElementList ):
-        subRecCheckList = parseElementList[:] + [ self ]
-        for e in self.exprs:
-            e.checkRecursion( subRecCheckList )
-
-
-class Each(ParseExpression):
-    """Requires all given :class:`ParseExpression` s to be found, but in
-    any order. Expressions may be separated by whitespace.
-
-    May be constructed using the ``'&'`` operator.
-
-    Example::
-
-        color = oneOf("RED ORANGE YELLOW GREEN BLUE PURPLE BLACK WHITE BROWN")
-        shape_type = oneOf("SQUARE CIRCLE TRIANGLE STAR HEXAGON OCTAGON")
-        integer = Word(nums)
-        shape_attr = "shape:" + shape_type("shape")
-        posn_attr = "posn:" + Group(integer("x") + ',' + integer("y"))("posn")
-        color_attr = "color:" + color("color")
-        size_attr = "size:" + integer("size")
-
-        # use Each (using operator '&') to accept attributes in any order
-        # (shape and posn are required, color and size are optional)
-        shape_spec = shape_attr & posn_attr & Optional(color_attr) & Optional(size_attr)
-
-        shape_spec.runTests('''
-            shape: SQUARE color: BLACK posn: 100, 120
-            shape: CIRCLE size: 50 color: BLUE posn: 50,80
-            color:GREEN size:20 shape:TRIANGLE posn:20,40
-            '''
-            )
-
-    prints::
-
-        shape: SQUARE color: BLACK posn: 100, 120
-        ['shape:', 'SQUARE', 'color:', 'BLACK', 'posn:', ['100', ',', '120']]
-        - color: BLACK
-        - posn: ['100', ',', '120']
-          - x: 100
-          - y: 120
-        - shape: SQUARE
-
-
-        shape: CIRCLE size: 50 color: BLUE posn: 50,80
-        ['shape:', 'CIRCLE', 'size:', '50', 'color:', 'BLUE', 'posn:', ['50', ',', '80']]
-        - color: BLUE
-        - posn: ['50', ',', '80']
-          - x: 50
-          - y: 80
-        - shape: CIRCLE
-        - size: 50
-
-
-        color: GREEN size: 20 shape: TRIANGLE posn: 20,40
-        ['color:', 'GREEN', 'size:', '20', 'shape:', 'TRIANGLE', 'posn:', ['20', ',', '40']]
-        - color: GREEN
-        - posn: ['20', ',', '40']
-          - x: 20
-          - y: 40
-        - shape: TRIANGLE
-        - size: 20
-    """
-    def __init__( self, exprs, savelist = True ):
-        super(Each,self).__init__(exprs, savelist)
-        self.mayReturnEmpty = all(e.mayReturnEmpty for e in self.exprs)
-        self.skipWhitespace = True
-        self.initExprGroups = True
-        self.saveAsList = True
-
-    def streamline(self):
-        super(Each, self).streamline()
-        self.mayReturnEmpty = all(e.mayReturnEmpty for e in self.exprs)
-        return self
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if self.initExprGroups:
-            self.opt1map = dict((id(e.expr),e) for e in self.exprs if isinstance(e,Optional))
-            opt1 = [ e.expr for e in self.exprs if isinstance(e,Optional) ]
-            opt2 = [ e for e in self.exprs if e.mayReturnEmpty and not isinstance(e,Optional)]
-            self.optionals = opt1 + opt2
-            self.multioptionals = [ e.expr for e in self.exprs if isinstance(e,ZeroOrMore) ]
-            self.multirequired = [ e.expr for e in self.exprs if isinstance(e,OneOrMore) ]
-            self.required = [ e for e in self.exprs if not isinstance(e,(Optional,ZeroOrMore,OneOrMore)) ]
-            self.required += self.multirequired
-            self.initExprGroups = False
-        tmpLoc = loc
-        tmpReqd = self.required[:]
-        tmpOpt  = self.optionals[:]
-        matchOrder = []
-
-        keepMatching = True
-        while keepMatching:
-            tmpExprs = tmpReqd + tmpOpt + self.multioptionals + self.multirequired
-            failed = []
-            for e in tmpExprs:
-                try:
-                    tmpLoc = e.tryParse( instring, tmpLoc )
-                except ParseException:
-                    failed.append(e)
-                else:
-                    matchOrder.append(self.opt1map.get(id(e),e))
-                    if e in tmpReqd:
-                        tmpReqd.remove(e)
-                    elif e in tmpOpt:
-                        tmpOpt.remove(e)
-            if len(failed) == len(tmpExprs):
-                keepMatching = False
-
-        if tmpReqd:
-            missing = ", ".join(_ustr(e) for e in tmpReqd)
-            raise ParseException(instring,loc,"Missing one or more required elements (%s)" % missing )
-
-        # add any unmatched Optionals, in case they have default values defined
-        matchOrder += [e for e in self.exprs if isinstance(e,Optional) and e.expr in tmpOpt]
-
-        resultlist = []
-        for e in matchOrder:
-            loc,results = e._parse(instring,loc,doActions)
-            resultlist.append(results)
-
-        finalResults = sum(resultlist, ParseResults([]))
-        return loc, finalResults
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "{" + " & ".join(_ustr(e) for e in self.exprs) + "}"
-
-        return self.strRepr
-
-    def checkRecursion( self, parseElementList ):
-        subRecCheckList = parseElementList[:] + [ self ]
-        for e in self.exprs:
-            e.checkRecursion( subRecCheckList )
-
-
-class ParseElementEnhance(ParserElement):
-    """Abstract subclass of :class:`ParserElement`, for combining and
-    post-processing parsed tokens.
-    """
-    def __init__( self, expr, savelist=False ):
-        super(ParseElementEnhance,self).__init__(savelist)
-        if isinstance( expr, basestring ):
-            if issubclass(ParserElement._literalStringClass, Token):
-                expr = ParserElement._literalStringClass(expr)
-            else:
-                expr = ParserElement._literalStringClass(Literal(expr))
-        self.expr = expr
-        self.strRepr = None
-        if expr is not None:
-            self.mayIndexError = expr.mayIndexError
-            self.mayReturnEmpty = expr.mayReturnEmpty
-            self.setWhitespaceChars( expr.whiteChars )
-            self.skipWhitespace = expr.skipWhitespace
-            self.saveAsList = expr.saveAsList
-            self.callPreparse = expr.callPreparse
-            self.ignoreExprs.extend(expr.ignoreExprs)
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if self.expr is not None:
-            return self.expr._parse( instring, loc, doActions, callPreParse=False )
-        else:
-            raise ParseException("",loc,self.errmsg,self)
-
-    def leaveWhitespace( self ):
-        self.skipWhitespace = False
-        self.expr = self.expr.copy()
-        if self.expr is not None:
-            self.expr.leaveWhitespace()
-        return self
-
-    def ignore( self, other ):
-        if isinstance( other, Suppress ):
-            if other not in self.ignoreExprs:
-                super( ParseElementEnhance, self).ignore( other )
-                if self.expr is not None:
-                    self.expr.ignore( self.ignoreExprs[-1] )
-        else:
-            super( ParseElementEnhance, self).ignore( other )
-            if self.expr is not None:
-                self.expr.ignore( self.ignoreExprs[-1] )
-        return self
-
-    def streamline( self ):
-        super(ParseElementEnhance,self).streamline()
-        if self.expr is not None:
-            self.expr.streamline()
-        return self
-
-    def checkRecursion( self, parseElementList ):
-        if self in parseElementList:
-            raise RecursiveGrammarException( parseElementList+[self] )
-        subRecCheckList = parseElementList[:] + [ self ]
-        if self.expr is not None:
-            self.expr.checkRecursion( subRecCheckList )
-
-    def validate( self, validateTrace=[] ):
-        tmp = validateTrace[:]+[self]
-        if self.expr is not None:
-            self.expr.validate(tmp)
-        self.checkRecursion( [] )
-
-    def __str__( self ):
-        try:
-            return super(ParseElementEnhance,self).__str__()
-        except Exception:
-            pass
-
-        if self.strRepr is None and self.expr is not None:
-            self.strRepr = "%s:(%s)" % ( self.__class__.__name__, _ustr(self.expr) )
-        return self.strRepr
-
-
-class FollowedBy(ParseElementEnhance):
-    """Lookahead matching of the given parse expression.
-    ``FollowedBy`` does *not* advance the parsing position within
-    the input string, it only verifies that the specified parse
-    expression matches at the current position.  ``FollowedBy``
-    always returns a null token list. If any results names are defined
-    in the lookahead expression, those *will* be returned for access by
-    name.
-
-    Example::
-
-        # use FollowedBy to match a label only if it is followed by a ':'
-        data_word = Word(alphas)
-        label = data_word + FollowedBy(':')
-        attr_expr = Group(label + Suppress(':') + OneOrMore(data_word, stopOn=label).setParseAction(' '.join))
-
-        OneOrMore(attr_expr).parseString("shape: SQUARE color: BLACK posn: upper left").pprint()
-
-    prints::
-
-        [['shape', 'SQUARE'], ['color', 'BLACK'], ['posn', 'upper left']]
-    """
-    def __init__( self, expr ):
-        super(FollowedBy,self).__init__(expr)
-        self.mayReturnEmpty = True
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        _, ret = self.expr._parse(instring, loc, doActions=doActions)
-        del ret[:]
-        return loc, ret
-
-
-class PrecededBy(ParseElementEnhance):
-    """Lookbehind matching of the given parse expression.
-    ``PrecededBy`` does not advance the parsing position within the
-    input string, it only verifies that the specified parse expression
-    matches prior to the current position.  ``PrecededBy`` always
-    returns a null token list, but if a results name is defined on the
-    given expression, it is returned.
-
-    Parameters:
-
-     - expr - expression that must match prior to the current parse
-       location
-     - retreat - (default= ``None``) - (int) maximum number of characters
-       to lookbehind prior to the current parse location
-
-    If the lookbehind expression is a string, Literal, Keyword, or
-    a Word or CharsNotIn with a specified exact or maximum length, then
-    the retreat parameter is not required. Otherwise, retreat must be
-    specified to give a maximum number of characters to look back from
-    the current parse position for a lookbehind match.
-
-    Example::
-
-        # VB-style variable names with type prefixes
-        int_var = PrecededBy("#") + pyparsing_common.identifier
-        str_var = PrecededBy("$") + pyparsing_common.identifier
-
-    """
-    def __init__(self, expr, retreat=None):
-        super(PrecededBy, self).__init__(expr)
-        self.expr = self.expr().leaveWhitespace()
-        self.mayReturnEmpty = True
-        self.mayIndexError = False
-        self.exact = False
-        if isinstance(expr, str):
-            retreat = len(expr)
-            self.exact = True
-        elif isinstance(expr, (Literal, Keyword)):
-            retreat = expr.matchLen
-            self.exact = True
-        elif isinstance(expr, (Word, CharsNotIn)) and expr.maxLen != _MAX_INT:
-            retreat = expr.maxLen
-            self.exact = True
-        elif isinstance(expr, _PositionToken):
-            retreat = 0
-            self.exact = True
-        self.retreat = retreat
-        self.errmsg = "not preceded by " + str(expr)
-        self.skipWhitespace = False
-
-    def parseImpl(self, instring, loc=0, doActions=True):
-        if self.exact:
-            if loc < self.retreat:
-                raise ParseException(instring, loc, self.errmsg)
-            start = loc - self.retreat
-            _, ret = self.expr._parse(instring, start)
-        else:
-            # retreat specified a maximum lookbehind window, iterate
-            test_expr = self.expr + StringEnd()
-            instring_slice = instring[:loc]
-            last_expr = ParseException(instring, loc, self.errmsg)
-            for offset in range(1, min(loc, self.retreat+1)):
-                try:
-                    _, ret = test_expr._parse(instring_slice, loc-offset)
-                except ParseBaseException as pbe:
-                    last_expr = pbe
-                else:
-                    break
-            else:
-                raise last_expr
-        # return empty list of tokens, but preserve any defined results names
-        del ret[:]
-        return loc, ret
-
-
-class NotAny(ParseElementEnhance):
-    """Lookahead to disallow matching with the given parse expression.
-    ``NotAny`` does *not* advance the parsing position within the
-    input string, it only verifies that the specified parse expression
-    does *not* match at the current position.  Also, ``NotAny`` does
-    *not* skip over leading whitespace. ``NotAny`` always returns
-    a null token list.  May be constructed using the '~' operator.
-
-    Example::
-
-        AND, OR, NOT = map(CaselessKeyword, "AND OR NOT".split())
-
-        # take care not to mistake keywords for identifiers
-        ident = ~(AND | OR | NOT) + Word(alphas)
-        boolean_term = Optional(NOT) + ident
-
-        # very crude boolean expression - to support parenthesis groups and
-        # operation hierarchy, use infixNotation
-        boolean_expr = boolean_term + ZeroOrMore((AND | OR) + boolean_term)
-
-        # integers that are followed by "." are actually floats
-        integer = Word(nums) + ~Char(".")
-    """
-    def __init__( self, expr ):
-        super(NotAny,self).__init__(expr)
-        #~ self.leaveWhitespace()
-        self.skipWhitespace = False  # do NOT use self.leaveWhitespace(), don't want to propagate to exprs
-        self.mayReturnEmpty = True
-        self.errmsg = "Found unwanted token, "+_ustr(self.expr)
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        if self.expr.canParseNext(instring, loc):
-            raise ParseException(instring, loc, self.errmsg, self)
-        return loc, []
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "~{" + _ustr(self.expr) + "}"
-
-        return self.strRepr
-
-class _MultipleMatch(ParseElementEnhance):
-    def __init__( self, expr, stopOn=None):
-        super(_MultipleMatch, self).__init__(expr)
-        self.saveAsList = True
-        ender = stopOn
-        if isinstance(ender, basestring):
-            ender = ParserElement._literalStringClass(ender)
-        self.not_ender = ~ender if ender is not None else None
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        self_expr_parse = self.expr._parse
-        self_skip_ignorables = self._skipIgnorables
-        check_ender = self.not_ender is not None
-        if check_ender:
-            try_not_ender = self.not_ender.tryParse
-
-        # must be at least one (but first see if we are the stopOn sentinel;
-        # if so, fail)
-        if check_ender:
-            try_not_ender(instring, loc)
-        loc, tokens = self_expr_parse( instring, loc, doActions, callPreParse=False )
-        try:
-            hasIgnoreExprs = (not not self.ignoreExprs)
-            while 1:
-                if check_ender:
-                    try_not_ender(instring, loc)
-                if hasIgnoreExprs:
-                    preloc = self_skip_ignorables( instring, loc )
-                else:
-                    preloc = loc
-                loc, tmptokens = self_expr_parse( instring, preloc, doActions )
-                if tmptokens or tmptokens.haskeys():
-                    tokens += tmptokens
-        except (ParseException,IndexError):
-            pass
-
-        return loc, tokens
-
-class OneOrMore(_MultipleMatch):
-    """Repetition of one or more of the given expression.
-
-    Parameters:
-     - expr - expression that must match one or more times
-     - stopOn - (default= ``None``) - expression for a terminating sentinel
-          (only required if the sentinel would ordinarily match the repetition
-          expression)
-
-    Example::
-
-        data_word = Word(alphas)
-        label = data_word + FollowedBy(':')
-        attr_expr = Group(label + Suppress(':') + OneOrMore(data_word).setParseAction(' '.join))
-
-        text = "shape: SQUARE posn: upper left color: BLACK"
-        OneOrMore(attr_expr).parseString(text).pprint()  # Fail! read 'color' as data instead of next label -> [['shape', 'SQUARE color']]
-
-        # use stopOn attribute for OneOrMore to avoid reading label string as part of the data
-        attr_expr = Group(label + Suppress(':') + OneOrMore(data_word, stopOn=label).setParseAction(' '.join))
-        OneOrMore(attr_expr).parseString(text).pprint() # Better -> [['shape', 'SQUARE'], ['posn', 'upper left'], ['color', 'BLACK']]
-
-        # could also be written as
-        (attr_expr * (1,)).parseString(text).pprint()
-    """
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "{" + _ustr(self.expr) + "}..."
-
-        return self.strRepr
-
-class ZeroOrMore(_MultipleMatch):
-    """Optional repetition of zero or more of the given expression.
-
-    Parameters:
-     - expr - expression that must match zero or more times
-     - stopOn - (default= ``None``) - expression for a terminating sentinel
-          (only required if the sentinel would ordinarily match the repetition
-          expression)
-
-    Example: similar to :class:`OneOrMore`
-    """
-    def __init__( self, expr, stopOn=None):
-        super(ZeroOrMore,self).__init__(expr, stopOn=stopOn)
-        self.mayReturnEmpty = True
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        try:
-            return super(ZeroOrMore, self).parseImpl(instring, loc, doActions)
-        except (ParseException,IndexError):
-            return loc, []
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "[" + _ustr(self.expr) + "]..."
-
-        return self.strRepr
-
-class _NullToken(object):
-    def __bool__(self):
-        return False
-    __nonzero__ = __bool__
-    def __str__(self):
-        return ""
-
-_optionalNotMatched = _NullToken()
-class Optional(ParseElementEnhance):
-    """Optional matching of the given expression.
-
-    Parameters:
-     - expr - expression that must match zero or more times
-     - default (optional) - value to be returned if the optional expression is not found.
-
-    Example::
-
-        # US postal code can be a 5-digit zip, plus optional 4-digit qualifier
-        zip = Combine(Word(nums, exact=5) + Optional('-' + Word(nums, exact=4)))
-        zip.runTests('''
-            # traditional ZIP code
-            12345
-
-            # ZIP+4 form
-            12101-0001
-
-            # invalid ZIP
-            98765-
-            ''')
-
-    prints::
-
-        # traditional ZIP code
-        12345
-        ['12345']
-
-        # ZIP+4 form
-        12101-0001
-        ['12101-0001']
-
-        # invalid ZIP
-        98765-
-             ^
-        FAIL: Expected end of text (at char 5), (line:1, col:6)
-    """
-    def __init__( self, expr, default=_optionalNotMatched ):
-        super(Optional,self).__init__( expr, savelist=False )
-        self.saveAsList = self.expr.saveAsList
-        self.defaultValue = default
-        self.mayReturnEmpty = True
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        try:
-            loc, tokens = self.expr._parse( instring, loc, doActions, callPreParse=False )
-        except (ParseException,IndexError):
-            if self.defaultValue is not _optionalNotMatched:
-                if self.expr.resultsName:
-                    tokens = ParseResults([ self.defaultValue ])
-                    tokens[self.expr.resultsName] = self.defaultValue
-                else:
-                    tokens = [ self.defaultValue ]
-            else:
-                tokens = []
-        return loc, tokens
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-
-        if self.strRepr is None:
-            self.strRepr = "[" + _ustr(self.expr) + "]"
-
-        return self.strRepr
-
-class SkipTo(ParseElementEnhance):
-    """Token for skipping over all undefined text until the matched
-    expression is found.
-
-    Parameters:
-     - expr - target expression marking the end of the data to be skipped
-     - include - (default= ``False``) if True, the target expression is also parsed
-          (the skipped text and target expression are returned as a 2-element list).
-     - ignore - (default= ``None``) used to define grammars (typically quoted strings and
-          comments) that might contain false matches to the target expression
-     - failOn - (default= ``None``) define expressions that are not allowed to be
-          included in the skipped test; if found before the target expression is found,
-          the SkipTo is not a match
-
-    Example::
-
-        report = '''
-            Outstanding Issues Report - 1 Jan 2000
-
-               # | Severity | Description                               |  Days Open
-            -----+----------+-------------------------------------------+-----------
-             101 | Critical | Intermittent system crash                 |          6
-              94 | Cosmetic | Spelling error on Login ('log|n')         |         14
-              79 | Minor    | System slow when running too many reports |         47
-            '''
-        integer = Word(nums)
-        SEP = Suppress('|')
-        # use SkipTo to simply match everything up until the next SEP
-        # - ignore quoted strings, so that a '|' character inside a quoted string does not match
-        # - parse action will call token.strip() for each matched token, i.e., the description body
-        string_data = SkipTo(SEP, ignore=quotedString)
-        string_data.setParseAction(tokenMap(str.strip))
-        ticket_expr = (integer("issue_num") + SEP
-                      + string_data("sev") + SEP
-                      + string_data("desc") + SEP
-                      + integer("days_open"))
-
-        for tkt in ticket_expr.searchString(report):
-            print tkt.dump()
-
-    prints::
-
-        ['101', 'Critical', 'Intermittent system crash', '6']
-        - days_open: 6
-        - desc: Intermittent system crash
-        - issue_num: 101
-        - sev: Critical
-        ['94', 'Cosmetic', "Spelling error on Login ('log|n')", '14']
-        - days_open: 14
-        - desc: Spelling error on Login ('log|n')
-        - issue_num: 94
-        - sev: Cosmetic
-        ['79', 'Minor', 'System slow when running too many reports', '47']
-        - days_open: 47
-        - desc: System slow when running too many reports
-        - issue_num: 79
-        - sev: Minor
-    """
-    def __init__( self, other, include=False, ignore=None, failOn=None ):
-        super( SkipTo, self ).__init__( other )
-        self.ignoreExpr = ignore
-        self.mayReturnEmpty = True
-        self.mayIndexError = False
-        self.includeMatch = include
-        self.saveAsList = False
-        if isinstance(failOn, basestring):
-            self.failOn = ParserElement._literalStringClass(failOn)
-        else:
-            self.failOn = failOn
-        self.errmsg = "No match found for "+_ustr(self.expr)
-
-    def parseImpl( self, instring, loc, doActions=True ):
-        startloc = loc
-        instrlen = len(instring)
-        expr = self.expr
-        expr_parse = self.expr._parse
-        self_failOn_canParseNext = self.failOn.canParseNext if self.failOn is not None else None
-        self_ignoreExpr_tryParse = self.ignoreExpr.tryParse if self.ignoreExpr is not None else None
-
-        tmploc = loc
-        while tmploc <= instrlen:
-            if self_failOn_canParseNext is not None:
-                # break if failOn expression matches
-                if self_failOn_canParseNext(instring, tmploc):
-                    break
-
-            if self_ignoreExpr_tryParse is not None:
-                # advance past ignore expressions
-                while 1:
-                    try:
-                        tmploc = self_ignoreExpr_tryParse(instring, tmploc)
-                    except ParseBaseException:
-                        break
-
-            try:
-                expr_parse(instring, tmploc, doActions=False, callPreParse=False)
-            except (ParseException, IndexError):
-                # no match, advance loc in string
-                tmploc += 1
-            else:
-                # matched skipto expr, done
-                break
-
-        else:
-            # ran off the end of the input string without matching skipto expr, fail
-            raise ParseException(instring, loc, self.errmsg, self)
-
-        # build up return values
-        loc = tmploc
-        skiptext = instring[startloc:loc]
-        skipresult = ParseResults(skiptext)
-
-        if self.includeMatch:
-            loc, mat = expr_parse(instring,loc,doActions,callPreParse=False)
-            skipresult += mat
-
-        return loc, skipresult
-
-class Forward(ParseElementEnhance):
-    """Forward declaration of an expression to be defined later -
-    used for recursive grammars, such as algebraic infix notation.
-    When the expression is known, it is assigned to the ``Forward``
-    variable using the '<<' operator.
-
-    Note: take care when assigning to ``Forward`` not to overlook
-    precedence of operators.
-
-    Specifically, '|' has a lower precedence than '<<', so that::
-
-        fwdExpr << a | b | c
-
-    will actually be evaluated as::
-
-        (fwdExpr << a) | b | c
-
-    thereby leaving b and c out as parseable alternatives.  It is recommended that you
-    explicitly group the values inserted into the ``Forward``::
-
-        fwdExpr << (a | b | c)
-
-    Converting to use the '<<=' operator instead will avoid this problem.
-
-    See :class:`ParseResults.pprint` for an example of a recursive
-    parser created using ``Forward``.
-    """
-    def __init__( self, other=None ):
-        super(Forward,self).__init__( other, savelist=False )
-
-    def __lshift__( self, other ):
-        if isinstance( other, basestring ):
-            other = ParserElement._literalStringClass(other)
-        self.expr = other
-        self.strRepr = None
-        self.mayIndexError = self.expr.mayIndexError
-        self.mayReturnEmpty = self.expr.mayReturnEmpty
-        self.setWhitespaceChars( self.expr.whiteChars )
-        self.skipWhitespace = self.expr.skipWhitespace
-        self.saveAsList = self.expr.saveAsList
-        self.ignoreExprs.extend(self.expr.ignoreExprs)
-        return self
-
-    def __ilshift__(self, other):
-        return self << other
-
-    def leaveWhitespace( self ):
-        self.skipWhitespace = False
-        return self
-
-    def streamline( self ):
-        if not self.streamlined:
-            self.streamlined = True
-            if self.expr is not None:
-                self.expr.streamline()
-        return self
-
-    def validate( self, validateTrace=[] ):
-        if self not in validateTrace:
-            tmp = validateTrace[:]+[self]
-            if self.expr is not None:
-                self.expr.validate(tmp)
-        self.checkRecursion([])
-
-    def __str__( self ):
-        if hasattr(self,"name"):
-            return self.name
-        return self.__class__.__name__ + ": ..."
-
-        # stubbed out for now - creates awful memory and perf issues
-        self._revertClass = self.__class__
-        self.__class__ = _ForwardNoRecurse
-        try:
-            if self.expr is not None:
-                retString = _ustr(self.expr)
-            else:
-                retString = "None"
-        finally:
-            self.__class__ = self._revertClass
-        return self.__class__.__name__ + ": " + retString
-
-    def copy(self):
-        if self.expr is not None:
-            return super(Forward,self).copy()
-        else:
-            ret = Forward()
-            ret <<= self
-            return ret
-
-class _ForwardNoRecurse(Forward):
-    def __str__( self ):
-        return "..."
-
-class TokenConverter(ParseElementEnhance):
-    """
-    Abstract subclass of :class:`ParseExpression`, for converting parsed results.
-    """
-    def __init__( self, expr, savelist=False ):
-        super(TokenConverter,self).__init__( expr )#, savelist )
-        self.saveAsList = False
-
-class Combine(TokenConverter):
-    """Converter to concatenate all matching tokens to a single string.
-    By default, the matching patterns must also be contiguous in the
-    input string; this can be disabled by specifying
-    ``'adjacent=False'`` in the constructor.
-
-    Example::
-
-        real = Word(nums) + '.' + Word(nums)
-        print(real.parseString('3.1416')) # -> ['3', '.', '1416']
-        # will also erroneously match the following
-        print(real.parseString('3. 1416')) # -> ['3', '.', '1416']
-
-        real = Combine(Word(nums) + '.' + Word(nums))
-        print(real.parseString('3.1416')) # -> ['3.1416']
-        # no match when there are internal spaces
-        print(real.parseString('3. 1416')) # -> Exception: Expected W:(0123...)
-    """
-    def __init__( self, expr, joinString="", adjacent=True ):
-        super(Combine,self).__init__( expr )
-        # suppress whitespace-stripping in contained parse expressions, but re-enable it on the Combine itself
-        if adjacent:
-            self.leaveWhitespace()
-        self.adjacent = adjacent
-        self.skipWhitespace = True
-        self.joinString = joinString
-        self.callPreparse = True
-
-    def ignore( self, other ):
-        if self.adjacent:
-            ParserElement.ignore(self, other)
-        else:
-            super( Combine, self).ignore( other )
-        return self
-
-    def postParse( self, instring, loc, tokenlist ):
-        retToks = tokenlist.copy()
-        del retToks[:]
-        retToks += ParseResults([ "".join(tokenlist._asStringList(self.joinString)) ], modal=self.modalResults)
-
-        if self.resultsName and retToks.haskeys():
-            return [ retToks ]
-        else:
-            return retToks
-
-class Group(TokenConverter):
-    """Converter to return the matched tokens as a list - useful for
-    returning tokens of :class:`ZeroOrMore` and :class:`OneOrMore` expressions.
-
-    Example::
-
-        ident = Word(alphas)
-        num = Word(nums)
-        term = ident | num
-        func = ident + Optional(delimitedList(term))
-        print(func.parseString("fn a,b,100"))  # -> ['fn', 'a', 'b', '100']
-
-        func = ident + Group(Optional(delimitedList(term)))
-        print(func.parseString("fn a,b,100"))  # -> ['fn', ['a', 'b', '100']]
-    """
-    def __init__( self, expr ):
-        super(Group,self).__init__( expr )
-        self.saveAsList = expr.saveAsList
-
-    def postParse( self, instring, loc, tokenlist ):
-        return [ tokenlist ]
-
-class Dict(TokenConverter):
-    """Converter to return a repetitive expression as a list, but also
-    as a dictionary. Each element can also be referenced using the first
-    token in the expression as its key. Useful for tabular report
-    scraping when the first column can be used as a item key.
-
-    Example::
-
-        data_word = Word(alphas)
-        label = data_word + FollowedBy(':')
-        attr_expr = Group(label + Suppress(':') + OneOrMore(data_word).setParseAction(' '.join))
-
-        text = "shape: SQUARE posn: upper left color: light blue texture: burlap"
-        attr_expr = (label + Suppress(':') + OneOrMore(data_word, stopOn=label).setParseAction(' '.join))
-
-        # print attributes as plain groups
-        print(OneOrMore(attr_expr).parseString(text).dump())
-
-        # instead of OneOrMore(expr), parse using Dict(OneOrMore(Group(expr))) - Dict will auto-assign names
-        result = Dict(OneOrMore(Group(attr_expr))).parseString(text)
-        print(result.dump())
-
-        # access named fields as dict entries, or output as dict
-        print(result['shape'])
-        print(result.asDict())
-
-    prints::
-
-        ['shape', 'SQUARE', 'posn', 'upper left', 'color', 'light blue', 'texture', 'burlap']
-        [['shape', 'SQUARE'], ['posn', 'upper left'], ['color', 'light blue'], ['texture', 'burlap']]
-        - color: light blue
-        - posn: upper left
-        - shape: SQUARE
-        - texture: burlap
-        SQUARE
-        {'color': 'light blue', 'posn': 'upper left', 'texture': 'burlap', 'shape': 'SQUARE'}
-
-    See more examples at :class:`ParseResults` of accessing fields by results name.
-    """
-    def __init__( self, expr ):
-        super(Dict,self).__init__( expr )
-        self.saveAsList = True
-
-    def postParse( self, instring, loc, tokenlist ):
-        for i,tok in enumerate(tokenlist):
-            if len(tok) == 0:
-                continue
-            ikey = tok[0]
-            if isinstance(ikey,int):
-                ikey = _ustr(tok[0]).strip()
-            if len(tok)==1:
-                tokenlist[ikey] = _ParseResultsWithOffset("",i)
-            elif len(tok)==2 and not isinstance(tok[1],ParseResults):
-                tokenlist[ikey] = _ParseResultsWithOffset(tok[1],i)
-            else:
-                dictvalue = tok.copy() #ParseResults(i)
-                del dictvalue[0]
-                if len(dictvalue)!= 1 or (isinstance(dictvalue,ParseResults) and dictvalue.haskeys()):
-                    tokenlist[ikey] = _ParseResultsWithOffset(dictvalue,i)
-                else:
-                    tokenlist[ikey] = _ParseResultsWithOffset(dictvalue[0],i)
-
-        if self.resultsName:
-            return [ tokenlist ]
-        else:
-            return tokenlist
-
-
-class Suppress(TokenConverter):
-    """Converter for ignoring the results of a parsed expression.
-
-    Example::
-
-        source = "a, b, c,d"
-        wd = Word(alphas)
-        wd_list1 = wd + ZeroOrMore(',' + wd)
-        print(wd_list1.parseString(source))
-
-        # often, delimiters that are useful during parsing are just in the
-        # way afterward - use Suppress to keep them out of the parsed output
-        wd_list2 = wd + ZeroOrMore(Suppress(',') + wd)
-        print(wd_list2.parseString(source))
-
-    prints::
-
-        ['a', ',', 'b', ',', 'c', ',', 'd']
-        ['a', 'b', 'c', 'd']
-
-    (See also :class:`delimitedList`.)
-    """
-    def postParse( self, instring, loc, tokenlist ):
-        return []
-
-    def suppress( self ):
-        return self
-
-
-class OnlyOnce(object):
-    """Wrapper for parse actions, to ensure they are only called once.
-    """
-    def __init__(self, methodCall):
-        self.callable = _trim_arity(methodCall)
-        self.called = False
-    def __call__(self,s,l,t):
-        if not self.called:
-            results = self.callable(s,l,t)
-            self.called = True
-            return results
-        raise ParseException(s,l,"")
-    def reset(self):
-        self.called = False
-
-def traceParseAction(f):
-    """Decorator for debugging parse actions.
-
-    When the parse action is called, this decorator will print
-    ``">> entering method-name(line:<current_source_line>, <parse_location>, <matched_tokens>)"``.
-    When the parse action completes, the decorator will print
-    ``"<<"`` followed by the returned value, or any exception that the parse action raised.
-
-    Example::
-
-        wd = Word(alphas)
-
-        @traceParseAction
-        def remove_duplicate_chars(tokens):
-            return ''.join(sorted(set(''.join(tokens))))
-
-        wds = OneOrMore(wd).setParseAction(remove_duplicate_chars)
-        print(wds.parseString("slkdjs sld sldd sdlf sdljf"))
-
-    prints::
-
-        >>entering remove_duplicate_chars(line: 'slkdjs sld sldd sdlf sdljf', 0, (['slkdjs', 'sld', 'sldd', 'sdlf', 'sdljf'], {}))
-        <<leaving remove_duplicate_chars (ret: 'dfjkls')
-        ['dfjkls']
-    """
-    f = _trim_arity(f)
-    def z(*paArgs):
-        thisFunc = f.__name__
-        s,l,t = paArgs[-3:]
-        if len(paArgs)>3:
-            thisFunc = paArgs[0].__class__.__name__ + '.' + thisFunc
-        sys.stderr.write( ">>entering %s(line: '%s', %d, %r)\n" % (thisFunc,line(l,s),l,t) )
-        try:
-            ret = f(*paArgs)
-        except Exception as exc:
-            sys.stderr.write( "<<leaving %s (exception: %s)\n" % (thisFunc,exc) )
-            raise
-        sys.stderr.write( "<<leaving %s (ret: %r)\n" % (thisFunc,ret) )
-        return ret
-    try:
-        z.__name__ = f.__name__
-    except AttributeError:
-        pass
-    return z
-
-#
-# global helpers
-#
-def delimitedList( expr, delim=",", combine=False ):
-    """Helper to define a delimited list of expressions - the delimiter
-    defaults to ','. By default, the list elements and delimiters can
-    have intervening whitespace, and comments, but this can be
-    overridden by passing ``combine=True`` in the constructor. If
-    ``combine`` is set to ``True``, the matching tokens are
-    returned as a single token string, with the delimiters included;
-    otherwise, the matching tokens are returned as a list of tokens,
-    with the delimiters suppressed.
-
-    Example::
-
-        delimitedList(Word(alphas)).parseString("aa,bb,cc") # -> ['aa', 'bb', 'cc']
-        delimitedList(Word(hexnums), delim=':', combine=True).parseString("AA:BB:CC:DD:EE") # -> ['AA:BB:CC:DD:EE']
-    """
-    dlName = _ustr(expr)+" ["+_ustr(delim)+" "+_ustr(expr)+"]..."
-    if combine:
-        return Combine( expr + ZeroOrMore( delim + expr ) ).setName(dlName)
-    else:
-        return ( expr + ZeroOrMore( Suppress( delim ) + expr ) ).setName(dlName)
-
-def countedArray( expr, intExpr=None ):
-    """Helper to define a counted list of expressions.
-
-    This helper defines a pattern of the form::
-
-        integer expr expr expr...
-
-    where the leading integer tells how many expr expressions follow.
-    The matched tokens returns the array of expr tokens as a list - the
-    leading count token is suppressed.
-
-    If ``intExpr`` is specified, it should be a pyparsing expression
-    that produces an integer value.
-
-    Example::
-
-        countedArray(Word(alphas)).parseString('2 ab cd ef')  # -> ['ab', 'cd']
-
-        # in this parser, the leading integer value is given in binary,
-        # '10' indicating that 2 values are in the array
-        binaryConstant = Word('01').setParseAction(lambda t: int(t[0], 2))
-        countedArray(Word(alphas), intExpr=binaryConstant).parseString('10 ab cd ef')  # -> ['ab', 'cd']
-    """
-    arrayExpr = Forward()
-    def countFieldParseAction(s,l,t):
-        n = t[0]
-        arrayExpr << (n and Group(And([expr]*n)) or Group(empty))
-        return []
-    if intExpr is None:
-        intExpr = Word(nums).setParseAction(lambda t:int(t[0]))
-    else:
-        intExpr = intExpr.copy()
-    intExpr.setName("arrayLen")
-    intExpr.addParseAction(countFieldParseAction, callDuringTry=True)
-    return ( intExpr + arrayExpr ).setName('(len) ' + _ustr(expr) + '...')
-
-def _flatten(L):
-    ret = []
-    for i in L:
-        if isinstance(i,list):
-            ret.extend(_flatten(i))
-        else:
-            ret.append(i)
-    return ret
-
-def matchPreviousLiteral(expr):
-    """Helper to define an expression that is indirectly defined from
-    the tokens matched in a previous expression, that is, it looks for
-    a 'repeat' of a previous expression.  For example::
-
-        first = Word(nums)
-        second = matchPreviousLiteral(first)
-        matchExpr = first + ":" + second
-
-    will match ``"1:1"``, but not ``"1:2"``.  Because this
-    matches a previous literal, will also match the leading
-    ``"1:1"`` in ``"1:10"``. If this is not desired, use
-    :class:`matchPreviousExpr`. Do *not* use with packrat parsing
-    enabled.
-    """
-    rep = Forward()
-    def copyTokenToRepeater(s,l,t):
-        if t:
-            if len(t) == 1:
-                rep << t[0]
-            else:
-                # flatten t tokens
-                tflat = _flatten(t.asList())
-                rep << And(Literal(tt) for tt in tflat)
-        else:
-            rep << Empty()
-    expr.addParseAction(copyTokenToRepeater, callDuringTry=True)
-    rep.setName('(prev) ' + _ustr(expr))
-    return rep
-
-def matchPreviousExpr(expr):
-    """Helper to define an expression that is indirectly defined from
-    the tokens matched in a previous expression, that is, it looks for
-    a 'repeat' of a previous expression.  For example::
-
-        first = Word(nums)
-        second = matchPreviousExpr(first)
-        matchExpr = first + ":" + second
-
-    will match ``"1:1"``, but not ``"1:2"``.  Because this
-    matches by expressions, will *not* match the leading ``"1:1"``
-    in ``"1:10"``; the expressions are evaluated first, and then
-    compared, so ``"1"`` is compared with ``"10"``. Do *not* use
-    with packrat parsing enabled.
-    """
-    rep = Forward()
-    e2 = expr.copy()
-    rep <<= e2
-    def copyTokenToRepeater(s,l,t):
-        matchTokens = _flatten(t.asList())
-        def mustMatchTheseTokens(s,l,t):
-            theseTokens = _flatten(t.asList())
-            if  theseTokens != matchTokens:
-                raise ParseException("",0,"")
-        rep.setParseAction( mustMatchTheseTokens, callDuringTry=True )
-    expr.addParseAction(copyTokenToRepeater, callDuringTry=True)
-    rep.setName('(prev) ' + _ustr(expr))
-    return rep
-
-def _escapeRegexRangeChars(s):
-    #~  escape these chars: ^-]
-    for c in r"\^-]":
-        s = s.replace(c,_bslash+c)
-    s = s.replace("\n",r"\n")
-    s = s.replace("\t",r"\t")
-    return _ustr(s)
-
-def oneOf( strs, caseless=False, useRegex=True ):
-    """Helper to quickly define a set of alternative Literals, and makes
-    sure to do longest-first testing when there is a conflict,
-    regardless of the input order, but returns
-    a :class:`MatchFirst` for best performance.
-
-    Parameters:
-
-     - strs - a string of space-delimited literals, or a collection of
-       string literals
-     - caseless - (default= ``False``) - treat all literals as
-       caseless
-     - useRegex - (default= ``True``) - as an optimization, will
-       generate a Regex object; otherwise, will generate
-       a :class:`MatchFirst` object (if ``caseless=True``, or if
-       creating a :class:`Regex` raises an exception)
-
-    Example::
-
-        comp_oper = oneOf("< = > <= >= !=")
-        var = Word(alphas)
-        number = Word(nums)
-        term = var | number
-        comparison_expr = term + comp_oper + term
-        print(comparison_expr.searchString("B = 12  AA=23 B<=AA AA>12"))
-
-    prints::
-
-        [['B', '=', '12'], ['AA', '=', '23'], ['B', '<=', 'AA'], ['AA', '>', '12']]
-    """
-    if caseless:
-        isequal = ( lambda a,b: a.upper() == b.upper() )
-        masks = ( lambda a,b: b.upper().startswith(a.upper()) )
-        parseElementClass = CaselessLiteral
-    else:
-        isequal = ( lambda a,b: a == b )
-        masks = ( lambda a,b: b.startswith(a) )
-        parseElementClass = Literal
-
-    symbols = []
-    if isinstance(strs,basestring):
-        symbols = strs.split()
-    elif isinstance(strs, Iterable):
-        symbols = list(strs)
-    else:
-        warnings.warn("Invalid argument to oneOf, expected string or iterable",
-                SyntaxWarning, stacklevel=2)
-    if not symbols:
-        return NoMatch()
-
-    i = 0
-    while i < len(symbols)-1:
-        cur = symbols[i]
-        for j,other in enumerate(symbols[i+1:]):
-            if ( isequal(other, cur) ):
-                del symbols[i+j+1]
-                break
-            elif ( masks(cur, other) ):
-                del symbols[i+j+1]
-                symbols.insert(i,other)
-                cur = other
-                break
-        else:
-            i += 1
-
-    if not caseless and useRegex:
-        #~ print (strs,"->", "|".join( [ _escapeRegexChars(sym) for sym in symbols] ))
-        try:
-            if len(symbols)==len("".join(symbols)):
-                return Regex( "[%s]" % "".join(_escapeRegexRangeChars(sym) for sym in symbols) ).setName(' | '.join(symbols))
-            else:
-                return Regex( "|".join(re.escape(sym) for sym in symbols) ).setName(' | '.join(symbols))
-        except Exception:
-            warnings.warn("Exception creating Regex for oneOf, building MatchFirst",
-                    SyntaxWarning, stacklevel=2)
-
-
-    # last resort, just use MatchFirst
-    return MatchFirst(parseElementClass(sym) for sym in symbols).setName(' | '.join(symbols))
-
-def dictOf( key, value ):
-    """Helper to easily and clearly define a dictionary by specifying
-    the respective patterns for the key and value.  Takes care of
-    defining the :class:`Dict`, :class:`ZeroOrMore`, and
-    :class:`Group` tokens in the proper order.  The key pattern
-    can include delimiting markers or punctuation, as long as they are
-    suppressed, thereby leaving the significant key text.  The value
-    pattern can include named results, so that the :class:`Dict` results
-    can include named token fields.
-
-    Example::
-
-        text = "shape: SQUARE posn: upper left color: light blue texture: burlap"
-        attr_expr = (label + Suppress(':') + OneOrMore(data_word, stopOn=label).setParseAction(' '.join))
-        print(OneOrMore(attr_expr).parseString(text).dump())
-
-        attr_label = label
-        attr_value = Suppress(':') + OneOrMore(data_word, stopOn=label).setParseAction(' '.join)
-
-        # similar to Dict, but simpler call format
-        result = dictOf(attr_label, attr_value).parseString(text)
-        print(result.dump())
-        print(result['shape'])
-        print(result.shape)  # object attribute access works too
-        print(result.asDict())
-
-    prints::
-
-        [['shape', 'SQUARE'], ['posn', 'upper left'], ['color', 'light blue'], ['texture', 'burlap']]
-        - color: light blue
-        - posn: upper left
-        - shape: SQUARE
-        - texture: burlap
-        SQUARE
-        SQUARE
-        {'color': 'light blue', 'shape': 'SQUARE', 'posn': 'upper left', 'texture': 'burlap'}
-    """
-    return Dict(OneOrMore(Group(key + value)))
-
-def originalTextFor(expr, asString=True):
-    """Helper to return the original, untokenized text for a given
-    expression.  Useful to restore the parsed fields of an HTML start
-    tag into the raw tag text itself, or to revert separate tokens with
-    intervening whitespace back to the original matching input text. By
-    default, returns astring containing the original parsed text.
-
-    If the optional ``asString`` argument is passed as
-    ``False``, then the return value is
-    a :class:`ParseResults` containing any results names that
-    were originally matched, and a single token containing the original
-    matched text from the input string.  So if the expression passed to
-    :class:`originalTextFor` contains expressions with defined
-    results names, you must set ``asString`` to ``False`` if you
-    want to preserve those results name values.
-
-    Example::
-
-        src = "this is test <b> bold <i>text</i> </b> normal text "
-        for tag in ("b","i"):
-            opener,closer = makeHTMLTags(tag)
-            patt = originalTextFor(opener + SkipTo(closer) + closer)
-            print(patt.searchString(src)[0])
-
-    prints::
-
-        ['<b> bold <i>text</i> </b>']
-        ['<i>text</i>']
-    """
-    locMarker = Empty().setParseAction(lambda s,loc,t: loc)
-    endlocMarker = locMarker.copy()
-    endlocMarker.callPreparse = False
-    matchExpr = locMarker("_original_start") + expr + endlocMarker("_original_end")
-    if asString:
-        extractText = lambda s,l,t: s[t._original_start:t._original_end]
-    else:
-        def extractText(s,l,t):
-            t[:] = [s[t.pop('_original_start'):t.pop('_original_end')]]
-    matchExpr.setParseAction(extractText)
-    matchExpr.ignoreExprs = expr.ignoreExprs
-    return matchExpr
-
-def ungroup(expr):
-    """Helper to undo pyparsing's default grouping of And expressions,
-    even if all but one are non-empty.
-    """
-    return TokenConverter(expr).setParseAction(lambda t:t[0])
-
-def locatedExpr(expr):
-    """Helper to decorate a returned token with its starting and ending
-    locations in the input string.
-
-    This helper adds the following results names:
-
-     - locn_start = location where matched expression begins
-     - locn_end = location where matched expression ends
-     - value = the actual parsed results
-
-    Be careful if the input text contains ``<TAB>`` characters, you
-    may want to call :class:`ParserElement.parseWithTabs`
-
-    Example::
-
-        wd = Word(alphas)
-        for match in locatedExpr(wd).searchString("ljsdf123lksdjjf123lkkjj1222"):
-            print(match)
-
-    prints::
-
-        [[0, 'ljsdf', 5]]
-        [[8, 'lksdjjf', 15]]
-        [[18, 'lkkjj', 23]]
-    """
-    locator = Empty().setParseAction(lambda s,l,t: l)
-    return Group(locator("locn_start") + expr("value") + locator.copy().leaveWhitespace()("locn_end"))
-
-
-# convenience constants for positional expressions
-empty       = Empty().setName("empty")
-lineStart   = LineStart().setName("lineStart")
-lineEnd     = LineEnd().setName("lineEnd")
-stringStart = StringStart().setName("stringStart")
-stringEnd   = StringEnd().setName("stringEnd")
-
-_escapedPunc = Word( _bslash, r"\[]-*.$+^?()~ ", exact=2 ).setParseAction(lambda s,l,t:t[0][1])
-_escapedHexChar = Regex(r"\\0?[xX][0-9a-fA-F]+").setParseAction(lambda s,l,t:unichr(int(t[0].lstrip(r'\0x'),16)))
-_escapedOctChar = Regex(r"\\0[0-7]+").setParseAction(lambda s,l,t:unichr(int(t[0][1:],8)))
-_singleChar = _escapedPunc | _escapedHexChar | _escapedOctChar | CharsNotIn(r'\]', exact=1)
-_charRange = Group(_singleChar + Suppress("-") + _singleChar)
-_reBracketExpr = Literal("[") + Optional("^").setResultsName("negate") + Group( OneOrMore( _charRange | _singleChar ) ).setResultsName("body") + "]"
-
-def srange(s):
-    r"""Helper to easily define string ranges for use in Word
-    construction. Borrows syntax from regexp '[]' string range
-    definitions::
-
-        srange("[0-9]")   -> "0123456789"
-        srange("[a-z]")   -> "abcdefghijklmnopqrstuvwxyz"
-        srange("[a-z$_]") -> "abcdefghijklmnopqrstuvwxyz$_"
-
-    The input string must be enclosed in []'s, and the returned string
-    is the expanded character set joined into a single string. The
-    values enclosed in the []'s may be:
-
-     - a single character
-     - an escaped character with a leading backslash (such as ``\-``
-       or ``\]``)
-     - an escaped hex character with a leading ``'\x'``
-       (``\x21``, which is a ``'!'`` character) (``\0x##``
-       is also supported for backwards compatibility)
-     - an escaped octal character with a leading ``'\0'``
-       (``\041``, which is a ``'!'`` character)
-     - a range of any of the above, separated by a dash (``'a-z'``,
-       etc.)
-     - any combination of the above (``'aeiouy'``,
-       ``'a-zA-Z0-9_$'``, etc.)
-    """
-    _expanded = lambda p: p if not isinstance(p,ParseResults) else ''.join(unichr(c) for c in range(ord(p[0]),ord(p[1])+1))
-    try:
-        return "".join(_expanded(part) for part in _reBracketExpr.parseString(s).body)
-    except Exception:
-        return ""
-
-def matchOnlyAtCol(n):
-    """Helper method for defining parse actions that require matching at
-    a specific column in the input text.
-    """
-    def verifyCol(strg,locn,toks):
-        if col(locn,strg) != n:
-            raise ParseException(strg,locn,"matched token not at column %d" % n)
-    return verifyCol
-
-def replaceWith(replStr):
-    """Helper method for common parse actions that simply return
-    a literal value.  Especially useful when used with
-    :class:`transformString<ParserElement.transformString>` ().
-
-    Example::
-
-        num = Word(nums).setParseAction(lambda toks: int(toks[0]))
-        na = oneOf("N/A NA").setParseAction(replaceWith(math.nan))
-        term = na | num
-
-        OneOrMore(term).parseString("324 234 N/A 234") # -> [324, 234, nan, 234]
-    """
-    return lambda s,l,t: [replStr]
-
-def removeQuotes(s,l,t):
-    """Helper parse action for removing quotation marks from parsed
-    quoted strings.
-
-    Example::
-
-        # by default, quotation marks are included in parsed results
-        quotedString.parseString("'Now is the Winter of our Discontent'") # -> ["'Now is the Winter of our Discontent'"]
-
-        # use removeQuotes to strip quotation marks from parsed results
-        quotedString.setParseAction(removeQuotes)
-        quotedString.parseString("'Now is the Winter of our Discontent'") # -> ["Now is the Winter of our Discontent"]
-    """
-    return t[0][1:-1]
-
-def tokenMap(func, *args):
-    """Helper to define a parse action by mapping a function to all
-    elements of a ParseResults list. If any additional args are passed,
-    they are forwarded to the given function as additional arguments
-    after the token, as in
-    ``hex_integer = Word(hexnums).setParseAction(tokenMap(int, 16))``,
-    which will convert the parsed data to an integer using base 16.
-
-    Example (compare the last to example in :class:`ParserElement.transformString`::
-
-        hex_ints = OneOrMore(Word(hexnums)).setParseAction(tokenMap(int, 16))
-        hex_ints.runTests('''
-            00 11 22 aa FF 0a 0d 1a
-            ''')
-
-        upperword = Word(alphas).setParseAction(tokenMap(str.upper))
-        OneOrMore(upperword).runTests('''
-            my kingdom for a horse
-            ''')
-
-        wd = Word(alphas).setParseAction(tokenMap(str.title))
-        OneOrMore(wd).setParseAction(' '.join).runTests('''
-            now is the winter of our discontent made glorious summer by this sun of york
-            ''')
-
-    prints::
-
-        00 11 22 aa FF 0a 0d 1a
-        [0, 17, 34, 170, 255, 10, 13, 26]
-
-        my kingdom for a horse
-        ['MY', 'KINGDOM', 'FOR', 'A', 'HORSE']
-
-        now is the winter of our discontent made glorious summer by this sun of york
-        ['Now Is The Winter Of Our Discontent Made Glorious Summer By This Sun Of York']
-    """
-    def pa(s,l,t):
-        return [func(tokn, *args) for tokn in t]
-
-    try:
-        func_name = getattr(func, '__name__',
-                            getattr(func, '__class__').__name__)
-    except Exception:
-        func_name = str(func)
-    pa.__name__ = func_name
-
-    return pa
-
-upcaseTokens = tokenMap(lambda t: _ustr(t).upper())
-"""(Deprecated) Helper parse action to convert tokens to upper case.
-Deprecated in favor of :class:`pyparsing_common.upcaseTokens`"""
-
-downcaseTokens = tokenMap(lambda t: _ustr(t).lower())
-"""(Deprecated) Helper parse action to convert tokens to lower case.
-Deprecated in favor of :class:`pyparsing_common.downcaseTokens`"""
-
-def _makeTags(tagStr, xml):
-    """Internal helper to construct opening and closing tag expressions, given a tag name"""
-    if isinstance(tagStr,basestring):
-        resname = tagStr
-        tagStr = Keyword(tagStr, caseless=not xml)
-    else:
-        resname = tagStr.name
-
-    tagAttrName = Word(alphas,alphanums+"_-:")
-    if (xml):
-        tagAttrValue = dblQuotedString.copy().setParseAction( removeQuotes )
-        openTag = Suppress("<") + tagStr("tag") + \
-                Dict(ZeroOrMore(Group( tagAttrName + Suppress("=") + tagAttrValue ))) + \
-                Optional("/",default=[False]).setResultsName("empty").setParseAction(lambda s,l,t:t[0]=='/') + Suppress(">")
-    else:
-        printablesLessRAbrack = "".join(c for c in printables if c not in ">")
-        tagAttrValue = quotedString.copy().setParseAction( removeQuotes ) | Word(printablesLessRAbrack)
-        openTag = Suppress("<") + tagStr("tag") + \
-                Dict(ZeroOrMore(Group( tagAttrName.setParseAction(downcaseTokens) + \
-                Optional( Suppress("=") + tagAttrValue ) ))) + \
-                Optional("/",default=[False]).setResultsName("empty").setParseAction(lambda s,l,t:t[0]=='/') + Suppress(">")
-    closeTag = Combine(_L("</") + tagStr + ">")
-
-    openTag = openTag.setResultsName("start"+"".join(resname.replace(":"," ").title().split())).setName("<%s>" % resname)
-    closeTag = closeTag.setResultsName("end"+"".join(resname.replace(":"," ").title().split())).setName("</%s>" % resname)
-    openTag.tag = resname
-    closeTag.tag = resname
-    return openTag, closeTag
-
-def makeHTMLTags(tagStr):
-    """Helper to construct opening and closing tag expressions for HTML,
-    given a tag name. Matches tags in either upper or lower case,
-    attributes with namespaces and with quoted or unquoted values.
-
-    Example::
-
-        text = '<td>More info at the <a href="https://github.com/pyparsing/pyparsing/wiki">pyparsing</a> wiki page</td>'
-        # makeHTMLTags returns pyparsing expressions for the opening and
-        # closing tags as a 2-tuple
-        a,a_end = makeHTMLTags("A")
-        link_expr = a + SkipTo(a_end)("link_text") + a_end
-
-        for link in link_expr.searchString(text):
-            # attributes in the <A> tag (like "href" shown here) are
-            # also accessible as named results
-            print(link.link_text, '->', link.href)
-
-    prints::
-
-        pyparsing -> https://github.com/pyparsing/pyparsing/wiki
-    """
-    return _makeTags( tagStr, False )
-
-def makeXMLTags(tagStr):
-    """Helper to construct opening and closing tag expressions for XML,
-    given a tag name. Matches tags only in the given upper/lower case.
-
-    Example: similar to :class:`makeHTMLTags`
-    """
-    return _makeTags( tagStr, True )
-
-def withAttribute(*args,**attrDict):
-    """Helper to create a validating parse action to be used with start
-    tags created with :class:`makeXMLTags` or
-    :class:`makeHTMLTags`. Use ``withAttribute`` to qualify
-    a starting tag with a required attribute value, to avoid false
-    matches on common tags such as ``<TD>`` or ``<DIV>``.
-
-    Call ``withAttribute`` with a series of attribute names and
-    values. Specify the list of filter attributes names and values as:
-
-     - keyword arguments, as in ``(align="right")``, or
-     - as an explicit dict with ``**`` operator, when an attribute
-       name is also a Python reserved word, as in ``**{"class":"Customer", "align":"right"}``
-     - a list of name-value tuples, as in ``(("ns1:class", "Customer"), ("ns2:align","right"))``
-
-    For attribute names with a namespace prefix, you must use the second
-    form.  Attribute names are matched insensitive to upper/lower case.
-
-    If just testing for ``class`` (with or without a namespace), use
-    :class:`withClass`.
-
-    To verify that the attribute exists, but without specifying a value,
-    pass ``withAttribute.ANY_VALUE`` as the value.
-
-    Example::
-
-        html = '''
-            <div>
-            Some text
-            <div type="grid">1 4 0 1 0</div>
-            <div type="graph">1,3 2,3 1,1</div>
-            <div>this has no type</div>
-            </div>
-
-        '''
-        div,div_end = makeHTMLTags("div")
-
-        # only match div tag having a type attribute with value "grid"
-        div_grid = div().setParseAction(withAttribute(type="grid"))
-        grid_expr = div_grid + SkipTo(div | div_end)("body")
-        for grid_header in grid_expr.searchString(html):
-            print(grid_header.body)
-
-        # construct a match with any div tag having a type attribute, regardless of the value
-        div_any_type = div().setParseAction(withAttribute(type=withAttribute.ANY_VALUE))
-        div_expr = div_any_type + SkipTo(div | div_end)("body")
-        for div_header in div_expr.searchString(html):
-            print(div_header.body)
-
-    prints::
-
-        1 4 0 1 0
-
-        1 4 0 1 0
-        1,3 2,3 1,1
-    """
-    if args:
-        attrs = args[:]
-    else:
-        attrs = attrDict.items()
-    attrs = [(k,v) for k,v in attrs]
-    def pa(s,l,tokens):
-        for attrName,attrValue in attrs:
-            if attrName not in tokens:
-                raise ParseException(s,l,"no matching attribute " + attrName)
-            if attrValue != withAttribute.ANY_VALUE and tokens[attrName] != attrValue:
-                raise ParseException(s,l,"attribute '%s' has value '%s', must be '%s'" %
-                                            (attrName, tokens[attrName], attrValue))
-    return pa
-withAttribute.ANY_VALUE = object()
-
-def withClass(classname, namespace=''):
-    """Simplified version of :class:`withAttribute` when
-    matching on a div class - made difficult because ``class`` is
-    a reserved word in Python.
-
-    Example::
-
-        html = '''
-            <div>
-            Some text
-            <div class="grid">1 4 0 1 0</div>
-            <div class="graph">1,3 2,3 1,1</div>
-            <div>this &lt;div&gt; has no class</div>
-            </div>
-
-        '''
-        div,div_end = makeHTMLTags("div")
-        div_grid = div().setParseAction(withClass("grid"))
-
-        grid_expr = div_grid + SkipTo(div | div_end)("body")
-        for grid_header in grid_expr.searchString(html):
-            print(grid_header.body)
-
-        div_any_type = div().setParseAction(withClass(withAttribute.ANY_VALUE))
-        div_expr = div_any_type + SkipTo(div | div_end)("body")
-        for div_header in div_expr.searchString(html):
-            print(div_header.body)
-
-    prints::
-
-        1 4 0 1 0
-
-        1 4 0 1 0
-        1,3 2,3 1,1
-    """
-    classattr = "%s:class" % namespace if namespace else "class"
-    return withAttribute(**{classattr : classname})
-
-opAssoc = SimpleNamespace()
-opAssoc.LEFT = object()
-opAssoc.RIGHT = object()
-
-def infixNotation( baseExpr, opList, lpar=Suppress('('), rpar=Suppress(')') ):
-    """Helper method for constructing grammars of expressions made up of
-    operators working in a precedence hierarchy.  Operators may be unary
-    or binary, left- or right-associative.  Parse actions can also be
-    attached to operator expressions. The generated parser will also
-    recognize the use of parentheses to override operator precedences
-    (see example below).
-
-    Note: if you define a deep operator list, you may see performance
-    issues when using infixNotation. See
-    :class:`ParserElement.enablePackrat` for a mechanism to potentially
-    improve your parser performance.
-
-    Parameters:
-     - baseExpr - expression representing the most basic element for the
-       nested
-     - opList - list of tuples, one for each operator precedence level
-       in the expression grammar; each tuple is of the form ``(opExpr,
-       numTerms, rightLeftAssoc, parseAction)``, where:
-
-       - opExpr is the pyparsing expression for the operator; may also
-         be a string, which will be converted to a Literal; if numTerms
-         is 3, opExpr is a tuple of two expressions, for the two
-         operators separating the 3 terms
-       - numTerms is the number of terms for this operator (must be 1,
-         2, or 3)
-       - rightLeftAssoc is the indicator whether the operator is right
-         or left associative, using the pyparsing-defined constants
-         ``opAssoc.RIGHT`` and ``opAssoc.LEFT``.
-       - parseAction is the parse action to be associated with
-         expressions matching this operator expression (the parse action
-         tuple member may be omitted); if the parse action is passed
-         a tuple or list of functions, this is equivalent to calling
-         ``setParseAction(*fn)``
-         (:class:`ParserElement.setParseAction`)
-     - lpar - expression for matching left-parentheses
-       (default= ``Suppress('(')``)
-     - rpar - expression for matching right-parentheses
-       (default= ``Suppress(')')``)
-
-    Example::
-
-        # simple example of four-function arithmetic with ints and
-        # variable names
-        integer = pyparsing_common.signed_integer
-        varname = pyparsing_common.identifier
-
-        arith_expr = infixNotation(integer | varname,
-            [
-            ('-', 1, opAssoc.RIGHT),
-            (oneOf('* /'), 2, opAssoc.LEFT),
-            (oneOf('+ -'), 2, opAssoc.LEFT),
-            ])
-
-        arith_expr.runTests('''
-            5+3*6
-            (5+3)*6
-            -2--11
-            ''', fullDump=False)
-
-    prints::
-
-        5+3*6
-        [[5, '+', [3, '*', 6]]]
-
-        (5+3)*6
-        [[[5, '+', 3], '*', 6]]
-
-        -2--11
-        [[['-', 2], '-', ['-', 11]]]
-    """
-    # captive version of FollowedBy that does not do parse actions or capture results names
-    class _FB(FollowedBy):
-        def parseImpl(self, instring, loc, doActions=True):
-            self.expr.tryParse(instring, loc)
-            return loc, []
-
-    ret = Forward()
-    lastExpr = baseExpr | ( lpar + ret + rpar )
-    for i,operDef in enumerate(opList):
-        opExpr,arity,rightLeftAssoc,pa = (operDef + (None,))[:4]
-        termName = "%s term" % opExpr if arity < 3 else "%s%s term" % opExpr
-        if arity == 3:
-            if opExpr is None or len(opExpr) != 2:
-                raise ValueError(
-                    "if numterms=3, opExpr must be a tuple or list of two expressions")
-            opExpr1, opExpr2 = opExpr
-        thisExpr = Forward().setName(termName)
-        if rightLeftAssoc == opAssoc.LEFT:
-            if arity == 1:
-                matchExpr = _FB(lastExpr + opExpr) + Group( lastExpr + OneOrMore( opExpr ) )
-            elif arity == 2:
-                if opExpr is not None:
-                    matchExpr = _FB(lastExpr + opExpr + lastExpr) + Group( lastExpr + OneOrMore( opExpr + lastExpr ) )
-                else:
-                    matchExpr = _FB(lastExpr+lastExpr) + Group( lastExpr + OneOrMore(lastExpr) )
-            elif arity == 3:
-                matchExpr = _FB(lastExpr + opExpr1 + lastExpr + opExpr2 + lastExpr) + \
-                            Group( lastExpr + opExpr1 + lastExpr + opExpr2 + lastExpr )
-            else:
-                raise ValueError("operator must be unary (1), binary (2), or ternary (3)")
-        elif rightLeftAssoc == opAssoc.RIGHT:
-            if arity == 1:
-                # try to avoid LR with this extra test
-                if not isinstance(opExpr, Optional):
-                    opExpr = Optional(opExpr)
-                matchExpr = _FB(opExpr.expr + thisExpr) + Group( opExpr + thisExpr )
-            elif arity == 2:
-                if opExpr is not None:
-                    matchExpr = _FB(lastExpr + opExpr + thisExpr) + Group( lastExpr + OneOrMore( opExpr + thisExpr ) )
-                else:
-                    matchExpr = _FB(lastExpr + thisExpr) + Group( lastExpr + OneOrMore( thisExpr ) )
-            elif arity == 3:
-                matchExpr = _FB(lastExpr + opExpr1 + thisExpr + opExpr2 + thisExpr) + \
-                            Group( lastExpr + opExpr1 + thisExpr + opExpr2 + thisExpr )
-            else:
-                raise ValueError("operator must be unary (1), binary (2), or ternary (3)")
-        else:
-            raise ValueError("operator must indicate right or left associativity")
-        if pa:
-            if isinstance(pa, (tuple, list)):
-                matchExpr.setParseAction(*pa)
-            else:
-                matchExpr.setParseAction(pa)
-        thisExpr <<= ( matchExpr.setName(termName) | lastExpr )
-        lastExpr = thisExpr
-    ret <<= lastExpr
-    return ret
-
-operatorPrecedence = infixNotation
-"""(Deprecated) Former name of :class:`infixNotation`, will be
-dropped in a future release."""
-
-dblQuotedString = Combine(Regex(r'"(?:[^"\n\r\\]|(?:"")|(?:\\(?:[^x]|x[0-9a-fA-F]+)))*')+'"').setName("string enclosed in double quotes")
-sglQuotedString = Combine(Regex(r"'(?:[^'\n\r\\]|(?:'')|(?:\\(?:[^x]|x[0-9a-fA-F]+)))*")+"'").setName("string enclosed in single quotes")
-quotedString = Combine(Regex(r'"(?:[^"\n\r\\]|(?:"")|(?:\\(?:[^x]|x[0-9a-fA-F]+)))*')+'"'|
-                       Regex(r"'(?:[^'\n\r\\]|(?:'')|(?:\\(?:[^x]|x[0-9a-fA-F]+)))*")+"'").setName("quotedString using single or double quotes")
-unicodeString = Combine(_L('u') + quotedString.copy()).setName("unicode string literal")
-
-def nestedExpr(opener="(", closer=")", content=None, ignoreExpr=quotedString.copy()):
-    """Helper method for defining nested lists enclosed in opening and
-    closing delimiters ("(" and ")" are the default).
-
-    Parameters:
-     - opener - opening character for a nested list
-       (default= ``"("``); can also be a pyparsing expression
-     - closer - closing character for a nested list
-       (default= ``")"``); can also be a pyparsing expression
-     - content - expression for items within the nested lists
-       (default= ``None``)
-     - ignoreExpr - expression for ignoring opening and closing
-       delimiters (default= :class:`quotedString`)
-
-    If an expression is not provided for the content argument, the
-    nested expression will capture all whitespace-delimited content
-    between delimiters as a list of separate values.
-
-    Use the ``ignoreExpr`` argument to define expressions that may
-    contain opening or closing characters that should not be treated as
-    opening or closing characters for nesting, such as quotedString or
-    a comment expression.  Specify multiple expressions using an
-    :class:`Or` or :class:`MatchFirst`. The default is
-    :class:`quotedString`, but if no expressions are to be ignored, then
-    pass ``None`` for this argument.
-
-    Example::
-
-        data_type = oneOf("void int short long char float double")
-        decl_data_type = Combine(data_type + Optional(Word('*')))
-        ident = Word(alphas+'_', alphanums+'_')
-        number = pyparsing_common.number
-        arg = Group(decl_data_type + ident)
-        LPAR,RPAR = map(Suppress, "()")
-
-        code_body = nestedExpr('{', '}', ignoreExpr=(quotedString | cStyleComment))
-
-        c_function = (decl_data_type("type")
-                      + ident("name")
-                      + LPAR + Optional(delimitedList(arg), [])("args") + RPAR
-                      + code_body("body"))
-        c_function.ignore(cStyleComment)
-
-        source_code = '''
-            int is_odd(int x) {
-                return (x%2);
-            }
-
-            int dec_to_hex(char hchar) {
-                if (hchar >= '0' && hchar <= '9') {
-                    return (ord(hchar)-ord('0'));
-                } else {
-                    return (10+ord(hchar)-ord('A'));
-                }
-            }
-        '''
-        for func in c_function.searchString(source_code):
-            print("%(name)s (%(type)s) args: %(args)s" % func)
-
-
-    prints::
-
-        is_odd (int) args: [['int', 'x']]
-        dec_to_hex (int) args: [['char', 'hchar']]
-    """
-    if opener == closer:
-        raise ValueError("opening and closing strings cannot be the same")
-    if content is None:
-        if isinstance(opener,basestring) and isinstance(closer,basestring):
-            if len(opener) == 1 and len(closer)==1:
-                if ignoreExpr is not None:
-                    content = (Combine(OneOrMore(~ignoreExpr +
-                                    CharsNotIn(opener+closer+ParserElement.DEFAULT_WHITE_CHARS,exact=1))
-                                ).setParseAction(lambda t:t[0].strip()))
-                else:
-                    content = (empty.copy()+CharsNotIn(opener+closer+ParserElement.DEFAULT_WHITE_CHARS
-                                ).setParseAction(lambda t:t[0].strip()))
-            else:
-                if ignoreExpr is not None:
-                    content = (Combine(OneOrMore(~ignoreExpr +
-                                    ~Literal(opener) + ~Literal(closer) +
-                                    CharsNotIn(ParserElement.DEFAULT_WHITE_CHARS,exact=1))
-                                ).setParseAction(lambda t:t[0].strip()))
-                else:
-                    content = (Combine(OneOrMore(~Literal(opener) + ~Literal(closer) +
-                                    CharsNotIn(ParserElement.DEFAULT_WHITE_CHARS,exact=1))
-                                ).setParseAction(lambda t:t[0].strip()))
-        else:
-            raise ValueError("opening and closing arguments must be strings if no content expression is given")
-    ret = Forward()
-    if ignoreExpr is not None:
-        ret <<= Group( Suppress(opener) + ZeroOrMore( ignoreExpr | ret | content ) + Suppress(closer) )
-    else:
-        ret <<= Group( Suppress(opener) + ZeroOrMore( ret | content )  + Suppress(closer) )
-    ret.setName('nested %s%s expression' % (opener,closer))
-    return ret
-
-def indentedBlock(blockStatementExpr, indentStack, indent=True):
-    """Helper method for defining space-delimited indentation blocks,
-    such as those used to define block statements in Python source code.
-
-    Parameters:
-
-     - blockStatementExpr - expression defining syntax of statement that
-       is repeated within the indented block
-     - indentStack - list created by caller to manage indentation stack
-       (multiple statementWithIndentedBlock expressions within a single
-       grammar should share a common indentStack)
-     - indent - boolean indicating whether block must be indented beyond
-       the the current level; set to False for block of left-most
-       statements (default= ``True``)
-
-    A valid block must contain at least one ``blockStatement``.
-
-    Example::
-
-        data = '''
-        def A(z):
-          A1
-          B = 100
-          G = A2
-          A2
-          A3
-        B
-        def BB(a,b,c):
-          BB1
-          def BBA():
-            bba1
-            bba2
-            bba3
-        C
-        D
-        def spam(x,y):
-             def eggs(z):
-                 pass
-        '''
-
-
-        indentStack = [1]
-        stmt = Forward()
-
-        identifier = Word(alphas, alphanums)
-        funcDecl = ("def" + identifier + Group( "(" + Optional( delimitedList(identifier) ) + ")" ) + ":")
-        func_body = indentedBlock(stmt, indentStack)
-        funcDef = Group( funcDecl + func_body )
-
-        rvalue = Forward()
-        funcCall = Group(identifier + "(" + Optional(delimitedList(rvalue)) + ")")
-        rvalue << (funcCall | identifier | Word(nums))
-        assignment = Group(identifier + "=" + rvalue)
-        stmt << ( funcDef | assignment | identifier )
-
-        module_body = OneOrMore(stmt)
-
-        parseTree = module_body.parseString(data)
-        parseTree.pprint()
-
-    prints::
-
-        [['def',
-          'A',
-          ['(', 'z', ')'],
-          ':',
-          [['A1'], [['B', '=', '100']], [['G', '=', 'A2']], ['A2'], ['A3']]],
-         'B',
-         ['def',
-          'BB',
-          ['(', 'a', 'b', 'c', ')'],
-          ':',
-          [['BB1'], [['def', 'BBA', ['(', ')'], ':', [['bba1'], ['bba2'], ['bba3']]]]]],
-         'C',
-         'D',
-         ['def',
-          'spam',
-          ['(', 'x', 'y', ')'],
-          ':',
-          [[['def', 'eggs', ['(', 'z', ')'], ':', [['pass']]]]]]]
-    """
-    def checkPeerIndent(s,l,t):
-        if l >= len(s): return
-        curCol = col(l,s)
-        if curCol != indentStack[-1]:
-            if curCol > indentStack[-1]:
-                raise ParseFatalException(s,l,"illegal nesting")
-            raise ParseException(s,l,"not a peer entry")
-
-    def checkSubIndent(s,l,t):
-        curCol = col(l,s)
-        if curCol > indentStack[-1]:
-            indentStack.append( curCol )
-        else:
-            raise ParseException(s,l,"not a subentry")
-
-    def checkUnindent(s,l,t):
-        if l >= len(s): return
-        curCol = col(l,s)
-        if not(indentStack and curCol < indentStack[-1] and curCol <= indentStack[-2]):
-            raise ParseException(s,l,"not an unindent")
-        indentStack.pop()
-
-    NL = OneOrMore(LineEnd().setWhitespaceChars("\t ").suppress())
-    INDENT = (Empty() + Empty().setParseAction(checkSubIndent)).setName('INDENT')
-    PEER   = Empty().setParseAction(checkPeerIndent).setName('')
-    UNDENT = Empty().setParseAction(checkUnindent).setName('UNINDENT')
-    if indent:
-        smExpr = Group( Optional(NL) +
-            #~ FollowedBy(blockStatementExpr) +
-            INDENT + (OneOrMore( PEER + Group(blockStatementExpr) + Optional(NL) )) + UNDENT)
-    else:
-        smExpr = Group( Optional(NL) +
-            (OneOrMore( PEER + Group(blockStatementExpr) + Optional(NL) )) )
-    blockStatementExpr.ignore(_bslash + LineEnd())
-    return smExpr.setName('indented block')
-
-alphas8bit = srange(r"[\0xc0-\0xd6\0xd8-\0xf6\0xf8-\0xff]")
-punc8bit = srange(r"[\0xa1-\0xbf\0xd7\0xf7]")
-
-anyOpenTag,anyCloseTag = makeHTMLTags(Word(alphas,alphanums+"_:").setName('any tag'))
-_htmlEntityMap = dict(zip("gt lt amp nbsp quot apos".split(),'><& "\''))
-commonHTMLEntity = Regex('&(?P<entity>' + '|'.join(_htmlEntityMap.keys()) +");").setName("common HTML entity")
-def replaceHTMLEntity(t):
-    """Helper parser action to replace common HTML entities with their special characters"""
-    return _htmlEntityMap.get(t.entity)
-
-# it's easy to get these comment structures wrong - they're very common, so may as well make them available
-cStyleComment = Combine(Regex(r"/\*(?:[^*]|\*(?!/))*") + '*/').setName("C style comment")
-"Comment of the form ``/* ... */``"
-
-htmlComment = Regex(r"<!--[\s\S]*?-->").setName("HTML comment")
-"Comment of the form ``<!-- ... -->``"
-
-restOfLine = Regex(r".*").leaveWhitespace().setName("rest of line")
-dblSlashComment = Regex(r"//(?:\\\n|[^\n])*").setName("// comment")
-"Comment of the form ``// ... (to end of line)``"
-
-cppStyleComment = Combine(Regex(r"/\*(?:[^*]|\*(?!/))*") + '*/'| dblSlashComment).setName("C++ style comment")
-"Comment of either form :class:`cStyleComment` or :class:`dblSlashComment`"
-
-javaStyleComment = cppStyleComment
-"Same as :class:`cppStyleComment`"
-
-pythonStyleComment = Regex(r"#.*").setName("Python style comment")
-"Comment of the form ``# ... (to end of line)``"
-
-_commasepitem = Combine(OneOrMore(Word(printables, excludeChars=',') +
-                                  Optional( Word(" \t") +
-                                            ~Literal(",") + ~LineEnd() ) ) ).streamline().setName("commaItem")
-commaSeparatedList = delimitedList( Optional( quotedString.copy() | _commasepitem, default="") ).setName("commaSeparatedList")
-"""(Deprecated) Predefined expression of 1 or more printable words or
-quoted strings, separated by commas.
-
-This expression is deprecated in favor of :class:`pyparsing_common.comma_separated_list`.
-"""
-
-# some other useful expressions - using lower-case class name since we are really using this as a namespace
-class pyparsing_common:
-    """Here are some common low-level expressions that may be useful in
-    jump-starting parser development:
-
-     - numeric forms (:class:`integers<integer>`, :class:`reals<real>`,
-       :class:`scientific notation<sci_real>`)
-     - common :class:`programming identifiers<identifier>`
-     - network addresses (:class:`MAC<mac_address>`,
-       :class:`IPv4<ipv4_address>`, :class:`IPv6<ipv6_address>`)
-     - ISO8601 :class:`dates<iso8601_date>` and
-       :class:`datetime<iso8601_datetime>`
-     - :class:`UUID<uuid>`
-     - :class:`comma-separated list<comma_separated_list>`
-
-    Parse actions:
-
-     - :class:`convertToInteger`
-     - :class:`convertToFloat`
-     - :class:`convertToDate`
-     - :class:`convertToDatetime`
-     - :class:`stripHTMLTags`
-     - :class:`upcaseTokens`
-     - :class:`downcaseTokens`
-
-    Example::
-
-        pyparsing_common.number.runTests('''
-            # any int or real number, returned as the appropriate type
-            100
-            -100
-            +100
-            3.14159
-            6.02e23
-            1e-12
-            ''')
-
-        pyparsing_common.fnumber.runTests('''
-            # any int or real number, returned as float
-            100
-            -100
-            +100
-            3.14159
-            6.02e23
-            1e-12
-            ''')
-
-        pyparsing_common.hex_integer.runTests('''
-            # hex numbers
-            100
-            FF
-            ''')
-
-        pyparsing_common.fraction.runTests('''
-            # fractions
-            1/2
-            -3/4
-            ''')
-
-        pyparsing_common.mixed_integer.runTests('''
-            # mixed fractions
-            1
-            1/2
-            -3/4
-            1-3/4
-            ''')
-
-        import uuid
-        pyparsing_common.uuid.setParseAction(tokenMap(uuid.UUID))
-        pyparsing_common.uuid.runTests('''
-            # uuid
-            12345678-1234-5678-1234-567812345678
-            ''')
-
-    prints::
-
-        # any int or real number, returned as the appropriate type
-        100
-        [100]
-
-        -100
-        [-100]
-
-        +100
-        [100]
-
-        3.14159
-        [3.14159]
-
-        6.02e23
-        [6.02e+23]
-
-        1e-12
-        [1e-12]
-
-        # any int or real number, returned as float
-        100
-        [100.0]
-
-        -100
-        [-100.0]
-
-        +100
-        [100.0]
-
-        3.14159
-        [3.14159]
-
-        6.02e23
-        [6.02e+23]
-
-        1e-12
-        [1e-12]
-
-        # hex numbers
-        100
-        [256]
-
-        FF
-        [255]
-
-        # fractions
-        1/2
-        [0.5]
-
-        -3/4
-        [-0.75]
-
-        # mixed fractions
-        1
-        [1]
-
-        1/2
-        [0.5]
-
-        -3/4
-        [-0.75]
-
-        1-3/4
-        [1.75]
-
-        # uuid
-        12345678-1234-5678-1234-567812345678
-        [UUID('12345678-1234-5678-1234-567812345678')]
-    """
-
-    convertToInteger = tokenMap(int)
-    """
-    Parse action for converting parsed integers to Python int
-    """
-
-    convertToFloat = tokenMap(float)
-    """
-    Parse action for converting parsed numbers to Python float
-    """
-
-    integer = Word(nums).setName("integer").setParseAction(convertToInteger)
-    """expression that parses an unsigned integer, returns an int"""
-
-    hex_integer = Word(hexnums).setName("hex integer").setParseAction(tokenMap(int,16))
-    """expression that parses a hexadecimal integer, returns an int"""
-
-    signed_integer = Regex(r'[+-]?\d+').setName("signed integer").setParseAction(convertToInteger)
-    """expression that parses an integer with optional leading sign, returns an int"""
-
-    fraction = (signed_integer().setParseAction(convertToFloat) + '/' + signed_integer().setParseAction(convertToFloat)).setName("fraction")
-    """fractional expression of an integer divided by an integer, returns a float"""
-    fraction.addParseAction(lambda t: t[0]/t[-1])
-
-    mixed_integer = (fraction | signed_integer + Optional(Optional('-').suppress() + fraction)).setName("fraction or mixed integer-fraction")
-    """mixed integer of the form 'integer - fraction', with optional leading integer, returns float"""
-    mixed_integer.addParseAction(sum)
-
-    real = Regex(r'[+-]?\d+\.\d*').setName("real number").setParseAction(convertToFloat)
-    """expression that parses a floating point number and returns a float"""
-
-    sci_real = Regex(r'[+-]?\d+([eE][+-]?\d+|\.\d*([eE][+-]?\d+)?)').setName("real number with scientific notation").setParseAction(convertToFloat)
-    """expression that parses a floating point number with optional
-    scientific notation and returns a float"""
-
-    # streamlining this expression makes the docs nicer-looking
-    number = (sci_real | real | signed_integer).streamline()
-    """any numeric expression, returns the corresponding Python type"""
-
-    fnumber = Regex(r'[+-]?\d+\.?\d*([eE][+-]?\d+)?').setName("fnumber").setParseAction(convertToFloat)
-    """any int or real number, returned as float"""
-
-    identifier = Word(alphas+'_', alphanums+'_').setName("identifier")
-    """typical code identifier (leading alpha or '_', followed by 0 or more alphas, nums, or '_')"""
-
-    ipv4_address = Regex(r'(25[0-5]|2[0-4][0-9]|1?[0-9]{1,2})(\.(25[0-5]|2[0-4][0-9]|1?[0-9]{1,2})){3}').setName("IPv4 address")
-    "IPv4 address (``0.0.0.0 - 255.255.255.255``)"
-
-    _ipv6_part = Regex(r'[0-9a-fA-F]{1,4}').setName("hex_integer")
-    _full_ipv6_address = (_ipv6_part + (':' + _ipv6_part)*7).setName("full IPv6 address")
-    _short_ipv6_address = (Optional(_ipv6_part + (':' + _ipv6_part)*(0,6)) + "::" + Optional(_ipv6_part + (':' + _ipv6_part)*(0,6))).setName("short IPv6 address")
-    _short_ipv6_address.addCondition(lambda t: sum(1 for tt in t if pyparsing_common._ipv6_part.matches(tt)) < 8)
-    _mixed_ipv6_address = ("::ffff:" + ipv4_address).setName("mixed IPv6 address")
-    ipv6_address = Combine((_full_ipv6_address | _mixed_ipv6_address | _short_ipv6_address).setName("IPv6 address")).setName("IPv6 address")
-    "IPv6 address (long, short, or mixed form)"
-
-    mac_address = Regex(r'[0-9a-fA-F]{2}([:.-])[0-9a-fA-F]{2}(?:\1[0-9a-fA-F]{2}){4}').setName("MAC address")
-    "MAC address xx:xx:xx:xx:xx (may also have '-' or '.' delimiters)"
-
-    @staticmethod
-    def convertToDate(fmt="%Y-%m-%d"):
-        """
-        Helper to create a parse action for converting parsed date string to Python datetime.date
-
-        Params -
-         - fmt - format to be passed to datetime.strptime (default= ``"%Y-%m-%d"``)
-
-        Example::
-
-            date_expr = pyparsing_common.iso8601_date.copy()
-            date_expr.setParseAction(pyparsing_common.convertToDate())
-            print(date_expr.parseString("1999-12-31"))
-
-        prints::
-
-            [datetime.date(1999, 12, 31)]
-        """
-        def cvt_fn(s,l,t):
-            try:
-                return datetime.strptime(t[0], fmt).date()
-            except ValueError as ve:
-                raise ParseException(s, l, str(ve))
-        return cvt_fn
-
-    @staticmethod
-    def convertToDatetime(fmt="%Y-%m-%dT%H:%M:%S.%f"):
-        """Helper to create a parse action for converting parsed
-        datetime string to Python datetime.datetime
-
-        Params -
-         - fmt - format to be passed to datetime.strptime (default= ``"%Y-%m-%dT%H:%M:%S.%f"``)
-
-        Example::
-
-            dt_expr = pyparsing_common.iso8601_datetime.copy()
-            dt_expr.setParseAction(pyparsing_common.convertToDatetime())
-            print(dt_expr.parseString("1999-12-31T23:59:59.999"))
-
-        prints::
-
-            [datetime.datetime(1999, 12, 31, 23, 59, 59, 999000)]
-        """
-        def cvt_fn(s,l,t):
-            try:
-                return datetime.strptime(t[0], fmt)
-            except ValueError as ve:
-                raise ParseException(s, l, str(ve))
-        return cvt_fn
-
-    iso8601_date = Regex(r'(?P<year>\d{4})(?:-(?P<month>\d\d)(?:-(?P<day>\d\d))?)?').setName("ISO8601 date")
-    "ISO8601 date (``yyyy-mm-dd``)"
-
-    iso8601_datetime = Regex(r'(?P<year>\d{4})-(?P<month>\d\d)-(?P<day>\d\d)[T ](?P<hour>\d\d):(?P<minute>\d\d)(:(?P<second>\d\d(\.\d*)?)?)?(?P<tz>Z|[+-]\d\d:?\d\d)?').setName("ISO8601 datetime")
-    "ISO8601 datetime (``yyyy-mm-ddThh:mm:ss.s(Z|+-00:00)``) - trailing seconds, milliseconds, and timezone optional; accepts separating ``'T'`` or ``' '``"
-
-    uuid = Regex(r'[0-9a-fA-F]{8}(-[0-9a-fA-F]{4}){3}-[0-9a-fA-F]{12}').setName("UUID")
-    "UUID (``xxxxxxxx-xxxx-xxxx-xxxx-xxxxxxxxxxxx``)"
-
-    _html_stripper = anyOpenTag.suppress() | anyCloseTag.suppress()
-    @staticmethod
-    def stripHTMLTags(s, l, tokens):
-        """Parse action to remove HTML tags from web page HTML source
-
-        Example::
-
-            # strip HTML links from normal text
-            text = '<td>More info at the <a href="https://github.com/pyparsing/pyparsing/wiki">pyparsing</a> wiki page</td>'
-            td,td_end = makeHTMLTags("TD")
-            table_text = td + SkipTo(td_end).setParseAction(pyparsing_common.stripHTMLTags)("body") + td_end
-            print(table_text.parseString(text).body)
-
-        Prints::
-
-            More info at the pyparsing wiki page
-        """
-        return pyparsing_common._html_stripper.transformString(tokens[0])
-
-    _commasepitem = Combine(OneOrMore(~Literal(",") + ~LineEnd() + Word(printables, excludeChars=',')
-                                        + Optional( White(" \t") ) ) ).streamline().setName("commaItem")
-    comma_separated_list = delimitedList( Optional( quotedString.copy() | _commasepitem, default="") ).setName("comma separated list")
-    """Predefined expression of 1 or more printable words or quoted strings, separated by commas."""
-
-    upcaseTokens = staticmethod(tokenMap(lambda t: _ustr(t).upper()))
-    """Parse action to convert tokens to upper case."""
-
-    downcaseTokens = staticmethod(tokenMap(lambda t: _ustr(t).lower()))
-    """Parse action to convert tokens to lower case."""
-
-
-class _lazyclassproperty(object):
-    def __init__(self, fn):
-        self.fn = fn
-        self.__doc__ = fn.__doc__
-        self.__name__ = fn.__name__
-
-    def __get__(self, obj, cls):
-        if cls is None:
-            cls = type(obj)
-        if not hasattr(cls, '_intern') or any(cls._intern is getattr(superclass, '_intern', []) for superclass in cls.__mro__[1:]):
-            cls._intern = {}
-        attrname = self.fn.__name__
-        if attrname not in cls._intern:
-            cls._intern[attrname] = self.fn(cls)
-        return cls._intern[attrname]
-
-
-class unicode_set(object):
-    """
-    A set of Unicode characters, for language-specific strings for
-    ``alphas``, ``nums``, ``alphanums``, and ``printables``.
-    A unicode_set is defined by a list of ranges in the Unicode character
-    set, in a class attribute ``_ranges``, such as::
-
-        _ranges = [(0x0020, 0x007e), (0x00a0, 0x00ff),]
-
-    A unicode set can also be defined using multiple inheritance of other unicode sets::
-
-        class CJK(Chinese, Japanese, Korean):
-            pass
-    """
-    _ranges = []
-
-    @classmethod
-    def _get_chars_for_ranges(cls):
-        ret = []
-        for cc in cls.__mro__:
-            if cc is unicode_set:
-                break
-            for rr in cc._ranges:
-                ret.extend(range(rr[0], rr[-1]+1))
-        return [unichr(c) for c in sorted(set(ret))]
-
-    @_lazyclassproperty
-    def printables(cls):
-        "all non-whitespace characters in this range"
-        return u''.join(filterfalse(unicode.isspace, cls._get_chars_for_ranges()))
-
-    @_lazyclassproperty
-    def alphas(cls):
-        "all alphabetic characters in this range"
-        return u''.join(filter(unicode.isalpha, cls._get_chars_for_ranges()))
-
-    @_lazyclassproperty
-    def nums(cls):
-        "all numeric digit characters in this range"
-        return u''.join(filter(unicode.isdigit, cls._get_chars_for_ranges()))
-
-    @_lazyclassproperty
-    def alphanums(cls):
-        "all alphanumeric characters in this range"
-        return cls.alphas + cls.nums
-
-
-class pyparsing_unicode(unicode_set):
-    """
-    A namespace class for defining common language unicode_sets.
-    """
-    _ranges = [(32, sys.maxunicode)]
-
-    class Latin1(unicode_set):
-        "Unicode set for Latin-1 Unicode Character Range"
-        _ranges = [(0x0020, 0x007e), (0x00a0, 0x00ff),]
-
-    class LatinA(unicode_set):
-        "Unicode set for Latin-A Unicode Character Range"
-        _ranges = [(0x0100, 0x017f),]
-
-    class LatinB(unicode_set):
-        "Unicode set for Latin-B Unicode Character Range"
-        _ranges = [(0x0180, 0x024f),]
-
-    class Greek(unicode_set):
-        "Unicode set for Greek Unicode Character Ranges"
-        _ranges = [
-            (0x0370, 0x03ff), (0x1f00, 0x1f15), (0x1f18, 0x1f1d), (0x1f20, 0x1f45), (0x1f48, 0x1f4d),
-            (0x1f50, 0x1f57), (0x1f59,), (0x1f5b,), (0x1f5d,), (0x1f5f, 0x1f7d), (0x1f80, 0x1fb4), (0x1fb6, 0x1fc4),
-            (0x1fc6, 0x1fd3), (0x1fd6, 0x1fdb), (0x1fdd, 0x1fef), (0x1ff2, 0x1ff4), (0x1ff6, 0x1ffe),
-        ]
-
-    class Cyrillic(unicode_set):
-        "Unicode set for Cyrillic Unicode Character Range"
-        _ranges = [(0x0400, 0x04ff)]
-
-    class Chinese(unicode_set):
-        "Unicode set for Chinese Unicode Character Range"
-        _ranges = [(0x4e00, 0x9fff), (0x3000, 0x303f), ]
-
-    class Japanese(unicode_set):
-        "Unicode set for Japanese Unicode Character Range, combining Kanji, Hiragana, and Katakana ranges"
-        _ranges = [ ]
-
-        class Kanji(unicode_set):
-            "Unicode set for Kanji Unicode Character Range"
-            _ranges = [(0x4E00, 0x9Fbf), (0x3000, 0x303f), ]
-
-        class Hiragana(unicode_set):
-            "Unicode set for Hiragana Unicode Character Range"
-            _ranges = [(0x3040, 0x309f), ]
-
-        class Katakana(unicode_set):
-            "Unicode set for Katakana  Unicode Character Range"
-            _ranges = [(0x30a0, 0x30ff), ]
-
-    class Korean(unicode_set):
-        "Unicode set for Korean Unicode Character Range"
-        _ranges = [(0xac00, 0xd7af), (0x1100, 0x11ff), (0x3130, 0x318f), (0xa960, 0xa97f), (0xd7b0, 0xd7ff), (0x3000, 0x303f), ]
-
-    class CJK(Chinese, Japanese, Korean):
-        "Unicode set for combined Chinese, Japanese, and Korean (CJK) Unicode Character Range"
-        pass
-
-    class Thai(unicode_set):
-        "Unicode set for Thai Unicode Character Range"
-        _ranges = [(0x0e01, 0x0e3a), (0x0e3f, 0x0e5b), ]
-
-    class Arabic(unicode_set):
-        "Unicode set for Arabic Unicode Character Range"
-        _ranges = [(0x0600, 0x061b), (0x061e, 0x06ff), (0x0700, 0x077f), ]
-
-    class Hebrew(unicode_set):
-        "Unicode set for Hebrew Unicode Character Range"
-        _ranges = [(0x0590, 0x05ff), ]
-
-    class Devanagari(unicode_set):
-        "Unicode set for Devanagari Unicode Character Range"
-        _ranges = [(0x0900, 0x097f), (0xa8e0, 0xa8ff)]
-
-pyparsing_unicode.Japanese._ranges = (pyparsing_unicode.Japanese.Kanji._ranges
-                                      + pyparsing_unicode.Japanese.Hiragana._ranges
-                                      + pyparsing_unicode.Japanese.Katakana._ranges)
-
-# define ranges in language character sets
-if PY_3:
-    setattr(pyparsing_unicode, "العربية", pyparsing_unicode.Arabic)
-    setattr(pyparsing_unicode, "中文", pyparsing_unicode.Chinese)
-    setattr(pyparsing_unicode, "кириллица", pyparsing_unicode.Cyrillic)
-    setattr(pyparsing_unicode, "Ελληνικά", pyparsing_unicode.Greek)
-    setattr(pyparsing_unicode, "עִברִית", pyparsing_unicode.Hebrew)
-    setattr(pyparsing_unicode, "日本語", pyparsing_unicode.Japanese)
-    setattr(pyparsing_unicode.Japanese, "漢字", pyparsing_unicode.Japanese.Kanji)
-    setattr(pyparsing_unicode.Japanese, "カタカナ", pyparsing_unicode.Japanese.Katakana)
-    setattr(pyparsing_unicode.Japanese, "ひらがな", pyparsing_unicode.Japanese.Hiragana)
-    setattr(pyparsing_unicode, "한국어", pyparsing_unicode.Korean)
-    setattr(pyparsing_unicode, "ไทย", pyparsing_unicode.Thai)
-    setattr(pyparsing_unicode, "देवनागरी", pyparsing_unicode.Devanagari)
-
-
-if __name__ == "__main__":
-
-    selectToken    = CaselessLiteral("select")
-    fromToken      = CaselessLiteral("from")
-
-    ident          = Word(alphas, alphanums + "_$")
-
-    columnName     = delimitedList(ident, ".", combine=True).setParseAction(upcaseTokens)
-    columnNameList = Group(delimitedList(columnName)).setName("columns")
-    columnSpec     = ('*' | columnNameList)
-
-    tableName      = delimitedList(ident, ".", combine=True).setParseAction(upcaseTokens)
-    tableNameList  = Group(delimitedList(tableName)).setName("tables")
-
-    simpleSQL      = selectToken("command") + columnSpec("columns") + fromToken + tableNameList("tables")
-
-    # demo runTests method, including embedded comments in test string
-    simpleSQL.runTests("""
-        # '*' as column list and dotted table name
-        select * from SYS.XYZZY
-
-        # caseless match on "SELECT", and casts back to "select"
-        SELECT * from XYZZY, ABC
-
-        # list of column names, and mixed case SELECT keyword
-        Select AA,BB,CC from Sys.dual
-
-        # multiple tables
-        Select A, B, C from Sys.dual, Table2
-
-        # invalid SELECT keyword - should fail
-        Xelect A, B, C from Sys.dual
-
-        # incomplete command - should fail
-        Select
-
-        # invalid column name - should fail
-        Select ^^^ frox Sys.dual
-
-        """)
-
-    pyparsing_common.number.runTests("""
-        100
-        -100
-        +100
-        3.14159
-        6.02e23
-        1e-12
-        """)
-
-    # any int or real number, returned as float
-    pyparsing_common.fnumber.runTests("""
-        100
-        -100
-        +100
-        3.14159
-        6.02e23
-        1e-12
-        """)
-
-    pyparsing_common.hex_integer.runTests("""
-        100
-        FF
-        """)
-
-    import uuid
-    pyparsing_common.uuid.setParseAction(tokenMap(uuid.UUID))
-    pyparsing_common.uuid.runTests("""
-        12345678-1234-5678-1234-567812345678
-        """)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__init__.py
deleted file mode 100644
index 8ed060f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__init__.py
+++ /dev/null
@@ -1,4 +0,0 @@
-from .core import TomlError
-from .parser import load, loads
-from .test import translate_to_test
-from .writer import dump, dumps
\ No newline at end of file
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 2e43497..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/core.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/core.cpython-37.pyc
deleted file mode 100644
index f908525..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/core.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/parser.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/parser.cpython-37.pyc
deleted file mode 100644
index aca22e2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/parser.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/test.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/test.cpython-37.pyc
deleted file mode 100644
index 7f9ef83..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/test.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index 1e22576..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/writer.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/writer.cpython-37.pyc
deleted file mode 100644
index f5c3ea7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/__pycache__/writer.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/core.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/core.py
deleted file mode 100644
index c182734..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/core.py
+++ /dev/null
@@ -1,13 +0,0 @@
-class TomlError(RuntimeError):
-    def __init__(self, message, line, col, filename):
-        RuntimeError.__init__(self, message, line, col, filename)
-        self.message = message
-        self.line = line
-        self.col = col
-        self.filename = filename
-
-    def __str__(self):
-        return '{}({}, {}): {}'.format(self.filename, self.line, self.col, self.message)
-
-    def __repr__(self):
-        return 'TomlError({!r}, {!r}, {!r}, {!r})'.format(self.message, self.line, self.col, self.filename)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/parser.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/parser.py
deleted file mode 100644
index 3493aa6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/parser.py
+++ /dev/null
@@ -1,341 +0,0 @@
-import string, re, sys, datetime
-from .core import TomlError
-from .utils import rfc3339_re, parse_rfc3339_re
-
-if sys.version_info[0] == 2:
-    _chr = unichr
-else:
-    _chr = chr
-
-def load(fin, translate=lambda t, x, v: v, object_pairs_hook=dict):
-    return loads(fin.read(), translate=translate, object_pairs_hook=object_pairs_hook, filename=getattr(fin, 'name', repr(fin)))
-
-def loads(s, filename='<string>', translate=lambda t, x, v: v, object_pairs_hook=dict):
-    if isinstance(s, bytes):
-        s = s.decode('utf-8')
-
-    s = s.replace('\r\n', '\n')
-
-    root = object_pairs_hook()
-    tables = object_pairs_hook()
-    scope = root
-
-    src = _Source(s, filename=filename)
-    ast = _p_toml(src, object_pairs_hook=object_pairs_hook)
-
-    def error(msg):
-        raise TomlError(msg, pos[0], pos[1], filename)
-
-    def process_value(v, object_pairs_hook):
-        kind, text, value, pos = v
-        if kind == 'str' and value.startswith('\n'):
-            value = value[1:]
-        if kind == 'array':
-            if value and any(k != value[0][0] for k, t, v, p in value[1:]):
-                error('array-type-mismatch')
-            value = [process_value(item, object_pairs_hook=object_pairs_hook) for item in value]
-        elif kind == 'table':
-            value = object_pairs_hook([(k, process_value(value[k], object_pairs_hook=object_pairs_hook)) for k in value])
-        return translate(kind, text, value)
-
-    for kind, value, pos in ast:
-        if kind == 'kv':
-            k, v = value
-            if k in scope:
-                error('duplicate_keys. Key "{0}" was used more than once.'.format(k))
-            scope[k] = process_value(v, object_pairs_hook=object_pairs_hook)
-        else:
-            is_table_array = (kind == 'table_array')
-            cur = tables
-            for name in value[:-1]:
-                if isinstance(cur.get(name), list):
-                    d, cur = cur[name][-1]
-                else:
-                    d, cur = cur.setdefault(name, (None, object_pairs_hook()))
-
-            scope = object_pairs_hook()
-            name = value[-1]
-            if name not in cur:
-                if is_table_array:
-                    cur[name] = [(scope, object_pairs_hook())]
-                else:
-                    cur[name] = (scope, object_pairs_hook())
-            elif isinstance(cur[name], list):
-                if not is_table_array:
-                    error('table_type_mismatch')
-                cur[name].append((scope, object_pairs_hook()))
-            else:
-                if is_table_array:
-                    error('table_type_mismatch')
-                old_scope, next_table = cur[name]
-                if old_scope is not None:
-                    error('duplicate_tables')
-                cur[name] = (scope, next_table)
-
-    def merge_tables(scope, tables):
-        if scope is None:
-            scope = object_pairs_hook()
-        for k in tables:
-            if k in scope:
-                error('key_table_conflict')
-            v = tables[k]
-            if isinstance(v, list):
-                scope[k] = [merge_tables(sc, tbl) for sc, tbl in v]
-            else:
-                scope[k] = merge_tables(v[0], v[1])
-        return scope
-
-    return merge_tables(root, tables)
-
-class _Source:
-    def __init__(self, s, filename=None):
-        self.s = s
-        self._pos = (1, 1)
-        self._last = None
-        self._filename = filename
-        self.backtrack_stack = []
-
-    def last(self):
-        return self._last
-
-    def pos(self):
-        return self._pos
-
-    def fail(self):
-        return self._expect(None)
-
-    def consume_dot(self):
-        if self.s:
-            self._last = self.s[0]
-            self.s = self[1:]
-            self._advance(self._last)
-            return self._last
-        return None
-
-    def expect_dot(self):
-        return self._expect(self.consume_dot())
-
-    def consume_eof(self):
-        if not self.s:
-            self._last = ''
-            return True
-        return False
-
-    def expect_eof(self):
-        return self._expect(self.consume_eof())
-
-    def consume(self, s):
-        if self.s.startswith(s):
-            self.s = self.s[len(s):]
-            self._last = s
-            self._advance(s)
-            return True
-        return False
-
-    def expect(self, s):
-        return self._expect(self.consume(s))
-
-    def consume_re(self, re):
-        m = re.match(self.s)
-        if m:
-            self.s = self.s[len(m.group(0)):]
-            self._last = m
-            self._advance(m.group(0))
-            return m
-        return None
-
-    def expect_re(self, re):
-        return self._expect(self.consume_re(re))
-
-    def __enter__(self):
-        self.backtrack_stack.append((self.s, self._pos))
-
-    def __exit__(self, type, value, traceback):
-        if type is None:
-            self.backtrack_stack.pop()
-        else:
-            self.s, self._pos = self.backtrack_stack.pop()
-        return type == TomlError
-
-    def commit(self):
-        self.backtrack_stack[-1] = (self.s, self._pos)
-
-    def _expect(self, r):
-        if not r:
-            raise TomlError('msg', self._pos[0], self._pos[1], self._filename)
-        return r
-
-    def _advance(self, s):
-        suffix_pos = s.rfind('\n')
-        if suffix_pos == -1:
-            self._pos = (self._pos[0], self._pos[1] + len(s))
-        else:
-            self._pos = (self._pos[0] + s.count('\n'), len(s) - suffix_pos)
-
-_ews_re = re.compile(r'(?:[ \t]|#[^\n]*\n|#[^\n]*\Z|\n)*')
-def _p_ews(s):
-    s.expect_re(_ews_re)
-
-_ws_re = re.compile(r'[ \t]*')
-def _p_ws(s):
-    s.expect_re(_ws_re)
-
-_escapes = { 'b': '\b', 'n': '\n', 'r': '\r', 't': '\t', '"': '"',
-    '\\': '\\', 'f': '\f' }
-
-_basicstr_re = re.compile(r'[^"\\\000-\037]*')
-_short_uni_re = re.compile(r'u([0-9a-fA-F]{4})')
-_long_uni_re = re.compile(r'U([0-9a-fA-F]{8})')
-_escapes_re = re.compile(r'[btnfr\"\\]')
-_newline_esc_re = re.compile('\n[ \t\n]*')
-def _p_basicstr_content(s, content=_basicstr_re):
-    res = []
-    while True:
-        res.append(s.expect_re(content).group(0))
-        if not s.consume('\\'):
-            break
-        if s.consume_re(_newline_esc_re):
-            pass
-        elif s.consume_re(_short_uni_re) or s.consume_re(_long_uni_re):
-            v = int(s.last().group(1), 16)
-            if 0xd800 <= v < 0xe000:
-                s.fail()
-            res.append(_chr(v))
-        else:
-            s.expect_re(_escapes_re)
-            res.append(_escapes[s.last().group(0)])
-    return ''.join(res)
-
-_key_re = re.compile(r'[0-9a-zA-Z-_]+')
-def _p_key(s):
-    with s:
-        s.expect('"')
-        r = _p_basicstr_content(s, _basicstr_re)
-        s.expect('"')
-        return r
-    if s.consume('\''):
-        if s.consume('\'\''):
-            r = s.expect_re(_litstr_ml_re).group(0)
-            s.expect('\'\'\'')
-        else:
-            r = s.expect_re(_litstr_re).group(0)
-            s.expect('\'')
-        return r
-    return s.expect_re(_key_re).group(0)
-
-_float_re = re.compile(r'[+-]?(?:0|[1-9](?:_?\d)*)(?:\.\d(?:_?\d)*)?(?:[eE][+-]?(?:\d(?:_?\d)*))?')
-
-_basicstr_ml_re = re.compile(r'(?:""?(?!")|[^"\\\000-\011\013-\037])*')
-_litstr_re = re.compile(r"[^'\000\010\012-\037]*")
-_litstr_ml_re = re.compile(r"(?:(?:|'|'')(?:[^'\000-\010\013-\037]))*")
-def _p_value(s, object_pairs_hook):
-    pos = s.pos()
-
-    if s.consume('true'):
-        return 'bool', s.last(), True, pos
-    if s.consume('false'):
-        return 'bool', s.last(), False, pos
-
-    if s.consume('"'):
-        if s.consume('""'):
-            r = _p_basicstr_content(s, _basicstr_ml_re)
-            s.expect('"""')
-        else:
-            r = _p_basicstr_content(s, _basicstr_re)
-            s.expect('"')
-        return 'str', r, r, pos
-
-    if s.consume('\''):
-        if s.consume('\'\''):
-            r = s.expect_re(_litstr_ml_re).group(0)
-            s.expect('\'\'\'')
-        else:
-            r = s.expect_re(_litstr_re).group(0)
-            s.expect('\'')
-        return 'str', r, r, pos
-
-    if s.consume_re(rfc3339_re):
-        m = s.last()
-        return 'datetime', m.group(0), parse_rfc3339_re(m), pos
-
-    if s.consume_re(_float_re):
-        m = s.last().group(0)
-        r = m.replace('_','')
-        if '.' in m or 'e' in m or 'E' in m:
-            return 'float', m, float(r), pos
-        else:
-            return 'int', m, int(r, 10), pos
-
-    if s.consume('['):
-        items = []
-        with s:
-            while True:
-                _p_ews(s)
-                items.append(_p_value(s, object_pairs_hook=object_pairs_hook))
-                s.commit()
-                _p_ews(s)
-                s.expect(',')
-                s.commit()
-        _p_ews(s)
-        s.expect(']')
-        return 'array', None, items, pos
-
-    if s.consume('{'):
-        _p_ws(s)
-        items = object_pairs_hook()
-        if not s.consume('}'):
-            k = _p_key(s)
-            _p_ws(s)
-            s.expect('=')
-            _p_ws(s)
-            items[k] = _p_value(s, object_pairs_hook=object_pairs_hook)
-            _p_ws(s)
-            while s.consume(','):
-                _p_ws(s)
-                k = _p_key(s)
-                _p_ws(s)
-                s.expect('=')
-                _p_ws(s)
-                items[k] = _p_value(s, object_pairs_hook=object_pairs_hook)
-                _p_ws(s)
-            s.expect('}')
-        return 'table', None, items, pos
-
-    s.fail()
-
-def _p_stmt(s, object_pairs_hook):
-    pos = s.pos()
-    if s.consume(   '['):
-        is_array = s.consume('[')
-        _p_ws(s)
-        keys = [_p_key(s)]
-        _p_ws(s)
-        while s.consume('.'):
-            _p_ws(s)
-            keys.append(_p_key(s))
-            _p_ws(s)
-        s.expect(']')
-        if is_array:
-            s.expect(']')
-        return 'table_array' if is_array else 'table', keys, pos
-
-    key = _p_key(s)
-    _p_ws(s)
-    s.expect('=')
-    _p_ws(s)
-    value = _p_value(s, object_pairs_hook=object_pairs_hook)
-    return 'kv', (key, value), pos
-
-_stmtsep_re = re.compile(r'(?:[ \t]*(?:#[^\n]*)?\n)+[ \t]*')
-def _p_toml(s, object_pairs_hook):
-    stmts = []
-    _p_ews(s)
-    with s:
-        stmts.append(_p_stmt(s, object_pairs_hook=object_pairs_hook))
-        while True:
-            s.commit()
-            s.expect_re(_stmtsep_re)
-            stmts.append(_p_stmt(s, object_pairs_hook=object_pairs_hook))
-    _p_ews(s)
-    s.expect_eof()
-    return stmts
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/test.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/test.py
deleted file mode 100644
index ec8abfc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/test.py
+++ /dev/null
@@ -1,30 +0,0 @@
-import datetime
-from .utils import format_rfc3339
-
-try:
-    _string_types = (str, unicode)
-    _int_types = (int, long)
-except NameError:
-    _string_types = str
-    _int_types = int
-
-def translate_to_test(v):
-    if isinstance(v, dict):
-        return { k: translate_to_test(v) for k, v in v.items() }
-    if isinstance(v, list):
-        a = [translate_to_test(x) for x in v]
-        if v and isinstance(v[0], dict):
-            return a
-        else:
-            return {'type': 'array', 'value': a}
-    if isinstance(v, datetime.datetime):
-        return {'type': 'datetime', 'value': format_rfc3339(v)}
-    if isinstance(v, bool):
-        return {'type': 'bool', 'value': 'true' if v else 'false'}
-    if isinstance(v, _int_types):
-        return {'type': 'integer', 'value': str(v)}
-    if isinstance(v, float):
-        return {'type': 'float', 'value': '{:.17}'.format(v)}
-    if isinstance(v, _string_types):
-        return {'type': 'string', 'value': v}
-    raise RuntimeError('unexpected value: {!r}'.format(v))
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/utils.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/utils.py
deleted file mode 100644
index 636a680..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/utils.py
+++ /dev/null
@@ -1,67 +0,0 @@
-import datetime
-import re
-
-rfc3339_re = re.compile(r'(\d{4})-(\d{2})-(\d{2})T(\d{2}):(\d{2}):(\d{2})(\.\d+)?(?:Z|([+-]\d{2}):(\d{2}))')
-
-def parse_rfc3339(v):
-    m = rfc3339_re.match(v)
-    if not m or m.group(0) != v:
-        return None
-    return parse_rfc3339_re(m)
-
-def parse_rfc3339_re(m):
-    r = map(int, m.groups()[:6])
-    if m.group(7):
-        micro = float(m.group(7))
-    else:
-        micro = 0
-
-    if m.group(8):
-        g = int(m.group(8), 10) * 60 + int(m.group(9), 10)
-        tz = _TimeZone(datetime.timedelta(0, g * 60))
-    else:
-        tz = _TimeZone(datetime.timedelta(0, 0))
-
-    y, m, d, H, M, S = r
-    return datetime.datetime(y, m, d, H, M, S, int(micro * 1000000), tz)
-
-
-def format_rfc3339(v):
-    offs = v.utcoffset()
-    offs = int(offs.total_seconds()) // 60 if offs is not None else 0
-
-    if offs == 0:
-        suffix = 'Z'
-    else:
-        if offs > 0:
-            suffix = '+'
-        else:
-            suffix = '-'
-            offs = -offs
-        suffix = '{0}{1:02}:{2:02}'.format(suffix, offs // 60, offs % 60)
-
-    if v.microsecond:
-        return v.strftime('%Y-%m-%dT%H:%M:%S.%f') + suffix
-    else:
-        return v.strftime('%Y-%m-%dT%H:%M:%S') + suffix
-
-class _TimeZone(datetime.tzinfo):
-    def __init__(self, offset):
-        self._offset = offset
-
-    def utcoffset(self, dt):
-        return self._offset
-
-    def dst(self, dt):
-        return None
-
-    def tzname(self, dt):
-        m = self._offset.total_seconds() // 60
-        if m < 0:
-            res = '-'
-            m = -m
-        else:
-            res = '+'
-        h = m // 60
-        m = m - h * 60
-        return '{}{:.02}{:.02}'.format(res, h, m)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/writer.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/writer.py
deleted file mode 100644
index 73b5089..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/pytoml/writer.py
+++ /dev/null
@@ -1,106 +0,0 @@
-from __future__ import unicode_literals
-import io, datetime, math, string, sys
-
-from .utils import format_rfc3339
-
-if sys.version_info[0] == 3:
-    long = int
-    unicode = str
-
-
-def dumps(obj, sort_keys=False):
-    fout = io.StringIO()
-    dump(obj, fout, sort_keys=sort_keys)
-    return fout.getvalue()
-
-
-_escapes = {'\n': 'n', '\r': 'r', '\\': '\\', '\t': 't', '\b': 'b', '\f': 'f', '"': '"'}
-
-
-def _escape_string(s):
-    res = []
-    start = 0
-
-    def flush():
-        if start != i:
-            res.append(s[start:i])
-        return i + 1
-
-    i = 0
-    while i < len(s):
-        c = s[i]
-        if c in '"\\\n\r\t\b\f':
-            start = flush()
-            res.append('\\' + _escapes[c])
-        elif ord(c) < 0x20:
-            start = flush()
-            res.append('\\u%04x' % ord(c))
-        i += 1
-
-    flush()
-    return '"' + ''.join(res) + '"'
-
-
-_key_chars = string.digits + string.ascii_letters + '-_'
-def _escape_id(s):
-    if any(c not in _key_chars for c in s):
-        return _escape_string(s)
-    return s
-
-
-def _format_value(v):
-    if isinstance(v, bool):
-        return 'true' if v else 'false'
-    if isinstance(v, int) or isinstance(v, long):
-        return unicode(v)
-    if isinstance(v, float):
-        if math.isnan(v) or math.isinf(v):
-            raise ValueError("{0} is not a valid TOML value".format(v))
-        else:
-            return repr(v)
-    elif isinstance(v, unicode) or isinstance(v, bytes):
-        return _escape_string(v)
-    elif isinstance(v, datetime.datetime):
-        return format_rfc3339(v)
-    elif isinstance(v, list):
-        return '[{0}]'.format(', '.join(_format_value(obj) for obj in v))
-    elif isinstance(v, dict):
-        return '{{{0}}}'.format(', '.join('{} = {}'.format(_escape_id(k), _format_value(obj)) for k, obj in v.items()))
-    else:
-        raise RuntimeError(v)
-
-
-def dump(obj, fout, sort_keys=False):
-    tables = [((), obj, False)]
-
-    while tables:
-        name, table, is_array = tables.pop()
-        if name:
-            section_name = '.'.join(_escape_id(c) for c in name)
-            if is_array:
-                fout.write('[[{0}]]\n'.format(section_name))
-            else:
-                fout.write('[{0}]\n'.format(section_name))
-
-        table_keys = sorted(table.keys()) if sort_keys else table.keys()
-        new_tables = []
-        has_kv = False
-        for k in table_keys:
-            v = table[k]
-            if isinstance(v, dict):
-                new_tables.append((name + (k,), v, False))
-            elif isinstance(v, list) and v and all(isinstance(o, dict) for o in v):
-                new_tables.extend((name + (k,), d, True) for d in v)
-            elif v is None:
-                # based on mojombo's comment: https://github.com/toml-lang/toml/issues/146#issuecomment-25019344
-                fout.write(
-                    '#{} = null  # To use: uncomment and replace null with value\n'.format(_escape_id(k)))
-                has_kv = True
-            else:
-                fout.write('{0} = {1}\n'.format(_escape_id(k), _format_value(v)))
-                has_kv = True
-
-        tables.extend(reversed(new_tables))
-
-        if (name or has_kv) and tables:
-            fout.write('\n')
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__init__.py
deleted file mode 100644
index 80c4ce1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__init__.py
+++ /dev/null
@@ -1,133 +0,0 @@
-# -*- coding: utf-8 -*-
-
-#   __
-#  /__)  _  _     _   _ _/   _
-# / (   (- (/ (/ (- _)  /  _)
-#          /
-
-"""
-Requests HTTP Library
-~~~~~~~~~~~~~~~~~~~~~
-
-Requests is an HTTP library, written in Python, for human beings. Basic GET
-usage:
-
-   >>> import requests
-   >>> r = requests.get('https://www.python.org')
-   >>> r.status_code
-   200
-   >>> 'Python is a programming language' in r.content
-   True
-
-... or POST:
-
-   >>> payload = dict(key1='value1', key2='value2')
-   >>> r = requests.post('https://httpbin.org/post', data=payload)
-   >>> print(r.text)
-   {
-     ...
-     "form": {
-       "key2": "value2",
-       "key1": "value1"
-     },
-     ...
-   }
-
-The other HTTP methods are supported - see `requests.api`. Full documentation
-is at <http://python-requests.org>.
-
-:copyright: (c) 2017 by Kenneth Reitz.
-:license: Apache 2.0, see LICENSE for more details.
-"""
-
-from pip._vendor import urllib3
-from pip._vendor import chardet
-import warnings
-from .exceptions import RequestsDependencyWarning
-
-
-def check_compatibility(urllib3_version, chardet_version):
-    urllib3_version = urllib3_version.split('.')
-    assert urllib3_version != ['dev']  # Verify urllib3 isn't installed from git.
-
-    # Sometimes, urllib3 only reports its version as 16.1.
-    if len(urllib3_version) == 2:
-        urllib3_version.append('0')
-
-    # Check urllib3 for compatibility.
-    major, minor, patch = urllib3_version  # noqa: F811
-    major, minor, patch = int(major), int(minor), int(patch)
-    # urllib3 >= 1.21.1, <= 1.24
-    assert major == 1
-    assert minor >= 21
-    assert minor <= 24
-
-    # Check chardet for compatibility.
-    major, minor, patch = chardet_version.split('.')[:3]
-    major, minor, patch = int(major), int(minor), int(patch)
-    # chardet >= 3.0.2, < 3.1.0
-    assert major == 3
-    assert minor < 1
-    assert patch >= 2
-
-
-def _check_cryptography(cryptography_version):
-    # cryptography < 1.3.4
-    try:
-        cryptography_version = list(map(int, cryptography_version.split('.')))
-    except ValueError:
-        return
-
-    if cryptography_version < [1, 3, 4]:
-        warning = 'Old version of cryptography ({}) may cause slowdown.'.format(cryptography_version)
-        warnings.warn(warning, RequestsDependencyWarning)
-
-# Check imported dependencies for compatibility.
-try:
-    check_compatibility(urllib3.__version__, chardet.__version__)
-except (AssertionError, ValueError):
-    warnings.warn("urllib3 ({}) or chardet ({}) doesn't match a supported "
-                  "version!".format(urllib3.__version__, chardet.__version__),
-                  RequestsDependencyWarning)
-
-# Attempt to enable urllib3's SNI support, if possible
-from pip._internal.utils.compat import WINDOWS
-if not WINDOWS:
-    try:
-        from pip._vendor.urllib3.contrib import pyopenssl
-        pyopenssl.inject_into_urllib3()
-
-        # Check cryptography version
-        from cryptography import __version__ as cryptography_version
-        _check_cryptography(cryptography_version)
-    except ImportError:
-        pass
-
-# urllib3's DependencyWarnings should be silenced.
-from pip._vendor.urllib3.exceptions import DependencyWarning
-warnings.simplefilter('ignore', DependencyWarning)
-
-from .__version__ import __title__, __description__, __url__, __version__
-from .__version__ import __build__, __author__, __author_email__, __license__
-from .__version__ import __copyright__, __cake__
-
-from . import utils
-from . import packages
-from .models import Request, Response, PreparedRequest
-from .api import request, get, head, post, patch, put, delete, options
-from .sessions import session, Session
-from .status_codes import codes
-from .exceptions import (
-    RequestException, Timeout, URLRequired,
-    TooManyRedirects, HTTPError, ConnectionError,
-    FileModeWarning, ConnectTimeout, ReadTimeout
-)
-
-# Set default logging handler to avoid "No handler found" warnings.
-import logging
-from logging import NullHandler
-
-logging.getLogger(__name__).addHandler(NullHandler())
-
-# FileModeWarnings go off per the default.
-warnings.simplefilter('default', FileModeWarning, append=True)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 65262d8..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/__version__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/__version__.cpython-37.pyc
deleted file mode 100644
index 7320fdb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/__version__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/_internal_utils.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/_internal_utils.cpython-37.pyc
deleted file mode 100644
index e1a4e7d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/_internal_utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/adapters.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/adapters.cpython-37.pyc
deleted file mode 100644
index 027fdbd..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/adapters.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/api.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/api.cpython-37.pyc
deleted file mode 100644
index d391e14..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/api.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/auth.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/auth.cpython-37.pyc
deleted file mode 100644
index b076636..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/auth.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/certs.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/certs.cpython-37.pyc
deleted file mode 100644
index 553e341..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/certs.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/compat.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/compat.cpython-37.pyc
deleted file mode 100644
index 47d10c7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/compat.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/cookies.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/cookies.cpython-37.pyc
deleted file mode 100644
index 4e74914..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/cookies.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/exceptions.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/exceptions.cpython-37.pyc
deleted file mode 100644
index b401152..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/exceptions.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/hooks.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/hooks.cpython-37.pyc
deleted file mode 100644
index f717b31..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/hooks.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/models.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/models.cpython-37.pyc
deleted file mode 100644
index 1410aaf..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/models.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/packages.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/packages.cpython-37.pyc
deleted file mode 100644
index 777bea6..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/packages.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/sessions.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/sessions.cpython-37.pyc
deleted file mode 100644
index 0b3539e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/sessions.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/status_codes.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/status_codes.cpython-37.pyc
deleted file mode 100644
index 7db68be..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/status_codes.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/structures.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/structures.cpython-37.pyc
deleted file mode 100644
index fea3c8c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/structures.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index 4d3b060..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__version__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__version__.py
deleted file mode 100644
index f5b5d03..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/__version__.py
+++ /dev/null
@@ -1,14 +0,0 @@
-# .-. .-. .-. . . .-. .-. .-. .-.
-# |(  |-  |.| | | |-  `-.  |  `-.
-# ' ' `-' `-`.`-' `-' `-'  '  `-'
-
-__title__ = 'requests'
-__description__ = 'Python HTTP for Humans.'
-__url__ = 'http://python-requests.org'
-__version__ = '2.21.0'
-__build__ = 0x022100
-__author__ = 'Kenneth Reitz'
-__author_email__ = 'me@kennethreitz.org'
-__license__ = 'Apache 2.0'
-__copyright__ = 'Copyright 2018 Kenneth Reitz'
-__cake__ = u'\u2728 \U0001f370 \u2728'
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/_internal_utils.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/_internal_utils.py
deleted file mode 100644
index 759d9a5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/_internal_utils.py
+++ /dev/null
@@ -1,42 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests._internal_utils
-~~~~~~~~~~~~~~
-
-Provides utility functions that are consumed internally by Requests
-which depend on extremely few external helpers (such as compat)
-"""
-
-from .compat import is_py2, builtin_str, str
-
-
-def to_native_string(string, encoding='ascii'):
-    """Given a string object, regardless of type, returns a representation of
-    that string in the native string type, encoding and decoding where
-    necessary. This assumes ASCII unless told otherwise.
-    """
-    if isinstance(string, builtin_str):
-        out = string
-    else:
-        if is_py2:
-            out = string.encode(encoding)
-        else:
-            out = string.decode(encoding)
-
-    return out
-
-
-def unicode_is_ascii(u_string):
-    """Determine if unicode string only contains ASCII characters.
-
-    :param str u_string: unicode string to check. Must be unicode
-        and not Python 2 `str`.
-    :rtype: bool
-    """
-    assert isinstance(u_string, str)
-    try:
-        u_string.encode('ascii')
-        return True
-    except UnicodeEncodeError:
-        return False
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/adapters.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/adapters.py
deleted file mode 100644
index c30e7c9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/adapters.py
+++ /dev/null
@@ -1,533 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.adapters
-~~~~~~~~~~~~~~~~~
-
-This module contains the transport adapters that Requests uses to define
-and maintain connections.
-"""
-
-import os.path
-import socket
-
-from pip._vendor.urllib3.poolmanager import PoolManager, proxy_from_url
-from pip._vendor.urllib3.response import HTTPResponse
-from pip._vendor.urllib3.util import parse_url
-from pip._vendor.urllib3.util import Timeout as TimeoutSauce
-from pip._vendor.urllib3.util.retry import Retry
-from pip._vendor.urllib3.exceptions import ClosedPoolError
-from pip._vendor.urllib3.exceptions import ConnectTimeoutError
-from pip._vendor.urllib3.exceptions import HTTPError as _HTTPError
-from pip._vendor.urllib3.exceptions import MaxRetryError
-from pip._vendor.urllib3.exceptions import NewConnectionError
-from pip._vendor.urllib3.exceptions import ProxyError as _ProxyError
-from pip._vendor.urllib3.exceptions import ProtocolError
-from pip._vendor.urllib3.exceptions import ReadTimeoutError
-from pip._vendor.urllib3.exceptions import SSLError as _SSLError
-from pip._vendor.urllib3.exceptions import ResponseError
-from pip._vendor.urllib3.exceptions import LocationValueError
-
-from .models import Response
-from .compat import urlparse, basestring
-from .utils import (DEFAULT_CA_BUNDLE_PATH, extract_zipped_paths,
-                    get_encoding_from_headers, prepend_scheme_if_needed,
-                    get_auth_from_url, urldefragauth, select_proxy)
-from .structures import CaseInsensitiveDict
-from .cookies import extract_cookies_to_jar
-from .exceptions import (ConnectionError, ConnectTimeout, ReadTimeout, SSLError,
-                         ProxyError, RetryError, InvalidSchema, InvalidProxyURL,
-                         InvalidURL)
-from .auth import _basic_auth_str
-
-try:
-    from pip._vendor.urllib3.contrib.socks import SOCKSProxyManager
-except ImportError:
-    def SOCKSProxyManager(*args, **kwargs):
-        raise InvalidSchema("Missing dependencies for SOCKS support.")
-
-DEFAULT_POOLBLOCK = False
-DEFAULT_POOLSIZE = 10
-DEFAULT_RETRIES = 0
-DEFAULT_POOL_TIMEOUT = None
-
-
-class BaseAdapter(object):
-    """The Base Transport Adapter"""
-
-    def __init__(self):
-        super(BaseAdapter, self).__init__()
-
-    def send(self, request, stream=False, timeout=None, verify=True,
-             cert=None, proxies=None):
-        """Sends PreparedRequest object. Returns Response object.
-
-        :param request: The :class:`PreparedRequest <PreparedRequest>` being sent.
-        :param stream: (optional) Whether to stream the request content.
-        :param timeout: (optional) How long to wait for the server to send
-            data before giving up, as a float, or a :ref:`(connect timeout,
-            read timeout) <timeouts>` tuple.
-        :type timeout: float or tuple
-        :param verify: (optional) Either a boolean, in which case it controls whether we verify
-            the server's TLS certificate, or a string, in which case it must be a path
-            to a CA bundle to use
-        :param cert: (optional) Any user-provided SSL certificate to be trusted.
-        :param proxies: (optional) The proxies dictionary to apply to the request.
-        """
-        raise NotImplementedError
-
-    def close(self):
-        """Cleans up adapter specific items."""
-        raise NotImplementedError
-
-
-class HTTPAdapter(BaseAdapter):
-    """The built-in HTTP Adapter for urllib3.
-
-    Provides a general-case interface for Requests sessions to contact HTTP and
-    HTTPS urls by implementing the Transport Adapter interface. This class will
-    usually be created by the :class:`Session <Session>` class under the
-    covers.
-
-    :param pool_connections: The number of urllib3 connection pools to cache.
-    :param pool_maxsize: The maximum number of connections to save in the pool.
-    :param max_retries: The maximum number of retries each connection
-        should attempt. Note, this applies only to failed DNS lookups, socket
-        connections and connection timeouts, never to requests where data has
-        made it to the server. By default, Requests does not retry failed
-        connections. If you need granular control over the conditions under
-        which we retry a request, import urllib3's ``Retry`` class and pass
-        that instead.
-    :param pool_block: Whether the connection pool should block for connections.
-
-    Usage::
-
-      >>> import requests
-      >>> s = requests.Session()
-      >>> a = requests.adapters.HTTPAdapter(max_retries=3)
-      >>> s.mount('http://', a)
-    """
-    __attrs__ = ['max_retries', 'config', '_pool_connections', '_pool_maxsize',
-                 '_pool_block']
-
-    def __init__(self, pool_connections=DEFAULT_POOLSIZE,
-                 pool_maxsize=DEFAULT_POOLSIZE, max_retries=DEFAULT_RETRIES,
-                 pool_block=DEFAULT_POOLBLOCK):
-        if max_retries == DEFAULT_RETRIES:
-            self.max_retries = Retry(0, read=False)
-        else:
-            self.max_retries = Retry.from_int(max_retries)
-        self.config = {}
-        self.proxy_manager = {}
-
-        super(HTTPAdapter, self).__init__()
-
-        self._pool_connections = pool_connections
-        self._pool_maxsize = pool_maxsize
-        self._pool_block = pool_block
-
-        self.init_poolmanager(pool_connections, pool_maxsize, block=pool_block)
-
-    def __getstate__(self):
-        return {attr: getattr(self, attr, None) for attr in self.__attrs__}
-
-    def __setstate__(self, state):
-        # Can't handle by adding 'proxy_manager' to self.__attrs__ because
-        # self.poolmanager uses a lambda function, which isn't pickleable.
-        self.proxy_manager = {}
-        self.config = {}
-
-        for attr, value in state.items():
-            setattr(self, attr, value)
-
-        self.init_poolmanager(self._pool_connections, self._pool_maxsize,
-                              block=self._pool_block)
-
-    def init_poolmanager(self, connections, maxsize, block=DEFAULT_POOLBLOCK, **pool_kwargs):
-        """Initializes a urllib3 PoolManager.
-
-        This method should not be called from user code, and is only
-        exposed for use when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        :param connections: The number of urllib3 connection pools to cache.
-        :param maxsize: The maximum number of connections to save in the pool.
-        :param block: Block when no free connections are available.
-        :param pool_kwargs: Extra keyword arguments used to initialize the Pool Manager.
-        """
-        # save these values for pickling
-        self._pool_connections = connections
-        self._pool_maxsize = maxsize
-        self._pool_block = block
-
-        self.poolmanager = PoolManager(num_pools=connections, maxsize=maxsize,
-                                       block=block, strict=True, **pool_kwargs)
-
-    def proxy_manager_for(self, proxy, **proxy_kwargs):
-        """Return urllib3 ProxyManager for the given proxy.
-
-        This method should not be called from user code, and is only
-        exposed for use when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        :param proxy: The proxy to return a urllib3 ProxyManager for.
-        :param proxy_kwargs: Extra keyword arguments used to configure the Proxy Manager.
-        :returns: ProxyManager
-        :rtype: urllib3.ProxyManager
-        """
-        if proxy in self.proxy_manager:
-            manager = self.proxy_manager[proxy]
-        elif proxy.lower().startswith('socks'):
-            username, password = get_auth_from_url(proxy)
-            manager = self.proxy_manager[proxy] = SOCKSProxyManager(
-                proxy,
-                username=username,
-                password=password,
-                num_pools=self._pool_connections,
-                maxsize=self._pool_maxsize,
-                block=self._pool_block,
-                **proxy_kwargs
-            )
-        else:
-            proxy_headers = self.proxy_headers(proxy)
-            manager = self.proxy_manager[proxy] = proxy_from_url(
-                proxy,
-                proxy_headers=proxy_headers,
-                num_pools=self._pool_connections,
-                maxsize=self._pool_maxsize,
-                block=self._pool_block,
-                **proxy_kwargs)
-
-        return manager
-
-    def cert_verify(self, conn, url, verify, cert):
-        """Verify a SSL certificate. This method should not be called from user
-        code, and is only exposed for use when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        :param conn: The urllib3 connection object associated with the cert.
-        :param url: The requested URL.
-        :param verify: Either a boolean, in which case it controls whether we verify
-            the server's TLS certificate, or a string, in which case it must be a path
-            to a CA bundle to use
-        :param cert: The SSL certificate to verify.
-        """
-        if url.lower().startswith('https') and verify:
-
-            cert_loc = None
-
-            # Allow self-specified cert location.
-            if verify is not True:
-                cert_loc = verify
-
-            if not cert_loc:
-                cert_loc = extract_zipped_paths(DEFAULT_CA_BUNDLE_PATH)
-
-            if not cert_loc or not os.path.exists(cert_loc):
-                raise IOError("Could not find a suitable TLS CA certificate bundle, "
-                              "invalid path: {}".format(cert_loc))
-
-            conn.cert_reqs = 'CERT_REQUIRED'
-
-            if not os.path.isdir(cert_loc):
-                conn.ca_certs = cert_loc
-            else:
-                conn.ca_cert_dir = cert_loc
-        else:
-            conn.cert_reqs = 'CERT_NONE'
-            conn.ca_certs = None
-            conn.ca_cert_dir = None
-
-        if cert:
-            if not isinstance(cert, basestring):
-                conn.cert_file = cert[0]
-                conn.key_file = cert[1]
-            else:
-                conn.cert_file = cert
-                conn.key_file = None
-            if conn.cert_file and not os.path.exists(conn.cert_file):
-                raise IOError("Could not find the TLS certificate file, "
-                              "invalid path: {}".format(conn.cert_file))
-            if conn.key_file and not os.path.exists(conn.key_file):
-                raise IOError("Could not find the TLS key file, "
-                              "invalid path: {}".format(conn.key_file))
-
-    def build_response(self, req, resp):
-        """Builds a :class:`Response <requests.Response>` object from a urllib3
-        response. This should not be called from user code, and is only exposed
-        for use when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`
-
-        :param req: The :class:`PreparedRequest <PreparedRequest>` used to generate the response.
-        :param resp: The urllib3 response object.
-        :rtype: requests.Response
-        """
-        response = Response()
-
-        # Fallback to None if there's no status_code, for whatever reason.
-        response.status_code = getattr(resp, 'status', None)
-
-        # Make headers case-insensitive.
-        response.headers = CaseInsensitiveDict(getattr(resp, 'headers', {}))
-
-        # Set encoding.
-        response.encoding = get_encoding_from_headers(response.headers)
-        response.raw = resp
-        response.reason = response.raw.reason
-
-        if isinstance(req.url, bytes):
-            response.url = req.url.decode('utf-8')
-        else:
-            response.url = req.url
-
-        # Add new cookies from the server.
-        extract_cookies_to_jar(response.cookies, req, resp)
-
-        # Give the Response some context.
-        response.request = req
-        response.connection = self
-
-        return response
-
-    def get_connection(self, url, proxies=None):
-        """Returns a urllib3 connection for the given URL. This should not be
-        called from user code, and is only exposed for use when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        :param url: The URL to connect to.
-        :param proxies: (optional) A Requests-style dictionary of proxies used on this request.
-        :rtype: urllib3.ConnectionPool
-        """
-        proxy = select_proxy(url, proxies)
-
-        if proxy:
-            proxy = prepend_scheme_if_needed(proxy, 'http')
-            proxy_url = parse_url(proxy)
-            if not proxy_url.host:
-                raise InvalidProxyURL("Please check proxy URL. It is malformed"
-                                      " and could be missing the host.")
-            proxy_manager = self.proxy_manager_for(proxy)
-            conn = proxy_manager.connection_from_url(url)
-        else:
-            # Only scheme should be lower case
-            parsed = urlparse(url)
-            url = parsed.geturl()
-            conn = self.poolmanager.connection_from_url(url)
-
-        return conn
-
-    def close(self):
-        """Disposes of any internal state.
-
-        Currently, this closes the PoolManager and any active ProxyManager,
-        which closes any pooled connections.
-        """
-        self.poolmanager.clear()
-        for proxy in self.proxy_manager.values():
-            proxy.clear()
-
-    def request_url(self, request, proxies):
-        """Obtain the url to use when making the final request.
-
-        If the message is being sent through a HTTP proxy, the full URL has to
-        be used. Otherwise, we should only use the path portion of the URL.
-
-        This should not be called from user code, and is only exposed for use
-        when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        :param request: The :class:`PreparedRequest <PreparedRequest>` being sent.
-        :param proxies: A dictionary of schemes or schemes and hosts to proxy URLs.
-        :rtype: str
-        """
-        proxy = select_proxy(request.url, proxies)
-        scheme = urlparse(request.url).scheme
-
-        is_proxied_http_request = (proxy and scheme != 'https')
-        using_socks_proxy = False
-        if proxy:
-            proxy_scheme = urlparse(proxy).scheme.lower()
-            using_socks_proxy = proxy_scheme.startswith('socks')
-
-        url = request.path_url
-        if is_proxied_http_request and not using_socks_proxy:
-            url = urldefragauth(request.url)
-
-        return url
-
-    def add_headers(self, request, **kwargs):
-        """Add any headers needed by the connection. As of v2.0 this does
-        nothing by default, but is left for overriding by users that subclass
-        the :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        This should not be called from user code, and is only exposed for use
-        when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        :param request: The :class:`PreparedRequest <PreparedRequest>` to add headers to.
-        :param kwargs: The keyword arguments from the call to send().
-        """
-        pass
-
-    def proxy_headers(self, proxy):
-        """Returns a dictionary of the headers to add to any request sent
-        through a proxy. This works with urllib3 magic to ensure that they are
-        correctly sent to the proxy, rather than in a tunnelled request if
-        CONNECT is being used.
-
-        This should not be called from user code, and is only exposed for use
-        when subclassing the
-        :class:`HTTPAdapter <requests.adapters.HTTPAdapter>`.
-
-        :param proxy: The url of the proxy being used for this request.
-        :rtype: dict
-        """
-        headers = {}
-        username, password = get_auth_from_url(proxy)
-
-        if username:
-            headers['Proxy-Authorization'] = _basic_auth_str(username,
-                                                             password)
-
-        return headers
-
-    def send(self, request, stream=False, timeout=None, verify=True, cert=None, proxies=None):
-        """Sends PreparedRequest object. Returns Response object.
-
-        :param request: The :class:`PreparedRequest <PreparedRequest>` being sent.
-        :param stream: (optional) Whether to stream the request content.
-        :param timeout: (optional) How long to wait for the server to send
-            data before giving up, as a float, or a :ref:`(connect timeout,
-            read timeout) <timeouts>` tuple.
-        :type timeout: float or tuple or urllib3 Timeout object
-        :param verify: (optional) Either a boolean, in which case it controls whether
-            we verify the server's TLS certificate, or a string, in which case it
-            must be a path to a CA bundle to use
-        :param cert: (optional) Any user-provided SSL certificate to be trusted.
-        :param proxies: (optional) The proxies dictionary to apply to the request.
-        :rtype: requests.Response
-        """
-
-        try:
-            conn = self.get_connection(request.url, proxies)
-        except LocationValueError as e:
-            raise InvalidURL(e, request=request)
-
-        self.cert_verify(conn, request.url, verify, cert)
-        url = self.request_url(request, proxies)
-        self.add_headers(request, stream=stream, timeout=timeout, verify=verify, cert=cert, proxies=proxies)
-
-        chunked = not (request.body is None or 'Content-Length' in request.headers)
-
-        if isinstance(timeout, tuple):
-            try:
-                connect, read = timeout
-                timeout = TimeoutSauce(connect=connect, read=read)
-            except ValueError as e:
-                # this may raise a string formatting error.
-                err = ("Invalid timeout {}. Pass a (connect, read) "
-                       "timeout tuple, or a single float to set "
-                       "both timeouts to the same value".format(timeout))
-                raise ValueError(err)
-        elif isinstance(timeout, TimeoutSauce):
-            pass
-        else:
-            timeout = TimeoutSauce(connect=timeout, read=timeout)
-
-        try:
-            if not chunked:
-                resp = conn.urlopen(
-                    method=request.method,
-                    url=url,
-                    body=request.body,
-                    headers=request.headers,
-                    redirect=False,
-                    assert_same_host=False,
-                    preload_content=False,
-                    decode_content=False,
-                    retries=self.max_retries,
-                    timeout=timeout
-                )
-
-            # Send the request.
-            else:
-                if hasattr(conn, 'proxy_pool'):
-                    conn = conn.proxy_pool
-
-                low_conn = conn._get_conn(timeout=DEFAULT_POOL_TIMEOUT)
-
-                try:
-                    low_conn.putrequest(request.method,
-                                        url,
-                                        skip_accept_encoding=True)
-
-                    for header, value in request.headers.items():
-                        low_conn.putheader(header, value)
-
-                    low_conn.endheaders()
-
-                    for i in request.body:
-                        low_conn.send(hex(len(i))[2:].encode('utf-8'))
-                        low_conn.send(b'\r\n')
-                        low_conn.send(i)
-                        low_conn.send(b'\r\n')
-                    low_conn.send(b'0\r\n\r\n')
-
-                    # Receive the response from the server
-                    try:
-                        # For Python 2.7, use buffering of HTTP responses
-                        r = low_conn.getresponse(buffering=True)
-                    except TypeError:
-                        # For compatibility with Python 3.3+
-                        r = low_conn.getresponse()
-
-                    resp = HTTPResponse.from_httplib(
-                        r,
-                        pool=conn,
-                        connection=low_conn,
-                        preload_content=False,
-                        decode_content=False
-                    )
-                except:
-                    # If we hit any problems here, clean up the connection.
-                    # Then, reraise so that we can handle the actual exception.
-                    low_conn.close()
-                    raise
-
-        except (ProtocolError, socket.error) as err:
-            raise ConnectionError(err, request=request)
-
-        except MaxRetryError as e:
-            if isinstance(e.reason, ConnectTimeoutError):
-                # TODO: Remove this in 3.0.0: see #2811
-                if not isinstance(e.reason, NewConnectionError):
-                    raise ConnectTimeout(e, request=request)
-
-            if isinstance(e.reason, ResponseError):
-                raise RetryError(e, request=request)
-
-            if isinstance(e.reason, _ProxyError):
-                raise ProxyError(e, request=request)
-
-            if isinstance(e.reason, _SSLError):
-                # This branch is for urllib3 v1.22 and later.
-                raise SSLError(e, request=request)
-
-            raise ConnectionError(e, request=request)
-
-        except ClosedPoolError as e:
-            raise ConnectionError(e, request=request)
-
-        except _ProxyError as e:
-            raise ProxyError(e)
-
-        except (_SSLError, _HTTPError) as e:
-            if isinstance(e, _SSLError):
-                # This branch is for urllib3 versions earlier than v1.22
-                raise SSLError(e, request=request)
-            elif isinstance(e, ReadTimeoutError):
-                raise ReadTimeout(e, request=request)
-            else:
-                raise
-
-        return self.build_response(request, resp)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/api.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/api.py
deleted file mode 100644
index abada96..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/api.py
+++ /dev/null
@@ -1,158 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.api
-~~~~~~~~~~~~
-
-This module implements the Requests API.
-
-:copyright: (c) 2012 by Kenneth Reitz.
-:license: Apache2, see LICENSE for more details.
-"""
-
-from . import sessions
-
-
-def request(method, url, **kwargs):
-    """Constructs and sends a :class:`Request <Request>`.
-
-    :param method: method for the new :class:`Request` object.
-    :param url: URL for the new :class:`Request` object.
-    :param params: (optional) Dictionary, list of tuples or bytes to send
-        in the body of the :class:`Request`.
-    :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-        object to send in the body of the :class:`Request`.
-    :param json: (optional) A JSON serializable Python object to send in the body of the :class:`Request`.
-    :param headers: (optional) Dictionary of HTTP Headers to send with the :class:`Request`.
-    :param cookies: (optional) Dict or CookieJar object to send with the :class:`Request`.
-    :param files: (optional) Dictionary of ``'name': file-like-objects`` (or ``{'name': file-tuple}``) for multipart encoding upload.
-        ``file-tuple`` can be a 2-tuple ``('filename', fileobj)``, 3-tuple ``('filename', fileobj, 'content_type')``
-        or a 4-tuple ``('filename', fileobj, 'content_type', custom_headers)``, where ``'content-type'`` is a string
-        defining the content type of the given file and ``custom_headers`` a dict-like object containing additional headers
-        to add for the file.
-    :param auth: (optional) Auth tuple to enable Basic/Digest/Custom HTTP Auth.
-    :param timeout: (optional) How many seconds to wait for the server to send data
-        before giving up, as a float, or a :ref:`(connect timeout, read
-        timeout) <timeouts>` tuple.
-    :type timeout: float or tuple
-    :param allow_redirects: (optional) Boolean. Enable/disable GET/OPTIONS/POST/PUT/PATCH/DELETE/HEAD redirection. Defaults to ``True``.
-    :type allow_redirects: bool
-    :param proxies: (optional) Dictionary mapping protocol to the URL of the proxy.
-    :param verify: (optional) Either a boolean, in which case it controls whether we verify
-            the server's TLS certificate, or a string, in which case it must be a path
-            to a CA bundle to use. Defaults to ``True``.
-    :param stream: (optional) if ``False``, the response content will be immediately downloaded.
-    :param cert: (optional) if String, path to ssl client cert file (.pem). If Tuple, ('cert', 'key') pair.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-
-    Usage::
-
-      >>> import requests
-      >>> req = requests.request('GET', 'https://httpbin.org/get')
-      <Response [200]>
-    """
-
-    # By using the 'with' statement we are sure the session is closed, thus we
-    # avoid leaving sockets open which can trigger a ResourceWarning in some
-    # cases, and look like a memory leak in others.
-    with sessions.Session() as session:
-        return session.request(method=method, url=url, **kwargs)
-
-
-def get(url, params=None, **kwargs):
-    r"""Sends a GET request.
-
-    :param url: URL for the new :class:`Request` object.
-    :param params: (optional) Dictionary, list of tuples or bytes to send
-        in the body of the :class:`Request`.
-    :param \*\*kwargs: Optional arguments that ``request`` takes.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-    """
-
-    kwargs.setdefault('allow_redirects', True)
-    return request('get', url, params=params, **kwargs)
-
-
-def options(url, **kwargs):
-    r"""Sends an OPTIONS request.
-
-    :param url: URL for the new :class:`Request` object.
-    :param \*\*kwargs: Optional arguments that ``request`` takes.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-    """
-
-    kwargs.setdefault('allow_redirects', True)
-    return request('options', url, **kwargs)
-
-
-def head(url, **kwargs):
-    r"""Sends a HEAD request.
-
-    :param url: URL for the new :class:`Request` object.
-    :param \*\*kwargs: Optional arguments that ``request`` takes.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-    """
-
-    kwargs.setdefault('allow_redirects', False)
-    return request('head', url, **kwargs)
-
-
-def post(url, data=None, json=None, **kwargs):
-    r"""Sends a POST request.
-
-    :param url: URL for the new :class:`Request` object.
-    :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-        object to send in the body of the :class:`Request`.
-    :param json: (optional) json data to send in the body of the :class:`Request`.
-    :param \*\*kwargs: Optional arguments that ``request`` takes.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-    """
-
-    return request('post', url, data=data, json=json, **kwargs)
-
-
-def put(url, data=None, **kwargs):
-    r"""Sends a PUT request.
-
-    :param url: URL for the new :class:`Request` object.
-    :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-        object to send in the body of the :class:`Request`.
-    :param json: (optional) json data to send in the body of the :class:`Request`.
-    :param \*\*kwargs: Optional arguments that ``request`` takes.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-    """
-
-    return request('put', url, data=data, **kwargs)
-
-
-def patch(url, data=None, **kwargs):
-    r"""Sends a PATCH request.
-
-    :param url: URL for the new :class:`Request` object.
-    :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-        object to send in the body of the :class:`Request`.
-    :param json: (optional) json data to send in the body of the :class:`Request`.
-    :param \*\*kwargs: Optional arguments that ``request`` takes.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-    """
-
-    return request('patch', url, data=data, **kwargs)
-
-
-def delete(url, **kwargs):
-    r"""Sends a DELETE request.
-
-    :param url: URL for the new :class:`Request` object.
-    :param \*\*kwargs: Optional arguments that ``request`` takes.
-    :return: :class:`Response <Response>` object
-    :rtype: requests.Response
-    """
-
-    return request('delete', url, **kwargs)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/auth.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/auth.py
deleted file mode 100644
index bdde51c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/auth.py
+++ /dev/null
@@ -1,305 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.auth
-~~~~~~~~~~~~~
-
-This module contains the authentication handlers for Requests.
-"""
-
-import os
-import re
-import time
-import hashlib
-import threading
-import warnings
-
-from base64 import b64encode
-
-from .compat import urlparse, str, basestring
-from .cookies import extract_cookies_to_jar
-from ._internal_utils import to_native_string
-from .utils import parse_dict_header
-
-CONTENT_TYPE_FORM_URLENCODED = 'application/x-www-form-urlencoded'
-CONTENT_TYPE_MULTI_PART = 'multipart/form-data'
-
-
-def _basic_auth_str(username, password):
-    """Returns a Basic Auth string."""
-
-    # "I want us to put a big-ol' comment on top of it that
-    # says that this behaviour is dumb but we need to preserve
-    # it because people are relying on it."
-    #    - Lukasa
-    #
-    # These are here solely to maintain backwards compatibility
-    # for things like ints. This will be removed in 3.0.0.
-    if not isinstance(username, basestring):
-        warnings.warn(
-            "Non-string usernames will no longer be supported in Requests "
-            "3.0.0. Please convert the object you've passed in ({!r}) to "
-            "a string or bytes object in the near future to avoid "
-            "problems.".format(username),
-            category=DeprecationWarning,
-        )
-        username = str(username)
-
-    if not isinstance(password, basestring):
-        warnings.warn(
-            "Non-string passwords will no longer be supported in Requests "
-            "3.0.0. Please convert the object you've passed in ({!r}) to "
-            "a string or bytes object in the near future to avoid "
-            "problems.".format(password),
-            category=DeprecationWarning,
-        )
-        password = str(password)
-    # -- End Removal --
-
-    if isinstance(username, str):
-        username = username.encode('latin1')
-
-    if isinstance(password, str):
-        password = password.encode('latin1')
-
-    authstr = 'Basic ' + to_native_string(
-        b64encode(b':'.join((username, password))).strip()
-    )
-
-    return authstr
-
-
-class AuthBase(object):
-    """Base class that all auth implementations derive from"""
-
-    def __call__(self, r):
-        raise NotImplementedError('Auth hooks must be callable.')
-
-
-class HTTPBasicAuth(AuthBase):
-    """Attaches HTTP Basic Authentication to the given Request object."""
-
-    def __init__(self, username, password):
-        self.username = username
-        self.password = password
-
-    def __eq__(self, other):
-        return all([
-            self.username == getattr(other, 'username', None),
-            self.password == getattr(other, 'password', None)
-        ])
-
-    def __ne__(self, other):
-        return not self == other
-
-    def __call__(self, r):
-        r.headers['Authorization'] = _basic_auth_str(self.username, self.password)
-        return r
-
-
-class HTTPProxyAuth(HTTPBasicAuth):
-    """Attaches HTTP Proxy Authentication to a given Request object."""
-
-    def __call__(self, r):
-        r.headers['Proxy-Authorization'] = _basic_auth_str(self.username, self.password)
-        return r
-
-
-class HTTPDigestAuth(AuthBase):
-    """Attaches HTTP Digest Authentication to the given Request object."""
-
-    def __init__(self, username, password):
-        self.username = username
-        self.password = password
-        # Keep state in per-thread local storage
-        self._thread_local = threading.local()
-
-    def init_per_thread_state(self):
-        # Ensure state is initialized just once per-thread
-        if not hasattr(self._thread_local, 'init'):
-            self._thread_local.init = True
-            self._thread_local.last_nonce = ''
-            self._thread_local.nonce_count = 0
-            self._thread_local.chal = {}
-            self._thread_local.pos = None
-            self._thread_local.num_401_calls = None
-
-    def build_digest_header(self, method, url):
-        """
-        :rtype: str
-        """
-
-        realm = self._thread_local.chal['realm']
-        nonce = self._thread_local.chal['nonce']
-        qop = self._thread_local.chal.get('qop')
-        algorithm = self._thread_local.chal.get('algorithm')
-        opaque = self._thread_local.chal.get('opaque')
-        hash_utf8 = None
-
-        if algorithm is None:
-            _algorithm = 'MD5'
-        else:
-            _algorithm = algorithm.upper()
-        # lambdas assume digest modules are imported at the top level
-        if _algorithm == 'MD5' or _algorithm == 'MD5-SESS':
-            def md5_utf8(x):
-                if isinstance(x, str):
-                    x = x.encode('utf-8')
-                return hashlib.md5(x).hexdigest()
-            hash_utf8 = md5_utf8
-        elif _algorithm == 'SHA':
-            def sha_utf8(x):
-                if isinstance(x, str):
-                    x = x.encode('utf-8')
-                return hashlib.sha1(x).hexdigest()
-            hash_utf8 = sha_utf8
-        elif _algorithm == 'SHA-256':
-            def sha256_utf8(x):
-                if isinstance(x, str):
-                    x = x.encode('utf-8')
-                return hashlib.sha256(x).hexdigest()
-            hash_utf8 = sha256_utf8
-        elif _algorithm == 'SHA-512':
-            def sha512_utf8(x):
-                if isinstance(x, str):
-                    x = x.encode('utf-8')
-                return hashlib.sha512(x).hexdigest()
-            hash_utf8 = sha512_utf8
-
-        KD = lambda s, d: hash_utf8("%s:%s" % (s, d))
-
-        if hash_utf8 is None:
-            return None
-
-        # XXX not implemented yet
-        entdig = None
-        p_parsed = urlparse(url)
-        #: path is request-uri defined in RFC 2616 which should not be empty
-        path = p_parsed.path or "/"
-        if p_parsed.query:
-            path += '?' + p_parsed.query
-
-        A1 = '%s:%s:%s' % (self.username, realm, self.password)
-        A2 = '%s:%s' % (method, path)
-
-        HA1 = hash_utf8(A1)
-        HA2 = hash_utf8(A2)
-
-        if nonce == self._thread_local.last_nonce:
-            self._thread_local.nonce_count += 1
-        else:
-            self._thread_local.nonce_count = 1
-        ncvalue = '%08x' % self._thread_local.nonce_count
-        s = str(self._thread_local.nonce_count).encode('utf-8')
-        s += nonce.encode('utf-8')
-        s += time.ctime().encode('utf-8')
-        s += os.urandom(8)
-
-        cnonce = (hashlib.sha1(s).hexdigest()[:16])
-        if _algorithm == 'MD5-SESS':
-            HA1 = hash_utf8('%s:%s:%s' % (HA1, nonce, cnonce))
-
-        if not qop:
-            respdig = KD(HA1, "%s:%s" % (nonce, HA2))
-        elif qop == 'auth' or 'auth' in qop.split(','):
-            noncebit = "%s:%s:%s:%s:%s" % (
-                nonce, ncvalue, cnonce, 'auth', HA2
-            )
-            respdig = KD(HA1, noncebit)
-        else:
-            # XXX handle auth-int.
-            return None
-
-        self._thread_local.last_nonce = nonce
-
-        # XXX should the partial digests be encoded too?
-        base = 'username="%s", realm="%s", nonce="%s", uri="%s", ' \
-               'response="%s"' % (self.username, realm, nonce, path, respdig)
-        if opaque:
-            base += ', opaque="%s"' % opaque
-        if algorithm:
-            base += ', algorithm="%s"' % algorithm
-        if entdig:
-            base += ', digest="%s"' % entdig
-        if qop:
-            base += ', qop="auth", nc=%s, cnonce="%s"' % (ncvalue, cnonce)
-
-        return 'Digest %s' % (base)
-
-    def handle_redirect(self, r, **kwargs):
-        """Reset num_401_calls counter on redirects."""
-        if r.is_redirect:
-            self._thread_local.num_401_calls = 1
-
-    def handle_401(self, r, **kwargs):
-        """
-        Takes the given response and tries digest-auth, if needed.
-
-        :rtype: requests.Response
-        """
-
-        # If response is not 4xx, do not auth
-        # See https://github.com/requests/requests/issues/3772
-        if not 400 <= r.status_code < 500:
-            self._thread_local.num_401_calls = 1
-            return r
-
-        if self._thread_local.pos is not None:
-            # Rewind the file position indicator of the body to where
-            # it was to resend the request.
-            r.request.body.seek(self._thread_local.pos)
-        s_auth = r.headers.get('www-authenticate', '')
-
-        if 'digest' in s_auth.lower() and self._thread_local.num_401_calls < 2:
-
-            self._thread_local.num_401_calls += 1
-            pat = re.compile(r'digest ', flags=re.IGNORECASE)
-            self._thread_local.chal = parse_dict_header(pat.sub('', s_auth, count=1))
-
-            # Consume content and release the original connection
-            # to allow our new request to reuse the same one.
-            r.content
-            r.close()
-            prep = r.request.copy()
-            extract_cookies_to_jar(prep._cookies, r.request, r.raw)
-            prep.prepare_cookies(prep._cookies)
-
-            prep.headers['Authorization'] = self.build_digest_header(
-                prep.method, prep.url)
-            _r = r.connection.send(prep, **kwargs)
-            _r.history.append(r)
-            _r.request = prep
-
-            return _r
-
-        self._thread_local.num_401_calls = 1
-        return r
-
-    def __call__(self, r):
-        # Initialize per-thread state, if needed
-        self.init_per_thread_state()
-        # If we have a saved nonce, skip the 401
-        if self._thread_local.last_nonce:
-            r.headers['Authorization'] = self.build_digest_header(r.method, r.url)
-        try:
-            self._thread_local.pos = r.body.tell()
-        except AttributeError:
-            # In the case of HTTPDigestAuth being reused and the body of
-            # the previous request was a file-like object, pos has the
-            # file position of the previous body. Ensure it's set to
-            # None.
-            self._thread_local.pos = None
-        r.register_hook('response', self.handle_401)
-        r.register_hook('response', self.handle_redirect)
-        self._thread_local.num_401_calls = 1
-
-        return r
-
-    def __eq__(self, other):
-        return all([
-            self.username == getattr(other, 'username', None),
-            self.password == getattr(other, 'password', None)
-        ])
-
-    def __ne__(self, other):
-        return not self == other
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/certs.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/certs.py
deleted file mode 100644
index 06a594e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/certs.py
+++ /dev/null
@@ -1,18 +0,0 @@
-#!/usr/bin/env python
-# -*- coding: utf-8 -*-
-
-"""
-requests.certs
-~~~~~~~~~~~~~~
-
-This module returns the preferred default CA certificate bundle. There is
-only one — the one from the certifi package.
-
-If you are packaging Requests, e.g., for a Linux distribution or a managed
-environment, you can change the definition of where() to return a separately
-packaged CA bundle.
-"""
-from pip._vendor.certifi import where
-
-if __name__ == '__main__':
-    print(where())
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/compat.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/compat.py
deleted file mode 100644
index 6a86893..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/compat.py
+++ /dev/null
@@ -1,74 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.compat
-~~~~~~~~~~~~~~~
-
-This module handles import compatibility issues between Python 2 and
-Python 3.
-"""
-
-from pip._vendor import chardet
-
-import sys
-
-# -------
-# Pythons
-# -------
-
-# Syntax sugar.
-_ver = sys.version_info
-
-#: Python 2.x?
-is_py2 = (_ver[0] == 2)
-
-#: Python 3.x?
-is_py3 = (_ver[0] == 3)
-
-# Note: We've patched out simplejson support in pip because it prevents
-#       upgrading simplejson on Windows.
-# try:
-#     import simplejson as json
-# except (ImportError, SyntaxError):
-#     # simplejson does not support Python 3.2, it throws a SyntaxError
-#     # because of u'...' Unicode literals.
-import json
-
-# ---------
-# Specifics
-# ---------
-
-if is_py2:
-    from urllib import (
-        quote, unquote, quote_plus, unquote_plus, urlencode, getproxies,
-        proxy_bypass, proxy_bypass_environment, getproxies_environment)
-    from urlparse import urlparse, urlunparse, urljoin, urlsplit, urldefrag
-    from urllib2 import parse_http_list
-    import cookielib
-    from Cookie import Morsel
-    from StringIO import StringIO
-    from collections import Callable, Mapping, MutableMapping, OrderedDict
-
-
-    builtin_str = str
-    bytes = str
-    str = unicode
-    basestring = basestring
-    numeric_types = (int, long, float)
-    integer_types = (int, long)
-
-elif is_py3:
-    from urllib.parse import urlparse, urlunparse, urljoin, urlsplit, urlencode, quote, unquote, quote_plus, unquote_plus, urldefrag
-    from urllib.request import parse_http_list, getproxies, proxy_bypass, proxy_bypass_environment, getproxies_environment
-    from http import cookiejar as cookielib
-    from http.cookies import Morsel
-    from io import StringIO
-    from collections import OrderedDict
-    from collections.abc import Callable, Mapping, MutableMapping
-
-    builtin_str = str
-    str = str
-    bytes = bytes
-    basestring = (str, bytes)
-    numeric_types = (int, float)
-    integer_types = (int,)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/cookies.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/cookies.py
deleted file mode 100644
index 56fccd9..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/cookies.py
+++ /dev/null
@@ -1,549 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.cookies
-~~~~~~~~~~~~~~~~
-
-Compatibility code to be able to use `cookielib.CookieJar` with requests.
-
-requests.utils imports from here, so be careful with imports.
-"""
-
-import copy
-import time
-import calendar
-
-from ._internal_utils import to_native_string
-from .compat import cookielib, urlparse, urlunparse, Morsel, MutableMapping
-
-try:
-    import threading
-except ImportError:
-    import dummy_threading as threading
-
-
-class MockRequest(object):
-    """Wraps a `requests.Request` to mimic a `urllib2.Request`.
-
-    The code in `cookielib.CookieJar` expects this interface in order to correctly
-    manage cookie policies, i.e., determine whether a cookie can be set, given the
-    domains of the request and the cookie.
-
-    The original request object is read-only. The client is responsible for collecting
-    the new headers via `get_new_headers()` and interpreting them appropriately. You
-    probably want `get_cookie_header`, defined below.
-    """
-
-    def __init__(self, request):
-        self._r = request
-        self._new_headers = {}
-        self.type = urlparse(self._r.url).scheme
-
-    def get_type(self):
-        return self.type
-
-    def get_host(self):
-        return urlparse(self._r.url).netloc
-
-    def get_origin_req_host(self):
-        return self.get_host()
-
-    def get_full_url(self):
-        # Only return the response's URL if the user hadn't set the Host
-        # header
-        if not self._r.headers.get('Host'):
-            return self._r.url
-        # If they did set it, retrieve it and reconstruct the expected domain
-        host = to_native_string(self._r.headers['Host'], encoding='utf-8')
-        parsed = urlparse(self._r.url)
-        # Reconstruct the URL as we expect it
-        return urlunparse([
-            parsed.scheme, host, parsed.path, parsed.params, parsed.query,
-            parsed.fragment
-        ])
-
-    def is_unverifiable(self):
-        return True
-
-    def has_header(self, name):
-        return name in self._r.headers or name in self._new_headers
-
-    def get_header(self, name, default=None):
-        return self._r.headers.get(name, self._new_headers.get(name, default))
-
-    def add_header(self, key, val):
-        """cookielib has no legitimate use for this method; add it back if you find one."""
-        raise NotImplementedError("Cookie headers should be added with add_unredirected_header()")
-
-    def add_unredirected_header(self, name, value):
-        self._new_headers[name] = value
-
-    def get_new_headers(self):
-        return self._new_headers
-
-    @property
-    def unverifiable(self):
-        return self.is_unverifiable()
-
-    @property
-    def origin_req_host(self):
-        return self.get_origin_req_host()
-
-    @property
-    def host(self):
-        return self.get_host()
-
-
-class MockResponse(object):
-    """Wraps a `httplib.HTTPMessage` to mimic a `urllib.addinfourl`.
-
-    ...what? Basically, expose the parsed HTTP headers from the server response
-    the way `cookielib` expects to see them.
-    """
-
-    def __init__(self, headers):
-        """Make a MockResponse for `cookielib` to read.
-
-        :param headers: a httplib.HTTPMessage or analogous carrying the headers
-        """
-        self._headers = headers
-
-    def info(self):
-        return self._headers
-
-    def getheaders(self, name):
-        self._headers.getheaders(name)
-
-
-def extract_cookies_to_jar(jar, request, response):
-    """Extract the cookies from the response into a CookieJar.
-
-    :param jar: cookielib.CookieJar (not necessarily a RequestsCookieJar)
-    :param request: our own requests.Request object
-    :param response: urllib3.HTTPResponse object
-    """
-    if not (hasattr(response, '_original_response') and
-            response._original_response):
-        return
-    # the _original_response field is the wrapped httplib.HTTPResponse object,
-    req = MockRequest(request)
-    # pull out the HTTPMessage with the headers and put it in the mock:
-    res = MockResponse(response._original_response.msg)
-    jar.extract_cookies(res, req)
-
-
-def get_cookie_header(jar, request):
-    """
-    Produce an appropriate Cookie header string to be sent with `request`, or None.
-
-    :rtype: str
-    """
-    r = MockRequest(request)
-    jar.add_cookie_header(r)
-    return r.get_new_headers().get('Cookie')
-
-
-def remove_cookie_by_name(cookiejar, name, domain=None, path=None):
-    """Unsets a cookie by name, by default over all domains and paths.
-
-    Wraps CookieJar.clear(), is O(n).
-    """
-    clearables = []
-    for cookie in cookiejar:
-        if cookie.name != name:
-            continue
-        if domain is not None and domain != cookie.domain:
-            continue
-        if path is not None and path != cookie.path:
-            continue
-        clearables.append((cookie.domain, cookie.path, cookie.name))
-
-    for domain, path, name in clearables:
-        cookiejar.clear(domain, path, name)
-
-
-class CookieConflictError(RuntimeError):
-    """There are two cookies that meet the criteria specified in the cookie jar.
-    Use .get and .set and include domain and path args in order to be more specific.
-    """
-
-
-class RequestsCookieJar(cookielib.CookieJar, MutableMapping):
-    """Compatibility class; is a cookielib.CookieJar, but exposes a dict
-    interface.
-
-    This is the CookieJar we create by default for requests and sessions that
-    don't specify one, since some clients may expect response.cookies and
-    session.cookies to support dict operations.
-
-    Requests does not use the dict interface internally; it's just for
-    compatibility with external client code. All requests code should work
-    out of the box with externally provided instances of ``CookieJar``, e.g.
-    ``LWPCookieJar`` and ``FileCookieJar``.
-
-    Unlike a regular CookieJar, this class is pickleable.
-
-    .. warning:: dictionary operations that are normally O(1) may be O(n).
-    """
-
-    def get(self, name, default=None, domain=None, path=None):
-        """Dict-like get() that also supports optional domain and path args in
-        order to resolve naming collisions from using one cookie jar over
-        multiple domains.
-
-        .. warning:: operation is O(n), not O(1).
-        """
-        try:
-            return self._find_no_duplicates(name, domain, path)
-        except KeyError:
-            return default
-
-    def set(self, name, value, **kwargs):
-        """Dict-like set() that also supports optional domain and path args in
-        order to resolve naming collisions from using one cookie jar over
-        multiple domains.
-        """
-        # support client code that unsets cookies by assignment of a None value:
-        if value is None:
-            remove_cookie_by_name(self, name, domain=kwargs.get('domain'), path=kwargs.get('path'))
-            return
-
-        if isinstance(value, Morsel):
-            c = morsel_to_cookie(value)
-        else:
-            c = create_cookie(name, value, **kwargs)
-        self.set_cookie(c)
-        return c
-
-    def iterkeys(self):
-        """Dict-like iterkeys() that returns an iterator of names of cookies
-        from the jar.
-
-        .. seealso:: itervalues() and iteritems().
-        """
-        for cookie in iter(self):
-            yield cookie.name
-
-    def keys(self):
-        """Dict-like keys() that returns a list of names of cookies from the
-        jar.
-
-        .. seealso:: values() and items().
-        """
-        return list(self.iterkeys())
-
-    def itervalues(self):
-        """Dict-like itervalues() that returns an iterator of values of cookies
-        from the jar.
-
-        .. seealso:: iterkeys() and iteritems().
-        """
-        for cookie in iter(self):
-            yield cookie.value
-
-    def values(self):
-        """Dict-like values() that returns a list of values of cookies from the
-        jar.
-
-        .. seealso:: keys() and items().
-        """
-        return list(self.itervalues())
-
-    def iteritems(self):
-        """Dict-like iteritems() that returns an iterator of name-value tuples
-        from the jar.
-
-        .. seealso:: iterkeys() and itervalues().
-        """
-        for cookie in iter(self):
-            yield cookie.name, cookie.value
-
-    def items(self):
-        """Dict-like items() that returns a list of name-value tuples from the
-        jar. Allows client-code to call ``dict(RequestsCookieJar)`` and get a
-        vanilla python dict of key value pairs.
-
-        .. seealso:: keys() and values().
-        """
-        return list(self.iteritems())
-
-    def list_domains(self):
-        """Utility method to list all the domains in the jar."""
-        domains = []
-        for cookie in iter(self):
-            if cookie.domain not in domains:
-                domains.append(cookie.domain)
-        return domains
-
-    def list_paths(self):
-        """Utility method to list all the paths in the jar."""
-        paths = []
-        for cookie in iter(self):
-            if cookie.path not in paths:
-                paths.append(cookie.path)
-        return paths
-
-    def multiple_domains(self):
-        """Returns True if there are multiple domains in the jar.
-        Returns False otherwise.
-
-        :rtype: bool
-        """
-        domains = []
-        for cookie in iter(self):
-            if cookie.domain is not None and cookie.domain in domains:
-                return True
-            domains.append(cookie.domain)
-        return False  # there is only one domain in jar
-
-    def get_dict(self, domain=None, path=None):
-        """Takes as an argument an optional domain and path and returns a plain
-        old Python dict of name-value pairs of cookies that meet the
-        requirements.
-
-        :rtype: dict
-        """
-        dictionary = {}
-        for cookie in iter(self):
-            if (
-                (domain is None or cookie.domain == domain) and
-                (path is None or cookie.path == path)
-            ):
-                dictionary[cookie.name] = cookie.value
-        return dictionary
-
-    def __contains__(self, name):
-        try:
-            return super(RequestsCookieJar, self).__contains__(name)
-        except CookieConflictError:
-            return True
-
-    def __getitem__(self, name):
-        """Dict-like __getitem__() for compatibility with client code. Throws
-        exception if there are more than one cookie with name. In that case,
-        use the more explicit get() method instead.
-
-        .. warning:: operation is O(n), not O(1).
-        """
-        return self._find_no_duplicates(name)
-
-    def __setitem__(self, name, value):
-        """Dict-like __setitem__ for compatibility with client code. Throws
-        exception if there is already a cookie of that name in the jar. In that
-        case, use the more explicit set() method instead.
-        """
-        self.set(name, value)
-
-    def __delitem__(self, name):
-        """Deletes a cookie given a name. Wraps ``cookielib.CookieJar``'s
-        ``remove_cookie_by_name()``.
-        """
-        remove_cookie_by_name(self, name)
-
-    def set_cookie(self, cookie, *args, **kwargs):
-        if hasattr(cookie.value, 'startswith') and cookie.value.startswith('"') and cookie.value.endswith('"'):
-            cookie.value = cookie.value.replace('\\"', '')
-        return super(RequestsCookieJar, self).set_cookie(cookie, *args, **kwargs)
-
-    def update(self, other):
-        """Updates this jar with cookies from another CookieJar or dict-like"""
-        if isinstance(other, cookielib.CookieJar):
-            for cookie in other:
-                self.set_cookie(copy.copy(cookie))
-        else:
-            super(RequestsCookieJar, self).update(other)
-
-    def _find(self, name, domain=None, path=None):
-        """Requests uses this method internally to get cookie values.
-
-        If there are conflicting cookies, _find arbitrarily chooses one.
-        See _find_no_duplicates if you want an exception thrown if there are
-        conflicting cookies.
-
-        :param name: a string containing name of cookie
-        :param domain: (optional) string containing domain of cookie
-        :param path: (optional) string containing path of cookie
-        :return: cookie.value
-        """
-        for cookie in iter(self):
-            if cookie.name == name:
-                if domain is None or cookie.domain == domain:
-                    if path is None or cookie.path == path:
-                        return cookie.value
-
-        raise KeyError('name=%r, domain=%r, path=%r' % (name, domain, path))
-
-    def _find_no_duplicates(self, name, domain=None, path=None):
-        """Both ``__get_item__`` and ``get`` call this function: it's never
-        used elsewhere in Requests.
-
-        :param name: a string containing name of cookie
-        :param domain: (optional) string containing domain of cookie
-        :param path: (optional) string containing path of cookie
-        :raises KeyError: if cookie is not found
-        :raises CookieConflictError: if there are multiple cookies
-            that match name and optionally domain and path
-        :return: cookie.value
-        """
-        toReturn = None
-        for cookie in iter(self):
-            if cookie.name == name:
-                if domain is None or cookie.domain == domain:
-                    if path is None or cookie.path == path:
-                        if toReturn is not None:  # if there are multiple cookies that meet passed in criteria
-                            raise CookieConflictError('There are multiple cookies with name, %r' % (name))
-                        toReturn = cookie.value  # we will eventually return this as long as no cookie conflict
-
-        if toReturn:
-            return toReturn
-        raise KeyError('name=%r, domain=%r, path=%r' % (name, domain, path))
-
-    def __getstate__(self):
-        """Unlike a normal CookieJar, this class is pickleable."""
-        state = self.__dict__.copy()
-        # remove the unpickleable RLock object
-        state.pop('_cookies_lock')
-        return state
-
-    def __setstate__(self, state):
-        """Unlike a normal CookieJar, this class is pickleable."""
-        self.__dict__.update(state)
-        if '_cookies_lock' not in self.__dict__:
-            self._cookies_lock = threading.RLock()
-
-    def copy(self):
-        """Return a copy of this RequestsCookieJar."""
-        new_cj = RequestsCookieJar()
-        new_cj.set_policy(self.get_policy())
-        new_cj.update(self)
-        return new_cj
-
-    def get_policy(self):
-        """Return the CookiePolicy instance used."""
-        return self._policy
-
-
-def _copy_cookie_jar(jar):
-    if jar is None:
-        return None
-
-    if hasattr(jar, 'copy'):
-        # We're dealing with an instance of RequestsCookieJar
-        return jar.copy()
-    # We're dealing with a generic CookieJar instance
-    new_jar = copy.copy(jar)
-    new_jar.clear()
-    for cookie in jar:
-        new_jar.set_cookie(copy.copy(cookie))
-    return new_jar
-
-
-def create_cookie(name, value, **kwargs):
-    """Make a cookie from underspecified parameters.
-
-    By default, the pair of `name` and `value` will be set for the domain ''
-    and sent on every request (this is sometimes called a "supercookie").
-    """
-    result = {
-        'version': 0,
-        'name': name,
-        'value': value,
-        'port': None,
-        'domain': '',
-        'path': '/',
-        'secure': False,
-        'expires': None,
-        'discard': True,
-        'comment': None,
-        'comment_url': None,
-        'rest': {'HttpOnly': None},
-        'rfc2109': False,
-    }
-
-    badargs = set(kwargs) - set(result)
-    if badargs:
-        err = 'create_cookie() got unexpected keyword arguments: %s'
-        raise TypeError(err % list(badargs))
-
-    result.update(kwargs)
-    result['port_specified'] = bool(result['port'])
-    result['domain_specified'] = bool(result['domain'])
-    result['domain_initial_dot'] = result['domain'].startswith('.')
-    result['path_specified'] = bool(result['path'])
-
-    return cookielib.Cookie(**result)
-
-
-def morsel_to_cookie(morsel):
-    """Convert a Morsel object into a Cookie containing the one k/v pair."""
-
-    expires = None
-    if morsel['max-age']:
-        try:
-            expires = int(time.time() + int(morsel['max-age']))
-        except ValueError:
-            raise TypeError('max-age: %s must be integer' % morsel['max-age'])
-    elif morsel['expires']:
-        time_template = '%a, %d-%b-%Y %H:%M:%S GMT'
-        expires = calendar.timegm(
-            time.strptime(morsel['expires'], time_template)
-        )
-    return create_cookie(
-        comment=morsel['comment'],
-        comment_url=bool(morsel['comment']),
-        discard=False,
-        domain=morsel['domain'],
-        expires=expires,
-        name=morsel.key,
-        path=morsel['path'],
-        port=None,
-        rest={'HttpOnly': morsel['httponly']},
-        rfc2109=False,
-        secure=bool(morsel['secure']),
-        value=morsel.value,
-        version=morsel['version'] or 0,
-    )
-
-
-def cookiejar_from_dict(cookie_dict, cookiejar=None, overwrite=True):
-    """Returns a CookieJar from a key/value dictionary.
-
-    :param cookie_dict: Dict of key/values to insert into CookieJar.
-    :param cookiejar: (optional) A cookiejar to add the cookies to.
-    :param overwrite: (optional) If False, will not replace cookies
-        already in the jar with new ones.
-    :rtype: CookieJar
-    """
-    if cookiejar is None:
-        cookiejar = RequestsCookieJar()
-
-    if cookie_dict is not None:
-        names_from_jar = [cookie.name for cookie in cookiejar]
-        for name in cookie_dict:
-            if overwrite or (name not in names_from_jar):
-                cookiejar.set_cookie(create_cookie(name, cookie_dict[name]))
-
-    return cookiejar
-
-
-def merge_cookies(cookiejar, cookies):
-    """Add cookies to cookiejar and returns a merged CookieJar.
-
-    :param cookiejar: CookieJar object to add the cookies to.
-    :param cookies: Dictionary or CookieJar object to be added.
-    :rtype: CookieJar
-    """
-    if not isinstance(cookiejar, cookielib.CookieJar):
-        raise ValueError('You can only merge into CookieJar')
-
-    if isinstance(cookies, dict):
-        cookiejar = cookiejar_from_dict(
-            cookies, cookiejar=cookiejar, overwrite=False)
-    elif isinstance(cookies, cookielib.CookieJar):
-        try:
-            cookiejar.update(cookies)
-        except AttributeError:
-            for cookie_in_jar in cookies:
-                cookiejar.set_cookie(cookie_in_jar)
-
-    return cookiejar
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/exceptions.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/exceptions.py
deleted file mode 100644
index a91e1fd..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/exceptions.py
+++ /dev/null
@@ -1,126 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.exceptions
-~~~~~~~~~~~~~~~~~~~
-
-This module contains the set of Requests' exceptions.
-"""
-from pip._vendor.urllib3.exceptions import HTTPError as BaseHTTPError
-
-
-class RequestException(IOError):
-    """There was an ambiguous exception that occurred while handling your
-    request.
-    """
-
-    def __init__(self, *args, **kwargs):
-        """Initialize RequestException with `request` and `response` objects."""
-        response = kwargs.pop('response', None)
-        self.response = response
-        self.request = kwargs.pop('request', None)
-        if (response is not None and not self.request and
-                hasattr(response, 'request')):
-            self.request = self.response.request
-        super(RequestException, self).__init__(*args, **kwargs)
-
-
-class HTTPError(RequestException):
-    """An HTTP error occurred."""
-
-
-class ConnectionError(RequestException):
-    """A Connection error occurred."""
-
-
-class ProxyError(ConnectionError):
-    """A proxy error occurred."""
-
-
-class SSLError(ConnectionError):
-    """An SSL error occurred."""
-
-
-class Timeout(RequestException):
-    """The request timed out.
-
-    Catching this error will catch both
-    :exc:`~requests.exceptions.ConnectTimeout` and
-    :exc:`~requests.exceptions.ReadTimeout` errors.
-    """
-
-
-class ConnectTimeout(ConnectionError, Timeout):
-    """The request timed out while trying to connect to the remote server.
-
-    Requests that produced this error are safe to retry.
-    """
-
-
-class ReadTimeout(Timeout):
-    """The server did not send any data in the allotted amount of time."""
-
-
-class URLRequired(RequestException):
-    """A valid URL is required to make a request."""
-
-
-class TooManyRedirects(RequestException):
-    """Too many redirects."""
-
-
-class MissingSchema(RequestException, ValueError):
-    """The URL schema (e.g. http or https) is missing."""
-
-
-class InvalidSchema(RequestException, ValueError):
-    """See defaults.py for valid schemas."""
-
-
-class InvalidURL(RequestException, ValueError):
-    """The URL provided was somehow invalid."""
-
-
-class InvalidHeader(RequestException, ValueError):
-    """The header value provided was somehow invalid."""
-
-
-class InvalidProxyURL(InvalidURL):
-    """The proxy URL provided is invalid."""
-
-
-class ChunkedEncodingError(RequestException):
-    """The server declared chunked encoding but sent an invalid chunk."""
-
-
-class ContentDecodingError(RequestException, BaseHTTPError):
-    """Failed to decode response content"""
-
-
-class StreamConsumedError(RequestException, TypeError):
-    """The content for this response was already consumed"""
-
-
-class RetryError(RequestException):
-    """Custom retries logic failed"""
-
-
-class UnrewindableBodyError(RequestException):
-    """Requests encountered an error when trying to rewind a body"""
-
-# Warnings
-
-
-class RequestsWarning(Warning):
-    """Base warning for Requests."""
-    pass
-
-
-class FileModeWarning(RequestsWarning, DeprecationWarning):
-    """A file was opened in text mode, but Requests determined its binary length."""
-    pass
-
-
-class RequestsDependencyWarning(RequestsWarning):
-    """An imported dependency doesn't match the expected version range."""
-    pass
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/help.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/help.py
deleted file mode 100644
index 3c3072b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/help.py
+++ /dev/null
@@ -1,119 +0,0 @@
-"""Module containing bug report helper(s)."""
-from __future__ import print_function
-
-import json
-import platform
-import sys
-import ssl
-
-from pip._vendor import idna
-from pip._vendor import urllib3
-from pip._vendor import chardet
-
-from . import __version__ as requests_version
-
-try:
-    from pip._vendor.urllib3.contrib import pyopenssl
-except ImportError:
-    pyopenssl = None
-    OpenSSL = None
-    cryptography = None
-else:
-    import OpenSSL
-    import cryptography
-
-
-def _implementation():
-    """Return a dict with the Python implementation and version.
-
-    Provide both the name and the version of the Python implementation
-    currently running. For example, on CPython 2.7.5 it will return
-    {'name': 'CPython', 'version': '2.7.5'}.
-
-    This function works best on CPython and PyPy: in particular, it probably
-    doesn't work for Jython or IronPython. Future investigation should be done
-    to work out the correct shape of the code for those platforms.
-    """
-    implementation = platform.python_implementation()
-
-    if implementation == 'CPython':
-        implementation_version = platform.python_version()
-    elif implementation == 'PyPy':
-        implementation_version = '%s.%s.%s' % (sys.pypy_version_info.major,
-                                               sys.pypy_version_info.minor,
-                                               sys.pypy_version_info.micro)
-        if sys.pypy_version_info.releaselevel != 'final':
-            implementation_version = ''.join([
-                implementation_version, sys.pypy_version_info.releaselevel
-            ])
-    elif implementation == 'Jython':
-        implementation_version = platform.python_version()  # Complete Guess
-    elif implementation == 'IronPython':
-        implementation_version = platform.python_version()  # Complete Guess
-    else:
-        implementation_version = 'Unknown'
-
-    return {'name': implementation, 'version': implementation_version}
-
-
-def info():
-    """Generate information for a bug report."""
-    try:
-        platform_info = {
-            'system': platform.system(),
-            'release': platform.release(),
-        }
-    except IOError:
-        platform_info = {
-            'system': 'Unknown',
-            'release': 'Unknown',
-        }
-
-    implementation_info = _implementation()
-    urllib3_info = {'version': urllib3.__version__}
-    chardet_info = {'version': chardet.__version__}
-
-    pyopenssl_info = {
-        'version': None,
-        'openssl_version': '',
-    }
-    if OpenSSL:
-        pyopenssl_info = {
-            'version': OpenSSL.__version__,
-            'openssl_version': '%x' % OpenSSL.SSL.OPENSSL_VERSION_NUMBER,
-        }
-    cryptography_info = {
-        'version': getattr(cryptography, '__version__', ''),
-    }
-    idna_info = {
-        'version': getattr(idna, '__version__', ''),
-    }
-
-    system_ssl = ssl.OPENSSL_VERSION_NUMBER
-    system_ssl_info = {
-        'version': '%x' % system_ssl if system_ssl is not None else ''
-    }
-
-    return {
-        'platform': platform_info,
-        'implementation': implementation_info,
-        'system_ssl': system_ssl_info,
-        'using_pyopenssl': pyopenssl is not None,
-        'pyOpenSSL': pyopenssl_info,
-        'urllib3': urllib3_info,
-        'chardet': chardet_info,
-        'cryptography': cryptography_info,
-        'idna': idna_info,
-        'requests': {
-            'version': requests_version,
-        },
-    }
-
-
-def main():
-    """Pretty-print the bug information as JSON."""
-    print(json.dumps(info(), sort_keys=True, indent=2))
-
-
-if __name__ == '__main__':
-    main()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/hooks.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/hooks.py
deleted file mode 100644
index 7a51f21..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/hooks.py
+++ /dev/null
@@ -1,34 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.hooks
-~~~~~~~~~~~~~~
-
-This module provides the capabilities for the Requests hooks system.
-
-Available hooks:
-
-``response``:
-    The response generated from a Request.
-"""
-HOOKS = ['response']
-
-
-def default_hooks():
-    return {event: [] for event in HOOKS}
-
-# TODO: response is the only one
-
-
-def dispatch_hook(key, hooks, hook_data, **kwargs):
-    """Dispatches a hook dictionary on a given piece of data."""
-    hooks = hooks or {}
-    hooks = hooks.get(key)
-    if hooks:
-        if hasattr(hooks, '__call__'):
-            hooks = [hooks]
-        for hook in hooks:
-            _hook_data = hook(hook_data, **kwargs)
-            if _hook_data is not None:
-                hook_data = _hook_data
-    return hook_data
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/models.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/models.py
deleted file mode 100644
index 0839957..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/models.py
+++ /dev/null
@@ -1,953 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.models
-~~~~~~~~~~~~~~~
-
-This module contains the primary objects that power Requests.
-"""
-
-import datetime
-import sys
-
-# Import encoding now, to avoid implicit import later.
-# Implicit import within threads may cause LookupError when standard library is in a ZIP,
-# such as in Embedded Python. See https://github.com/requests/requests/issues/3578.
-import encodings.idna
-
-from pip._vendor.urllib3.fields import RequestField
-from pip._vendor.urllib3.filepost import encode_multipart_formdata
-from pip._vendor.urllib3.util import parse_url
-from pip._vendor.urllib3.exceptions import (
-    DecodeError, ReadTimeoutError, ProtocolError, LocationParseError)
-
-from io import UnsupportedOperation
-from .hooks import default_hooks
-from .structures import CaseInsensitiveDict
-
-from .auth import HTTPBasicAuth
-from .cookies import cookiejar_from_dict, get_cookie_header, _copy_cookie_jar
-from .exceptions import (
-    HTTPError, MissingSchema, InvalidURL, ChunkedEncodingError,
-    ContentDecodingError, ConnectionError, StreamConsumedError)
-from ._internal_utils import to_native_string, unicode_is_ascii
-from .utils import (
-    guess_filename, get_auth_from_url, requote_uri,
-    stream_decode_response_unicode, to_key_val_list, parse_header_links,
-    iter_slices, guess_json_utf, super_len, check_header_validity)
-from .compat import (
-    Callable, Mapping,
-    cookielib, urlunparse, urlsplit, urlencode, str, bytes,
-    is_py2, chardet, builtin_str, basestring)
-from .compat import json as complexjson
-from .status_codes import codes
-
-#: The set of HTTP status codes that indicate an automatically
-#: processable redirect.
-REDIRECT_STATI = (
-    codes.moved,               # 301
-    codes.found,               # 302
-    codes.other,               # 303
-    codes.temporary_redirect,  # 307
-    codes.permanent_redirect,  # 308
-)
-
-DEFAULT_REDIRECT_LIMIT = 30
-CONTENT_CHUNK_SIZE = 10 * 1024
-ITER_CHUNK_SIZE = 512
-
-
-class RequestEncodingMixin(object):
-    @property
-    def path_url(self):
-        """Build the path URL to use."""
-
-        url = []
-
-        p = urlsplit(self.url)
-
-        path = p.path
-        if not path:
-            path = '/'
-
-        url.append(path)
-
-        query = p.query
-        if query:
-            url.append('?')
-            url.append(query)
-
-        return ''.join(url)
-
-    @staticmethod
-    def _encode_params(data):
-        """Encode parameters in a piece of data.
-
-        Will successfully encode parameters when passed as a dict or a list of
-        2-tuples. Order is retained if data is a list of 2-tuples but arbitrary
-        if parameters are supplied as a dict.
-        """
-
-        if isinstance(data, (str, bytes)):
-            return data
-        elif hasattr(data, 'read'):
-            return data
-        elif hasattr(data, '__iter__'):
-            result = []
-            for k, vs in to_key_val_list(data):
-                if isinstance(vs, basestring) or not hasattr(vs, '__iter__'):
-                    vs = [vs]
-                for v in vs:
-                    if v is not None:
-                        result.append(
-                            (k.encode('utf-8') if isinstance(k, str) else k,
-                             v.encode('utf-8') if isinstance(v, str) else v))
-            return urlencode(result, doseq=True)
-        else:
-            return data
-
-    @staticmethod
-    def _encode_files(files, data):
-        """Build the body for a multipart/form-data request.
-
-        Will successfully encode files when passed as a dict or a list of
-        tuples. Order is retained if data is a list of tuples but arbitrary
-        if parameters are supplied as a dict.
-        The tuples may be 2-tuples (filename, fileobj), 3-tuples (filename, fileobj, contentype)
-        or 4-tuples (filename, fileobj, contentype, custom_headers).
-        """
-        if (not files):
-            raise ValueError("Files must be provided.")
-        elif isinstance(data, basestring):
-            raise ValueError("Data must not be a string.")
-
-        new_fields = []
-        fields = to_key_val_list(data or {})
-        files = to_key_val_list(files or {})
-
-        for field, val in fields:
-            if isinstance(val, basestring) or not hasattr(val, '__iter__'):
-                val = [val]
-            for v in val:
-                if v is not None:
-                    # Don't call str() on bytestrings: in Py3 it all goes wrong.
-                    if not isinstance(v, bytes):
-                        v = str(v)
-
-                    new_fields.append(
-                        (field.decode('utf-8') if isinstance(field, bytes) else field,
-                         v.encode('utf-8') if isinstance(v, str) else v))
-
-        for (k, v) in files:
-            # support for explicit filename
-            ft = None
-            fh = None
-            if isinstance(v, (tuple, list)):
-                if len(v) == 2:
-                    fn, fp = v
-                elif len(v) == 3:
-                    fn, fp, ft = v
-                else:
-                    fn, fp, ft, fh = v
-            else:
-                fn = guess_filename(v) or k
-                fp = v
-
-            if isinstance(fp, (str, bytes, bytearray)):
-                fdata = fp
-            elif hasattr(fp, 'read'):
-                fdata = fp.read()
-            elif fp is None:
-                continue
-            else:
-                fdata = fp
-
-            rf = RequestField(name=k, data=fdata, filename=fn, headers=fh)
-            rf.make_multipart(content_type=ft)
-            new_fields.append(rf)
-
-        body, content_type = encode_multipart_formdata(new_fields)
-
-        return body, content_type
-
-
-class RequestHooksMixin(object):
-    def register_hook(self, event, hook):
-        """Properly register a hook."""
-
-        if event not in self.hooks:
-            raise ValueError('Unsupported event specified, with event name "%s"' % (event))
-
-        if isinstance(hook, Callable):
-            self.hooks[event].append(hook)
-        elif hasattr(hook, '__iter__'):
-            self.hooks[event].extend(h for h in hook if isinstance(h, Callable))
-
-    def deregister_hook(self, event, hook):
-        """Deregister a previously registered hook.
-        Returns True if the hook existed, False if not.
-        """
-
-        try:
-            self.hooks[event].remove(hook)
-            return True
-        except ValueError:
-            return False
-
-
-class Request(RequestHooksMixin):
-    """A user-created :class:`Request <Request>` object.
-
-    Used to prepare a :class:`PreparedRequest <PreparedRequest>`, which is sent to the server.
-
-    :param method: HTTP method to use.
-    :param url: URL to send.
-    :param headers: dictionary of headers to send.
-    :param files: dictionary of {filename: fileobject} files to multipart upload.
-    :param data: the body to attach to the request. If a dictionary or
-        list of tuples ``[(key, value)]`` is provided, form-encoding will
-        take place.
-    :param json: json for the body to attach to the request (if files or data is not specified).
-    :param params: URL parameters to append to the URL. If a dictionary or
-        list of tuples ``[(key, value)]`` is provided, form-encoding will
-        take place.
-    :param auth: Auth handler or (user, pass) tuple.
-    :param cookies: dictionary or CookieJar of cookies to attach to this request.
-    :param hooks: dictionary of callback hooks, for internal usage.
-
-    Usage::
-
-      >>> import requests
-      >>> req = requests.Request('GET', 'https://httpbin.org/get')
-      >>> req.prepare()
-      <PreparedRequest [GET]>
-    """
-
-    def __init__(self,
-            method=None, url=None, headers=None, files=None, data=None,
-            params=None, auth=None, cookies=None, hooks=None, json=None):
-
-        # Default empty dicts for dict params.
-        data = [] if data is None else data
-        files = [] if files is None else files
-        headers = {} if headers is None else headers
-        params = {} if params is None else params
-        hooks = {} if hooks is None else hooks
-
-        self.hooks = default_hooks()
-        for (k, v) in list(hooks.items()):
-            self.register_hook(event=k, hook=v)
-
-        self.method = method
-        self.url = url
-        self.headers = headers
-        self.files = files
-        self.data = data
-        self.json = json
-        self.params = params
-        self.auth = auth
-        self.cookies = cookies
-
-    def __repr__(self):
-        return '<Request [%s]>' % (self.method)
-
-    def prepare(self):
-        """Constructs a :class:`PreparedRequest <PreparedRequest>` for transmission and returns it."""
-        p = PreparedRequest()
-        p.prepare(
-            method=self.method,
-            url=self.url,
-            headers=self.headers,
-            files=self.files,
-            data=self.data,
-            json=self.json,
-            params=self.params,
-            auth=self.auth,
-            cookies=self.cookies,
-            hooks=self.hooks,
-        )
-        return p
-
-
-class PreparedRequest(RequestEncodingMixin, RequestHooksMixin):
-    """The fully mutable :class:`PreparedRequest <PreparedRequest>` object,
-    containing the exact bytes that will be sent to the server.
-
-    Generated from either a :class:`Request <Request>` object or manually.
-
-    Usage::
-
-      >>> import requests
-      >>> req = requests.Request('GET', 'https://httpbin.org/get')
-      >>> r = req.prepare()
-      <PreparedRequest [GET]>
-
-      >>> s = requests.Session()
-      >>> s.send(r)
-      <Response [200]>
-    """
-
-    def __init__(self):
-        #: HTTP verb to send to the server.
-        self.method = None
-        #: HTTP URL to send the request to.
-        self.url = None
-        #: dictionary of HTTP headers.
-        self.headers = None
-        # The `CookieJar` used to create the Cookie header will be stored here
-        # after prepare_cookies is called
-        self._cookies = None
-        #: request body to send to the server.
-        self.body = None
-        #: dictionary of callback hooks, for internal usage.
-        self.hooks = default_hooks()
-        #: integer denoting starting position of a readable file-like body.
-        self._body_position = None
-
-    def prepare(self,
-            method=None, url=None, headers=None, files=None, data=None,
-            params=None, auth=None, cookies=None, hooks=None, json=None):
-        """Prepares the entire request with the given parameters."""
-
-        self.prepare_method(method)
-        self.prepare_url(url, params)
-        self.prepare_headers(headers)
-        self.prepare_cookies(cookies)
-        self.prepare_body(data, files, json)
-        self.prepare_auth(auth, url)
-
-        # Note that prepare_auth must be last to enable authentication schemes
-        # such as OAuth to work on a fully prepared request.
-
-        # This MUST go after prepare_auth. Authenticators could add a hook
-        self.prepare_hooks(hooks)
-
-    def __repr__(self):
-        return '<PreparedRequest [%s]>' % (self.method)
-
-    def copy(self):
-        p = PreparedRequest()
-        p.method = self.method
-        p.url = self.url
-        p.headers = self.headers.copy() if self.headers is not None else None
-        p._cookies = _copy_cookie_jar(self._cookies)
-        p.body = self.body
-        p.hooks = self.hooks
-        p._body_position = self._body_position
-        return p
-
-    def prepare_method(self, method):
-        """Prepares the given HTTP method."""
-        self.method = method
-        if self.method is not None:
-            self.method = to_native_string(self.method.upper())
-
-    @staticmethod
-    def _get_idna_encoded_host(host):
-        from pip._vendor import idna
-
-        try:
-            host = idna.encode(host, uts46=True).decode('utf-8')
-        except idna.IDNAError:
-            raise UnicodeError
-        return host
-
-    def prepare_url(self, url, params):
-        """Prepares the given HTTP URL."""
-        #: Accept objects that have string representations.
-        #: We're unable to blindly call unicode/str functions
-        #: as this will include the bytestring indicator (b'')
-        #: on python 3.x.
-        #: https://github.com/requests/requests/pull/2238
-        if isinstance(url, bytes):
-            url = url.decode('utf8')
-        else:
-            url = unicode(url) if is_py2 else str(url)
-
-        # Remove leading whitespaces from url
-        url = url.lstrip()
-
-        # Don't do any URL preparation for non-HTTP schemes like `mailto`,
-        # `data` etc to work around exceptions from `url_parse`, which
-        # handles RFC 3986 only.
-        if ':' in url and not url.lower().startswith('http'):
-            self.url = url
-            return
-
-        # Support for unicode domain names and paths.
-        try:
-            scheme, auth, host, port, path, query, fragment = parse_url(url)
-        except LocationParseError as e:
-            raise InvalidURL(*e.args)
-
-        if not scheme:
-            error = ("Invalid URL {0!r}: No schema supplied. Perhaps you meant http://{0}?")
-            error = error.format(to_native_string(url, 'utf8'))
-
-            raise MissingSchema(error)
-
-        if not host:
-            raise InvalidURL("Invalid URL %r: No host supplied" % url)
-
-        # In general, we want to try IDNA encoding the hostname if the string contains
-        # non-ASCII characters. This allows users to automatically get the correct IDNA
-        # behaviour. For strings containing only ASCII characters, we need to also verify
-        # it doesn't start with a wildcard (*), before allowing the unencoded hostname.
-        if not unicode_is_ascii(host):
-            try:
-                host = self._get_idna_encoded_host(host)
-            except UnicodeError:
-                raise InvalidURL('URL has an invalid label.')
-        elif host.startswith(u'*'):
-            raise InvalidURL('URL has an invalid label.')
-
-        # Carefully reconstruct the network location
-        netloc = auth or ''
-        if netloc:
-            netloc += '@'
-        netloc += host
-        if port:
-            netloc += ':' + str(port)
-
-        # Bare domains aren't valid URLs.
-        if not path:
-            path = '/'
-
-        if is_py2:
-            if isinstance(scheme, str):
-                scheme = scheme.encode('utf-8')
-            if isinstance(netloc, str):
-                netloc = netloc.encode('utf-8')
-            if isinstance(path, str):
-                path = path.encode('utf-8')
-            if isinstance(query, str):
-                query = query.encode('utf-8')
-            if isinstance(fragment, str):
-                fragment = fragment.encode('utf-8')
-
-        if isinstance(params, (str, bytes)):
-            params = to_native_string(params)
-
-        enc_params = self._encode_params(params)
-        if enc_params:
-            if query:
-                query = '%s&%s' % (query, enc_params)
-            else:
-                query = enc_params
-
-        url = requote_uri(urlunparse([scheme, netloc, path, None, query, fragment]))
-        self.url = url
-
-    def prepare_headers(self, headers):
-        """Prepares the given HTTP headers."""
-
-        self.headers = CaseInsensitiveDict()
-        if headers:
-            for header in headers.items():
-                # Raise exception on invalid header value.
-                check_header_validity(header)
-                name, value = header
-                self.headers[to_native_string(name)] = value
-
-    def prepare_body(self, data, files, json=None):
-        """Prepares the given HTTP body data."""
-
-        # Check if file, fo, generator, iterator.
-        # If not, run through normal process.
-
-        # Nottin' on you.
-        body = None
-        content_type = None
-
-        if not data and json is not None:
-            # urllib3 requires a bytes-like body. Python 2's json.dumps
-            # provides this natively, but Python 3 gives a Unicode string.
-            content_type = 'application/json'
-            body = complexjson.dumps(json)
-            if not isinstance(body, bytes):
-                body = body.encode('utf-8')
-
-        is_stream = all([
-            hasattr(data, '__iter__'),
-            not isinstance(data, (basestring, list, tuple, Mapping))
-        ])
-
-        try:
-            length = super_len(data)
-        except (TypeError, AttributeError, UnsupportedOperation):
-            length = None
-
-        if is_stream:
-            body = data
-
-            if getattr(body, 'tell', None) is not None:
-                # Record the current file position before reading.
-                # This will allow us to rewind a file in the event
-                # of a redirect.
-                try:
-                    self._body_position = body.tell()
-                except (IOError, OSError):
-                    # This differentiates from None, allowing us to catch
-                    # a failed `tell()` later when trying to rewind the body
-                    self._body_position = object()
-
-            if files:
-                raise NotImplementedError('Streamed bodies and files are mutually exclusive.')
-
-            if length:
-                self.headers['Content-Length'] = builtin_str(length)
-            else:
-                self.headers['Transfer-Encoding'] = 'chunked'
-        else:
-            # Multi-part file uploads.
-            if files:
-                (body, content_type) = self._encode_files(files, data)
-            else:
-                if data:
-                    body = self._encode_params(data)
-                    if isinstance(data, basestring) or hasattr(data, 'read'):
-                        content_type = None
-                    else:
-                        content_type = 'application/x-www-form-urlencoded'
-
-            self.prepare_content_length(body)
-
-            # Add content-type if it wasn't explicitly provided.
-            if content_type and ('content-type' not in self.headers):
-                self.headers['Content-Type'] = content_type
-
-        self.body = body
-
-    def prepare_content_length(self, body):
-        """Prepare Content-Length header based on request method and body"""
-        if body is not None:
-            length = super_len(body)
-            if length:
-                # If length exists, set it. Otherwise, we fallback
-                # to Transfer-Encoding: chunked.
-                self.headers['Content-Length'] = builtin_str(length)
-        elif self.method not in ('GET', 'HEAD') and self.headers.get('Content-Length') is None:
-            # Set Content-Length to 0 for methods that can have a body
-            # but don't provide one. (i.e. not GET or HEAD)
-            self.headers['Content-Length'] = '0'
-
-    def prepare_auth(self, auth, url=''):
-        """Prepares the given HTTP auth data."""
-
-        # If no Auth is explicitly provided, extract it from the URL first.
-        if auth is None:
-            url_auth = get_auth_from_url(self.url)
-            auth = url_auth if any(url_auth) else None
-
-        if auth:
-            if isinstance(auth, tuple) and len(auth) == 2:
-                # special-case basic HTTP auth
-                auth = HTTPBasicAuth(*auth)
-
-            # Allow auth to make its changes.
-            r = auth(self)
-
-            # Update self to reflect the auth changes.
-            self.__dict__.update(r.__dict__)
-
-            # Recompute Content-Length
-            self.prepare_content_length(self.body)
-
-    def prepare_cookies(self, cookies):
-        """Prepares the given HTTP cookie data.
-
-        This function eventually generates a ``Cookie`` header from the
-        given cookies using cookielib. Due to cookielib's design, the header
-        will not be regenerated if it already exists, meaning this function
-        can only be called once for the life of the
-        :class:`PreparedRequest <PreparedRequest>` object. Any subsequent calls
-        to ``prepare_cookies`` will have no actual effect, unless the "Cookie"
-        header is removed beforehand.
-        """
-        if isinstance(cookies, cookielib.CookieJar):
-            self._cookies = cookies
-        else:
-            self._cookies = cookiejar_from_dict(cookies)
-
-        cookie_header = get_cookie_header(self._cookies, self)
-        if cookie_header is not None:
-            self.headers['Cookie'] = cookie_header
-
-    def prepare_hooks(self, hooks):
-        """Prepares the given hooks."""
-        # hooks can be passed as None to the prepare method and to this
-        # method. To prevent iterating over None, simply use an empty list
-        # if hooks is False-y
-        hooks = hooks or []
-        for event in hooks:
-            self.register_hook(event, hooks[event])
-
-
-class Response(object):
-    """The :class:`Response <Response>` object, which contains a
-    server's response to an HTTP request.
-    """
-
-    __attrs__ = [
-        '_content', 'status_code', 'headers', 'url', 'history',
-        'encoding', 'reason', 'cookies', 'elapsed', 'request'
-    ]
-
-    def __init__(self):
-        self._content = False
-        self._content_consumed = False
-        self._next = None
-
-        #: Integer Code of responded HTTP Status, e.g. 404 or 200.
-        self.status_code = None
-
-        #: Case-insensitive Dictionary of Response Headers.
-        #: For example, ``headers['content-encoding']`` will return the
-        #: value of a ``'Content-Encoding'`` response header.
-        self.headers = CaseInsensitiveDict()
-
-        #: File-like object representation of response (for advanced usage).
-        #: Use of ``raw`` requires that ``stream=True`` be set on the request.
-        # This requirement does not apply for use internally to Requests.
-        self.raw = None
-
-        #: Final URL location of Response.
-        self.url = None
-
-        #: Encoding to decode with when accessing r.text.
-        self.encoding = None
-
-        #: A list of :class:`Response <Response>` objects from
-        #: the history of the Request. Any redirect responses will end
-        #: up here. The list is sorted from the oldest to the most recent request.
-        self.history = []
-
-        #: Textual reason of responded HTTP Status, e.g. "Not Found" or "OK".
-        self.reason = None
-
-        #: A CookieJar of Cookies the server sent back.
-        self.cookies = cookiejar_from_dict({})
-
-        #: The amount of time elapsed between sending the request
-        #: and the arrival of the response (as a timedelta).
-        #: This property specifically measures the time taken between sending
-        #: the first byte of the request and finishing parsing the headers. It
-        #: is therefore unaffected by consuming the response content or the
-        #: value of the ``stream`` keyword argument.
-        self.elapsed = datetime.timedelta(0)
-
-        #: The :class:`PreparedRequest <PreparedRequest>` object to which this
-        #: is a response.
-        self.request = None
-
-    def __enter__(self):
-        return self
-
-    def __exit__(self, *args):
-        self.close()
-
-    def __getstate__(self):
-        # Consume everything; accessing the content attribute makes
-        # sure the content has been fully read.
-        if not self._content_consumed:
-            self.content
-
-        return {attr: getattr(self, attr, None) for attr in self.__attrs__}
-
-    def __setstate__(self, state):
-        for name, value in state.items():
-            setattr(self, name, value)
-
-        # pickled objects do not have .raw
-        setattr(self, '_content_consumed', True)
-        setattr(self, 'raw', None)
-
-    def __repr__(self):
-        return '<Response [%s]>' % (self.status_code)
-
-    def __bool__(self):
-        """Returns True if :attr:`status_code` is less than 400.
-
-        This attribute checks if the status code of the response is between
-        400 and 600 to see if there was a client error or a server error. If
-        the status code, is between 200 and 400, this will return True. This
-        is **not** a check to see if the response code is ``200 OK``.
-        """
-        return self.ok
-
-    def __nonzero__(self):
-        """Returns True if :attr:`status_code` is less than 400.
-
-        This attribute checks if the status code of the response is between
-        400 and 600 to see if there was a client error or a server error. If
-        the status code, is between 200 and 400, this will return True. This
-        is **not** a check to see if the response code is ``200 OK``.
-        """
-        return self.ok
-
-    def __iter__(self):
-        """Allows you to use a response as an iterator."""
-        return self.iter_content(128)
-
-    @property
-    def ok(self):
-        """Returns True if :attr:`status_code` is less than 400, False if not.
-
-        This attribute checks if the status code of the response is between
-        400 and 600 to see if there was a client error or a server error. If
-        the status code is between 200 and 400, this will return True. This
-        is **not** a check to see if the response code is ``200 OK``.
-        """
-        try:
-            self.raise_for_status()
-        except HTTPError:
-            return False
-        return True
-
-    @property
-    def is_redirect(self):
-        """True if this Response is a well-formed HTTP redirect that could have
-        been processed automatically (by :meth:`Session.resolve_redirects`).
-        """
-        return ('location' in self.headers and self.status_code in REDIRECT_STATI)
-
-    @property
-    def is_permanent_redirect(self):
-        """True if this Response one of the permanent versions of redirect."""
-        return ('location' in self.headers and self.status_code in (codes.moved_permanently, codes.permanent_redirect))
-
-    @property
-    def next(self):
-        """Returns a PreparedRequest for the next request in a redirect chain, if there is one."""
-        return self._next
-
-    @property
-    def apparent_encoding(self):
-        """The apparent encoding, provided by the chardet library."""
-        return chardet.detect(self.content)['encoding']
-
-    def iter_content(self, chunk_size=1, decode_unicode=False):
-        """Iterates over the response data.  When stream=True is set on the
-        request, this avoids reading the content at once into memory for
-        large responses.  The chunk size is the number of bytes it should
-        read into memory.  This is not necessarily the length of each item
-        returned as decoding can take place.
-
-        chunk_size must be of type int or None. A value of None will
-        function differently depending on the value of `stream`.
-        stream=True will read data as it arrives in whatever size the
-        chunks are received. If stream=False, data is returned as
-        a single chunk.
-
-        If decode_unicode is True, content will be decoded using the best
-        available encoding based on the response.
-        """
-
-        def generate():
-            # Special case for urllib3.
-            if hasattr(self.raw, 'stream'):
-                try:
-                    for chunk in self.raw.stream(chunk_size, decode_content=True):
-                        yield chunk
-                except ProtocolError as e:
-                    raise ChunkedEncodingError(e)
-                except DecodeError as e:
-                    raise ContentDecodingError(e)
-                except ReadTimeoutError as e:
-                    raise ConnectionError(e)
-            else:
-                # Standard file-like object.
-                while True:
-                    chunk = self.raw.read(chunk_size)
-                    if not chunk:
-                        break
-                    yield chunk
-
-            self._content_consumed = True
-
-        if self._content_consumed and isinstance(self._content, bool):
-            raise StreamConsumedError()
-        elif chunk_size is not None and not isinstance(chunk_size, int):
-            raise TypeError("chunk_size must be an int, it is instead a %s." % type(chunk_size))
-        # simulate reading small chunks of the content
-        reused_chunks = iter_slices(self._content, chunk_size)
-
-        stream_chunks = generate()
-
-        chunks = reused_chunks if self._content_consumed else stream_chunks
-
-        if decode_unicode:
-            chunks = stream_decode_response_unicode(chunks, self)
-
-        return chunks
-
-    def iter_lines(self, chunk_size=ITER_CHUNK_SIZE, decode_unicode=False, delimiter=None):
-        """Iterates over the response data, one line at a time.  When
-        stream=True is set on the request, this avoids reading the
-        content at once into memory for large responses.
-
-        .. note:: This method is not reentrant safe.
-        """
-
-        pending = None
-
-        for chunk in self.iter_content(chunk_size=chunk_size, decode_unicode=decode_unicode):
-
-            if pending is not None:
-                chunk = pending + chunk
-
-            if delimiter:
-                lines = chunk.split(delimiter)
-            else:
-                lines = chunk.splitlines()
-
-            if lines and lines[-1] and chunk and lines[-1][-1] == chunk[-1]:
-                pending = lines.pop()
-            else:
-                pending = None
-
-            for line in lines:
-                yield line
-
-        if pending is not None:
-            yield pending
-
-    @property
-    def content(self):
-        """Content of the response, in bytes."""
-
-        if self._content is False:
-            # Read the contents.
-            if self._content_consumed:
-                raise RuntimeError(
-                    'The content for this response was already consumed')
-
-            if self.status_code == 0 or self.raw is None:
-                self._content = None
-            else:
-                self._content = b''.join(self.iter_content(CONTENT_CHUNK_SIZE)) or b''
-
-        self._content_consumed = True
-        # don't need to release the connection; that's been handled by urllib3
-        # since we exhausted the data.
-        return self._content
-
-    @property
-    def text(self):
-        """Content of the response, in unicode.
-
-        If Response.encoding is None, encoding will be guessed using
-        ``chardet``.
-
-        The encoding of the response content is determined based solely on HTTP
-        headers, following RFC 2616 to the letter. If you can take advantage of
-        non-HTTP knowledge to make a better guess at the encoding, you should
-        set ``r.encoding`` appropriately before accessing this property.
-        """
-
-        # Try charset from content-type
-        content = None
-        encoding = self.encoding
-
-        if not self.content:
-            return str('')
-
-        # Fallback to auto-detected encoding.
-        if self.encoding is None:
-            encoding = self.apparent_encoding
-
-        # Decode unicode from given encoding.
-        try:
-            content = str(self.content, encoding, errors='replace')
-        except (LookupError, TypeError):
-            # A LookupError is raised if the encoding was not found which could
-            # indicate a misspelling or similar mistake.
-            #
-            # A TypeError can be raised if encoding is None
-            #
-            # So we try blindly encoding.
-            content = str(self.content, errors='replace')
-
-        return content
-
-    def json(self, **kwargs):
-        r"""Returns the json-encoded content of a response, if any.
-
-        :param \*\*kwargs: Optional arguments that ``json.loads`` takes.
-        :raises ValueError: If the response body does not contain valid json.
-        """
-
-        if not self.encoding and self.content and len(self.content) > 3:
-            # No encoding set. JSON RFC 4627 section 3 states we should expect
-            # UTF-8, -16 or -32. Detect which one to use; If the detection or
-            # decoding fails, fall back to `self.text` (using chardet to make
-            # a best guess).
-            encoding = guess_json_utf(self.content)
-            if encoding is not None:
-                try:
-                    return complexjson.loads(
-                        self.content.decode(encoding), **kwargs
-                    )
-                except UnicodeDecodeError:
-                    # Wrong UTF codec detected; usually because it's not UTF-8
-                    # but some other 8-bit codec.  This is an RFC violation,
-                    # and the server didn't bother to tell us what codec *was*
-                    # used.
-                    pass
-        return complexjson.loads(self.text, **kwargs)
-
-    @property
-    def links(self):
-        """Returns the parsed header links of the response, if any."""
-
-        header = self.headers.get('link')
-
-        # l = MultiDict()
-        l = {}
-
-        if header:
-            links = parse_header_links(header)
-
-            for link in links:
-                key = link.get('rel') or link.get('url')
-                l[key] = link
-
-        return l
-
-    def raise_for_status(self):
-        """Raises stored :class:`HTTPError`, if one occurred."""
-
-        http_error_msg = ''
-        if isinstance(self.reason, bytes):
-            # We attempt to decode utf-8 first because some servers
-            # choose to localize their reason strings. If the string
-            # isn't utf-8, we fall back to iso-8859-1 for all other
-            # encodings. (See PR #3538)
-            try:
-                reason = self.reason.decode('utf-8')
-            except UnicodeDecodeError:
-                reason = self.reason.decode('iso-8859-1')
-        else:
-            reason = self.reason
-
-        if 400 <= self.status_code < 500:
-            http_error_msg = u'%s Client Error: %s for url: %s' % (self.status_code, reason, self.url)
-
-        elif 500 <= self.status_code < 600:
-            http_error_msg = u'%s Server Error: %s for url: %s' % (self.status_code, reason, self.url)
-
-        if http_error_msg:
-            raise HTTPError(http_error_msg, response=self)
-
-    def close(self):
-        """Releases the connection back to the pool. Once this method has been
-        called the underlying ``raw`` object must not be accessed again.
-
-        *Note: Should not normally need to be called explicitly.*
-        """
-        if not self._content_consumed:
-            self.raw.close()
-
-        release_conn = getattr(self.raw, 'release_conn', None)
-        if release_conn is not None:
-            release_conn()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/packages.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/packages.py
deleted file mode 100644
index 9582fa7..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/packages.py
+++ /dev/null
@@ -1,16 +0,0 @@
-import sys
-
-# This code exists for backwards compatibility reasons.
-# I don't like it either. Just look the other way. :)
-
-for package in ('urllib3', 'idna', 'chardet'):
-    vendored_package = "pip._vendor." + package
-    locals()[package] = __import__(vendored_package)
-    # This traversal is apparently necessary such that the identities are
-    # preserved (requests.packages.urllib3.* is urllib3.*)
-    for mod in list(sys.modules):
-        if mod == vendored_package or mod.startswith(vendored_package + '.'):
-            unprefixed_mod = mod[len("pip._vendor."):]
-            sys.modules['pip._vendor.requests.packages.' + unprefixed_mod] = sys.modules[mod]
-
-# Kinda cool, though, right?
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/sessions.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/sessions.py
deleted file mode 100644
index d73d700..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/sessions.py
+++ /dev/null
@@ -1,770 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.session
-~~~~~~~~~~~~~~~~
-
-This module provides a Session object to manage and persist settings across
-requests (cookies, auth, proxies).
-"""
-import os
-import sys
-import time
-from datetime import timedelta
-
-from .auth import _basic_auth_str
-from .compat import cookielib, is_py3, OrderedDict, urljoin, urlparse, Mapping
-from .cookies import (
-    cookiejar_from_dict, extract_cookies_to_jar, RequestsCookieJar, merge_cookies)
-from .models import Request, PreparedRequest, DEFAULT_REDIRECT_LIMIT
-from .hooks import default_hooks, dispatch_hook
-from ._internal_utils import to_native_string
-from .utils import to_key_val_list, default_headers, DEFAULT_PORTS
-from .exceptions import (
-    TooManyRedirects, InvalidSchema, ChunkedEncodingError, ContentDecodingError)
-
-from .structures import CaseInsensitiveDict
-from .adapters import HTTPAdapter
-
-from .utils import (
-    requote_uri, get_environ_proxies, get_netrc_auth, should_bypass_proxies,
-    get_auth_from_url, rewind_body
-)
-
-from .status_codes import codes
-
-# formerly defined here, reexposed here for backward compatibility
-from .models import REDIRECT_STATI
-
-# Preferred clock, based on which one is more accurate on a given system.
-if sys.platform == 'win32':
-    try:  # Python 3.4+
-        preferred_clock = time.perf_counter
-    except AttributeError:  # Earlier than Python 3.
-        preferred_clock = time.clock
-else:
-    preferred_clock = time.time
-
-
-def merge_setting(request_setting, session_setting, dict_class=OrderedDict):
-    """Determines appropriate setting for a given request, taking into account
-    the explicit setting on that request, and the setting in the session. If a
-    setting is a dictionary, they will be merged together using `dict_class`
-    """
-
-    if session_setting is None:
-        return request_setting
-
-    if request_setting is None:
-        return session_setting
-
-    # Bypass if not a dictionary (e.g. verify)
-    if not (
-            isinstance(session_setting, Mapping) and
-            isinstance(request_setting, Mapping)
-    ):
-        return request_setting
-
-    merged_setting = dict_class(to_key_val_list(session_setting))
-    merged_setting.update(to_key_val_list(request_setting))
-
-    # Remove keys that are set to None. Extract keys first to avoid altering
-    # the dictionary during iteration.
-    none_keys = [k for (k, v) in merged_setting.items() if v is None]
-    for key in none_keys:
-        del merged_setting[key]
-
-    return merged_setting
-
-
-def merge_hooks(request_hooks, session_hooks, dict_class=OrderedDict):
-    """Properly merges both requests and session hooks.
-
-    This is necessary because when request_hooks == {'response': []}, the
-    merge breaks Session hooks entirely.
-    """
-    if session_hooks is None or session_hooks.get('response') == []:
-        return request_hooks
-
-    if request_hooks is None or request_hooks.get('response') == []:
-        return session_hooks
-
-    return merge_setting(request_hooks, session_hooks, dict_class)
-
-
-class SessionRedirectMixin(object):
-
-    def get_redirect_target(self, resp):
-        """Receives a Response. Returns a redirect URI or ``None``"""
-        # Due to the nature of how requests processes redirects this method will
-        # be called at least once upon the original response and at least twice
-        # on each subsequent redirect response (if any).
-        # If a custom mixin is used to handle this logic, it may be advantageous
-        # to cache the redirect location onto the response object as a private
-        # attribute.
-        if resp.is_redirect:
-            location = resp.headers['location']
-            # Currently the underlying http module on py3 decode headers
-            # in latin1, but empirical evidence suggests that latin1 is very
-            # rarely used with non-ASCII characters in HTTP headers.
-            # It is more likely to get UTF8 header rather than latin1.
-            # This causes incorrect handling of UTF8 encoded location headers.
-            # To solve this, we re-encode the location in latin1.
-            if is_py3:
-                location = location.encode('latin1')
-            return to_native_string(location, 'utf8')
-        return None
-
-    def should_strip_auth(self, old_url, new_url):
-        """Decide whether Authorization header should be removed when redirecting"""
-        old_parsed = urlparse(old_url)
-        new_parsed = urlparse(new_url)
-        if old_parsed.hostname != new_parsed.hostname:
-            return True
-        # Special case: allow http -> https redirect when using the standard
-        # ports. This isn't specified by RFC 7235, but is kept to avoid
-        # breaking backwards compatibility with older versions of requests
-        # that allowed any redirects on the same host.
-        if (old_parsed.scheme == 'http' and old_parsed.port in (80, None)
-                and new_parsed.scheme == 'https' and new_parsed.port in (443, None)):
-            return False
-
-        # Handle default port usage corresponding to scheme.
-        changed_port = old_parsed.port != new_parsed.port
-        changed_scheme = old_parsed.scheme != new_parsed.scheme
-        default_port = (DEFAULT_PORTS.get(old_parsed.scheme, None), None)
-        if (not changed_scheme and old_parsed.port in default_port
-                and new_parsed.port in default_port):
-            return False
-
-        # Standard case: root URI must match
-        return changed_port or changed_scheme
-
-    def resolve_redirects(self, resp, req, stream=False, timeout=None,
-                          verify=True, cert=None, proxies=None, yield_requests=False, **adapter_kwargs):
-        """Receives a Response. Returns a generator of Responses or Requests."""
-
-        hist = []  # keep track of history
-
-        url = self.get_redirect_target(resp)
-        previous_fragment = urlparse(req.url).fragment
-        while url:
-            prepared_request = req.copy()
-
-            # Update history and keep track of redirects.
-            # resp.history must ignore the original request in this loop
-            hist.append(resp)
-            resp.history = hist[1:]
-
-            try:
-                resp.content  # Consume socket so it can be released
-            except (ChunkedEncodingError, ContentDecodingError, RuntimeError):
-                resp.raw.read(decode_content=False)
-
-            if len(resp.history) >= self.max_redirects:
-                raise TooManyRedirects('Exceeded %s redirects.' % self.max_redirects, response=resp)
-
-            # Release the connection back into the pool.
-            resp.close()
-
-            # Handle redirection without scheme (see: RFC 1808 Section 4)
-            if url.startswith('//'):
-                parsed_rurl = urlparse(resp.url)
-                url = '%s:%s' % (to_native_string(parsed_rurl.scheme), url)
-
-            # Normalize url case and attach previous fragment if needed (RFC 7231 7.1.2)
-            parsed = urlparse(url)
-            if parsed.fragment == '' and previous_fragment:
-                parsed = parsed._replace(fragment=previous_fragment)
-            elif parsed.fragment:
-                previous_fragment = parsed.fragment
-            url = parsed.geturl()
-
-            # Facilitate relative 'location' headers, as allowed by RFC 7231.
-            # (e.g. '/path/to/resource' instead of 'http://domain.tld/path/to/resource')
-            # Compliant with RFC3986, we percent encode the url.
-            if not parsed.netloc:
-                url = urljoin(resp.url, requote_uri(url))
-            else:
-                url = requote_uri(url)
-
-            prepared_request.url = to_native_string(url)
-
-            self.rebuild_method(prepared_request, resp)
-
-            # https://github.com/requests/requests/issues/1084
-            if resp.status_code not in (codes.temporary_redirect, codes.permanent_redirect):
-                # https://github.com/requests/requests/issues/3490
-                purged_headers = ('Content-Length', 'Content-Type', 'Transfer-Encoding')
-                for header in purged_headers:
-                    prepared_request.headers.pop(header, None)
-                prepared_request.body = None
-
-            headers = prepared_request.headers
-            try:
-                del headers['Cookie']
-            except KeyError:
-                pass
-
-            # Extract any cookies sent on the response to the cookiejar
-            # in the new request. Because we've mutated our copied prepared
-            # request, use the old one that we haven't yet touched.
-            extract_cookies_to_jar(prepared_request._cookies, req, resp.raw)
-            merge_cookies(prepared_request._cookies, self.cookies)
-            prepared_request.prepare_cookies(prepared_request._cookies)
-
-            # Rebuild auth and proxy information.
-            proxies = self.rebuild_proxies(prepared_request, proxies)
-            self.rebuild_auth(prepared_request, resp)
-
-            # A failed tell() sets `_body_position` to `object()`. This non-None
-            # value ensures `rewindable` will be True, allowing us to raise an
-            # UnrewindableBodyError, instead of hanging the connection.
-            rewindable = (
-                prepared_request._body_position is not None and
-                ('Content-Length' in headers or 'Transfer-Encoding' in headers)
-            )
-
-            # Attempt to rewind consumed file-like object.
-            if rewindable:
-                rewind_body(prepared_request)
-
-            # Override the original request.
-            req = prepared_request
-
-            if yield_requests:
-                yield req
-            else:
-
-                resp = self.send(
-                    req,
-                    stream=stream,
-                    timeout=timeout,
-                    verify=verify,
-                    cert=cert,
-                    proxies=proxies,
-                    allow_redirects=False,
-                    **adapter_kwargs
-                )
-
-                extract_cookies_to_jar(self.cookies, prepared_request, resp.raw)
-
-                # extract redirect url, if any, for the next loop
-                url = self.get_redirect_target(resp)
-                yield resp
-
-    def rebuild_auth(self, prepared_request, response):
-        """When being redirected we may want to strip authentication from the
-        request to avoid leaking credentials. This method intelligently removes
-        and reapplies authentication where possible to avoid credential loss.
-        """
-        headers = prepared_request.headers
-        url = prepared_request.url
-
-        if 'Authorization' in headers and self.should_strip_auth(response.request.url, url):
-            # If we get redirected to a new host, we should strip out any
-            # authentication headers.
-            del headers['Authorization']
-
-        # .netrc might have more auth for us on our new host.
-        new_auth = get_netrc_auth(url) if self.trust_env else None
-        if new_auth is not None:
-            prepared_request.prepare_auth(new_auth)
-
-        return
-
-    def rebuild_proxies(self, prepared_request, proxies):
-        """This method re-evaluates the proxy configuration by considering the
-        environment variables. If we are redirected to a URL covered by
-        NO_PROXY, we strip the proxy configuration. Otherwise, we set missing
-        proxy keys for this URL (in case they were stripped by a previous
-        redirect).
-
-        This method also replaces the Proxy-Authorization header where
-        necessary.
-
-        :rtype: dict
-        """
-        proxies = proxies if proxies is not None else {}
-        headers = prepared_request.headers
-        url = prepared_request.url
-        scheme = urlparse(url).scheme
-        new_proxies = proxies.copy()
-        no_proxy = proxies.get('no_proxy')
-
-        bypass_proxy = should_bypass_proxies(url, no_proxy=no_proxy)
-        if self.trust_env and not bypass_proxy:
-            environ_proxies = get_environ_proxies(url, no_proxy=no_proxy)
-
-            proxy = environ_proxies.get(scheme, environ_proxies.get('all'))
-
-            if proxy:
-                new_proxies.setdefault(scheme, proxy)
-
-        if 'Proxy-Authorization' in headers:
-            del headers['Proxy-Authorization']
-
-        try:
-            username, password = get_auth_from_url(new_proxies[scheme])
-        except KeyError:
-            username, password = None, None
-
-        if username and password:
-            headers['Proxy-Authorization'] = _basic_auth_str(username, password)
-
-        return new_proxies
-
-    def rebuild_method(self, prepared_request, response):
-        """When being redirected we may want to change the method of the request
-        based on certain specs or browser behavior.
-        """
-        method = prepared_request.method
-
-        # https://tools.ietf.org/html/rfc7231#section-6.4.4
-        if response.status_code == codes.see_other and method != 'HEAD':
-            method = 'GET'
-
-        # Do what the browsers do, despite standards...
-        # First, turn 302s into GETs.
-        if response.status_code == codes.found and method != 'HEAD':
-            method = 'GET'
-
-        # Second, if a POST is responded to with a 301, turn it into a GET.
-        # This bizarre behaviour is explained in Issue 1704.
-        if response.status_code == codes.moved and method == 'POST':
-            method = 'GET'
-
-        prepared_request.method = method
-
-
-class Session(SessionRedirectMixin):
-    """A Requests session.
-
-    Provides cookie persistence, connection-pooling, and configuration.
-
-    Basic Usage::
-
-      >>> import requests
-      >>> s = requests.Session()
-      >>> s.get('https://httpbin.org/get')
-      <Response [200]>
-
-    Or as a context manager::
-
-      >>> with requests.Session() as s:
-      >>>     s.get('https://httpbin.org/get')
-      <Response [200]>
-    """
-
-    __attrs__ = [
-        'headers', 'cookies', 'auth', 'proxies', 'hooks', 'params', 'verify',
-        'cert', 'prefetch', 'adapters', 'stream', 'trust_env',
-        'max_redirects',
-    ]
-
-    def __init__(self):
-
-        #: A case-insensitive dictionary of headers to be sent on each
-        #: :class:`Request <Request>` sent from this
-        #: :class:`Session <Session>`.
-        self.headers = default_headers()
-
-        #: Default Authentication tuple or object to attach to
-        #: :class:`Request <Request>`.
-        self.auth = None
-
-        #: Dictionary mapping protocol or protocol and host to the URL of the proxy
-        #: (e.g. {'http': 'foo.bar:3128', 'http://host.name': 'foo.bar:4012'}) to
-        #: be used on each :class:`Request <Request>`.
-        self.proxies = {}
-
-        #: Event-handling hooks.
-        self.hooks = default_hooks()
-
-        #: Dictionary of querystring data to attach to each
-        #: :class:`Request <Request>`. The dictionary values may be lists for
-        #: representing multivalued query parameters.
-        self.params = {}
-
-        #: Stream response content default.
-        self.stream = False
-
-        #: SSL Verification default.
-        self.verify = True
-
-        #: SSL client certificate default, if String, path to ssl client
-        #: cert file (.pem). If Tuple, ('cert', 'key') pair.
-        self.cert = None
-
-        #: Maximum number of redirects allowed. If the request exceeds this
-        #: limit, a :class:`TooManyRedirects` exception is raised.
-        #: This defaults to requests.models.DEFAULT_REDIRECT_LIMIT, which is
-        #: 30.
-        self.max_redirects = DEFAULT_REDIRECT_LIMIT
-
-        #: Trust environment settings for proxy configuration, default
-        #: authentication and similar.
-        self.trust_env = True
-
-        #: A CookieJar containing all currently outstanding cookies set on this
-        #: session. By default it is a
-        #: :class:`RequestsCookieJar <requests.cookies.RequestsCookieJar>`, but
-        #: may be any other ``cookielib.CookieJar`` compatible object.
-        self.cookies = cookiejar_from_dict({})
-
-        # Default connection adapters.
-        self.adapters = OrderedDict()
-        self.mount('https://', HTTPAdapter())
-        self.mount('http://', HTTPAdapter())
-
-    def __enter__(self):
-        return self
-
-    def __exit__(self, *args):
-        self.close()
-
-    def prepare_request(self, request):
-        """Constructs a :class:`PreparedRequest <PreparedRequest>` for
-        transmission and returns it. The :class:`PreparedRequest` has settings
-        merged from the :class:`Request <Request>` instance and those of the
-        :class:`Session`.
-
-        :param request: :class:`Request` instance to prepare with this
-            session's settings.
-        :rtype: requests.PreparedRequest
-        """
-        cookies = request.cookies or {}
-
-        # Bootstrap CookieJar.
-        if not isinstance(cookies, cookielib.CookieJar):
-            cookies = cookiejar_from_dict(cookies)
-
-        # Merge with session cookies
-        merged_cookies = merge_cookies(
-            merge_cookies(RequestsCookieJar(), self.cookies), cookies)
-
-        # Set environment's basic authentication if not explicitly set.
-        auth = request.auth
-        if self.trust_env and not auth and not self.auth:
-            auth = get_netrc_auth(request.url)
-
-        p = PreparedRequest()
-        p.prepare(
-            method=request.method.upper(),
-            url=request.url,
-            files=request.files,
-            data=request.data,
-            json=request.json,
-            headers=merge_setting(request.headers, self.headers, dict_class=CaseInsensitiveDict),
-            params=merge_setting(request.params, self.params),
-            auth=merge_setting(auth, self.auth),
-            cookies=merged_cookies,
-            hooks=merge_hooks(request.hooks, self.hooks),
-        )
-        return p
-
-    def request(self, method, url,
-            params=None, data=None, headers=None, cookies=None, files=None,
-            auth=None, timeout=None, allow_redirects=True, proxies=None,
-            hooks=None, stream=None, verify=None, cert=None, json=None):
-        """Constructs a :class:`Request <Request>`, prepares it and sends it.
-        Returns :class:`Response <Response>` object.
-
-        :param method: method for the new :class:`Request` object.
-        :param url: URL for the new :class:`Request` object.
-        :param params: (optional) Dictionary or bytes to be sent in the query
-            string for the :class:`Request`.
-        :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-            object to send in the body of the :class:`Request`.
-        :param json: (optional) json to send in the body of the
-            :class:`Request`.
-        :param headers: (optional) Dictionary of HTTP Headers to send with the
-            :class:`Request`.
-        :param cookies: (optional) Dict or CookieJar object to send with the
-            :class:`Request`.
-        :param files: (optional) Dictionary of ``'filename': file-like-objects``
-            for multipart encoding upload.
-        :param auth: (optional) Auth tuple or callable to enable
-            Basic/Digest/Custom HTTP Auth.
-        :param timeout: (optional) How long to wait for the server to send
-            data before giving up, as a float, or a :ref:`(connect timeout,
-            read timeout) <timeouts>` tuple.
-        :type timeout: float or tuple
-        :param allow_redirects: (optional) Set to True by default.
-        :type allow_redirects: bool
-        :param proxies: (optional) Dictionary mapping protocol or protocol and
-            hostname to the URL of the proxy.
-        :param stream: (optional) whether to immediately download the response
-            content. Defaults to ``False``.
-        :param verify: (optional) Either a boolean, in which case it controls whether we verify
-            the server's TLS certificate, or a string, in which case it must be a path
-            to a CA bundle to use. Defaults to ``True``.
-        :param cert: (optional) if String, path to ssl client cert file (.pem).
-            If Tuple, ('cert', 'key') pair.
-        :rtype: requests.Response
-        """
-        # Create the Request.
-        req = Request(
-            method=method.upper(),
-            url=url,
-            headers=headers,
-            files=files,
-            data=data or {},
-            json=json,
-            params=params or {},
-            auth=auth,
-            cookies=cookies,
-            hooks=hooks,
-        )
-        prep = self.prepare_request(req)
-
-        proxies = proxies or {}
-
-        settings = self.merge_environment_settings(
-            prep.url, proxies, stream, verify, cert
-        )
-
-        # Send the request.
-        send_kwargs = {
-            'timeout': timeout,
-            'allow_redirects': allow_redirects,
-        }
-        send_kwargs.update(settings)
-        resp = self.send(prep, **send_kwargs)
-
-        return resp
-
-    def get(self, url, **kwargs):
-        r"""Sends a GET request. Returns :class:`Response` object.
-
-        :param url: URL for the new :class:`Request` object.
-        :param \*\*kwargs: Optional arguments that ``request`` takes.
-        :rtype: requests.Response
-        """
-
-        kwargs.setdefault('allow_redirects', True)
-        return self.request('GET', url, **kwargs)
-
-    def options(self, url, **kwargs):
-        r"""Sends a OPTIONS request. Returns :class:`Response` object.
-
-        :param url: URL for the new :class:`Request` object.
-        :param \*\*kwargs: Optional arguments that ``request`` takes.
-        :rtype: requests.Response
-        """
-
-        kwargs.setdefault('allow_redirects', True)
-        return self.request('OPTIONS', url, **kwargs)
-
-    def head(self, url, **kwargs):
-        r"""Sends a HEAD request. Returns :class:`Response` object.
-
-        :param url: URL for the new :class:`Request` object.
-        :param \*\*kwargs: Optional arguments that ``request`` takes.
-        :rtype: requests.Response
-        """
-
-        kwargs.setdefault('allow_redirects', False)
-        return self.request('HEAD', url, **kwargs)
-
-    def post(self, url, data=None, json=None, **kwargs):
-        r"""Sends a POST request. Returns :class:`Response` object.
-
-        :param url: URL for the new :class:`Request` object.
-        :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-            object to send in the body of the :class:`Request`.
-        :param json: (optional) json to send in the body of the :class:`Request`.
-        :param \*\*kwargs: Optional arguments that ``request`` takes.
-        :rtype: requests.Response
-        """
-
-        return self.request('POST', url, data=data, json=json, **kwargs)
-
-    def put(self, url, data=None, **kwargs):
-        r"""Sends a PUT request. Returns :class:`Response` object.
-
-        :param url: URL for the new :class:`Request` object.
-        :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-            object to send in the body of the :class:`Request`.
-        :param \*\*kwargs: Optional arguments that ``request`` takes.
-        :rtype: requests.Response
-        """
-
-        return self.request('PUT', url, data=data, **kwargs)
-
-    def patch(self, url, data=None, **kwargs):
-        r"""Sends a PATCH request. Returns :class:`Response` object.
-
-        :param url: URL for the new :class:`Request` object.
-        :param data: (optional) Dictionary, list of tuples, bytes, or file-like
-            object to send in the body of the :class:`Request`.
-        :param \*\*kwargs: Optional arguments that ``request`` takes.
-        :rtype: requests.Response
-        """
-
-        return self.request('PATCH', url, data=data, **kwargs)
-
-    def delete(self, url, **kwargs):
-        r"""Sends a DELETE request. Returns :class:`Response` object.
-
-        :param url: URL for the new :class:`Request` object.
-        :param \*\*kwargs: Optional arguments that ``request`` takes.
-        :rtype: requests.Response
-        """
-
-        return self.request('DELETE', url, **kwargs)
-
-    def send(self, request, **kwargs):
-        """Send a given PreparedRequest.
-
-        :rtype: requests.Response
-        """
-        # Set defaults that the hooks can utilize to ensure they always have
-        # the correct parameters to reproduce the previous request.
-        kwargs.setdefault('stream', self.stream)
-        kwargs.setdefault('verify', self.verify)
-        kwargs.setdefault('cert', self.cert)
-        kwargs.setdefault('proxies', self.proxies)
-
-        # It's possible that users might accidentally send a Request object.
-        # Guard against that specific failure case.
-        if isinstance(request, Request):
-            raise ValueError('You can only send PreparedRequests.')
-
-        # Set up variables needed for resolve_redirects and dispatching of hooks
-        allow_redirects = kwargs.pop('allow_redirects', True)
-        stream = kwargs.get('stream')
-        hooks = request.hooks
-
-        # Get the appropriate adapter to use
-        adapter = self.get_adapter(url=request.url)
-
-        # Start time (approximately) of the request
-        start = preferred_clock()
-
-        # Send the request
-        r = adapter.send(request, **kwargs)
-
-        # Total elapsed time of the request (approximately)
-        elapsed = preferred_clock() - start
-        r.elapsed = timedelta(seconds=elapsed)
-
-        # Response manipulation hooks
-        r = dispatch_hook('response', hooks, r, **kwargs)
-
-        # Persist cookies
-        if r.history:
-
-            # If the hooks create history then we want those cookies too
-            for resp in r.history:
-                extract_cookies_to_jar(self.cookies, resp.request, resp.raw)
-
-        extract_cookies_to_jar(self.cookies, request, r.raw)
-
-        # Redirect resolving generator.
-        gen = self.resolve_redirects(r, request, **kwargs)
-
-        # Resolve redirects if allowed.
-        history = [resp for resp in gen] if allow_redirects else []
-
-        # Shuffle things around if there's history.
-        if history:
-            # Insert the first (original) request at the start
-            history.insert(0, r)
-            # Get the last request made
-            r = history.pop()
-            r.history = history
-
-        # If redirects aren't being followed, store the response on the Request for Response.next().
-        if not allow_redirects:
-            try:
-                r._next = next(self.resolve_redirects(r, request, yield_requests=True, **kwargs))
-            except StopIteration:
-                pass
-
-        if not stream:
-            r.content
-
-        return r
-
-    def merge_environment_settings(self, url, proxies, stream, verify, cert):
-        """
-        Check the environment and merge it with some settings.
-
-        :rtype: dict
-        """
-        # Gather clues from the surrounding environment.
-        if self.trust_env:
-            # Set environment's proxies.
-            no_proxy = proxies.get('no_proxy') if proxies is not None else None
-            env_proxies = get_environ_proxies(url, no_proxy=no_proxy)
-            for (k, v) in env_proxies.items():
-                proxies.setdefault(k, v)
-
-            # Look for requests environment configuration and be compatible
-            # with cURL.
-            if verify is True or verify is None:
-                verify = (os.environ.get('REQUESTS_CA_BUNDLE') or
-                          os.environ.get('CURL_CA_BUNDLE'))
-
-        # Merge all the kwargs.
-        proxies = merge_setting(proxies, self.proxies)
-        stream = merge_setting(stream, self.stream)
-        verify = merge_setting(verify, self.verify)
-        cert = merge_setting(cert, self.cert)
-
-        return {'verify': verify, 'proxies': proxies, 'stream': stream,
-                'cert': cert}
-
-    def get_adapter(self, url):
-        """
-        Returns the appropriate connection adapter for the given URL.
-
-        :rtype: requests.adapters.BaseAdapter
-        """
-        for (prefix, adapter) in self.adapters.items():
-
-            if url.lower().startswith(prefix.lower()):
-                return adapter
-
-        # Nothing matches :-/
-        raise InvalidSchema("No connection adapters were found for '%s'" % url)
-
-    def close(self):
-        """Closes all adapters and as such the session"""
-        for v in self.adapters.values():
-            v.close()
-
-    def mount(self, prefix, adapter):
-        """Registers a connection adapter to a prefix.
-
-        Adapters are sorted in descending order by prefix length.
-        """
-        self.adapters[prefix] = adapter
-        keys_to_move = [k for k in self.adapters if len(k) < len(prefix)]
-
-        for key in keys_to_move:
-            self.adapters[key] = self.adapters.pop(key)
-
-    def __getstate__(self):
-        state = {attr: getattr(self, attr, None) for attr in self.__attrs__}
-        return state
-
-    def __setstate__(self, state):
-        for attr, value in state.items():
-            setattr(self, attr, value)
-
-
-def session():
-    """
-    Returns a :class:`Session` for context-management.
-
-    .. deprecated:: 1.0.0
-
-        This method has been deprecated since version 1.0.0 and is only kept for
-        backwards compatibility. New code should use :class:`~requests.sessions.Session`
-        to create a session. This may be removed at a future date.
-
-    :rtype: Session
-    """
-    return Session()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/status_codes.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/status_codes.py
deleted file mode 100644
index 813e8c4..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/status_codes.py
+++ /dev/null
@@ -1,120 +0,0 @@
-# -*- coding: utf-8 -*-
-
-r"""
-The ``codes`` object defines a mapping from common names for HTTP statuses
-to their numerical codes, accessible either as attributes or as dictionary
-items.
-
->>> requests.codes['temporary_redirect']
-307
->>> requests.codes.teapot
-418
->>> requests.codes['\o/']
-200
-
-Some codes have multiple names, and both upper- and lower-case versions of
-the names are allowed. For example, ``codes.ok``, ``codes.OK``, and
-``codes.okay`` all correspond to the HTTP status code 200.
-"""
-
-from .structures import LookupDict
-
-_codes = {
-
-    # Informational.
-    100: ('continue',),
-    101: ('switching_protocols',),
-    102: ('processing',),
-    103: ('checkpoint',),
-    122: ('uri_too_long', 'request_uri_too_long'),
-    200: ('ok', 'okay', 'all_ok', 'all_okay', 'all_good', '\\o/', '✓'),
-    201: ('created',),
-    202: ('accepted',),
-    203: ('non_authoritative_info', 'non_authoritative_information'),
-    204: ('no_content',),
-    205: ('reset_content', 'reset'),
-    206: ('partial_content', 'partial'),
-    207: ('multi_status', 'multiple_status', 'multi_stati', 'multiple_stati'),
-    208: ('already_reported',),
-    226: ('im_used',),
-
-    # Redirection.
-    300: ('multiple_choices',),
-    301: ('moved_permanently', 'moved', '\\o-'),
-    302: ('found',),
-    303: ('see_other', 'other'),
-    304: ('not_modified',),
-    305: ('use_proxy',),
-    306: ('switch_proxy',),
-    307: ('temporary_redirect', 'temporary_moved', 'temporary'),
-    308: ('permanent_redirect',
-          'resume_incomplete', 'resume',),  # These 2 to be removed in 3.0
-
-    # Client Error.
-    400: ('bad_request', 'bad'),
-    401: ('unauthorized',),
-    402: ('payment_required', 'payment'),
-    403: ('forbidden',),
-    404: ('not_found', '-o-'),
-    405: ('method_not_allowed', 'not_allowed'),
-    406: ('not_acceptable',),
-    407: ('proxy_authentication_required', 'proxy_auth', 'proxy_authentication'),
-    408: ('request_timeout', 'timeout'),
-    409: ('conflict',),
-    410: ('gone',),
-    411: ('length_required',),
-    412: ('precondition_failed', 'precondition'),
-    413: ('request_entity_too_large',),
-    414: ('request_uri_too_large',),
-    415: ('unsupported_media_type', 'unsupported_media', 'media_type'),
-    416: ('requested_range_not_satisfiable', 'requested_range', 'range_not_satisfiable'),
-    417: ('expectation_failed',),
-    418: ('im_a_teapot', 'teapot', 'i_am_a_teapot'),
-    421: ('misdirected_request',),
-    422: ('unprocessable_entity', 'unprocessable'),
-    423: ('locked',),
-    424: ('failed_dependency', 'dependency'),
-    425: ('unordered_collection', 'unordered'),
-    426: ('upgrade_required', 'upgrade'),
-    428: ('precondition_required', 'precondition'),
-    429: ('too_many_requests', 'too_many'),
-    431: ('header_fields_too_large', 'fields_too_large'),
-    444: ('no_response', 'none'),
-    449: ('retry_with', 'retry'),
-    450: ('blocked_by_windows_parental_controls', 'parental_controls'),
-    451: ('unavailable_for_legal_reasons', 'legal_reasons'),
-    499: ('client_closed_request',),
-
-    # Server Error.
-    500: ('internal_server_error', 'server_error', '/o\\', '✗'),
-    501: ('not_implemented',),
-    502: ('bad_gateway',),
-    503: ('service_unavailable', 'unavailable'),
-    504: ('gateway_timeout',),
-    505: ('http_version_not_supported', 'http_version'),
-    506: ('variant_also_negotiates',),
-    507: ('insufficient_storage',),
-    509: ('bandwidth_limit_exceeded', 'bandwidth'),
-    510: ('not_extended',),
-    511: ('network_authentication_required', 'network_auth', 'network_authentication'),
-}
-
-codes = LookupDict(name='status_codes')
-
-def _init():
-    for code, titles in _codes.items():
-        for title in titles:
-            setattr(codes, title, code)
-            if not title.startswith(('\\', '/')):
-                setattr(codes, title.upper(), code)
-
-    def doc(code):
-        names = ', '.join('``%s``' % n for n in _codes[code])
-        return '* %d: %s' % (code, names)
-
-    global __doc__
-    __doc__ = (__doc__ + '\n' +
-               '\n'.join(doc(code) for code in sorted(_codes))
-               if __doc__ is not None else None)
-
-_init()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/structures.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/structures.py
deleted file mode 100644
index da930e2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/structures.py
+++ /dev/null
@@ -1,103 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.structures
-~~~~~~~~~~~~~~~~~~~
-
-Data structures that power Requests.
-"""
-
-from .compat import OrderedDict, Mapping, MutableMapping
-
-
-class CaseInsensitiveDict(MutableMapping):
-    """A case-insensitive ``dict``-like object.
-
-    Implements all methods and operations of
-    ``MutableMapping`` as well as dict's ``copy``. Also
-    provides ``lower_items``.
-
-    All keys are expected to be strings. The structure remembers the
-    case of the last key to be set, and ``iter(instance)``,
-    ``keys()``, ``items()``, ``iterkeys()``, and ``iteritems()``
-    will contain case-sensitive keys. However, querying and contains
-    testing is case insensitive::
-
-        cid = CaseInsensitiveDict()
-        cid['Accept'] = 'application/json'
-        cid['aCCEPT'] == 'application/json'  # True
-        list(cid) == ['Accept']  # True
-
-    For example, ``headers['content-encoding']`` will return the
-    value of a ``'Content-Encoding'`` response header, regardless
-    of how the header name was originally stored.
-
-    If the constructor, ``.update``, or equality comparison
-    operations are given keys that have equal ``.lower()``s, the
-    behavior is undefined.
-    """
-
-    def __init__(self, data=None, **kwargs):
-        self._store = OrderedDict()
-        if data is None:
-            data = {}
-        self.update(data, **kwargs)
-
-    def __setitem__(self, key, value):
-        # Use the lowercased key for lookups, but store the actual
-        # key alongside the value.
-        self._store[key.lower()] = (key, value)
-
-    def __getitem__(self, key):
-        return self._store[key.lower()][1]
-
-    def __delitem__(self, key):
-        del self._store[key.lower()]
-
-    def __iter__(self):
-        return (casedkey for casedkey, mappedvalue in self._store.values())
-
-    def __len__(self):
-        return len(self._store)
-
-    def lower_items(self):
-        """Like iteritems(), but with all lowercase keys."""
-        return (
-            (lowerkey, keyval[1])
-            for (lowerkey, keyval)
-            in self._store.items()
-        )
-
-    def __eq__(self, other):
-        if isinstance(other, Mapping):
-            other = CaseInsensitiveDict(other)
-        else:
-            return NotImplemented
-        # Compare insensitively
-        return dict(self.lower_items()) == dict(other.lower_items())
-
-    # Copy is required
-    def copy(self):
-        return CaseInsensitiveDict(self._store.values())
-
-    def __repr__(self):
-        return str(dict(self.items()))
-
-
-class LookupDict(dict):
-    """Dictionary lookup object."""
-
-    def __init__(self, name=None):
-        self.name = name
-        super(LookupDict, self).__init__()
-
-    def __repr__(self):
-        return '<lookup \'%s\'>' % (self.name)
-
-    def __getitem__(self, key):
-        # We allow fall-through here, so values default to None
-
-        return self.__dict__.get(key, None)
-
-    def get(self, key, default=None):
-        return self.__dict__.get(key, default)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/utils.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/utils.py
deleted file mode 100644
index 8170a8d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/requests/utils.py
+++ /dev/null
@@ -1,977 +0,0 @@
-# -*- coding: utf-8 -*-
-
-"""
-requests.utils
-~~~~~~~~~~~~~~
-
-This module provides utility functions that are used within Requests
-that are also useful for external consumption.
-"""
-
-import codecs
-import contextlib
-import io
-import os
-import re
-import socket
-import struct
-import sys
-import tempfile
-import warnings
-import zipfile
-
-from .__version__ import __version__
-from . import certs
-# to_native_string is unused here, but imported here for backwards compatibility
-from ._internal_utils import to_native_string
-from .compat import parse_http_list as _parse_list_header
-from .compat import (
-    quote, urlparse, bytes, str, OrderedDict, unquote, getproxies,
-    proxy_bypass, urlunparse, basestring, integer_types, is_py3,
-    proxy_bypass_environment, getproxies_environment, Mapping)
-from .cookies import cookiejar_from_dict
-from .structures import CaseInsensitiveDict
-from .exceptions import (
-    InvalidURL, InvalidHeader, FileModeWarning, UnrewindableBodyError)
-
-NETRC_FILES = ('.netrc', '_netrc')
-
-DEFAULT_CA_BUNDLE_PATH = certs.where()
-
-DEFAULT_PORTS = {'http': 80, 'https': 443}
-
-
-if sys.platform == 'win32':
-    # provide a proxy_bypass version on Windows without DNS lookups
-
-    def proxy_bypass_registry(host):
-        try:
-            if is_py3:
-                import winreg
-            else:
-                import _winreg as winreg
-        except ImportError:
-            return False
-
-        try:
-            internetSettings = winreg.OpenKey(winreg.HKEY_CURRENT_USER,
-                r'Software\Microsoft\Windows\CurrentVersion\Internet Settings')
-            # ProxyEnable could be REG_SZ or REG_DWORD, normalizing it
-            proxyEnable = int(winreg.QueryValueEx(internetSettings,
-                                              'ProxyEnable')[0])
-            # ProxyOverride is almost always a string
-            proxyOverride = winreg.QueryValueEx(internetSettings,
-                                                'ProxyOverride')[0]
-        except OSError:
-            return False
-        if not proxyEnable or not proxyOverride:
-            return False
-
-        # make a check value list from the registry entry: replace the
-        # '<local>' string by the localhost entry and the corresponding
-        # canonical entry.
-        proxyOverride = proxyOverride.split(';')
-        # now check if we match one of the registry values.
-        for test in proxyOverride:
-            if test == '<local>':
-                if '.' not in host:
-                    return True
-            test = test.replace(".", r"\.")     # mask dots
-            test = test.replace("*", r".*")     # change glob sequence
-            test = test.replace("?", r".")      # change glob char
-            if re.match(test, host, re.I):
-                return True
-        return False
-
-    def proxy_bypass(host):  # noqa
-        """Return True, if the host should be bypassed.
-
-        Checks proxy settings gathered from the environment, if specified,
-        or the registry.
-        """
-        if getproxies_environment():
-            return proxy_bypass_environment(host)
-        else:
-            return proxy_bypass_registry(host)
-
-
-def dict_to_sequence(d):
-    """Returns an internal sequence dictionary update."""
-
-    if hasattr(d, 'items'):
-        d = d.items()
-
-    return d
-
-
-def super_len(o):
-    total_length = None
-    current_position = 0
-
-    if hasattr(o, '__len__'):
-        total_length = len(o)
-
-    elif hasattr(o, 'len'):
-        total_length = o.len
-
-    elif hasattr(o, 'fileno'):
-        try:
-            fileno = o.fileno()
-        except io.UnsupportedOperation:
-            pass
-        else:
-            total_length = os.fstat(fileno).st_size
-
-            # Having used fstat to determine the file length, we need to
-            # confirm that this file was opened up in binary mode.
-            if 'b' not in o.mode:
-                warnings.warn((
-                    "Requests has determined the content-length for this "
-                    "request using the binary size of the file: however, the "
-                    "file has been opened in text mode (i.e. without the 'b' "
-                    "flag in the mode). This may lead to an incorrect "
-                    "content-length. In Requests 3.0, support will be removed "
-                    "for files in text mode."),
-                    FileModeWarning
-                )
-
-    if hasattr(o, 'tell'):
-        try:
-            current_position = o.tell()
-        except (OSError, IOError):
-            # This can happen in some weird situations, such as when the file
-            # is actually a special file descriptor like stdin. In this
-            # instance, we don't know what the length is, so set it to zero and
-            # let requests chunk it instead.
-            if total_length is not None:
-                current_position = total_length
-        else:
-            if hasattr(o, 'seek') and total_length is None:
-                # StringIO and BytesIO have seek but no useable fileno
-                try:
-                    # seek to end of file
-                    o.seek(0, 2)
-                    total_length = o.tell()
-
-                    # seek back to current position to support
-                    # partially read file-like objects
-                    o.seek(current_position or 0)
-                except (OSError, IOError):
-                    total_length = 0
-
-    if total_length is None:
-        total_length = 0
-
-    return max(0, total_length - current_position)
-
-
-def get_netrc_auth(url, raise_errors=False):
-    """Returns the Requests tuple auth for a given url from netrc."""
-
-    try:
-        from netrc import netrc, NetrcParseError
-
-        netrc_path = None
-
-        for f in NETRC_FILES:
-            try:
-                loc = os.path.expanduser('~/{}'.format(f))
-            except KeyError:
-                # os.path.expanduser can fail when $HOME is undefined and
-                # getpwuid fails. See https://bugs.python.org/issue20164 &
-                # https://github.com/requests/requests/issues/1846
-                return
-
-            if os.path.exists(loc):
-                netrc_path = loc
-                break
-
-        # Abort early if there isn't one.
-        if netrc_path is None:
-            return
-
-        ri = urlparse(url)
-
-        # Strip port numbers from netloc. This weird `if...encode`` dance is
-        # used for Python 3.2, which doesn't support unicode literals.
-        splitstr = b':'
-        if isinstance(url, str):
-            splitstr = splitstr.decode('ascii')
-        host = ri.netloc.split(splitstr)[0]
-
-        try:
-            _netrc = netrc(netrc_path).authenticators(host)
-            if _netrc:
-                # Return with login / password
-                login_i = (0 if _netrc[0] else 1)
-                return (_netrc[login_i], _netrc[2])
-        except (NetrcParseError, IOError):
-            # If there was a parsing error or a permissions issue reading the file,
-            # we'll just skip netrc auth unless explicitly asked to raise errors.
-            if raise_errors:
-                raise
-
-    # AppEngine hackiness.
-    except (ImportError, AttributeError):
-        pass
-
-
-def guess_filename(obj):
-    """Tries to guess the filename of the given object."""
-    name = getattr(obj, 'name', None)
-    if (name and isinstance(name, basestring) and name[0] != '<' and
-            name[-1] != '>'):
-        return os.path.basename(name)
-
-
-def extract_zipped_paths(path):
-    """Replace nonexistent paths that look like they refer to a member of a zip
-    archive with the location of an extracted copy of the target, or else
-    just return the provided path unchanged.
-    """
-    if os.path.exists(path):
-        # this is already a valid path, no need to do anything further
-        return path
-
-    # find the first valid part of the provided path and treat that as a zip archive
-    # assume the rest of the path is the name of a member in the archive
-    archive, member = os.path.split(path)
-    while archive and not os.path.exists(archive):
-        archive, prefix = os.path.split(archive)
-        member = '/'.join([prefix, member])
-
-    if not zipfile.is_zipfile(archive):
-        return path
-
-    zip_file = zipfile.ZipFile(archive)
-    if member not in zip_file.namelist():
-        return path
-
-    # we have a valid zip archive and a valid member of that archive
-    tmp = tempfile.gettempdir()
-    extracted_path = os.path.join(tmp, *member.split('/'))
-    if not os.path.exists(extracted_path):
-        extracted_path = zip_file.extract(member, path=tmp)
-
-    return extracted_path
-
-
-def from_key_val_list(value):
-    """Take an object and test to see if it can be represented as a
-    dictionary. Unless it can not be represented as such, return an
-    OrderedDict, e.g.,
-
-    ::
-
-        >>> from_key_val_list([('key', 'val')])
-        OrderedDict([('key', 'val')])
-        >>> from_key_val_list('string')
-        ValueError: cannot encode objects that are not 2-tuples
-        >>> from_key_val_list({'key': 'val'})
-        OrderedDict([('key', 'val')])
-
-    :rtype: OrderedDict
-    """
-    if value is None:
-        return None
-
-    if isinstance(value, (str, bytes, bool, int)):
-        raise ValueError('cannot encode objects that are not 2-tuples')
-
-    return OrderedDict(value)
-
-
-def to_key_val_list(value):
-    """Take an object and test to see if it can be represented as a
-    dictionary. If it can be, return a list of tuples, e.g.,
-
-    ::
-
-        >>> to_key_val_list([('key', 'val')])
-        [('key', 'val')]
-        >>> to_key_val_list({'key': 'val'})
-        [('key', 'val')]
-        >>> to_key_val_list('string')
-        ValueError: cannot encode objects that are not 2-tuples.
-
-    :rtype: list
-    """
-    if value is None:
-        return None
-
-    if isinstance(value, (str, bytes, bool, int)):
-        raise ValueError('cannot encode objects that are not 2-tuples')
-
-    if isinstance(value, Mapping):
-        value = value.items()
-
-    return list(value)
-
-
-# From mitsuhiko/werkzeug (used with permission).
-def parse_list_header(value):
-    """Parse lists as described by RFC 2068 Section 2.
-
-    In particular, parse comma-separated lists where the elements of
-    the list may include quoted-strings.  A quoted-string could
-    contain a comma.  A non-quoted string could have quotes in the
-    middle.  Quotes are removed automatically after parsing.
-
-    It basically works like :func:`parse_set_header` just that items
-    may appear multiple times and case sensitivity is preserved.
-
-    The return value is a standard :class:`list`:
-
-    >>> parse_list_header('token, "quoted value"')
-    ['token', 'quoted value']
-
-    To create a header from the :class:`list` again, use the
-    :func:`dump_header` function.
-
-    :param value: a string with a list header.
-    :return: :class:`list`
-    :rtype: list
-    """
-    result = []
-    for item in _parse_list_header(value):
-        if item[:1] == item[-1:] == '"':
-            item = unquote_header_value(item[1:-1])
-        result.append(item)
-    return result
-
-
-# From mitsuhiko/werkzeug (used with permission).
-def parse_dict_header(value):
-    """Parse lists of key, value pairs as described by RFC 2068 Section 2 and
-    convert them into a python dict:
-
-    >>> d = parse_dict_header('foo="is a fish", bar="as well"')
-    >>> type(d) is dict
-    True
-    >>> sorted(d.items())
-    [('bar', 'as well'), ('foo', 'is a fish')]
-
-    If there is no value for a key it will be `None`:
-
-    >>> parse_dict_header('key_without_value')
-    {'key_without_value': None}
-
-    To create a header from the :class:`dict` again, use the
-    :func:`dump_header` function.
-
-    :param value: a string with a dict header.
-    :return: :class:`dict`
-    :rtype: dict
-    """
-    result = {}
-    for item in _parse_list_header(value):
-        if '=' not in item:
-            result[item] = None
-            continue
-        name, value = item.split('=', 1)
-        if value[:1] == value[-1:] == '"':
-            value = unquote_header_value(value[1:-1])
-        result[name] = value
-    return result
-
-
-# From mitsuhiko/werkzeug (used with permission).
-def unquote_header_value(value, is_filename=False):
-    r"""Unquotes a header value.  (Reversal of :func:`quote_header_value`).
-    This does not use the real unquoting but what browsers are actually
-    using for quoting.
-
-    :param value: the header value to unquote.
-    :rtype: str
-    """
-    if value and value[0] == value[-1] == '"':
-        # this is not the real unquoting, but fixing this so that the
-        # RFC is met will result in bugs with internet explorer and
-        # probably some other browsers as well.  IE for example is
-        # uploading files with "C:\foo\bar.txt" as filename
-        value = value[1:-1]
-
-        # if this is a filename and the starting characters look like
-        # a UNC path, then just return the value without quotes.  Using the
-        # replace sequence below on a UNC path has the effect of turning
-        # the leading double slash into a single slash and then
-        # _fix_ie_filename() doesn't work correctly.  See #458.
-        if not is_filename or value[:2] != '\\\\':
-            return value.replace('\\\\', '\\').replace('\\"', '"')
-    return value
-
-
-def dict_from_cookiejar(cj):
-    """Returns a key/value dictionary from a CookieJar.
-
-    :param cj: CookieJar object to extract cookies from.
-    :rtype: dict
-    """
-
-    cookie_dict = {}
-
-    for cookie in cj:
-        cookie_dict[cookie.name] = cookie.value
-
-    return cookie_dict
-
-
-def add_dict_to_cookiejar(cj, cookie_dict):
-    """Returns a CookieJar from a key/value dictionary.
-
-    :param cj: CookieJar to insert cookies into.
-    :param cookie_dict: Dict of key/values to insert into CookieJar.
-    :rtype: CookieJar
-    """
-
-    return cookiejar_from_dict(cookie_dict, cj)
-
-
-def get_encodings_from_content(content):
-    """Returns encodings from given content string.
-
-    :param content: bytestring to extract encodings from.
-    """
-    warnings.warn((
-        'In requests 3.0, get_encodings_from_content will be removed. For '
-        'more information, please see the discussion on issue #2266. (This'
-        ' warning should only appear once.)'),
-        DeprecationWarning)
-
-    charset_re = re.compile(r'<meta.*?charset=["\']*(.+?)["\'>]', flags=re.I)
-    pragma_re = re.compile(r'<meta.*?content=["\']*;?charset=(.+?)["\'>]', flags=re.I)
-    xml_re = re.compile(r'^<\?xml.*?encoding=["\']*(.+?)["\'>]')
-
-    return (charset_re.findall(content) +
-            pragma_re.findall(content) +
-            xml_re.findall(content))
-
-
-def _parse_content_type_header(header):
-    """Returns content type and parameters from given header
-
-    :param header: string
-    :return: tuple containing content type and dictionary of
-         parameters
-    """
-
-    tokens = header.split(';')
-    content_type, params = tokens[0].strip(), tokens[1:]
-    params_dict = {}
-    items_to_strip = "\"' "
-
-    for param in params:
-        param = param.strip()
-        if param:
-            key, value = param, True
-            index_of_equals = param.find("=")
-            if index_of_equals != -1:
-                key = param[:index_of_equals].strip(items_to_strip)
-                value = param[index_of_equals + 1:].strip(items_to_strip)
-            params_dict[key.lower()] = value
-    return content_type, params_dict
-
-
-def get_encoding_from_headers(headers):
-    """Returns encodings from given HTTP Header Dict.
-
-    :param headers: dictionary to extract encoding from.
-    :rtype: str
-    """
-
-    content_type = headers.get('content-type')
-
-    if not content_type:
-        return None
-
-    content_type, params = _parse_content_type_header(content_type)
-
-    if 'charset' in params:
-        return params['charset'].strip("'\"")
-
-    if 'text' in content_type:
-        return 'ISO-8859-1'
-
-
-def stream_decode_response_unicode(iterator, r):
-    """Stream decodes a iterator."""
-
-    if r.encoding is None:
-        for item in iterator:
-            yield item
-        return
-
-    decoder = codecs.getincrementaldecoder(r.encoding)(errors='replace')
-    for chunk in iterator:
-        rv = decoder.decode(chunk)
-        if rv:
-            yield rv
-    rv = decoder.decode(b'', final=True)
-    if rv:
-        yield rv
-
-
-def iter_slices(string, slice_length):
-    """Iterate over slices of a string."""
-    pos = 0
-    if slice_length is None or slice_length <= 0:
-        slice_length = len(string)
-    while pos < len(string):
-        yield string[pos:pos + slice_length]
-        pos += slice_length
-
-
-def get_unicode_from_response(r):
-    """Returns the requested content back in unicode.
-
-    :param r: Response object to get unicode content from.
-
-    Tried:
-
-    1. charset from content-type
-    2. fall back and replace all unicode characters
-
-    :rtype: str
-    """
-    warnings.warn((
-        'In requests 3.0, get_unicode_from_response will be removed. For '
-        'more information, please see the discussion on issue #2266. (This'
-        ' warning should only appear once.)'),
-        DeprecationWarning)
-
-    tried_encodings = []
-
-    # Try charset from content-type
-    encoding = get_encoding_from_headers(r.headers)
-
-    if encoding:
-        try:
-            return str(r.content, encoding)
-        except UnicodeError:
-            tried_encodings.append(encoding)
-
-    # Fall back:
-    try:
-        return str(r.content, encoding, errors='replace')
-    except TypeError:
-        return r.content
-
-
-# The unreserved URI characters (RFC 3986)
-UNRESERVED_SET = frozenset(
-    "ABCDEFGHIJKLMNOPQRSTUVWXYZabcdefghijklmnopqrstuvwxyz" + "0123456789-._~")
-
-
-def unquote_unreserved(uri):
-    """Un-escape any percent-escape sequences in a URI that are unreserved
-    characters. This leaves all reserved, illegal and non-ASCII bytes encoded.
-
-    :rtype: str
-    """
-    parts = uri.split('%')
-    for i in range(1, len(parts)):
-        h = parts[i][0:2]
-        if len(h) == 2 and h.isalnum():
-            try:
-                c = chr(int(h, 16))
-            except ValueError:
-                raise InvalidURL("Invalid percent-escape sequence: '%s'" % h)
-
-            if c in UNRESERVED_SET:
-                parts[i] = c + parts[i][2:]
-            else:
-                parts[i] = '%' + parts[i]
-        else:
-            parts[i] = '%' + parts[i]
-    return ''.join(parts)
-
-
-def requote_uri(uri):
-    """Re-quote the given URI.
-
-    This function passes the given URI through an unquote/quote cycle to
-    ensure that it is fully and consistently quoted.
-
-    :rtype: str
-    """
-    safe_with_percent = "!#$%&'()*+,/:;=?@[]~"
-    safe_without_percent = "!#$&'()*+,/:;=?@[]~"
-    try:
-        # Unquote only the unreserved characters
-        # Then quote only illegal characters (do not quote reserved,
-        # unreserved, or '%')
-        return quote(unquote_unreserved(uri), safe=safe_with_percent)
-    except InvalidURL:
-        # We couldn't unquote the given URI, so let's try quoting it, but
-        # there may be unquoted '%'s in the URI. We need to make sure they're
-        # properly quoted so they do not cause issues elsewhere.
-        return quote(uri, safe=safe_without_percent)
-
-
-def address_in_network(ip, net):
-    """This function allows you to check if an IP belongs to a network subnet
-
-    Example: returns True if ip = 192.168.1.1 and net = 192.168.1.0/24
-             returns False if ip = 192.168.1.1 and net = 192.168.100.0/24
-
-    :rtype: bool
-    """
-    ipaddr = struct.unpack('=L', socket.inet_aton(ip))[0]
-    netaddr, bits = net.split('/')
-    netmask = struct.unpack('=L', socket.inet_aton(dotted_netmask(int(bits))))[0]
-    network = struct.unpack('=L', socket.inet_aton(netaddr))[0] & netmask
-    return (ipaddr & netmask) == (network & netmask)
-
-
-def dotted_netmask(mask):
-    """Converts mask from /xx format to xxx.xxx.xxx.xxx
-
-    Example: if mask is 24 function returns 255.255.255.0
-
-    :rtype: str
-    """
-    bits = 0xffffffff ^ (1 << 32 - mask) - 1
-    return socket.inet_ntoa(struct.pack('>I', bits))
-
-
-def is_ipv4_address(string_ip):
-    """
-    :rtype: bool
-    """
-    try:
-        socket.inet_aton(string_ip)
-    except socket.error:
-        return False
-    return True
-
-
-def is_valid_cidr(string_network):
-    """
-    Very simple check of the cidr format in no_proxy variable.
-
-    :rtype: bool
-    """
-    if string_network.count('/') == 1:
-        try:
-            mask = int(string_network.split('/')[1])
-        except ValueError:
-            return False
-
-        if mask < 1 or mask > 32:
-            return False
-
-        try:
-            socket.inet_aton(string_network.split('/')[0])
-        except socket.error:
-            return False
-    else:
-        return False
-    return True
-
-
-@contextlib.contextmanager
-def set_environ(env_name, value):
-    """Set the environment variable 'env_name' to 'value'
-
-    Save previous value, yield, and then restore the previous value stored in
-    the environment variable 'env_name'.
-
-    If 'value' is None, do nothing"""
-    value_changed = value is not None
-    if value_changed:
-        old_value = os.environ.get(env_name)
-        os.environ[env_name] = value
-    try:
-        yield
-    finally:
-        if value_changed:
-            if old_value is None:
-                del os.environ[env_name]
-            else:
-                os.environ[env_name] = old_value
-
-
-def should_bypass_proxies(url, no_proxy):
-    """
-    Returns whether we should bypass proxies or not.
-
-    :rtype: bool
-    """
-    # Prioritize lowercase environment variables over uppercase
-    # to keep a consistent behaviour with other http projects (curl, wget).
-    get_proxy = lambda k: os.environ.get(k) or os.environ.get(k.upper())
-
-    # First check whether no_proxy is defined. If it is, check that the URL
-    # we're getting isn't in the no_proxy list.
-    no_proxy_arg = no_proxy
-    if no_proxy is None:
-        no_proxy = get_proxy('no_proxy')
-    parsed = urlparse(url)
-
-    if parsed.hostname is None:
-        # URLs don't always have hostnames, e.g. file:/// urls.
-        return True
-
-    if no_proxy:
-        # We need to check whether we match here. We need to see if we match
-        # the end of the hostname, both with and without the port.
-        no_proxy = (
-            host for host in no_proxy.replace(' ', '').split(',') if host
-        )
-
-        if is_ipv4_address(parsed.hostname):
-            for proxy_ip in no_proxy:
-                if is_valid_cidr(proxy_ip):
-                    if address_in_network(parsed.hostname, proxy_ip):
-                        return True
-                elif parsed.hostname == proxy_ip:
-                    # If no_proxy ip was defined in plain IP notation instead of cidr notation &
-                    # matches the IP of the index
-                    return True
-        else:
-            host_with_port = parsed.hostname
-            if parsed.port:
-                host_with_port += ':{}'.format(parsed.port)
-
-            for host in no_proxy:
-                if parsed.hostname.endswith(host) or host_with_port.endswith(host):
-                    # The URL does match something in no_proxy, so we don't want
-                    # to apply the proxies on this URL.
-                    return True
-
-    with set_environ('no_proxy', no_proxy_arg):
-        # parsed.hostname can be `None` in cases such as a file URI.
-        try:
-            bypass = proxy_bypass(parsed.hostname)
-        except (TypeError, socket.gaierror):
-            bypass = False
-
-    if bypass:
-        return True
-
-    return False
-
-
-def get_environ_proxies(url, no_proxy=None):
-    """
-    Return a dict of environment proxies.
-
-    :rtype: dict
-    """
-    if should_bypass_proxies(url, no_proxy=no_proxy):
-        return {}
-    else:
-        return getproxies()
-
-
-def select_proxy(url, proxies):
-    """Select a proxy for the url, if applicable.
-
-    :param url: The url being for the request
-    :param proxies: A dictionary of schemes or schemes and hosts to proxy URLs
-    """
-    proxies = proxies or {}
-    urlparts = urlparse(url)
-    if urlparts.hostname is None:
-        return proxies.get(urlparts.scheme, proxies.get('all'))
-
-    proxy_keys = [
-        urlparts.scheme + '://' + urlparts.hostname,
-        urlparts.scheme,
-        'all://' + urlparts.hostname,
-        'all',
-    ]
-    proxy = None
-    for proxy_key in proxy_keys:
-        if proxy_key in proxies:
-            proxy = proxies[proxy_key]
-            break
-
-    return proxy
-
-
-def default_user_agent(name="python-requests"):
-    """
-    Return a string representing the default user agent.
-
-    :rtype: str
-    """
-    return '%s/%s' % (name, __version__)
-
-
-def default_headers():
-    """
-    :rtype: requests.structures.CaseInsensitiveDict
-    """
-    return CaseInsensitiveDict({
-        'User-Agent': default_user_agent(),
-        'Accept-Encoding': ', '.join(('gzip', 'deflate')),
-        'Accept': '*/*',
-        'Connection': 'keep-alive',
-    })
-
-
-def parse_header_links(value):
-    """Return a list of parsed link headers proxies.
-
-    i.e. Link: <http:/.../front.jpeg>; rel=front; type="image/jpeg",<http://.../back.jpeg>; rel=back;type="image/jpeg"
-
-    :rtype: list
-    """
-
-    links = []
-
-    replace_chars = ' \'"'
-
-    value = value.strip(replace_chars)
-    if not value:
-        return links
-
-    for val in re.split(', *<', value):
-        try:
-            url, params = val.split(';', 1)
-        except ValueError:
-            url, params = val, ''
-
-        link = {'url': url.strip('<> \'"')}
-
-        for param in params.split(';'):
-            try:
-                key, value = param.split('=')
-            except ValueError:
-                break
-
-            link[key.strip(replace_chars)] = value.strip(replace_chars)
-
-        links.append(link)
-
-    return links
-
-
-# Null bytes; no need to recreate these on each call to guess_json_utf
-_null = '\x00'.encode('ascii')  # encoding to ASCII for Python 3
-_null2 = _null * 2
-_null3 = _null * 3
-
-
-def guess_json_utf(data):
-    """
-    :rtype: str
-    """
-    # JSON always starts with two ASCII characters, so detection is as
-    # easy as counting the nulls and from their location and count
-    # determine the encoding. Also detect a BOM, if present.
-    sample = data[:4]
-    if sample in (codecs.BOM_UTF32_LE, codecs.BOM_UTF32_BE):
-        return 'utf-32'     # BOM included
-    if sample[:3] == codecs.BOM_UTF8:
-        return 'utf-8-sig'  # BOM included, MS style (discouraged)
-    if sample[:2] in (codecs.BOM_UTF16_LE, codecs.BOM_UTF16_BE):
-        return 'utf-16'     # BOM included
-    nullcount = sample.count(_null)
-    if nullcount == 0:
-        return 'utf-8'
-    if nullcount == 2:
-        if sample[::2] == _null2:   # 1st and 3rd are null
-            return 'utf-16-be'
-        if sample[1::2] == _null2:  # 2nd and 4th are null
-            return 'utf-16-le'
-        # Did not detect 2 valid UTF-16 ascii-range characters
-    if nullcount == 3:
-        if sample[:3] == _null3:
-            return 'utf-32-be'
-        if sample[1:] == _null3:
-            return 'utf-32-le'
-        # Did not detect a valid UTF-32 ascii-range character
-    return None
-
-
-def prepend_scheme_if_needed(url, new_scheme):
-    """Given a URL that may or may not have a scheme, prepend the given scheme.
-    Does not replace a present scheme with the one provided as an argument.
-
-    :rtype: str
-    """
-    scheme, netloc, path, params, query, fragment = urlparse(url, new_scheme)
-
-    # urlparse is a finicky beast, and sometimes decides that there isn't a
-    # netloc present. Assume that it's being over-cautious, and switch netloc
-    # and path if urlparse decided there was no netloc.
-    if not netloc:
-        netloc, path = path, netloc
-
-    return urlunparse((scheme, netloc, path, params, query, fragment))
-
-
-def get_auth_from_url(url):
-    """Given a url with authentication components, extract them into a tuple of
-    username,password.
-
-    :rtype: (str,str)
-    """
-    parsed = urlparse(url)
-
-    try:
-        auth = (unquote(parsed.username), unquote(parsed.password))
-    except (AttributeError, TypeError):
-        auth = ('', '')
-
-    return auth
-
-
-# Moved outside of function to avoid recompile every call
-_CLEAN_HEADER_REGEX_BYTE = re.compile(b'^\\S[^\\r\\n]*$|^$')
-_CLEAN_HEADER_REGEX_STR = re.compile(r'^\S[^\r\n]*$|^$')
-
-
-def check_header_validity(header):
-    """Verifies that header value is a string which doesn't contain
-    leading whitespace or return characters. This prevents unintended
-    header injection.
-
-    :param header: tuple, in the format (name, value).
-    """
-    name, value = header
-
-    if isinstance(value, bytes):
-        pat = _CLEAN_HEADER_REGEX_BYTE
-    else:
-        pat = _CLEAN_HEADER_REGEX_STR
-    try:
-        if not pat.match(value):
-            raise InvalidHeader("Invalid return character or leading space in header: %s" % name)
-    except TypeError:
-        raise InvalidHeader("Value for header {%s: %s} must be of type str or "
-                            "bytes, not %s" % (name, value, type(value)))
-
-
-def urldefragauth(url):
-    """
-    Given a url remove the fragment and the authentication part.
-
-    :rtype: str
-    """
-    scheme, netloc, path, params, query, fragment = urlparse(url)
-
-    # see func:`prepend_scheme_if_needed`
-    if not netloc:
-        netloc, path = path, netloc
-
-    netloc = netloc.rsplit('@', 1)[-1]
-
-    return urlunparse((scheme, netloc, path, params, query, ''))
-
-
-def rewind_body(prepared_request):
-    """Move file pointer back to its recorded starting position
-    so it can be read again on redirect.
-    """
-    body_seek = getattr(prepared_request.body, 'seek', None)
-    if body_seek is not None and isinstance(prepared_request._body_position, integer_types):
-        try:
-            body_seek(prepared_request._body_position)
-        except (IOError, OSError):
-            raise UnrewindableBodyError("An error occurred when rewinding request "
-                                        "body for redirect.")
-    else:
-        raise UnrewindableBodyError("Unable to rewind request body for redirect.")
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/retrying.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/retrying.py
deleted file mode 100644
index 6d1e627..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/retrying.py
+++ /dev/null
@@ -1,267 +0,0 @@
-## Copyright 2013-2014 Ray Holder
-##
-## Licensed under the Apache License, Version 2.0 (the "License");
-## you may not use this file except in compliance with the License.
-## You may obtain a copy of the License at
-##
-## http://www.apache.org/licenses/LICENSE-2.0
-##
-## Unless required by applicable law or agreed to in writing, software
-## distributed under the License is distributed on an "AS IS" BASIS,
-## WITHOUT WARRANTIES OR CONDITIONS OF ANY KIND, either express or implied.
-## See the License for the specific language governing permissions and
-## limitations under the License.
-
-import random
-from pip._vendor import six
-import sys
-import time
-import traceback
-
-
-# sys.maxint / 2, since Python 3.2 doesn't have a sys.maxint...
-MAX_WAIT = 1073741823
-
-
-def retry(*dargs, **dkw):
-    """
-    Decorator function that instantiates the Retrying object
-    @param *dargs: positional arguments passed to Retrying object
-    @param **dkw: keyword arguments passed to the Retrying object
-    """
-    # support both @retry and @retry() as valid syntax
-    if len(dargs) == 1 and callable(dargs[0]):
-        def wrap_simple(f):
-
-            @six.wraps(f)
-            def wrapped_f(*args, **kw):
-                return Retrying().call(f, *args, **kw)
-
-            return wrapped_f
-
-        return wrap_simple(dargs[0])
-
-    else:
-        def wrap(f):
-
-            @six.wraps(f)
-            def wrapped_f(*args, **kw):
-                return Retrying(*dargs, **dkw).call(f, *args, **kw)
-
-            return wrapped_f
-
-        return wrap
-
-
-class Retrying(object):
-
-    def __init__(self,
-                 stop=None, wait=None,
-                 stop_max_attempt_number=None,
-                 stop_max_delay=None,
-                 wait_fixed=None,
-                 wait_random_min=None, wait_random_max=None,
-                 wait_incrementing_start=None, wait_incrementing_increment=None,
-                 wait_exponential_multiplier=None, wait_exponential_max=None,
-                 retry_on_exception=None,
-                 retry_on_result=None,
-                 wrap_exception=False,
-                 stop_func=None,
-                 wait_func=None,
-                 wait_jitter_max=None):
-
-        self._stop_max_attempt_number = 5 if stop_max_attempt_number is None else stop_max_attempt_number
-        self._stop_max_delay = 100 if stop_max_delay is None else stop_max_delay
-        self._wait_fixed = 1000 if wait_fixed is None else wait_fixed
-        self._wait_random_min = 0 if wait_random_min is None else wait_random_min
-        self._wait_random_max = 1000 if wait_random_max is None else wait_random_max
-        self._wait_incrementing_start = 0 if wait_incrementing_start is None else wait_incrementing_start
-        self._wait_incrementing_increment = 100 if wait_incrementing_increment is None else wait_incrementing_increment
-        self._wait_exponential_multiplier = 1 if wait_exponential_multiplier is None else wait_exponential_multiplier
-        self._wait_exponential_max = MAX_WAIT if wait_exponential_max is None else wait_exponential_max
-        self._wait_jitter_max = 0 if wait_jitter_max is None else wait_jitter_max
-
-        # TODO add chaining of stop behaviors
-        # stop behavior
-        stop_funcs = []
-        if stop_max_attempt_number is not None:
-            stop_funcs.append(self.stop_after_attempt)
-
-        if stop_max_delay is not None:
-            stop_funcs.append(self.stop_after_delay)
-
-        if stop_func is not None:
-            self.stop = stop_func
-
-        elif stop is None:
-            self.stop = lambda attempts, delay: any(f(attempts, delay) for f in stop_funcs)
-
-        else:
-            self.stop = getattr(self, stop)
-
-        # TODO add chaining of wait behaviors
-        # wait behavior
-        wait_funcs = [lambda *args, **kwargs: 0]
-        if wait_fixed is not None:
-            wait_funcs.append(self.fixed_sleep)
-
-        if wait_random_min is not None or wait_random_max is not None:
-            wait_funcs.append(self.random_sleep)
-
-        if wait_incrementing_start is not None or wait_incrementing_increment is not None:
-            wait_funcs.append(self.incrementing_sleep)
-
-        if wait_exponential_multiplier is not None or wait_exponential_max is not None:
-            wait_funcs.append(self.exponential_sleep)
-
-        if wait_func is not None:
-            self.wait = wait_func
-
-        elif wait is None:
-            self.wait = lambda attempts, delay: max(f(attempts, delay) for f in wait_funcs)
-
-        else:
-            self.wait = getattr(self, wait)
-
-        # retry on exception filter
-        if retry_on_exception is None:
-            self._retry_on_exception = self.always_reject
-        else:
-            self._retry_on_exception = retry_on_exception
-
-        # TODO simplify retrying by Exception types
-        # retry on result filter
-        if retry_on_result is None:
-            self._retry_on_result = self.never_reject
-        else:
-            self._retry_on_result = retry_on_result
-
-        self._wrap_exception = wrap_exception
-
-    def stop_after_attempt(self, previous_attempt_number, delay_since_first_attempt_ms):
-        """Stop after the previous attempt >= stop_max_attempt_number."""
-        return previous_attempt_number >= self._stop_max_attempt_number
-
-    def stop_after_delay(self, previous_attempt_number, delay_since_first_attempt_ms):
-        """Stop after the time from the first attempt >= stop_max_delay."""
-        return delay_since_first_attempt_ms >= self._stop_max_delay
-
-    def no_sleep(self, previous_attempt_number, delay_since_first_attempt_ms):
-        """Don't sleep at all before retrying."""
-        return 0
-
-    def fixed_sleep(self, previous_attempt_number, delay_since_first_attempt_ms):
-        """Sleep a fixed amount of time between each retry."""
-        return self._wait_fixed
-
-    def random_sleep(self, previous_attempt_number, delay_since_first_attempt_ms):
-        """Sleep a random amount of time between wait_random_min and wait_random_max"""
-        return random.randint(self._wait_random_min, self._wait_random_max)
-
-    def incrementing_sleep(self, previous_attempt_number, delay_since_first_attempt_ms):
-        """
-        Sleep an incremental amount of time after each attempt, starting at
-        wait_incrementing_start and incrementing by wait_incrementing_increment
-        """
-        result = self._wait_incrementing_start + (self._wait_incrementing_increment * (previous_attempt_number - 1))
-        if result < 0:
-            result = 0
-        return result
-
-    def exponential_sleep(self, previous_attempt_number, delay_since_first_attempt_ms):
-        exp = 2 ** previous_attempt_number
-        result = self._wait_exponential_multiplier * exp
-        if result > self._wait_exponential_max:
-            result = self._wait_exponential_max
-        if result < 0:
-            result = 0
-        return result
-
-    def never_reject(self, result):
-        return False
-
-    def always_reject(self, result):
-        return True
-
-    def should_reject(self, attempt):
-        reject = False
-        if attempt.has_exception:
-            reject |= self._retry_on_exception(attempt.value[1])
-        else:
-            reject |= self._retry_on_result(attempt.value)
-
-        return reject
-
-    def call(self, fn, *args, **kwargs):
-        start_time = int(round(time.time() * 1000))
-        attempt_number = 1
-        while True:
-            try:
-                attempt = Attempt(fn(*args, **kwargs), attempt_number, False)
-            except:
-                tb = sys.exc_info()
-                attempt = Attempt(tb, attempt_number, True)
-
-            if not self.should_reject(attempt):
-                return attempt.get(self._wrap_exception)
-
-            delay_since_first_attempt_ms = int(round(time.time() * 1000)) - start_time
-            if self.stop(attempt_number, delay_since_first_attempt_ms):
-                if not self._wrap_exception and attempt.has_exception:
-                    # get() on an attempt with an exception should cause it to be raised, but raise just in case
-                    raise attempt.get()
-                else:
-                    raise RetryError(attempt)
-            else:
-                sleep = self.wait(attempt_number, delay_since_first_attempt_ms)
-                if self._wait_jitter_max:
-                    jitter = random.random() * self._wait_jitter_max
-                    sleep = sleep + max(0, jitter)
-                time.sleep(sleep / 1000.0)
-
-            attempt_number += 1
-
-
-class Attempt(object):
-    """
-    An Attempt encapsulates a call to a target function that may end as a
-    normal return value from the function or an Exception depending on what
-    occurred during the execution.
-    """
-
-    def __init__(self, value, attempt_number, has_exception):
-        self.value = value
-        self.attempt_number = attempt_number
-        self.has_exception = has_exception
-
-    def get(self, wrap_exception=False):
-        """
-        Return the return value of this Attempt instance or raise an Exception.
-        If wrap_exception is true, this Attempt is wrapped inside of a
-        RetryError before being raised.
-        """
-        if self.has_exception:
-            if wrap_exception:
-                raise RetryError(self)
-            else:
-                six.reraise(self.value[0], self.value[1], self.value[2])
-        else:
-            return self.value
-
-    def __repr__(self):
-        if self.has_exception:
-            return "Attempts: {0}, Error:\n{1}".format(self.attempt_number, "".join(traceback.format_tb(self.value[2])))
-        else:
-            return "Attempts: {0}, Value: {1}".format(self.attempt_number, self.value)
-
-
-class RetryError(Exception):
-    """
-    A RetryError encapsulates the last Attempt instance right before giving up.
-    """
-
-    def __init__(self, last_attempt):
-        self.last_attempt = last_attempt
-
-    def __str__(self):
-        return "RetryError[{0}]".format(self.last_attempt)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/six.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/six.py
deleted file mode 100644
index 89b2188..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/six.py
+++ /dev/null
@@ -1,952 +0,0 @@
-# Copyright (c) 2010-2018 Benjamin Peterson
-#
-# Permission is hereby granted, free of charge, to any person obtaining a copy
-# of this software and associated documentation files (the "Software"), to deal
-# in the Software without restriction, including without limitation the rights
-# to use, copy, modify, merge, publish, distribute, sublicense, and/or sell
-# copies of the Software, and to permit persons to whom the Software is
-# furnished to do so, subject to the following conditions:
-#
-# The above copyright notice and this permission notice shall be included in all
-# copies or substantial portions of the Software.
-#
-# THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR
-# IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF MERCHANTABILITY,
-# FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL THE
-# AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER
-# LIABILITY, WHETHER IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING FROM,
-# OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR OTHER DEALINGS IN THE
-# SOFTWARE.
-
-"""Utilities for writing code that runs on Python 2 and 3"""
-
-from __future__ import absolute_import
-
-import functools
-import itertools
-import operator
-import sys
-import types
-
-__author__ = "Benjamin Peterson <benjamin@python.org>"
-__version__ = "1.12.0"
-
-
-# Useful for very coarse version differentiation.
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-PY34 = sys.version_info[0:2] >= (3, 4)
-
-if PY3:
-    string_types = str,
-    integer_types = int,
-    class_types = type,
-    text_type = str
-    binary_type = bytes
-
-    MAXSIZE = sys.maxsize
-else:
-    string_types = basestring,
-    integer_types = (int, long)
-    class_types = (type, types.ClassType)
-    text_type = unicode
-    binary_type = str
-
-    if sys.platform.startswith("java"):
-        # Jython always uses 32 bits.
-        MAXSIZE = int((1 << 31) - 1)
-    else:
-        # It's possible to have sizeof(long) != sizeof(Py_ssize_t).
-        class X(object):
-
-            def __len__(self):
-                return 1 << 31
-        try:
-            len(X())
-        except OverflowError:
-            # 32-bit
-            MAXSIZE = int((1 << 31) - 1)
-        else:
-            # 64-bit
-            MAXSIZE = int((1 << 63) - 1)
-        del X
-
-
-def _add_doc(func, doc):
-    """Add documentation to a function."""
-    func.__doc__ = doc
-
-
-def _import_module(name):
-    """Import module, returning the module after the last dot."""
-    __import__(name)
-    return sys.modules[name]
-
-
-class _LazyDescr(object):
-
-    def __init__(self, name):
-        self.name = name
-
-    def __get__(self, obj, tp):
-        result = self._resolve()
-        setattr(obj, self.name, result)  # Invokes __set__.
-        try:
-            # This is a bit ugly, but it avoids running this again by
-            # removing this descriptor.
-            delattr(obj.__class__, self.name)
-        except AttributeError:
-            pass
-        return result
-
-
-class MovedModule(_LazyDescr):
-
-    def __init__(self, name, old, new=None):
-        super(MovedModule, self).__init__(name)
-        if PY3:
-            if new is None:
-                new = name
-            self.mod = new
-        else:
-            self.mod = old
-
-    def _resolve(self):
-        return _import_module(self.mod)
-
-    def __getattr__(self, attr):
-        _module = self._resolve()
-        value = getattr(_module, attr)
-        setattr(self, attr, value)
-        return value
-
-
-class _LazyModule(types.ModuleType):
-
-    def __init__(self, name):
-        super(_LazyModule, self).__init__(name)
-        self.__doc__ = self.__class__.__doc__
-
-    def __dir__(self):
-        attrs = ["__doc__", "__name__"]
-        attrs += [attr.name for attr in self._moved_attributes]
-        return attrs
-
-    # Subclasses should override this
-    _moved_attributes = []
-
-
-class MovedAttribute(_LazyDescr):
-
-    def __init__(self, name, old_mod, new_mod, old_attr=None, new_attr=None):
-        super(MovedAttribute, self).__init__(name)
-        if PY3:
-            if new_mod is None:
-                new_mod = name
-            self.mod = new_mod
-            if new_attr is None:
-                if old_attr is None:
-                    new_attr = name
-                else:
-                    new_attr = old_attr
-            self.attr = new_attr
-        else:
-            self.mod = old_mod
-            if old_attr is None:
-                old_attr = name
-            self.attr = old_attr
-
-    def _resolve(self):
-        module = _import_module(self.mod)
-        return getattr(module, self.attr)
-
-
-class _SixMetaPathImporter(object):
-
-    """
-    A meta path importer to import six.moves and its submodules.
-
-    This class implements a PEP302 finder and loader. It should be compatible
-    with Python 2.5 and all existing versions of Python3
-    """
-
-    def __init__(self, six_module_name):
-        self.name = six_module_name
-        self.known_modules = {}
-
-    def _add_module(self, mod, *fullnames):
-        for fullname in fullnames:
-            self.known_modules[self.name + "." + fullname] = mod
-
-    def _get_module(self, fullname):
-        return self.known_modules[self.name + "." + fullname]
-
-    def find_module(self, fullname, path=None):
-        if fullname in self.known_modules:
-            return self
-        return None
-
-    def __get_module(self, fullname):
-        try:
-            return self.known_modules[fullname]
-        except KeyError:
-            raise ImportError("This loader does not know module " + fullname)
-
-    def load_module(self, fullname):
-        try:
-            # in case of a reload
-            return sys.modules[fullname]
-        except KeyError:
-            pass
-        mod = self.__get_module(fullname)
-        if isinstance(mod, MovedModule):
-            mod = mod._resolve()
-        else:
-            mod.__loader__ = self
-        sys.modules[fullname] = mod
-        return mod
-
-    def is_package(self, fullname):
-        """
-        Return true, if the named module is a package.
-
-        We need this method to get correct spec objects with
-        Python 3.4 (see PEP451)
-        """
-        return hasattr(self.__get_module(fullname), "__path__")
-
-    def get_code(self, fullname):
-        """Return None
-
-        Required, if is_package is implemented"""
-        self.__get_module(fullname)  # eventually raises ImportError
-        return None
-    get_source = get_code  # same as get_code
-
-_importer = _SixMetaPathImporter(__name__)
-
-
-class _MovedItems(_LazyModule):
-
-    """Lazy loading of moved objects"""
-    __path__ = []  # mark as package
-
-
-_moved_attributes = [
-    MovedAttribute("cStringIO", "cStringIO", "io", "StringIO"),
-    MovedAttribute("filter", "itertools", "builtins", "ifilter", "filter"),
-    MovedAttribute("filterfalse", "itertools", "itertools", "ifilterfalse", "filterfalse"),
-    MovedAttribute("input", "__builtin__", "builtins", "raw_input", "input"),
-    MovedAttribute("intern", "__builtin__", "sys"),
-    MovedAttribute("map", "itertools", "builtins", "imap", "map"),
-    MovedAttribute("getcwd", "os", "os", "getcwdu", "getcwd"),
-    MovedAttribute("getcwdb", "os", "os", "getcwd", "getcwdb"),
-    MovedAttribute("getoutput", "commands", "subprocess"),
-    MovedAttribute("range", "__builtin__", "builtins", "xrange", "range"),
-    MovedAttribute("reload_module", "__builtin__", "importlib" if PY34 else "imp", "reload"),
-    MovedAttribute("reduce", "__builtin__", "functools"),
-    MovedAttribute("shlex_quote", "pipes", "shlex", "quote"),
-    MovedAttribute("StringIO", "StringIO", "io"),
-    MovedAttribute("UserDict", "UserDict", "collections"),
-    MovedAttribute("UserList", "UserList", "collections"),
-    MovedAttribute("UserString", "UserString", "collections"),
-    MovedAttribute("xrange", "__builtin__", "builtins", "xrange", "range"),
-    MovedAttribute("zip", "itertools", "builtins", "izip", "zip"),
-    MovedAttribute("zip_longest", "itertools", "itertools", "izip_longest", "zip_longest"),
-    MovedModule("builtins", "__builtin__"),
-    MovedModule("configparser", "ConfigParser"),
-    MovedModule("copyreg", "copy_reg"),
-    MovedModule("dbm_gnu", "gdbm", "dbm.gnu"),
-    MovedModule("_dummy_thread", "dummy_thread", "_dummy_thread"),
-    MovedModule("http_cookiejar", "cookielib", "http.cookiejar"),
-    MovedModule("http_cookies", "Cookie", "http.cookies"),
-    MovedModule("html_entities", "htmlentitydefs", "html.entities"),
-    MovedModule("html_parser", "HTMLParser", "html.parser"),
-    MovedModule("http_client", "httplib", "http.client"),
-    MovedModule("email_mime_base", "email.MIMEBase", "email.mime.base"),
-    MovedModule("email_mime_image", "email.MIMEImage", "email.mime.image"),
-    MovedModule("email_mime_multipart", "email.MIMEMultipart", "email.mime.multipart"),
-    MovedModule("email_mime_nonmultipart", "email.MIMENonMultipart", "email.mime.nonmultipart"),
-    MovedModule("email_mime_text", "email.MIMEText", "email.mime.text"),
-    MovedModule("BaseHTTPServer", "BaseHTTPServer", "http.server"),
-    MovedModule("CGIHTTPServer", "CGIHTTPServer", "http.server"),
-    MovedModule("SimpleHTTPServer", "SimpleHTTPServer", "http.server"),
-    MovedModule("cPickle", "cPickle", "pickle"),
-    MovedModule("queue", "Queue"),
-    MovedModule("reprlib", "repr"),
-    MovedModule("socketserver", "SocketServer"),
-    MovedModule("_thread", "thread", "_thread"),
-    MovedModule("tkinter", "Tkinter"),
-    MovedModule("tkinter_dialog", "Dialog", "tkinter.dialog"),
-    MovedModule("tkinter_filedialog", "FileDialog", "tkinter.filedialog"),
-    MovedModule("tkinter_scrolledtext", "ScrolledText", "tkinter.scrolledtext"),
-    MovedModule("tkinter_simpledialog", "SimpleDialog", "tkinter.simpledialog"),
-    MovedModule("tkinter_tix", "Tix", "tkinter.tix"),
-    MovedModule("tkinter_ttk", "ttk", "tkinter.ttk"),
-    MovedModule("tkinter_constants", "Tkconstants", "tkinter.constants"),
-    MovedModule("tkinter_dnd", "Tkdnd", "tkinter.dnd"),
-    MovedModule("tkinter_colorchooser", "tkColorChooser",
-                "tkinter.colorchooser"),
-    MovedModule("tkinter_commondialog", "tkCommonDialog",
-                "tkinter.commondialog"),
-    MovedModule("tkinter_tkfiledialog", "tkFileDialog", "tkinter.filedialog"),
-    MovedModule("tkinter_font", "tkFont", "tkinter.font"),
-    MovedModule("tkinter_messagebox", "tkMessageBox", "tkinter.messagebox"),
-    MovedModule("tkinter_tksimpledialog", "tkSimpleDialog",
-                "tkinter.simpledialog"),
-    MovedModule("urllib_parse", __name__ + ".moves.urllib_parse", "urllib.parse"),
-    MovedModule("urllib_error", __name__ + ".moves.urllib_error", "urllib.error"),
-    MovedModule("urllib", __name__ + ".moves.urllib", __name__ + ".moves.urllib"),
-    MovedModule("urllib_robotparser", "robotparser", "urllib.robotparser"),
-    MovedModule("xmlrpc_client", "xmlrpclib", "xmlrpc.client"),
-    MovedModule("xmlrpc_server", "SimpleXMLRPCServer", "xmlrpc.server"),
-]
-# Add windows specific modules.
-if sys.platform == "win32":
-    _moved_attributes += [
-        MovedModule("winreg", "_winreg"),
-    ]
-
-for attr in _moved_attributes:
-    setattr(_MovedItems, attr.name, attr)
-    if isinstance(attr, MovedModule):
-        _importer._add_module(attr, "moves." + attr.name)
-del attr
-
-_MovedItems._moved_attributes = _moved_attributes
-
-moves = _MovedItems(__name__ + ".moves")
-_importer._add_module(moves, "moves")
-
-
-class Module_six_moves_urllib_parse(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_parse"""
-
-
-_urllib_parse_moved_attributes = [
-    MovedAttribute("ParseResult", "urlparse", "urllib.parse"),
-    MovedAttribute("SplitResult", "urlparse", "urllib.parse"),
-    MovedAttribute("parse_qs", "urlparse", "urllib.parse"),
-    MovedAttribute("parse_qsl", "urlparse", "urllib.parse"),
-    MovedAttribute("urldefrag", "urlparse", "urllib.parse"),
-    MovedAttribute("urljoin", "urlparse", "urllib.parse"),
-    MovedAttribute("urlparse", "urlparse", "urllib.parse"),
-    MovedAttribute("urlsplit", "urlparse", "urllib.parse"),
-    MovedAttribute("urlunparse", "urlparse", "urllib.parse"),
-    MovedAttribute("urlunsplit", "urlparse", "urllib.parse"),
-    MovedAttribute("quote", "urllib", "urllib.parse"),
-    MovedAttribute("quote_plus", "urllib", "urllib.parse"),
-    MovedAttribute("unquote", "urllib", "urllib.parse"),
-    MovedAttribute("unquote_plus", "urllib", "urllib.parse"),
-    MovedAttribute("unquote_to_bytes", "urllib", "urllib.parse", "unquote", "unquote_to_bytes"),
-    MovedAttribute("urlencode", "urllib", "urllib.parse"),
-    MovedAttribute("splitquery", "urllib", "urllib.parse"),
-    MovedAttribute("splittag", "urllib", "urllib.parse"),
-    MovedAttribute("splituser", "urllib", "urllib.parse"),
-    MovedAttribute("splitvalue", "urllib", "urllib.parse"),
-    MovedAttribute("uses_fragment", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_netloc", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_params", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_query", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_relative", "urlparse", "urllib.parse"),
-]
-for attr in _urllib_parse_moved_attributes:
-    setattr(Module_six_moves_urllib_parse, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_parse._moved_attributes = _urllib_parse_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_parse(__name__ + ".moves.urllib_parse"),
-                      "moves.urllib_parse", "moves.urllib.parse")
-
-
-class Module_six_moves_urllib_error(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_error"""
-
-
-_urllib_error_moved_attributes = [
-    MovedAttribute("URLError", "urllib2", "urllib.error"),
-    MovedAttribute("HTTPError", "urllib2", "urllib.error"),
-    MovedAttribute("ContentTooShortError", "urllib", "urllib.error"),
-]
-for attr in _urllib_error_moved_attributes:
-    setattr(Module_six_moves_urllib_error, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_error._moved_attributes = _urllib_error_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_error(__name__ + ".moves.urllib.error"),
-                      "moves.urllib_error", "moves.urllib.error")
-
-
-class Module_six_moves_urllib_request(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_request"""
-
-
-_urllib_request_moved_attributes = [
-    MovedAttribute("urlopen", "urllib2", "urllib.request"),
-    MovedAttribute("install_opener", "urllib2", "urllib.request"),
-    MovedAttribute("build_opener", "urllib2", "urllib.request"),
-    MovedAttribute("pathname2url", "urllib", "urllib.request"),
-    MovedAttribute("url2pathname", "urllib", "urllib.request"),
-    MovedAttribute("getproxies", "urllib", "urllib.request"),
-    MovedAttribute("Request", "urllib2", "urllib.request"),
-    MovedAttribute("OpenerDirector", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPDefaultErrorHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPRedirectHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPCookieProcessor", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyHandler", "urllib2", "urllib.request"),
-    MovedAttribute("BaseHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPPasswordMgr", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPPasswordMgrWithDefaultRealm", "urllib2", "urllib.request"),
-    MovedAttribute("AbstractBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("AbstractDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPSHandler", "urllib2", "urllib.request"),
-    MovedAttribute("FileHandler", "urllib2", "urllib.request"),
-    MovedAttribute("FTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("CacheFTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("UnknownHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPErrorProcessor", "urllib2", "urllib.request"),
-    MovedAttribute("urlretrieve", "urllib", "urllib.request"),
-    MovedAttribute("urlcleanup", "urllib", "urllib.request"),
-    MovedAttribute("URLopener", "urllib", "urllib.request"),
-    MovedAttribute("FancyURLopener", "urllib", "urllib.request"),
-    MovedAttribute("proxy_bypass", "urllib", "urllib.request"),
-    MovedAttribute("parse_http_list", "urllib2", "urllib.request"),
-    MovedAttribute("parse_keqv_list", "urllib2", "urllib.request"),
-]
-for attr in _urllib_request_moved_attributes:
-    setattr(Module_six_moves_urllib_request, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_request._moved_attributes = _urllib_request_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_request(__name__ + ".moves.urllib.request"),
-                      "moves.urllib_request", "moves.urllib.request")
-
-
-class Module_six_moves_urllib_response(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_response"""
-
-
-_urllib_response_moved_attributes = [
-    MovedAttribute("addbase", "urllib", "urllib.response"),
-    MovedAttribute("addclosehook", "urllib", "urllib.response"),
-    MovedAttribute("addinfo", "urllib", "urllib.response"),
-    MovedAttribute("addinfourl", "urllib", "urllib.response"),
-]
-for attr in _urllib_response_moved_attributes:
-    setattr(Module_six_moves_urllib_response, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_response._moved_attributes = _urllib_response_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_response(__name__ + ".moves.urllib.response"),
-                      "moves.urllib_response", "moves.urllib.response")
-
-
-class Module_six_moves_urllib_robotparser(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_robotparser"""
-
-
-_urllib_robotparser_moved_attributes = [
-    MovedAttribute("RobotFileParser", "robotparser", "urllib.robotparser"),
-]
-for attr in _urllib_robotparser_moved_attributes:
-    setattr(Module_six_moves_urllib_robotparser, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_robotparser._moved_attributes = _urllib_robotparser_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_robotparser(__name__ + ".moves.urllib.robotparser"),
-                      "moves.urllib_robotparser", "moves.urllib.robotparser")
-
-
-class Module_six_moves_urllib(types.ModuleType):
-
-    """Create a six.moves.urllib namespace that resembles the Python 3 namespace"""
-    __path__ = []  # mark as package
-    parse = _importer._get_module("moves.urllib_parse")
-    error = _importer._get_module("moves.urllib_error")
-    request = _importer._get_module("moves.urllib_request")
-    response = _importer._get_module("moves.urllib_response")
-    robotparser = _importer._get_module("moves.urllib_robotparser")
-
-    def __dir__(self):
-        return ['parse', 'error', 'request', 'response', 'robotparser']
-
-_importer._add_module(Module_six_moves_urllib(__name__ + ".moves.urllib"),
-                      "moves.urllib")
-
-
-def add_move(move):
-    """Add an item to six.moves."""
-    setattr(_MovedItems, move.name, move)
-
-
-def remove_move(name):
-    """Remove item from six.moves."""
-    try:
-        delattr(_MovedItems, name)
-    except AttributeError:
-        try:
-            del moves.__dict__[name]
-        except KeyError:
-            raise AttributeError("no such move, %r" % (name,))
-
-
-if PY3:
-    _meth_func = "__func__"
-    _meth_self = "__self__"
-
-    _func_closure = "__closure__"
-    _func_code = "__code__"
-    _func_defaults = "__defaults__"
-    _func_globals = "__globals__"
-else:
-    _meth_func = "im_func"
-    _meth_self = "im_self"
-
-    _func_closure = "func_closure"
-    _func_code = "func_code"
-    _func_defaults = "func_defaults"
-    _func_globals = "func_globals"
-
-
-try:
-    advance_iterator = next
-except NameError:
-    def advance_iterator(it):
-        return it.next()
-next = advance_iterator
-
-
-try:
-    callable = callable
-except NameError:
-    def callable(obj):
-        return any("__call__" in klass.__dict__ for klass in type(obj).__mro__)
-
-
-if PY3:
-    def get_unbound_function(unbound):
-        return unbound
-
-    create_bound_method = types.MethodType
-
-    def create_unbound_method(func, cls):
-        return func
-
-    Iterator = object
-else:
-    def get_unbound_function(unbound):
-        return unbound.im_func
-
-    def create_bound_method(func, obj):
-        return types.MethodType(func, obj, obj.__class__)
-
-    def create_unbound_method(func, cls):
-        return types.MethodType(func, None, cls)
-
-    class Iterator(object):
-
-        def next(self):
-            return type(self).__next__(self)
-
-    callable = callable
-_add_doc(get_unbound_function,
-         """Get the function out of a possibly unbound function""")
-
-
-get_method_function = operator.attrgetter(_meth_func)
-get_method_self = operator.attrgetter(_meth_self)
-get_function_closure = operator.attrgetter(_func_closure)
-get_function_code = operator.attrgetter(_func_code)
-get_function_defaults = operator.attrgetter(_func_defaults)
-get_function_globals = operator.attrgetter(_func_globals)
-
-
-if PY3:
-    def iterkeys(d, **kw):
-        return iter(d.keys(**kw))
-
-    def itervalues(d, **kw):
-        return iter(d.values(**kw))
-
-    def iteritems(d, **kw):
-        return iter(d.items(**kw))
-
-    def iterlists(d, **kw):
-        return iter(d.lists(**kw))
-
-    viewkeys = operator.methodcaller("keys")
-
-    viewvalues = operator.methodcaller("values")
-
-    viewitems = operator.methodcaller("items")
-else:
-    def iterkeys(d, **kw):
-        return d.iterkeys(**kw)
-
-    def itervalues(d, **kw):
-        return d.itervalues(**kw)
-
-    def iteritems(d, **kw):
-        return d.iteritems(**kw)
-
-    def iterlists(d, **kw):
-        return d.iterlists(**kw)
-
-    viewkeys = operator.methodcaller("viewkeys")
-
-    viewvalues = operator.methodcaller("viewvalues")
-
-    viewitems = operator.methodcaller("viewitems")
-
-_add_doc(iterkeys, "Return an iterator over the keys of a dictionary.")
-_add_doc(itervalues, "Return an iterator over the values of a dictionary.")
-_add_doc(iteritems,
-         "Return an iterator over the (key, value) pairs of a dictionary.")
-_add_doc(iterlists,
-         "Return an iterator over the (key, [values]) pairs of a dictionary.")
-
-
-if PY3:
-    def b(s):
-        return s.encode("latin-1")
-
-    def u(s):
-        return s
-    unichr = chr
-    import struct
-    int2byte = struct.Struct(">B").pack
-    del struct
-    byte2int = operator.itemgetter(0)
-    indexbytes = operator.getitem
-    iterbytes = iter
-    import io
-    StringIO = io.StringIO
-    BytesIO = io.BytesIO
-    _assertCountEqual = "assertCountEqual"
-    if sys.version_info[1] <= 1:
-        _assertRaisesRegex = "assertRaisesRegexp"
-        _assertRegex = "assertRegexpMatches"
-    else:
-        _assertRaisesRegex = "assertRaisesRegex"
-        _assertRegex = "assertRegex"
-else:
-    def b(s):
-        return s
-    # Workaround for standalone backslash
-
-    def u(s):
-        return unicode(s.replace(r'\\', r'\\\\'), "unicode_escape")
-    unichr = unichr
-    int2byte = chr
-
-    def byte2int(bs):
-        return ord(bs[0])
-
-    def indexbytes(buf, i):
-        return ord(buf[i])
-    iterbytes = functools.partial(itertools.imap, ord)
-    import StringIO
-    StringIO = BytesIO = StringIO.StringIO
-    _assertCountEqual = "assertItemsEqual"
-    _assertRaisesRegex = "assertRaisesRegexp"
-    _assertRegex = "assertRegexpMatches"
-_add_doc(b, """Byte literal""")
-_add_doc(u, """Text literal""")
-
-
-def assertCountEqual(self, *args, **kwargs):
-    return getattr(self, _assertCountEqual)(*args, **kwargs)
-
-
-def assertRaisesRegex(self, *args, **kwargs):
-    return getattr(self, _assertRaisesRegex)(*args, **kwargs)
-
-
-def assertRegex(self, *args, **kwargs):
-    return getattr(self, _assertRegex)(*args, **kwargs)
-
-
-if PY3:
-    exec_ = getattr(moves.builtins, "exec")
-
-    def reraise(tp, value, tb=None):
-        try:
-            if value is None:
-                value = tp()
-            if value.__traceback__ is not tb:
-                raise value.with_traceback(tb)
-            raise value
-        finally:
-            value = None
-            tb = None
-
-else:
-    def exec_(_code_, _globs_=None, _locs_=None):
-        """Execute code in a namespace."""
-        if _globs_ is None:
-            frame = sys._getframe(1)
-            _globs_ = frame.f_globals
-            if _locs_ is None:
-                _locs_ = frame.f_locals
-            del frame
-        elif _locs_ is None:
-            _locs_ = _globs_
-        exec("""exec _code_ in _globs_, _locs_""")
-
-    exec_("""def reraise(tp, value, tb=None):
-    try:
-        raise tp, value, tb
-    finally:
-        tb = None
-""")
-
-
-if sys.version_info[:2] == (3, 2):
-    exec_("""def raise_from(value, from_value):
-    try:
-        if from_value is None:
-            raise value
-        raise value from from_value
-    finally:
-        value = None
-""")
-elif sys.version_info[:2] > (3, 2):
-    exec_("""def raise_from(value, from_value):
-    try:
-        raise value from from_value
-    finally:
-        value = None
-""")
-else:
-    def raise_from(value, from_value):
-        raise value
-
-
-print_ = getattr(moves.builtins, "print", None)
-if print_ is None:
-    def print_(*args, **kwargs):
-        """The new-style print function for Python 2.4 and 2.5."""
-        fp = kwargs.pop("file", sys.stdout)
-        if fp is None:
-            return
-
-        def write(data):
-            if not isinstance(data, basestring):
-                data = str(data)
-            # If the file has an encoding, encode unicode with it.
-            if (isinstance(fp, file) and
-                    isinstance(data, unicode) and
-                    fp.encoding is not None):
-                errors = getattr(fp, "errors", None)
-                if errors is None:
-                    errors = "strict"
-                data = data.encode(fp.encoding, errors)
-            fp.write(data)
-        want_unicode = False
-        sep = kwargs.pop("sep", None)
-        if sep is not None:
-            if isinstance(sep, unicode):
-                want_unicode = True
-            elif not isinstance(sep, str):
-                raise TypeError("sep must be None or a string")
-        end = kwargs.pop("end", None)
-        if end is not None:
-            if isinstance(end, unicode):
-                want_unicode = True
-            elif not isinstance(end, str):
-                raise TypeError("end must be None or a string")
-        if kwargs:
-            raise TypeError("invalid keyword arguments to print()")
-        if not want_unicode:
-            for arg in args:
-                if isinstance(arg, unicode):
-                    want_unicode = True
-                    break
-        if want_unicode:
-            newline = unicode("\n")
-            space = unicode(" ")
-        else:
-            newline = "\n"
-            space = " "
-        if sep is None:
-            sep = space
-        if end is None:
-            end = newline
-        for i, arg in enumerate(args):
-            if i:
-                write(sep)
-            write(arg)
-        write(end)
-if sys.version_info[:2] < (3, 3):
-    _print = print_
-
-    def print_(*args, **kwargs):
-        fp = kwargs.get("file", sys.stdout)
-        flush = kwargs.pop("flush", False)
-        _print(*args, **kwargs)
-        if flush and fp is not None:
-            fp.flush()
-
-_add_doc(reraise, """Reraise an exception.""")
-
-if sys.version_info[0:2] < (3, 4):
-    def wraps(wrapped, assigned=functools.WRAPPER_ASSIGNMENTS,
-              updated=functools.WRAPPER_UPDATES):
-        def wrapper(f):
-            f = functools.wraps(wrapped, assigned, updated)(f)
-            f.__wrapped__ = wrapped
-            return f
-        return wrapper
-else:
-    wraps = functools.wraps
-
-
-def with_metaclass(meta, *bases):
-    """Create a base class with a metaclass."""
-    # This requires a bit of explanation: the basic idea is to make a dummy
-    # metaclass for one level of class instantiation that replaces itself with
-    # the actual metaclass.
-    class metaclass(type):
-
-        def __new__(cls, name, this_bases, d):
-            return meta(name, bases, d)
-
-        @classmethod
-        def __prepare__(cls, name, this_bases):
-            return meta.__prepare__(name, bases)
-    return type.__new__(metaclass, 'temporary_class', (), {})
-
-
-def add_metaclass(metaclass):
-    """Class decorator for creating a class with a metaclass."""
-    def wrapper(cls):
-        orig_vars = cls.__dict__.copy()
-        slots = orig_vars.get('__slots__')
-        if slots is not None:
-            if isinstance(slots, str):
-                slots = [slots]
-            for slots_var in slots:
-                orig_vars.pop(slots_var)
-        orig_vars.pop('__dict__', None)
-        orig_vars.pop('__weakref__', None)
-        if hasattr(cls, '__qualname__'):
-            orig_vars['__qualname__'] = cls.__qualname__
-        return metaclass(cls.__name__, cls.__bases__, orig_vars)
-    return wrapper
-
-
-def ensure_binary(s, encoding='utf-8', errors='strict'):
-    """Coerce **s** to six.binary_type.
-
-    For Python 2:
-      - `unicode` -> encoded to `str`
-      - `str` -> `str`
-
-    For Python 3:
-      - `str` -> encoded to `bytes`
-      - `bytes` -> `bytes`
-    """
-    if isinstance(s, text_type):
-        return s.encode(encoding, errors)
-    elif isinstance(s, binary_type):
-        return s
-    else:
-        raise TypeError("not expecting type '%s'" % type(s))
-
-
-def ensure_str(s, encoding='utf-8', errors='strict'):
-    """Coerce *s* to `str`.
-
-    For Python 2:
-      - `unicode` -> encoded to `str`
-      - `str` -> `str`
-
-    For Python 3:
-      - `str` -> `str`
-      - `bytes` -> decoded to `str`
-    """
-    if not isinstance(s, (text_type, binary_type)):
-        raise TypeError("not expecting type '%s'" % type(s))
-    if PY2 and isinstance(s, text_type):
-        s = s.encode(encoding, errors)
-    elif PY3 and isinstance(s, binary_type):
-        s = s.decode(encoding, errors)
-    return s
-
-
-def ensure_text(s, encoding='utf-8', errors='strict'):
-    """Coerce *s* to six.text_type.
-
-    For Python 2:
-      - `unicode` -> `unicode`
-      - `str` -> `unicode`
-
-    For Python 3:
-      - `str` -> `str`
-      - `bytes` -> decoded to `str`
-    """
-    if isinstance(s, binary_type):
-        return s.decode(encoding, errors)
-    elif isinstance(s, text_type):
-        return s
-    else:
-        raise TypeError("not expecting type '%s'" % type(s))
-
-
-
-def python_2_unicode_compatible(klass):
-    """
-    A decorator that defines __unicode__ and __str__ methods under Python 2.
-    Under Python 3 it does nothing.
-
-    To support Python 2 and 3 with a single code base, define a __str__ method
-    returning text and apply this decorator to the class.
-    """
-    if PY2:
-        if '__str__' not in klass.__dict__:
-            raise ValueError("@python_2_unicode_compatible cannot be applied "
-                             "to %s because it doesn't define __str__()." %
-                             klass.__name__)
-        klass.__unicode__ = klass.__str__
-        klass.__str__ = lambda self: self.__unicode__().encode('utf-8')
-    return klass
-
-
-# Complete the moves implementation.
-# This code is at the end of this module to speed up module loading.
-# Turn this module into a package.
-__path__ = []  # required for PEP 302 and PEP 451
-__package__ = __name__  # see PEP 366 @ReservedAssignment
-if globals().get("__spec__") is not None:
-    __spec__.submodule_search_locations = []  # PEP 451 @UndefinedVariable
-# Remove other six meta path importers, since they cause problems. This can
-# happen if six is removed from sys.modules and then reloaded. (Setuptools does
-# this for some reason.)
-if sys.meta_path:
-    for i, importer in enumerate(sys.meta_path):
-        # Here's some real nastiness: Another "instance" of the six module might
-        # be floating around. Therefore, we can't use isinstance() to check for
-        # the six meta path importer, since the other six instance will have
-        # inserted an importer with different class.
-        if (type(importer).__name__ == "_SixMetaPathImporter" and
-                importer.name == __name__):
-            del sys.meta_path[i]
-            break
-    del i, importer
-# Finally, add the importer to the meta path import hook.
-sys.meta_path.append(_importer)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__init__.py
deleted file mode 100644
index 148a9c3..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__init__.py
+++ /dev/null
@@ -1,92 +0,0 @@
-"""
-urllib3 - Thread-safe connection pooling and re-using.
-"""
-
-from __future__ import absolute_import
-import warnings
-
-from .connectionpool import (
-    HTTPConnectionPool,
-    HTTPSConnectionPool,
-    connection_from_url
-)
-
-from . import exceptions
-from .filepost import encode_multipart_formdata
-from .poolmanager import PoolManager, ProxyManager, proxy_from_url
-from .response import HTTPResponse
-from .util.request import make_headers
-from .util.url import get_host
-from .util.timeout import Timeout
-from .util.retry import Retry
-
-
-# Set default logging handler to avoid "No handler found" warnings.
-import logging
-from logging import NullHandler
-
-__author__ = 'Andrey Petrov (andrey.petrov@shazow.net)'
-__license__ = 'MIT'
-__version__ = '1.24.1'
-
-__all__ = (
-    'HTTPConnectionPool',
-    'HTTPSConnectionPool',
-    'PoolManager',
-    'ProxyManager',
-    'HTTPResponse',
-    'Retry',
-    'Timeout',
-    'add_stderr_logger',
-    'connection_from_url',
-    'disable_warnings',
-    'encode_multipart_formdata',
-    'get_host',
-    'make_headers',
-    'proxy_from_url',
-)
-
-logging.getLogger(__name__).addHandler(NullHandler())
-
-
-def add_stderr_logger(level=logging.DEBUG):
-    """
-    Helper for quickly adding a StreamHandler to the logger. Useful for
-    debugging.
-
-    Returns the handler after adding it.
-    """
-    # This method needs to be in this __init__.py to get the __name__ correct
-    # even if urllib3 is vendored within another package.
-    logger = logging.getLogger(__name__)
-    handler = logging.StreamHandler()
-    handler.setFormatter(logging.Formatter('%(asctime)s %(levelname)s %(message)s'))
-    logger.addHandler(handler)
-    logger.setLevel(level)
-    logger.debug('Added a stderr logging handler to logger: %s', __name__)
-    return handler
-
-
-# ... Clean up.
-del NullHandler
-
-
-# All warning filters *must* be appended unless you're really certain that they
-# shouldn't be: otherwise, it's very hard for users to use most Python
-# mechanisms to silence them.
-# SecurityWarning's always go off by default.
-warnings.simplefilter('always', exceptions.SecurityWarning, append=True)
-# SubjectAltNameWarning's should go off once per host
-warnings.simplefilter('default', exceptions.SubjectAltNameWarning, append=True)
-# InsecurePlatformWarning's don't vary between requests, so we keep it default.
-warnings.simplefilter('default', exceptions.InsecurePlatformWarning,
-                      append=True)
-# SNIMissingWarnings should go off only once.
-warnings.simplefilter('default', exceptions.SNIMissingWarning, append=True)
-
-
-def disable_warnings(category=exceptions.HTTPWarning):
-    """
-    Helper for quickly disabling all urllib3 warnings.
-    """
-    warnings.simplefilter('ignore', category)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 0c50378..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/_collections.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/_collections.cpython-37.pyc
deleted file mode 100644
index 96c67f0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/_collections.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/connection.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/connection.cpython-37.pyc
deleted file mode 100644
index 72edb3c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/connection.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/connectionpool.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/connectionpool.cpython-37.pyc
deleted file mode 100644
index b90ca7c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/connectionpool.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/exceptions.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/exceptions.cpython-37.pyc
deleted file mode 100644
index 2b66920..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/exceptions.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/fields.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/fields.cpython-37.pyc
deleted file mode 100644
index 414b4ca..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/fields.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/filepost.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/filepost.cpython-37.pyc
deleted file mode 100644
index 418b90d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/filepost.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/poolmanager.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/poolmanager.cpython-37.pyc
deleted file mode 100644
index 59a3835..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/poolmanager.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/request.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/request.cpython-37.pyc
deleted file mode 100644
index ebe9d09..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/request.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/response.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/response.cpython-37.pyc
deleted file mode 100644
index ce00e7d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/__pycache__/response.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/_collections.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/_collections.py
deleted file mode 100644
index 34f2381..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/_collections.py
+++ /dev/null
@@ -1,329 +0,0 @@
-from __future__ import absolute_import
-try:
-    from collections.abc import Mapping, MutableMapping
-except ImportError:
-    from collections import Mapping, MutableMapping
-try:
-    from threading import RLock
-except ImportError:  # Platform-specific: No threads available
-    class RLock:
-        def __enter__(self):
-            pass
-
-        def __exit__(self, exc_type, exc_value, traceback):
-            pass
-
-
-from collections import OrderedDict
-from .exceptions import InvalidHeader
-from .packages.six import iterkeys, itervalues, PY3
-
-
-__all__ = ['RecentlyUsedContainer', 'HTTPHeaderDict']
-
-
-_Null = object()
-
-
-class RecentlyUsedContainer(MutableMapping):
-    """
-    Provides a thread-safe dict-like container which maintains up to
-    ``maxsize`` keys while throwing away the least-recently-used keys beyond
-    ``maxsize``.
-
-    :param maxsize:
-        Maximum number of recent elements to retain.
-
-    :param dispose_func:
-        Every time an item is evicted from the container,
-        ``dispose_func(value)`` is called.  Callback which will get called
-    """
-
-    ContainerCls = OrderedDict
-
-    def __init__(self, maxsize=10, dispose_func=None):
-        self._maxsize = maxsize
-        self.dispose_func = dispose_func
-
-        self._container = self.ContainerCls()
-        self.lock = RLock()
-
-    def __getitem__(self, key):
-        # Re-insert the item, moving it to the end of the eviction line.
-        with self.lock:
-            item = self._container.pop(key)
-            self._container[key] = item
-            return item
-
-    def __setitem__(self, key, value):
-        evicted_value = _Null
-        with self.lock:
-            # Possibly evict the existing value of 'key'
-            evicted_value = self._container.get(key, _Null)
-            self._container[key] = value
-
-            # If we didn't evict an existing value, we might have to evict the
-            # least recently used item from the beginning of the container.
-            if len(self._container) > self._maxsize:
-                _key, evicted_value = self._container.popitem(last=False)
-
-        if self.dispose_func and evicted_value is not _Null:
-            self.dispose_func(evicted_value)
-
-    def __delitem__(self, key):
-        with self.lock:
-            value = self._container.pop(key)
-
-        if self.dispose_func:
-            self.dispose_func(value)
-
-    def __len__(self):
-        with self.lock:
-            return len(self._container)
-
-    def __iter__(self):
-        raise NotImplementedError('Iteration over this class is unlikely to be threadsafe.')
-
-    def clear(self):
-        with self.lock:
-            # Copy pointers to all values, then wipe the mapping
-            values = list(itervalues(self._container))
-            self._container.clear()
-
-        if self.dispose_func:
-            for value in values:
-                self.dispose_func(value)
-
-    def keys(self):
-        with self.lock:
-            return list(iterkeys(self._container))
-
-
-class HTTPHeaderDict(MutableMapping):
-    """
-    :param headers:
-        An iterable of field-value pairs. Must not contain multiple field names
-        when compared case-insensitively.
-
-    :param kwargs:
-        Additional field-value pairs to pass in to ``dict.update``.
-
-    A ``dict`` like container for storing HTTP Headers.
-
-    Field names are stored and compared case-insensitively in compliance with
-    RFC 7230. Iteration provides the first case-sensitive key seen for each
-    case-insensitive pair.
-
-    Using ``__setitem__`` syntax overwrites fields that compare equal
-    case-insensitively in order to maintain ``dict``'s api. For fields that
-    compare equal, instead create a new ``HTTPHeaderDict`` and use ``.add``
-    in a loop.
-
-    If multiple fields that are equal case-insensitively are passed to the
-    constructor or ``.update``, the behavior is undefined and some will be
-    lost.
-
-    >>> headers = HTTPHeaderDict()
-    >>> headers.add('Set-Cookie', 'foo=bar')
-    >>> headers.add('set-cookie', 'baz=quxx')
-    >>> headers['content-length'] = '7'
-    >>> headers['SET-cookie']
-    'foo=bar, baz=quxx'
-    >>> headers['Content-Length']
-    '7'
-    """
-
-    def __init__(self, headers=None, **kwargs):
-        super(HTTPHeaderDict, self).__init__()
-        self._container = OrderedDict()
-        if headers is not None:
-            if isinstance(headers, HTTPHeaderDict):
-                self._copy_from(headers)
-            else:
-                self.extend(headers)
-        if kwargs:
-            self.extend(kwargs)
-
-    def __setitem__(self, key, val):
-        self._container[key.lower()] = [key, val]
-        return self._container[key.lower()]
-
-    def __getitem__(self, key):
-        val = self._container[key.lower()]
-        return ', '.join(val[1:])
-
-    def __delitem__(self, key):
-        del self._container[key.lower()]
-
-    def __contains__(self, key):
-        return key.lower() in self._container
-
-    def __eq__(self, other):
-        if not isinstance(other, Mapping) and not hasattr(other, 'keys'):
-            return False
-        if not isinstance(other, type(self)):
-            other = type(self)(other)
-        return (dict((k.lower(), v) for k, v in self.itermerged()) ==
-                dict((k.lower(), v) for k, v in other.itermerged()))
-
-    def __ne__(self, other):
-        return not self.__eq__(other)
-
-    if not PY3:  # Python 2
-        iterkeys = MutableMapping.iterkeys
-        itervalues = MutableMapping.itervalues
-
-    __marker = object()
-
-    def __len__(self):
-        return len(self._container)
-
-    def __iter__(self):
-        # Only provide the originally cased names
-        for vals in self._container.values():
-            yield vals[0]
-
-    def pop(self, key, default=__marker):
-        '''D.pop(k[,d]) -> v, remove specified key and return the corresponding value.
-          If key is not found, d is returned if given, otherwise KeyError is raised.
-        '''
-        # Using the MutableMapping function directly fails due to the private marker.
-        # Using ordinary dict.pop would expose the internal structures.
-        # So let's reinvent the wheel.
-        try:
-            value = self[key]
-        except KeyError:
-            if default is self.__marker:
-                raise
-            return default
-        else:
-            del self[key]
-            return value
-
-    def discard(self, key):
-        try:
-            del self[key]
-        except KeyError:
-            pass
-
-    def add(self, key, val):
-        """Adds a (name, value) pair, doesn't overwrite the value if it already
-        exists.
-
-        >>> headers = HTTPHeaderDict(foo='bar')
-        >>> headers.add('Foo', 'baz')
-        >>> headers['foo']
-        'bar, baz'
-        """
-        key_lower = key.lower()
-        new_vals = [key, val]
-        # Keep the common case aka no item present as fast as possible
-        vals = self._container.setdefault(key_lower, new_vals)
-        if new_vals is not vals:
-            vals.append(val)
-
-    def extend(self, *args, **kwargs):
-        """Generic import function for any type of header-like object.
-        Adapted version of MutableMapping.update in order to insert items
-        with self.add instead of self.__setitem__
-        """
-        if len(args) > 1:
-            raise TypeError("extend() takes at most 1 positional "
-                            "arguments ({0} given)".format(len(args)))
-        other = args[0] if len(args) >= 1 else ()
-
-        if isinstance(other, HTTPHeaderDict):
-            for key, val in other.iteritems():
-                self.add(key, val)
-        elif isinstance(other, Mapping):
-            for key in other:
-                self.add(key, other[key])
-        elif hasattr(other, "keys"):
-            for key in other.keys():
-                self.add(key, other[key])
-        else:
-            for key, value in other:
-                self.add(key, value)
-
-        for key, value in kwargs.items():
-            self.add(key, value)
-
-    def getlist(self, key, default=__marker):
-        """Returns a list of all the values for the named field. Returns an
-        empty list if the key doesn't exist."""
-        try:
-            vals = self._container[key.lower()]
-        except KeyError:
-            if default is self.__marker:
-                return []
-            return default
-        else:
-            return vals[1:]
-
-    # Backwards compatibility for httplib
-    getheaders = getlist
-    getallmatchingheaders = getlist
-    iget = getlist
-
-    # Backwards compatibility for http.cookiejar
-    get_all = getlist
-
-    def __repr__(self):
-        return "%s(%s)" % (type(self).__name__, dict(self.itermerged()))
-
-    def _copy_from(self, other):
-        for key in other:
-            val = other.getlist(key)
-            if isinstance(val, list):
-                # Don't need to convert tuples
-                val = list(val)
-            self._container[key.lower()] = [key] + val
-
-    def copy(self):
-        clone = type(self)()
-        clone._copy_from(self)
-        return clone
-
-    def iteritems(self):
-        """Iterate over all header lines, including duplicate ones."""
-        for key in self:
-            vals = self._container[key.lower()]
-            for val in vals[1:]:
-                yield vals[0], val
-
-    def itermerged(self):
-        """Iterate over all headers, merging duplicate ones together."""
-        for key in self:
-            val = self._container[key.lower()]
-            yield val[0], ', '.join(val[1:])
-
-    def items(self):
-        return list(self.iteritems())
-
-    @classmethod
-    def from_httplib(cls, message):  # Python 2
-        """Read headers from a Python 2 httplib message object."""
-        # python2.7 does not expose a proper API for exporting multiheaders
-        # efficiently. This function re-reads raw lines from the message
-        # object and extracts the multiheaders properly.
-        obs_fold_continued_leaders = (' ', '\t')
-        headers = []
-
-        for line in message.headers:
-            if line.startswith(obs_fold_continued_leaders):
-                if not headers:
-                    # We received a header line that starts with OWS as described
-                    # in RFC-7230 S3.2.4. This indicates a multiline header, but
-                    # there exists no previous header to which we can attach it.
-                    raise InvalidHeader(
-                        'Header continuation with no previous header: %s' % line
-                    )
-                else:
-                    key, value = headers[-1]
-                    headers[-1] = (key, value + ' ' + line.strip())
-                    continue
-
-            key, value = line.split(':', 1)
-            headers.append((key, value.strip()))
-
-        return cls(headers)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/connection.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/connection.py
deleted file mode 100644
index 02b3665..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/connection.py
+++ /dev/null
@@ -1,391 +0,0 @@
-from __future__ import absolute_import
-import datetime
-import logging
-import os
-import socket
-from socket import error as SocketError, timeout as SocketTimeout
-import warnings
-from .packages import six
-from .packages.six.moves.http_client import HTTPConnection as _HTTPConnection
-from .packages.six.moves.http_client import HTTPException  # noqa: F401
-
-try:  # Compiled with SSL?
-    import ssl
-    BaseSSLError = ssl.SSLError
-except (ImportError, AttributeError):  # Platform-specific: No SSL.
-    ssl = None
-
-    class BaseSSLError(BaseException):
-        pass
-
-
-try:  # Python 3:
-    # Not a no-op, we're adding this to the namespace so it can be imported.
-    ConnectionError = ConnectionError
-except NameError:  # Python 2:
-    class ConnectionError(Exception):
-        pass
-
-
-from .exceptions import (
-    NewConnectionError,
-    ConnectTimeoutError,
-    SubjectAltNameWarning,
-    SystemTimeWarning,
-)
-from .packages.ssl_match_hostname import match_hostname, CertificateError
-
-from .util.ssl_ import (
-    resolve_cert_reqs,
-    resolve_ssl_version,
-    assert_fingerprint,
-    create_urllib3_context,
-    ssl_wrap_socket
-)
-
-
-from .util import connection
-
-from ._collections import HTTPHeaderDict
-
-log = logging.getLogger(__name__)
-
-port_by_scheme = {
-    'http': 80,
-    'https': 443,
-}
-
-# When updating RECENT_DATE, move it to within two years of the current date,
-# and not less than 6 months ago.
-# Example: if Today is 2018-01-01, then RECENT_DATE should be any date on or
-# after 2016-01-01 (today - 2 years) AND before 2017-07-01 (today - 6 months)
-RECENT_DATE = datetime.date(2017, 6, 30)
-
-
-class DummyConnection(object):
-    """Used to detect a failed ConnectionCls import."""
-    pass
-
-
-class HTTPConnection(_HTTPConnection, object):
-    """
-    Based on httplib.HTTPConnection but provides an extra constructor
-    backwards-compatibility layer between older and newer Pythons.
-
-    Additional keyword parameters are used to configure attributes of the connection.
-    Accepted parameters include:
-
-      - ``strict``: See the documentation on :class:`urllib3.connectionpool.HTTPConnectionPool`
-      - ``source_address``: Set the source address for the current connection.
-      - ``socket_options``: Set specific options on the underlying socket. If not specified, then
-        defaults are loaded from ``HTTPConnection.default_socket_options`` which includes disabling
-        Nagle's algorithm (sets TCP_NODELAY to 1) unless the connection is behind a proxy.
-
-        For example, if you wish to enable TCP Keep Alive in addition to the defaults,
-        you might pass::
-
-            HTTPConnection.default_socket_options + [
-                (socket.SOL_SOCKET, socket.SO_KEEPALIVE, 1),
-            ]
-
-        Or you may want to disable the defaults by passing an empty list (e.g., ``[]``).
-    """
-
-    default_port = port_by_scheme['http']
-
-    #: Disable Nagle's algorithm by default.
-    #: ``[(socket.IPPROTO_TCP, socket.TCP_NODELAY, 1)]``
-    default_socket_options = [(socket.IPPROTO_TCP, socket.TCP_NODELAY, 1)]
-
-    #: Whether this connection verifies the host's certificate.
-    is_verified = False
-
-    def __init__(self, *args, **kw):
-        if six.PY3:  # Python 3
-            kw.pop('strict', None)
-
-        # Pre-set source_address.
-        self.source_address = kw.get('source_address')
-
-        #: The socket options provided by the user. If no options are
-        #: provided, we use the default options.
-        self.socket_options = kw.pop('socket_options', self.default_socket_options)
-
-        _HTTPConnection.__init__(self, *args, **kw)
-
-    @property
-    def host(self):
-        """
-        Getter method to remove any trailing dots that indicate the hostname is an FQDN.
-
-        In general, SSL certificates don't include the trailing dot indicating a
-        fully-qualified domain name, and thus, they don't validate properly when
-        checked against a domain name that includes the dot. In addition, some
-        servers may not expect to receive the trailing dot when provided.
-
-        However, the hostname with trailing dot is critical to DNS resolution; doing a
-        lookup with the trailing dot will properly only resolve the appropriate FQDN,
-        whereas a lookup without a trailing dot will search the system's search domain
-        list. Thus, it's important to keep the original host around for use only in
-        those cases where it's appropriate (i.e., when doing DNS lookup to establish the
-        actual TCP connection across which we're going to send HTTP requests).
-        """
-        return self._dns_host.rstrip('.')
-
-    @host.setter
-    def host(self, value):
-        """
-        Setter for the `host` property.
-
-        We assume that only urllib3 uses the _dns_host attribute; httplib itself
-        only uses `host`, and it seems reasonable that other libraries follow suit.
-        """
-        self._dns_host = value
-
-    def _new_conn(self):
-        """ Establish a socket connection and set nodelay settings on it.
-
-        :return: New socket connection.
-        """
-        extra_kw = {}
-        if self.source_address:
-            extra_kw['source_address'] = self.source_address
-
-        if self.socket_options:
-            extra_kw['socket_options'] = self.socket_options
-
-        try:
-            conn = connection.create_connection(
-                (self._dns_host, self.port), self.timeout, **extra_kw)
-
-        except SocketTimeout as e:
-            raise ConnectTimeoutError(
-                self, "Connection to %s timed out. (connect timeout=%s)" %
-                (self.host, self.timeout))
-
-        except SocketError as e:
-            raise NewConnectionError(
-                self, "Failed to establish a new connection: %s" % e)
-
-        return conn
-
-    def _prepare_conn(self, conn):
-        self.sock = conn
-        if self._tunnel_host:
-            # TODO: Fix tunnel so it doesn't depend on self.sock state.
-            self._tunnel()
-            # Mark this connection as not reusable
-            self.auto_open = 0
-
-    def connect(self):
-        conn = self._new_conn()
-        self._prepare_conn(conn)
-
-    def request_chunked(self, method, url, body=None, headers=None):
-        """
-        Alternative to the common request method, which sends the
-        body with chunked encoding and not as one block
-        """
-        headers = HTTPHeaderDict(headers if headers is not None else {})
-        skip_accept_encoding = 'accept-encoding' in headers
-        skip_host = 'host' in headers
-        self.putrequest(
-            method,
-            url,
-            skip_accept_encoding=skip_accept_encoding,
-            skip_host=skip_host
-        )
-        for header, value in headers.items():
-            self.putheader(header, value)
-        if 'transfer-encoding' not in headers:
-            self.putheader('Transfer-Encoding', 'chunked')
-        self.endheaders()
-
-        if body is not None:
-            stringish_types = six.string_types + (bytes,)
-            if isinstance(body, stringish_types):
-                body = (body,)
-            for chunk in body:
-                if not chunk:
-                    continue
-                if not isinstance(chunk, bytes):
-                    chunk = chunk.encode('utf8')
-                len_str = hex(len(chunk))[2:]
-                self.send(len_str.encode('utf-8'))
-                self.send(b'\r\n')
-                self.send(chunk)
-                self.send(b'\r\n')
-
-        # After the if clause, to always have a closed body
-        self.send(b'0\r\n\r\n')
-
-
-class HTTPSConnection(HTTPConnection):
-    default_port = port_by_scheme['https']
-
-    ssl_version = None
-
-    def __init__(self, host, port=None, key_file=None, cert_file=None,
-                 strict=None, timeout=socket._GLOBAL_DEFAULT_TIMEOUT,
-                 ssl_context=None, server_hostname=None, **kw):
-
-        HTTPConnection.__init__(self, host, port, strict=strict,
-                                timeout=timeout, **kw)
-
-        self.key_file = key_file
-        self.cert_file = cert_file
-        self.ssl_context = ssl_context
-        self.server_hostname = server_hostname
-
-        # Required property for Google AppEngine 1.9.0 which otherwise causes
-        # HTTPS requests to go out as HTTP. (See Issue #356)
-        self._protocol = 'https'
-
-    def connect(self):
-        conn = self._new_conn()
-        self._prepare_conn(conn)
-
-        if self.ssl_context is None:
-            self.ssl_context = create_urllib3_context(
-                ssl_version=resolve_ssl_version(None),
-                cert_reqs=resolve_cert_reqs(None),
-            )
-
-        self.sock = ssl_wrap_socket(
-            sock=conn,
-            keyfile=self.key_file,
-            certfile=self.cert_file,
-            ssl_context=self.ssl_context,
-            server_hostname=self.server_hostname
-        )
-
-
-class VerifiedHTTPSConnection(HTTPSConnection):
-    """
-    Based on httplib.HTTPSConnection but wraps the socket with
-    SSL certification.
-    """
-    cert_reqs = None
-    ca_certs = None
-    ca_cert_dir = None
-    ssl_version = None
-    assert_fingerprint = None
-
-    def set_cert(self, key_file=None, cert_file=None,
-                 cert_reqs=None, ca_certs=None,
-                 assert_hostname=None, assert_fingerprint=None,
-                 ca_cert_dir=None):
-        """
-        This method should only be called once, before the connection is used.
-        """
-        # If cert_reqs is not provided, we can try to guess. If the user gave
-        # us a cert database, we assume they want to use it: otherwise, if
-        # they gave us an SSL Context object we should use whatever is set for
-        # it.
-        if cert_reqs is None:
-            if ca_certs or ca_cert_dir:
-                cert_reqs = 'CERT_REQUIRED'
-            elif self.ssl_context is not None:
-                cert_reqs = self.ssl_context.verify_mode
-
-        self.key_file = key_file
-        self.cert_file = cert_file
-        self.cert_reqs = cert_reqs
-        self.assert_hostname = assert_hostname
-        self.assert_fingerprint = assert_fingerprint
-        self.ca_certs = ca_certs and os.path.expanduser(ca_certs)
-        self.ca_cert_dir = ca_cert_dir and os.path.expanduser(ca_cert_dir)
-
-    def connect(self):
-        # Add certificate verification
-        conn = self._new_conn()
-        hostname = self.host
-
-        if self._tunnel_host:
-            self.sock = conn
-            # Calls self._set_hostport(), so self.host is
-            # self._tunnel_host below.
-            self._tunnel()
-            # Mark this connection as not reusable
-            self.auto_open = 0
-
-            # Override the host with the one we're requesting data from.
-            hostname = self._tunnel_host
-
-        server_hostname = hostname
-        if self.server_hostname is not None:
-            server_hostname = self.server_hostname
-
-        is_time_off = datetime.date.today() < RECENT_DATE
-        if is_time_off:
-            warnings.warn((
-                'System time is way off (before {0}). This will probably '
-                'lead to SSL verification errors').format(RECENT_DATE),
-                SystemTimeWarning
-            )
-
-        # Wrap socket using verification with the root certs in
-        # trusted_root_certs
-        if self.ssl_context is None:
-            self.ssl_context = create_urllib3_context(
-                ssl_version=resolve_ssl_version(self.ssl_version),
-                cert_reqs=resolve_cert_reqs(self.cert_reqs),
-            )
-
-        context = self.ssl_context
-        context.verify_mode = resolve_cert_reqs(self.cert_reqs)
-        self.sock = ssl_wrap_socket(
-            sock=conn,
-            keyfile=self.key_file,
-            certfile=self.cert_file,
-            ca_certs=self.ca_certs,
-            ca_cert_dir=self.ca_cert_dir,
-            server_hostname=server_hostname,
-            ssl_context=context)
-
-        if self.assert_fingerprint:
-            assert_fingerprint(self.sock.getpeercert(binary_form=True),
-                               self.assert_fingerprint)
-        elif context.verify_mode != ssl.CERT_NONE \
-                and not getattr(context, 'check_hostname', False) \
-                and self.assert_hostname is not False:
-            # While urllib3 attempts to always turn off hostname matching from
-            # the TLS library, this cannot always be done. So we check whether
-            # the TLS Library still thinks it's matching hostnames.
-            cert = self.sock.getpeercert()
-            if not cert.get('subjectAltName', ()):
-                warnings.warn((
-                    'Certificate for {0} has no `subjectAltName`, falling back to check for a '
-                    '`commonName` for now. This feature is being removed by major browsers and '
-                    'deprecated by RFC 2818. (See https://github.com/shazow/urllib3/issues/497 '
-                    'for details.)'.format(hostname)),
-                    SubjectAltNameWarning
-                )
-            _match_hostname(cert, self.assert_hostname or server_hostname)
-
-        self.is_verified = (
-            context.verify_mode == ssl.CERT_REQUIRED or
-            self.assert_fingerprint is not None
-        )
-
-
-def _match_hostname(cert, asserted_hostname):
-    try:
-        match_hostname(cert, asserted_hostname)
-    except CertificateError as e:
-        log.error(
-            'Certificate did not match expected hostname: %s. '
-            'Certificate: %s', asserted_hostname, cert
-        )
-        # Add cert to exception and reraise so client code can inspect
-        # the cert when catching the exception, if they want to
-        e._peer_cert = cert
-        raise
-
-
-if ssl:
-    # Make a copy for testing.
-    UnverifiedHTTPSConnection = HTTPSConnection
-    HTTPSConnection = VerifiedHTTPSConnection
-else:
-    HTTPSConnection = DummyConnection
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/connectionpool.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/connectionpool.py
deleted file mode 100644
index f7a8f19..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/connectionpool.py
+++ /dev/null
@@ -1,896 +0,0 @@
-from __future__ import absolute_import
-import errno
-import logging
-import sys
-import warnings
-
-from socket import error as SocketError, timeout as SocketTimeout
-import socket
-
-
-from .exceptions import (
-    ClosedPoolError,
-    ProtocolError,
-    EmptyPoolError,
-    HeaderParsingError,
-    HostChangedError,
-    LocationValueError,
-    MaxRetryError,
-    ProxyError,
-    ReadTimeoutError,
-    SSLError,
-    TimeoutError,
-    InsecureRequestWarning,
-    NewConnectionError,
-)
-from .packages.ssl_match_hostname import CertificateError
-from .packages import six
-from .packages.six.moves import queue
-from .connection import (
-    port_by_scheme,
-    DummyConnection,
-    HTTPConnection, HTTPSConnection, VerifiedHTTPSConnection,
-    HTTPException, BaseSSLError,
-)
-from .request import RequestMethods
-from .response import HTTPResponse
-
-from .util.connection import is_connection_dropped
-from .util.request import set_file_position
-from .util.response import assert_header_parsing
-from .util.retry import Retry
-from .util.timeout import Timeout
-from .util.url import get_host, Url, NORMALIZABLE_SCHEMES
-from .util.queue import LifoQueue
-
-
-xrange = six.moves.xrange
-
-log = logging.getLogger(__name__)
-
-_Default = object()
-
-
-# Pool objects
-class ConnectionPool(object):
-    """
-    Base class for all connection pools, such as
-    :class:`.HTTPConnectionPool` and :class:`.HTTPSConnectionPool`.
-    """
-
-    scheme = None
-    QueueCls = LifoQueue
-
-    def __init__(self, host, port=None):
-        if not host:
-            raise LocationValueError("No host specified.")
-
-        self.host = _ipv6_host(host, self.scheme)
-        self._proxy_host = host.lower()
-        self.port = port
-
-    def __str__(self):
-        return '%s(host=%r, port=%r)' % (type(self).__name__,
-                                         self.host, self.port)
-
-    def __enter__(self):
-        return self
-
-    def __exit__(self, exc_type, exc_val, exc_tb):
-        self.close()
-        # Return False to re-raise any potential exceptions
-        return False
-
-    def close(self):
-        """
-        Close all pooled connections and disable the pool.
-        """
-        pass
-
-
-# This is taken from http://hg.python.org/cpython/file/7aaba721ebc0/Lib/socket.py#l252
-_blocking_errnos = {errno.EAGAIN, errno.EWOULDBLOCK}
-
-
-class HTTPConnectionPool(ConnectionPool, RequestMethods):
-    """
-    Thread-safe connection pool for one host.
-
-    :param host:
-        Host used for this HTTP Connection (e.g. "localhost"), passed into
-        :class:`httplib.HTTPConnection`.
-
-    :param port:
-        Port used for this HTTP Connection (None is equivalent to 80), passed
-        into :class:`httplib.HTTPConnection`.
-
-    :param strict:
-        Causes BadStatusLine to be raised if the status line can't be parsed
-        as a valid HTTP/1.0 or 1.1 status line, passed into
-        :class:`httplib.HTTPConnection`.
-
-        .. note::
-           Only works in Python 2. This parameter is ignored in Python 3.
-
-    :param timeout:
-        Socket timeout in seconds for each individual connection. This can
-        be a float or integer, which sets the timeout for the HTTP request,
-        or an instance of :class:`urllib3.util.Timeout` which gives you more
-        fine-grained control over request timeouts. After the constructor has
-        been parsed, this is always a `urllib3.util.Timeout` object.
-
-    :param maxsize:
-        Number of connections to save that can be reused. More than 1 is useful
-        in multithreaded situations. If ``block`` is set to False, more
-        connections will be created but they will not be saved once they've
-        been used.
-
-    :param block:
-        If set to True, no more than ``maxsize`` connections will be used at
-        a time. When no free connections are available, the call will block
-        until a connection has been released. This is a useful side effect for
-        particular multithreaded situations where one does not want to use more
-        than maxsize connections per host to prevent flooding.
-
-    :param headers:
-        Headers to include with all requests, unless other headers are given
-        explicitly.
-
-    :param retries:
-        Retry configuration to use by default with requests in this pool.
-
-    :param _proxy:
-        Parsed proxy URL, should not be used directly, instead, see
-        :class:`urllib3.connectionpool.ProxyManager`"
-
-    :param _proxy_headers:
-        A dictionary with proxy headers, should not be used directly,
-        instead, see :class:`urllib3.connectionpool.ProxyManager`"
-
-    :param \\**conn_kw:
-        Additional parameters are used to create fresh :class:`urllib3.connection.HTTPConnection`,
-        :class:`urllib3.connection.HTTPSConnection` instances.
-    """
-
-    scheme = 'http'
-    ConnectionCls = HTTPConnection
-    ResponseCls = HTTPResponse
-
-    def __init__(self, host, port=None, strict=False,
-                 timeout=Timeout.DEFAULT_TIMEOUT, maxsize=1, block=False,
-                 headers=None, retries=None,
-                 _proxy=None, _proxy_headers=None,
-                 **conn_kw):
-        ConnectionPool.__init__(self, host, port)
-        RequestMethods.__init__(self, headers)
-
-        self.strict = strict
-
-        if not isinstance(timeout, Timeout):
-            timeout = Timeout.from_float(timeout)
-
-        if retries is None:
-            retries = Retry.DEFAULT
-
-        self.timeout = timeout
-        self.retries = retries
-
-        self.pool = self.QueueCls(maxsize)
-        self.block = block
-
-        self.proxy = _proxy
-        self.proxy_headers = _proxy_headers or {}
-
-        # Fill the queue up so that doing get() on it will block properly
-        for _ in xrange(maxsize):
-            self.pool.put(None)
-
-        # These are mostly for testing and debugging purposes.
-        self.num_connections = 0
-        self.num_requests = 0
-        self.conn_kw = conn_kw
-
-        if self.proxy:
-            # Enable Nagle's algorithm for proxies, to avoid packet fragmentation.
-            # We cannot know if the user has added default socket options, so we cannot replace the
-            # list.
-            self.conn_kw.setdefault('socket_options', [])
-
-    def _new_conn(self):
-        """
-        Return a fresh :class:`HTTPConnection`.
-        """
-        self.num_connections += 1
-        log.debug("Starting new HTTP connection (%d): %s:%s",
-                  self.num_connections, self.host, self.port or "80")
-
-        conn = self.ConnectionCls(host=self.host, port=self.port,
-                                  timeout=self.timeout.connect_timeout,
-                                  strict=self.strict, **self.conn_kw)
-        return conn
-
-    def _get_conn(self, timeout=None):
-        """
-        Get a connection. Will return a pooled connection if one is available.
-
-        If no connections are available and :prop:`.block` is ``False``, then a
-        fresh connection is returned.
-
-        :param timeout:
-            Seconds to wait before giving up and raising
-            :class:`urllib3.exceptions.EmptyPoolError` if the pool is empty and
-            :prop:`.block` is ``True``.
-        """
-        conn = None
-        try:
-            conn = self.pool.get(block=self.block, timeout=timeout)
-
-        except AttributeError:  # self.pool is None
-            raise ClosedPoolError(self, "Pool is closed.")
-
-        except queue.Empty:
-            if self.block:
-                raise EmptyPoolError(self,
-                                     "Pool reached maximum size and no more "
-                                     "connections are allowed.")
-            pass  # Oh well, we'll create a new connection then
-
-        # If this is a persistent connection, check if it got disconnected
-        if conn and is_connection_dropped(conn):
-            log.debug("Resetting dropped connection: %s", self.host)
-            conn.close()
-            if getattr(conn, 'auto_open', 1) == 0:
-                # This is a proxied connection that has been mutated by
-                # httplib._tunnel() and cannot be reused (since it would
-                # attempt to bypass the proxy)
-                conn = None
-
-        return conn or self._new_conn()
-
-    def _put_conn(self, conn):
-        """
-        Put a connection back into the pool.
-
-        :param conn:
-            Connection object for the current host and port as returned by
-            :meth:`._new_conn` or :meth:`._get_conn`.
-
-        If the pool is already full, the connection is closed and discarded
-        because we exceeded maxsize. If connections are discarded frequently,
-        then maxsize should be increased.
-
-        If the pool is closed, then the connection will be closed and discarded.
-        """
-        try:
-            self.pool.put(conn, block=False)
-            return  # Everything is dandy, done.
-        except AttributeError:
-            # self.pool is None.
-            pass
-        except queue.Full:
-            # This should never happen if self.block == True
-            log.warning(
-                "Connection pool is full, discarding connection: %s",
-                self.host)
-
-        # Connection never got put back into the pool, close it.
-        if conn:
-            conn.close()
-
-    def _validate_conn(self, conn):
-        """
-        Called right before a request is made, after the socket is created.
-        """
-        pass
-
-    def _prepare_proxy(self, conn):
-        # Nothing to do for HTTP connections.
-        pass
-
-    def _get_timeout(self, timeout):
-        """ Helper that always returns a :class:`urllib3.util.Timeout` """
-        if timeout is _Default:
-            return self.timeout.clone()
-
-        if isinstance(timeout, Timeout):
-            return timeout.clone()
-        else:
-            # User passed us an int/float. This is for backwards compatibility,
-            # can be removed later
-            return Timeout.from_float(timeout)
-
-    def _raise_timeout(self, err, url, timeout_value):
-        """Is the error actually a timeout? Will raise a ReadTimeout or pass"""
-
-        if isinstance(err, SocketTimeout):
-            raise ReadTimeoutError(self, url, "Read timed out. (read timeout=%s)" % timeout_value)
-
-        # See the above comment about EAGAIN in Python 3. In Python 2 we have
-        # to specifically catch it and throw the timeout error
-        if hasattr(err, 'errno') and err.errno in _blocking_errnos:
-            raise ReadTimeoutError(self, url, "Read timed out. (read timeout=%s)" % timeout_value)
-
-        # Catch possible read timeouts thrown as SSL errors. If not the
-        # case, rethrow the original. We need to do this because of:
-        # http://bugs.python.org/issue10272
-        if 'timed out' in str(err) or 'did not complete (read)' in str(err):  # Python < 2.7.4
-            raise ReadTimeoutError(self, url, "Read timed out. (read timeout=%s)" % timeout_value)
-
-    def _make_request(self, conn, method, url, timeout=_Default, chunked=False,
-                      **httplib_request_kw):
-        """
-        Perform a request on a given urllib connection object taken from our
-        pool.
-
-        :param conn:
-            a connection from one of our connection pools
-
-        :param timeout:
-            Socket timeout in seconds for the request. This can be a
-            float or integer, which will set the same timeout value for
-            the socket connect and the socket read, or an instance of
-            :class:`urllib3.util.Timeout`, which gives you more fine-grained
-            control over your timeouts.
-        """
-        self.num_requests += 1
-
-        timeout_obj = self._get_timeout(timeout)
-        timeout_obj.start_connect()
-        conn.timeout = timeout_obj.connect_timeout
-
-        # Trigger any extra validation we need to do.
-        try:
-            self._validate_conn(conn)
-        except (SocketTimeout, BaseSSLError) as e:
-            # Py2 raises this as a BaseSSLError, Py3 raises it as socket timeout.
-            self._raise_timeout(err=e, url=url, timeout_value=conn.timeout)
-            raise
-
-        # conn.request() calls httplib.*.request, not the method in
-        # urllib3.request. It also calls makefile (recv) on the socket.
-        if chunked:
-            conn.request_chunked(method, url, **httplib_request_kw)
-        else:
-            conn.request(method, url, **httplib_request_kw)
-
-        # Reset the timeout for the recv() on the socket
-        read_timeout = timeout_obj.read_timeout
-
-        # App Engine doesn't have a sock attr
-        if getattr(conn, 'sock', None):
-            # In Python 3 socket.py will catch EAGAIN and return None when you
-            # try and read into the file pointer created by http.client, which
-            # instead raises a BadStatusLine exception. Instead of catching
-            # the exception and assuming all BadStatusLine exceptions are read
-            # timeouts, check for a zero timeout before making the request.
-            if read_timeout == 0:
-                raise ReadTimeoutError(
-                    self, url, "Read timed out. (read timeout=%s)" % read_timeout)
-            if read_timeout is Timeout.DEFAULT_TIMEOUT:
-                conn.sock.settimeout(socket.getdefaulttimeout())
-            else:  # None or a value
-                conn.sock.settimeout(read_timeout)
-
-        # Receive the response from the server
-        try:
-            try:  # Python 2.7, use buffering of HTTP responses
-                httplib_response = conn.getresponse(buffering=True)
-            except TypeError:  # Python 3
-                try:
-                    httplib_response = conn.getresponse()
-                except Exception as e:
-                    # Remove the TypeError from the exception chain in Python 3;
-                    # otherwise it looks like a programming error was the cause.
-                    six.raise_from(e, None)
-        except (SocketTimeout, BaseSSLError, SocketError) as e:
-            self._raise_timeout(err=e, url=url, timeout_value=read_timeout)
-            raise
-
-        # AppEngine doesn't have a version attr.
-        http_version = getattr(conn, '_http_vsn_str', 'HTTP/?')
-        log.debug("%s://%s:%s \"%s %s %s\" %s %s", self.scheme, self.host, self.port,
-                  method, url, http_version, httplib_response.status,
-                  httplib_response.length)
-
-        try:
-            assert_header_parsing(httplib_response.msg)
-        except (HeaderParsingError, TypeError) as hpe:  # Platform-specific: Python 3
-            log.warning(
-                'Failed to parse headers (url=%s): %s',
-                self._absolute_url(url), hpe, exc_info=True)
-
-        return httplib_response
-
-    def _absolute_url(self, path):
-        return Url(scheme=self.scheme, host=self.host, port=self.port, path=path).url
-
-    def close(self):
-        """
-        Close all pooled connections and disable the pool.
-        """
-        if self.pool is None:
-            return
-        # Disable access to the pool
-        old_pool, self.pool = self.pool, None
-
-        try:
-            while True:
-                conn = old_pool.get(block=False)
-                if conn:
-                    conn.close()
-
-        except queue.Empty:
-            pass  # Done.
-
-    def is_same_host(self, url):
-        """
-        Check if the given ``url`` is a member of the same host as this
-        connection pool.
-        """
-        if url.startswith('/'):
-            return True
-
-        # TODO: Add optional support for socket.gethostbyname checking.
-        scheme, host, port = get_host(url)
-
-        host = _ipv6_host(host, self.scheme)
-
-        # Use explicit default port for comparison when none is given
-        if self.port and not port:
-            port = port_by_scheme.get(scheme)
-        elif not self.port and port == port_by_scheme.get(scheme):
-            port = None
-
-        return (scheme, host, port) == (self.scheme, self.host, self.port)
-
-    def urlopen(self, method, url, body=None, headers=None, retries=None,
-                redirect=True, assert_same_host=True, timeout=_Default,
-                pool_timeout=None, release_conn=None, chunked=False,
-                body_pos=None, **response_kw):
-        """
-        Get a connection from the pool and perform an HTTP request. This is the
-        lowest level call for making a request, so you'll need to specify all
-        the raw details.
-
-        .. note::
-
-           More commonly, it's appropriate to use a convenience method provided
-           by :class:`.RequestMethods`, such as :meth:`request`.
-
-        .. note::
-
-           `release_conn` will only behave as expected if
-           `preload_content=False` because we want to make
-           `preload_content=False` the default behaviour someday soon without
-           breaking backwards compatibility.
-
-        :param method:
-            HTTP request method (such as GET, POST, PUT, etc.)
-
-        :param body:
-            Data to send in the request body (useful for creating
-            POST requests, see HTTPConnectionPool.post_url for
-            more convenience).
-
-        :param headers:
-            Dictionary of custom headers to send, such as User-Agent,
-            If-None-Match, etc. If None, pool headers are used. If provided,
-            these headers completely replace any pool-specific headers.
-
-        :param retries:
-            Configure the number of retries to allow before raising a
-            :class:`~urllib3.exceptions.MaxRetryError` exception.
-
-            Pass ``None`` to retry until you receive a response. Pass a
-            :class:`~urllib3.util.retry.Retry` object for fine-grained control
-            over different types of retries.
-            Pass an integer number to retry connection errors that many times,
-            but no other types of errors. Pass zero to never retry.
-
-            If ``False``, then retries are disabled and any exception is raised
-            immediately. Also, instead of raising a MaxRetryError on redirects,
-            the redirect response will be returned.
-
-        :type retries: :class:`~urllib3.util.retry.Retry`, False, or an int.
-
-        :param redirect:
-            If True, automatically handle redirects (status codes 301, 302,
-            303, 307, 308). Each redirect counts as a retry. Disabling retries
-            will disable redirect, too.
-
-        :param assert_same_host:
-            If ``True``, will make sure that the host of the pool requests is
-            consistent else will raise HostChangedError. When False, you can
-            use the pool on an HTTP proxy and request foreign hosts.
-
-        :param timeout:
-            If specified, overrides the default timeout for this one
-            request. It may be a float (in seconds) or an instance of
-            :class:`urllib3.util.Timeout`.
-
-        :param pool_timeout:
-            If set and the pool is set to block=True, then this method will
-            block for ``pool_timeout`` seconds and raise EmptyPoolError if no
-            connection is available within the time period.
-
-        :param release_conn:
-            If False, then the urlopen call will not release the connection
-            back into the pool once a response is received (but will release if
-            you read the entire contents of the response such as when
-            `preload_content=True`). This is useful if you're not preloading
-            the response's content immediately. You will need to call
-            ``r.release_conn()`` on the response ``r`` to return the connection
-            back into the pool. If None, it takes the value of
-            ``response_kw.get('preload_content', True)``.
-
-        :param chunked:
-            If True, urllib3 will send the body using chunked transfer
-            encoding. Otherwise, urllib3 will send the body using the standard
-            content-length form. Defaults to False.
-
-        :param int body_pos:
-            Position to seek to in file-like body in the event of a retry or
-            redirect. Typically this won't need to be set because urllib3 will
-            auto-populate the value when needed.
-
-        :param \\**response_kw:
-            Additional parameters are passed to
-            :meth:`urllib3.response.HTTPResponse.from_httplib`
-        """
-        if headers is None:
-            headers = self.headers
-
-        if not isinstance(retries, Retry):
-            retries = Retry.from_int(retries, redirect=redirect, default=self.retries)
-
-        if release_conn is None:
-            release_conn = response_kw.get('preload_content', True)
-
-        # Check host
-        if assert_same_host and not self.is_same_host(url):
-            raise HostChangedError(self, url, retries)
-
-        conn = None
-
-        # Track whether `conn` needs to be released before
-        # returning/raising/recursing. Update this variable if necessary, and
-        # leave `release_conn` constant throughout the function. That way, if
-        # the function recurses, the original value of `release_conn` will be
-        # passed down into the recursive call, and its value will be respected.
-        #
-        # See issue #651 [1] for details.
-        #
-        # [1] <https://github.com/shazow/urllib3/issues/651>
-        release_this_conn = release_conn
-
-        # Merge the proxy headers. Only do this in HTTP. We have to copy the
-        # headers dict so we can safely change it without those changes being
-        # reflected in anyone else's copy.
-        if self.scheme == 'http':
-            headers = headers.copy()
-            headers.update(self.proxy_headers)
-
-        # Must keep the exception bound to a separate variable or else Python 3
-        # complains about UnboundLocalError.
-        err = None
-
-        # Keep track of whether we cleanly exited the except block. This
-        # ensures we do proper cleanup in finally.
-        clean_exit = False
-
-        # Rewind body position, if needed. Record current position
-        # for future rewinds in the event of a redirect/retry.
-        body_pos = set_file_position(body, body_pos)
-
-        try:
-            # Request a connection from the queue.
-            timeout_obj = self._get_timeout(timeout)
-            conn = self._get_conn(timeout=pool_timeout)
-
-            conn.timeout = timeout_obj.connect_timeout
-
-            is_new_proxy_conn = self.proxy is not None and not getattr(conn, 'sock', None)
-            if is_new_proxy_conn:
-                self._prepare_proxy(conn)
-
-            # Make the request on the httplib connection object.
-            httplib_response = self._make_request(conn, method, url,
-                                                  timeout=timeout_obj,
-                                                  body=body, headers=headers,
-                                                  chunked=chunked)
-
-            # If we're going to release the connection in ``finally:``, then
-            # the response doesn't need to know about the connection. Otherwise
-            # it will also try to release it and we'll have a double-release
-            # mess.
-            response_conn = conn if not release_conn else None
-
-            # Pass method to Response for length checking
-            response_kw['request_method'] = method
-
-            # Import httplib's response into our own wrapper object
-            response = self.ResponseCls.from_httplib(httplib_response,
-                                                     pool=self,
-                                                     connection=response_conn,
-                                                     retries=retries,
-                                                     **response_kw)
-
-            # Everything went great!
-            clean_exit = True
-
-        except queue.Empty:
-            # Timed out by queue.
-            raise EmptyPoolError(self, "No pool connections are available.")
-
-        except (TimeoutError, HTTPException, SocketError, ProtocolError,
-                BaseSSLError, SSLError, CertificateError) as e:
-            # Discard the connection for these exceptions. It will be
-            # replaced during the next _get_conn() call.
-            clean_exit = False
-            if isinstance(e, (BaseSSLError, CertificateError)):
-                e = SSLError(e)
-            elif isinstance(e, (SocketError, NewConnectionError)) and self.proxy:
-                e = ProxyError('Cannot connect to proxy.', e)
-            elif isinstance(e, (SocketError, HTTPException)):
-                e = ProtocolError('Connection aborted.', e)
-
-            retries = retries.increment(method, url, error=e, _pool=self,
-                                        _stacktrace=sys.exc_info()[2])
-            retries.sleep()
-
-            # Keep track of the error for the retry warning.
-            err = e
-
-        finally:
-            if not clean_exit:
-                # We hit some kind of exception, handled or otherwise. We need
-                # to throw the connection away unless explicitly told not to.
-                # Close the connection, set the variable to None, and make sure
-                # we put the None back in the pool to avoid leaking it.
-                conn = conn and conn.close()
-                release_this_conn = True
-
-            if release_this_conn:
-                # Put the connection back to be reused. If the connection is
-                # expired then it will be None, which will get replaced with a
-                # fresh connection during _get_conn.
-                self._put_conn(conn)
-
-        if not conn:
-            # Try again
-            log.warning("Retrying (%r) after connection "
-                        "broken by '%r': %s", retries, err, url)
-            return self.urlopen(method, url, body, headers, retries,
-                                redirect, assert_same_host,
-                                timeout=timeout, pool_timeout=pool_timeout,
-                                release_conn=release_conn, body_pos=body_pos,
-                                **response_kw)
-
-        def drain_and_release_conn(response):
-            try:
-                # discard any remaining response body, the connection will be
-                # released back to the pool once the entire response is read
-                response.read()
-            except (TimeoutError, HTTPException, SocketError, ProtocolError,
-                    BaseSSLError, SSLError) as e:
-                pass
-
-        # Handle redirect?
-        redirect_location = redirect and response.get_redirect_location()
-        if redirect_location:
-            if response.status == 303:
-                method = 'GET'
-
-            try:
-                retries = retries.increment(method, url, response=response, _pool=self)
-            except MaxRetryError:
-                if retries.raise_on_redirect:
-                    # Drain and release the connection for this response, since
-                    # we're not returning it to be released manually.
-                    drain_and_release_conn(response)
-                    raise
-                return response
-
-            # drain and return the connection to the pool before recursing
-            drain_and_release_conn(response)
-
-            retries.sleep_for_retry(response)
-            log.debug("Redirecting %s -> %s", url, redirect_location)
-            return self.urlopen(
-                method, redirect_location, body, headers,
-                retries=retries, redirect=redirect,
-                assert_same_host=assert_same_host,
-                timeout=timeout, pool_timeout=pool_timeout,
-                release_conn=release_conn, body_pos=body_pos,
-                **response_kw)
-
-        # Check if we should retry the HTTP response.
-        has_retry_after = bool(response.getheader('Retry-After'))
-        if retries.is_retry(method, response.status, has_retry_after):
-            try:
-                retries = retries.increment(method, url, response=response, _pool=self)
-            except MaxRetryError:
-                if retries.raise_on_status:
-                    # Drain and release the connection for this response, since
-                    # we're not returning it to be released manually.
-                    drain_and_release_conn(response)
-                    raise
-                return response
-
-            # drain and return the connection to the pool before recursing
-            drain_and_release_conn(response)
-
-            retries.sleep(response)
-            log.debug("Retry: %s", url)
-            return self.urlopen(
-                method, url, body, headers,
-                retries=retries, redirect=redirect,
-                assert_same_host=assert_same_host,
-                timeout=timeout, pool_timeout=pool_timeout,
-                release_conn=release_conn,
-                body_pos=body_pos, **response_kw)
-
-        return response
-
-
-class HTTPSConnectionPool(HTTPConnectionPool):
-    """
-    Same as :class:`.HTTPConnectionPool`, but HTTPS.
-
-    When Python is compiled with the :mod:`ssl` module, then
-    :class:`.VerifiedHTTPSConnection` is used, which *can* verify certificates,
-    instead of :class:`.HTTPSConnection`.
-
-    :class:`.VerifiedHTTPSConnection` uses one of ``assert_fingerprint``,
-    ``assert_hostname`` and ``host`` in this order to verify connections.
-    If ``assert_hostname`` is False, no verification is done.
-
-    The ``key_file``, ``cert_file``, ``cert_reqs``, ``ca_certs``,
-    ``ca_cert_dir``, and ``ssl_version`` are only used if :mod:`ssl` is
-    available and are fed into :meth:`urllib3.util.ssl_wrap_socket` to upgrade
-    the connection socket into an SSL socket.
-    """
-
-    scheme = 'https'
-    ConnectionCls = HTTPSConnection
-
-    def __init__(self, host, port=None,
-                 strict=False, timeout=Timeout.DEFAULT_TIMEOUT, maxsize=1,
-                 block=False, headers=None, retries=None,
-                 _proxy=None, _proxy_headers=None,
-                 key_file=None, cert_file=None, cert_reqs=None,
-                 ca_certs=None, ssl_version=None,
-                 assert_hostname=None, assert_fingerprint=None,
-                 ca_cert_dir=None, **conn_kw):
-
-        HTTPConnectionPool.__init__(self, host, port, strict, timeout, maxsize,
-                                    block, headers, retries, _proxy, _proxy_headers,
-                                    **conn_kw)
-
-        if ca_certs and cert_reqs is None:
-            cert_reqs = 'CERT_REQUIRED'
-
-        self.key_file = key_file
-        self.cert_file = cert_file
-        self.cert_reqs = cert_reqs
-        self.ca_certs = ca_certs
-        self.ca_cert_dir = ca_cert_dir
-        self.ssl_version = ssl_version
-        self.assert_hostname = assert_hostname
-        self.assert_fingerprint = assert_fingerprint
-
-    def _prepare_conn(self, conn):
-        """
-        Prepare the ``connection`` for :meth:`urllib3.util.ssl_wrap_socket`
-        and establish the tunnel if proxy is used.
-        """
-
-        if isinstance(conn, VerifiedHTTPSConnection):
-            conn.set_cert(key_file=self.key_file,
-                          cert_file=self.cert_file,
-                          cert_reqs=self.cert_reqs,
-                          ca_certs=self.ca_certs,
-                          ca_cert_dir=self.ca_cert_dir,
-                          assert_hostname=self.assert_hostname,
-                          assert_fingerprint=self.assert_fingerprint)
-            conn.ssl_version = self.ssl_version
-        return conn
-
-    def _prepare_proxy(self, conn):
-        """
-        Establish tunnel connection early, because otherwise httplib
-        would improperly set Host: header to proxy's IP:port.
-        """
-        conn.set_tunnel(self._proxy_host, self.port, self.proxy_headers)
-        conn.connect()
-
-    def _new_conn(self):
-        """
-        Return a fresh :class:`httplib.HTTPSConnection`.
-        """
-        self.num_connections += 1
-        log.debug("Starting new HTTPS connection (%d): %s:%s",
-                  self.num_connections, self.host, self.port or "443")
-
-        if not self.ConnectionCls or self.ConnectionCls is DummyConnection:
-            raise SSLError("Can't connect to HTTPS URL because the SSL "
-                           "module is not available.")
-
-        actual_host = self.host
-        actual_port = self.port
-        if self.proxy is not None:
-            actual_host = self.proxy.host
-            actual_port = self.proxy.port
-
-        conn = self.ConnectionCls(host=actual_host, port=actual_port,
-                                  timeout=self.timeout.connect_timeout,
-                                  strict=self.strict, **self.conn_kw)
-
-        return self._prepare_conn(conn)
-
-    def _validate_conn(self, conn):
-        """
-        Called right before a request is made, after the socket is created.
-        """
-        super(HTTPSConnectionPool, self)._validate_conn(conn)
-
-        # Force connect early to allow us to validate the connection.
-        if not getattr(conn, 'sock', None):  # AppEngine might not have  `.sock`
-            conn.connect()
-
-        if not conn.is_verified:
-            warnings.warn((
-                'Unverified HTTPS request is being made. '
-                'Adding certificate verification is strongly advised. See: '
-                'https://urllib3.readthedocs.io/en/latest/advanced-usage.html'
-                '#ssl-warnings'),
-                InsecureRequestWarning)
-
-
-def connection_from_url(url, **kw):
-    """
-    Given a url, return an :class:`.ConnectionPool` instance of its host.
-
-    This is a shortcut for not having to parse out the scheme, host, and port
-    of the url before creating an :class:`.ConnectionPool` instance.
-
-    :param url:
-        Absolute URL string that must include the scheme. Port is optional.
-
-    :param \\**kw:
-        Passes additional parameters to the constructor of the appropriate
-        :class:`.ConnectionPool`. Useful for specifying things like
-        timeout, maxsize, headers, etc.
-
-    Example::
-
-        >>> conn = connection_from_url('http://google.com/')
-        >>> r = conn.request('GET', '/')
-    """
-    scheme, host, port = get_host(url)
-    port = port or port_by_scheme.get(scheme, 80)
-    if scheme == 'https':
-        return HTTPSConnectionPool(host, port=port, **kw)
-    else:
-        return HTTPConnectionPool(host, port=port, **kw)
-
-
-def _ipv6_host(host, scheme):
-    """
-    Process IPv6 address literals
-    """
-
-    # httplib doesn't like it when we include brackets in IPv6 addresses
-    # Specifically, if we include brackets but also pass the port then
-    # httplib crazily doubles up the square brackets on the Host header.
-    # Instead, we need to make sure we never pass ``None`` as the port.
-    # However, for backward compatibility reasons we can't actually
-    # *assert* that.  See http://bugs.python.org/issue28539
-    #
-    # Also if an IPv6 address literal has a zone identifier, the
-    # percent sign might be URIencoded, convert it back into ASCII
-    if host.startswith('[') and host.endswith(']'):
-        host = host.replace('%25', '%').strip('[]')
-    if scheme in NORMALIZABLE_SCHEMES:
-        host = host.lower()
-    return host
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__init__.py
deleted file mode 100644
index e69de29..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__init__.py
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 560347f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/_appengine_environ.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/_appengine_environ.cpython-37.pyc
deleted file mode 100644
index e23a2e0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/_appengine_environ.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/socks.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/socks.cpython-37.pyc
deleted file mode 100644
index 73a6831..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/__pycache__/socks.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_appengine_environ.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_appengine_environ.py
deleted file mode 100644
index f3e0094..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_appengine_environ.py
+++ /dev/null
@@ -1,30 +0,0 @@
-"""
-This module provides means to detect the App Engine environment.
-"""
-
-import os
-
-
-def is_appengine():
-    return (is_local_appengine() or
-            is_prod_appengine() or
-            is_prod_appengine_mvms())
-
-
-def is_appengine_sandbox():
-    return is_appengine() and not is_prod_appengine_mvms()
-
-
-def is_local_appengine():
-    return ('APPENGINE_RUNTIME' in os.environ and
-            'Development/' in os.environ['SERVER_SOFTWARE'])
-
-
-def is_prod_appengine():
-    return ('APPENGINE_RUNTIME' in os.environ and
-            'Google App Engine/' in os.environ['SERVER_SOFTWARE'] and
-            not is_prod_appengine_mvms())
-
-
-def is_prod_appengine_mvms():
-    return os.environ.get('GAE_VM', False) == 'true'
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/__init__.py
deleted file mode 100644
index e69de29..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/__init__.py
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/bindings.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/bindings.py
deleted file mode 100644
index bcf41c0..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/bindings.py
+++ /dev/null
@@ -1,593 +0,0 @@
-"""
-This module uses ctypes to bind a whole bunch of functions and constants from
-SecureTransport. The goal here is to provide the low-level API to
-SecureTransport. These are essentially the C-level functions and constants, and
-they're pretty gross to work with.
-
-This code is a bastardised version of the code found in Will Bond's oscrypto
-library. An enormous debt is owed to him for blazing this trail for us. For
-that reason, this code should be considered to be covered both by urllib3's
-license and by oscrypto's:
-
-    Copyright (c) 2015-2016 Will Bond <will@wbond.net>
-
-    Permission is hereby granted, free of charge, to any person obtaining a
-    copy of this software and associated documentation files (the "Software"),
-    to deal in the Software without restriction, including without limitation
-    the rights to use, copy, modify, merge, publish, distribute, sublicense,
-    and/or sell copies of the Software, and to permit persons to whom the
-    Software is furnished to do so, subject to the following conditions:
-
-    The above copyright notice and this permission notice shall be included in
-    all copies or substantial portions of the Software.
-
-    THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR
-    IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF MERCHANTABILITY,
-    FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL THE
-    AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER
-    LIABILITY, WHETHER IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING
-    FROM, OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR OTHER
-    DEALINGS IN THE SOFTWARE.
-"""
-from __future__ import absolute_import
-
-import platform
-from ctypes.util import find_library
-from ctypes import (
-    c_void_p, c_int32, c_char_p, c_size_t, c_byte, c_uint32, c_ulong, c_long,
-    c_bool
-)
-from ctypes import CDLL, POINTER, CFUNCTYPE
-
-
-security_path = find_library('Security')
-if not security_path:
-    raise ImportError('The library Security could not be found')
-
-
-core_foundation_path = find_library('CoreFoundation')
-if not core_foundation_path:
-    raise ImportError('The library CoreFoundation could not be found')
-
-
-version = platform.mac_ver()[0]
-version_info = tuple(map(int, version.split('.')))
-if version_info < (10, 8):
-    raise OSError(
-        'Only OS X 10.8 and newer are supported, not %s.%s' % (
-            version_info[0], version_info[1]
-        )
-    )
-
-Security = CDLL(security_path, use_errno=True)
-CoreFoundation = CDLL(core_foundation_path, use_errno=True)
-
-Boolean = c_bool
-CFIndex = c_long
-CFStringEncoding = c_uint32
-CFData = c_void_p
-CFString = c_void_p
-CFArray = c_void_p
-CFMutableArray = c_void_p
-CFDictionary = c_void_p
-CFError = c_void_p
-CFType = c_void_p
-CFTypeID = c_ulong
-
-CFTypeRef = POINTER(CFType)
-CFAllocatorRef = c_void_p
-
-OSStatus = c_int32
-
-CFDataRef = POINTER(CFData)
-CFStringRef = POINTER(CFString)
-CFArrayRef = POINTER(CFArray)
-CFMutableArrayRef = POINTER(CFMutableArray)
-CFDictionaryRef = POINTER(CFDictionary)
-CFArrayCallBacks = c_void_p
-CFDictionaryKeyCallBacks = c_void_p
-CFDictionaryValueCallBacks = c_void_p
-
-SecCertificateRef = POINTER(c_void_p)
-SecExternalFormat = c_uint32
-SecExternalItemType = c_uint32
-SecIdentityRef = POINTER(c_void_p)
-SecItemImportExportFlags = c_uint32
-SecItemImportExportKeyParameters = c_void_p
-SecKeychainRef = POINTER(c_void_p)
-SSLProtocol = c_uint32
-SSLCipherSuite = c_uint32
-SSLContextRef = POINTER(c_void_p)
-SecTrustRef = POINTER(c_void_p)
-SSLConnectionRef = c_uint32
-SecTrustResultType = c_uint32
-SecTrustOptionFlags = c_uint32
-SSLProtocolSide = c_uint32
-SSLConnectionType = c_uint32
-SSLSessionOption = c_uint32
-
-
-try:
-    Security.SecItemImport.argtypes = [
-        CFDataRef,
-        CFStringRef,
-        POINTER(SecExternalFormat),
-        POINTER(SecExternalItemType),
-        SecItemImportExportFlags,
-        POINTER(SecItemImportExportKeyParameters),
-        SecKeychainRef,
-        POINTER(CFArrayRef),
-    ]
-    Security.SecItemImport.restype = OSStatus
-
-    Security.SecCertificateGetTypeID.argtypes = []
-    Security.SecCertificateGetTypeID.restype = CFTypeID
-
-    Security.SecIdentityGetTypeID.argtypes = []
-    Security.SecIdentityGetTypeID.restype = CFTypeID
-
-    Security.SecKeyGetTypeID.argtypes = []
-    Security.SecKeyGetTypeID.restype = CFTypeID
-
-    Security.SecCertificateCreateWithData.argtypes = [
-        CFAllocatorRef,
-        CFDataRef
-    ]
-    Security.SecCertificateCreateWithData.restype = SecCertificateRef
-
-    Security.SecCertificateCopyData.argtypes = [
-        SecCertificateRef
-    ]
-    Security.SecCertificateCopyData.restype = CFDataRef
-
-    Security.SecCopyErrorMessageString.argtypes = [
-        OSStatus,
-        c_void_p
-    ]
-    Security.SecCopyErrorMessageString.restype = CFStringRef
-
-    Security.SecIdentityCreateWithCertificate.argtypes = [
-        CFTypeRef,
-        SecCertificateRef,
-        POINTER(SecIdentityRef)
-    ]
-    Security.SecIdentityCreateWithCertificate.restype = OSStatus
-
-    Security.SecKeychainCreate.argtypes = [
-        c_char_p,
-        c_uint32,
-        c_void_p,
-        Boolean,
-        c_void_p,
-        POINTER(SecKeychainRef)
-    ]
-    Security.SecKeychainCreate.restype = OSStatus
-
-    Security.SecKeychainDelete.argtypes = [
-        SecKeychainRef
-    ]
-    Security.SecKeychainDelete.restype = OSStatus
-
-    Security.SecPKCS12Import.argtypes = [
-        CFDataRef,
-        CFDictionaryRef,
-        POINTER(CFArrayRef)
-    ]
-    Security.SecPKCS12Import.restype = OSStatus
-
-    SSLReadFunc = CFUNCTYPE(OSStatus, SSLConnectionRef, c_void_p, POINTER(c_size_t))
-    SSLWriteFunc = CFUNCTYPE(OSStatus, SSLConnectionRef, POINTER(c_byte), POINTER(c_size_t))
-
-    Security.SSLSetIOFuncs.argtypes = [
-        SSLContextRef,
-        SSLReadFunc,
-        SSLWriteFunc
-    ]
-    Security.SSLSetIOFuncs.restype = OSStatus
-
-    Security.SSLSetPeerID.argtypes = [
-        SSLContextRef,
-        c_char_p,
-        c_size_t
-    ]
-    Security.SSLSetPeerID.restype = OSStatus
-
-    Security.SSLSetCertificate.argtypes = [
-        SSLContextRef,
-        CFArrayRef
-    ]
-    Security.SSLSetCertificate.restype = OSStatus
-
-    Security.SSLSetCertificateAuthorities.argtypes = [
-        SSLContextRef,
-        CFTypeRef,
-        Boolean
-    ]
-    Security.SSLSetCertificateAuthorities.restype = OSStatus
-
-    Security.SSLSetConnection.argtypes = [
-        SSLContextRef,
-        SSLConnectionRef
-    ]
-    Security.SSLSetConnection.restype = OSStatus
-
-    Security.SSLSetPeerDomainName.argtypes = [
-        SSLContextRef,
-        c_char_p,
-        c_size_t
-    ]
-    Security.SSLSetPeerDomainName.restype = OSStatus
-
-    Security.SSLHandshake.argtypes = [
-        SSLContextRef
-    ]
-    Security.SSLHandshake.restype = OSStatus
-
-    Security.SSLRead.argtypes = [
-        SSLContextRef,
-        c_char_p,
-        c_size_t,
-        POINTER(c_size_t)
-    ]
-    Security.SSLRead.restype = OSStatus
-
-    Security.SSLWrite.argtypes = [
-        SSLContextRef,
-        c_char_p,
-        c_size_t,
-        POINTER(c_size_t)
-    ]
-    Security.SSLWrite.restype = OSStatus
-
-    Security.SSLClose.argtypes = [
-        SSLContextRef
-    ]
-    Security.SSLClose.restype = OSStatus
-
-    Security.SSLGetNumberSupportedCiphers.argtypes = [
-        SSLContextRef,
-        POINTER(c_size_t)
-    ]
-    Security.SSLGetNumberSupportedCiphers.restype = OSStatus
-
-    Security.SSLGetSupportedCiphers.argtypes = [
-        SSLContextRef,
-        POINTER(SSLCipherSuite),
-        POINTER(c_size_t)
-    ]
-    Security.SSLGetSupportedCiphers.restype = OSStatus
-
-    Security.SSLSetEnabledCiphers.argtypes = [
-        SSLContextRef,
-        POINTER(SSLCipherSuite),
-        c_size_t
-    ]
-    Security.SSLSetEnabledCiphers.restype = OSStatus
-
-    Security.SSLGetNumberEnabledCiphers.argtype = [
-        SSLContextRef,
-        POINTER(c_size_t)
-    ]
-    Security.SSLGetNumberEnabledCiphers.restype = OSStatus
-
-    Security.SSLGetEnabledCiphers.argtypes = [
-        SSLContextRef,
-        POINTER(SSLCipherSuite),
-        POINTER(c_size_t)
-    ]
-    Security.SSLGetEnabledCiphers.restype = OSStatus
-
-    Security.SSLGetNegotiatedCipher.argtypes = [
-        SSLContextRef,
-        POINTER(SSLCipherSuite)
-    ]
-    Security.SSLGetNegotiatedCipher.restype = OSStatus
-
-    Security.SSLGetNegotiatedProtocolVersion.argtypes = [
-        SSLContextRef,
-        POINTER(SSLProtocol)
-    ]
-    Security.SSLGetNegotiatedProtocolVersion.restype = OSStatus
-
-    Security.SSLCopyPeerTrust.argtypes = [
-        SSLContextRef,
-        POINTER(SecTrustRef)
-    ]
-    Security.SSLCopyPeerTrust.restype = OSStatus
-
-    Security.SecTrustSetAnchorCertificates.argtypes = [
-        SecTrustRef,
-        CFArrayRef
-    ]
-    Security.SecTrustSetAnchorCertificates.restype = OSStatus
-
-    Security.SecTrustSetAnchorCertificatesOnly.argstypes = [
-        SecTrustRef,
-        Boolean
-    ]
-    Security.SecTrustSetAnchorCertificatesOnly.restype = OSStatus
-
-    Security.SecTrustEvaluate.argtypes = [
-        SecTrustRef,
-        POINTER(SecTrustResultType)
-    ]
-    Security.SecTrustEvaluate.restype = OSStatus
-
-    Security.SecTrustGetCertificateCount.argtypes = [
-        SecTrustRef
-    ]
-    Security.SecTrustGetCertificateCount.restype = CFIndex
-
-    Security.SecTrustGetCertificateAtIndex.argtypes = [
-        SecTrustRef,
-        CFIndex
-    ]
-    Security.SecTrustGetCertificateAtIndex.restype = SecCertificateRef
-
-    Security.SSLCreateContext.argtypes = [
-        CFAllocatorRef,
-        SSLProtocolSide,
-        SSLConnectionType
-    ]
-    Security.SSLCreateContext.restype = SSLContextRef
-
-    Security.SSLSetSessionOption.argtypes = [
-        SSLContextRef,
-        SSLSessionOption,
-        Boolean
-    ]
-    Security.SSLSetSessionOption.restype = OSStatus
-
-    Security.SSLSetProtocolVersionMin.argtypes = [
-        SSLContextRef,
-        SSLProtocol
-    ]
-    Security.SSLSetProtocolVersionMin.restype = OSStatus
-
-    Security.SSLSetProtocolVersionMax.argtypes = [
-        SSLContextRef,
-        SSLProtocol
-    ]
-    Security.SSLSetProtocolVersionMax.restype = OSStatus
-
-    Security.SecCopyErrorMessageString.argtypes = [
-        OSStatus,
-        c_void_p
-    ]
-    Security.SecCopyErrorMessageString.restype = CFStringRef
-
-    Security.SSLReadFunc = SSLReadFunc
-    Security.SSLWriteFunc = SSLWriteFunc
-    Security.SSLContextRef = SSLContextRef
-    Security.SSLProtocol = SSLProtocol
-    Security.SSLCipherSuite = SSLCipherSuite
-    Security.SecIdentityRef = SecIdentityRef
-    Security.SecKeychainRef = SecKeychainRef
-    Security.SecTrustRef = SecTrustRef
-    Security.SecTrustResultType = SecTrustResultType
-    Security.SecExternalFormat = SecExternalFormat
-    Security.OSStatus = OSStatus
-
-    Security.kSecImportExportPassphrase = CFStringRef.in_dll(
-        Security, 'kSecImportExportPassphrase'
-    )
-    Security.kSecImportItemIdentity = CFStringRef.in_dll(
-        Security, 'kSecImportItemIdentity'
-    )
-
-    # CoreFoundation time!
-    CoreFoundation.CFRetain.argtypes = [
-        CFTypeRef
-    ]
-    CoreFoundation.CFRetain.restype = CFTypeRef
-
-    CoreFoundation.CFRelease.argtypes = [
-        CFTypeRef
-    ]
-    CoreFoundation.CFRelease.restype = None
-
-    CoreFoundation.CFGetTypeID.argtypes = [
-        CFTypeRef
-    ]
-    CoreFoundation.CFGetTypeID.restype = CFTypeID
-
-    CoreFoundation.CFStringCreateWithCString.argtypes = [
-        CFAllocatorRef,
-        c_char_p,
-        CFStringEncoding
-    ]
-    CoreFoundation.CFStringCreateWithCString.restype = CFStringRef
-
-    CoreFoundation.CFStringGetCStringPtr.argtypes = [
-        CFStringRef,
-        CFStringEncoding
-    ]
-    CoreFoundation.CFStringGetCStringPtr.restype = c_char_p
-
-    CoreFoundation.CFStringGetCString.argtypes = [
-        CFStringRef,
-        c_char_p,
-        CFIndex,
-        CFStringEncoding
-    ]
-    CoreFoundation.CFStringGetCString.restype = c_bool
-
-    CoreFoundation.CFDataCreate.argtypes = [
-        CFAllocatorRef,
-        c_char_p,
-        CFIndex
-    ]
-    CoreFoundation.CFDataCreate.restype = CFDataRef
-
-    CoreFoundation.CFDataGetLength.argtypes = [
-        CFDataRef
-    ]
-    CoreFoundation.CFDataGetLength.restype = CFIndex
-
-    CoreFoundation.CFDataGetBytePtr.argtypes = [
-        CFDataRef
-    ]
-    CoreFoundation.CFDataGetBytePtr.restype = c_void_p
-
-    CoreFoundation.CFDictionaryCreate.argtypes = [
-        CFAllocatorRef,
-        POINTER(CFTypeRef),
-        POINTER(CFTypeRef),
-        CFIndex,
-        CFDictionaryKeyCallBacks,
-        CFDictionaryValueCallBacks
-    ]
-    CoreFoundation.CFDictionaryCreate.restype = CFDictionaryRef
-
-    CoreFoundation.CFDictionaryGetValue.argtypes = [
-        CFDictionaryRef,
-        CFTypeRef
-    ]
-    CoreFoundation.CFDictionaryGetValue.restype = CFTypeRef
-
-    CoreFoundation.CFArrayCreate.argtypes = [
-        CFAllocatorRef,
-        POINTER(CFTypeRef),
-        CFIndex,
-        CFArrayCallBacks,
-    ]
-    CoreFoundation.CFArrayCreate.restype = CFArrayRef
-
-    CoreFoundation.CFArrayCreateMutable.argtypes = [
-        CFAllocatorRef,
-        CFIndex,
-        CFArrayCallBacks
-    ]
-    CoreFoundation.CFArrayCreateMutable.restype = CFMutableArrayRef
-
-    CoreFoundation.CFArrayAppendValue.argtypes = [
-        CFMutableArrayRef,
-        c_void_p
-    ]
-    CoreFoundation.CFArrayAppendValue.restype = None
-
-    CoreFoundation.CFArrayGetCount.argtypes = [
-        CFArrayRef
-    ]
-    CoreFoundation.CFArrayGetCount.restype = CFIndex
-
-    CoreFoundation.CFArrayGetValueAtIndex.argtypes = [
-        CFArrayRef,
-        CFIndex
-    ]
-    CoreFoundation.CFArrayGetValueAtIndex.restype = c_void_p
-
-    CoreFoundation.kCFAllocatorDefault = CFAllocatorRef.in_dll(
-        CoreFoundation, 'kCFAllocatorDefault'
-    )
-    CoreFoundation.kCFTypeArrayCallBacks = c_void_p.in_dll(CoreFoundation, 'kCFTypeArrayCallBacks')
-    CoreFoundation.kCFTypeDictionaryKeyCallBacks = c_void_p.in_dll(
-        CoreFoundation, 'kCFTypeDictionaryKeyCallBacks'
-    )
-    CoreFoundation.kCFTypeDictionaryValueCallBacks = c_void_p.in_dll(
-        CoreFoundation, 'kCFTypeDictionaryValueCallBacks'
-    )
-
-    CoreFoundation.CFTypeRef = CFTypeRef
-    CoreFoundation.CFArrayRef = CFArrayRef
-    CoreFoundation.CFStringRef = CFStringRef
-    CoreFoundation.CFDictionaryRef = CFDictionaryRef
-
-except (AttributeError):
-    raise ImportError('Error initializing ctypes')
-
-
-class CFConst(object):
-    """
-    A class object that acts as essentially a namespace for CoreFoundation
-    constants.
-    """
-    kCFStringEncodingUTF8 = CFStringEncoding(0x08000100)
-
-
-class SecurityConst(object):
-    """
-    A class object that acts as essentially a namespace for Security constants.
-    """
-    kSSLSessionOptionBreakOnServerAuth = 0
-
-    kSSLProtocol2 = 1
-    kSSLProtocol3 = 2
-    kTLSProtocol1 = 4
-    kTLSProtocol11 = 7
-    kTLSProtocol12 = 8
-
-    kSSLClientSide = 1
-    kSSLStreamType = 0
-
-    kSecFormatPEMSequence = 10
-
-    kSecTrustResultInvalid = 0
-    kSecTrustResultProceed = 1
-    # This gap is present on purpose: this was kSecTrustResultConfirm, which
-    # is deprecated.
-    kSecTrustResultDeny = 3
-    kSecTrustResultUnspecified = 4
-    kSecTrustResultRecoverableTrustFailure = 5
-    kSecTrustResultFatalTrustFailure = 6
-    kSecTrustResultOtherError = 7
-
-    errSSLProtocol = -9800
-    errSSLWouldBlock = -9803
-    errSSLClosedGraceful = -9805
-    errSSLClosedNoNotify = -9816
-    errSSLClosedAbort = -9806
-
-    errSSLXCertChainInvalid = -9807
-    errSSLCrypto = -9809
-    errSSLInternal = -9810
-    errSSLCertExpired = -9814
-    errSSLCertNotYetValid = -9815
-    errSSLUnknownRootCert = -9812
-    errSSLNoRootCert = -9813
-    errSSLHostNameMismatch = -9843
-    errSSLPeerHandshakeFail = -9824
-    errSSLPeerUserCancelled = -9839
-    errSSLWeakPeerEphemeralDHKey = -9850
-    errSSLServerAuthCompleted = -9841
-    errSSLRecordOverflow = -9847
-
-    errSecVerifyFailed = -67808
-    errSecNoTrustSettings = -25263
-    errSecItemNotFound = -25300
-    errSecInvalidTrustSettings = -25262
-
-    # Cipher suites. We only pick the ones our default cipher string allows.
-    TLS_ECDHE_ECDSA_WITH_AES_256_GCM_SHA384 = 0xC02C
-    TLS_ECDHE_RSA_WITH_AES_256_GCM_SHA384 = 0xC030
-    TLS_ECDHE_ECDSA_WITH_AES_128_GCM_SHA256 = 0xC02B
-    TLS_ECDHE_RSA_WITH_AES_128_GCM_SHA256 = 0xC02F
-    TLS_DHE_DSS_WITH_AES_256_GCM_SHA384 = 0x00A3
-    TLS_DHE_RSA_WITH_AES_256_GCM_SHA384 = 0x009F
-    TLS_DHE_DSS_WITH_AES_128_GCM_SHA256 = 0x00A2
-    TLS_DHE_RSA_WITH_AES_128_GCM_SHA256 = 0x009E
-    TLS_ECDHE_ECDSA_WITH_AES_256_CBC_SHA384 = 0xC024
-    TLS_ECDHE_RSA_WITH_AES_256_CBC_SHA384 = 0xC028
-    TLS_ECDHE_ECDSA_WITH_AES_256_CBC_SHA = 0xC00A
-    TLS_ECDHE_RSA_WITH_AES_256_CBC_SHA = 0xC014
-    TLS_DHE_RSA_WITH_AES_256_CBC_SHA256 = 0x006B
-    TLS_DHE_DSS_WITH_AES_256_CBC_SHA256 = 0x006A
-    TLS_DHE_RSA_WITH_AES_256_CBC_SHA = 0x0039
-    TLS_DHE_DSS_WITH_AES_256_CBC_SHA = 0x0038
-    TLS_ECDHE_ECDSA_WITH_AES_128_CBC_SHA256 = 0xC023
-    TLS_ECDHE_RSA_WITH_AES_128_CBC_SHA256 = 0xC027
-    TLS_ECDHE_ECDSA_WITH_AES_128_CBC_SHA = 0xC009
-    TLS_ECDHE_RSA_WITH_AES_128_CBC_SHA = 0xC013
-    TLS_DHE_RSA_WITH_AES_128_CBC_SHA256 = 0x0067
-    TLS_DHE_DSS_WITH_AES_128_CBC_SHA256 = 0x0040
-    TLS_DHE_RSA_WITH_AES_128_CBC_SHA = 0x0033
-    TLS_DHE_DSS_WITH_AES_128_CBC_SHA = 0x0032
-    TLS_RSA_WITH_AES_256_GCM_SHA384 = 0x009D
-    TLS_RSA_WITH_AES_128_GCM_SHA256 = 0x009C
-    TLS_RSA_WITH_AES_256_CBC_SHA256 = 0x003D
-    TLS_RSA_WITH_AES_128_CBC_SHA256 = 0x003C
-    TLS_RSA_WITH_AES_256_CBC_SHA = 0x0035
-    TLS_RSA_WITH_AES_128_CBC_SHA = 0x002F
-    TLS_AES_128_GCM_SHA256 = 0x1301
-    TLS_AES_256_GCM_SHA384 = 0x1302
-    TLS_CHACHA20_POLY1305_SHA256 = 0x1303
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/low_level.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/low_level.py
deleted file mode 100644
index b13cd9e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/_securetransport/low_level.py
+++ /dev/null
@@ -1,346 +0,0 @@
-"""
-Low-level helpers for the SecureTransport bindings.
-
-These are Python functions that are not directly related to the high-level APIs
-but are necessary to get them to work. They include a whole bunch of low-level
-CoreFoundation messing about and memory management. The concerns in this module
-are almost entirely about trying to avoid memory leaks and providing
-appropriate and useful assistance to the higher-level code.
-"""
-import base64
-import ctypes
-import itertools
-import re
-import os
-import ssl
-import tempfile
-
-from .bindings import Security, CoreFoundation, CFConst
-
-
-# This regular expression is used to grab PEM data out of a PEM bundle.
-_PEM_CERTS_RE = re.compile(
-    b"-----BEGIN CERTIFICATE-----\n(.*?)\n-----END CERTIFICATE-----", re.DOTALL
-)
-
-
-def _cf_data_from_bytes(bytestring):
-    """
-    Given a bytestring, create a CFData object from it. This CFData object must
-    be CFReleased by the caller.
-    """
-    return CoreFoundation.CFDataCreate(
-        CoreFoundation.kCFAllocatorDefault, bytestring, len(bytestring)
-    )
-
-
-def _cf_dictionary_from_tuples(tuples):
-    """
-    Given a list of Python tuples, create an associated CFDictionary.
-    """
-    dictionary_size = len(tuples)
-
-    # We need to get the dictionary keys and values out in the same order.
-    keys = (t[0] for t in tuples)
-    values = (t[1] for t in tuples)
-    cf_keys = (CoreFoundation.CFTypeRef * dictionary_size)(*keys)
-    cf_values = (CoreFoundation.CFTypeRef * dictionary_size)(*values)
-
-    return CoreFoundation.CFDictionaryCreate(
-        CoreFoundation.kCFAllocatorDefault,
-        cf_keys,
-        cf_values,
-        dictionary_size,
-        CoreFoundation.kCFTypeDictionaryKeyCallBacks,
-        CoreFoundation.kCFTypeDictionaryValueCallBacks,
-    )
-
-
-def _cf_string_to_unicode(value):
-    """
-    Creates a Unicode string from a CFString object. Used entirely for error
-    reporting.
-
-    Yes, it annoys me quite a lot that this function is this complex.
-    """
-    value_as_void_p = ctypes.cast(value, ctypes.POINTER(ctypes.c_void_p))
-
-    string = CoreFoundation.CFStringGetCStringPtr(
-        value_as_void_p,
-        CFConst.kCFStringEncodingUTF8
-    )
-    if string is None:
-        buffer = ctypes.create_string_buffer(1024)
-        result = CoreFoundation.CFStringGetCString(
-            value_as_void_p,
-            buffer,
-            1024,
-            CFConst.kCFStringEncodingUTF8
-        )
-        if not result:
-            raise OSError('Error copying C string from CFStringRef')
-        string = buffer.value
-    if string is not None:
-        string = string.decode('utf-8')
-    return string
-
-
-def _assert_no_error(error, exception_class=None):
-    """
-    Checks the return code and throws an exception if there is an error to
-    report
-    """
-    if error == 0:
-        return
-
-    cf_error_string = Security.SecCopyErrorMessageString(error, None)
-    output = _cf_string_to_unicode(cf_error_string)
-    CoreFoundation.CFRelease(cf_error_string)
-
-    if output is None or output == u'':
-        output = u'OSStatus %s' % error
-
-    if exception_class is None:
-        exception_class = ssl.SSLError
-
-    raise exception_class(output)
-
-
-def _cert_array_from_pem(pem_bundle):
-    """
-    Given a bundle of certs in PEM format, turns them into a CFArray of certs
-    that can be used to validate a cert chain.
-    """
-    # Normalize the PEM bundle's line endings.
-    pem_bundle = pem_bundle.replace(b"\r\n", b"\n")
-
-    der_certs = [
-        base64.b64decode(match.group(1))
-        for match in _PEM_CERTS_RE.finditer(pem_bundle)
-    ]
-    if not der_certs:
-        raise ssl.SSLError("No root certificates specified")
-
-    cert_array = CoreFoundation.CFArrayCreateMutable(
-        CoreFoundation.kCFAllocatorDefault,
-        0,
-        ctypes.byref(CoreFoundation.kCFTypeArrayCallBacks)
-    )
-    if not cert_array:
-        raise ssl.SSLError("Unable to allocate memory!")
-
-    try:
-        for der_bytes in der_certs:
-            certdata = _cf_data_from_bytes(der_bytes)
-            if not certdata:
-                raise ssl.SSLError("Unable to allocate memory!")
-            cert = Security.SecCertificateCreateWithData(
-                CoreFoundation.kCFAllocatorDefault, certdata
-            )
-            CoreFoundation.CFRelease(certdata)
-            if not cert:
-                raise ssl.SSLError("Unable to build cert object!")
-
-            CoreFoundation.CFArrayAppendValue(cert_array, cert)
-            CoreFoundation.CFRelease(cert)
-    except Exception:
-        # We need to free the array before the exception bubbles further.
-        # We only want to do that if an error occurs: otherwise, the caller
-        # should free.
-        CoreFoundation.CFRelease(cert_array)
-
-    return cert_array
-
-
-def _is_cert(item):
-    """
-    Returns True if a given CFTypeRef is a certificate.
-    """
-    expected = Security.SecCertificateGetTypeID()
-    return CoreFoundation.CFGetTypeID(item) == expected
-
-
-def _is_identity(item):
-    """
-    Returns True if a given CFTypeRef is an identity.
-    """
-    expected = Security.SecIdentityGetTypeID()
-    return CoreFoundation.CFGetTypeID(item) == expected
-
-
-def _temporary_keychain():
-    """
-    This function creates a temporary Mac keychain that we can use to work with
-    credentials. This keychain uses a one-time password and a temporary file to
-    store the data. We expect to have one keychain per socket. The returned
-    SecKeychainRef must be freed by the caller, including calling
-    SecKeychainDelete.
-
-    Returns a tuple of the SecKeychainRef and the path to the temporary
-    directory that contains it.
-    """
-    # Unfortunately, SecKeychainCreate requires a path to a keychain. This
-    # means we cannot use mkstemp to use a generic temporary file. Instead,
-    # we're going to create a temporary directory and a filename to use there.
-    # This filename will be 8 random bytes expanded into base64. We also need
-    # some random bytes to password-protect the keychain we're creating, so we
-    # ask for 40 random bytes.
-    random_bytes = os.urandom(40)
-    filename = base64.b16encode(random_bytes[:8]).decode('utf-8')
-    password = base64.b16encode(random_bytes[8:])  # Must be valid UTF-8
-    tempdirectory = tempfile.mkdtemp()
-
-    keychain_path = os.path.join(tempdirectory, filename).encode('utf-8')
-
-    # We now want to create the keychain itself.
-    keychain = Security.SecKeychainRef()
-    status = Security.SecKeychainCreate(
-        keychain_path,
-        len(password),
-        password,
-        False,
-        None,
-        ctypes.byref(keychain)
-    )
-    _assert_no_error(status)
-
-    # Having created the keychain, we want to pass it off to the caller.
-    return keychain, tempdirectory
-
-
-def _load_items_from_file(keychain, path):
-    """
-    Given a single file, loads all the trust objects from it into arrays and
-    the keychain.
-    Returns a tuple of lists: the first list is a list of identities, the
-    second a list of certs.
-    """
-    certificates = []
-    identities = []
-    result_array = None
-
-    with open(path, 'rb') as f:
-        raw_filedata = f.read()
-
-    try:
-        filedata = CoreFoundation.CFDataCreate(
-            CoreFoundation.kCFAllocatorDefault,
-            raw_filedata,
-            len(raw_filedata)
-        )
-        result_array = CoreFoundation.CFArrayRef()
-        result = Security.SecItemImport(
-            filedata,  # cert data
-            None,  # Filename, leaving it out for now
-            None,  # What the type of the file is, we don't care
-            None,  # what's in the file, we don't care
-            0,  # import flags
-            None,  # key params, can include passphrase in the future
-            keychain,  # The keychain to insert into
-            ctypes.byref(result_array)  # Results
-        )
-        _assert_no_error(result)
-
-        # A CFArray is not very useful to us as an intermediary
-        # representation, so we are going to extract the objects we want
-        # and then free the array. We don't need to keep hold of keys: the
-        # keychain already has them!
-        result_count = CoreFoundation.CFArrayGetCount(result_array)
-        for index in range(result_count):
-            item = CoreFoundation.CFArrayGetValueAtIndex(
-                result_array, index
-            )
-            item = ctypes.cast(item, CoreFoundation.CFTypeRef)
-
-            if _is_cert(item):
-                CoreFoundation.CFRetain(item)
-                certificates.append(item)
-            elif _is_identity(item):
-                CoreFoundation.CFRetain(item)
-                identities.append(item)
-    finally:
-        if result_array:
-            CoreFoundation.CFRelease(result_array)
-
-        CoreFoundation.CFRelease(filedata)
-
-    return (identities, certificates)
-
-
-def _load_client_cert_chain(keychain, *paths):
-    """
-    Load certificates and maybe keys from a number of files. Has the end goal
-    of returning a CFArray containing one SecIdentityRef, and then zero or more
-    SecCertificateRef objects, suitable for use as a client certificate trust
-    chain.
-    """
-    # Ok, the strategy.
-    #
-    # This relies on knowing that macOS will not give you a SecIdentityRef
-    # unless you have imported a key into a keychain. This is a somewhat
-    # artificial limitation of macOS (for example, it doesn't necessarily
-    # affect iOS), but there is nothing inside Security.framework that lets you
-    # get a SecIdentityRef without having a key in a keychain.
-    #
-    # So the policy here is we take all the files and iterate them in order.
-    # Each one will use SecItemImport to have one or more objects loaded from
-    # it. We will also point at a keychain that macOS can use to work with the
-    # private key.
-    #
-    # Once we have all the objects, we'll check what we actually have. If we
-    # already have a SecIdentityRef in hand, fab: we'll use that. Otherwise,
-    # we'll take the first certificate (which we assume to be our leaf) and
-    # ask the keychain to give us a SecIdentityRef with that cert's associated
-    # key.
-    #
-    # We'll then return a CFArray containing the trust chain: one
-    # SecIdentityRef and then zero-or-more SecCertificateRef objects. The
-    # responsibility for freeing this CFArray will be with the caller. This
-    # CFArray must remain alive for the entire connection, so in practice it
-    # will be stored with a single SSLSocket, along with the reference to the
-    # keychain.
-    certificates = []
-    identities = []
-
-    # Filter out bad paths.
-    paths = (path for path in paths if path)
-
-    try:
-        for file_path in paths:
-            new_identities, new_certs = _load_items_from_file(
-                keychain, file_path
-            )
-            identities.extend(new_identities)
-            certificates.extend(new_certs)
-
-        # Ok, we have everything. The question is: do we have an identity? If
-        # not, we want to grab one from the first cert we have.
-        if not identities:
-            new_identity = Security.SecIdentityRef()
-            status = Security.SecIdentityCreateWithCertificate(
-                keychain,
-                certificates[0],
-                ctypes.byref(new_identity)
-            )
-            _assert_no_error(status)
-            identities.append(new_identity)
-
-            # We now want to release the original certificate, as we no longer
-            # need it.
-            CoreFoundation.CFRelease(certificates.pop(0))
-
-        # We now need to build a new CFArray that holds the trust chain.
-        trust_chain = CoreFoundation.CFArrayCreateMutable(
-            CoreFoundation.kCFAllocatorDefault,
-            0,
-            ctypes.byref(CoreFoundation.kCFTypeArrayCallBacks),
-        )
-        for item in itertools.chain(identities, certificates):
-            # ArrayAppendValue does a CFRetain on the item. That's fine,
-            # because the finally block will release our other refs to them.
-            CoreFoundation.CFArrayAppendValue(trust_chain, item)
-
-        return trust_chain
-    finally:
-        for obj in itertools.chain(identities, certificates):
-            CoreFoundation.CFRelease(obj)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/appengine.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/appengine.py
deleted file mode 100644
index 9b42952..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/appengine.py
+++ /dev/null
@@ -1,289 +0,0 @@
-"""
-This module provides a pool manager that uses Google App Engine's
-`URLFetch Service <https://cloud.google.com/appengine/docs/python/urlfetch>`_.
-
-Example usage::
-
-    from pip._vendor.urllib3 import PoolManager
-    from pip._vendor.urllib3.contrib.appengine import AppEngineManager, is_appengine_sandbox
-
-    if is_appengine_sandbox():
-        # AppEngineManager uses AppEngine's URLFetch API behind the scenes
-        http = AppEngineManager()
-    else:
-        # PoolManager uses a socket-level API behind the scenes
-        http = PoolManager()
-
-    r = http.request('GET', 'https://google.com/')
-
-There are `limitations <https://cloud.google.com/appengine/docs/python/\
-urlfetch/#Python_Quotas_and_limits>`_ to the URLFetch service and it may not be
-the best choice for your application. There are three options for using
-urllib3 on Google App Engine:
-
-1. You can use :class:`AppEngineManager` with URLFetch. URLFetch is
-   cost-effective in many circumstances as long as your usage is within the
-   limitations.
-2. You can use a normal :class:`~urllib3.PoolManager` by enabling sockets.
-   Sockets also have `limitations and restrictions
-   <https://cloud.google.com/appengine/docs/python/sockets/\
-   #limitations-and-restrictions>`_ and have a lower free quota than URLFetch.
-   To use sockets, be sure to specify the following in your ``app.yaml``::
-
-        env_variables:
-            GAE_USE_SOCKETS_HTTPLIB : 'true'
-
-3. If you are using `App Engine Flexible
-<https://cloud.google.com/appengine/docs/flexible/>`_, you can use the standard
-:class:`PoolManager` without any configuration or special environment variables.
-"""
-
-from __future__ import absolute_import
-import io
-import logging
-import warnings
-from ..packages.six.moves.urllib.parse import urljoin
-
-from ..exceptions import (
-    HTTPError,
-    HTTPWarning,
-    MaxRetryError,
-    ProtocolError,
-    TimeoutError,
-    SSLError
-)
-
-from ..request import RequestMethods
-from ..response import HTTPResponse
-from ..util.timeout import Timeout
-from ..util.retry import Retry
-from . import _appengine_environ
-
-try:
-    from google.appengine.api import urlfetch
-except ImportError:
-    urlfetch = None
-
-
-log = logging.getLogger(__name__)
-
-
-class AppEnginePlatformWarning(HTTPWarning):
-    pass
-
-
-class AppEnginePlatformError(HTTPError):
-    pass
-
-
-class AppEngineManager(RequestMethods):
-    """
-    Connection manager for Google App Engine sandbox applications.
-
-    This manager uses the URLFetch service directly instead of using the
-    emulated httplib, and is subject to URLFetch limitations as described in
-    the App Engine documentation `here
-    <https://cloud.google.com/appengine/docs/python/urlfetch>`_.
-
-    Notably it will raise an :class:`AppEnginePlatformError` if:
-        * URLFetch is not available.
-        * If you attempt to use this on App Engine Flexible, as full socket
-          support is available.
-        * If a request size is more than 10 megabytes.
-        * If a response size is more than 32 megabtyes.
-        * If you use an unsupported request method such as OPTIONS.
-
-    Beyond those cases, it will raise normal urllib3 errors.
-    """
-
-    def __init__(self, headers=None, retries=None, validate_certificate=True,
-                 urlfetch_retries=True):
-        if not urlfetch:
-            raise AppEnginePlatformError(
-                "URLFetch is not available in this environment.")
-
-        if is_prod_appengine_mvms():
-            raise AppEnginePlatformError(
-                "Use normal urllib3.PoolManager instead of AppEngineManager"
-                "on Managed VMs, as using URLFetch is not necessary in "
-                "this environment.")
-
-        warnings.warn(
-            "urllib3 is using URLFetch on Google App Engine sandbox instead "
-            "of sockets. To use sockets directly instead of URLFetch see "
-            "https://urllib3.readthedocs.io/en/latest/reference/urllib3.contrib.html.",
-            AppEnginePlatformWarning)
-
-        RequestMethods.__init__(self, headers)
-        self.validate_certificate = validate_certificate
-        self.urlfetch_retries = urlfetch_retries
-
-        self.retries = retries or Retry.DEFAULT
-
-    def __enter__(self):
-        return self
-
-    def __exit__(self, exc_type, exc_val, exc_tb):
-        # Return False to re-raise any potential exceptions
-        return False
-
-    def urlopen(self, method, url, body=None, headers=None,
-                retries=None, redirect=True, timeout=Timeout.DEFAULT_TIMEOUT,
-                **response_kw):
-
-        retries = self._get_retries(retries, redirect)
-
-        try:
-            follow_redirects = (
-                    redirect and
-                    retries.redirect != 0 and
-                    retries.total)
-            response = urlfetch.fetch(
-                url,
-                payload=body,
-                method=method,
-                headers=headers or {},
-                allow_truncated=False,
-                follow_redirects=self.urlfetch_retries and follow_redirects,
-                deadline=self._get_absolute_timeout(timeout),
-                validate_certificate=self.validate_certificate,
-            )
-        except urlfetch.DeadlineExceededError as e:
-            raise TimeoutError(self, e)
-
-        except urlfetch.InvalidURLError as e:
-            if 'too large' in str(e):
-                raise AppEnginePlatformError(
-                    "URLFetch request too large, URLFetch only "
-                    "supports requests up to 10mb in size.", e)
-            raise ProtocolError(e)
-
-        except urlfetch.DownloadError as e:
-            if 'Too many redirects' in str(e):
-                raise MaxRetryError(self, url, reason=e)
-            raise ProtocolError(e)
-
-        except urlfetch.ResponseTooLargeError as e:
-            raise AppEnginePlatformError(
-                "URLFetch response too large, URLFetch only supports"
-                "responses up to 32mb in size.", e)
-
-        except urlfetch.SSLCertificateError as e:
-            raise SSLError(e)
-
-        except urlfetch.InvalidMethodError as e:
-            raise AppEnginePlatformError(
-                "URLFetch does not support method: %s" % method, e)
-
-        http_response = self._urlfetch_response_to_http_response(
-            response, retries=retries, **response_kw)
-
-        # Handle redirect?
-        redirect_location = redirect and http_response.get_redirect_location()
-        if redirect_location:
-            # Check for redirect response
-            if (self.urlfetch_retries and retries.raise_on_redirect):
-                raise MaxRetryError(self, url, "too many redirects")
-            else:
-                if http_response.status == 303:
-                    method = 'GET'
-
-                try:
-                    retries = retries.increment(method, url, response=http_response, _pool=self)
-                except MaxRetryError:
-                    if retries.raise_on_redirect:
-                        raise MaxRetryError(self, url, "too many redirects")
-                    return http_response
-
-                retries.sleep_for_retry(http_response)
-                log.debug("Redirecting %s -> %s", url, redirect_location)
-                redirect_url = urljoin(url, redirect_location)
-                return self.urlopen(
-                    method, redirect_url, body, headers,
-                    retries=retries, redirect=redirect,
-                    timeout=timeout, **response_kw)
-
-        # Check if we should retry the HTTP response.
-        has_retry_after = bool(http_response.getheader('Retry-After'))
-        if retries.is_retry(method, http_response.status, has_retry_after):
-            retries = retries.increment(
-                method, url, response=http_response, _pool=self)
-            log.debug("Retry: %s", url)
-            retries.sleep(http_response)
-            return self.urlopen(
-                method, url,
-                body=body, headers=headers,
-                retries=retries, redirect=redirect,
-                timeout=timeout, **response_kw)
-
-        return http_response
-
-    def _urlfetch_response_to_http_response(self, urlfetch_resp, **response_kw):
-
-        if is_prod_appengine():
-            # Production GAE handles deflate encoding automatically, but does
-            # not remove the encoding header.
-            content_encoding = urlfetch_resp.headers.get('content-encoding')
-
-            if content_encoding == 'deflate':
-                del urlfetch_resp.headers['content-encoding']
-
-        transfer_encoding = urlfetch_resp.headers.get('transfer-encoding')
-        # We have a full response's content,
-        # so let's make sure we don't report ourselves as chunked data.
-        if transfer_encoding == 'chunked':
-            encodings = transfer_encoding.split(",")
-            encodings.remove('chunked')
-            urlfetch_resp.headers['transfer-encoding'] = ','.join(encodings)
-
-        original_response = HTTPResponse(
-            # In order for decoding to work, we must present the content as
-            # a file-like object.
-            body=io.BytesIO(urlfetch_resp.content),
-            msg=urlfetch_resp.header_msg,
-            headers=urlfetch_resp.headers,
-            status=urlfetch_resp.status_code,
-            **response_kw
-        )
-
-        return HTTPResponse(
-            body=io.BytesIO(urlfetch_resp.content),
-            headers=urlfetch_resp.headers,
-            status=urlfetch_resp.status_code,
-            original_response=original_response,
-            **response_kw
-        )
-
-    def _get_absolute_timeout(self, timeout):
-        if timeout is Timeout.DEFAULT_TIMEOUT:
-            return None  # Defer to URLFetch's default.
-        if isinstance(timeout, Timeout):
-            if timeout._read is not None or timeout._connect is not None:
-                warnings.warn(
-                    "URLFetch does not support granular timeout settings, "
-                    "reverting to total or default URLFetch timeout.",
-                    AppEnginePlatformWarning)
-            return timeout.total
-        return timeout
-
-    def _get_retries(self, retries, redirect):
-        if not isinstance(retries, Retry):
-            retries = Retry.from_int(
-                retries, redirect=redirect, default=self.retries)
-
-        if retries.connect or retries.read or retries.redirect:
-            warnings.warn(
-                "URLFetch only supports total retries and does not "
-                "recognize connect, read, or redirect retry parameters.",
-                AppEnginePlatformWarning)
-
-        return retries
-
-
-# Alias methods from _appengine_environ to maintain public API interface.
-
-is_appengine = _appengine_environ.is_appengine
-is_appengine_sandbox = _appengine_environ.is_appengine_sandbox
-is_local_appengine = _appengine_environ.is_local_appengine
-is_prod_appengine = _appengine_environ.is_prod_appengine
-is_prod_appengine_mvms = _appengine_environ.is_prod_appengine_mvms
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/ntlmpool.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/ntlmpool.py
deleted file mode 100644
index 8ea127c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/ntlmpool.py
+++ /dev/null
@@ -1,111 +0,0 @@
-"""
-NTLM authenticating pool, contributed by erikcederstran
-
-Issue #10, see: http://code.google.com/p/urllib3/issues/detail?id=10
-"""
-from __future__ import absolute_import
-
-from logging import getLogger
-from ntlm import ntlm
-
-from .. import HTTPSConnectionPool
-from ..packages.six.moves.http_client import HTTPSConnection
-
-
-log = getLogger(__name__)
-
-
-class NTLMConnectionPool(HTTPSConnectionPool):
-    """
-    Implements an NTLM authentication version of an urllib3 connection pool
-    """
-
-    scheme = 'https'
-
-    def __init__(self, user, pw, authurl, *args, **kwargs):
-        """
-        authurl is a random URL on the server that is protected by NTLM.
-        user is the Windows user, probably in the DOMAIN\\username format.
-        pw is the password for the user.
-        """
-        super(NTLMConnectionPool, self).__init__(*args, **kwargs)
-        self.authurl = authurl
-        self.rawuser = user
-        user_parts = user.split('\\', 1)
-        self.domain = user_parts[0].upper()
-        self.user = user_parts[1]
-        self.pw = pw
-
-    def _new_conn(self):
-        # Performs the NTLM handshake that secures the connection. The socket
-        # must be kept open while requests are performed.
-        self.num_connections += 1
-        log.debug('Starting NTLM HTTPS connection no. %d: https://%s%s',
-                  self.num_connections, self.host, self.authurl)
-
-        headers = {'Connection': 'Keep-Alive'}
-        req_header = 'Authorization'
-        resp_header = 'www-authenticate'
-
-        conn = HTTPSConnection(host=self.host, port=self.port)
-
-        # Send negotiation message
-        headers[req_header] = (
-            'NTLM %s' % ntlm.create_NTLM_NEGOTIATE_MESSAGE(self.rawuser))
-        log.debug('Request headers: %s', headers)
-        conn.request('GET', self.authurl, None, headers)
-        res = conn.getresponse()
-        reshdr = dict(res.getheaders())
-        log.debug('Response status: %s %s', res.status, res.reason)
-        log.debug('Response headers: %s', reshdr)
-        log.debug('Response data: %s [...]', res.read(100))
-
-        # Remove the reference to the socket, so that it can not be closed by
-        # the response object (we want to keep the socket open)
-        res.fp = None
-
-        # Server should respond with a challenge message
-        auth_header_values = reshdr[resp_header].split(', ')
-        auth_header_value = None
-        for s in auth_header_values:
-            if s[:5] == 'NTLM ':
-                auth_header_value = s[5:]
-        if auth_header_value is None:
-            raise Exception('Unexpected %s response header: %s' %
-                            (resp_header, reshdr[resp_header]))
-
-        # Send authentication message
-        ServerChallenge, NegotiateFlags = \
-            ntlm.parse_NTLM_CHALLENGE_MESSAGE(auth_header_value)
-        auth_msg = ntlm.create_NTLM_AUTHENTICATE_MESSAGE(ServerChallenge,
-                                                         self.user,
-                                                         self.domain,
-                                                         self.pw,
-                                                         NegotiateFlags)
-        headers[req_header] = 'NTLM %s' % auth_msg
-        log.debug('Request headers: %s', headers)
-        conn.request('GET', self.authurl, None, headers)
-        res = conn.getresponse()
-        log.debug('Response status: %s %s', res.status, res.reason)
-        log.debug('Response headers: %s', dict(res.getheaders()))
-        log.debug('Response data: %s [...]', res.read()[:100])
-        if res.status != 200:
-            if res.status == 401:
-                raise Exception('Server rejected request: wrong '
-                                'username or password')
-            raise Exception('Wrong server response: %s %s' %
-                            (res.status, res.reason))
-
-        res.fp = None
-        log.debug('Connection established')
-        return conn
-
-    def urlopen(self, method, url, body=None, headers=None, retries=3,
-                redirect=True, assert_same_host=True):
-        if headers is None:
-            headers = {}
-        headers['Connection'] = 'Keep-Alive'
-        return super(NTLMConnectionPool, self).urlopen(method, url, body,
-                                                       headers, retries,
-                                                       redirect,
-                                                       assert_same_host)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/pyopenssl.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/pyopenssl.py
deleted file mode 100644
index 363667c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/pyopenssl.py
+++ /dev/null
@@ -1,466 +0,0 @@
-"""
-SSL with SNI_-support for Python 2. Follow these instructions if you would
-like to verify SSL certificates in Python 2. Note, the default libraries do
-*not* do certificate checking; you need to do additional work to validate
-certificates yourself.
-
-This needs the following packages installed:
-
-* pyOpenSSL (tested with 16.0.0)
-* cryptography (minimum 1.3.4, from pyopenssl)
-* idna (minimum 2.0, from cryptography)
-
-However, pyopenssl depends on cryptography, which depends on idna, so while we
-use all three directly here we end up having relatively few packages required.
-
-You can install them with the following command:
-
-    pip install pyopenssl cryptography idna
-
-To activate certificate checking, call
-:func:`~urllib3.contrib.pyopenssl.inject_into_urllib3` from your Python code
-before you begin making HTTP requests. This can be done in a ``sitecustomize``
-module, or at any other time before your application begins using ``urllib3``,
-like this::
-
-    try:
-        import urllib3.contrib.pyopenssl
-        urllib3.contrib.pyopenssl.inject_into_urllib3()
-    except ImportError:
-        pass
-
-Now you can use :mod:`urllib3` as you normally would, and it will support SNI
-when the required modules are installed.
-
-Activating this module also has the positive side effect of disabling SSL/TLS
-compression in Python 2 (see `CRIME attack`_).
-
-If you want to configure the default list of supported cipher suites, you can
-set the ``urllib3.contrib.pyopenssl.DEFAULT_SSL_CIPHER_LIST`` variable.
-
-.. _sni: https://en.wikipedia.org/wiki/Server_Name_Indication
-.. _crime attack: https://en.wikipedia.org/wiki/CRIME_(security_exploit)
-"""
-from __future__ import absolute_import
-
-import OpenSSL.SSL
-from cryptography import x509
-from cryptography.hazmat.backends.openssl import backend as openssl_backend
-from cryptography.hazmat.backends.openssl.x509 import _Certificate
-try:
-    from cryptography.x509 import UnsupportedExtension
-except ImportError:
-    # UnsupportedExtension is gone in cryptography >= 2.1.0
-    class UnsupportedExtension(Exception):
-        pass
-
-from socket import timeout, error as SocketError
-from io import BytesIO
-
-try:  # Platform-specific: Python 2
-    from socket import _fileobject
-except ImportError:  # Platform-specific: Python 3
-    _fileobject = None
-    from ..packages.backports.makefile import backport_makefile
-
-import logging
-import ssl
-from ..packages import six
-import sys
-
-from .. import util
-
-__all__ = ['inject_into_urllib3', 'extract_from_urllib3']
-
-# SNI always works.
-HAS_SNI = True
-
-# Map from urllib3 to PyOpenSSL compatible parameter-values.
-_openssl_versions = {
-    ssl.PROTOCOL_SSLv23: OpenSSL.SSL.SSLv23_METHOD,
-    ssl.PROTOCOL_TLSv1: OpenSSL.SSL.TLSv1_METHOD,
-}
-
-if hasattr(ssl, 'PROTOCOL_TLSv1_1') and hasattr(OpenSSL.SSL, 'TLSv1_1_METHOD'):
-    _openssl_versions[ssl.PROTOCOL_TLSv1_1] = OpenSSL.SSL.TLSv1_1_METHOD
-
-if hasattr(ssl, 'PROTOCOL_TLSv1_2') and hasattr(OpenSSL.SSL, 'TLSv1_2_METHOD'):
-    _openssl_versions[ssl.PROTOCOL_TLSv1_2] = OpenSSL.SSL.TLSv1_2_METHOD
-
-try:
-    _openssl_versions.update({ssl.PROTOCOL_SSLv3: OpenSSL.SSL.SSLv3_METHOD})
-except AttributeError:
-    pass
-
-_stdlib_to_openssl_verify = {
-    ssl.CERT_NONE: OpenSSL.SSL.VERIFY_NONE,
-    ssl.CERT_OPTIONAL: OpenSSL.SSL.VERIFY_PEER,
-    ssl.CERT_REQUIRED:
-        OpenSSL.SSL.VERIFY_PEER + OpenSSL.SSL.VERIFY_FAIL_IF_NO_PEER_CERT,
-}
-_openssl_to_stdlib_verify = dict(
-    (v, k) for k, v in _stdlib_to_openssl_verify.items()
-)
-
-# OpenSSL will only write 16K at a time
-SSL_WRITE_BLOCKSIZE = 16384
-
-orig_util_HAS_SNI = util.HAS_SNI
-orig_util_SSLContext = util.ssl_.SSLContext
-
-
-log = logging.getLogger(__name__)
-
-
-def inject_into_urllib3():
-    'Monkey-patch urllib3 with PyOpenSSL-backed SSL-support.'
-
-    _validate_dependencies_met()
-
-    util.ssl_.SSLContext = PyOpenSSLContext
-    util.HAS_SNI = HAS_SNI
-    util.ssl_.HAS_SNI = HAS_SNI
-    util.IS_PYOPENSSL = True
-    util.ssl_.IS_PYOPENSSL = True
-
-
-def extract_from_urllib3():
-    'Undo monkey-patching by :func:`inject_into_urllib3`.'
-
-    util.ssl_.SSLContext = orig_util_SSLContext
-    util.HAS_SNI = orig_util_HAS_SNI
-    util.ssl_.HAS_SNI = orig_util_HAS_SNI
-    util.IS_PYOPENSSL = False
-    util.ssl_.IS_PYOPENSSL = False
-
-
-def _validate_dependencies_met():
-    """
-    Verifies that PyOpenSSL's package-level dependencies have been met.
-    Throws `ImportError` if they are not met.
-    """
-    # Method added in `cryptography==1.1`; not available in older versions
-    from cryptography.x509.extensions import Extensions
-    if getattr(Extensions, "get_extension_for_class", None) is None:
-        raise ImportError("'cryptography' module missing required functionality.  "
-                          "Try upgrading to v1.3.4 or newer.")
-
-    # pyOpenSSL 0.14 and above use cryptography for OpenSSL bindings. The _x509
-    # attribute is only present on those versions.
-    from OpenSSL.crypto import X509
-    x509 = X509()
-    if getattr(x509, "_x509", None) is None:
-        raise ImportError("'pyOpenSSL' module missing required functionality. "
-                          "Try upgrading to v0.14 or newer.")
-
-
-def _dnsname_to_stdlib(name):
-    """
-    Converts a dNSName SubjectAlternativeName field to the form used by the
-    standard library on the given Python version.
-
-    Cryptography produces a dNSName as a unicode string that was idna-decoded
-    from ASCII bytes. We need to idna-encode that string to get it back, and
-    then on Python 3 we also need to convert to unicode via UTF-8 (the stdlib
-    uses PyUnicode_FromStringAndSize on it, which decodes via UTF-8).
-
-    If the name cannot be idna-encoded then we return None signalling that
-    the name given should be skipped.
-    """
-    def idna_encode(name):
-        """
-        Borrowed wholesale from the Python Cryptography Project. It turns out
-        that we can't just safely call `idna.encode`: it can explode for
-        wildcard names. This avoids that problem.
-        """
-        from pip._vendor import idna
-
-        try:
-            for prefix in [u'*.', u'.']:
-                if name.startswith(prefix):
-                    name = name[len(prefix):]
-                    return prefix.encode('ascii') + idna.encode(name)
-            return idna.encode(name)
-        except idna.core.IDNAError:
-            return None
-
-    name = idna_encode(name)
-    if name is None:
-        return None
-    elif sys.version_info >= (3, 0):
-        name = name.decode('utf-8')
-    return name
-
-
-def get_subj_alt_name(peer_cert):
-    """
-    Given an PyOpenSSL certificate, provides all the subject alternative names.
-    """
-    # Pass the cert to cryptography, which has much better APIs for this.
-    if hasattr(peer_cert, "to_cryptography"):
-        cert = peer_cert.to_cryptography()
-    else:
-        # This is technically using private APIs, but should work across all
-        # relevant versions before PyOpenSSL got a proper API for this.
-        cert = _Certificate(openssl_backend, peer_cert._x509)
-
-    # We want to find the SAN extension. Ask Cryptography to locate it (it's
-    # faster than looping in Python)
-    try:
-        ext = cert.extensions.get_extension_for_class(
-            x509.SubjectAlternativeName
-        ).value
-    except x509.ExtensionNotFound:
-        # No such extension, return the empty list.
-        return []
-    except (x509.DuplicateExtension, UnsupportedExtension,
-            x509.UnsupportedGeneralNameType, UnicodeError) as e:
-        # A problem has been found with the quality of the certificate. Assume
-        # no SAN field is present.
-        log.warning(
-            "A problem was encountered with the certificate that prevented "
-            "urllib3 from finding the SubjectAlternativeName field. This can "
-            "affect certificate validation. The error was %s",
-            e,
-        )
-        return []
-
-    # We want to return dNSName and iPAddress fields. We need to cast the IPs
-    # back to strings because the match_hostname function wants them as
-    # strings.
-    # Sadly the DNS names need to be idna encoded and then, on Python 3, UTF-8
-    # decoded. This is pretty frustrating, but that's what the standard library
-    # does with certificates, and so we need to attempt to do the same.
-    # We also want to skip over names which cannot be idna encoded.
-    names = [
-        ('DNS', name) for name in map(_dnsname_to_stdlib, ext.get_values_for_type(x509.DNSName))
-        if name is not None
-    ]
-    names.extend(
-        ('IP Address', str(name))
-        for name in ext.get_values_for_type(x509.IPAddress)
-    )
-
-    return names
-
-
-class WrappedSocket(object):
-    '''API-compatibility wrapper for Python OpenSSL's Connection-class.
-
-    Note: _makefile_refs, _drop() and _reuse() are needed for the garbage
-    collector of pypy.
-    '''
-
-    def __init__(self, connection, socket, suppress_ragged_eofs=True):
-        self.connection = connection
-        self.socket = socket
-        self.suppress_ragged_eofs = suppress_ragged_eofs
-        self._makefile_refs = 0
-        self._closed = False
-
-    def fileno(self):
-        return self.socket.fileno()
-
-    # Copy-pasted from Python 3.5 source code
-    def _decref_socketios(self):
-        if self._makefile_refs > 0:
-            self._makefile_refs -= 1
-        if self._closed:
-            self.close()
-
-    def recv(self, *args, **kwargs):
-        try:
-            data = self.connection.recv(*args, **kwargs)
-        except OpenSSL.SSL.SysCallError as e:
-            if self.suppress_ragged_eofs and e.args == (-1, 'Unexpected EOF'):
-                return b''
-            else:
-                raise SocketError(str(e))
-        except OpenSSL.SSL.ZeroReturnError as e:
-            if self.connection.get_shutdown() == OpenSSL.SSL.RECEIVED_SHUTDOWN:
-                return b''
-            else:
-                raise
-        except OpenSSL.SSL.WantReadError:
-            if not util.wait_for_read(self.socket, self.socket.gettimeout()):
-                raise timeout('The read operation timed out')
-            else:
-                return self.recv(*args, **kwargs)
-        else:
-            return data
-
-    def recv_into(self, *args, **kwargs):
-        try:
-            return self.connection.recv_into(*args, **kwargs)
-        except OpenSSL.SSL.SysCallError as e:
-            if self.suppress_ragged_eofs and e.args == (-1, 'Unexpected EOF'):
-                return 0
-            else:
-                raise SocketError(str(e))
-        except OpenSSL.SSL.ZeroReturnError as e:
-            if self.connection.get_shutdown() == OpenSSL.SSL.RECEIVED_SHUTDOWN:
-                return 0
-            else:
-                raise
-        except OpenSSL.SSL.WantReadError:
-            if not util.wait_for_read(self.socket, self.socket.gettimeout()):
-                raise timeout('The read operation timed out')
-            else:
-                return self.recv_into(*args, **kwargs)
-
-    def settimeout(self, timeout):
-        return self.socket.settimeout(timeout)
-
-    def _send_until_done(self, data):
-        while True:
-            try:
-                return self.connection.send(data)
-            except OpenSSL.SSL.WantWriteError:
-                if not util.wait_for_write(self.socket, self.socket.gettimeout()):
-                    raise timeout()
-                continue
-            except OpenSSL.SSL.SysCallError as e:
-                raise SocketError(str(e))
-
-    def sendall(self, data):
-        total_sent = 0
-        while total_sent < len(data):
-            sent = self._send_until_done(data[total_sent:total_sent + SSL_WRITE_BLOCKSIZE])
-            total_sent += sent
-
-    def shutdown(self):
-        # FIXME rethrow compatible exceptions should we ever use this
-        self.connection.shutdown()
-
-    def close(self):
-        if self._makefile_refs < 1:
-            try:
-                self._closed = True
-                return self.connection.close()
-            except OpenSSL.SSL.Error:
-                return
-        else:
-            self._makefile_refs -= 1
-
-    def getpeercert(self, binary_form=False):
-        x509 = self.connection.get_peer_certificate()
-
-        if not x509:
-            return x509
-
-        if binary_form:
-            return OpenSSL.crypto.dump_certificate(
-                OpenSSL.crypto.FILETYPE_ASN1,
-                x509)
-
-        return {
-            'subject': (
-                (('commonName', x509.get_subject().CN),),
-            ),
-            'subjectAltName': get_subj_alt_name(x509)
-        }
-
-    def _reuse(self):
-        self._makefile_refs += 1
-
-    def _drop(self):
-        if self._makefile_refs < 1:
-            self.close()
-        else:
-            self._makefile_refs -= 1
-
-
-if _fileobject:  # Platform-specific: Python 2
-    def makefile(self, mode, bufsize=-1):
-        self._makefile_refs += 1
-        return _fileobject(self, mode, bufsize, close=True)
-else:  # Platform-specific: Python 3
-    makefile = backport_makefile
-
-WrappedSocket.makefile = makefile
-
-
-class PyOpenSSLContext(object):
-    """
-    I am a wrapper class for the PyOpenSSL ``Context`` object. I am responsible
-    for translating the interface of the standard library ``SSLContext`` object
-    to calls into PyOpenSSL.
-    """
-    def __init__(self, protocol):
-        self.protocol = _openssl_versions[protocol]
-        self._ctx = OpenSSL.SSL.Context(self.protocol)
-        self._options = 0
-        self.check_hostname = False
-
-    @property
-    def options(self):
-        return self._options
-
-    @options.setter
-    def options(self, value):
-        self._options = value
-        self._ctx.set_options(value)
-
-    @property
-    def verify_mode(self):
-        return _openssl_to_stdlib_verify[self._ctx.get_verify_mode()]
-
-    @verify_mode.setter
-    def verify_mode(self, value):
-        self._ctx.set_verify(
-            _stdlib_to_openssl_verify[value],
-            _verify_callback
-        )
-
-    def set_default_verify_paths(self):
-        self._ctx.set_default_verify_paths()
-
-    def set_ciphers(self, ciphers):
-        if isinstance(ciphers, six.text_type):
-            ciphers = ciphers.encode('utf-8')
-        self._ctx.set_cipher_list(ciphers)
-
-    def load_verify_locations(self, cafile=None, capath=None, cadata=None):
-        if cafile is not None:
-            cafile = cafile.encode('utf-8')
-        if capath is not None:
-            capath = capath.encode('utf-8')
-        self._ctx.load_verify_locations(cafile, capath)
-        if cadata is not None:
-            self._ctx.load_verify_locations(BytesIO(cadata))
-
-    def load_cert_chain(self, certfile, keyfile=None, password=None):
-        self._ctx.use_certificate_chain_file(certfile)
-        if password is not None:
-            self._ctx.set_passwd_cb(lambda max_length, prompt_twice, userdata: password)
-        self._ctx.use_privatekey_file(keyfile or certfile)
-
-    def wrap_socket(self, sock, server_side=False,
-                    do_handshake_on_connect=True, suppress_ragged_eofs=True,
-                    server_hostname=None):
-        cnx = OpenSSL.SSL.Connection(self._ctx, sock)
-
-        if isinstance(server_hostname, six.text_type):  # Platform-specific: Python 3
-            server_hostname = server_hostname.encode('utf-8')
-
-        if server_hostname is not None:
-            cnx.set_tlsext_host_name(server_hostname)
-
-        cnx.set_connect_state()
-
-        while True:
-            try:
-                cnx.do_handshake()
-            except OpenSSL.SSL.WantReadError:
-                if not util.wait_for_read(sock, sock.gettimeout()):
-                    raise timeout('select timed out')
-                continue
-            except OpenSSL.SSL.Error as e:
-                raise ssl.SSLError('bad handshake: %r' % e)
-            break
-
-        return WrappedSocket(cnx, sock)
-
-
-def _verify_callback(cnx, x509, err_no, err_depth, return_code):
-    return err_no == 0
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/securetransport.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/securetransport.py
deleted file mode 100644
index 77cb59e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/securetransport.py
+++ /dev/null
@@ -1,804 +0,0 @@
-"""
-SecureTranport support for urllib3 via ctypes.
-
-This makes platform-native TLS available to urllib3 users on macOS without the
-use of a compiler. This is an important feature because the Python Package
-Index is moving to become a TLSv1.2-or-higher server, and the default OpenSSL
-that ships with macOS is not capable of doing TLSv1.2. The only way to resolve
-this is to give macOS users an alternative solution to the problem, and that
-solution is to use SecureTransport.
-
-We use ctypes here because this solution must not require a compiler. That's
-because pip is not allowed to require a compiler either.
-
-This is not intended to be a seriously long-term solution to this problem.
-The hope is that PEP 543 will eventually solve this issue for us, at which
-point we can retire this contrib module. But in the short term, we need to
-solve the impending tire fire that is Python on Mac without this kind of
-contrib module. So...here we are.
-
-To use this module, simply import and inject it::
-
-    import urllib3.contrib.securetransport
-    urllib3.contrib.securetransport.inject_into_urllib3()
-
-Happy TLSing!
-"""
-from __future__ import absolute_import
-
-import contextlib
-import ctypes
-import errno
-import os.path
-import shutil
-import socket
-import ssl
-import threading
-import weakref
-
-from .. import util
-from ._securetransport.bindings import (
-    Security, SecurityConst, CoreFoundation
-)
-from ._securetransport.low_level import (
-    _assert_no_error, _cert_array_from_pem, _temporary_keychain,
-    _load_client_cert_chain
-)
-
-try:  # Platform-specific: Python 2
-    from socket import _fileobject
-except ImportError:  # Platform-specific: Python 3
-    _fileobject = None
-    from ..packages.backports.makefile import backport_makefile
-
-__all__ = ['inject_into_urllib3', 'extract_from_urllib3']
-
-# SNI always works
-HAS_SNI = True
-
-orig_util_HAS_SNI = util.HAS_SNI
-orig_util_SSLContext = util.ssl_.SSLContext
-
-# This dictionary is used by the read callback to obtain a handle to the
-# calling wrapped socket. This is a pretty silly approach, but for now it'll
-# do. I feel like I should be able to smuggle a handle to the wrapped socket
-# directly in the SSLConnectionRef, but for now this approach will work I
-# guess.
-#
-# We need to lock around this structure for inserts, but we don't do it for
-# reads/writes in the callbacks. The reasoning here goes as follows:
-#
-#    1. It is not possible to call into the callbacks before the dictionary is
-#       populated, so once in the callback the id must be in the dictionary.
-#    2. The callbacks don't mutate the dictionary, they only read from it, and
-#       so cannot conflict with any of the insertions.
-#
-# This is good: if we had to lock in the callbacks we'd drastically slow down
-# the performance of this code.
-_connection_refs = weakref.WeakValueDictionary()
-_connection_ref_lock = threading.Lock()
-
-# Limit writes to 16kB. This is OpenSSL's limit, but we'll cargo-cult it over
-# for no better reason than we need *a* limit, and this one is right there.
-SSL_WRITE_BLOCKSIZE = 16384
-
-# This is our equivalent of util.ssl_.DEFAULT_CIPHERS, but expanded out to
-# individual cipher suites. We need to do this because this is how
-# SecureTransport wants them.
-CIPHER_SUITES = [
-    SecurityConst.TLS_AES_256_GCM_SHA384,
-    SecurityConst.TLS_CHACHA20_POLY1305_SHA256,
-    SecurityConst.TLS_AES_128_GCM_SHA256,
-    SecurityConst.TLS_ECDHE_ECDSA_WITH_AES_256_GCM_SHA384,
-    SecurityConst.TLS_ECDHE_RSA_WITH_AES_256_GCM_SHA384,
-    SecurityConst.TLS_ECDHE_ECDSA_WITH_AES_128_GCM_SHA256,
-    SecurityConst.TLS_ECDHE_RSA_WITH_AES_128_GCM_SHA256,
-    SecurityConst.TLS_DHE_DSS_WITH_AES_256_GCM_SHA384,
-    SecurityConst.TLS_DHE_RSA_WITH_AES_256_GCM_SHA384,
-    SecurityConst.TLS_DHE_DSS_WITH_AES_128_GCM_SHA256,
-    SecurityConst.TLS_DHE_RSA_WITH_AES_128_GCM_SHA256,
-    SecurityConst.TLS_ECDHE_ECDSA_WITH_AES_256_CBC_SHA384,
-    SecurityConst.TLS_ECDHE_RSA_WITH_AES_256_CBC_SHA384,
-    SecurityConst.TLS_ECDHE_ECDSA_WITH_AES_256_CBC_SHA,
-    SecurityConst.TLS_ECDHE_RSA_WITH_AES_256_CBC_SHA,
-    SecurityConst.TLS_DHE_RSA_WITH_AES_256_CBC_SHA256,
-    SecurityConst.TLS_DHE_DSS_WITH_AES_256_CBC_SHA256,
-    SecurityConst.TLS_DHE_RSA_WITH_AES_256_CBC_SHA,
-    SecurityConst.TLS_DHE_DSS_WITH_AES_256_CBC_SHA,
-    SecurityConst.TLS_ECDHE_ECDSA_WITH_AES_128_CBC_SHA256,
-    SecurityConst.TLS_ECDHE_RSA_WITH_AES_128_CBC_SHA256,
-    SecurityConst.TLS_ECDHE_ECDSA_WITH_AES_128_CBC_SHA,
-    SecurityConst.TLS_ECDHE_RSA_WITH_AES_128_CBC_SHA,
-    SecurityConst.TLS_DHE_RSA_WITH_AES_128_CBC_SHA256,
-    SecurityConst.TLS_DHE_DSS_WITH_AES_128_CBC_SHA256,
-    SecurityConst.TLS_DHE_RSA_WITH_AES_128_CBC_SHA,
-    SecurityConst.TLS_DHE_DSS_WITH_AES_128_CBC_SHA,
-    SecurityConst.TLS_RSA_WITH_AES_256_GCM_SHA384,
-    SecurityConst.TLS_RSA_WITH_AES_128_GCM_SHA256,
-    SecurityConst.TLS_RSA_WITH_AES_256_CBC_SHA256,
-    SecurityConst.TLS_RSA_WITH_AES_128_CBC_SHA256,
-    SecurityConst.TLS_RSA_WITH_AES_256_CBC_SHA,
-    SecurityConst.TLS_RSA_WITH_AES_128_CBC_SHA,
-]
-
-# Basically this is simple: for PROTOCOL_SSLv23 we turn it into a low of
-# TLSv1 and a high of TLSv1.2. For everything else, we pin to that version.
-_protocol_to_min_max = {
-    ssl.PROTOCOL_SSLv23: (SecurityConst.kTLSProtocol1, SecurityConst.kTLSProtocol12),
-}
-
-if hasattr(ssl, "PROTOCOL_SSLv2"):
-    _protocol_to_min_max[ssl.PROTOCOL_SSLv2] = (
-        SecurityConst.kSSLProtocol2, SecurityConst.kSSLProtocol2
-    )
-if hasattr(ssl, "PROTOCOL_SSLv3"):
-    _protocol_to_min_max[ssl.PROTOCOL_SSLv3] = (
-        SecurityConst.kSSLProtocol3, SecurityConst.kSSLProtocol3
-    )
-if hasattr(ssl, "PROTOCOL_TLSv1"):
-    _protocol_to_min_max[ssl.PROTOCOL_TLSv1] = (
-        SecurityConst.kTLSProtocol1, SecurityConst.kTLSProtocol1
-    )
-if hasattr(ssl, "PROTOCOL_TLSv1_1"):
-    _protocol_to_min_max[ssl.PROTOCOL_TLSv1_1] = (
-        SecurityConst.kTLSProtocol11, SecurityConst.kTLSProtocol11
-    )
-if hasattr(ssl, "PROTOCOL_TLSv1_2"):
-    _protocol_to_min_max[ssl.PROTOCOL_TLSv1_2] = (
-        SecurityConst.kTLSProtocol12, SecurityConst.kTLSProtocol12
-    )
-if hasattr(ssl, "PROTOCOL_TLS"):
-    _protocol_to_min_max[ssl.PROTOCOL_TLS] = _protocol_to_min_max[ssl.PROTOCOL_SSLv23]
-
-
-def inject_into_urllib3():
-    """
-    Monkey-patch urllib3 with SecureTransport-backed SSL-support.
-    """
-    util.ssl_.SSLContext = SecureTransportContext
-    util.HAS_SNI = HAS_SNI
-    util.ssl_.HAS_SNI = HAS_SNI
-    util.IS_SECURETRANSPORT = True
-    util.ssl_.IS_SECURETRANSPORT = True
-
-
-def extract_from_urllib3():
-    """
-    Undo monkey-patching by :func:`inject_into_urllib3`.
-    """
-    util.ssl_.SSLContext = orig_util_SSLContext
-    util.HAS_SNI = orig_util_HAS_SNI
-    util.ssl_.HAS_SNI = orig_util_HAS_SNI
-    util.IS_SECURETRANSPORT = False
-    util.ssl_.IS_SECURETRANSPORT = False
-
-
-def _read_callback(connection_id, data_buffer, data_length_pointer):
-    """
-    SecureTransport read callback. This is called by ST to request that data
-    be returned from the socket.
-    """
-    wrapped_socket = None
-    try:
-        wrapped_socket = _connection_refs.get(connection_id)
-        if wrapped_socket is None:
-            return SecurityConst.errSSLInternal
-        base_socket = wrapped_socket.socket
-
-        requested_length = data_length_pointer[0]
-
-        timeout = wrapped_socket.gettimeout()
-        error = None
-        read_count = 0
-
-        try:
-            while read_count < requested_length:
-                if timeout is None or timeout >= 0:
-                    if not util.wait_for_read(base_socket, timeout):
-                        raise socket.error(errno.EAGAIN, 'timed out')
-
-                remaining = requested_length - read_count
-                buffer = (ctypes.c_char * remaining).from_address(
-                    data_buffer + read_count
-                )
-                chunk_size = base_socket.recv_into(buffer, remaining)
-                read_count += chunk_size
-                if not chunk_size:
-                    if not read_count:
-                        return SecurityConst.errSSLClosedGraceful
-                    break
-        except (socket.error) as e:
-            error = e.errno
-
-            if error is not None and error != errno.EAGAIN:
-                data_length_pointer[0] = read_count
-                if error == errno.ECONNRESET or error == errno.EPIPE:
-                    return SecurityConst.errSSLClosedAbort
-                raise
-
-        data_length_pointer[0] = read_count
-
-        if read_count != requested_length:
-            return SecurityConst.errSSLWouldBlock
-
-        return 0
-    except Exception as e:
-        if wrapped_socket is not None:
-            wrapped_socket._exception = e
-        return SecurityConst.errSSLInternal
-
-
-def _write_callback(connection_id, data_buffer, data_length_pointer):
-    """
-    SecureTransport write callback. This is called by ST to request that data
-    actually be sent on the network.
-    """
-    wrapped_socket = None
-    try:
-        wrapped_socket = _connection_refs.get(connection_id)
-        if wrapped_socket is None:
-            return SecurityConst.errSSLInternal
-        base_socket = wrapped_socket.socket
-
-        bytes_to_write = data_length_pointer[0]
-        data = ctypes.string_at(data_buffer, bytes_to_write)
-
-        timeout = wrapped_socket.gettimeout()
-        error = None
-        sent = 0
-
-        try:
-            while sent < bytes_to_write:
-                if timeout is None or timeout >= 0:
-                    if not util.wait_for_write(base_socket, timeout):
-                        raise socket.error(errno.EAGAIN, 'timed out')
-                chunk_sent = base_socket.send(data)
-                sent += chunk_sent
-
-                # This has some needless copying here, but I'm not sure there's
-                # much value in optimising this data path.
-                data = data[chunk_sent:]
-        except (socket.error) as e:
-            error = e.errno
-
-            if error is not None and error != errno.EAGAIN:
-                data_length_pointer[0] = sent
-                if error == errno.ECONNRESET or error == errno.EPIPE:
-                    return SecurityConst.errSSLClosedAbort
-                raise
-
-        data_length_pointer[0] = sent
-
-        if sent != bytes_to_write:
-            return SecurityConst.errSSLWouldBlock
-
-        return 0
-    except Exception as e:
-        if wrapped_socket is not None:
-            wrapped_socket._exception = e
-        return SecurityConst.errSSLInternal
-
-
-# We need to keep these two objects references alive: if they get GC'd while
-# in use then SecureTransport could attempt to call a function that is in freed
-# memory. That would be...uh...bad. Yeah, that's the word. Bad.
-_read_callback_pointer = Security.SSLReadFunc(_read_callback)
-_write_callback_pointer = Security.SSLWriteFunc(_write_callback)
-
-
-class WrappedSocket(object):
-    """
-    API-compatibility wrapper for Python's OpenSSL wrapped socket object.
-
-    Note: _makefile_refs, _drop(), and _reuse() are needed for the garbage
-    collector of PyPy.
-    """
-    def __init__(self, socket):
-        self.socket = socket
-        self.context = None
-        self._makefile_refs = 0
-        self._closed = False
-        self._exception = None
-        self._keychain = None
-        self._keychain_dir = None
-        self._client_cert_chain = None
-
-        # We save off the previously-configured timeout and then set it to
-        # zero. This is done because we use select and friends to handle the
-        # timeouts, but if we leave the timeout set on the lower socket then
-        # Python will "kindly" call select on that socket again for us. Avoid
-        # that by forcing the timeout to zero.
-        self._timeout = self.socket.gettimeout()
-        self.socket.settimeout(0)
-
-    @contextlib.contextmanager
-    def _raise_on_error(self):
-        """
-        A context manager that can be used to wrap calls that do I/O from
-        SecureTransport. If any of the I/O callbacks hit an exception, this
-        context manager will correctly propagate the exception after the fact.
-        This avoids silently swallowing those exceptions.
-
-        It also correctly forces the socket closed.
-        """
-        self._exception = None
-
-        # We explicitly don't catch around this yield because in the unlikely
-        # event that an exception was hit in the block we don't want to swallow
-        # it.
-        yield
-        if self._exception is not None:
-            exception, self._exception = self._exception, None
-            self.close()
-            raise exception
-
-    def _set_ciphers(self):
-        """
-        Sets up the allowed ciphers. By default this matches the set in
-        util.ssl_.DEFAULT_CIPHERS, at least as supported by macOS. This is done
-        custom and doesn't allow changing at this time, mostly because parsing
-        OpenSSL cipher strings is going to be a freaking nightmare.
-        """
-        ciphers = (Security.SSLCipherSuite * len(CIPHER_SUITES))(*CIPHER_SUITES)
-        result = Security.SSLSetEnabledCiphers(
-            self.context, ciphers, len(CIPHER_SUITES)
-        )
-        _assert_no_error(result)
-
-    def _custom_validate(self, verify, trust_bundle):
-        """
-        Called when we have set custom validation. We do this in two cases:
-        first, when cert validation is entirely disabled; and second, when
-        using a custom trust DB.
-        """
-        # If we disabled cert validation, just say: cool.
-        if not verify:
-            return
-
-        # We want data in memory, so load it up.
-        if os.path.isfile(trust_bundle):
-            with open(trust_bundle, 'rb') as f:
-                trust_bundle = f.read()
-
-        cert_array = None
-        trust = Security.SecTrustRef()
-
-        try:
-            # Get a CFArray that contains the certs we want.
-            cert_array = _cert_array_from_pem(trust_bundle)
-
-            # Ok, now the hard part. We want to get the SecTrustRef that ST has
-            # created for this connection, shove our CAs into it, tell ST to
-            # ignore everything else it knows, and then ask if it can build a
-            # chain. This is a buuuunch of code.
-            result = Security.SSLCopyPeerTrust(
-                self.context, ctypes.byref(trust)
-            )
-            _assert_no_error(result)
-            if not trust:
-                raise ssl.SSLError("Failed to copy trust reference")
-
-            result = Security.SecTrustSetAnchorCertificates(trust, cert_array)
-            _assert_no_error(result)
-
-            result = Security.SecTrustSetAnchorCertificatesOnly(trust, True)
-            _assert_no_error(result)
-
-            trust_result = Security.SecTrustResultType()
-            result = Security.SecTrustEvaluate(
-                trust, ctypes.byref(trust_result)
-            )
-            _assert_no_error(result)
-        finally:
-            if trust:
-                CoreFoundation.CFRelease(trust)
-
-            if cert_array is not None:
-                CoreFoundation.CFRelease(cert_array)
-
-        # Ok, now we can look at what the result was.
-        successes = (
-            SecurityConst.kSecTrustResultUnspecified,
-            SecurityConst.kSecTrustResultProceed
-        )
-        if trust_result.value not in successes:
-            raise ssl.SSLError(
-                "certificate verify failed, error code: %d" %
-                trust_result.value
-            )
-
-    def handshake(self,
-                  server_hostname,
-                  verify,
-                  trust_bundle,
-                  min_version,
-                  max_version,
-                  client_cert,
-                  client_key,
-                  client_key_passphrase):
-        """
-        Actually performs the TLS handshake. This is run automatically by
-        wrapped socket, and shouldn't be needed in user code.
-        """
-        # First, we do the initial bits of connection setup. We need to create
-        # a context, set its I/O funcs, and set the connection reference.
-        self.context = Security.SSLCreateContext(
-            None, SecurityConst.kSSLClientSide, SecurityConst.kSSLStreamType
-        )
-        result = Security.SSLSetIOFuncs(
-            self.context, _read_callback_pointer, _write_callback_pointer
-        )
-        _assert_no_error(result)
-
-        # Here we need to compute the handle to use. We do this by taking the
-        # id of self modulo 2**31 - 1. If this is already in the dictionary, we
-        # just keep incrementing by one until we find a free space.
-        with _connection_ref_lock:
-            handle = id(self) % 2147483647
-            while handle in _connection_refs:
-                handle = (handle + 1) % 2147483647
-            _connection_refs[handle] = self
-
-        result = Security.SSLSetConnection(self.context, handle)
-        _assert_no_error(result)
-
-        # If we have a server hostname, we should set that too.
-        if server_hostname:
-            if not isinstance(server_hostname, bytes):
-                server_hostname = server_hostname.encode('utf-8')
-
-            result = Security.SSLSetPeerDomainName(
-                self.context, server_hostname, len(server_hostname)
-            )
-            _assert_no_error(result)
-
-        # Setup the ciphers.
-        self._set_ciphers()
-
-        # Set the minimum and maximum TLS versions.
-        result = Security.SSLSetProtocolVersionMin(self.context, min_version)
-        _assert_no_error(result)
-        result = Security.SSLSetProtocolVersionMax(self.context, max_version)
-        _assert_no_error(result)
-
-        # If there's a trust DB, we need to use it. We do that by telling
-        # SecureTransport to break on server auth. We also do that if we don't
-        # want to validate the certs at all: we just won't actually do any
-        # authing in that case.
-        if not verify or trust_bundle is not None:
-            result = Security.SSLSetSessionOption(
-                self.context,
-                SecurityConst.kSSLSessionOptionBreakOnServerAuth,
-                True
-            )
-            _assert_no_error(result)
-
-        # If there's a client cert, we need to use it.
-        if client_cert:
-            self._keychain, self._keychain_dir = _temporary_keychain()
-            self._client_cert_chain = _load_client_cert_chain(
-                self._keychain, client_cert, client_key
-            )
-            result = Security.SSLSetCertificate(
-                self.context, self._client_cert_chain
-            )
-            _assert_no_error(result)
-
-        while True:
-            with self._raise_on_error():
-                result = Security.SSLHandshake(self.context)
-
-                if result == SecurityConst.errSSLWouldBlock:
-                    raise socket.timeout("handshake timed out")
-                elif result == SecurityConst.errSSLServerAuthCompleted:
-                    self._custom_validate(verify, trust_bundle)
-                    continue
-                else:
-                    _assert_no_error(result)
-                    break
-
-    def fileno(self):
-        return self.socket.fileno()
-
-    # Copy-pasted from Python 3.5 source code
-    def _decref_socketios(self):
-        if self._makefile_refs > 0:
-            self._makefile_refs -= 1
-        if self._closed:
-            self.close()
-
-    def recv(self, bufsiz):
-        buffer = ctypes.create_string_buffer(bufsiz)
-        bytes_read = self.recv_into(buffer, bufsiz)
-        data = buffer[:bytes_read]
-        return data
-
-    def recv_into(self, buffer, nbytes=None):
-        # Read short on EOF.
-        if self._closed:
-            return 0
-
-        if nbytes is None:
-            nbytes = len(buffer)
-
-        buffer = (ctypes.c_char * nbytes).from_buffer(buffer)
-        processed_bytes = ctypes.c_size_t(0)
-
-        with self._raise_on_error():
-            result = Security.SSLRead(
-                self.context, buffer, nbytes, ctypes.byref(processed_bytes)
-            )
-
-        # There are some result codes that we want to treat as "not always
-        # errors". Specifically, those are errSSLWouldBlock,
-        # errSSLClosedGraceful, and errSSLClosedNoNotify.
-        if (result == SecurityConst.errSSLWouldBlock):
-            # If we didn't process any bytes, then this was just a time out.
-            # However, we can get errSSLWouldBlock in situations when we *did*
-            # read some data, and in those cases we should just read "short"
-            # and return.
-            if processed_bytes.value == 0:
-                # Timed out, no data read.
-                raise socket.timeout("recv timed out")
-        elif result in (SecurityConst.errSSLClosedGraceful, SecurityConst.errSSLClosedNoNotify):
-            # The remote peer has closed this connection. We should do so as
-            # well. Note that we don't actually return here because in
-            # principle this could actually be fired along with return data.
-            # It's unlikely though.
-            self.close()
-        else:
-            _assert_no_error(result)
-
-        # Ok, we read and probably succeeded. We should return whatever data
-        # was actually read.
-        return processed_bytes.value
-
-    def settimeout(self, timeout):
-        self._timeout = timeout
-
-    def gettimeout(self):
-        return self._timeout
-
-    def send(self, data):
-        processed_bytes = ctypes.c_size_t(0)
-
-        with self._raise_on_error():
-            result = Security.SSLWrite(
-                self.context, data, len(data), ctypes.byref(processed_bytes)
-            )
-
-        if result == SecurityConst.errSSLWouldBlock and processed_bytes.value == 0:
-            # Timed out
-            raise socket.timeout("send timed out")
-        else:
-            _assert_no_error(result)
-
-        # We sent, and probably succeeded. Tell them how much we sent.
-        return processed_bytes.value
-
-    def sendall(self, data):
-        total_sent = 0
-        while total_sent < len(data):
-            sent = self.send(data[total_sent:total_sent + SSL_WRITE_BLOCKSIZE])
-            total_sent += sent
-
-    def shutdown(self):
-        with self._raise_on_error():
-            Security.SSLClose(self.context)
-
-    def close(self):
-        # TODO: should I do clean shutdown here? Do I have to?
-        if self._makefile_refs < 1:
-            self._closed = True
-            if self.context:
-                CoreFoundation.CFRelease(self.context)
-                self.context = None
-            if self._client_cert_chain:
-                CoreFoundation.CFRelease(self._client_cert_chain)
-                self._client_cert_chain = None
-            if self._keychain:
-                Security.SecKeychainDelete(self._keychain)
-                CoreFoundation.CFRelease(self._keychain)
-                shutil.rmtree(self._keychain_dir)
-                self._keychain = self._keychain_dir = None
-            return self.socket.close()
-        else:
-            self._makefile_refs -= 1
-
-    def getpeercert(self, binary_form=False):
-        # Urgh, annoying.
-        #
-        # Here's how we do this:
-        #
-        # 1. Call SSLCopyPeerTrust to get hold of the trust object for this
-        #    connection.
-        # 2. Call SecTrustGetCertificateAtIndex for index 0 to get the leaf.
-        # 3. To get the CN, call SecCertificateCopyCommonName and process that
-        #    string so that it's of the appropriate type.
-        # 4. To get the SAN, we need to do something a bit more complex:
-        #    a. Call SecCertificateCopyValues to get the data, requesting
-        #       kSecOIDSubjectAltName.
-        #    b. Mess about with this dictionary to try to get the SANs out.
-        #
-        # This is gross. Really gross. It's going to be a few hundred LoC extra
-        # just to repeat something that SecureTransport can *already do*. So my
-        # operating assumption at this time is that what we want to do is
-        # instead to just flag to urllib3 that it shouldn't do its own hostname
-        # validation when using SecureTransport.
-        if not binary_form:
-            raise ValueError(
-                "SecureTransport only supports dumping binary certs"
-            )
-        trust = Security.SecTrustRef()
-        certdata = None
-        der_bytes = None
-
-        try:
-            # Grab the trust store.
-            result = Security.SSLCopyPeerTrust(
-                self.context, ctypes.byref(trust)
-            )
-            _assert_no_error(result)
-            if not trust:
-                # Probably we haven't done the handshake yet. No biggie.
-                return None
-
-            cert_count = Security.SecTrustGetCertificateCount(trust)
-            if not cert_count:
-                # Also a case that might happen if we haven't handshaked.
-                # Handshook? Handshaken?
-                return None
-
-            leaf = Security.SecTrustGetCertificateAtIndex(trust, 0)
-            assert leaf
-
-            # Ok, now we want the DER bytes.
-            certdata = Security.SecCertificateCopyData(leaf)
-            assert certdata
-
-            data_length = CoreFoundation.CFDataGetLength(certdata)
-            data_buffer = CoreFoundation.CFDataGetBytePtr(certdata)
-            der_bytes = ctypes.string_at(data_buffer, data_length)
-        finally:
-            if certdata:
-                CoreFoundation.CFRelease(certdata)
-            if trust:
-                CoreFoundation.CFRelease(trust)
-
-        return der_bytes
-
-    def _reuse(self):
-        self._makefile_refs += 1
-
-    def _drop(self):
-        if self._makefile_refs < 1:
-            self.close()
-        else:
-            self._makefile_refs -= 1
-
-
-if _fileobject:  # Platform-specific: Python 2
-    def makefile(self, mode, bufsize=-1):
-        self._makefile_refs += 1
-        return _fileobject(self, mode, bufsize, close=True)
-else:  # Platform-specific: Python 3
-    def makefile(self, mode="r", buffering=None, *args, **kwargs):
-        # We disable buffering with SecureTransport because it conflicts with
-        # the buffering that ST does internally (see issue #1153 for more).
-        buffering = 0
-        return backport_makefile(self, mode, buffering, *args, **kwargs)
-
-WrappedSocket.makefile = makefile
-
-
-class SecureTransportContext(object):
-    """
-    I am a wrapper class for the SecureTransport library, to translate the
-    interface of the standard library ``SSLContext`` object to calls into
-    SecureTransport.
-    """
-    def __init__(self, protocol):
-        self._min_version, self._max_version = _protocol_to_min_max[protocol]
-        self._options = 0
-        self._verify = False
-        self._trust_bundle = None
-        self._client_cert = None
-        self._client_key = None
-        self._client_key_passphrase = None
-
-    @property
-    def check_hostname(self):
-        """
-        SecureTransport cannot have its hostname checking disabled. For more,
-        see the comment on getpeercert() in this file.
-        """
-        return True
-
-    @check_hostname.setter
-    def check_hostname(self, value):
-        """
-        SecureTransport cannot have its hostname checking disabled. For more,
-        see the comment on getpeercert() in this file.
-        """
-        pass
-
-    @property
-    def options(self):
-        # TODO: Well, crap.
-        #
-        # So this is the bit of the code that is the most likely to cause us
-        # trouble. Essentially we need to enumerate all of the SSL options that
-        # users might want to use and try to see if we can sensibly translate
-        # them, or whether we should just ignore them.
-        return self._options
-
-    @options.setter
-    def options(self, value):
-        # TODO: Update in line with above.
-        self._options = value
-
-    @property
-    def verify_mode(self):
-        return ssl.CERT_REQUIRED if self._verify else ssl.CERT_NONE
-
-    @verify_mode.setter
-    def verify_mode(self, value):
-        self._verify = True if value == ssl.CERT_REQUIRED else False
-
-    def set_default_verify_paths(self):
-        # So, this has to do something a bit weird. Specifically, what it does
-        # is nothing.
-        #
-        # This means that, if we had previously had load_verify_locations
-        # called, this does not undo that. We need to do that because it turns
-        # out that the rest of the urllib3 code will attempt to load the
-        # default verify paths if it hasn't been told about any paths, even if
-        # the context itself was sometime earlier. We resolve that by just
-        # ignoring it.
-        pass
-
-    def load_default_certs(self):
-        return self.set_default_verify_paths()
-
-    def set_ciphers(self, ciphers):
-        # For now, we just require the default cipher string.
-        if ciphers != util.ssl_.DEFAULT_CIPHERS:
-            raise ValueError(
-                "SecureTransport doesn't support custom cipher strings"
-            )
-
-    def load_verify_locations(self, cafile=None, capath=None, cadata=None):
-        # OK, we only really support cadata and cafile.
-        if capath is not None:
-            raise ValueError(
-                "SecureTransport does not support cert directories"
-            )
-
-        self._trust_bundle = cafile or cadata
-
-    def load_cert_chain(self, certfile, keyfile=None, password=None):
-        self._client_cert = certfile
-        self._client_key = keyfile
-        self._client_cert_passphrase = password
-
-    def wrap_socket(self, sock, server_side=False,
-                    do_handshake_on_connect=True, suppress_ragged_eofs=True,
-                    server_hostname=None):
-        # So, what do we do here? Firstly, we assert some properties. This is a
-        # stripped down shim, so there is some functionality we don't support.
-        # See PEP 543 for the real deal.
-        assert not server_side
-        assert do_handshake_on_connect
-        assert suppress_ragged_eofs
-
-        # Ok, we're good to go. Now we want to create the wrapped socket object
-        # and store it in the appropriate place.
-        wrapped_socket = WrappedSocket(sock)
-
-        # Now we can handshake
-        wrapped_socket.handshake(
-            server_hostname, self._verify, self._trust_bundle,
-            self._min_version, self._max_version, self._client_cert,
-            self._client_key, self._client_key_passphrase
-        )
-        return wrapped_socket
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/socks.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/socks.py
deleted file mode 100644
index 811e312..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/contrib/socks.py
+++ /dev/null
@@ -1,192 +0,0 @@
-# -*- coding: utf-8 -*-
-"""
-This module contains provisional support for SOCKS proxies from within
-urllib3. This module supports SOCKS4 (specifically the SOCKS4A variant) and
-SOCKS5. To enable its functionality, either install PySocks or install this
-module with the ``socks`` extra.
-
-The SOCKS implementation supports the full range of urllib3 features. It also
-supports the following SOCKS features:
-
-- SOCKS4
-- SOCKS4a
-- SOCKS5
-- Usernames and passwords for the SOCKS proxy
-
-Known Limitations:
-
-- Currently PySocks does not support contacting remote websites via literal
-  IPv6 addresses. Any such connection attempt will fail. You must use a domain
-  name.
-- Currently PySocks does not support IPv6 connections to the SOCKS proxy. Any
-  such connection attempt will fail.
-"""
-from __future__ import absolute_import
-
-try:
-    import socks
-except ImportError:
-    import warnings
-    from ..exceptions import DependencyWarning
-
-    warnings.warn((
-        'SOCKS support in urllib3 requires the installation of optional '
-        'dependencies: specifically, PySocks.  For more information, see '
-        'https://urllib3.readthedocs.io/en/latest/contrib.html#socks-proxies'
-        ),
-        DependencyWarning
-    )
-    raise
-
-from socket import error as SocketError, timeout as SocketTimeout
-
-from ..connection import (
-    HTTPConnection, HTTPSConnection
-)
-from ..connectionpool import (
-    HTTPConnectionPool, HTTPSConnectionPool
-)
-from ..exceptions import ConnectTimeoutError, NewConnectionError
-from ..poolmanager import PoolManager
-from ..util.url import parse_url
-
-try:
-    import ssl
-except ImportError:
-    ssl = None
-
-
-class SOCKSConnection(HTTPConnection):
-    """
-    A plain-text HTTP connection that connects via a SOCKS proxy.
-    """
-    def __init__(self, *args, **kwargs):
-        self._socks_options = kwargs.pop('_socks_options')
-        super(SOCKSConnection, self).__init__(*args, **kwargs)
-
-    def _new_conn(self):
-        """
-        Establish a new connection via the SOCKS proxy.
-        """
-        extra_kw = {}
-        if self.source_address:
-            extra_kw['source_address'] = self.source_address
-
-        if self.socket_options:
-            extra_kw['socket_options'] = self.socket_options
-
-        try:
-            conn = socks.create_connection(
-                (self.host, self.port),
-                proxy_type=self._socks_options['socks_version'],
-                proxy_addr=self._socks_options['proxy_host'],
-                proxy_port=self._socks_options['proxy_port'],
-                proxy_username=self._socks_options['username'],
-                proxy_password=self._socks_options['password'],
-                proxy_rdns=self._socks_options['rdns'],
-                timeout=self.timeout,
-                **extra_kw
-            )
-
-        except SocketTimeout as e:
-            raise ConnectTimeoutError(
-                self, "Connection to %s timed out. (connect timeout=%s)" %
-                (self.host, self.timeout))
-
-        except socks.ProxyError as e:
-            # This is fragile as hell, but it seems to be the only way to raise
-            # useful errors here.
-            if e.socket_err:
-                error = e.socket_err
-                if isinstance(error, SocketTimeout):
-                    raise ConnectTimeoutError(
-                        self,
-                        "Connection to %s timed out. (connect timeout=%s)" %
-                        (self.host, self.timeout)
-                    )
-                else:
-                    raise NewConnectionError(
-                        self,
-                        "Failed to establish a new connection: %s" % error
-                    )
-            else:
-                raise NewConnectionError(
-                    self,
-                    "Failed to establish a new connection: %s" % e
-                )
-
-        except SocketError as e:  # Defensive: PySocks should catch all these.
-            raise NewConnectionError(
-                self, "Failed to establish a new connection: %s" % e)
-
-        return conn
-
-
-# We don't need to duplicate the Verified/Unverified distinction from
-# urllib3/connection.py here because the HTTPSConnection will already have been
-# correctly set to either the Verified or Unverified form by that module. This
-# means the SOCKSHTTPSConnection will automatically be the correct type.
-class SOCKSHTTPSConnection(SOCKSConnection, HTTPSConnection):
-    pass
-
-
-class SOCKSHTTPConnectionPool(HTTPConnectionPool):
-    ConnectionCls = SOCKSConnection
-
-
-class SOCKSHTTPSConnectionPool(HTTPSConnectionPool):
-    ConnectionCls = SOCKSHTTPSConnection
-
-
-class SOCKSProxyManager(PoolManager):
-    """
-    A version of the urllib3 ProxyManager that routes connections via the
-    defined SOCKS proxy.
-    """
-    pool_classes_by_scheme = {
-        'http': SOCKSHTTPConnectionPool,
-        'https': SOCKSHTTPSConnectionPool,
-    }
-
-    def __init__(self, proxy_url, username=None, password=None,
-                 num_pools=10, headers=None, **connection_pool_kw):
-        parsed = parse_url(proxy_url)
-
-        if username is None and password is None and parsed.auth is not None:
-            split = parsed.auth.split(':')
-            if len(split) == 2:
-                username, password = split
-        if parsed.scheme == 'socks5':
-            socks_version = socks.PROXY_TYPE_SOCKS5
-            rdns = False
-        elif parsed.scheme == 'socks5h':
-            socks_version = socks.PROXY_TYPE_SOCKS5
-            rdns = True
-        elif parsed.scheme == 'socks4':
-            socks_version = socks.PROXY_TYPE_SOCKS4
-            rdns = False
-        elif parsed.scheme == 'socks4a':
-            socks_version = socks.PROXY_TYPE_SOCKS4
-            rdns = True
-        else:
-            raise ValueError(
-                "Unable to determine SOCKS version from %s" % proxy_url
-            )
-
-        self.proxy_url = proxy_url
-
-        socks_options = {
-            'socks_version': socks_version,
-            'proxy_host': parsed.host,
-            'proxy_port': parsed.port,
-            'username': username,
-            'password': password,
-            'rdns': rdns
-        }
-        connection_pool_kw['_socks_options'] = socks_options
-
-        super(SOCKSProxyManager, self).__init__(
-            num_pools, headers, **connection_pool_kw
-        )
-
-        self.pool_classes_by_scheme = SOCKSProxyManager.pool_classes_by_scheme
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/exceptions.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/exceptions.py
deleted file mode 100644
index 7bbaa98..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/exceptions.py
+++ /dev/null
@@ -1,246 +0,0 @@
-from __future__ import absolute_import
-from .packages.six.moves.http_client import (
-    IncompleteRead as httplib_IncompleteRead
-)
-# Base Exceptions
-
-
-class HTTPError(Exception):
-    "Base exception used by this module."
-    pass
-
-
-class HTTPWarning(Warning):
-    "Base warning used by this module."
-    pass
-
-
-class PoolError(HTTPError):
-    "Base exception for errors caused within a pool."
-    def __init__(self, pool, message):
-        self.pool = pool
-        HTTPError.__init__(self, "%s: %s" % (pool, message))
-
-    def __reduce__(self):
-        # For pickling purposes.
-        return self.__class__, (None, None)
-
-
-class RequestError(PoolError):
-    "Base exception for PoolErrors that have associated URLs."
-    def __init__(self, pool, url, message):
-        self.url = url
-        PoolError.__init__(self, pool, message)
-
-    def __reduce__(self):
-        # For pickling purposes.
-        return self.__class__, (None, self.url, None)
-
-
-class SSLError(HTTPError):
-    "Raised when SSL certificate fails in an HTTPS connection."
-    pass
-
-
-class ProxyError(HTTPError):
-    "Raised when the connection to a proxy fails."
-    pass
-
-
-class DecodeError(HTTPError):
-    "Raised when automatic decoding based on Content-Type fails."
-    pass
-
-
-class ProtocolError(HTTPError):
-    "Raised when something unexpected happens mid-request/response."
-    pass
-
-
-#: Renamed to ProtocolError but aliased for backwards compatibility.
-ConnectionError = ProtocolError
-
-
-# Leaf Exceptions
-
-class MaxRetryError(RequestError):
-    """Raised when the maximum number of retries is exceeded.
-
-    :param pool: The connection pool
-    :type pool: :class:`~urllib3.connectionpool.HTTPConnectionPool`
-    :param string url: The requested Url
-    :param exceptions.Exception reason: The underlying error
-
-    """
-
-    def __init__(self, pool, url, reason=None):
-        self.reason = reason
-
-        message = "Max retries exceeded with url: %s (Caused by %r)" % (
-            url, reason)
-
-        RequestError.__init__(self, pool, url, message)
-
-
-class HostChangedError(RequestError):
-    "Raised when an existing pool gets a request for a foreign host."
-
-    def __init__(self, pool, url, retries=3):
-        message = "Tried to open a foreign host with url: %s" % url
-        RequestError.__init__(self, pool, url, message)
-        self.retries = retries
-
-
-class TimeoutStateError(HTTPError):
-    """ Raised when passing an invalid state to a timeout """
-    pass
-
-
-class TimeoutError(HTTPError):
-    """ Raised when a socket timeout error occurs.
-
-    Catching this error will catch both :exc:`ReadTimeoutErrors
-    <ReadTimeoutError>` and :exc:`ConnectTimeoutErrors <ConnectTimeoutError>`.
-    """
-    pass
-
-
-class ReadTimeoutError(TimeoutError, RequestError):
-    "Raised when a socket timeout occurs while receiving data from a server"
-    pass
-
-
-# This timeout error does not have a URL attached and needs to inherit from the
-# base HTTPError
-class ConnectTimeoutError(TimeoutError):
-    "Raised when a socket timeout occurs while connecting to a server"
-    pass
-
-
-class NewConnectionError(ConnectTimeoutError, PoolError):
-    "Raised when we fail to establish a new connection. Usually ECONNREFUSED."
-    pass
-
-
-class EmptyPoolError(PoolError):
-    "Raised when a pool runs out of connections and no more are allowed."
-    pass
-
-
-class ClosedPoolError(PoolError):
-    "Raised when a request enters a pool after the pool has been closed."
-    pass
-
-
-class LocationValueError(ValueError, HTTPError):
-    "Raised when there is something wrong with a given URL input."
-    pass
-
-
-class LocationParseError(LocationValueError):
-    "Raised when get_host or similar fails to parse the URL input."
-
-    def __init__(self, location):
-        message = "Failed to parse: %s" % location
-        HTTPError.__init__(self, message)
-
-        self.location = location
-
-
-class ResponseError(HTTPError):
-    "Used as a container for an error reason supplied in a MaxRetryError."
-    GENERIC_ERROR = 'too many error responses'
-    SPECIFIC_ERROR = 'too many {status_code} error responses'
-
-
-class SecurityWarning(HTTPWarning):
-    "Warned when performing security reducing actions"
-    pass
-
-
-class SubjectAltNameWarning(SecurityWarning):
-    "Warned when connecting to a host with a certificate missing a SAN."
-    pass
-
-
-class InsecureRequestWarning(SecurityWarning):
-    "Warned when making an unverified HTTPS request."
-    pass
-
-
-class SystemTimeWarning(SecurityWarning):
-    "Warned when system time is suspected to be wrong"
-    pass
-
-
-class InsecurePlatformWarning(SecurityWarning):
-    "Warned when certain SSL configuration is not available on a platform."
-    pass
-
-
-class SNIMissingWarning(HTTPWarning):
-    "Warned when making a HTTPS request without SNI available."
-    pass
-
-
-class DependencyWarning(HTTPWarning):
-    """
-    Warned when an attempt is made to import a module with missing optional
-    dependencies.
-    """
-    pass
-
-
-class ResponseNotChunked(ProtocolError, ValueError):
-    "Response needs to be chunked in order to read it as chunks."
-    pass
-
-
-class BodyNotHttplibCompatible(HTTPError):
-    """
-    Body should be httplib.HTTPResponse like (have an fp attribute which
-    returns raw chunks) for read_chunked().
-    """
-    pass
-
-
-class IncompleteRead(HTTPError, httplib_IncompleteRead):
-    """
-    Response length doesn't match expected Content-Length
-
-    Subclass of http_client.IncompleteRead to allow int value
-    for `partial` to avoid creating large objects on streamed
-    reads.
-    """
-    def __init__(self, partial, expected):
-        super(IncompleteRead, self).__init__(partial, expected)
-
-    def __repr__(self):
-        return ('IncompleteRead(%i bytes read, '
-                '%i more expected)' % (self.partial, self.expected))
-
-
-class InvalidHeader(HTTPError):
-    "The header provided was somehow invalid."
-    pass
-
-
-class ProxySchemeUnknown(AssertionError, ValueError):
-    "ProxyManager does not support the supplied scheme"
-    # TODO(t-8ch): Stop inheriting from AssertionError in v2.0.
-
-    def __init__(self, scheme):
-        message = "Not supported proxy scheme %s" % scheme
-        super(ProxySchemeUnknown, self).__init__(message)
-
-
-class HeaderParsingError(HTTPError):
-    "Raised by assert_header_parsing, but we convert it to a log.warning statement."
-    def __init__(self, defects, unparsed_data):
-        message = '%s, unparsed data: %r' % (defects or 'Unknown', unparsed_data)
-        super(HeaderParsingError, self).__init__(message)
-
-
-class UnrewindableBodyError(HTTPError):
-    "urllib3 encountered an error when trying to rewind a body"
-    pass
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/fields.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/fields.py
deleted file mode 100644
index 37fe64a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/fields.py
+++ /dev/null
@@ -1,178 +0,0 @@
-from __future__ import absolute_import
-import email.utils
-import mimetypes
-
-from .packages import six
-
-
-def guess_content_type(filename, default='application/octet-stream'):
-    """
-    Guess the "Content-Type" of a file.
-
-    :param filename:
-        The filename to guess the "Content-Type" of using :mod:`mimetypes`.
-    :param default:
-        If no "Content-Type" can be guessed, default to `default`.
-    """
-    if filename:
-        return mimetypes.guess_type(filename)[0] or default
-    return default
-
-
-def format_header_param(name, value):
-    """
-    Helper function to format and quote a single header parameter.
-
-    Particularly useful for header parameters which might contain
-    non-ASCII values, like file names. This follows RFC 2231, as
-    suggested by RFC 2388 Section 4.4.
-
-    :param name:
-        The name of the parameter, a string expected to be ASCII only.
-    :param value:
-        The value of the parameter, provided as a unicode string.
-    """
-    if not any(ch in value for ch in '"\\\r\n'):
-        result = '%s="%s"' % (name, value)
-        try:
-            result.encode('ascii')
-        except (UnicodeEncodeError, UnicodeDecodeError):
-            pass
-        else:
-            return result
-    if not six.PY3 and isinstance(value, six.text_type):  # Python 2:
-        value = value.encode('utf-8')
-    value = email.utils.encode_rfc2231(value, 'utf-8')
-    value = '%s*=%s' % (name, value)
-    return value
-
-
-class RequestField(object):
-    """
-    A data container for request body parameters.
-
-    :param name:
-        The name of this request field.
-    :param data:
-        The data/value body.
-    :param filename:
-        An optional filename of the request field.
-    :param headers:
-        An optional dict-like object of headers to initially use for the field.
-    """
-    def __init__(self, name, data, filename=None, headers=None):
-        self._name = name
-        self._filename = filename
-        self.data = data
-        self.headers = {}
-        if headers:
-            self.headers = dict(headers)
-
-    @classmethod
-    def from_tuples(cls, fieldname, value):
-        """
-        A :class:`~urllib3.fields.RequestField` factory from old-style tuple parameters.
-
-        Supports constructing :class:`~urllib3.fields.RequestField` from
-        parameter of key/value strings AND key/filetuple. A filetuple is a
-        (filename, data, MIME type) tuple where the MIME type is optional.
-        For example::
-
-            'foo': 'bar',
-            'fakefile': ('foofile.txt', 'contents of foofile'),
-            'realfile': ('barfile.txt', open('realfile').read()),
-            'typedfile': ('bazfile.bin', open('bazfile').read(), 'image/jpeg'),
-            'nonamefile': 'contents of nonamefile field',
-
-        Field names and filenames must be unicode.
-        """
-        if isinstance(value, tuple):
-            if len(value) == 3:
-                filename, data, content_type = value
-            else:
-                filename, data = value
-                content_type = guess_content_type(filename)
-        else:
-            filename = None
-            content_type = None
-            data = value
-
-        request_param = cls(fieldname, data, filename=filename)
-        request_param.make_multipart(content_type=content_type)
-
-        return request_param
-
-    def _render_part(self, name, value):
-        """
-        Overridable helper function to format a single header parameter.
-
-        :param name:
-            The name of the parameter, a string expected to be ASCII only.
-        :param value:
-            The value of the parameter, provided as a unicode string.
-        """
-        return format_header_param(name, value)
-
-    def _render_parts(self, header_parts):
-        """
-        Helper function to format and quote a single header.
-
-        Useful for single headers that are composed of multiple items. E.g.,
-        'Content-Disposition' fields.
-
-        :param header_parts:
-            A sequence of (k, v) tuples or a :class:`dict` of (k, v) to format
-            as `k1="v1"; k2="v2"; ...`.
-        """
-        parts = []
-        iterable = header_parts
-        if isinstance(header_parts, dict):
-            iterable = header_parts.items()
-
-        for name, value in iterable:
-            if value is not None:
-                parts.append(self._render_part(name, value))
-
-        return '; '.join(parts)
-
-    def render_headers(self):
-        """
-        Renders the headers for this request field.
-        """
-        lines = []
-
-        sort_keys = ['Content-Disposition', 'Content-Type', 'Content-Location']
-        for sort_key in sort_keys:
-            if self.headers.get(sort_key, False):
-                lines.append('%s: %s' % (sort_key, self.headers[sort_key]))
-
-        for header_name, header_value in self.headers.items():
-            if header_name not in sort_keys:
-                if header_value:
-                    lines.append('%s: %s' % (header_name, header_value))
-
-        lines.append('\r\n')
-        return '\r\n'.join(lines)
-
-    def make_multipart(self, content_disposition=None, content_type=None,
-                       content_location=None):
-        """
-        Makes this request field into a multipart request field.
-
-        This method overrides "Content-Disposition", "Content-Type" and
-        "Content-Location" headers to the request parameter.
-
-        :param content_type:
-            The 'Content-Type' of the request body.
-        :param content_location:
-            The 'Content-Location' of the request body.
-
-        """
-        self.headers['Content-Disposition'] = content_disposition or 'form-data'
-        self.headers['Content-Disposition'] += '; '.join([
-            '', self._render_parts(
-                (('name', self._name), ('filename', self._filename))
-            )
-        ])
-        self.headers['Content-Type'] = content_type
-        self.headers['Content-Location'] = content_location
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/filepost.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/filepost.py
deleted file mode 100644
index 78f1e19..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/filepost.py
+++ /dev/null
@@ -1,98 +0,0 @@
-from __future__ import absolute_import
-import binascii
-import codecs
-import os
-
-from io import BytesIO
-
-from .packages import six
-from .packages.six import b
-from .fields import RequestField
-
-writer = codecs.lookup('utf-8')[3]
-
-
-def choose_boundary():
-    """
-    Our embarrassingly-simple replacement for mimetools.choose_boundary.
-    """
-    boundary = binascii.hexlify(os.urandom(16))
-    if six.PY3:
-        boundary = boundary.decode('ascii')
-    return boundary
-
-
-def iter_field_objects(fields):
-    """
-    Iterate over fields.
-
-    Supports list of (k, v) tuples and dicts, and lists of
-    :class:`~urllib3.fields.RequestField`.
-
-    """
-    if isinstance(fields, dict):
-        i = six.iteritems(fields)
-    else:
-        i = iter(fields)
-
-    for field in i:
-        if isinstance(field, RequestField):
-            yield field
-        else:
-            yield RequestField.from_tuples(*field)
-
-
-def iter_fields(fields):
-    """
-    .. deprecated:: 1.6
-
-    Iterate over fields.
-
-    The addition of :class:`~urllib3.fields.RequestField` makes this function
-    obsolete. Instead, use :func:`iter_field_objects`, which returns
-    :class:`~urllib3.fields.RequestField` objects.
-
-    Supports list of (k, v) tuples and dicts.
-    """
-    if isinstance(fields, dict):
-        return ((k, v) for k, v in six.iteritems(fields))
-
-    return ((k, v) for k, v in fields)
-
-
-def encode_multipart_formdata(fields, boundary=None):
-    """
-    Encode a dictionary of ``fields`` using the multipart/form-data MIME format.
-
-    :param fields:
-        Dictionary of fields or list of (key, :class:`~urllib3.fields.RequestField`).
-
-    :param boundary:
-        If not specified, then a random boundary will be generated using
-        :func:`urllib3.filepost.choose_boundary`.
-    """
-    body = BytesIO()
-    if boundary is None:
-        boundary = choose_boundary()
-
-    for field in iter_field_objects(fields):
-        body.write(b('--%s\r\n' % (boundary)))
-
-        writer(body).write(field.render_headers())
-        data = field.data
-
-        if isinstance(data, int):
-            data = str(data)  # Backwards compatibility
-
-        if isinstance(data, six.text_type):
-            writer(body).write(data)
-        else:
-            body.write(data)
-
-        body.write(b'\r\n')
-
-    body.write(b('--%s--\r\n' % (boundary)))
-
-    content_type = str('multipart/form-data; boundary=%s' % boundary)
-
-    return body.getvalue(), content_type
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__init__.py
deleted file mode 100644
index 170e974..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__init__.py
+++ /dev/null
@@ -1,5 +0,0 @@
-from __future__ import absolute_import
-
-from . import ssl_match_hostname
-
-__all__ = ('ssl_match_hostname', )
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index eb1d7d1..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__pycache__/six.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__pycache__/six.cpython-37.pyc
deleted file mode 100644
index 1447ede..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/__pycache__/six.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/backports/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/backports/__init__.py
deleted file mode 100644
index e69de29..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/backports/__init__.py
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/backports/makefile.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/backports/makefile.py
deleted file mode 100644
index 740db37..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/backports/makefile.py
+++ /dev/null
@@ -1,53 +0,0 @@
-# -*- coding: utf-8 -*-
-"""
-backports.makefile
-~~~~~~~~~~~~~~~~~~
-
-Backports the Python 3 ``socket.makefile`` method for use with anything that
-wants to create a "fake" socket object.
-"""
-import io
-
-from socket import SocketIO
-
-
-def backport_makefile(self, mode="r", buffering=None, encoding=None,
-                      errors=None, newline=None):
-    """
-    Backport of ``socket.makefile`` from Python 3.5.
-    """
-    if not set(mode) <= {"r", "w", "b"}:
-        raise ValueError(
-            "invalid mode %r (only r, w, b allowed)" % (mode,)
-        )
-    writing = "w" in mode
-    reading = "r" in mode or not writing
-    assert reading or writing
-    binary = "b" in mode
-    rawmode = ""
-    if reading:
-        rawmode += "r"
-    if writing:
-        rawmode += "w"
-    raw = SocketIO(self, rawmode)
-    self._makefile_refs += 1
-    if buffering is None:
-        buffering = -1
-    if buffering < 0:
-        buffering = io.DEFAULT_BUFFER_SIZE
-    if buffering == 0:
-        if not binary:
-            raise ValueError("unbuffered streams must be binary")
-        return raw
-    if reading and writing:
-        buffer = io.BufferedRWPair(raw, raw, buffering)
-    elif reading:
-        buffer = io.BufferedReader(raw, buffering)
-    else:
-        assert writing
-        buffer = io.BufferedWriter(raw, buffering)
-    if binary:
-        return buffer
-    text = io.TextIOWrapper(buffer, encoding, errors, newline)
-    text.mode = mode
-    return text
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/six.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/six.py
deleted file mode 100644
index 190c023..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/six.py
+++ /dev/null
@@ -1,868 +0,0 @@
-"""Utilities for writing code that runs on Python 2 and 3"""
-
-# Copyright (c) 2010-2015 Benjamin Peterson
-#
-# Permission is hereby granted, free of charge, to any person obtaining a copy
-# of this software and associated documentation files (the "Software"), to deal
-# in the Software without restriction, including without limitation the rights
-# to use, copy, modify, merge, publish, distribute, sublicense, and/or sell
-# copies of the Software, and to permit persons to whom the Software is
-# furnished to do so, subject to the following conditions:
-#
-# The above copyright notice and this permission notice shall be included in all
-# copies or substantial portions of the Software.
-#
-# THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR
-# IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF MERCHANTABILITY,
-# FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL THE
-# AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER
-# LIABILITY, WHETHER IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING FROM,
-# OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR OTHER DEALINGS IN THE
-# SOFTWARE.
-
-from __future__ import absolute_import
-
-import functools
-import itertools
-import operator
-import sys
-import types
-
-__author__ = "Benjamin Peterson <benjamin@python.org>"
-__version__ = "1.10.0"
-
-
-# Useful for very coarse version differentiation.
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-PY34 = sys.version_info[0:2] >= (3, 4)
-
-if PY3:
-    string_types = str,
-    integer_types = int,
-    class_types = type,
-    text_type = str
-    binary_type = bytes
-
-    MAXSIZE = sys.maxsize
-else:
-    string_types = basestring,
-    integer_types = (int, long)
-    class_types = (type, types.ClassType)
-    text_type = unicode
-    binary_type = str
-
-    if sys.platform.startswith("java"):
-        # Jython always uses 32 bits.
-        MAXSIZE = int((1 << 31) - 1)
-    else:
-        # It's possible to have sizeof(long) != sizeof(Py_ssize_t).
-        class X(object):
-
-            def __len__(self):
-                return 1 << 31
-        try:
-            len(X())
-        except OverflowError:
-            # 32-bit
-            MAXSIZE = int((1 << 31) - 1)
-        else:
-            # 64-bit
-            MAXSIZE = int((1 << 63) - 1)
-        del X
-
-
-def _add_doc(func, doc):
-    """Add documentation to a function."""
-    func.__doc__ = doc
-
-
-def _import_module(name):
-    """Import module, returning the module after the last dot."""
-    __import__(name)
-    return sys.modules[name]
-
-
-class _LazyDescr(object):
-
-    def __init__(self, name):
-        self.name = name
-
-    def __get__(self, obj, tp):
-        result = self._resolve()
-        setattr(obj, self.name, result)  # Invokes __set__.
-        try:
-            # This is a bit ugly, but it avoids running this again by
-            # removing this descriptor.
-            delattr(obj.__class__, self.name)
-        except AttributeError:
-            pass
-        return result
-
-
-class MovedModule(_LazyDescr):
-
-    def __init__(self, name, old, new=None):
-        super(MovedModule, self).__init__(name)
-        if PY3:
-            if new is None:
-                new = name
-            self.mod = new
-        else:
-            self.mod = old
-
-    def _resolve(self):
-        return _import_module(self.mod)
-
-    def __getattr__(self, attr):
-        _module = self._resolve()
-        value = getattr(_module, attr)
-        setattr(self, attr, value)
-        return value
-
-
-class _LazyModule(types.ModuleType):
-
-    def __init__(self, name):
-        super(_LazyModule, self).__init__(name)
-        self.__doc__ = self.__class__.__doc__
-
-    def __dir__(self):
-        attrs = ["__doc__", "__name__"]
-        attrs += [attr.name for attr in self._moved_attributes]
-        return attrs
-
-    # Subclasses should override this
-    _moved_attributes = []
-
-
-class MovedAttribute(_LazyDescr):
-
-    def __init__(self, name, old_mod, new_mod, old_attr=None, new_attr=None):
-        super(MovedAttribute, self).__init__(name)
-        if PY3:
-            if new_mod is None:
-                new_mod = name
-            self.mod = new_mod
-            if new_attr is None:
-                if old_attr is None:
-                    new_attr = name
-                else:
-                    new_attr = old_attr
-            self.attr = new_attr
-        else:
-            self.mod = old_mod
-            if old_attr is None:
-                old_attr = name
-            self.attr = old_attr
-
-    def _resolve(self):
-        module = _import_module(self.mod)
-        return getattr(module, self.attr)
-
-
-class _SixMetaPathImporter(object):
-
-    """
-    A meta path importer to import six.moves and its submodules.
-
-    This class implements a PEP302 finder and loader. It should be compatible
-    with Python 2.5 and all existing versions of Python3
-    """
-
-    def __init__(self, six_module_name):
-        self.name = six_module_name
-        self.known_modules = {}
-
-    def _add_module(self, mod, *fullnames):
-        for fullname in fullnames:
-            self.known_modules[self.name + "." + fullname] = mod
-
-    def _get_module(self, fullname):
-        return self.known_modules[self.name + "." + fullname]
-
-    def find_module(self, fullname, path=None):
-        if fullname in self.known_modules:
-            return self
-        return None
-
-    def __get_module(self, fullname):
-        try:
-            return self.known_modules[fullname]
-        except KeyError:
-            raise ImportError("This loader does not know module " + fullname)
-
-    def load_module(self, fullname):
-        try:
-            # in case of a reload
-            return sys.modules[fullname]
-        except KeyError:
-            pass
-        mod = self.__get_module(fullname)
-        if isinstance(mod, MovedModule):
-            mod = mod._resolve()
-        else:
-            mod.__loader__ = self
-        sys.modules[fullname] = mod
-        return mod
-
-    def is_package(self, fullname):
-        """
-        Return true, if the named module is a package.
-
-        We need this method to get correct spec objects with
-        Python 3.4 (see PEP451)
-        """
-        return hasattr(self.__get_module(fullname), "__path__")
-
-    def get_code(self, fullname):
-        """Return None
-
-        Required, if is_package is implemented"""
-        self.__get_module(fullname)  # eventually raises ImportError
-        return None
-    get_source = get_code  # same as get_code
-
-_importer = _SixMetaPathImporter(__name__)
-
-
-class _MovedItems(_LazyModule):
-
-    """Lazy loading of moved objects"""
-    __path__ = []  # mark as package
-
-
-_moved_attributes = [
-    MovedAttribute("cStringIO", "cStringIO", "io", "StringIO"),
-    MovedAttribute("filter", "itertools", "builtins", "ifilter", "filter"),
-    MovedAttribute("filterfalse", "itertools", "itertools", "ifilterfalse", "filterfalse"),
-    MovedAttribute("input", "__builtin__", "builtins", "raw_input", "input"),
-    MovedAttribute("intern", "__builtin__", "sys"),
-    MovedAttribute("map", "itertools", "builtins", "imap", "map"),
-    MovedAttribute("getcwd", "os", "os", "getcwdu", "getcwd"),
-    MovedAttribute("getcwdb", "os", "os", "getcwd", "getcwdb"),
-    MovedAttribute("range", "__builtin__", "builtins", "xrange", "range"),
-    MovedAttribute("reload_module", "__builtin__", "importlib" if PY34 else "imp", "reload"),
-    MovedAttribute("reduce", "__builtin__", "functools"),
-    MovedAttribute("shlex_quote", "pipes", "shlex", "quote"),
-    MovedAttribute("StringIO", "StringIO", "io"),
-    MovedAttribute("UserDict", "UserDict", "collections"),
-    MovedAttribute("UserList", "UserList", "collections"),
-    MovedAttribute("UserString", "UserString", "collections"),
-    MovedAttribute("xrange", "__builtin__", "builtins", "xrange", "range"),
-    MovedAttribute("zip", "itertools", "builtins", "izip", "zip"),
-    MovedAttribute("zip_longest", "itertools", "itertools", "izip_longest", "zip_longest"),
-    MovedModule("builtins", "__builtin__"),
-    MovedModule("configparser", "ConfigParser"),
-    MovedModule("copyreg", "copy_reg"),
-    MovedModule("dbm_gnu", "gdbm", "dbm.gnu"),
-    MovedModule("_dummy_thread", "dummy_thread", "_dummy_thread"),
-    MovedModule("http_cookiejar", "cookielib", "http.cookiejar"),
-    MovedModule("http_cookies", "Cookie", "http.cookies"),
-    MovedModule("html_entities", "htmlentitydefs", "html.entities"),
-    MovedModule("html_parser", "HTMLParser", "html.parser"),
-    MovedModule("http_client", "httplib", "http.client"),
-    MovedModule("email_mime_multipart", "email.MIMEMultipart", "email.mime.multipart"),
-    MovedModule("email_mime_nonmultipart", "email.MIMENonMultipart", "email.mime.nonmultipart"),
-    MovedModule("email_mime_text", "email.MIMEText", "email.mime.text"),
-    MovedModule("email_mime_base", "email.MIMEBase", "email.mime.base"),
-    MovedModule("BaseHTTPServer", "BaseHTTPServer", "http.server"),
-    MovedModule("CGIHTTPServer", "CGIHTTPServer", "http.server"),
-    MovedModule("SimpleHTTPServer", "SimpleHTTPServer", "http.server"),
-    MovedModule("cPickle", "cPickle", "pickle"),
-    MovedModule("queue", "Queue"),
-    MovedModule("reprlib", "repr"),
-    MovedModule("socketserver", "SocketServer"),
-    MovedModule("_thread", "thread", "_thread"),
-    MovedModule("tkinter", "Tkinter"),
-    MovedModule("tkinter_dialog", "Dialog", "tkinter.dialog"),
-    MovedModule("tkinter_filedialog", "FileDialog", "tkinter.filedialog"),
-    MovedModule("tkinter_scrolledtext", "ScrolledText", "tkinter.scrolledtext"),
-    MovedModule("tkinter_simpledialog", "SimpleDialog", "tkinter.simpledialog"),
-    MovedModule("tkinter_tix", "Tix", "tkinter.tix"),
-    MovedModule("tkinter_ttk", "ttk", "tkinter.ttk"),
-    MovedModule("tkinter_constants", "Tkconstants", "tkinter.constants"),
-    MovedModule("tkinter_dnd", "Tkdnd", "tkinter.dnd"),
-    MovedModule("tkinter_colorchooser", "tkColorChooser",
-                "tkinter.colorchooser"),
-    MovedModule("tkinter_commondialog", "tkCommonDialog",
-                "tkinter.commondialog"),
-    MovedModule("tkinter_tkfiledialog", "tkFileDialog", "tkinter.filedialog"),
-    MovedModule("tkinter_font", "tkFont", "tkinter.font"),
-    MovedModule("tkinter_messagebox", "tkMessageBox", "tkinter.messagebox"),
-    MovedModule("tkinter_tksimpledialog", "tkSimpleDialog",
-                "tkinter.simpledialog"),
-    MovedModule("urllib_parse", __name__ + ".moves.urllib_parse", "urllib.parse"),
-    MovedModule("urllib_error", __name__ + ".moves.urllib_error", "urllib.error"),
-    MovedModule("urllib", __name__ + ".moves.urllib", __name__ + ".moves.urllib"),
-    MovedModule("urllib_robotparser", "robotparser", "urllib.robotparser"),
-    MovedModule("xmlrpc_client", "xmlrpclib", "xmlrpc.client"),
-    MovedModule("xmlrpc_server", "SimpleXMLRPCServer", "xmlrpc.server"),
-]
-# Add windows specific modules.
-if sys.platform == "win32":
-    _moved_attributes += [
-        MovedModule("winreg", "_winreg"),
-    ]
-
-for attr in _moved_attributes:
-    setattr(_MovedItems, attr.name, attr)
-    if isinstance(attr, MovedModule):
-        _importer._add_module(attr, "moves." + attr.name)
-del attr
-
-_MovedItems._moved_attributes = _moved_attributes
-
-moves = _MovedItems(__name__ + ".moves")
-_importer._add_module(moves, "moves")
-
-
-class Module_six_moves_urllib_parse(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_parse"""
-
-
-_urllib_parse_moved_attributes = [
-    MovedAttribute("ParseResult", "urlparse", "urllib.parse"),
-    MovedAttribute("SplitResult", "urlparse", "urllib.parse"),
-    MovedAttribute("parse_qs", "urlparse", "urllib.parse"),
-    MovedAttribute("parse_qsl", "urlparse", "urllib.parse"),
-    MovedAttribute("urldefrag", "urlparse", "urllib.parse"),
-    MovedAttribute("urljoin", "urlparse", "urllib.parse"),
-    MovedAttribute("urlparse", "urlparse", "urllib.parse"),
-    MovedAttribute("urlsplit", "urlparse", "urllib.parse"),
-    MovedAttribute("urlunparse", "urlparse", "urllib.parse"),
-    MovedAttribute("urlunsplit", "urlparse", "urllib.parse"),
-    MovedAttribute("quote", "urllib", "urllib.parse"),
-    MovedAttribute("quote_plus", "urllib", "urllib.parse"),
-    MovedAttribute("unquote", "urllib", "urllib.parse"),
-    MovedAttribute("unquote_plus", "urllib", "urllib.parse"),
-    MovedAttribute("urlencode", "urllib", "urllib.parse"),
-    MovedAttribute("splitquery", "urllib", "urllib.parse"),
-    MovedAttribute("splittag", "urllib", "urllib.parse"),
-    MovedAttribute("splituser", "urllib", "urllib.parse"),
-    MovedAttribute("uses_fragment", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_netloc", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_params", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_query", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_relative", "urlparse", "urllib.parse"),
-]
-for attr in _urllib_parse_moved_attributes:
-    setattr(Module_six_moves_urllib_parse, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_parse._moved_attributes = _urllib_parse_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_parse(__name__ + ".moves.urllib_parse"),
-                      "moves.urllib_parse", "moves.urllib.parse")
-
-
-class Module_six_moves_urllib_error(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_error"""
-
-
-_urllib_error_moved_attributes = [
-    MovedAttribute("URLError", "urllib2", "urllib.error"),
-    MovedAttribute("HTTPError", "urllib2", "urllib.error"),
-    MovedAttribute("ContentTooShortError", "urllib", "urllib.error"),
-]
-for attr in _urllib_error_moved_attributes:
-    setattr(Module_six_moves_urllib_error, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_error._moved_attributes = _urllib_error_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_error(__name__ + ".moves.urllib.error"),
-                      "moves.urllib_error", "moves.urllib.error")
-
-
-class Module_six_moves_urllib_request(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_request"""
-
-
-_urllib_request_moved_attributes = [
-    MovedAttribute("urlopen", "urllib2", "urllib.request"),
-    MovedAttribute("install_opener", "urllib2", "urllib.request"),
-    MovedAttribute("build_opener", "urllib2", "urllib.request"),
-    MovedAttribute("pathname2url", "urllib", "urllib.request"),
-    MovedAttribute("url2pathname", "urllib", "urllib.request"),
-    MovedAttribute("getproxies", "urllib", "urllib.request"),
-    MovedAttribute("Request", "urllib2", "urllib.request"),
-    MovedAttribute("OpenerDirector", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPDefaultErrorHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPRedirectHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPCookieProcessor", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyHandler", "urllib2", "urllib.request"),
-    MovedAttribute("BaseHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPPasswordMgr", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPPasswordMgrWithDefaultRealm", "urllib2", "urllib.request"),
-    MovedAttribute("AbstractBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("AbstractDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPSHandler", "urllib2", "urllib.request"),
-    MovedAttribute("FileHandler", "urllib2", "urllib.request"),
-    MovedAttribute("FTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("CacheFTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("UnknownHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPErrorProcessor", "urllib2", "urllib.request"),
-    MovedAttribute("urlretrieve", "urllib", "urllib.request"),
-    MovedAttribute("urlcleanup", "urllib", "urllib.request"),
-    MovedAttribute("URLopener", "urllib", "urllib.request"),
-    MovedAttribute("FancyURLopener", "urllib", "urllib.request"),
-    MovedAttribute("proxy_bypass", "urllib", "urllib.request"),
-]
-for attr in _urllib_request_moved_attributes:
-    setattr(Module_six_moves_urllib_request, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_request._moved_attributes = _urllib_request_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_request(__name__ + ".moves.urllib.request"),
-                      "moves.urllib_request", "moves.urllib.request")
-
-
-class Module_six_moves_urllib_response(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_response"""
-
-
-_urllib_response_moved_attributes = [
-    MovedAttribute("addbase", "urllib", "urllib.response"),
-    MovedAttribute("addclosehook", "urllib", "urllib.response"),
-    MovedAttribute("addinfo", "urllib", "urllib.response"),
-    MovedAttribute("addinfourl", "urllib", "urllib.response"),
-]
-for attr in _urllib_response_moved_attributes:
-    setattr(Module_six_moves_urllib_response, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_response._moved_attributes = _urllib_response_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_response(__name__ + ".moves.urllib.response"),
-                      "moves.urllib_response", "moves.urllib.response")
-
-
-class Module_six_moves_urllib_robotparser(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_robotparser"""
-
-
-_urllib_robotparser_moved_attributes = [
-    MovedAttribute("RobotFileParser", "robotparser", "urllib.robotparser"),
-]
-for attr in _urllib_robotparser_moved_attributes:
-    setattr(Module_six_moves_urllib_robotparser, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_robotparser._moved_attributes = _urllib_robotparser_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_robotparser(__name__ + ".moves.urllib.robotparser"),
-                      "moves.urllib_robotparser", "moves.urllib.robotparser")
-
-
-class Module_six_moves_urllib(types.ModuleType):
-
-    """Create a six.moves.urllib namespace that resembles the Python 3 namespace"""
-    __path__ = []  # mark as package
-    parse = _importer._get_module("moves.urllib_parse")
-    error = _importer._get_module("moves.urllib_error")
-    request = _importer._get_module("moves.urllib_request")
-    response = _importer._get_module("moves.urllib_response")
-    robotparser = _importer._get_module("moves.urllib_robotparser")
-
-    def __dir__(self):
-        return ['parse', 'error', 'request', 'response', 'robotparser']
-
-_importer._add_module(Module_six_moves_urllib(__name__ + ".moves.urllib"),
-                      "moves.urllib")
-
-
-def add_move(move):
-    """Add an item to six.moves."""
-    setattr(_MovedItems, move.name, move)
-
-
-def remove_move(name):
-    """Remove item from six.moves."""
-    try:
-        delattr(_MovedItems, name)
-    except AttributeError:
-        try:
-            del moves.__dict__[name]
-        except KeyError:
-            raise AttributeError("no such move, %r" % (name,))
-
-
-if PY3:
-    _meth_func = "__func__"
-    _meth_self = "__self__"
-
-    _func_closure = "__closure__"
-    _func_code = "__code__"
-    _func_defaults = "__defaults__"
-    _func_globals = "__globals__"
-else:
-    _meth_func = "im_func"
-    _meth_self = "im_self"
-
-    _func_closure = "func_closure"
-    _func_code = "func_code"
-    _func_defaults = "func_defaults"
-    _func_globals = "func_globals"
-
-
-try:
-    advance_iterator = next
-except NameError:
-    def advance_iterator(it):
-        return it.next()
-next = advance_iterator
-
-
-try:
-    callable = callable
-except NameError:
-    def callable(obj):
-        return any("__call__" in klass.__dict__ for klass in type(obj).__mro__)
-
-
-if PY3:
-    def get_unbound_function(unbound):
-        return unbound
-
-    create_bound_method = types.MethodType
-
-    def create_unbound_method(func, cls):
-        return func
-
-    Iterator = object
-else:
-    def get_unbound_function(unbound):
-        return unbound.im_func
-
-    def create_bound_method(func, obj):
-        return types.MethodType(func, obj, obj.__class__)
-
-    def create_unbound_method(func, cls):
-        return types.MethodType(func, None, cls)
-
-    class Iterator(object):
-
-        def next(self):
-            return type(self).__next__(self)
-
-    callable = callable
-_add_doc(get_unbound_function,
-         """Get the function out of a possibly unbound function""")
-
-
-get_method_function = operator.attrgetter(_meth_func)
-get_method_self = operator.attrgetter(_meth_self)
-get_function_closure = operator.attrgetter(_func_closure)
-get_function_code = operator.attrgetter(_func_code)
-get_function_defaults = operator.attrgetter(_func_defaults)
-get_function_globals = operator.attrgetter(_func_globals)
-
-
-if PY3:
-    def iterkeys(d, **kw):
-        return iter(d.keys(**kw))
-
-    def itervalues(d, **kw):
-        return iter(d.values(**kw))
-
-    def iteritems(d, **kw):
-        return iter(d.items(**kw))
-
-    def iterlists(d, **kw):
-        return iter(d.lists(**kw))
-
-    viewkeys = operator.methodcaller("keys")
-
-    viewvalues = operator.methodcaller("values")
-
-    viewitems = operator.methodcaller("items")
-else:
-    def iterkeys(d, **kw):
-        return d.iterkeys(**kw)
-
-    def itervalues(d, **kw):
-        return d.itervalues(**kw)
-
-    def iteritems(d, **kw):
-        return d.iteritems(**kw)
-
-    def iterlists(d, **kw):
-        return d.iterlists(**kw)
-
-    viewkeys = operator.methodcaller("viewkeys")
-
-    viewvalues = operator.methodcaller("viewvalues")
-
-    viewitems = operator.methodcaller("viewitems")
-
-_add_doc(iterkeys, "Return an iterator over the keys of a dictionary.")
-_add_doc(itervalues, "Return an iterator over the values of a dictionary.")
-_add_doc(iteritems,
-         "Return an iterator over the (key, value) pairs of a dictionary.")
-_add_doc(iterlists,
-         "Return an iterator over the (key, [values]) pairs of a dictionary.")
-
-
-if PY3:
-    def b(s):
-        return s.encode("latin-1")
-
-    def u(s):
-        return s
-    unichr = chr
-    import struct
-    int2byte = struct.Struct(">B").pack
-    del struct
-    byte2int = operator.itemgetter(0)
-    indexbytes = operator.getitem
-    iterbytes = iter
-    import io
-    StringIO = io.StringIO
-    BytesIO = io.BytesIO
-    _assertCountEqual = "assertCountEqual"
-    if sys.version_info[1] <= 1:
-        _assertRaisesRegex = "assertRaisesRegexp"
-        _assertRegex = "assertRegexpMatches"
-    else:
-        _assertRaisesRegex = "assertRaisesRegex"
-        _assertRegex = "assertRegex"
-else:
-    def b(s):
-        return s
-    # Workaround for standalone backslash
-
-    def u(s):
-        return unicode(s.replace(r'\\', r'\\\\'), "unicode_escape")
-    unichr = unichr
-    int2byte = chr
-
-    def byte2int(bs):
-        return ord(bs[0])
-
-    def indexbytes(buf, i):
-        return ord(buf[i])
-    iterbytes = functools.partial(itertools.imap, ord)
-    import StringIO
-    StringIO = BytesIO = StringIO.StringIO
-    _assertCountEqual = "assertItemsEqual"
-    _assertRaisesRegex = "assertRaisesRegexp"
-    _assertRegex = "assertRegexpMatches"
-_add_doc(b, """Byte literal""")
-_add_doc(u, """Text literal""")
-
-
-def assertCountEqual(self, *args, **kwargs):
-    return getattr(self, _assertCountEqual)(*args, **kwargs)
-
-
-def assertRaisesRegex(self, *args, **kwargs):
-    return getattr(self, _assertRaisesRegex)(*args, **kwargs)
-
-
-def assertRegex(self, *args, **kwargs):
-    return getattr(self, _assertRegex)(*args, **kwargs)
-
-
-if PY3:
-    exec_ = getattr(moves.builtins, "exec")
-
-    def reraise(tp, value, tb=None):
-        if value is None:
-            value = tp()
-        if value.__traceback__ is not tb:
-            raise value.with_traceback(tb)
-        raise value
-
-else:
-    def exec_(_code_, _globs_=None, _locs_=None):
-        """Execute code in a namespace."""
-        if _globs_ is None:
-            frame = sys._getframe(1)
-            _globs_ = frame.f_globals
-            if _locs_ is None:
-                _locs_ = frame.f_locals
-            del frame
-        elif _locs_ is None:
-            _locs_ = _globs_
-        exec("""exec _code_ in _globs_, _locs_""")
-
-    exec_("""def reraise(tp, value, tb=None):
-    raise tp, value, tb
-""")
-
-
-if sys.version_info[:2] == (3, 2):
-    exec_("""def raise_from(value, from_value):
-    if from_value is None:
-        raise value
-    raise value from from_value
-""")
-elif sys.version_info[:2] > (3, 2):
-    exec_("""def raise_from(value, from_value):
-    raise value from from_value
-""")
-else:
-    def raise_from(value, from_value):
-        raise value
-
-
-print_ = getattr(moves.builtins, "print", None)
-if print_ is None:
-    def print_(*args, **kwargs):
-        """The new-style print function for Python 2.4 and 2.5."""
-        fp = kwargs.pop("file", sys.stdout)
-        if fp is None:
-            return
-
-        def write(data):
-            if not isinstance(data, basestring):
-                data = str(data)
-            # If the file has an encoding, encode unicode with it.
-            if (isinstance(fp, file) and
-                    isinstance(data, unicode) and
-                    fp.encoding is not None):
-                errors = getattr(fp, "errors", None)
-                if errors is None:
-                    errors = "strict"
-                data = data.encode(fp.encoding, errors)
-            fp.write(data)
-        want_unicode = False
-        sep = kwargs.pop("sep", None)
-        if sep is not None:
-            if isinstance(sep, unicode):
-                want_unicode = True
-            elif not isinstance(sep, str):
-                raise TypeError("sep must be None or a string")
-        end = kwargs.pop("end", None)
-        if end is not None:
-            if isinstance(end, unicode):
-                want_unicode = True
-            elif not isinstance(end, str):
-                raise TypeError("end must be None or a string")
-        if kwargs:
-            raise TypeError("invalid keyword arguments to print()")
-        if not want_unicode:
-            for arg in args:
-                if isinstance(arg, unicode):
-                    want_unicode = True
-                    break
-        if want_unicode:
-            newline = unicode("\n")
-            space = unicode(" ")
-        else:
-            newline = "\n"
-            space = " "
-        if sep is None:
-            sep = space
-        if end is None:
-            end = newline
-        for i, arg in enumerate(args):
-            if i:
-                write(sep)
-            write(arg)
-        write(end)
-if sys.version_info[:2] < (3, 3):
-    _print = print_
-
-    def print_(*args, **kwargs):
-        fp = kwargs.get("file", sys.stdout)
-        flush = kwargs.pop("flush", False)
-        _print(*args, **kwargs)
-        if flush and fp is not None:
-            fp.flush()
-
-_add_doc(reraise, """Reraise an exception.""")
-
-if sys.version_info[0:2] < (3, 4):
-    def wraps(wrapped, assigned=functools.WRAPPER_ASSIGNMENTS,
-              updated=functools.WRAPPER_UPDATES):
-        def wrapper(f):
-            f = functools.wraps(wrapped, assigned, updated)(f)
-            f.__wrapped__ = wrapped
-            return f
-        return wrapper
-else:
-    wraps = functools.wraps
-
-
-def with_metaclass(meta, *bases):
-    """Create a base class with a metaclass."""
-    # This requires a bit of explanation: the basic idea is to make a dummy
-    # metaclass for one level of class instantiation that replaces itself with
-    # the actual metaclass.
-    class metaclass(meta):
-
-        def __new__(cls, name, this_bases, d):
-            return meta(name, bases, d)
-    return type.__new__(metaclass, 'temporary_class', (), {})
-
-
-def add_metaclass(metaclass):
-    """Class decorator for creating a class with a metaclass."""
-    def wrapper(cls):
-        orig_vars = cls.__dict__.copy()
-        slots = orig_vars.get('__slots__')
-        if slots is not None:
-            if isinstance(slots, str):
-                slots = [slots]
-            for slots_var in slots:
-                orig_vars.pop(slots_var)
-        orig_vars.pop('__dict__', None)
-        orig_vars.pop('__weakref__', None)
-        return metaclass(cls.__name__, cls.__bases__, orig_vars)
-    return wrapper
-
-
-def python_2_unicode_compatible(klass):
-    """
-    A decorator that defines __unicode__ and __str__ methods under Python 2.
-    Under Python 3 it does nothing.
-
-    To support Python 2 and 3 with a single code base, define a __str__ method
-    returning text and apply this decorator to the class.
-    """
-    if PY2:
-        if '__str__' not in klass.__dict__:
-            raise ValueError("@python_2_unicode_compatible cannot be applied "
-                             "to %s because it doesn't define __str__()." %
-                             klass.__name__)
-        klass.__unicode__ = klass.__str__
-        klass.__str__ = lambda self: self.__unicode__().encode('utf-8')
-    return klass
-
-
-# Complete the moves implementation.
-# This code is at the end of this module to speed up module loading.
-# Turn this module into a package.
-__path__ = []  # required for PEP 302 and PEP 451
-__package__ = __name__  # see PEP 366 @ReservedAssignment
-if globals().get("__spec__") is not None:
-    __spec__.submodule_search_locations = []  # PEP 451 @UndefinedVariable
-# Remove other six meta path importers, since they cause problems. This can
-# happen if six is removed from sys.modules and then reloaded. (Setuptools does
-# this for some reason.)
-if sys.meta_path:
-    for i, importer in enumerate(sys.meta_path):
-        # Here's some real nastiness: Another "instance" of the six module might
-        # be floating around. Therefore, we can't use isinstance() to check for
-        # the six meta path importer, since the other six instance will have
-        # inserted an importer with different class.
-        if (type(importer).__name__ == "_SixMetaPathImporter" and
-                importer.name == __name__):
-            del sys.meta_path[i]
-            break
-    del i, importer
-# Finally, add the importer to the meta path import hook.
-sys.meta_path.append(_importer)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/__init__.py
deleted file mode 100644
index d6594eb..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/__init__.py
+++ /dev/null
@@ -1,19 +0,0 @@
-import sys
-
-try:
-    # Our match_hostname function is the same as 3.5's, so we only want to
-    # import the match_hostname function if it's at least that good.
-    if sys.version_info < (3, 5):
-        raise ImportError("Fallback to vendored code")
-
-    from ssl import CertificateError, match_hostname
-except ImportError:
-    try:
-        # Backport of the function from a pypi module
-        from backports.ssl_match_hostname import CertificateError, match_hostname
-    except ImportError:
-        # Our vendored copy
-        from ._implementation import CertificateError, match_hostname
-
-# Not needed, but documenting what we provide.
-__all__ = ('CertificateError', 'match_hostname')
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 247f178..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/_implementation.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/_implementation.py
deleted file mode 100644
index 970cf65..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/packages/ssl_match_hostname/_implementation.py
+++ /dev/null
@@ -1,156 +0,0 @@
-"""The match_hostname() function from Python 3.3.3, essential when using SSL."""
-
-# Note: This file is under the PSF license as the code comes from the python
-# stdlib.   http://docs.python.org/3/license.html
-
-import re
-import sys
-
-# ipaddress has been backported to 2.6+ in pypi.  If it is installed on the
-# system, use it to handle IPAddress ServerAltnames (this was added in
-# python-3.5) otherwise only do DNS matching.  This allows
-# backports.ssl_match_hostname to continue to be used in Python 2.7.
-try:
-    from pip._vendor import ipaddress
-except ImportError:
-    ipaddress = None
-
-__version__ = '3.5.0.1'
-
-
-class CertificateError(ValueError):
-    pass
-
-
-def _dnsname_match(dn, hostname, max_wildcards=1):
-    """Matching according to RFC 6125, section 6.4.3
-
-    http://tools.ietf.org/html/rfc6125#section-6.4.3
-    """
-    pats = []
-    if not dn:
-        return False
-
-    # Ported from python3-syntax:
-    # leftmost, *remainder = dn.split(r'.')
-    parts = dn.split(r'.')
-    leftmost = parts[0]
-    remainder = parts[1:]
-
-    wildcards = leftmost.count('*')
-    if wildcards > max_wildcards:
-        # Issue #17980: avoid denials of service by refusing more
-        # than one wildcard per fragment.  A survey of established
-        # policy among SSL implementations showed it to be a
-        # reasonable choice.
-        raise CertificateError(
-            "too many wildcards in certificate DNS name: " + repr(dn))
-
-    # speed up common case w/o wildcards
-    if not wildcards:
-        return dn.lower() == hostname.lower()
-
-    # RFC 6125, section 6.4.3, subitem 1.
-    # The client SHOULD NOT attempt to match a presented identifier in which
-    # the wildcard character comprises a label other than the left-most label.
-    if leftmost == '*':
-        # When '*' is a fragment by itself, it matches a non-empty dotless
-        # fragment.
-        pats.append('[^.]+')
-    elif leftmost.startswith('xn--') or hostname.startswith('xn--'):
-        # RFC 6125, section 6.4.3, subitem 3.
-        # The client SHOULD NOT attempt to match a presented identifier
-        # where the wildcard character is embedded within an A-label or
-        # U-label of an internationalized domain name.
-        pats.append(re.escape(leftmost))
-    else:
-        # Otherwise, '*' matches any dotless string, e.g. www*
-        pats.append(re.escape(leftmost).replace(r'\*', '[^.]*'))
-
-    # add the remaining fragments, ignore any wildcards
-    for frag in remainder:
-        pats.append(re.escape(frag))
-
-    pat = re.compile(r'\A' + r'\.'.join(pats) + r'\Z', re.IGNORECASE)
-    return pat.match(hostname)
-
-
-def _to_unicode(obj):
-    if isinstance(obj, str) and sys.version_info < (3,):
-        obj = unicode(obj, encoding='ascii', errors='strict')
-    return obj
-
-def _ipaddress_match(ipname, host_ip):
-    """Exact matching of IP addresses.
-
-    RFC 6125 explicitly doesn't define an algorithm for this
-    (section 1.7.2 - "Out of Scope").
-    """
-    # OpenSSL may add a trailing newline to a subjectAltName's IP address
-    # Divergence from upstream: ipaddress can't handle byte str
-    ip = ipaddress.ip_address(_to_unicode(ipname).rstrip())
-    return ip == host_ip
-
-
-def match_hostname(cert, hostname):
-    """Verify that *cert* (in decoded format as returned by
-    SSLSocket.getpeercert()) matches the *hostname*.  RFC 2818 and RFC 6125
-    rules are followed, but IP addresses are not accepted for *hostname*.
-
-    CertificateError is raised on failure. On success, the function
-    returns nothing.
-    """
-    if not cert:
-        raise ValueError("empty or no certificate, match_hostname needs a "
-                         "SSL socket or SSL context with either "
-                         "CERT_OPTIONAL or CERT_REQUIRED")
-    try:
-        # Divergence from upstream: ipaddress can't handle byte str
-        host_ip = ipaddress.ip_address(_to_unicode(hostname))
-    except ValueError:
-        # Not an IP address (common case)
-        host_ip = None
-    except UnicodeError:
-        # Divergence from upstream: Have to deal with ipaddress not taking
-        # byte strings.  addresses should be all ascii, so we consider it not
-        # an ipaddress in this case
-        host_ip = None
-    except AttributeError:
-        # Divergence from upstream: Make ipaddress library optional
-        if ipaddress is None:
-            host_ip = None
-        else:
-            raise
-    dnsnames = []
-    san = cert.get('subjectAltName', ())
-    for key, value in san:
-        if key == 'DNS':
-            if host_ip is None and _dnsname_match(value, hostname):
-                return
-            dnsnames.append(value)
-        elif key == 'IP Address':
-            if host_ip is not None and _ipaddress_match(value, host_ip):
-                return
-            dnsnames.append(value)
-    if not dnsnames:
-        # The subject is only checked when there is no dNSName entry
-        # in subjectAltName
-        for sub in cert.get('subject', ()):
-            for key, value in sub:
-                # XXX according to RFC 2818, the most specific Common Name
-                # must be used.
-                if key == 'commonName':
-                    if _dnsname_match(value, hostname):
-                        return
-                    dnsnames.append(value)
-    if len(dnsnames) > 1:
-        raise CertificateError("hostname %r "
-            "doesn't match either of %s"
-            % (hostname, ', '.join(map(repr, dnsnames))))
-    elif len(dnsnames) == 1:
-        raise CertificateError("hostname %r "
-            "doesn't match %r"
-            % (hostname, dnsnames[0]))
-    else:
-        raise CertificateError("no appropriate commonName or "
-            "subjectAltName fields were found")
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/poolmanager.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/poolmanager.py
deleted file mode 100644
index fe5491c..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/poolmanager.py
+++ /dev/null
@@ -1,450 +0,0 @@
-from __future__ import absolute_import
-import collections
-import functools
-import logging
-
-from ._collections import RecentlyUsedContainer
-from .connectionpool import HTTPConnectionPool, HTTPSConnectionPool
-from .connectionpool import port_by_scheme
-from .exceptions import LocationValueError, MaxRetryError, ProxySchemeUnknown
-from .packages.six.moves.urllib.parse import urljoin
-from .request import RequestMethods
-from .util.url import parse_url
-from .util.retry import Retry
-
-
-__all__ = ['PoolManager', 'ProxyManager', 'proxy_from_url']
-
-
-log = logging.getLogger(__name__)
-
-SSL_KEYWORDS = ('key_file', 'cert_file', 'cert_reqs', 'ca_certs',
-                'ssl_version', 'ca_cert_dir', 'ssl_context')
-
-# All known keyword arguments that could be provided to the pool manager, its
-# pools, or the underlying connections. This is used to construct a pool key.
-_key_fields = (
-    'key_scheme',  # str
-    'key_host',  # str
-    'key_port',  # int
-    'key_timeout',  # int or float or Timeout
-    'key_retries',  # int or Retry
-    'key_strict',  # bool
-    'key_block',  # bool
-    'key_source_address',  # str
-    'key_key_file',  # str
-    'key_cert_file',  # str
-    'key_cert_reqs',  # str
-    'key_ca_certs',  # str
-    'key_ssl_version',  # str
-    'key_ca_cert_dir',  # str
-    'key_ssl_context',  # instance of ssl.SSLContext or urllib3.util.ssl_.SSLContext
-    'key_maxsize',  # int
-    'key_headers',  # dict
-    'key__proxy',  # parsed proxy url
-    'key__proxy_headers',  # dict
-    'key_socket_options',  # list of (level (int), optname (int), value (int or str)) tuples
-    'key__socks_options',  # dict
-    'key_assert_hostname',  # bool or string
-    'key_assert_fingerprint',  # str
-    'key_server_hostname', #str
-)
-
-#: The namedtuple class used to construct keys for the connection pool.
-#: All custom key schemes should include the fields in this key at a minimum.
-PoolKey = collections.namedtuple('PoolKey', _key_fields)
-
-
-def _default_key_normalizer(key_class, request_context):
-    """
-    Create a pool key out of a request context dictionary.
-
-    According to RFC 3986, both the scheme and host are case-insensitive.
-    Therefore, this function normalizes both before constructing the pool
-    key for an HTTPS request. If you wish to change this behaviour, provide
-    alternate callables to ``key_fn_by_scheme``.
-
-    :param key_class:
-        The class to use when constructing the key. This should be a namedtuple
-        with the ``scheme`` and ``host`` keys at a minimum.
-    :type  key_class: namedtuple
-    :param request_context:
-        A dictionary-like object that contain the context for a request.
-    :type  request_context: dict
-
-    :return: A namedtuple that can be used as a connection pool key.
-    :rtype:  PoolKey
-    """
-    # Since we mutate the dictionary, make a copy first
-    context = request_context.copy()
-    context['scheme'] = context['scheme'].lower()
-    context['host'] = context['host'].lower()
-
-    # These are both dictionaries and need to be transformed into frozensets
-    for key in ('headers', '_proxy_headers', '_socks_options'):
-        if key in context and context[key] is not None:
-            context[key] = frozenset(context[key].items())
-
-    # The socket_options key may be a list and needs to be transformed into a
-    # tuple.
-    socket_opts = context.get('socket_options')
-    if socket_opts is not None:
-        context['socket_options'] = tuple(socket_opts)
-
-    # Map the kwargs to the names in the namedtuple - this is necessary since
-    # namedtuples can't have fields starting with '_'.
-    for key in list(context.keys()):
-        context['key_' + key] = context.pop(key)
-
-    # Default to ``None`` for keys missing from the context
-    for field in key_class._fields:
-        if field not in context:
-            context[field] = None
-
-    return key_class(**context)
-
-
-#: A dictionary that maps a scheme to a callable that creates a pool key.
-#: This can be used to alter the way pool keys are constructed, if desired.
-#: Each PoolManager makes a copy of this dictionary so they can be configured
-#: globally here, or individually on the instance.
-key_fn_by_scheme = {
-    'http': functools.partial(_default_key_normalizer, PoolKey),
-    'https': functools.partial(_default_key_normalizer, PoolKey),
-}
-
-pool_classes_by_scheme = {
-    'http': HTTPConnectionPool,
-    'https': HTTPSConnectionPool,
-}
-
-
-class PoolManager(RequestMethods):
-    """
-    Allows for arbitrary requests while transparently keeping track of
-    necessary connection pools for you.
-
-    :param num_pools:
-        Number of connection pools to cache before discarding the least
-        recently used pool.
-
-    :param headers:
-        Headers to include with all requests, unless other headers are given
-        explicitly.
-
-    :param \\**connection_pool_kw:
-        Additional parameters are used to create fresh
-        :class:`urllib3.connectionpool.ConnectionPool` instances.
-
-    Example::
-
-        >>> manager = PoolManager(num_pools=2)
-        >>> r = manager.request('GET', 'http://google.com/')
-        >>> r = manager.request('GET', 'http://google.com/mail')
-        >>> r = manager.request('GET', 'http://yahoo.com/')
-        >>> len(manager.pools)
-        2
-
-    """
-
-    proxy = None
-
-    def __init__(self, num_pools=10, headers=None, **connection_pool_kw):
-        RequestMethods.__init__(self, headers)
-        self.connection_pool_kw = connection_pool_kw
-        self.pools = RecentlyUsedContainer(num_pools,
-                                           dispose_func=lambda p: p.close())
-
-        # Locally set the pool classes and keys so other PoolManagers can
-        # override them.
-        self.pool_classes_by_scheme = pool_classes_by_scheme
-        self.key_fn_by_scheme = key_fn_by_scheme.copy()
-
-    def __enter__(self):
-        return self
-
-    def __exit__(self, exc_type, exc_val, exc_tb):
-        self.clear()
-        # Return False to re-raise any potential exceptions
-        return False
-
-    def _new_pool(self, scheme, host, port, request_context=None):
-        """
-        Create a new :class:`ConnectionPool` based on host, port, scheme, and
-        any additional pool keyword arguments.
-
-        If ``request_context`` is provided, it is provided as keyword arguments
-        to the pool class used. This method is used to actually create the
-        connection pools handed out by :meth:`connection_from_url` and
-        companion methods. It is intended to be overridden for customization.
-        """
-        pool_cls = self.pool_classes_by_scheme[scheme]
-        if request_context is None:
-            request_context = self.connection_pool_kw.copy()
-
-        # Although the context has everything necessary to create the pool,
-        # this function has historically only used the scheme, host, and port
-        # in the positional args. When an API change is acceptable these can
-        # be removed.
-        for key in ('scheme', 'host', 'port'):
-            request_context.pop(key, None)
-
-        if scheme == 'http':
-            for kw in SSL_KEYWORDS:
-                request_context.pop(kw, None)
-
-        return pool_cls(host, port, **request_context)
-
-    def clear(self):
-        """
-        Empty our store of pools and direct them all to close.
-
-        This will not affect in-flight connections, but they will not be
-        re-used after completion.
-        """
-        self.pools.clear()
-
-    def connection_from_host(self, host, port=None, scheme='http', pool_kwargs=None):
-        """
-        Get a :class:`ConnectionPool` based on the host, port, and scheme.
-
-        If ``port`` isn't given, it will be derived from the ``scheme`` using
-        ``urllib3.connectionpool.port_by_scheme``. If ``pool_kwargs`` is
-        provided, it is merged with the instance's ``connection_pool_kw``
-        variable and used to create the new connection pool, if one is
-        needed.
-        """
-
-        if not host:
-            raise LocationValueError("No host specified.")
-
-        request_context = self._merge_pool_kwargs(pool_kwargs)
-        request_context['scheme'] = scheme or 'http'
-        if not port:
-            port = port_by_scheme.get(request_context['scheme'].lower(), 80)
-        request_context['port'] = port
-        request_context['host'] = host
-
-        return self.connection_from_context(request_context)
-
-    def connection_from_context(self, request_context):
-        """
-        Get a :class:`ConnectionPool` based on the request context.
-
-        ``request_context`` must at least contain the ``scheme`` key and its
-        value must be a key in ``key_fn_by_scheme`` instance variable.
-        """
-        scheme = request_context['scheme'].lower()
-        pool_key_constructor = self.key_fn_by_scheme[scheme]
-        pool_key = pool_key_constructor(request_context)
-
-        return self.connection_from_pool_key(pool_key, request_context=request_context)
-
-    def connection_from_pool_key(self, pool_key, request_context=None):
-        """
-        Get a :class:`ConnectionPool` based on the provided pool key.
-
-        ``pool_key`` should be a namedtuple that only contains immutable
-        objects. At a minimum it must have the ``scheme``, ``host``, and
-        ``port`` fields.
-        """
-        with self.pools.lock:
-            # If the scheme, host, or port doesn't match existing open
-            # connections, open a new ConnectionPool.
-            pool = self.pools.get(pool_key)
-            if pool:
-                return pool
-
-            # Make a fresh ConnectionPool of the desired type
-            scheme = request_context['scheme']
-            host = request_context['host']
-            port = request_context['port']
-            pool = self._new_pool(scheme, host, port, request_context=request_context)
-            self.pools[pool_key] = pool
-
-        return pool
-
-    def connection_from_url(self, url, pool_kwargs=None):
-        """
-        Similar to :func:`urllib3.connectionpool.connection_from_url`.
-
-        If ``pool_kwargs`` is not provided and a new pool needs to be
-        constructed, ``self.connection_pool_kw`` is used to initialize
-        the :class:`urllib3.connectionpool.ConnectionPool`. If ``pool_kwargs``
-        is provided, it is used instead. Note that if a new pool does not
-        need to be created for the request, the provided ``pool_kwargs`` are
-        not used.
-        """
-        u = parse_url(url)
-        return self.connection_from_host(u.host, port=u.port, scheme=u.scheme,
-                                         pool_kwargs=pool_kwargs)
-
-    def _merge_pool_kwargs(self, override):
-        """
-        Merge a dictionary of override values for self.connection_pool_kw.
-
-        This does not modify self.connection_pool_kw and returns a new dict.
-        Any keys in the override dictionary with a value of ``None`` are
-        removed from the merged dictionary.
-        """
-        base_pool_kwargs = self.connection_pool_kw.copy()
-        if override:
-            for key, value in override.items():
-                if value is None:
-                    try:
-                        del base_pool_kwargs[key]
-                    except KeyError:
-                        pass
-                else:
-                    base_pool_kwargs[key] = value
-        return base_pool_kwargs
-
-    def urlopen(self, method, url, redirect=True, **kw):
-        """
-        Same as :meth:`urllib3.connectionpool.HTTPConnectionPool.urlopen`
-        with custom cross-host redirect logic and only sends the request-uri
-        portion of the ``url``.
-
-        The given ``url`` parameter must be absolute, such that an appropriate
-        :class:`urllib3.connectionpool.ConnectionPool` can be chosen for it.
-        """
-        u = parse_url(url)
-        conn = self.connection_from_host(u.host, port=u.port, scheme=u.scheme)
-
-        kw['assert_same_host'] = False
-        kw['redirect'] = False
-
-        if 'headers' not in kw:
-            kw['headers'] = self.headers.copy()
-
-        if self.proxy is not None and u.scheme == "http":
-            response = conn.urlopen(method, url, **kw)
-        else:
-            response = conn.urlopen(method, u.request_uri, **kw)
-
-        redirect_location = redirect and response.get_redirect_location()
-        if not redirect_location:
-            return response
-
-        # Support relative URLs for redirecting.
-        redirect_location = urljoin(url, redirect_location)
-
-        # RFC 7231, Section 6.4.4
-        if response.status == 303:
-            method = 'GET'
-
-        retries = kw.get('retries')
-        if not isinstance(retries, Retry):
-            retries = Retry.from_int(retries, redirect=redirect)
-
-        # Strip headers marked as unsafe to forward to the redirected location.
-        # Check remove_headers_on_redirect to avoid a potential network call within
-        # conn.is_same_host() which may use socket.gethostbyname() in the future.
-        if (retries.remove_headers_on_redirect
-                and not conn.is_same_host(redirect_location)):
-            for header in retries.remove_headers_on_redirect:
-                kw['headers'].pop(header, None)
-
-        try:
-            retries = retries.increment(method, url, response=response, _pool=conn)
-        except MaxRetryError:
-            if retries.raise_on_redirect:
-                raise
-            return response
-
-        kw['retries'] = retries
-        kw['redirect'] = redirect
-
-        log.info("Redirecting %s -> %s", url, redirect_location)
-        return self.urlopen(method, redirect_location, **kw)
-
-
-class ProxyManager(PoolManager):
-    """
-    Behaves just like :class:`PoolManager`, but sends all requests through
-    the defined proxy, using the CONNECT method for HTTPS URLs.
-
-    :param proxy_url:
-        The URL of the proxy to be used.
-
-    :param proxy_headers:
-        A dictionary containing headers that will be sent to the proxy. In case
-        of HTTP they are being sent with each request, while in the
-        HTTPS/CONNECT case they are sent only once. Could be used for proxy
-        authentication.
-
-    Example:
-        >>> proxy = urllib3.ProxyManager('http://localhost:3128/')
-        >>> r1 = proxy.request('GET', 'http://google.com/')
-        >>> r2 = proxy.request('GET', 'http://httpbin.org/')
-        >>> len(proxy.pools)
-        1
-        >>> r3 = proxy.request('GET', 'https://httpbin.org/')
-        >>> r4 = proxy.request('GET', 'https://twitter.com/')
-        >>> len(proxy.pools)
-        3
-
-    """
-
-    def __init__(self, proxy_url, num_pools=10, headers=None,
-                 proxy_headers=None, **connection_pool_kw):
-
-        if isinstance(proxy_url, HTTPConnectionPool):
-            proxy_url = '%s://%s:%i' % (proxy_url.scheme, proxy_url.host,
-                                        proxy_url.port)
-        proxy = parse_url(proxy_url)
-        if not proxy.port:
-            port = port_by_scheme.get(proxy.scheme, 80)
-            proxy = proxy._replace(port=port)
-
-        if proxy.scheme not in ("http", "https"):
-            raise ProxySchemeUnknown(proxy.scheme)
-
-        self.proxy = proxy
-        self.proxy_headers = proxy_headers or {}
-
-        connection_pool_kw['_proxy'] = self.proxy
-        connection_pool_kw['_proxy_headers'] = self.proxy_headers
-
-        super(ProxyManager, self).__init__(
-            num_pools, headers, **connection_pool_kw)
-
-    def connection_from_host(self, host, port=None, scheme='http', pool_kwargs=None):
-        if scheme == "https":
-            return super(ProxyManager, self).connection_from_host(
-                host, port, scheme, pool_kwargs=pool_kwargs)
-
-        return super(ProxyManager, self).connection_from_host(
-            self.proxy.host, self.proxy.port, self.proxy.scheme, pool_kwargs=pool_kwargs)
-
-    def _set_proxy_headers(self, url, headers=None):
-        """
-        Sets headers needed by proxies: specifically, the Accept and Host
-        headers. Only sets headers not provided by the user.
-        """
-        headers_ = {'Accept': '*/*'}
-
-        netloc = parse_url(url).netloc
-        if netloc:
-            headers_['Host'] = netloc
-
-        if headers:
-            headers_.update(headers)
-        return headers_
-
-    def urlopen(self, method, url, redirect=True, **kw):
-        "Same as HTTP(S)ConnectionPool.urlopen, ``url`` must be absolute."
-        u = parse_url(url)
-
-        if u.scheme == "http":
-            # For proxied HTTPS requests, httplib sets the necessary headers
-            # on the CONNECT to the proxy. For HTTP, we'll definitely
-            # need to set 'Host' at the very least.
-            headers = kw.get('headers', self.headers)
-            kw['headers'] = self._set_proxy_headers(url, headers)
-
-        return super(ProxyManager, self).urlopen(method, url, redirect=redirect, **kw)
-
-
-def proxy_from_url(url, **kw):
-    return ProxyManager(proxy_url=url, **kw)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/request.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/request.py
deleted file mode 100644
index 8f2f44b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/request.py
+++ /dev/null
@@ -1,150 +0,0 @@
-from __future__ import absolute_import
-
-from .filepost import encode_multipart_formdata
-from .packages.six.moves.urllib.parse import urlencode
-
-
-__all__ = ['RequestMethods']
-
-
-class RequestMethods(object):
-    """
-    Convenience mixin for classes who implement a :meth:`urlopen` method, such
-    as :class:`~urllib3.connectionpool.HTTPConnectionPool` and
-    :class:`~urllib3.poolmanager.PoolManager`.
-
-    Provides behavior for making common types of HTTP request methods and
-    decides which type of request field encoding to use.
-
-    Specifically,
-
-    :meth:`.request_encode_url` is for sending requests whose fields are
-    encoded in the URL (such as GET, HEAD, DELETE).
-
-    :meth:`.request_encode_body` is for sending requests whose fields are
-    encoded in the *body* of the request using multipart or www-form-urlencoded
-    (such as for POST, PUT, PATCH).
-
-    :meth:`.request` is for making any kind of request, it will look up the
-    appropriate encoding format and use one of the above two methods to make
-    the request.
-
-    Initializer parameters:
-
-    :param headers:
-        Headers to include with all requests, unless other headers are given
-        explicitly.
-    """
-
-    _encode_url_methods = {'DELETE', 'GET', 'HEAD', 'OPTIONS'}
-
-    def __init__(self, headers=None):
-        self.headers = headers or {}
-
-    def urlopen(self, method, url, body=None, headers=None,
-                encode_multipart=True, multipart_boundary=None,
-                **kw):  # Abstract
-        raise NotImplementedError("Classes extending RequestMethods must implement "
-                                  "their own ``urlopen`` method.")
-
-    def request(self, method, url, fields=None, headers=None, **urlopen_kw):
-        """
-        Make a request using :meth:`urlopen` with the appropriate encoding of
-        ``fields`` based on the ``method`` used.
-
-        This is a convenience method that requires the least amount of manual
-        effort. It can be used in most situations, while still having the
-        option to drop down to more specific methods when necessary, such as
-        :meth:`request_encode_url`, :meth:`request_encode_body`,
-        or even the lowest level :meth:`urlopen`.
-        """
-        method = method.upper()
-
-        urlopen_kw['request_url'] = url
-
-        if method in self._encode_url_methods:
-            return self.request_encode_url(method, url, fields=fields,
-                                           headers=headers,
-                                           **urlopen_kw)
-        else:
-            return self.request_encode_body(method, url, fields=fields,
-                                            headers=headers,
-                                            **urlopen_kw)
-
-    def request_encode_url(self, method, url, fields=None, headers=None,
-                           **urlopen_kw):
-        """
-        Make a request using :meth:`urlopen` with the ``fields`` encoded in
-        the url. This is useful for request methods like GET, HEAD, DELETE, etc.
-        """
-        if headers is None:
-            headers = self.headers
-
-        extra_kw = {'headers': headers}
-        extra_kw.update(urlopen_kw)
-
-        if fields:
-            url += '?' + urlencode(fields)
-
-        return self.urlopen(method, url, **extra_kw)
-
-    def request_encode_body(self, method, url, fields=None, headers=None,
-                            encode_multipart=True, multipart_boundary=None,
-                            **urlopen_kw):
-        """
-        Make a request using :meth:`urlopen` with the ``fields`` encoded in
-        the body. This is useful for request methods like POST, PUT, PATCH, etc.
-
-        When ``encode_multipart=True`` (default), then
-        :meth:`urllib3.filepost.encode_multipart_formdata` is used to encode
-        the payload with the appropriate content type. Otherwise
-        :meth:`urllib.urlencode` is used with the
-        'application/x-www-form-urlencoded' content type.
-
-        Multipart encoding must be used when posting files, and it's reasonably
-        safe to use it in other times too. However, it may break request
-        signing, such as with OAuth.
-
-        Supports an optional ``fields`` parameter of key/value strings AND
-        key/filetuple. A filetuple is a (filename, data, MIME type) tuple where
-        the MIME type is optional. For example::
-
-            fields = {
-                'foo': 'bar',
-                'fakefile': ('foofile.txt', 'contents of foofile'),
-                'realfile': ('barfile.txt', open('realfile').read()),
-                'typedfile': ('bazfile.bin', open('bazfile').read(),
-                              'image/jpeg'),
-                'nonamefile': 'contents of nonamefile field',
-            }
-
-        When uploading a file, providing a filename (the first parameter of the
-        tuple) is optional but recommended to best mimic behavior of browsers.
-
-        Note that if ``headers`` are supplied, the 'Content-Type' header will
-        be overwritten because it depends on the dynamic random boundary string
-        which is used to compose the body of the request. The random boundary
-        string can be explicitly set with the ``multipart_boundary`` parameter.
-        """
-        if headers is None:
-            headers = self.headers
-
-        extra_kw = {'headers': {}}
-
-        if fields:
-            if 'body' in urlopen_kw:
-                raise TypeError(
-                    "request got values for both 'fields' and 'body', can only specify one.")
-
-            if encode_multipart:
-                body, content_type = encode_multipart_formdata(fields, boundary=multipart_boundary)
-            else:
-                body, content_type = urlencode(fields), 'application/x-www-form-urlencoded'
-
-            extra_kw['body'] = body
-            extra_kw['headers'] = {'Content-Type': content_type}
-
-        extra_kw['headers'].update(headers)
-        extra_kw.update(urlopen_kw)
-
-        return self.urlopen(method, url, **extra_kw)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/response.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/response.py
deleted file mode 100644
index c112690..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/response.py
+++ /dev/null
@@ -1,705 +0,0 @@
-from __future__ import absolute_import
-from contextlib import contextmanager
-import zlib
-import io
-import logging
-from socket import timeout as SocketTimeout
-from socket import error as SocketError
-
-from ._collections import HTTPHeaderDict
-from .exceptions import (
-    BodyNotHttplibCompatible, ProtocolError, DecodeError, ReadTimeoutError,
-    ResponseNotChunked, IncompleteRead, InvalidHeader
-)
-from .packages.six import string_types as basestring, PY3
-from .packages.six.moves import http_client as httplib
-from .connection import HTTPException, BaseSSLError
-from .util.response import is_fp_closed, is_response_to_head
-
-log = logging.getLogger(__name__)
-
-
-class DeflateDecoder(object):
-
-    def __init__(self):
-        self._first_try = True
-        self._data = b''
-        self._obj = zlib.decompressobj()
-
-    def __getattr__(self, name):
-        return getattr(self._obj, name)
-
-    def decompress(self, data):
-        if not data:
-            return data
-
-        if not self._first_try:
-            return self._obj.decompress(data)
-
-        self._data += data
-        try:
-            decompressed = self._obj.decompress(data)
-            if decompressed:
-                self._first_try = False
-                self._data = None
-            return decompressed
-        except zlib.error:
-            self._first_try = False
-            self._obj = zlib.decompressobj(-zlib.MAX_WBITS)
-            try:
-                return self.decompress(self._data)
-            finally:
-                self._data = None
-
-
-class GzipDecoderState(object):
-
-    FIRST_MEMBER = 0
-    OTHER_MEMBERS = 1
-    SWALLOW_DATA = 2
-
-
-class GzipDecoder(object):
-
-    def __init__(self):
-        self._obj = zlib.decompressobj(16 + zlib.MAX_WBITS)
-        self._state = GzipDecoderState.FIRST_MEMBER
-
-    def __getattr__(self, name):
-        return getattr(self._obj, name)
-
-    def decompress(self, data):
-        ret = bytearray()
-        if self._state == GzipDecoderState.SWALLOW_DATA or not data:
-            return bytes(ret)
-        while True:
-            try:
-                ret += self._obj.decompress(data)
-            except zlib.error:
-                previous_state = self._state
-                # Ignore data after the first error
-                self._state = GzipDecoderState.SWALLOW_DATA
-                if previous_state == GzipDecoderState.OTHER_MEMBERS:
-                    # Allow trailing garbage acceptable in other gzip clients
-                    return bytes(ret)
-                raise
-            data = self._obj.unused_data
-            if not data:
-                return bytes(ret)
-            self._state = GzipDecoderState.OTHER_MEMBERS
-            self._obj = zlib.decompressobj(16 + zlib.MAX_WBITS)
-
-
-class MultiDecoder(object):
-    """
-    From RFC7231:
-        If one or more encodings have been applied to a representation, the
-        sender that applied the encodings MUST generate a Content-Encoding
-        header field that lists the content codings in the order in which
-        they were applied.
-    """
-
-    def __init__(self, modes):
-        self._decoders = [_get_decoder(m.strip()) for m in modes.split(',')]
-
-    def flush(self):
-        return self._decoders[0].flush()
-
-    def decompress(self, data):
-        for d in reversed(self._decoders):
-            data = d.decompress(data)
-        return data
-
-
-def _get_decoder(mode):
-    if ',' in mode:
-        return MultiDecoder(mode)
-
-    if mode == 'gzip':
-        return GzipDecoder()
-
-    return DeflateDecoder()
-
-
-class HTTPResponse(io.IOBase):
-    """
-    HTTP Response container.
-
-    Backwards-compatible to httplib's HTTPResponse but the response ``body`` is
-    loaded and decoded on-demand when the ``data`` property is accessed.  This
-    class is also compatible with the Python standard library's :mod:`io`
-    module, and can hence be treated as a readable object in the context of that
-    framework.
-
-    Extra parameters for behaviour not present in httplib.HTTPResponse:
-
-    :param preload_content:
-        If True, the response's body will be preloaded during construction.
-
-    :param decode_content:
-        If True, will attempt to decode the body based on the
-        'content-encoding' header.
-
-    :param original_response:
-        When this HTTPResponse wrapper is generated from an httplib.HTTPResponse
-        object, it's convenient to include the original for debug purposes. It's
-        otherwise unused.
-
-    :param retries:
-        The retries contains the last :class:`~urllib3.util.retry.Retry` that
-        was used during the request.
-
-    :param enforce_content_length:
-        Enforce content length checking. Body returned by server must match
-        value of Content-Length header, if present. Otherwise, raise error.
-    """
-
-    CONTENT_DECODERS = ['gzip', 'deflate']
-    REDIRECT_STATUSES = [301, 302, 303, 307, 308]
-
-    def __init__(self, body='', headers=None, status=0, version=0, reason=None,
-                 strict=0, preload_content=True, decode_content=True,
-                 original_response=None, pool=None, connection=None, msg=None,
-                 retries=None, enforce_content_length=False,
-                 request_method=None, request_url=None):
-
-        if isinstance(headers, HTTPHeaderDict):
-            self.headers = headers
-        else:
-            self.headers = HTTPHeaderDict(headers)
-        self.status = status
-        self.version = version
-        self.reason = reason
-        self.strict = strict
-        self.decode_content = decode_content
-        self.retries = retries
-        self.enforce_content_length = enforce_content_length
-
-        self._decoder = None
-        self._body = None
-        self._fp = None
-        self._original_response = original_response
-        self._fp_bytes_read = 0
-        self.msg = msg
-        self._request_url = request_url
-
-        if body and isinstance(body, (basestring, bytes)):
-            self._body = body
-
-        self._pool = pool
-        self._connection = connection
-
-        if hasattr(body, 'read'):
-            self._fp = body
-
-        # Are we using the chunked-style of transfer encoding?
-        self.chunked = False
-        self.chunk_left = None
-        tr_enc = self.headers.get('transfer-encoding', '').lower()
-        # Don't incur the penalty of creating a list and then discarding it
-        encodings = (enc.strip() for enc in tr_enc.split(","))
-        if "chunked" in encodings:
-            self.chunked = True
-
-        # Determine length of response
-        self.length_remaining = self._init_length(request_method)
-
-        # If requested, preload the body.
-        if preload_content and not self._body:
-            self._body = self.read(decode_content=decode_content)
-
-    def get_redirect_location(self):
-        """
-        Should we redirect and where to?
-
-        :returns: Truthy redirect location string if we got a redirect status
-            code and valid location. ``None`` if redirect status and no
-            location. ``False`` if not a redirect status code.
-        """
-        if self.status in self.REDIRECT_STATUSES:
-            return self.headers.get('location')
-
-        return False
-
-    def release_conn(self):
-        if not self._pool or not self._connection:
-            return
-
-        self._pool._put_conn(self._connection)
-        self._connection = None
-
-    @property
-    def data(self):
-        # For backwords-compat with earlier urllib3 0.4 and earlier.
-        if self._body:
-            return self._body
-
-        if self._fp:
-            return self.read(cache_content=True)
-
-    @property
-    def connection(self):
-        return self._connection
-
-    def isclosed(self):
-        return is_fp_closed(self._fp)
-
-    def tell(self):
-        """
-        Obtain the number of bytes pulled over the wire so far. May differ from
-        the amount of content returned by :meth:``HTTPResponse.read`` if bytes
-        are encoded on the wire (e.g, compressed).
-        """
-        return self._fp_bytes_read
-
-    def _init_length(self, request_method):
-        """
-        Set initial length value for Response content if available.
-        """
-        length = self.headers.get('content-length')
-
-        if length is not None:
-            if self.chunked:
-                # This Response will fail with an IncompleteRead if it can't be
-                # received as chunked. This method falls back to attempt reading
-                # the response before raising an exception.
-                log.warning("Received response with both Content-Length and "
-                            "Transfer-Encoding set. This is expressly forbidden "
-                            "by RFC 7230 sec 3.3.2. Ignoring Content-Length and "
-                            "attempting to process response as Transfer-Encoding: "
-                            "chunked.")
-                return None
-
-            try:
-                # RFC 7230 section 3.3.2 specifies multiple content lengths can
-                # be sent in a single Content-Length header
-                # (e.g. Content-Length: 42, 42). This line ensures the values
-                # are all valid ints and that as long as the `set` length is 1,
-                # all values are the same. Otherwise, the header is invalid.
-                lengths = set([int(val) for val in length.split(',')])
-                if len(lengths) > 1:
-                    raise InvalidHeader("Content-Length contained multiple "
-                                        "unmatching values (%s)" % length)
-                length = lengths.pop()
-            except ValueError:
-                length = None
-            else:
-                if length < 0:
-                    length = None
-
-        # Convert status to int for comparison
-        # In some cases, httplib returns a status of "_UNKNOWN"
-        try:
-            status = int(self.status)
-        except ValueError:
-            status = 0
-
-        # Check for responses that shouldn't include a body
-        if status in (204, 304) or 100 <= status < 200 or request_method == 'HEAD':
-            length = 0
-
-        return length
-
-    def _init_decoder(self):
-        """
-        Set-up the _decoder attribute if necessary.
-        """
-        # Note: content-encoding value should be case-insensitive, per RFC 7230
-        # Section 3.2
-        content_encoding = self.headers.get('content-encoding', '').lower()
-        if self._decoder is None:
-            if content_encoding in self.CONTENT_DECODERS:
-                self._decoder = _get_decoder(content_encoding)
-            elif ',' in content_encoding:
-                encodings = [e.strip() for e in content_encoding.split(',') if e.strip() in self.CONTENT_DECODERS]
-                if len(encodings):
-                    self._decoder = _get_decoder(content_encoding)
-
-    def _decode(self, data, decode_content, flush_decoder):
-        """
-        Decode the data passed in and potentially flush the decoder.
-        """
-        try:
-            if decode_content and self._decoder:
-                data = self._decoder.decompress(data)
-        except (IOError, zlib.error) as e:
-            content_encoding = self.headers.get('content-encoding', '').lower()
-            raise DecodeError(
-                "Received response with content-encoding: %s, but "
-                "failed to decode it." % content_encoding, e)
-
-        if flush_decoder and decode_content:
-            data += self._flush_decoder()
-
-        return data
-
-    def _flush_decoder(self):
-        """
-        Flushes the decoder. Should only be called if the decoder is actually
-        being used.
-        """
-        if self._decoder:
-            buf = self._decoder.decompress(b'')
-            return buf + self._decoder.flush()
-
-        return b''
-
-    @contextmanager
-    def _error_catcher(self):
-        """
-        Catch low-level python exceptions, instead re-raising urllib3
-        variants, so that low-level exceptions are not leaked in the
-        high-level api.
-
-        On exit, release the connection back to the pool.
-        """
-        clean_exit = False
-
-        try:
-            try:
-                yield
-
-            except SocketTimeout:
-                # FIXME: Ideally we'd like to include the url in the ReadTimeoutError but
-                # there is yet no clean way to get at it from this context.
-                raise ReadTimeoutError(self._pool, None, 'Read timed out.')
-
-            except BaseSSLError as e:
-                # FIXME: Is there a better way to differentiate between SSLErrors?
-                if 'read operation timed out' not in str(e):  # Defensive:
-                    # This shouldn't happen but just in case we're missing an edge
-                    # case, let's avoid swallowing SSL errors.
-                    raise
-
-                raise ReadTimeoutError(self._pool, None, 'Read timed out.')
-
-            except (HTTPException, SocketError) as e:
-                # This includes IncompleteRead.
-                raise ProtocolError('Connection broken: %r' % e, e)
-
-            # If no exception is thrown, we should avoid cleaning up
-            # unnecessarily.
-            clean_exit = True
-        finally:
-            # If we didn't terminate cleanly, we need to throw away our
-            # connection.
-            if not clean_exit:
-                # The response may not be closed but we're not going to use it
-                # anymore so close it now to ensure that the connection is
-                # released back to the pool.
-                if self._original_response:
-                    self._original_response.close()
-
-                # Closing the response may not actually be sufficient to close
-                # everything, so if we have a hold of the connection close that
-                # too.
-                if self._connection:
-                    self._connection.close()
-
-            # If we hold the original response but it's closed now, we should
-            # return the connection back to the pool.
-            if self._original_response and self._original_response.isclosed():
-                self.release_conn()
-
-    def read(self, amt=None, decode_content=None, cache_content=False):
-        """
-        Similar to :meth:`httplib.HTTPResponse.read`, but with two additional
-        parameters: ``decode_content`` and ``cache_content``.
-
-        :param amt:
-            How much of the content to read. If specified, caching is skipped
-            because it doesn't make sense to cache partial content as the full
-            response.
-
-        :param decode_content:
-            If True, will attempt to decode the body based on the
-            'content-encoding' header.
-
-        :param cache_content:
-            If True, will save the returned data such that the same result is
-            returned despite of the state of the underlying file object. This
-            is useful if you want the ``.data`` property to continue working
-            after having ``.read()`` the file object. (Overridden if ``amt`` is
-            set.)
-        """
-        self._init_decoder()
-        if decode_content is None:
-            decode_content = self.decode_content
-
-        if self._fp is None:
-            return
-
-        flush_decoder = False
-        data = None
-
-        with self._error_catcher():
-            if amt is None:
-                # cStringIO doesn't like amt=None
-                data = self._fp.read()
-                flush_decoder = True
-            else:
-                cache_content = False
-                data = self._fp.read(amt)
-                if amt != 0 and not data:  # Platform-specific: Buggy versions of Python.
-                    # Close the connection when no data is returned
-                    #
-                    # This is redundant to what httplib/http.client _should_
-                    # already do.  However, versions of python released before
-                    # December 15, 2012 (http://bugs.python.org/issue16298) do
-                    # not properly close the connection in all cases. There is
-                    # no harm in redundantly calling close.
-                    self._fp.close()
-                    flush_decoder = True
-                    if self.enforce_content_length and self.length_remaining not in (0, None):
-                        # This is an edge case that httplib failed to cover due
-                        # to concerns of backward compatibility. We're
-                        # addressing it here to make sure IncompleteRead is
-                        # raised during streaming, so all calls with incorrect
-                        # Content-Length are caught.
-                        raise IncompleteRead(self._fp_bytes_read, self.length_remaining)
-
-        if data:
-            self._fp_bytes_read += len(data)
-            if self.length_remaining is not None:
-                self.length_remaining -= len(data)
-
-            data = self._decode(data, decode_content, flush_decoder)
-
-            if cache_content:
-                self._body = data
-
-        return data
-
-    def stream(self, amt=2**16, decode_content=None):
-        """
-        A generator wrapper for the read() method. A call will block until
-        ``amt`` bytes have been read from the connection or until the
-        connection is closed.
-
-        :param amt:
-            How much of the content to read. The generator will return up to
-            much data per iteration, but may return less. This is particularly
-            likely when using compressed data. However, the empty string will
-            never be returned.
-
-        :param decode_content:
-            If True, will attempt to decode the body based on the
-            'content-encoding' header.
-        """
-        if self.chunked and self.supports_chunked_reads():
-            for line in self.read_chunked(amt, decode_content=decode_content):
-                yield line
-        else:
-            while not is_fp_closed(self._fp):
-                data = self.read(amt=amt, decode_content=decode_content)
-
-                if data:
-                    yield data
-
-    @classmethod
-    def from_httplib(ResponseCls, r, **response_kw):
-        """
-        Given an :class:`httplib.HTTPResponse` instance ``r``, return a
-        corresponding :class:`urllib3.response.HTTPResponse` object.
-
-        Remaining parameters are passed to the HTTPResponse constructor, along
-        with ``original_response=r``.
-        """
-        headers = r.msg
-
-        if not isinstance(headers, HTTPHeaderDict):
-            if PY3:  # Python 3
-                headers = HTTPHeaderDict(headers.items())
-            else:  # Python 2
-                headers = HTTPHeaderDict.from_httplib(headers)
-
-        # HTTPResponse objects in Python 3 don't have a .strict attribute
-        strict = getattr(r, 'strict', 0)
-        resp = ResponseCls(body=r,
-                           headers=headers,
-                           status=r.status,
-                           version=r.version,
-                           reason=r.reason,
-                           strict=strict,
-                           original_response=r,
-                           **response_kw)
-        return resp
-
-    # Backwards-compatibility methods for httplib.HTTPResponse
-    def getheaders(self):
-        return self.headers
-
-    def getheader(self, name, default=None):
-        return self.headers.get(name, default)
-
-    # Backwards compatibility for http.cookiejar
-    def info(self):
-        return self.headers
-
-    # Overrides from io.IOBase
-    def close(self):
-        if not self.closed:
-            self._fp.close()
-
-        if self._connection:
-            self._connection.close()
-
-    @property
-    def closed(self):
-        if self._fp is None:
-            return True
-        elif hasattr(self._fp, 'isclosed'):
-            return self._fp.isclosed()
-        elif hasattr(self._fp, 'closed'):
-            return self._fp.closed
-        else:
-            return True
-
-    def fileno(self):
-        if self._fp is None:
-            raise IOError("HTTPResponse has no file to get a fileno from")
-        elif hasattr(self._fp, "fileno"):
-            return self._fp.fileno()
-        else:
-            raise IOError("The file-like object this HTTPResponse is wrapped "
-                          "around has no file descriptor")
-
-    def flush(self):
-        if self._fp is not None and hasattr(self._fp, 'flush'):
-            return self._fp.flush()
-
-    def readable(self):
-        # This method is required for `io` module compatibility.
-        return True
-
-    def readinto(self, b):
-        # This method is required for `io` module compatibility.
-        temp = self.read(len(b))
-        if len(temp) == 0:
-            return 0
-        else:
-            b[:len(temp)] = temp
-            return len(temp)
-
-    def supports_chunked_reads(self):
-        """
-        Checks if the underlying file-like object looks like a
-        httplib.HTTPResponse object. We do this by testing for the fp
-        attribute. If it is present we assume it returns raw chunks as
-        processed by read_chunked().
-        """
-        return hasattr(self._fp, 'fp')
-
-    def _update_chunk_length(self):
-        # First, we'll figure out length of a chunk and then
-        # we'll try to read it from socket.
-        if self.chunk_left is not None:
-            return
-        line = self._fp.fp.readline()
-        line = line.split(b';', 1)[0]
-        try:
-            self.chunk_left = int(line, 16)
-        except ValueError:
-            # Invalid chunked protocol response, abort.
-            self.close()
-            raise httplib.IncompleteRead(line)
-
-    def _handle_chunk(self, amt):
-        returned_chunk = None
-        if amt is None:
-            chunk = self._fp._safe_read(self.chunk_left)
-            returned_chunk = chunk
-            self._fp._safe_read(2)  # Toss the CRLF at the end of the chunk.
-            self.chunk_left = None
-        elif amt < self.chunk_left:
-            value = self._fp._safe_read(amt)
-            self.chunk_left = self.chunk_left - amt
-            returned_chunk = value
-        elif amt == self.chunk_left:
-            value = self._fp._safe_read(amt)
-            self._fp._safe_read(2)  # Toss the CRLF at the end of the chunk.
-            self.chunk_left = None
-            returned_chunk = value
-        else:  # amt > self.chunk_left
-            returned_chunk = self._fp._safe_read(self.chunk_left)
-            self._fp._safe_read(2)  # Toss the CRLF at the end of the chunk.
-            self.chunk_left = None
-        return returned_chunk
-
-    def read_chunked(self, amt=None, decode_content=None):
-        """
-        Similar to :meth:`HTTPResponse.read`, but with an additional
-        parameter: ``decode_content``.
-
-        :param amt:
-            How much of the content to read. If specified, caching is skipped
-            because it doesn't make sense to cache partial content as the full
-            response.
-
-        :param decode_content:
-            If True, will attempt to decode the body based on the
-            'content-encoding' header.
-        """
-        self._init_decoder()
-        # FIXME: Rewrite this method and make it a class with a better structured logic.
-        if not self.chunked:
-            raise ResponseNotChunked(
-                "Response is not chunked. "
-                "Header 'transfer-encoding: chunked' is missing.")
-        if not self.supports_chunked_reads():
-            raise BodyNotHttplibCompatible(
-                "Body should be httplib.HTTPResponse like. "
-                "It should have have an fp attribute which returns raw chunks.")
-
-        with self._error_catcher():
-            # Don't bother reading the body of a HEAD request.
-            if self._original_response and is_response_to_head(self._original_response):
-                self._original_response.close()
-                return
-
-            # If a response is already read and closed
-            # then return immediately.
-            if self._fp.fp is None:
-                return
-
-            while True:
-                self._update_chunk_length()
-                if self.chunk_left == 0:
-                    break
-                chunk = self._handle_chunk(amt)
-                decoded = self._decode(chunk, decode_content=decode_content,
-                                       flush_decoder=False)
-                if decoded:
-                    yield decoded
-
-            if decode_content:
-                # On CPython and PyPy, we should never need to flush the
-                # decoder. However, on Jython we *might* need to, so
-                # lets defensively do it anyway.
-                decoded = self._flush_decoder()
-                if decoded:  # Platform-specific: Jython.
-                    yield decoded
-
-            # Chunk content ends with \r\n: discard it.
-            while True:
-                line = self._fp.fp.readline()
-                if not line:
-                    # Some sites may not end with '\r\n'.
-                    break
-                if line == b'\r\n':
-                    break
-
-            # We read everything; close the "file".
-            if self._original_response:
-                self._original_response.close()
-
-    def geturl(self):
-        """
-        Returns the URL that was the source of this response.
-        If the request that generated this response redirected, this method
-        will return the final redirect location.
-        """
-        if self.retries is not None and len(self.retries.history):
-            return self.retries.history[-1].redirect_location
-        else:
-            return self._request_url
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__init__.py
deleted file mode 100644
index 2f2770b..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__init__.py
+++ /dev/null
@@ -1,54 +0,0 @@
-from __future__ import absolute_import
-# For backwards compatibility, provide imports that used to be here.
-from .connection import is_connection_dropped
-from .request import make_headers
-from .response import is_fp_closed
-from .ssl_ import (
-    SSLContext,
-    HAS_SNI,
-    IS_PYOPENSSL,
-    IS_SECURETRANSPORT,
-    assert_fingerprint,
-    resolve_cert_reqs,
-    resolve_ssl_version,
-    ssl_wrap_socket,
-)
-from .timeout import (
-    current_time,
-    Timeout,
-)
-
-from .retry import Retry
-from .url import (
-    get_host,
-    parse_url,
-    split_first,
-    Url,
-)
-from .wait import (
-    wait_for_read,
-    wait_for_write
-)
-
-__all__ = (
-    'HAS_SNI',
-    'IS_PYOPENSSL',
-    'IS_SECURETRANSPORT',
-    'SSLContext',
-    'Retry',
-    'Timeout',
-    'Url',
-    'assert_fingerprint',
-    'current_time',
-    'is_connection_dropped',
-    'is_fp_closed',
-    'get_host',
-    'parse_url',
-    'make_headers',
-    'resolve_cert_reqs',
-    'resolve_ssl_version',
-    'split_first',
-    'ssl_wrap_socket',
-    'wait_for_read',
-    'wait_for_write'
-)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index bd7877f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/connection.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/connection.cpython-37.pyc
deleted file mode 100644
index c580ddc..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/connection.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/queue.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/queue.cpython-37.pyc
deleted file mode 100644
index 373e38e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/queue.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/request.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/request.cpython-37.pyc
deleted file mode 100644
index 557c15d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/request.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/response.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/response.cpython-37.pyc
deleted file mode 100644
index 1359375..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/response.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/retry.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/retry.cpython-37.pyc
deleted file mode 100644
index f9eba95..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/retry.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/ssl_.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/ssl_.cpython-37.pyc
deleted file mode 100644
index 5cfb7de..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/ssl_.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/timeout.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/timeout.cpython-37.pyc
deleted file mode 100644
index 2710b82..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/timeout.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/url.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/url.cpython-37.pyc
deleted file mode 100644
index dd79999..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/url.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/wait.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/wait.cpython-37.pyc
deleted file mode 100644
index 64d3721..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/__pycache__/wait.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/connection.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/connection.py
deleted file mode 100644
index 5ad70b2..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/connection.py
+++ /dev/null
@@ -1,134 +0,0 @@
-from __future__ import absolute_import
-import socket
-from .wait import NoWayToWaitForSocketError, wait_for_read
-from ..contrib import _appengine_environ
-
-
-def is_connection_dropped(conn):  # Platform-specific
-    """
-    Returns True if the connection is dropped and should be closed.
-
-    :param conn:
-        :class:`httplib.HTTPConnection` object.
-
-    Note: For platforms like AppEngine, this will always return ``False`` to
-    let the platform handle connection recycling transparently for us.
-    """
-    sock = getattr(conn, 'sock', False)
-    if sock is False:  # Platform-specific: AppEngine
-        return False
-    if sock is None:  # Connection already closed (such as by httplib).
-        return True
-    try:
-        # Returns True if readable, which here means it's been dropped
-        return wait_for_read(sock, timeout=0.0)
-    except NoWayToWaitForSocketError:  # Platform-specific: AppEngine
-        return False
-
-
-# This function is copied from socket.py in the Python 2.7 standard
-# library test suite. Added to its signature is only `socket_options`.
-# One additional modification is that we avoid binding to IPv6 servers
-# discovered in DNS if the system doesn't have IPv6 functionality.
-def create_connection(address, timeout=socket._GLOBAL_DEFAULT_TIMEOUT,
-                      source_address=None, socket_options=None):
-    """Connect to *address* and return the socket object.
-
-    Convenience function.  Connect to *address* (a 2-tuple ``(host,
-    port)``) and return the socket object.  Passing the optional
-    *timeout* parameter will set the timeout on the socket instance
-    before attempting to connect.  If no *timeout* is supplied, the
-    global default timeout setting returned by :func:`getdefaulttimeout`
-    is used.  If *source_address* is set it must be a tuple of (host, port)
-    for the socket to bind as a source address before making the connection.
-    An host of '' or port 0 tells the OS to use the default.
-    """
-
-    host, port = address
-    if host.startswith('['):
-        host = host.strip('[]')
-    err = None
-
-    # Using the value from allowed_gai_family() in the context of getaddrinfo lets
-    # us select whether to work with IPv4 DNS records, IPv6 records, or both.
-    # The original create_connection function always returns all records.
-    family = allowed_gai_family()
-
-    for res in socket.getaddrinfo(host, port, family, socket.SOCK_STREAM):
-        af, socktype, proto, canonname, sa = res
-        sock = None
-        try:
-            sock = socket.socket(af, socktype, proto)
-
-            # If provided, set socket level options before connecting.
-            _set_socket_options(sock, socket_options)
-
-            if timeout is not socket._GLOBAL_DEFAULT_TIMEOUT:
-                sock.settimeout(timeout)
-            if source_address:
-                sock.bind(source_address)
-            sock.connect(sa)
-            return sock
-
-        except socket.error as e:
-            err = e
-            if sock is not None:
-                sock.close()
-                sock = None
-
-    if err is not None:
-        raise err
-
-    raise socket.error("getaddrinfo returns an empty list")
-
-
-def _set_socket_options(sock, options):
-    if options is None:
-        return
-
-    for opt in options:
-        sock.setsockopt(*opt)
-
-
-def allowed_gai_family():
-    """This function is designed to work in the context of
-    getaddrinfo, where family=socket.AF_UNSPEC is the default and
-    will perform a DNS search for both IPv6 and IPv4 records."""
-
-    family = socket.AF_INET
-    if HAS_IPV6:
-        family = socket.AF_UNSPEC
-    return family
-
-
-def _has_ipv6(host):
-    """ Returns True if the system can bind an IPv6 address. """
-    sock = None
-    has_ipv6 = False
-
-    # App Engine doesn't support IPV6 sockets and actually has a quota on the
-    # number of sockets that can be used, so just early out here instead of
-    # creating a socket needlessly.
-    # See https://github.com/urllib3/urllib3/issues/1446
-    if _appengine_environ.is_appengine_sandbox():
-        return False
-
-    if socket.has_ipv6:
-        # has_ipv6 returns true if cPython was compiled with IPv6 support.
-        # It does not tell us if the system has IPv6 support enabled. To
-        # determine that we must bind to an IPv6 address.
-        # https://github.com/shazow/urllib3/pull/611
-        # https://bugs.python.org/issue658327
-        try:
-            sock = socket.socket(socket.AF_INET6)
-            sock.bind((host, 0))
-            has_ipv6 = True
-        except Exception:
-            pass
-
-    if sock:
-        sock.close()
-    return has_ipv6
-
-
-HAS_IPV6 = _has_ipv6('::1')
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/queue.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/queue.py
deleted file mode 100644
index d3d379a..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/queue.py
+++ /dev/null
@@ -1,21 +0,0 @@
-import collections
-from ..packages import six
-from ..packages.six.moves import queue
-
-if six.PY2:
-    # Queue is imported for side effects on MS Windows. See issue #229.
-    import Queue as _unused_module_Queue  # noqa: F401
-
-
-class LifoQueue(queue.Queue):
-    def _init(self, _):
-        self.queue = collections.deque()
-
-    def _qsize(self, len=len):
-        return len(self.queue)
-
-    def _put(self, item):
-        self.queue.append(item)
-
-    def _get(self):
-        return self.queue.pop()
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/request.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/request.py
deleted file mode 100644
index 3ddfcd5..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/request.py
+++ /dev/null
@@ -1,118 +0,0 @@
-from __future__ import absolute_import
-from base64 import b64encode
-
-from ..packages.six import b, integer_types
-from ..exceptions import UnrewindableBodyError
-
-ACCEPT_ENCODING = 'gzip,deflate'
-_FAILEDTELL = object()
-
-
-def make_headers(keep_alive=None, accept_encoding=None, user_agent=None,
-                 basic_auth=None, proxy_basic_auth=None, disable_cache=None):
-    """
-    Shortcuts for generating request headers.
-
-    :param keep_alive:
-        If ``True``, adds 'connection: keep-alive' header.
-
-    :param accept_encoding:
-        Can be a boolean, list, or string.
-        ``True`` translates to 'gzip,deflate'.
-        List will get joined by comma.
-        String will be used as provided.
-
-    :param user_agent:
-        String representing the user-agent you want, such as
-        "python-urllib3/0.6"
-
-    :param basic_auth:
-        Colon-separated username:password string for 'authorization: basic ...'
-        auth header.
-
-    :param proxy_basic_auth:
-        Colon-separated username:password string for 'proxy-authorization: basic ...'
-        auth header.
-
-    :param disable_cache:
-        If ``True``, adds 'cache-control: no-cache' header.
-
-    Example::
-
-        >>> make_headers(keep_alive=True, user_agent="Batman/1.0")
-        {'connection': 'keep-alive', 'user-agent': 'Batman/1.0'}
-        >>> make_headers(accept_encoding=True)
-        {'accept-encoding': 'gzip,deflate'}
-    """
-    headers = {}
-    if accept_encoding:
-        if isinstance(accept_encoding, str):
-            pass
-        elif isinstance(accept_encoding, list):
-            accept_encoding = ','.join(accept_encoding)
-        else:
-            accept_encoding = ACCEPT_ENCODING
-        headers['accept-encoding'] = accept_encoding
-
-    if user_agent:
-        headers['user-agent'] = user_agent
-
-    if keep_alive:
-        headers['connection'] = 'keep-alive'
-
-    if basic_auth:
-        headers['authorization'] = 'Basic ' + \
-            b64encode(b(basic_auth)).decode('utf-8')
-
-    if proxy_basic_auth:
-        headers['proxy-authorization'] = 'Basic ' + \
-            b64encode(b(proxy_basic_auth)).decode('utf-8')
-
-    if disable_cache:
-        headers['cache-control'] = 'no-cache'
-
-    return headers
-
-
-def set_file_position(body, pos):
-    """
-    If a position is provided, move file to that point.
-    Otherwise, we'll attempt to record a position for future use.
-    """
-    if pos is not None:
-        rewind_body(body, pos)
-    elif getattr(body, 'tell', None) is not None:
-        try:
-            pos = body.tell()
-        except (IOError, OSError):
-            # This differentiates from None, allowing us to catch
-            # a failed `tell()` later when trying to rewind the body.
-            pos = _FAILEDTELL
-
-    return pos
-
-
-def rewind_body(body, body_pos):
-    """
-    Attempt to rewind body to a certain position.
-    Primarily used for request redirects and retries.
-
-    :param body:
-        File-like object that supports seek.
-
-    :param int pos:
-        Position to seek to in file.
-    """
-    body_seek = getattr(body, 'seek', None)
-    if body_seek is not None and isinstance(body_pos, integer_types):
-        try:
-            body_seek(body_pos)
-        except (IOError, OSError):
-            raise UnrewindableBodyError("An error occurred when rewinding request "
-                                        "body for redirect/retry.")
-    elif body_pos is _FAILEDTELL:
-        raise UnrewindableBodyError("Unable to record file position for rewinding "
-                                    "request body during a redirect/retry.")
-    else:
-        raise ValueError("body_pos must be of type integer, "
-                         "instead it was %s." % type(body_pos))
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/response.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/response.py
deleted file mode 100644
index 3d54864..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/response.py
+++ /dev/null
@@ -1,87 +0,0 @@
-from __future__ import absolute_import
-from ..packages.six.moves import http_client as httplib
-
-from ..exceptions import HeaderParsingError
-
-
-def is_fp_closed(obj):
-    """
-    Checks whether a given file-like object is closed.
-
-    :param obj:
-        The file-like object to check.
-    """
-
-    try:
-        # Check `isclosed()` first, in case Python3 doesn't set `closed`.
-        # GH Issue #928
-        return obj.isclosed()
-    except AttributeError:
-        pass
-
-    try:
-        # Check via the official file-like-object way.
-        return obj.closed
-    except AttributeError:
-        pass
-
-    try:
-        # Check if the object is a container for another file-like object that
-        # gets released on exhaustion (e.g. HTTPResponse).
-        return obj.fp is None
-    except AttributeError:
-        pass
-
-    raise ValueError("Unable to determine whether fp is closed.")
-
-
-def assert_header_parsing(headers):
-    """
-    Asserts whether all headers have been successfully parsed.
-    Extracts encountered errors from the result of parsing headers.
-
-    Only works on Python 3.
-
-    :param headers: Headers to verify.
-    :type headers: `httplib.HTTPMessage`.
-
-    :raises urllib3.exceptions.HeaderParsingError:
-        If parsing errors are found.
-    """
-
-    # This will fail silently if we pass in the wrong kind of parameter.
-    # To make debugging easier add an explicit check.
-    if not isinstance(headers, httplib.HTTPMessage):
-        raise TypeError('expected httplib.Message, got {0}.'.format(
-            type(headers)))
-
-    defects = getattr(headers, 'defects', None)
-    get_payload = getattr(headers, 'get_payload', None)
-
-    unparsed_data = None
-    if get_payload:
-        # get_payload is actually email.message.Message.get_payload;
-        # we're only interested in the result if it's not a multipart message
-        if not headers.is_multipart():
-            payload = get_payload()
-
-            if isinstance(payload, (bytes, str)):
-                unparsed_data = payload
-
-    if defects or unparsed_data:
-        raise HeaderParsingError(defects=defects, unparsed_data=unparsed_data)
-
-
-def is_response_to_head(response):
-    """
-    Checks whether the request of a response has been a HEAD-request.
-    Handles the quirks of AppEngine.
-
-    :param conn:
-    :type conn: :class:`httplib.HTTPResponse`
-    """
-    # FIXME: Can we do this somehow without accessing private httplib _method?
-    method = response._method
-    if isinstance(method, int):  # Platform-specific: Appengine
-        return method == 3
-    return method.upper() == 'HEAD'
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/retry.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/retry.py
deleted file mode 100644
index e7d0abd..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/retry.py
+++ /dev/null
@@ -1,411 +0,0 @@
-from __future__ import absolute_import
-import time
-import logging
-from collections import namedtuple
-from itertools import takewhile
-import email
-import re
-
-from ..exceptions import (
-    ConnectTimeoutError,
-    MaxRetryError,
-    ProtocolError,
-    ReadTimeoutError,
-    ResponseError,
-    InvalidHeader,
-)
-from ..packages import six
-
-
-log = logging.getLogger(__name__)
-
-
-# Data structure for representing the metadata of requests that result in a retry.
-RequestHistory = namedtuple('RequestHistory', ["method", "url", "error",
-                                               "status", "redirect_location"])
-
-
-class Retry(object):
-    """ Retry configuration.
-
-    Each retry attempt will create a new Retry object with updated values, so
-    they can be safely reused.
-
-    Retries can be defined as a default for a pool::
-
-        retries = Retry(connect=5, read=2, redirect=5)
-        http = PoolManager(retries=retries)
-        response = http.request('GET', 'http://example.com/')
-
-    Or per-request (which overrides the default for the pool)::
-
-        response = http.request('GET', 'http://example.com/', retries=Retry(10))
-
-    Retries can be disabled by passing ``False``::
-
-        response = http.request('GET', 'http://example.com/', retries=False)
-
-    Errors will be wrapped in :class:`~urllib3.exceptions.MaxRetryError` unless
-    retries are disabled, in which case the causing exception will be raised.
-
-    :param int total:
-        Total number of retries to allow. Takes precedence over other counts.
-
-        Set to ``None`` to remove this constraint and fall back on other
-        counts. It's a good idea to set this to some sensibly-high value to
-        account for unexpected edge cases and avoid infinite retry loops.
-
-        Set to ``0`` to fail on the first retry.
-
-        Set to ``False`` to disable and imply ``raise_on_redirect=False``.
-
-    :param int connect:
-        How many connection-related errors to retry on.
-
-        These are errors raised before the request is sent to the remote server,
-        which we assume has not triggered the server to process the request.
-
-        Set to ``0`` to fail on the first retry of this type.
-
-    :param int read:
-        How many times to retry on read errors.
-
-        These errors are raised after the request was sent to the server, so the
-        request may have side-effects.
-
-        Set to ``0`` to fail on the first retry of this type.
-
-    :param int redirect:
-        How many redirects to perform. Limit this to avoid infinite redirect
-        loops.
-
-        A redirect is a HTTP response with a status code 301, 302, 303, 307 or
-        308.
-
-        Set to ``0`` to fail on the first retry of this type.
-
-        Set to ``False`` to disable and imply ``raise_on_redirect=False``.
-
-    :param int status:
-        How many times to retry on bad status codes.
-
-        These are retries made on responses, where status code matches
-        ``status_forcelist``.
-
-        Set to ``0`` to fail on the first retry of this type.
-
-    :param iterable method_whitelist:
-        Set of uppercased HTTP method verbs that we should retry on.
-
-        By default, we only retry on methods which are considered to be
-        idempotent (multiple requests with the same parameters end with the
-        same state). See :attr:`Retry.DEFAULT_METHOD_WHITELIST`.
-
-        Set to a ``False`` value to retry on any verb.
-
-    :param iterable status_forcelist:
-        A set of integer HTTP status codes that we should force a retry on.
-        A retry is initiated if the request method is in ``method_whitelist``
-        and the response status code is in ``status_forcelist``.
-
-        By default, this is disabled with ``None``.
-
-    :param float backoff_factor:
-        A backoff factor to apply between attempts after the second try
-        (most errors are resolved immediately by a second try without a
-        delay). urllib3 will sleep for::
-
-            {backoff factor} * (2 ** ({number of total retries} - 1))
-
-        seconds. If the backoff_factor is 0.1, then :func:`.sleep` will sleep
-        for [0.0s, 0.2s, 0.4s, ...] between retries. It will never be longer
-        than :attr:`Retry.BACKOFF_MAX`.
-
-        By default, backoff is disabled (set to 0).
-
-    :param bool raise_on_redirect: Whether, if the number of redirects is
-        exhausted, to raise a MaxRetryError, or to return a response with a
-        response code in the 3xx range.
-
-    :param bool raise_on_status: Similar meaning to ``raise_on_redirect``:
-        whether we should raise an exception, or return a response,
-        if status falls in ``status_forcelist`` range and retries have
-        been exhausted.
-
-    :param tuple history: The history of the request encountered during
-        each call to :meth:`~Retry.increment`. The list is in the order
-        the requests occurred. Each list item is of class :class:`RequestHistory`.
-
-    :param bool respect_retry_after_header:
-        Whether to respect Retry-After header on status codes defined as
-        :attr:`Retry.RETRY_AFTER_STATUS_CODES` or not.
-
-    :param iterable remove_headers_on_redirect:
-        Sequence of headers to remove from the request when a response
-        indicating a redirect is returned before firing off the redirected
-        request.
-    """
-
-    DEFAULT_METHOD_WHITELIST = frozenset([
-        'HEAD', 'GET', 'PUT', 'DELETE', 'OPTIONS', 'TRACE'])
-
-    RETRY_AFTER_STATUS_CODES = frozenset([413, 429, 503])
-
-    DEFAULT_REDIRECT_HEADERS_BLACKLIST = frozenset(['Authorization'])
-
-    #: Maximum backoff time.
-    BACKOFF_MAX = 120
-
-    def __init__(self, total=10, connect=None, read=None, redirect=None, status=None,
-                 method_whitelist=DEFAULT_METHOD_WHITELIST, status_forcelist=None,
-                 backoff_factor=0, raise_on_redirect=True, raise_on_status=True,
-                 history=None, respect_retry_after_header=True,
-                 remove_headers_on_redirect=DEFAULT_REDIRECT_HEADERS_BLACKLIST):
-
-        self.total = total
-        self.connect = connect
-        self.read = read
-        self.status = status
-
-        if redirect is False or total is False:
-            redirect = 0
-            raise_on_redirect = False
-
-        self.redirect = redirect
-        self.status_forcelist = status_forcelist or set()
-        self.method_whitelist = method_whitelist
-        self.backoff_factor = backoff_factor
-        self.raise_on_redirect = raise_on_redirect
-        self.raise_on_status = raise_on_status
-        self.history = history or tuple()
-        self.respect_retry_after_header = respect_retry_after_header
-        self.remove_headers_on_redirect = remove_headers_on_redirect
-
-    def new(self, **kw):
-        params = dict(
-            total=self.total,
-            connect=self.connect, read=self.read, redirect=self.redirect, status=self.status,
-            method_whitelist=self.method_whitelist,
-            status_forcelist=self.status_forcelist,
-            backoff_factor=self.backoff_factor,
-            raise_on_redirect=self.raise_on_redirect,
-            raise_on_status=self.raise_on_status,
-            history=self.history,
-            remove_headers_on_redirect=self.remove_headers_on_redirect
-        )
-        params.update(kw)
-        return type(self)(**params)
-
-    @classmethod
-    def from_int(cls, retries, redirect=True, default=None):
-        """ Backwards-compatibility for the old retries format."""
-        if retries is None:
-            retries = default if default is not None else cls.DEFAULT
-
-        if isinstance(retries, Retry):
-            return retries
-
-        redirect = bool(redirect) and None
-        new_retries = cls(retries, redirect=redirect)
-        log.debug("Converted retries value: %r -> %r", retries, new_retries)
-        return new_retries
-
-    def get_backoff_time(self):
-        """ Formula for computing the current backoff
-
-        :rtype: float
-        """
-        # We want to consider only the last consecutive errors sequence (Ignore redirects).
-        consecutive_errors_len = len(list(takewhile(lambda x: x.redirect_location is None,
-                                                    reversed(self.history))))
-        if consecutive_errors_len <= 1:
-            return 0
-
-        backoff_value = self.backoff_factor * (2 ** (consecutive_errors_len - 1))
-        return min(self.BACKOFF_MAX, backoff_value)
-
-    def parse_retry_after(self, retry_after):
-        # Whitespace: https://tools.ietf.org/html/rfc7230#section-3.2.4
-        if re.match(r"^\s*[0-9]+\s*$", retry_after):
-            seconds = int(retry_after)
-        else:
-            retry_date_tuple = email.utils.parsedate(retry_after)
-            if retry_date_tuple is None:
-                raise InvalidHeader("Invalid Retry-After header: %s" % retry_after)
-            retry_date = time.mktime(retry_date_tuple)
-            seconds = retry_date - time.time()
-
-        if seconds < 0:
-            seconds = 0
-
-        return seconds
-
-    def get_retry_after(self, response):
-        """ Get the value of Retry-After in seconds. """
-
-        retry_after = response.getheader("Retry-After")
-
-        if retry_after is None:
-            return None
-
-        return self.parse_retry_after(retry_after)
-
-    def sleep_for_retry(self, response=None):
-        retry_after = self.get_retry_after(response)
-        if retry_after:
-            time.sleep(retry_after)
-            return True
-
-        return False
-
-    def _sleep_backoff(self):
-        backoff = self.get_backoff_time()
-        if backoff <= 0:
-            return
-        time.sleep(backoff)
-
-    def sleep(self, response=None):
-        """ Sleep between retry attempts.
-
-        This method will respect a server's ``Retry-After`` response header
-        and sleep the duration of the time requested. If that is not present, it
-        will use an exponential backoff. By default, the backoff factor is 0 and
-        this method will return immediately.
-        """
-
-        if response:
-            slept = self.sleep_for_retry(response)
-            if slept:
-                return
-
-        self._sleep_backoff()
-
-    def _is_connection_error(self, err):
-        """ Errors when we're fairly sure that the server did not receive the
-        request, so it should be safe to retry.
-        """
-        return isinstance(err, ConnectTimeoutError)
-
-    def _is_read_error(self, err):
-        """ Errors that occur after the request has been started, so we should
-        assume that the server began processing it.
-        """
-        return isinstance(err, (ReadTimeoutError, ProtocolError))
-
-    def _is_method_retryable(self, method):
-        """ Checks if a given HTTP method should be retried upon, depending if
-        it is included on the method whitelist.
-        """
-        if self.method_whitelist and method.upper() not in self.method_whitelist:
-            return False
-
-        return True
-
-    def is_retry(self, method, status_code, has_retry_after=False):
-        """ Is this method/status code retryable? (Based on whitelists and control
-        variables such as the number of total retries to allow, whether to
-        respect the Retry-After header, whether this header is present, and
-        whether the returned status code is on the list of status codes to
-        be retried upon on the presence of the aforementioned header)
-        """
-        if not self._is_method_retryable(method):
-            return False
-
-        if self.status_forcelist and status_code in self.status_forcelist:
-            return True
-
-        return (self.total and self.respect_retry_after_header and
-                has_retry_after and (status_code in self.RETRY_AFTER_STATUS_CODES))
-
-    def is_exhausted(self):
-        """ Are we out of retries? """
-        retry_counts = (self.total, self.connect, self.read, self.redirect, self.status)
-        retry_counts = list(filter(None, retry_counts))
-        if not retry_counts:
-            return False
-
-        return min(retry_counts) < 0
-
-    def increment(self, method=None, url=None, response=None, error=None,
-                  _pool=None, _stacktrace=None):
-        """ Return a new Retry object with incremented retry counters.
-
-        :param response: A response object, or None, if the server did not
-            return a response.
-        :type response: :class:`~urllib3.response.HTTPResponse`
-        :param Exception error: An error encountered during the request, or
-            None if the response was received successfully.
-
-        :return: A new ``Retry`` object.
-        """
-        if self.total is False and error:
-            # Disabled, indicate to re-raise the error.
-            raise six.reraise(type(error), error, _stacktrace)
-
-        total = self.total
-        if total is not None:
-            total -= 1
-
-        connect = self.connect
-        read = self.read
-        redirect = self.redirect
-        status_count = self.status
-        cause = 'unknown'
-        status = None
-        redirect_location = None
-
-        if error and self._is_connection_error(error):
-            # Connect retry?
-            if connect is False:
-                raise six.reraise(type(error), error, _stacktrace)
-            elif connect is not None:
-                connect -= 1
-
-        elif error and self._is_read_error(error):
-            # Read retry?
-            if read is False or not self._is_method_retryable(method):
-                raise six.reraise(type(error), error, _stacktrace)
-            elif read is not None:
-                read -= 1
-
-        elif response and response.get_redirect_location():
-            # Redirect retry?
-            if redirect is not None:
-                redirect -= 1
-            cause = 'too many redirects'
-            redirect_location = response.get_redirect_location()
-            status = response.status
-
-        else:
-            # Incrementing because of a server error like a 500 in
-            # status_forcelist and a the given method is in the whitelist
-            cause = ResponseError.GENERIC_ERROR
-            if response and response.status:
-                if status_count is not None:
-                    status_count -= 1
-                cause = ResponseError.SPECIFIC_ERROR.format(
-                    status_code=response.status)
-                status = response.status
-
-        history = self.history + (RequestHistory(method, url, error, status, redirect_location),)
-
-        new_retry = self.new(
-            total=total,
-            connect=connect, read=read, redirect=redirect, status=status_count,
-            history=history)
-
-        if new_retry.is_exhausted():
-            raise MaxRetryError(_pool, url, error or ResponseError(cause))
-
-        log.debug("Incremented Retry for (url='%s'): %r", url, new_retry)
-
-        return new_retry
-
-    def __repr__(self):
-        return ('{cls.__name__}(total={self.total}, connect={self.connect}, '
-                'read={self.read}, redirect={self.redirect}, status={self.status})').format(
-                    cls=type(self), self=self)
-
-
-# For backwards compatibility (equivalent to pre-v1.9):
-Retry.DEFAULT = Retry(3)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/ssl_.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/ssl_.py
deleted file mode 100644
index dfc553f..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/ssl_.py
+++ /dev/null
@@ -1,381 +0,0 @@
-from __future__ import absolute_import
-import errno
-import warnings
-import hmac
-import socket
-
-from binascii import hexlify, unhexlify
-from hashlib import md5, sha1, sha256
-
-from ..exceptions import SSLError, InsecurePlatformWarning, SNIMissingWarning
-from ..packages import six
-
-
-SSLContext = None
-HAS_SNI = False
-IS_PYOPENSSL = False
-IS_SECURETRANSPORT = False
-
-# Maps the length of a digest to a possible hash function producing this digest
-HASHFUNC_MAP = {
-    32: md5,
-    40: sha1,
-    64: sha256,
-}
-
-
-def _const_compare_digest_backport(a, b):
-    """
-    Compare two digests of equal length in constant time.
-
-    The digests must be of type str/bytes.
-    Returns True if the digests match, and False otherwise.
-    """
-    result = abs(len(a) - len(b))
-    for l, r in zip(bytearray(a), bytearray(b)):
-        result |= l ^ r
-    return result == 0
-
-
-_const_compare_digest = getattr(hmac, 'compare_digest',
-                                _const_compare_digest_backport)
-
-
-try:  # Test for SSL features
-    import ssl
-    from ssl import wrap_socket, CERT_NONE, PROTOCOL_SSLv23
-    from ssl import HAS_SNI  # Has SNI?
-except ImportError:
-    pass
-
-
-try:
-    from ssl import OP_NO_SSLv2, OP_NO_SSLv3, OP_NO_COMPRESSION
-except ImportError:
-    OP_NO_SSLv2, OP_NO_SSLv3 = 0x1000000, 0x2000000
-    OP_NO_COMPRESSION = 0x20000
-
-
-# Python 2.7 doesn't have inet_pton on non-Linux so we fallback on inet_aton in
-# those cases. This means that we can only detect IPv4 addresses in this case.
-if hasattr(socket, 'inet_pton'):
-    inet_pton = socket.inet_pton
-else:
-    # Maybe we can use ipaddress if the user has urllib3[secure]?
-    try:
-        from pip._vendor import ipaddress
-
-        def inet_pton(_, host):
-            if isinstance(host, bytes):
-                host = host.decode('ascii')
-            return ipaddress.ip_address(host)
-
-    except ImportError:  # Platform-specific: Non-Linux
-        def inet_pton(_, host):
-            return socket.inet_aton(host)
-
-
-# A secure default.
-# Sources for more information on TLS ciphers:
-#
-# - https://wiki.mozilla.org/Security/Server_Side_TLS
-# - https://www.ssllabs.com/projects/best-practices/index.html
-# - https://hynek.me/articles/hardening-your-web-servers-ssl-ciphers/
-#
-# The general intent is:
-# - Prefer TLS 1.3 cipher suites
-# - prefer cipher suites that offer perfect forward secrecy (DHE/ECDHE),
-# - prefer ECDHE over DHE for better performance,
-# - prefer any AES-GCM and ChaCha20 over any AES-CBC for better performance and
-#   security,
-# - prefer AES-GCM over ChaCha20 because hardware-accelerated AES is common,
-# - disable NULL authentication, MD5 MACs and DSS for security reasons.
-DEFAULT_CIPHERS = ':'.join([
-    'TLS13-AES-256-GCM-SHA384',
-    'TLS13-CHACHA20-POLY1305-SHA256',
-    'TLS13-AES-128-GCM-SHA256',
-    'ECDH+AESGCM',
-    'ECDH+CHACHA20',
-    'DH+AESGCM',
-    'DH+CHACHA20',
-    'ECDH+AES256',
-    'DH+AES256',
-    'ECDH+AES128',
-    'DH+AES',
-    'RSA+AESGCM',
-    'RSA+AES',
-    '!aNULL',
-    '!eNULL',
-    '!MD5',
-])
-
-try:
-    from ssl import SSLContext  # Modern SSL?
-except ImportError:
-    import sys
-
-    class SSLContext(object):  # Platform-specific: Python 2
-        def __init__(self, protocol_version):
-            self.protocol = protocol_version
-            # Use default values from a real SSLContext
-            self.check_hostname = False
-            self.verify_mode = ssl.CERT_NONE
-            self.ca_certs = None
-            self.options = 0
-            self.certfile = None
-            self.keyfile = None
-            self.ciphers = None
-
-        def load_cert_chain(self, certfile, keyfile):
-            self.certfile = certfile
-            self.keyfile = keyfile
-
-        def load_verify_locations(self, cafile=None, capath=None):
-            self.ca_certs = cafile
-
-            if capath is not None:
-                raise SSLError("CA directories not supported in older Pythons")
-
-        def set_ciphers(self, cipher_suite):
-            self.ciphers = cipher_suite
-
-        def wrap_socket(self, socket, server_hostname=None, server_side=False):
-            warnings.warn(
-                'A true SSLContext object is not available. This prevents '
-                'urllib3 from configuring SSL appropriately and may cause '
-                'certain SSL connections to fail. You can upgrade to a newer '
-                'version of Python to solve this. For more information, see '
-                'https://urllib3.readthedocs.io/en/latest/advanced-usage.html'
-                '#ssl-warnings',
-                InsecurePlatformWarning
-            )
-            kwargs = {
-                'keyfile': self.keyfile,
-                'certfile': self.certfile,
-                'ca_certs': self.ca_certs,
-                'cert_reqs': self.verify_mode,
-                'ssl_version': self.protocol,
-                'server_side': server_side,
-            }
-            return wrap_socket(socket, ciphers=self.ciphers, **kwargs)
-
-
-def assert_fingerprint(cert, fingerprint):
-    """
-    Checks if given fingerprint matches the supplied certificate.
-
-    :param cert:
-        Certificate as bytes object.
-    :param fingerprint:
-        Fingerprint as string of hexdigits, can be interspersed by colons.
-    """
-
-    fingerprint = fingerprint.replace(':', '').lower()
-    digest_length = len(fingerprint)
-    hashfunc = HASHFUNC_MAP.get(digest_length)
-    if not hashfunc:
-        raise SSLError(
-            'Fingerprint of invalid length: {0}'.format(fingerprint))
-
-    # We need encode() here for py32; works on py2 and p33.
-    fingerprint_bytes = unhexlify(fingerprint.encode())
-
-    cert_digest = hashfunc(cert).digest()
-
-    if not _const_compare_digest(cert_digest, fingerprint_bytes):
-        raise SSLError('Fingerprints did not match. Expected "{0}", got "{1}".'
-                       .format(fingerprint, hexlify(cert_digest)))
-
-
-def resolve_cert_reqs(candidate):
-    """
-    Resolves the argument to a numeric constant, which can be passed to
-    the wrap_socket function/method from the ssl module.
-    Defaults to :data:`ssl.CERT_NONE`.
-    If given a string it is assumed to be the name of the constant in the
-    :mod:`ssl` module or its abbreviation.
-    (So you can specify `REQUIRED` instead of `CERT_REQUIRED`.
-    If it's neither `None` nor a string we assume it is already the numeric
-    constant which can directly be passed to wrap_socket.
-    """
-    if candidate is None:
-        return CERT_NONE
-
-    if isinstance(candidate, str):
-        res = getattr(ssl, candidate, None)
-        if res is None:
-            res = getattr(ssl, 'CERT_' + candidate)
-        return res
-
-    return candidate
-
-
-def resolve_ssl_version(candidate):
-    """
-    like resolve_cert_reqs
-    """
-    if candidate is None:
-        return PROTOCOL_SSLv23
-
-    if isinstance(candidate, str):
-        res = getattr(ssl, candidate, None)
-        if res is None:
-            res = getattr(ssl, 'PROTOCOL_' + candidate)
-        return res
-
-    return candidate
-
-
-def create_urllib3_context(ssl_version=None, cert_reqs=None,
-                           options=None, ciphers=None):
-    """All arguments have the same meaning as ``ssl_wrap_socket``.
-
-    By default, this function does a lot of the same work that
-    ``ssl.create_default_context`` does on Python 3.4+. It:
-
-    - Disables SSLv2, SSLv3, and compression
-    - Sets a restricted set of server ciphers
-
-    If you wish to enable SSLv3, you can do::
-
-        from pip._vendor.urllib3.util import ssl_
-        context = ssl_.create_urllib3_context()
-        context.options &= ~ssl_.OP_NO_SSLv3
-
-    You can do the same to enable compression (substituting ``COMPRESSION``
-    for ``SSLv3`` in the last line above).
-
-    :param ssl_version:
-        The desired protocol version to use. This will default to
-        PROTOCOL_SSLv23 which will negotiate the highest protocol that both
-        the server and your installation of OpenSSL support.
-    :param cert_reqs:
-        Whether to require the certificate verification. This defaults to
-        ``ssl.CERT_REQUIRED``.
-    :param options:
-        Specific OpenSSL options. These default to ``ssl.OP_NO_SSLv2``,
-        ``ssl.OP_NO_SSLv3``, ``ssl.OP_NO_COMPRESSION``.
-    :param ciphers:
-        Which cipher suites to allow the server to select.
-    :returns:
-        Constructed SSLContext object with specified options
-    :rtype: SSLContext
-    """
-    context = SSLContext(ssl_version or ssl.PROTOCOL_SSLv23)
-
-    context.set_ciphers(ciphers or DEFAULT_CIPHERS)
-
-    # Setting the default here, as we may have no ssl module on import
-    cert_reqs = ssl.CERT_REQUIRED if cert_reqs is None else cert_reqs
-
-    if options is None:
-        options = 0
-        # SSLv2 is easily broken and is considered harmful and dangerous
-        options |= OP_NO_SSLv2
-        # SSLv3 has several problems and is now dangerous
-        options |= OP_NO_SSLv3
-        # Disable compression to prevent CRIME attacks for OpenSSL 1.0+
-        # (issue #309)
-        options |= OP_NO_COMPRESSION
-
-    context.options |= options
-
-    context.verify_mode = cert_reqs
-    if getattr(context, 'check_hostname', None) is not None:  # Platform-specific: Python 3.2
-        # We do our own verification, including fingerprints and alternative
-        # hostnames. So disable it here
-        context.check_hostname = False
-    return context
-
-
-def ssl_wrap_socket(sock, keyfile=None, certfile=None, cert_reqs=None,
-                    ca_certs=None, server_hostname=None,
-                    ssl_version=None, ciphers=None, ssl_context=None,
-                    ca_cert_dir=None):
-    """
-    All arguments except for server_hostname, ssl_context, and ca_cert_dir have
-    the same meaning as they do when using :func:`ssl.wrap_socket`.
-
-    :param server_hostname:
-        When SNI is supported, the expected hostname of the certificate
-    :param ssl_context:
-        A pre-made :class:`SSLContext` object. If none is provided, one will
-        be created using :func:`create_urllib3_context`.
-    :param ciphers:
-        A string of ciphers we wish the client to support.
-    :param ca_cert_dir:
-        A directory containing CA certificates in multiple separate files, as
-        supported by OpenSSL's -CApath flag or the capath argument to
-        SSLContext.load_verify_locations().
-    """
-    context = ssl_context
-    if context is None:
-        # Note: This branch of code and all the variables in it are no longer
-        # used by urllib3 itself. We should consider deprecating and removing
-        # this code.
-        context = create_urllib3_context(ssl_version, cert_reqs,
-                                         ciphers=ciphers)
-
-    if ca_certs or ca_cert_dir:
-        try:
-            context.load_verify_locations(ca_certs, ca_cert_dir)
-        except IOError as e:  # Platform-specific: Python 2.7
-            raise SSLError(e)
-        # Py33 raises FileNotFoundError which subclasses OSError
-        # These are not equivalent unless we check the errno attribute
-        except OSError as e:  # Platform-specific: Python 3.3 and beyond
-            if e.errno == errno.ENOENT:
-                raise SSLError(e)
-            raise
-    elif getattr(context, 'load_default_certs', None) is not None:
-        # try to load OS default certs; works well on Windows (require Python3.4+)
-        context.load_default_certs()
-
-    if certfile:
-        context.load_cert_chain(certfile, keyfile)
-
-    # If we detect server_hostname is an IP address then the SNI
-    # extension should not be used according to RFC3546 Section 3.1
-    # We shouldn't warn the user if SNI isn't available but we would
-    # not be using SNI anyways due to IP address for server_hostname.
-    if ((server_hostname is not None and not is_ipaddress(server_hostname))
-            or IS_SECURETRANSPORT):
-        if HAS_SNI and server_hostname is not None:
-            return context.wrap_socket(sock, server_hostname=server_hostname)
-
-        warnings.warn(
-            'An HTTPS request has been made, but the SNI (Server Name '
-            'Indication) extension to TLS is not available on this platform. '
-            'This may cause the server to present an incorrect TLS '
-            'certificate, which can cause validation failures. You can upgrade to '
-            'a newer version of Python to solve this. For more information, see '
-            'https://urllib3.readthedocs.io/en/latest/advanced-usage.html'
-            '#ssl-warnings',
-            SNIMissingWarning
-        )
-
-    return context.wrap_socket(sock)
-
-
-def is_ipaddress(hostname):
-    """Detects whether the hostname given is an IP address.
-
-    :param str hostname: Hostname to examine.
-    :return: True if the hostname is an IP address, False otherwise.
-    """
-    if six.PY3 and isinstance(hostname, bytes):
-        # IDN A-label bytes are ASCII compatible.
-        hostname = hostname.decode('ascii')
-
-    families = [socket.AF_INET]
-    if hasattr(socket, 'AF_INET6'):
-        families.append(socket.AF_INET6)
-
-    for af in families:
-        try:
-            inet_pton(af, hostname)
-        except (socket.error, ValueError, OSError):
-            pass
-        else:
-            return True
-    return False
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/timeout.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/timeout.py
deleted file mode 100644
index cec817e..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/timeout.py
+++ /dev/null
@@ -1,242 +0,0 @@
-from __future__ import absolute_import
-# The default socket timeout, used by httplib to indicate that no timeout was
-# specified by the user
-from socket import _GLOBAL_DEFAULT_TIMEOUT
-import time
-
-from ..exceptions import TimeoutStateError
-
-# A sentinel value to indicate that no timeout was specified by the user in
-# urllib3
-_Default = object()
-
-
-# Use time.monotonic if available.
-current_time = getattr(time, "monotonic", time.time)
-
-
-class Timeout(object):
-    """ Timeout configuration.
-
-    Timeouts can be defined as a default for a pool::
-
-        timeout = Timeout(connect=2.0, read=7.0)
-        http = PoolManager(timeout=timeout)
-        response = http.request('GET', 'http://example.com/')
-
-    Or per-request (which overrides the default for the pool)::
-
-        response = http.request('GET', 'http://example.com/', timeout=Timeout(10))
-
-    Timeouts can be disabled by setting all the parameters to ``None``::
-
-        no_timeout = Timeout(connect=None, read=None)
-        response = http.request('GET', 'http://example.com/, timeout=no_timeout)
-
-
-    :param total:
-        This combines the connect and read timeouts into one; the read timeout
-        will be set to the time leftover from the connect attempt. In the
-        event that both a connect timeout and a total are specified, or a read
-        timeout and a total are specified, the shorter timeout will be applied.
-
-        Defaults to None.
-
-    :type total: integer, float, or None
-
-    :param connect:
-        The maximum amount of time to wait for a connection attempt to a server
-        to succeed. Omitting the parameter will default the connect timeout to
-        the system default, probably `the global default timeout in socket.py
-        <http://hg.python.org/cpython/file/603b4d593758/Lib/socket.py#l535>`_.
-        None will set an infinite timeout for connection attempts.
-
-    :type connect: integer, float, or None
-
-    :param read:
-        The maximum amount of time to wait between consecutive
-        read operations for a response from the server. Omitting
-        the parameter will default the read timeout to the system
-        default, probably `the global default timeout in socket.py
-        <http://hg.python.org/cpython/file/603b4d593758/Lib/socket.py#l535>`_.
-        None will set an infinite timeout.
-
-    :type read: integer, float, or None
-
-    .. note::
-
-        Many factors can affect the total amount of time for urllib3 to return
-        an HTTP response.
-
-        For example, Python's DNS resolver does not obey the timeout specified
-        on the socket. Other factors that can affect total request time include
-        high CPU load, high swap, the program running at a low priority level,
-        or other behaviors.
-
-        In addition, the read and total timeouts only measure the time between
-        read operations on the socket connecting the client and the server,
-        not the total amount of time for the request to return a complete
-        response. For most requests, the timeout is raised because the server
-        has not sent the first byte in the specified time. This is not always
-        the case; if a server streams one byte every fifteen seconds, a timeout
-        of 20 seconds will not trigger, even though the request will take
-        several minutes to complete.
-
-        If your goal is to cut off any request after a set amount of wall clock
-        time, consider having a second "watcher" thread to cut off a slow
-        request.
-    """
-
-    #: A sentinel object representing the default timeout value
-    DEFAULT_TIMEOUT = _GLOBAL_DEFAULT_TIMEOUT
-
-    def __init__(self, total=None, connect=_Default, read=_Default):
-        self._connect = self._validate_timeout(connect, 'connect')
-        self._read = self._validate_timeout(read, 'read')
-        self.total = self._validate_timeout(total, 'total')
-        self._start_connect = None
-
-    def __str__(self):
-        return '%s(connect=%r, read=%r, total=%r)' % (
-            type(self).__name__, self._connect, self._read, self.total)
-
-    @classmethod
-    def _validate_timeout(cls, value, name):
-        """ Check that a timeout attribute is valid.
-
-        :param value: The timeout value to validate
-        :param name: The name of the timeout attribute to validate. This is
-            used to specify in error messages.
-        :return: The validated and casted version of the given value.
-        :raises ValueError: If it is a numeric value less than or equal to
-            zero, or the type is not an integer, float, or None.
-        """
-        if value is _Default:
-            return cls.DEFAULT_TIMEOUT
-
-        if value is None or value is cls.DEFAULT_TIMEOUT:
-            return value
-
-        if isinstance(value, bool):
-            raise ValueError("Timeout cannot be a boolean value. It must "
-                             "be an int, float or None.")
-        try:
-            float(value)
-        except (TypeError, ValueError):
-            raise ValueError("Timeout value %s was %s, but it must be an "
-                             "int, float or None." % (name, value))
-
-        try:
-            if value <= 0:
-                raise ValueError("Attempted to set %s timeout to %s, but the "
-                                 "timeout cannot be set to a value less "
-                                 "than or equal to 0." % (name, value))
-        except TypeError:  # Python 3
-            raise ValueError("Timeout value %s was %s, but it must be an "
-                             "int, float or None." % (name, value))
-
-        return value
-
-    @classmethod
-    def from_float(cls, timeout):
-        """ Create a new Timeout from a legacy timeout value.
-
-        The timeout value used by httplib.py sets the same timeout on the
-        connect(), and recv() socket requests. This creates a :class:`Timeout`
-        object that sets the individual timeouts to the ``timeout`` value
-        passed to this function.
-
-        :param timeout: The legacy timeout value.
-        :type timeout: integer, float, sentinel default object, or None
-        :return: Timeout object
-        :rtype: :class:`Timeout`
-        """
-        return Timeout(read=timeout, connect=timeout)
-
-    def clone(self):
-        """ Create a copy of the timeout object
-
-        Timeout properties are stored per-pool but each request needs a fresh
-        Timeout object to ensure each one has its own start/stop configured.
-
-        :return: a copy of the timeout object
-        :rtype: :class:`Timeout`
-        """
-        # We can't use copy.deepcopy because that will also create a new object
-        # for _GLOBAL_DEFAULT_TIMEOUT, which socket.py uses as a sentinel to
-        # detect the user default.
-        return Timeout(connect=self._connect, read=self._read,
-                       total=self.total)
-
-    def start_connect(self):
-        """ Start the timeout clock, used during a connect() attempt
-
-        :raises urllib3.exceptions.TimeoutStateError: if you attempt
-            to start a timer that has been started already.
-        """
-        if self._start_connect is not None:
-            raise TimeoutStateError("Timeout timer has already been started.")
-        self._start_connect = current_time()
-        return self._start_connect
-
-    def get_connect_duration(self):
-        """ Gets the time elapsed since the call to :meth:`start_connect`.
-
-        :return: Elapsed time.
-        :rtype: float
-        :raises urllib3.exceptions.TimeoutStateError: if you attempt
-            to get duration for a timer that hasn't been started.
-        """
-        if self._start_connect is None:
-            raise TimeoutStateError("Can't get connect duration for timer "
-                                    "that has not started.")
-        return current_time() - self._start_connect
-
-    @property
-    def connect_timeout(self):
-        """ Get the value to use when setting a connection timeout.
-
-        This will be a positive float or integer, the value None
-        (never timeout), or the default system timeout.
-
-        :return: Connect timeout.
-        :rtype: int, float, :attr:`Timeout.DEFAULT_TIMEOUT` or None
-        """
-        if self.total is None:
-            return self._connect
-
-        if self._connect is None or self._connect is self.DEFAULT_TIMEOUT:
-            return self.total
-
-        return min(self._connect, self.total)
-
-    @property
-    def read_timeout(self):
-        """ Get the value for the read timeout.
-
-        This assumes some time has elapsed in the connection timeout and
-        computes the read timeout appropriately.
-
-        If self.total is set, the read timeout is dependent on the amount of
-        time taken by the connect timeout. If the connection time has not been
-        established, a :exc:`~urllib3.exceptions.TimeoutStateError` will be
-        raised.
-
-        :return: Value to use for the read timeout.
-        :rtype: int, float, :attr:`Timeout.DEFAULT_TIMEOUT` or None
-        :raises urllib3.exceptions.TimeoutStateError: If :meth:`start_connect`
-            has not yet been called on this object.
-        """
-        if (self.total is not None and
-                self.total is not self.DEFAULT_TIMEOUT and
-                self._read is not None and
-                self._read is not self.DEFAULT_TIMEOUT):
-            # In case the connect timeout has not yet been established.
-            if self._start_connect is None:
-                return self._read
-            return max(0, min(self.total - self.get_connect_duration(),
-                              self._read))
-        elif self.total is not None and self.total is not self.DEFAULT_TIMEOUT:
-            return max(0, self.total - self.get_connect_duration())
-        else:
-            return self._read
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/url.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/url.py
deleted file mode 100644
index 6b6f996..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/url.py
+++ /dev/null
@@ -1,230 +0,0 @@
-from __future__ import absolute_import
-from collections import namedtuple
-
-from ..exceptions import LocationParseError
-
-
-url_attrs = ['scheme', 'auth', 'host', 'port', 'path', 'query', 'fragment']
-
-# We only want to normalize urls with an HTTP(S) scheme.
-# urllib3 infers URLs without a scheme (None) to be http.
-NORMALIZABLE_SCHEMES = ('http', 'https', None)
-
-
-class Url(namedtuple('Url', url_attrs)):
-    """
-    Datastructure for representing an HTTP URL. Used as a return value for
-    :func:`parse_url`. Both the scheme and host are normalized as they are
-    both case-insensitive according to RFC 3986.
-    """
-    __slots__ = ()
-
-    def __new__(cls, scheme=None, auth=None, host=None, port=None, path=None,
-                query=None, fragment=None):
-        if path and not path.startswith('/'):
-            path = '/' + path
-        if scheme:
-            scheme = scheme.lower()
-        if host and scheme in NORMALIZABLE_SCHEMES:
-            host = host.lower()
-        return super(Url, cls).__new__(cls, scheme, auth, host, port, path,
-                                       query, fragment)
-
-    @property
-    def hostname(self):
-        """For backwards-compatibility with urlparse. We're nice like that."""
-        return self.host
-
-    @property
-    def request_uri(self):
-        """Absolute path including the query string."""
-        uri = self.path or '/'
-
-        if self.query is not None:
-            uri += '?' + self.query
-
-        return uri
-
-    @property
-    def netloc(self):
-        """Network location including host and port"""
-        if self.port:
-            return '%s:%d' % (self.host, self.port)
-        return self.host
-
-    @property
-    def url(self):
-        """
-        Convert self into a url
-
-        This function should more or less round-trip with :func:`.parse_url`. The
-        returned url may not be exactly the same as the url inputted to
-        :func:`.parse_url`, but it should be equivalent by the RFC (e.g., urls
-        with a blank port will have : removed).
-
-        Example: ::
-
-            >>> U = parse_url('http://google.com/mail/')
-            >>> U.url
-            'http://google.com/mail/'
-            >>> Url('http', 'username:password', 'host.com', 80,
-            ... '/path', 'query', 'fragment').url
-            'http://username:password@host.com:80/path?query#fragment'
-        """
-        scheme, auth, host, port, path, query, fragment = self
-        url = ''
-
-        # We use "is not None" we want things to happen with empty strings (or 0 port)
-        if scheme is not None:
-            url += scheme + '://'
-        if auth is not None:
-            url += auth + '@'
-        if host is not None:
-            url += host
-        if port is not None:
-            url += ':' + str(port)
-        if path is not None:
-            url += path
-        if query is not None:
-            url += '?' + query
-        if fragment is not None:
-            url += '#' + fragment
-
-        return url
-
-    def __str__(self):
-        return self.url
-
-
-def split_first(s, delims):
-    """
-    Given a string and an iterable of delimiters, split on the first found
-    delimiter. Return two split parts and the matched delimiter.
-
-    If not found, then the first part is the full input string.
-
-    Example::
-
-        >>> split_first('foo/bar?baz', '?/=')
-        ('foo', 'bar?baz', '/')
-        >>> split_first('foo/bar?baz', '123')
-        ('foo/bar?baz', '', None)
-
-    Scales linearly with number of delims. Not ideal for large number of delims.
-    """
-    min_idx = None
-    min_delim = None
-    for d in delims:
-        idx = s.find(d)
-        if idx < 0:
-            continue
-
-        if min_idx is None or idx < min_idx:
-            min_idx = idx
-            min_delim = d
-
-    if min_idx is None or min_idx < 0:
-        return s, '', None
-
-    return s[:min_idx], s[min_idx + 1:], min_delim
-
-
-def parse_url(url):
-    """
-    Given a url, return a parsed :class:`.Url` namedtuple. Best-effort is
-    performed to parse incomplete urls. Fields not provided will be None.
-
-    Partly backwards-compatible with :mod:`urlparse`.
-
-    Example::
-
-        >>> parse_url('http://google.com/mail/')
-        Url(scheme='http', host='google.com', port=None, path='/mail/', ...)
-        >>> parse_url('google.com:80')
-        Url(scheme=None, host='google.com', port=80, path=None, ...)
-        >>> parse_url('/foo?bar')
-        Url(scheme=None, host=None, port=None, path='/foo', query='bar', ...)
-    """
-
-    # While this code has overlap with stdlib's urlparse, it is much
-    # simplified for our needs and less annoying.
-    # Additionally, this implementations does silly things to be optimal
-    # on CPython.
-
-    if not url:
-        # Empty
-        return Url()
-
-    scheme = None
-    auth = None
-    host = None
-    port = None
-    path = None
-    fragment = None
-    query = None
-
-    # Scheme
-    if '://' in url:
-        scheme, url = url.split('://', 1)
-
-    # Find the earliest Authority Terminator
-    # (http://tools.ietf.org/html/rfc3986#section-3.2)
-    url, path_, delim = split_first(url, ['/', '?', '#'])
-
-    if delim:
-        # Reassemble the path
-        path = delim + path_
-
-    # Auth
-    if '@' in url:
-        # Last '@' denotes end of auth part
-        auth, url = url.rsplit('@', 1)
-
-    # IPv6
-    if url and url[0] == '[':
-        host, url = url.split(']', 1)
-        host += ']'
-
-    # Port
-    if ':' in url:
-        _host, port = url.split(':', 1)
-
-        if not host:
-            host = _host
-
-        if port:
-            # If given, ports must be integers. No whitespace, no plus or
-            # minus prefixes, no non-integer digits such as ^2 (superscript).
-            if not port.isdigit():
-                raise LocationParseError(url)
-            try:
-                port = int(port)
-            except ValueError:
-                raise LocationParseError(url)
-        else:
-            # Blank ports are cool, too. (rfc3986#section-3.2.3)
-            port = None
-
-    elif not host and url:
-        host = url
-
-    if not path:
-        return Url(scheme, auth, host, port, path, query, fragment)
-
-    # Fragment
-    if '#' in path:
-        path, fragment = path.split('#', 1)
-
-    # Query
-    if '?' in path:
-        path, query = path.split('?', 1)
-
-    return Url(scheme, auth, host, port, path, query, fragment)
-
-
-def get_host(url):
-    """
-    Deprecated. Use :func:`parse_url` instead.
-    """
-    p = parse_url(url)
-    return p.scheme or 'http', p.hostname, p.port
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/wait.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/wait.py
deleted file mode 100644
index 4db71ba..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/urllib3/util/wait.py
+++ /dev/null
@@ -1,150 +0,0 @@
-import errno
-from functools import partial
-import select
-import sys
-try:
-    from time import monotonic
-except ImportError:
-    from time import time as monotonic
-
-__all__ = ["NoWayToWaitForSocketError", "wait_for_read", "wait_for_write"]
-
-
-class NoWayToWaitForSocketError(Exception):
-    pass
-
-
-# How should we wait on sockets?
-#
-# There are two types of APIs you can use for waiting on sockets: the fancy
-# modern stateful APIs like epoll/kqueue, and the older stateless APIs like
-# select/poll. The stateful APIs are more efficient when you have a lots of
-# sockets to keep track of, because you can set them up once and then use them
-# lots of times. But we only ever want to wait on a single socket at a time
-# and don't want to keep track of state, so the stateless APIs are actually
-# more efficient. So we want to use select() or poll().
-#
-# Now, how do we choose between select() and poll()? On traditional Unixes,
-# select() has a strange calling convention that makes it slow, or fail
-# altogether, for high-numbered file descriptors. The point of poll() is to fix
-# that, so on Unixes, we prefer poll().
-#
-# On Windows, there is no poll() (or at least Python doesn't provide a wrapper
-# for it), but that's OK, because on Windows, select() doesn't have this
-# strange calling convention; plain select() works fine.
-#
-# So: on Windows we use select(), and everywhere else we use poll(). We also
-# fall back to select() in case poll() is somehow broken or missing.
-
-if sys.version_info >= (3, 5):
-    # Modern Python, that retries syscalls by default
-    def _retry_on_intr(fn, timeout):
-        return fn(timeout)
-else:
-    # Old and broken Pythons.
-    def _retry_on_intr(fn, timeout):
-        if timeout is None:
-            deadline = float("inf")
-        else:
-            deadline = monotonic() + timeout
-
-        while True:
-            try:
-                return fn(timeout)
-            # OSError for 3 <= pyver < 3.5, select.error for pyver <= 2.7
-            except (OSError, select.error) as e:
-                # 'e.args[0]' incantation works for both OSError and select.error
-                if e.args[0] != errno.EINTR:
-                    raise
-                else:
-                    timeout = deadline - monotonic()
-                    if timeout < 0:
-                        timeout = 0
-                    if timeout == float("inf"):
-                        timeout = None
-                    continue
-
-
-def select_wait_for_socket(sock, read=False, write=False, timeout=None):
-    if not read and not write:
-        raise RuntimeError("must specify at least one of read=True, write=True")
-    rcheck = []
-    wcheck = []
-    if read:
-        rcheck.append(sock)
-    if write:
-        wcheck.append(sock)
-    # When doing a non-blocking connect, most systems signal success by
-    # marking the socket writable. Windows, though, signals success by marked
-    # it as "exceptional". We paper over the difference by checking the write
-    # sockets for both conditions. (The stdlib selectors module does the same
-    # thing.)
-    fn = partial(select.select, rcheck, wcheck, wcheck)
-    rready, wready, xready = _retry_on_intr(fn, timeout)
-    return bool(rready or wready or xready)
-
-
-def poll_wait_for_socket(sock, read=False, write=False, timeout=None):
-    if not read and not write:
-        raise RuntimeError("must specify at least one of read=True, write=True")
-    mask = 0
-    if read:
-        mask |= select.POLLIN
-    if write:
-        mask |= select.POLLOUT
-    poll_obj = select.poll()
-    poll_obj.register(sock, mask)
-
-    # For some reason, poll() takes timeout in milliseconds
-    def do_poll(t):
-        if t is not None:
-            t *= 1000
-        return poll_obj.poll(t)
-
-    return bool(_retry_on_intr(do_poll, timeout))
-
-
-def null_wait_for_socket(*args, **kwargs):
-    raise NoWayToWaitForSocketError("no select-equivalent available")
-
-
-def _have_working_poll():
-    # Apparently some systems have a select.poll that fails as soon as you try
-    # to use it, either due to strange configuration or broken monkeypatching
-    # from libraries like eventlet/greenlet.
-    try:
-        poll_obj = select.poll()
-        _retry_on_intr(poll_obj.poll, 0)
-    except (AttributeError, OSError):
-        return False
-    else:
-        return True
-
-
-def wait_for_socket(*args, **kwargs):
-    # We delay choosing which implementation to use until the first time we're
-    # called. We could do it at import time, but then we might make the wrong
-    # decision if someone goes wild with monkeypatching select.poll after
-    # we're imported.
-    global wait_for_socket
-    if _have_working_poll():
-        wait_for_socket = poll_wait_for_socket
-    elif hasattr(select, "select"):
-        wait_for_socket = select_wait_for_socket
-    else:  # Platform-specific: Appengine.
-        wait_for_socket = null_wait_for_socket
-    return wait_for_socket(*args, **kwargs)
-
-
-def wait_for_read(sock, timeout=None):
-    """ Waits for reading to be available on a given socket.
-    Returns True if the socket is readable, or False if the timeout expired.
-    """
-    return wait_for_socket(sock, read=True, timeout=timeout)
-
-
-def wait_for_write(sock, timeout=None):
-    """ Waits for writing to be available on a given socket.
-    Returns True if the socket is readable, or False if the timeout expired.
-    """
-    return wait_for_socket(sock, write=True, timeout=timeout)
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__init__.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__init__.py
deleted file mode 100644
index d21d697..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__init__.py
+++ /dev/null
@@ -1,342 +0,0 @@
-# coding: utf-8
-"""
-
-    webencodings
-    ~~~~~~~~~~~~
-
-    This is a Python implementation of the `WHATWG Encoding standard
-    <http://encoding.spec.whatwg.org/>`. See README for details.
-
-    :copyright: Copyright 2012 by Simon Sapin
-    :license: BSD, see LICENSE for details.
-
-"""
-
-from __future__ import unicode_literals
-
-import codecs
-
-from .labels import LABELS
-
-
-VERSION = '0.5.1'
-
-
-# Some names in Encoding are not valid Python aliases. Remap these.
-PYTHON_NAMES = {
-    'iso-8859-8-i': 'iso-8859-8',
-    'x-mac-cyrillic': 'mac-cyrillic',
-    'macintosh': 'mac-roman',
-    'windows-874': 'cp874'}
-
-CACHE = {}
-
-
-def ascii_lower(string):
-    r"""Transform (only) ASCII letters to lower case: A-Z is mapped to a-z.
-
-    :param string: An Unicode string.
-    :returns: A new Unicode string.
-
-    This is used for `ASCII case-insensitive
-    <http://encoding.spec.whatwg.org/#ascii-case-insensitive>`_
-    matching of encoding labels.
-    The same matching is also used, among other things,
-    for `CSS keywords <http://dev.w3.org/csswg/css-values/#keywords>`_.
-
-    This is different from the :meth:`~py:str.lower` method of Unicode strings
-    which also affect non-ASCII characters,
-    sometimes mapping them into the ASCII range:
-
-        >>> keyword = u'Bac\N{KELVIN SIGN}ground'
-        >>> assert keyword.lower() == u'background'
-        >>> assert ascii_lower(keyword) != keyword.lower()
-        >>> assert ascii_lower(keyword) == u'bac\N{KELVIN SIGN}ground'
-
-    """
-    # This turns out to be faster than unicode.translate()
-    return string.encode('utf8').lower().decode('utf8')
-
-
-def lookup(label):
-    """
-    Look for an encoding by its label.
-    This is the spec’s `get an encoding
-    <http://encoding.spec.whatwg.org/#concept-encoding-get>`_ algorithm.
-    Supported labels are listed there.
-
-    :param label: A string.
-    :returns:
-        An :class:`Encoding` object, or :obj:`None` for an unknown label.
-
-    """
-    # Only strip ASCII whitespace: U+0009, U+000A, U+000C, U+000D, and U+0020.
-    label = ascii_lower(label.strip('\t\n\f\r '))
-    name = LABELS.get(label)
-    if name is None:
-        return None
-    encoding = CACHE.get(name)
-    if encoding is None:
-        if name == 'x-user-defined':
-            from .x_user_defined import codec_info
-        else:
-            python_name = PYTHON_NAMES.get(name, name)
-            # Any python_name value that gets to here should be valid.
-            codec_info = codecs.lookup(python_name)
-        encoding = Encoding(name, codec_info)
-        CACHE[name] = encoding
-    return encoding
-
-
-def _get_encoding(encoding_or_label):
-    """
-    Accept either an encoding object or label.
-
-    :param encoding: An :class:`Encoding` object or a label string.
-    :returns: An :class:`Encoding` object.
-    :raises: :exc:`~exceptions.LookupError` for an unknown label.
-
-    """
-    if hasattr(encoding_or_label, 'codec_info'):
-        return encoding_or_label
-
-    encoding = lookup(encoding_or_label)
-    if encoding is None:
-        raise LookupError('Unknown encoding label: %r' % encoding_or_label)
-    return encoding
-
-
-class Encoding(object):
-    """Reresents a character encoding such as UTF-8,
-    that can be used for decoding or encoding.
-
-    .. attribute:: name
-
-        Canonical name of the encoding
-
-    .. attribute:: codec_info
-
-        The actual implementation of the encoding,
-        a stdlib :class:`~codecs.CodecInfo` object.
-        See :func:`codecs.register`.
-
-    """
-    def __init__(self, name, codec_info):
-        self.name = name
-        self.codec_info = codec_info
-
-    def __repr__(self):
-        return '<Encoding %s>' % self.name
-
-
-#: The UTF-8 encoding. Should be used for new content and formats.
-UTF8 = lookup('utf-8')
-
-_UTF16LE = lookup('utf-16le')
-_UTF16BE = lookup('utf-16be')
-
-
-def decode(input, fallback_encoding, errors='replace'):
-    """
-    Decode a single string.
-
-    :param input: A byte string
-    :param fallback_encoding:
-        An :class:`Encoding` object or a label string.
-        The encoding to use if :obj:`input` does note have a BOM.
-    :param errors: Type of error handling. See :func:`codecs.register`.
-    :raises: :exc:`~exceptions.LookupError` for an unknown encoding label.
-    :return:
-        A ``(output, encoding)`` tuple of an Unicode string
-        and an :obj:`Encoding`.
-
-    """
-    # Fail early if `encoding` is an invalid label.
-    fallback_encoding = _get_encoding(fallback_encoding)
-    bom_encoding, input = _detect_bom(input)
-    encoding = bom_encoding or fallback_encoding
-    return encoding.codec_info.decode(input, errors)[0], encoding
-
-
-def _detect_bom(input):
-    """Return (bom_encoding, input), with any BOM removed from the input."""
-    if input.startswith(b'\xFF\xFE'):
-        return _UTF16LE, input[2:]
-    if input.startswith(b'\xFE\xFF'):
-        return _UTF16BE, input[2:]
-    if input.startswith(b'\xEF\xBB\xBF'):
-        return UTF8, input[3:]
-    return None, input
-
-
-def encode(input, encoding=UTF8, errors='strict'):
-    """
-    Encode a single string.
-
-    :param input: An Unicode string.
-    :param encoding: An :class:`Encoding` object or a label string.
-    :param errors: Type of error handling. See :func:`codecs.register`.
-    :raises: :exc:`~exceptions.LookupError` for an unknown encoding label.
-    :return: A byte string.
-
-    """
-    return _get_encoding(encoding).codec_info.encode(input, errors)[0]
-
-
-def iter_decode(input, fallback_encoding, errors='replace'):
-    """
-    "Pull"-based decoder.
-
-    :param input:
-        An iterable of byte strings.
-
-        The input is first consumed just enough to determine the encoding
-        based on the precense of a BOM,
-        then consumed on demand when the return value is.
-    :param fallback_encoding:
-        An :class:`Encoding` object or a label string.
-        The encoding to use if :obj:`input` does note have a BOM.
-    :param errors: Type of error handling. See :func:`codecs.register`.
-    :raises: :exc:`~exceptions.LookupError` for an unknown encoding label.
-    :returns:
-        An ``(output, encoding)`` tuple.
-        :obj:`output` is an iterable of Unicode strings,
-        :obj:`encoding` is the :obj:`Encoding` that is being used.
-
-    """
-
-    decoder = IncrementalDecoder(fallback_encoding, errors)
-    generator = _iter_decode_generator(input, decoder)
-    encoding = next(generator)
-    return generator, encoding
-
-
-def _iter_decode_generator(input, decoder):
-    """Return a generator that first yields the :obj:`Encoding`,
-    then yields output chukns as Unicode strings.
-
-    """
-    decode = decoder.decode
-    input = iter(input)
-    for chunck in input:
-        output = decode(chunck)
-        if output:
-            assert decoder.encoding is not None
-            yield decoder.encoding
-            yield output
-            break
-    else:
-        # Input exhausted without determining the encoding
-        output = decode(b'', final=True)
-        assert decoder.encoding is not None
-        yield decoder.encoding
-        if output:
-            yield output
-        return
-
-    for chunck in input:
-        output = decode(chunck)
-        if output:
-            yield output
-    output = decode(b'', final=True)
-    if output:
-        yield output
-
-
-def iter_encode(input, encoding=UTF8, errors='strict'):
-    """
-    “Pull”-based encoder.
-
-    :param input: An iterable of Unicode strings.
-    :param encoding: An :class:`Encoding` object or a label string.
-    :param errors: Type of error handling. See :func:`codecs.register`.
-    :raises: :exc:`~exceptions.LookupError` for an unknown encoding label.
-    :returns: An iterable of byte strings.
-
-    """
-    # Fail early if `encoding` is an invalid label.
-    encode = IncrementalEncoder(encoding, errors).encode
-    return _iter_encode_generator(input, encode)
-
-
-def _iter_encode_generator(input, encode):
-    for chunck in input:
-        output = encode(chunck)
-        if output:
-            yield output
-    output = encode('', final=True)
-    if output:
-        yield output
-
-
-class IncrementalDecoder(object):
-    """
-    “Push”-based decoder.
-
-    :param fallback_encoding:
-        An :class:`Encoding` object or a label string.
-        The encoding to use if :obj:`input` does note have a BOM.
-    :param errors: Type of error handling. See :func:`codecs.register`.
-    :raises: :exc:`~exceptions.LookupError` for an unknown encoding label.
-
-    """
-    def __init__(self, fallback_encoding, errors='replace'):
-        # Fail early if `encoding` is an invalid label.
-        self._fallback_encoding = _get_encoding(fallback_encoding)
-        self._errors = errors
-        self._buffer = b''
-        self._decoder = None
-        #: The actual :class:`Encoding` that is being used,
-        #: or :obj:`None` if that is not determined yet.
-        #: (Ie. if there is not enough input yet to determine
-        #: if there is a BOM.)
-        self.encoding = None  # Not known yet.
-
-    def decode(self, input, final=False):
-        """Decode one chunk of the input.
-
-        :param input: A byte string.
-        :param final:
-            Indicate that no more input is available.
-            Must be :obj:`True` if this is the last call.
-        :returns: An Unicode string.
-
-        """
-        decoder = self._decoder
-        if decoder is not None:
-            return decoder(input, final)
-
-        input = self._buffer + input
-        encoding, input = _detect_bom(input)
-        if encoding is None:
-            if len(input) < 3 and not final:  # Not enough data yet.
-                self._buffer = input
-                return ''
-            else:  # No BOM
-                encoding = self._fallback_encoding
-        decoder = encoding.codec_info.incrementaldecoder(self._errors).decode
-        self._decoder = decoder
-        self.encoding = encoding
-        return decoder(input, final)
-
-
-class IncrementalEncoder(object):
-    """
-    “Push”-based encoder.
-
-    :param encoding: An :class:`Encoding` object or a label string.
-    :param errors: Type of error handling. See :func:`codecs.register`.
-    :raises: :exc:`~exceptions.LookupError` for an unknown encoding label.
-
-    .. method:: encode(input, final=False)
-
-        :param input: An Unicode string.
-        :param final:
-            Indicate that no more input is available.
-            Must be :obj:`True` if this is the last call.
-        :returns: A byte string.
-
-    """
-    def __init__(self, encoding=UTF8, errors='strict'):
-        encoding = _get_encoding(encoding)
-        self.encode = encoding.codec_info.incrementalencoder(errors).encode
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index f2a122d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__pycache__/labels.cpython-37.pyc b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__pycache__/labels.cpython-37.pyc
deleted file mode 100644
index 5530901..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/__pycache__/labels.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/labels.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/labels.py
deleted file mode 100644
index 29cbf91..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/labels.py
+++ /dev/null
@@ -1,231 +0,0 @@
-"""
-
-    webencodings.labels
-    ~~~~~~~~~~~~~~~~~~~
-
-    Map encoding labels to their name.
-
-    :copyright: Copyright 2012 by Simon Sapin
-    :license: BSD, see LICENSE for details.
-
-"""
-
-# XXX Do not edit!
-# This file is automatically generated by mklabels.py
-
-LABELS = {
-    'unicode-1-1-utf-8':   'utf-8',
-    'utf-8':               'utf-8',
-    'utf8':                'utf-8',
-    '866':                 'ibm866',
-    'cp866':               'ibm866',
-    'csibm866':            'ibm866',
-    'ibm866':              'ibm866',
-    'csisolatin2':         'iso-8859-2',
-    'iso-8859-2':          'iso-8859-2',
-    'iso-ir-101':          'iso-8859-2',
-    'iso8859-2':           'iso-8859-2',
-    'iso88592':            'iso-8859-2',
-    'iso_8859-2':          'iso-8859-2',
-    'iso_8859-2:1987':     'iso-8859-2',
-    'l2':                  'iso-8859-2',
-    'latin2':              'iso-8859-2',
-    'csisolatin3':         'iso-8859-3',
-    'iso-8859-3':          'iso-8859-3',
-    'iso-ir-109':          'iso-8859-3',
-    'iso8859-3':           'iso-8859-3',
-    'iso88593':            'iso-8859-3',
-    'iso_8859-3':          'iso-8859-3',
-    'iso_8859-3:1988':     'iso-8859-3',
-    'l3':                  'iso-8859-3',
-    'latin3':              'iso-8859-3',
-    'csisolatin4':         'iso-8859-4',
-    'iso-8859-4':          'iso-8859-4',
-    'iso-ir-110':          'iso-8859-4',
-    'iso8859-4':           'iso-8859-4',
-    'iso88594':            'iso-8859-4',
-    'iso_8859-4':          'iso-8859-4',
-    'iso_8859-4:1988':     'iso-8859-4',
-    'l4':                  'iso-8859-4',
-    'latin4':              'iso-8859-4',
-    'csisolatincyrillic':  'iso-8859-5',
-    'cyrillic':            'iso-8859-5',
-    'iso-8859-5':          'iso-8859-5',
-    'iso-ir-144':          'iso-8859-5',
-    'iso8859-5':           'iso-8859-5',
-    'iso88595':            'iso-8859-5',
-    'iso_8859-5':          'iso-8859-5',
-    'iso_8859-5:1988':     'iso-8859-5',
-    'arabic':              'iso-8859-6',
-    'asmo-708':            'iso-8859-6',
-    'csiso88596e':         'iso-8859-6',
-    'csiso88596i':         'iso-8859-6',
-    'csisolatinarabic':    'iso-8859-6',
-    'ecma-114':            'iso-8859-6',
-    'iso-8859-6':          'iso-8859-6',
-    'iso-8859-6-e':        'iso-8859-6',
-    'iso-8859-6-i':        'iso-8859-6',
-    'iso-ir-127':          'iso-8859-6',
-    'iso8859-6':           'iso-8859-6',
-    'iso88596':            'iso-8859-6',
-    'iso_8859-6':          'iso-8859-6',
-    'iso_8859-6:1987':     'iso-8859-6',
-    'csisolatingreek':     'iso-8859-7',
-    'ecma-118':            'iso-8859-7',
-    'elot_928':            'iso-8859-7',
-    'greek':               'iso-8859-7',
-    'greek8':              'iso-8859-7',
-    'iso-8859-7':          'iso-8859-7',
-    'iso-ir-126':          'iso-8859-7',
-    'iso8859-7':           'iso-8859-7',
-    'iso88597':            'iso-8859-7',
-    'iso_8859-7':          'iso-8859-7',
-    'iso_8859-7:1987':     'iso-8859-7',
-    'sun_eu_greek':        'iso-8859-7',
-    'csiso88598e':         'iso-8859-8',
-    'csisolatinhebrew':    'iso-8859-8',
-    'hebrew':              'iso-8859-8',
-    'iso-8859-8':          'iso-8859-8',
-    'iso-8859-8-e':        'iso-8859-8',
-    'iso-ir-138':          'iso-8859-8',
-    'iso8859-8':           'iso-8859-8',
-    'iso88598':            'iso-8859-8',
-    'iso_8859-8':          'iso-8859-8',
-    'iso_8859-8:1988':     'iso-8859-8',
-    'visual':              'iso-8859-8',
-    'csiso88598i':         'iso-8859-8-i',
-    'iso-8859-8-i':        'iso-8859-8-i',
-    'logical':             'iso-8859-8-i',
-    'csisolatin6':         'iso-8859-10',
-    'iso-8859-10':         'iso-8859-10',
-    'iso-ir-157':          'iso-8859-10',
-    'iso8859-10':          'iso-8859-10',
-    'iso885910':           'iso-8859-10',
-    'l6':                  'iso-8859-10',
-    'latin6':              'iso-8859-10',
-    'iso-8859-13':         'iso-8859-13',
-    'iso8859-13':          'iso-8859-13',
-    'iso885913':           'iso-8859-13',
-    'iso-8859-14':         'iso-8859-14',
-    'iso8859-14':          'iso-8859-14',
-    'iso885914':           'iso-8859-14',
-    'csisolatin9':         'iso-8859-15',
-    'iso-8859-15':         'iso-8859-15',
-    'iso8859-15':          'iso-8859-15',
-    'iso885915':           'iso-8859-15',
-    'iso_8859-15':         'iso-8859-15',
-    'l9':                  'iso-8859-15',
-    'iso-8859-16':         'iso-8859-16',
-    'cskoi8r':             'koi8-r',
-    'koi':                 'koi8-r',
-    'koi8':                'koi8-r',
-    'koi8-r':              'koi8-r',
-    'koi8_r':              'koi8-r',
-    'koi8-u':              'koi8-u',
-    'csmacintosh':         'macintosh',
-    'mac':                 'macintosh',
-    'macintosh':           'macintosh',
-    'x-mac-roman':         'macintosh',
-    'dos-874':             'windows-874',
-    'iso-8859-11':         'windows-874',
-    'iso8859-11':          'windows-874',
-    'iso885911':           'windows-874',
-    'tis-620':             'windows-874',
-    'windows-874':         'windows-874',
-    'cp1250':              'windows-1250',
-    'windows-1250':        'windows-1250',
-    'x-cp1250':            'windows-1250',
-    'cp1251':              'windows-1251',
-    'windows-1251':        'windows-1251',
-    'x-cp1251':            'windows-1251',
-    'ansi_x3.4-1968':      'windows-1252',
-    'ascii':               'windows-1252',
-    'cp1252':              'windows-1252',
-    'cp819':               'windows-1252',
-    'csisolatin1':         'windows-1252',
-    'ibm819':              'windows-1252',
-    'iso-8859-1':          'windows-1252',
-    'iso-ir-100':          'windows-1252',
-    'iso8859-1':           'windows-1252',
-    'iso88591':            'windows-1252',
-    'iso_8859-1':          'windows-1252',
-    'iso_8859-1:1987':     'windows-1252',
-    'l1':                  'windows-1252',
-    'latin1':              'windows-1252',
-    'us-ascii':            'windows-1252',
-    'windows-1252':        'windows-1252',
-    'x-cp1252':            'windows-1252',
-    'cp1253':              'windows-1253',
-    'windows-1253':        'windows-1253',
-    'x-cp1253':            'windows-1253',
-    'cp1254':              'windows-1254',
-    'csisolatin5':         'windows-1254',
-    'iso-8859-9':          'windows-1254',
-    'iso-ir-148':          'windows-1254',
-    'iso8859-9':           'windows-1254',
-    'iso88599':            'windows-1254',
-    'iso_8859-9':          'windows-1254',
-    'iso_8859-9:1989':     'windows-1254',
-    'l5':                  'windows-1254',
-    'latin5':              'windows-1254',
-    'windows-1254':        'windows-1254',
-    'x-cp1254':            'windows-1254',
-    'cp1255':              'windows-1255',
-    'windows-1255':        'windows-1255',
-    'x-cp1255':            'windows-1255',
-    'cp1256':              'windows-1256',
-    'windows-1256':        'windows-1256',
-    'x-cp1256':            'windows-1256',
-    'cp1257':              'windows-1257',
-    'windows-1257':        'windows-1257',
-    'x-cp1257':            'windows-1257',
-    'cp1258':              'windows-1258',
-    'windows-1258':        'windows-1258',
-    'x-cp1258':            'windows-1258',
-    'x-mac-cyrillic':      'x-mac-cyrillic',
-    'x-mac-ukrainian':     'x-mac-cyrillic',
-    'chinese':             'gbk',
-    'csgb2312':            'gbk',
-    'csiso58gb231280':     'gbk',
-    'gb2312':              'gbk',
-    'gb_2312':             'gbk',
-    'gb_2312-80':          'gbk',
-    'gbk':                 'gbk',
-    'iso-ir-58':           'gbk',
-    'x-gbk':               'gbk',
-    'gb18030':             'gb18030',
-    'hz-gb-2312':          'hz-gb-2312',
-    'big5':                'big5',
-    'big5-hkscs':          'big5',
-    'cn-big5':             'big5',
-    'csbig5':              'big5',
-    'x-x-big5':            'big5',
-    'cseucpkdfmtjapanese': 'euc-jp',
-    'euc-jp':              'euc-jp',
-    'x-euc-jp':            'euc-jp',
-    'csiso2022jp':         'iso-2022-jp',
-    'iso-2022-jp':         'iso-2022-jp',
-    'csshiftjis':          'shift_jis',
-    'ms_kanji':            'shift_jis',
-    'shift-jis':           'shift_jis',
-    'shift_jis':           'shift_jis',
-    'sjis':                'shift_jis',
-    'windows-31j':         'shift_jis',
-    'x-sjis':              'shift_jis',
-    'cseuckr':             'euc-kr',
-    'csksc56011987':       'euc-kr',
-    'euc-kr':              'euc-kr',
-    'iso-ir-149':          'euc-kr',
-    'korean':              'euc-kr',
-    'ks_c_5601-1987':      'euc-kr',
-    'ks_c_5601-1989':      'euc-kr',
-    'ksc5601':             'euc-kr',
-    'ksc_5601':            'euc-kr',
-    'windows-949':         'euc-kr',
-    'csiso2022kr':         'iso-2022-kr',
-    'iso-2022-kr':         'iso-2022-kr',
-    'utf-16be':            'utf-16be',
-    'utf-16':              'utf-16le',
-    'utf-16le':            'utf-16le',
-    'x-user-defined':      'x-user-defined',
-}
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/mklabels.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/mklabels.py
deleted file mode 100644
index 295dc92..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/mklabels.py
+++ /dev/null
@@ -1,59 +0,0 @@
-"""
-
-    webencodings.mklabels
-    ~~~~~~~~~~~~~~~~~~~~~
-
-    Regenarate the webencodings.labels module.
-
-    :copyright: Copyright 2012 by Simon Sapin
-    :license: BSD, see LICENSE for details.
-
-"""
-
-import json
-try:
-    from urllib import urlopen
-except ImportError:
-    from urllib.request import urlopen
-
-
-def assert_lower(string):
-    assert string == string.lower()
-    return string
-
-
-def generate(url):
-    parts = ['''\
-"""
-
-    webencodings.labels
-    ~~~~~~~~~~~~~~~~~~~
-
-    Map encoding labels to their name.
-
-    :copyright: Copyright 2012 by Simon Sapin
-    :license: BSD, see LICENSE for details.
-
-"""
-
-# XXX Do not edit!
-# This file is automatically generated by mklabels.py
-
-LABELS = {
-''']
-    labels = [
-        (repr(assert_lower(label)).lstrip('u'),
-         repr(encoding['name']).lstrip('u'))
-        for category in json.loads(urlopen(url).read().decode('ascii'))
-        for encoding in category['encodings']
-        for label in encoding['labels']]
-    max_len = max(len(label) for label, name in labels)
-    parts.extend(
-        '    %s:%s %s,\n' % (label, ' ' * (max_len - len(label)), name)
-        for label, name in labels)
-    parts.append('}')
-    return ''.join(parts)
-
-
-if __name__ == '__main__':
-    print(generate('http://encoding.spec.whatwg.org/encodings.json'))
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/tests.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/tests.py
deleted file mode 100644
index e12c10d..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/tests.py
+++ /dev/null
@@ -1,153 +0,0 @@
-# coding: utf-8
-"""
-
-    webencodings.tests
-    ~~~~~~~~~~~~~~~~~~
-
-    A basic test suite for Encoding.
-
-    :copyright: Copyright 2012 by Simon Sapin
-    :license: BSD, see LICENSE for details.
-
-"""
-
-from __future__ import unicode_literals
-
-from . import (lookup, LABELS, decode, encode, iter_decode, iter_encode,
-               IncrementalDecoder, IncrementalEncoder, UTF8)
-
-
-def assert_raises(exception, function, *args, **kwargs):
-    try:
-        function(*args, **kwargs)
-    except exception:
-        return
-    else:  # pragma: no cover
-        raise AssertionError('Did not raise %s.' % exception)
-
-
-def test_labels():
-    assert lookup('utf-8').name == 'utf-8'
-    assert lookup('Utf-8').name == 'utf-8'
-    assert lookup('UTF-8').name == 'utf-8'
-    assert lookup('utf8').name == 'utf-8'
-    assert lookup('utf8').name == 'utf-8'
-    assert lookup('utf8 ').name == 'utf-8'
-    assert lookup(' \r\nutf8\t').name == 'utf-8'
-    assert lookup('u8') is None  # Python label.
-    assert lookup('utf-8 ') is None  # Non-ASCII white space.
-
-    assert lookup('US-ASCII').name == 'windows-1252'
-    assert lookup('iso-8859-1').name == 'windows-1252'
-    assert lookup('latin1').name == 'windows-1252'
-    assert lookup('LATIN1').name == 'windows-1252'
-    assert lookup('latin-1') is None
-    assert lookup('LATİN1') is None  # ASCII-only case insensitivity.
-
-
-def test_all_labels():
-    for label in LABELS:
-        assert decode(b'', label) == ('', lookup(label))
-        assert encode('', label) == b''
-        for repeat in [0, 1, 12]:
-            output, _ = iter_decode([b''] * repeat, label)
-            assert list(output) == []
-            assert list(iter_encode([''] * repeat, label)) == []
-        decoder = IncrementalDecoder(label)
-        assert decoder.decode(b'') == ''
-        assert decoder.decode(b'', final=True) == ''
-        encoder = IncrementalEncoder(label)
-        assert encoder.encode('') == b''
-        assert encoder.encode('', final=True) == b''
-    # All encoding names are valid labels too:
-    for name in set(LABELS.values()):
-        assert lookup(name).name == name
-
-
-def test_invalid_label():
-    assert_raises(LookupError, decode, b'\xEF\xBB\xBF\xc3\xa9', 'invalid')
-    assert_raises(LookupError, encode, 'é', 'invalid')
-    assert_raises(LookupError, iter_decode, [], 'invalid')
-    assert_raises(LookupError, iter_encode, [], 'invalid')
-    assert_raises(LookupError, IncrementalDecoder, 'invalid')
-    assert_raises(LookupError, IncrementalEncoder, 'invalid')
-
-
-def test_decode():
-    assert decode(b'\x80', 'latin1') == ('€', lookup('latin1'))
-    assert decode(b'\x80', lookup('latin1')) == ('€', lookup('latin1'))
-    assert decode(b'\xc3\xa9', 'utf8') == ('é', lookup('utf8'))
-    assert decode(b'\xc3\xa9', UTF8) == ('é', lookup('utf8'))
-    assert decode(b'\xc3\xa9', 'ascii') == ('é', lookup('ascii'))
-    assert decode(b'\xEF\xBB\xBF\xc3\xa9', 'ascii') == ('é', lookup('utf8'))  # UTF-8 with BOM
-
-    assert decode(b'\xFE\xFF\x00\xe9', 'ascii') == ('é', lookup('utf-16be'))  # UTF-16-BE with BOM
-    assert decode(b'\xFF\xFE\xe9\x00', 'ascii') == ('é', lookup('utf-16le'))  # UTF-16-LE with BOM
-    assert decode(b'\xFE\xFF\xe9\x00', 'ascii') == ('\ue900', lookup('utf-16be'))
-    assert decode(b'\xFF\xFE\x00\xe9', 'ascii') == ('\ue900', lookup('utf-16le'))
-
-    assert decode(b'\x00\xe9', 'UTF-16BE') == ('é', lookup('utf-16be'))
-    assert decode(b'\xe9\x00', 'UTF-16LE') == ('é', lookup('utf-16le'))
-    assert decode(b'\xe9\x00', 'UTF-16') == ('é', lookup('utf-16le'))
-
-    assert decode(b'\xe9\x00', 'UTF-16BE') == ('\ue900', lookup('utf-16be'))
-    assert decode(b'\x00\xe9', 'UTF-16LE') == ('\ue900', lookup('utf-16le'))
-    assert decode(b'\x00\xe9', 'UTF-16') == ('\ue900', lookup('utf-16le'))
-
-
-def test_encode():
-    assert encode('é', 'latin1') == b'\xe9'
-    assert encode('é', 'utf8') == b'\xc3\xa9'
-    assert encode('é', 'utf8') == b'\xc3\xa9'
-    assert encode('é', 'utf-16') == b'\xe9\x00'
-    assert encode('é', 'utf-16le') == b'\xe9\x00'
-    assert encode('é', 'utf-16be') == b'\x00\xe9'
-
-
-def test_iter_decode():
-    def iter_decode_to_string(input, fallback_encoding):
-        output, _encoding = iter_decode(input, fallback_encoding)
-        return ''.join(output)
-    assert iter_decode_to_string([], 'latin1') == ''
-    assert iter_decode_to_string([b''], 'latin1') == ''
-    assert iter_decode_to_string([b'\xe9'], 'latin1') == 'é'
-    assert iter_decode_to_string([b'hello'], 'latin1') == 'hello'
-    assert iter_decode_to_string([b'he', b'llo'], 'latin1') == 'hello'
-    assert iter_decode_to_string([b'hell', b'o'], 'latin1') == 'hello'
-    assert iter_decode_to_string([b'\xc3\xa9'], 'latin1') == 'é'
-    assert iter_decode_to_string([b'\xEF\xBB\xBF\xc3\xa9'], 'latin1') == 'é'
-    assert iter_decode_to_string([
-        b'\xEF\xBB\xBF', b'\xc3', b'\xa9'], 'latin1') == 'é'
-    assert iter_decode_to_string([
-        b'\xEF\xBB\xBF', b'a', b'\xc3'], 'latin1') == 'a\uFFFD'
-    assert iter_decode_to_string([
-        b'', b'\xEF', b'', b'', b'\xBB\xBF\xc3', b'\xa9'], 'latin1') == 'é'
-    assert iter_decode_to_string([b'\xEF\xBB\xBF'], 'latin1') == ''
-    assert iter_decode_to_string([b'\xEF\xBB'], 'latin1') == 'ï»'
-    assert iter_decode_to_string([b'\xFE\xFF\x00\xe9'], 'latin1') == 'é'
-    assert iter_decode_to_string([b'\xFF\xFE\xe9\x00'], 'latin1') == 'é'
-    assert iter_decode_to_string([
-        b'', b'\xFF', b'', b'', b'\xFE\xe9', b'\x00'], 'latin1') == 'é'
-    assert iter_decode_to_string([
-        b'', b'h\xe9', b'llo'], 'x-user-defined') == 'h\uF7E9llo'
-
-
-def test_iter_encode():
-    assert b''.join(iter_encode([], 'latin1')) == b''
-    assert b''.join(iter_encode([''], 'latin1')) == b''
-    assert b''.join(iter_encode(['é'], 'latin1')) == b'\xe9'
-    assert b''.join(iter_encode(['', 'é', '', ''], 'latin1')) == b'\xe9'
-    assert b''.join(iter_encode(['', 'é', '', ''], 'utf-16')) == b'\xe9\x00'
-    assert b''.join(iter_encode(['', 'é', '', ''], 'utf-16le')) == b'\xe9\x00'
-    assert b''.join(iter_encode(['', 'é', '', ''], 'utf-16be')) == b'\x00\xe9'
-    assert b''.join(iter_encode([
-        '', 'h\uF7E9', '', 'llo'], 'x-user-defined')) == b'h\xe9llo'
-
-
-def test_x_user_defined():
-    encoded = b'2,\x0c\x0b\x1aO\xd9#\xcb\x0f\xc9\xbbt\xcf\xa8\xca'
-    decoded = '2,\x0c\x0b\x1aO\uf7d9#\uf7cb\x0f\uf7c9\uf7bbt\uf7cf\uf7a8\uf7ca'
-    encoded = b'aa'
-    decoded = 'aa'
-    assert decode(encoded, 'x-user-defined') == (decoded, lookup('x-user-defined'))
-    assert encode(decoded, 'x-user-defined') == encoded
diff --git a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/x_user_defined.py b/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/x_user_defined.py
deleted file mode 100644
index d16e326..0000000
--- a/venv/Lib/site-packages/pip-19.0.3-py3.7.egg/pip/_vendor/webencodings/x_user_defined.py
+++ /dev/null
@@ -1,325 +0,0 @@
-# coding: utf-8
-"""
-
-    webencodings.x_user_defined
-    ~~~~~~~~~~~~~~~~~~~~~~~~~~~
-
-    An implementation of the x-user-defined encoding.
-
-    :copyright: Copyright 2012 by Simon Sapin
-    :license: BSD, see LICENSE for details.
-
-"""
-
-from __future__ import unicode_literals
-
-import codecs
-
-
-### Codec APIs
-
-class Codec(codecs.Codec):
-
-    def encode(self, input, errors='strict'):
-        return codecs.charmap_encode(input, errors, encoding_table)
-
-    def decode(self, input, errors='strict'):
-        return codecs.charmap_decode(input, errors, decoding_table)
-
-
-class IncrementalEncoder(codecs.IncrementalEncoder):
-    def encode(self, input, final=False):
-        return codecs.charmap_encode(input, self.errors, encoding_table)[0]
-
-
-class IncrementalDecoder(codecs.IncrementalDecoder):
-    def decode(self, input, final=False):
-        return codecs.charmap_decode(input, self.errors, decoding_table)[0]
-
-
-class StreamWriter(Codec, codecs.StreamWriter):
-    pass
-
-
-class StreamReader(Codec, codecs.StreamReader):
-    pass
-
-
-### encodings module API
-
-codec_info = codecs.CodecInfo(
-    name='x-user-defined',
-    encode=Codec().encode,
-    decode=Codec().decode,
-    incrementalencoder=IncrementalEncoder,
-    incrementaldecoder=IncrementalDecoder,
-    streamreader=StreamReader,
-    streamwriter=StreamWriter,
-)
-
-
-### Decoding Table
-
-# Python 3:
-# for c in range(256): print('    %r' % chr(c if c < 128 else c + 0xF700))
-decoding_table = (
-    '\x00'
-    '\x01'
-    '\x02'
-    '\x03'
-    '\x04'
-    '\x05'
-    '\x06'
-    '\x07'
-    '\x08'
-    '\t'
-    '\n'
-    '\x0b'
-    '\x0c'
-    '\r'
-    '\x0e'
-    '\x0f'
-    '\x10'
-    '\x11'
-    '\x12'
-    '\x13'
-    '\x14'
-    '\x15'
-    '\x16'
-    '\x17'
-    '\x18'
-    '\x19'
-    '\x1a'
-    '\x1b'
-    '\x1c'
-    '\x1d'
-    '\x1e'
-    '\x1f'
-    ' '
-    '!'
-    '"'
-    '#'
-    '$'
-    '%'
-    '&'
-    "'"
-    '('
-    ')'
-    '*'
-    '+'
-    ','
-    '-'
-    '.'
-    '/'
-    '0'
-    '1'
-    '2'
-    '3'
-    '4'
-    '5'
-    '6'
-    '7'
-    '8'
-    '9'
-    ':'
-    ';'
-    '<'
-    '='
-    '>'
-    '?'
-    '@'
-    'A'
-    'B'
-    'C'
-    'D'
-    'E'
-    'F'
-    'G'
-    'H'
-    'I'
-    'J'
-    'K'
-    'L'
-    'M'
-    'N'
-    'O'
-    'P'
-    'Q'
-    'R'
-    'S'
-    'T'
-    'U'
-    'V'
-    'W'
-    'X'
-    'Y'
-    'Z'
-    '['
-    '\\'
-    ']'
-    '^'
-    '_'
-    '`'
-    'a'
-    'b'
-    'c'
-    'd'
-    'e'
-    'f'
-    'g'
-    'h'
-    'i'
-    'j'
-    'k'
-    'l'
-    'm'
-    'n'
-    'o'
-    'p'
-    'q'
-    'r'
-    's'
-    't'
-    'u'
-    'v'
-    'w'
-    'x'
-    'y'
-    'z'
-    '{'
-    '|'
-    '}'
-    '~'
-    '\x7f'
-    '\uf780'
-    '\uf781'
-    '\uf782'
-    '\uf783'
-    '\uf784'
-    '\uf785'
-    '\uf786'
-    '\uf787'
-    '\uf788'
-    '\uf789'
-    '\uf78a'
-    '\uf78b'
-    '\uf78c'
-    '\uf78d'
-    '\uf78e'
-    '\uf78f'
-    '\uf790'
-    '\uf791'
-    '\uf792'
-    '\uf793'
-    '\uf794'
-    '\uf795'
-    '\uf796'
-    '\uf797'
-    '\uf798'
-    '\uf799'
-    '\uf79a'
-    '\uf79b'
-    '\uf79c'
-    '\uf79d'
-    '\uf79e'
-    '\uf79f'
-    '\uf7a0'
-    '\uf7a1'
-    '\uf7a2'
-    '\uf7a3'
-    '\uf7a4'
-    '\uf7a5'
-    '\uf7a6'
-    '\uf7a7'
-    '\uf7a8'
-    '\uf7a9'
-    '\uf7aa'
-    '\uf7ab'
-    '\uf7ac'
-    '\uf7ad'
-    '\uf7ae'
-    '\uf7af'
-    '\uf7b0'
-    '\uf7b1'
-    '\uf7b2'
-    '\uf7b3'
-    '\uf7b4'
-    '\uf7b5'
-    '\uf7b6'
-    '\uf7b7'
-    '\uf7b8'
-    '\uf7b9'
-    '\uf7ba'
-    '\uf7bb'
-    '\uf7bc'
-    '\uf7bd'
-    '\uf7be'
-    '\uf7bf'
-    '\uf7c0'
-    '\uf7c1'
-    '\uf7c2'
-    '\uf7c3'
-    '\uf7c4'
-    '\uf7c5'
-    '\uf7c6'
-    '\uf7c7'
-    '\uf7c8'
-    '\uf7c9'
-    '\uf7ca'
-    '\uf7cb'
-    '\uf7cc'
-    '\uf7cd'
-    '\uf7ce'
-    '\uf7cf'
-    '\uf7d0'
-    '\uf7d1'
-    '\uf7d2'
-    '\uf7d3'
-    '\uf7d4'
-    '\uf7d5'
-    '\uf7d6'
-    '\uf7d7'
-    '\uf7d8'
-    '\uf7d9'
-    '\uf7da'
-    '\uf7db'
-    '\uf7dc'
-    '\uf7dd'
-    '\uf7de'
-    '\uf7df'
-    '\uf7e0'
-    '\uf7e1'
-    '\uf7e2'
-    '\uf7e3'
-    '\uf7e4'
-    '\uf7e5'
-    '\uf7e6'
-    '\uf7e7'
-    '\uf7e8'
-    '\uf7e9'
-    '\uf7ea'
-    '\uf7eb'
-    '\uf7ec'
-    '\uf7ed'
-    '\uf7ee'
-    '\uf7ef'
-    '\uf7f0'
-    '\uf7f1'
-    '\uf7f2'
-    '\uf7f3'
-    '\uf7f4'
-    '\uf7f5'
-    '\uf7f6'
-    '\uf7f7'
-    '\uf7f8'
-    '\uf7f9'
-    '\uf7fa'
-    '\uf7fb'
-    '\uf7fc'
-    '\uf7fd'
-    '\uf7fe'
-    '\uf7ff'
-)
-
-### Encoding table
-encoding_table = codecs.charmap_build(decoding_table)
diff --git a/venv/Lib/site-packages/pylint-2.4.4.dist-info/COPYING b/venv/Lib/site-packages/pylint-2.4.4.dist-info/COPYING
deleted file mode 100644
index b7b5f53..0000000
--- a/venv/Lib/site-packages/pylint-2.4.4.dist-info/COPYING
+++ /dev/null
@@ -1,340 +0,0 @@
-		    GNU GENERAL PUBLIC LICENSE
-		       Version 2, June 1991
-
- Copyright (C) 1989, 1991 Free Software Foundation, Inc.
-	51 Franklin St, Fifth Floor, Boston, MA  02110-1301  USA
- Everyone is permitted to copy and distribute verbatim copies
- of this license document, but changing it is not allowed.
-
-			    Preamble
-
-  The licenses for most software are designed to take away your
-freedom to share and change it.  By contrast, the GNU General Public
-License is intended to guarantee your freedom to share and change free
-software--to make sure the software is free for all its users.  This
-General Public License applies to most of the Free Software
-Foundation's software and to any other program whose authors commit to
-using it.  (Some other Free Software Foundation software is covered by
-the GNU Library General Public License instead.)  You can apply it to
-your programs, too.
-
-  When we speak of free software, we are referring to freedom, not
-price.  Our General Public Licenses are designed to make sure that you
-have the freedom to distribute copies of free software (and charge for
-this service if you wish), that you receive source code or can get it
-if you want it, that you can change the software or use pieces of it
-in new free programs; and that you know you can do these things.
-
-  To protect your rights, we need to make restrictions that forbid
-anyone to deny you these rights or to ask you to surrender the rights.
-These restrictions translate to certain responsibilities for you if you
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diff --git a/venv/Lib/site-packages/pylint-2.4.4.dist-info/INSTALLER b/venv/Lib/site-packages/pylint-2.4.4.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/pylint-2.4.4.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/pylint-2.4.4.dist-info/METADATA b/venv/Lib/site-packages/pylint-2.4.4.dist-info/METADATA
deleted file mode 100644
index 993f92b..0000000
--- a/venv/Lib/site-packages/pylint-2.4.4.dist-info/METADATA
+++ /dev/null
@@ -1,202 +0,0 @@
-Metadata-Version: 2.1
-Name: pylint
-Version: 2.4.4
-Summary: python code static checker
-Home-page: https://github.com/PyCQA/pylint
-Author: Python Code Quality Authority
-Author-email: code-quality@python.org
-License: GPL
-Platform: UNKNOWN
-Classifier: Development Status :: 6 - Mature
-Classifier: Environment :: Console
-Classifier: Intended Audience :: Developers
-Classifier: License :: OSI Approved :: GNU General Public License (GPL)
-Classifier: Operating System :: OS Independent
-Classifier: Programming Language :: Python
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: 3 :: Only
-Classifier: Programming Language :: Python :: Implementation :: CPython
-Classifier: Programming Language :: Python :: Implementation :: PyPy
-Classifier: Topic :: Software Development :: Debuggers
-Classifier: Topic :: Software Development :: Quality Assurance
-Classifier: Topic :: Software Development :: Testing
-Requires-Python: >=3.5.*
-Requires-Dist: astroid (<2.4,>=2.3.0)
-Requires-Dist: isort (<5,>=4.2.5)
-Requires-Dist: mccabe (<0.7,>=0.6)
-Requires-Dist: colorama ; sys_platform=="win32"
-
-
-README for Pylint - http://pylint.pycqa.org/
-============================================
-
-.. image:: https://travis-ci.org/PyCQA/pylint.svg?branch=master
-    :target: https://travis-ci.org/PyCQA/pylint
-
-.. image:: https://ci.appveyor.com/api/projects/status/rbvwhakyj1y09atb/branch/master?svg=true
-    :alt: AppVeyor Build Status
-    :target: https://ci.appveyor.com/project/PCManticore/pylint
-
-.. image:: https://coveralls.io/repos/github/PyCQA/pylint/badge.svg?branch=master
-    :target: https://coveralls.io/github/PyCQA/pylint?branch=master
-
-
-.. image:: https://img.shields.io/pypi/v/pylint.svg
-    :alt: Pypi Package version
-    :target: https://pypi.python.org/pypi/pylint
-
-.. image:: https://readthedocs.org/projects/pylint/badge/?version=latest
-    :target: http://pylint.readthedocs.io/en/latest/?badge=latest
-    :alt: Documentation Status
-
-.. image:: https://img.shields.io/badge/code%20style-black-000000.svg
-    :target: https://github.com/ambv/black
-
-.. |tideliftlogo| image:: doc/media/Tidelift_Logos_RGB_Tidelift_Shorthand_On-White_small.png
-   :width: 75
-   :height: 60
-   :alt: Tidelift
-
-.. list-table::
-   :widths: 10 100
-
-   * - |tideliftlogo|
-     - Professional support for pylint is available as part of the `Tidelift
-       Subscription`_.  Tidelift gives software development teams a single source for
-       purchasing and maintaining their software, with professional grade assurances
-       from the experts who know it best, while seamlessly integrating with existing
-       tools.
-
-.. _Tidelift Subscription: https://tidelift.com/subscription/pkg/pypi-pylint?utm_source=pypi-pylint&utm_medium=referral&utm_campaign=readme
-
-
-======
-Pylint
-======
-
-**It's not just a linter that annoys you!**
-
-Pylint is a Python static code analysis tool which looks for programming errors,
-helps enforcing a coding standard, sniffs for code smells and offers simple refactoring
-suggestions.
-
-It's highly configurable, having special pragmas to control its errors and warnings
-from within your code, as well as from an extensive configuration file.
-It is also possible to write your own plugins for adding your own checks or for
-extending pylint in one way or another.
-
-It's a free software distributed under the GNU General Public Licence unless
-otherwise specified.
-
-Development is hosted on GitHub: https://github.com/PyCQA/pylint/
-
-You can use the code-quality@python.org mailing list to discuss about
-Pylint. Subscribe at https://mail.python.org/mailman/listinfo/code-quality/
-or read the archives at https://mail.python.org/pipermail/code-quality/
-
-Pull requests are amazing and most welcome.
-
-Install
--------
-
-Pylint can be simply installed by running::
-
-    pip install pylint
-
-If you are using Python 3.6+, upgrade to get full support for your version::
-
-    pip install pylint --upgrade
-
-If you want to install from a source distribution, extract the tarball and run
-the following command ::
-
-    python setup.py install
-
-
-Do make sure to do the same for astroid, which is used internally by pylint.
-
-For debian and rpm packages, use your usual tools according to your Linux distribution.
-
-More information about installation and available distribution format
-can be found here_.
-
-Documentation
--------------
-
-The documentation lives at http://pylint.pycqa.org/.
-
-Pylint is shipped with following additional commands:
-
-* pyreverse: an UML diagram generator
-* symilar: an independent similarities checker
-* epylint: Emacs and Flymake compatible Pylint
-
-
-Testing
--------
-
-We use tox_ for running the test suite. You should be able to install it with::
-
-    pip install tox pytest
-
-
-To run the test suite for a particular Python version, you can do::
-
-    tox -e py37
-
-
-To run individual tests with ``tox``, you can do::
-
-    tox -e py37 -- -k name_of_the_test
-
-
-We use pytest_ for testing ``pylint``, which you can use without using ``tox`` for a faster development cycle.
-
-If you want to run tests on a specific portion of the code with pytest_, (pytest-cov_) and your local python version::
-
-    # ( pip install pytest-cov )
-    # Everything:
-    python3 -m pytest tests/
-    # Everything in tests/message with coverage for the relevant code:
-    python3 -m pytest tests/message/ --cov=pylint.message
-    coverage html
-    # Only the functional test "missing_kwoa_py3":
-    python3 -m pytest "tests/test_functional.py::test_functional[missing_kwoa_py3]"
-
-
-Do not forget to clone astroid_ and install the last version::
-
-
-    git clone https://github.com/PyCQA/astroid.git
-
-    # From source
-    python3 astroid/setup.py build sdist
-    pip3 install astroid/dist/astroid*.tar.gz
-
-    # Using an editable installation
-    cd astroid
-    python3 -m pip install -e .
-
-
-For more detailed information, check the documentation.
-
-.. _here: http://pylint.pycqa.org/en/latest/user_guide/installation.html
-.. _tox: https://tox.readthedocs.io/en/latest/
-.. _pytest: https://docs.pytest.org/en/latest/
-.. _pytest-cov: https://pypi.org/project/pytest-cov/
-.. _astroid: https://github.com/PyCQA/astroid
-
-License
--------
-
-pylint is, with a few exceptions listed below, `GPLv2 <COPYING>`_.
-
-The icon files are licensed under the `CC BY-SA 4.0 <https://creativecommons.org/licenses/by-sa/4.0/>`_ license:
-
-- `doc/logo.png <doc/logo.png>`_
-- `doc/logo.svg <doc/logo.svg>`_
-
-
diff --git a/venv/Lib/site-packages/pylint-2.4.4.dist-info/RECORD b/venv/Lib/site-packages/pylint-2.4.4.dist-info/RECORD
deleted file mode 100644
index f35fd61..0000000
--- a/venv/Lib/site-packages/pylint-2.4.4.dist-info/RECORD
+++ /dev/null
@@ -1,161 +0,0 @@
-../../Scripts/epylint.exe,sha256=IVTqWxqMOvlJ9zcdZWsui4X5jbN-3_FC8R_NgS_rlXQ,102800
-../../Scripts/pylint.exe,sha256=G1_p5-RPnqvYkXT9XqTZw-dlKg5V25zz7_ESJXJDKEk,102798
-../../Scripts/pyreverse.exe,sha256=s0kRApzPy-mLHHLzDwKeCVAaEqjaHOamzyoeLGhSGIs,102804
-../../Scripts/symilar.exe,sha256=da7da6dG6_65KS3ouxsgrDbNzO4mJyVO79jt-RJrQu4,102800
-pylint-2.4.4.data/scripts/epylint,sha256=ebDphNeMoKus049k5MQbxN1JYsHUsOXZxws0Do6gCG0,51
-pylint-2.4.4.data/scripts/pylint,sha256=wXf1V2_-AB_S1uuYztSS90GiTeCkJ4eBOGEQ7CO2Nmc,53
-pylint-2.4.4.data/scripts/pyreverse,sha256=4UQf7-hfOAx6Ux8d5g0d2KIjpUPRMwFhBdsKsu0gWg0,59
-pylint-2.4.4.data/scripts/symilar,sha256=iz6DGtePyfs0haoFobDfsRsMjaFOizh7E3vsevB2Ipw,55
-pylint-2.4.4.dist-info/COPYING,sha256=w4runjyMTV1ZT_VIob4FRTAjAW1ihpMfZRLbIV7B_UI,17989
-pylint-2.4.4.dist-info/INSTALLER,sha256=zuuue4knoyJ-UwPPXg8fezS7VCrXJQrAP7zeNuwvFQg,4
-pylint-2.4.4.dist-info/METADATA,sha256=RNy4cq2r2CQ1GQdc8lt_Ds-gFkFKSR2GbllMSCa4B1c,6549
-pylint-2.4.4.dist-info/RECORD,,
-pylint-2.4.4.dist-info/WHEEL,sha256=p46_5Uhzqz6AzeSosiOnxK-zmFja1i22CrQCjmYe8ec,92
-pylint-2.4.4.dist-info/entry_points.txt,sha256=WUTwHM2ZcExO-VSvss18AMFsQL-XcWg6O3_MwobWfmw,137
-pylint-2.4.4.dist-info/top_level.txt,sha256=j6Z9i__pIuaiCka6Ul9YIy6yI5aw5QbCtldLvZlMksE,7
-pylint/__init__.py,sha256=4q6rdl1balJqnrIL-PvmRQjhUVZudPskFR_FCmyXCNI,1075
-pylint/__main__.py,sha256=8vKyCk6C5CcmdnhB7enBUDvHlzfPw3kCOg1NDMYT2f8,206
-pylint/__pkginfo__.py,sha256=DZsRD_0SjytZvXFo8vddIUj4IHkHu2u9wkslchWzPsY,3416
-pylint/__pycache__/__init__.cpython-37.pyc,,
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diff --git a/venv/Lib/site-packages/pylint-2.4.4.dist-info/WHEEL b/venv/Lib/site-packages/pylint-2.4.4.dist-info/WHEEL
deleted file mode 100644
index 3b5c403..0000000
--- a/venv/Lib/site-packages/pylint-2.4.4.dist-info/WHEEL
+++ /dev/null
@@ -1,5 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.33.6)
-Root-Is-Purelib: true
-Tag: py3-none-any
-
diff --git a/venv/Lib/site-packages/pylint-2.4.4.dist-info/entry_points.txt b/venv/Lib/site-packages/pylint-2.4.4.dist-info/entry_points.txt
deleted file mode 100644
index 063b5e4..0000000
--- a/venv/Lib/site-packages/pylint-2.4.4.dist-info/entry_points.txt
+++ /dev/null
@@ -1,6 +0,0 @@
-[console_scripts]
-epylint = pylint:run_epylint
-pylint = pylint:run_pylint
-pyreverse = pylint:run_pyreverse
-symilar = pylint:run_symilar
-
diff --git a/venv/Lib/site-packages/pylint-2.4.4.dist-info/top_level.txt b/venv/Lib/site-packages/pylint-2.4.4.dist-info/top_level.txt
deleted file mode 100644
index 7fb0ea1..0000000
--- a/venv/Lib/site-packages/pylint-2.4.4.dist-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-pylint
diff --git a/venv/Lib/site-packages/pylint/__init__.py b/venv/Lib/site-packages/pylint/__init__.py
deleted file mode 100644
index 8980938..0000000
--- a/venv/Lib/site-packages/pylint/__init__.py
+++ /dev/null
@@ -1,43 +0,0 @@
-# Copyright (c) 2008, 2012 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014, 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import sys
-
-from pylint.__pkginfo__ import version as __version__
-from pylint.checkers.similar import Run as SimilarRun
-from pylint.epylint import Run as EpylintRun
-from pylint.lint import Run as PylintRun
-from pylint.pyreverse.main import Run as PyreverseRun
-
-
-def run_pylint():
-    """run pylint"""
-
-    try:
-        PylintRun(sys.argv[1:])
-    except KeyboardInterrupt:
-        sys.exit(1)
-
-
-def run_epylint():
-    """run pylint"""
-
-    EpylintRun()
-
-
-def run_pyreverse():
-    """run pyreverse"""
-
-    PyreverseRun(sys.argv[1:])
-
-
-def run_symilar():
-    """run symilar"""
-
-    SimilarRun(sys.argv[1:])
diff --git a/venv/Lib/site-packages/pylint/__main__.py b/venv/Lib/site-packages/pylint/__main__.py
deleted file mode 100644
index e12309b..0000000
--- a/venv/Lib/site-packages/pylint/__main__.py
+++ /dev/null
@@ -1,7 +0,0 @@
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-#!/usr/bin/env python
-import pylint
-
-pylint.run_pylint()
diff --git a/venv/Lib/site-packages/pylint/__pkginfo__.py b/venv/Lib/site-packages/pylint/__pkginfo__.py
deleted file mode 100644
index 68702f4..0000000
--- a/venv/Lib/site-packages/pylint/__pkginfo__.py
+++ /dev/null
@@ -1,85 +0,0 @@
-# Copyright (c) 2006-2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Julien Jehannet <julien.jehannet@logilab.fr>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Ricardo Gemignani <ricardo.gemignani@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2016 Florian Bruhin <git@the-compiler.org>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2017-2018 Hugo <hugovk@users.noreply.github.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-# pylint: disable=redefined-builtin,invalid-name
-"""pylint packaging information"""
-
-from os.path import join
-
-# For an official release, use dev_version = None
-numversion = (2, 4, 4)
-dev_version = None
-
-version = ".".join(str(num) for num in numversion)
-if dev_version is not None:
-    version += "-dev" + str(dev_version)
-
-install_requires = ["astroid>=2.3.0,<2.4", "isort>=4.2.5,<5", "mccabe>=0.6,<0.7"]
-
-dependency_links = []  # type: ignore
-
-extras_require = {}
-extras_require[':sys_platform=="win32"'] = ["colorama"]
-
-license = "GPL"
-description = "python code static checker"
-web = "https://github.com/PyCQA/pylint"
-mailinglist = "mailto:code-quality@python.org"
-author = "Python Code Quality Authority"
-author_email = "code-quality@python.org"
-
-classifiers = [
-    "Development Status :: 6 - Mature",
-    "Environment :: Console",
-    "Intended Audience :: Developers",
-    "License :: OSI Approved :: GNU General Public License (GPL)",
-    "Operating System :: OS Independent",
-    "Programming Language :: Python",
-    "Programming Language :: Python :: 3",
-    "Programming Language :: Python :: 3.5",
-    "Programming Language :: Python :: 3.6",
-    "Programming Language :: Python :: 3.7",
-    "Programming Language :: Python :: 3 :: Only",
-    "Programming Language :: Python :: Implementation :: CPython",
-    "Programming Language :: Python :: Implementation :: PyPy",
-    "Topic :: Software Development :: Debuggers",
-    "Topic :: Software Development :: Quality Assurance",
-    "Topic :: Software Development :: Testing",
-]
-
-
-long_desc = """\
- Pylint is a Python source code analyzer which looks for programming
- errors, helps enforcing a coding standard and sniffs for some code
- smells (as defined in Martin Fowler's Refactoring book)
- .
- Pylint can be seen as another PyChecker since nearly all tests you
- can do with PyChecker can also be done with Pylint. However, Pylint
- offers some more features, like checking length of lines of code,
- checking if variable names are well-formed according to your coding
- standard, or checking if declared interfaces are truly implemented,
- and much more.
- .
- Additionally, it is possible to write plugins to add your own checks.
- .
- Pylint is shipped with "pyreverse" (UML diagram generator)
- and "symilar" (an independent similarities checker)."""
-
-scripts = [
-    join("bin", filename) for filename in ("pylint", "symilar", "epylint", "pyreverse")
-]
diff --git a/venv/Lib/site-packages/pylint/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/__pycache__/__init__.cpython-37.pyc
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index ed84248..0000000
--- a/venv/Lib/site-packages/pylint/__pycache__/lint.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/__pycache__/testutils.cpython-37.pyc b/venv/Lib/site-packages/pylint/__pycache__/testutils.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pylint/checkers/__init__.py b/venv/Lib/site-packages/pylint/checkers/__init__.py
deleted file mode 100644
index 9c6306f..0000000
--- a/venv/Lib/site-packages/pylint/checkers/__init__.py
+++ /dev/null
@@ -1,64 +0,0 @@
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2013 buck@yelp.com <buck@yelp.com>
-# Copyright (c) 2014-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2017-2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""utilities methods and classes for checkers
-
-Base id of standard checkers (used in msg and report ids):
-01: base
-02: classes
-03: format
-04: import
-05: misc
-06: variables
-07: exceptions
-08: similar
-09: design_analysis
-10: newstyle
-11: typecheck
-12: logging
-13: string_format
-14: string_constant
-15: stdlib
-16: python3
-17: refactoring
-18-50: not yet used: reserved for future internal checkers.
-51-99: perhaps used: reserved for external checkers
-
-The raw_metrics checker has no number associated since it doesn't emit any
-messages nor reports. XXX not true, emit a 07 report !
-
-"""
-
-from pylint.checkers.base_checker import BaseChecker, BaseTokenChecker
-from pylint.utils import register_plugins
-
-
-def table_lines_from_stats(stats, _, columns):
-    """get values listed in <columns> from <stats> and <old_stats>,
-    and return a formated list of values, designed to be given to a
-    ureport.Table object
-    """
-    lines = []
-    for m_type in columns:
-        new = stats[m_type]
-        new = "%.3f" % new if isinstance(new, float) else str(new)
-        lines += (m_type.replace("_", " "), new, "NC", "NC")
-    return lines
-
-
-def initialize(linter):
-    """initialize linter with checkers in this package """
-    register_plugins(linter, __path__[0])
-
-
-__all__ = ("BaseChecker", "BaseTokenChecker", "initialize")
diff --git a/venv/Lib/site-packages/pylint/checkers/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/checkers/__pycache__/__init__.cpython-37.pyc
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diff --git a/venv/Lib/site-packages/pylint/checkers/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/pylint/checkers/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index 90e8ff1..0000000
--- a/venv/Lib/site-packages/pylint/checkers/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/checkers/__pycache__/variables.cpython-37.pyc b/venv/Lib/site-packages/pylint/checkers/__pycache__/variables.cpython-37.pyc
deleted file mode 100644
index 943ffbd..0000000
--- a/venv/Lib/site-packages/pylint/checkers/__pycache__/variables.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/checkers/async.py b/venv/Lib/site-packages/pylint/checkers/async.py
deleted file mode 100644
index c33071e..0000000
--- a/venv/Lib/site-packages/pylint/checkers/async.py
+++ /dev/null
@@ -1,89 +0,0 @@
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2017 Derek Gustafson <degustaf@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Checker for anything related to the async protocol (PEP 492)."""
-
-import sys
-
-import astroid
-from astroid import bases, exceptions
-
-from pylint import checkers, interfaces, utils
-from pylint.checkers import utils as checker_utils
-from pylint.checkers.utils import decorated_with
-
-
-class AsyncChecker(checkers.BaseChecker):
-    __implements__ = interfaces.IAstroidChecker
-    name = "async"
-    msgs = {
-        "E1700": (
-            "Yield inside async function",
-            "yield-inside-async-function",
-            "Used when an `yield` or `yield from` statement is "
-            "found inside an async function.",
-            {"minversion": (3, 5)},
-        ),
-        "E1701": (
-            "Async context manager '%s' doesn't implement __aenter__ and __aexit__.",
-            "not-async-context-manager",
-            "Used when an async context manager is used with an object "
-            "that does not implement the async context management protocol.",
-            {"minversion": (3, 5)},
-        ),
-    }
-
-    def open(self):
-        self._ignore_mixin_members = utils.get_global_option(
-            self, "ignore-mixin-members"
-        )
-        self._async_generators = ["contextlib.asynccontextmanager"]
-
-    @checker_utils.check_messages("yield-inside-async-function")
-    def visit_asyncfunctiondef(self, node):
-        for child in node.nodes_of_class(astroid.Yield):
-            if child.scope() is node and (
-                sys.version_info[:2] == (3, 5) or isinstance(child, astroid.YieldFrom)
-            ):
-                self.add_message("yield-inside-async-function", node=child)
-
-    @checker_utils.check_messages("not-async-context-manager")
-    def visit_asyncwith(self, node):
-        for ctx_mgr, _ in node.items:
-            inferred = checker_utils.safe_infer(ctx_mgr)
-            if inferred is None or inferred is astroid.Uninferable:
-                continue
-
-            if isinstance(inferred, bases.AsyncGenerator):
-                # Check if we are dealing with a function decorated
-                # with contextlib.asynccontextmanager.
-                if decorated_with(inferred.parent, self._async_generators):
-                    continue
-            else:
-                try:
-                    inferred.getattr("__aenter__")
-                    inferred.getattr("__aexit__")
-                except exceptions.NotFoundError:
-                    if isinstance(inferred, astroid.Instance):
-                        # If we do not know the bases of this class,
-                        # just skip it.
-                        if not checker_utils.has_known_bases(inferred):
-                            continue
-                        # Just ignore mixin classes.
-                        if self._ignore_mixin_members:
-                            if inferred.name[-5:].lower() == "mixin":
-                                continue
-                else:
-                    continue
-
-            self.add_message(
-                "not-async-context-manager", node=node, args=(inferred.name,)
-            )
-
-
-def register(linter):
-    """required method to auto register this checker"""
-    linter.register_checker(AsyncChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/base.py b/venv/Lib/site-packages/pylint/checkers/base.py
deleted file mode 100644
index c94676e..0000000
--- a/venv/Lib/site-packages/pylint/checkers/base.py
+++ /dev/null
@@ -1,2333 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2016 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Nick Bastin <nick.bastin@gmail.com>
-# Copyright (c) 2015 Michael Kefeder <oss@multiwave.ch>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2015 Stephane Wirtel <stephane@wirtel.be>
-# Copyright (c) 2015 Cosmin Poieana <cmin@ropython.org>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Radu Ciorba <radu@devrandom.ro>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016, 2018 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016-2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2016 Elias Dorneles <eliasdorneles@gmail.com>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016 Yannack <yannack@users.noreply.github.com>
-# Copyright (c) 2016 Alex Jurkiewicz <alex@jurkiewi.cz>
-# Copyright (c) 2017 Jacques Kvam <jwkvam@gmail.com>
-# Copyright (c) 2017 ttenhoeve-aa <ttenhoeve@appannie.com>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Steven M. Vascellaro <svascellaro@gmail.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Chris Lamb <chris@chris-lamb.co.uk>
-# Copyright (c) 2018 glmdgrielson <32415403+glmdgrielson@users.noreply.github.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""basic checker for Python code"""
-
-import builtins
-import collections
-import itertools
-import re
-import sys
-from typing import Pattern
-
-import astroid
-import astroid.bases
-import astroid.scoped_nodes
-from astroid.arguments import CallSite
-
-import pylint.utils as lint_utils
-from pylint import checkers, exceptions, interfaces
-from pylint.checkers import utils
-from pylint.checkers.utils import is_property_setter_or_deleter
-from pylint.reporters.ureports import nodes as reporter_nodes
-
-
-class NamingStyle:
-    # It may seem counterintuitive that single naming style
-    # has multiple "accepted" forms of regular expressions,
-    # but we need to special-case stuff like dunder names
-    # in method names.
-    CLASS_NAME_RGX = None  # type: Pattern[str]
-    MOD_NAME_RGX = None  # type: Pattern[str]
-    CONST_NAME_RGX = None  # type: Pattern[str]
-    COMP_VAR_RGX = None  # type: Pattern[str]
-    DEFAULT_NAME_RGX = None  # type: Pattern[str]
-    CLASS_ATTRIBUTE_RGX = None  # type: Pattern[str]
-
-    @classmethod
-    def get_regex(cls, name_type):
-        return {
-            "module": cls.MOD_NAME_RGX,
-            "const": cls.CONST_NAME_RGX,
-            "class": cls.CLASS_NAME_RGX,
-            "function": cls.DEFAULT_NAME_RGX,
-            "method": cls.DEFAULT_NAME_RGX,
-            "attr": cls.DEFAULT_NAME_RGX,
-            "argument": cls.DEFAULT_NAME_RGX,
-            "variable": cls.DEFAULT_NAME_RGX,
-            "class_attribute": cls.CLASS_ATTRIBUTE_RGX,
-            "inlinevar": cls.COMP_VAR_RGX,
-        }[name_type]
-
-
-class SnakeCaseStyle(NamingStyle):
-    """Regex rules for snake_case naming style."""
-
-    CLASS_NAME_RGX = re.compile("[a-z_][a-z0-9_]+$")
-    MOD_NAME_RGX = re.compile("([a-z_][a-z0-9_]*)$")
-    CONST_NAME_RGX = re.compile("(([a-z_][a-z0-9_]*)|(__.*__))$")
-    COMP_VAR_RGX = re.compile("[a-z_][a-z0-9_]*$")
-    DEFAULT_NAME_RGX = re.compile(
-        "(([a-z_][a-z0-9_]{2,})|(_[a-z0-9_]*)|(__[a-z][a-z0-9_]+__))$"
-    )
-    CLASS_ATTRIBUTE_RGX = re.compile(r"(([a-z_][a-z0-9_]{2,}|(__.*__)))$")
-
-
-class CamelCaseStyle(NamingStyle):
-    """Regex rules for camelCase naming style."""
-
-    CLASS_NAME_RGX = re.compile("[a-z_][a-zA-Z0-9]+$")
-    MOD_NAME_RGX = re.compile("([a-z_][a-zA-Z0-9]*)$")
-    CONST_NAME_RGX = re.compile("(([a-z_][A-Za-z0-9]*)|(__.*__))$")
-    COMP_VAR_RGX = re.compile("[a-z_][A-Za-z0-9]*$")
-    DEFAULT_NAME_RGX = re.compile("(([a-z_][a-zA-Z0-9]{2,})|(__[a-z][a-zA-Z0-9_]+__))$")
-    CLASS_ATTRIBUTE_RGX = re.compile(r"([a-z_][A-Za-z0-9]{2,}|(__.*__))$")
-
-
-class PascalCaseStyle(NamingStyle):
-    """Regex rules for PascalCase naming style."""
-
-    CLASS_NAME_RGX = re.compile("[A-Z_][a-zA-Z0-9]+$")
-    MOD_NAME_RGX = re.compile("[A-Z_][a-zA-Z0-9]+$")
-    CONST_NAME_RGX = re.compile("(([A-Z_][A-Za-z0-9]*)|(__.*__))$")
-    COMP_VAR_RGX = re.compile("[A-Z_][a-zA-Z0-9]+$")
-    DEFAULT_NAME_RGX = re.compile("[A-Z_][a-zA-Z0-9]{2,}$|(__[a-z][a-zA-Z0-9_]+__)$")
-    CLASS_ATTRIBUTE_RGX = re.compile("[A-Z_][a-zA-Z0-9]{2,}$")
-
-
-class UpperCaseStyle(NamingStyle):
-    """Regex rules for UPPER_CASE naming style."""
-
-    CLASS_NAME_RGX = re.compile("[A-Z_][A-Z0-9_]+$")
-    MOD_NAME_RGX = re.compile("[A-Z_][A-Z0-9_]+$")
-    CONST_NAME_RGX = re.compile("(([A-Z_][A-Z0-9_]*)|(__.*__))$")
-    COMP_VAR_RGX = re.compile("[A-Z_][A-Z0-9_]+$")
-    DEFAULT_NAME_RGX = re.compile("([A-Z_][A-Z0-9_]{2,})|(__[a-z][a-zA-Z0-9_]+__)$")
-    CLASS_ATTRIBUTE_RGX = re.compile("[A-Z_][A-Z0-9_]{2,}$")
-
-
-class AnyStyle(NamingStyle):
-    @classmethod
-    def get_regex(cls, name_type):
-        return re.compile(".*")
-
-
-NAMING_STYLES = {
-    "snake_case": SnakeCaseStyle,
-    "camelCase": CamelCaseStyle,
-    "PascalCase": PascalCaseStyle,
-    "UPPER_CASE": UpperCaseStyle,
-    "any": AnyStyle,
-}
-
-# do not require a doc string on private/system methods
-NO_REQUIRED_DOC_RGX = re.compile("^_")
-REVERSED_PROTOCOL_METHOD = "__reversed__"
-SEQUENCE_PROTOCOL_METHODS = ("__getitem__", "__len__")
-REVERSED_METHODS = (SEQUENCE_PROTOCOL_METHODS, (REVERSED_PROTOCOL_METHOD,))
-TYPECHECK_COMPARISON_OPERATORS = frozenset(("is", "is not", "==", "!=", "in", "not in"))
-LITERAL_NODE_TYPES = (astroid.Const, astroid.Dict, astroid.List, astroid.Set)
-UNITTEST_CASE = "unittest.case"
-BUILTINS = builtins.__name__
-TYPE_QNAME = "%s.type" % BUILTINS
-ABC_METACLASSES = {"_py_abc.ABCMeta", "abc.ABCMeta"}  # Python 3.7+,
-
-# Name categories that are always consistent with all naming conventions.
-EXEMPT_NAME_CATEGORIES = {"exempt", "ignore"}
-
-# A mapping from builtin-qname -> symbol, to be used when generating messages
-# about dangerous default values as arguments
-DEFAULT_ARGUMENT_SYMBOLS = dict(
-    zip(
-        [".".join([BUILTINS, x]) for x in ("set", "dict", "list")],
-        ["set()", "{}", "[]"],
-    )
-)
-REVERSED_COMPS = {"<": ">", "<=": ">=", ">": "<", ">=": "<="}
-COMPARISON_OPERATORS = frozenset(("==", "!=", "<", ">", "<=", ">="))
-# List of methods which can be redefined
-REDEFINABLE_METHODS = frozenset(("__module__",))
-TYPING_FORWARD_REF_QNAME = "typing.ForwardRef"
-
-
-def _redefines_import(node):
-    """ Detect that the given node (AssignName) is inside an
-    exception handler and redefines an import from the tryexcept body.
-    Returns True if the node redefines an import, False otherwise.
-    """
-    current = node
-    while current and not isinstance(current.parent, astroid.ExceptHandler):
-        current = current.parent
-    if not current or not utils.error_of_type(current.parent, ImportError):
-        return False
-    try_block = current.parent.parent
-    for import_node in try_block.nodes_of_class((astroid.ImportFrom, astroid.Import)):
-        for name, alias in import_node.names:
-            if alias:
-                if alias == node.name:
-                    return True
-            elif name == node.name:
-                return True
-    return False
-
-
-def in_loop(node):
-    """return True if the node is inside a kind of for loop"""
-    parent = node.parent
-    while parent is not None:
-        if isinstance(
-            parent,
-            (
-                astroid.For,
-                astroid.ListComp,
-                astroid.SetComp,
-                astroid.DictComp,
-                astroid.GeneratorExp,
-            ),
-        ):
-            return True
-        parent = parent.parent
-    return False
-
-
-def in_nested_list(nested_list, obj):
-    """return true if the object is an element of <nested_list> or of a nested
-    list
-    """
-    for elmt in nested_list:
-        if isinstance(elmt, (list, tuple)):
-            if in_nested_list(elmt, obj):
-                return True
-        elif elmt == obj:
-            return True
-    return False
-
-
-def _get_break_loop_node(break_node):
-    """
-    Returns the loop node that holds the break node in arguments.
-
-    Args:
-        break_node (astroid.Break): the break node of interest.
-
-    Returns:
-        astroid.For or astroid.While: the loop node holding the break node.
-    """
-    loop_nodes = (astroid.For, astroid.While)
-    parent = break_node.parent
-    while not isinstance(parent, loop_nodes) or break_node in getattr(
-        parent, "orelse", []
-    ):
-        break_node = parent
-        parent = parent.parent
-        if parent is None:
-            break
-    return parent
-
-
-def _loop_exits_early(loop):
-    """
-    Returns true if a loop may ends up in a break statement.
-
-    Args:
-        loop (astroid.For, astroid.While): the loop node inspected.
-
-    Returns:
-        bool: True if the loop may ends up in a break statement, False otherwise.
-    """
-    loop_nodes = (astroid.For, astroid.While)
-    definition_nodes = (astroid.FunctionDef, astroid.ClassDef)
-    inner_loop_nodes = [
-        _node
-        for _node in loop.nodes_of_class(loop_nodes, skip_klass=definition_nodes)
-        if _node != loop
-    ]
-    return any(
-        _node
-        for _node in loop.nodes_of_class(astroid.Break, skip_klass=definition_nodes)
-        if _get_break_loop_node(_node) not in inner_loop_nodes
-    )
-
-
-def _is_multi_naming_match(match, node_type, confidence):
-    return (
-        match is not None
-        and match.lastgroup is not None
-        and match.lastgroup not in EXEMPT_NAME_CATEGORIES
-        and (node_type != "method" or confidence != interfaces.INFERENCE_FAILURE)
-    )
-
-
-BUILTIN_PROPERTY = "builtins.property"
-
-
-def _get_properties(config):
-    """Returns a tuple of property classes and names.
-
-    Property classes are fully qualified, such as 'abc.abstractproperty' and
-    property names are the actual names, such as 'abstract_property'.
-    """
-    property_classes = {BUILTIN_PROPERTY}
-    property_names = set()  # Not returning 'property', it has its own check.
-    if config is not None:
-        property_classes.update(config.property_classes)
-        property_names.update(
-            (prop.rsplit(".", 1)[-1] for prop in config.property_classes)
-        )
-    return property_classes, property_names
-
-
-def _determine_function_name_type(node, config=None):
-    """Determine the name type whose regex the a function's name should match.
-
-    :param node: A function node.
-    :type node: astroid.node_classes.NodeNG
-    :param config: Configuration from which to pull additional property classes.
-    :type config: :class:`optparse.Values`
-
-    :returns: One of ('function', 'method', 'attr')
-    :rtype: str
-    """
-    property_classes, property_names = _get_properties(config)
-    if not node.is_method():
-        return "function"
-
-    if is_property_setter_or_deleter(node):
-        # If the function is decorated using the prop_method.{setter,getter}
-        # form, treat it like an attribute as well.
-        return "attr"
-
-    if node.decorators:
-        decorators = node.decorators.nodes
-    else:
-        decorators = []
-    for decorator in decorators:
-        # If the function is a property (decorated with @property
-        # or @abc.abstractproperty), the name type is 'attr'.
-        if isinstance(decorator, astroid.Name) or (
-            isinstance(decorator, astroid.Attribute)
-            and decorator.attrname in property_names
-        ):
-            inferred = utils.safe_infer(decorator)
-            if inferred and inferred.qname() in property_classes:
-                return "attr"
-    return "method"
-
-
-def _has_abstract_methods(node):
-    """
-    Determine if the given `node` has abstract methods.
-
-    The methods should be made abstract by decorating them
-    with `abc` decorators.
-    """
-    return len(utils.unimplemented_abstract_methods(node)) > 0
-
-
-def report_by_type_stats(sect, stats, _):
-    """make a report of
-
-    * percentage of different types documented
-    * percentage of different types with a bad name
-    """
-    # percentage of different types documented and/or with a bad name
-    nice_stats = {}
-    for node_type in ("module", "class", "method", "function"):
-        try:
-            total = stats[node_type]
-        except KeyError:
-            raise exceptions.EmptyReportError()
-        nice_stats[node_type] = {}
-        if total != 0:
-            try:
-                documented = total - stats["undocumented_" + node_type]
-                percent = (documented * 100.0) / total
-                nice_stats[node_type]["percent_documented"] = "%.2f" % percent
-            except KeyError:
-                nice_stats[node_type]["percent_documented"] = "NC"
-            try:
-                percent = (stats["badname_" + node_type] * 100.0) / total
-                nice_stats[node_type]["percent_badname"] = "%.2f" % percent
-            except KeyError:
-                nice_stats[node_type]["percent_badname"] = "NC"
-    lines = ("type", "number", "old number", "difference", "%documented", "%badname")
-    for node_type in ("module", "class", "method", "function"):
-        new = stats[node_type]
-        lines += (
-            node_type,
-            str(new),
-            "NC",
-            "NC",
-            nice_stats[node_type].get("percent_documented", "0"),
-            nice_stats[node_type].get("percent_badname", "0"),
-        )
-    sect.append(reporter_nodes.Table(children=lines, cols=6, rheaders=1))
-
-
-def redefined_by_decorator(node):
-    """return True if the object is a method redefined via decorator.
-
-    For example:
-        @property
-        def x(self): return self._x
-        @x.setter
-        def x(self, value): self._x = value
-    """
-    if node.decorators:
-        for decorator in node.decorators.nodes:
-            if (
-                isinstance(decorator, astroid.Attribute)
-                and getattr(decorator.expr, "name", None) == node.name
-            ):
-                return True
-    return False
-
-
-class _BasicChecker(checkers.BaseChecker):
-    __implements__ = interfaces.IAstroidChecker
-    name = "basic"
-
-
-class BasicErrorChecker(_BasicChecker):
-    msgs = {
-        "E0100": (
-            "__init__ method is a generator",
-            "init-is-generator",
-            "Used when the special class method __init__ is turned into a "
-            "generator by a yield in its body.",
-        ),
-        "E0101": (
-            "Explicit return in __init__",
-            "return-in-init",
-            "Used when the special class method __init__ has an explicit "
-            "return value.",
-        ),
-        "E0102": (
-            "%s already defined line %s",
-            "function-redefined",
-            "Used when a function / class / method is redefined.",
-        ),
-        "E0103": (
-            "%r not properly in loop",
-            "not-in-loop",
-            "Used when break or continue keywords are used outside a loop.",
-        ),
-        "E0104": (
-            "Return outside function",
-            "return-outside-function",
-            'Used when a "return" statement is found outside a function or method.',
-        ),
-        "E0105": (
-            "Yield outside function",
-            "yield-outside-function",
-            'Used when a "yield" statement is found outside a function or method.',
-        ),
-        "E0106": (
-            "Return with argument inside generator",
-            "return-arg-in-generator",
-            'Used when a "return" statement with an argument is found '
-            "outside in a generator function or method (e.g. with some "
-            '"yield" statements).',
-            {"maxversion": (3, 3)},
-        ),
-        "E0107": (
-            "Use of the non-existent %s operator",
-            "nonexistent-operator",
-            "Used when you attempt to use the C-style pre-increment or "
-            "pre-decrement operator -- and ++, which doesn't exist in Python.",
-        ),
-        "E0108": (
-            "Duplicate argument name %s in function definition",
-            "duplicate-argument-name",
-            "Duplicate argument names in function definitions are syntax errors.",
-        ),
-        "E0110": (
-            "Abstract class %r with abstract methods instantiated",
-            "abstract-class-instantiated",
-            "Used when an abstract class with `abc.ABCMeta` as metaclass "
-            "has abstract methods and is instantiated.",
-        ),
-        "W0120": (
-            "Else clause on loop without a break statement",
-            "useless-else-on-loop",
-            "Loops should only have an else clause if they can exit early "
-            "with a break statement, otherwise the statements under else "
-            "should be on the same scope as the loop itself.",
-        ),
-        "E0112": (
-            "More than one starred expression in assignment",
-            "too-many-star-expressions",
-            "Emitted when there are more than one starred "
-            "expressions (`*x`) in an assignment. This is a SyntaxError.",
-        ),
-        "E0113": (
-            "Starred assignment target must be in a list or tuple",
-            "invalid-star-assignment-target",
-            "Emitted when a star expression is used as a starred assignment target.",
-        ),
-        "E0114": (
-            "Can use starred expression only in assignment target",
-            "star-needs-assignment-target",
-            "Emitted when a star expression is not used in an assignment target.",
-        ),
-        "E0115": (
-            "Name %r is nonlocal and global",
-            "nonlocal-and-global",
-            "Emitted when a name is both nonlocal and global.",
-        ),
-        "E0116": (
-            "'continue' not supported inside 'finally' clause",
-            "continue-in-finally",
-            "Emitted when the `continue` keyword is found "
-            "inside a finally clause, which is a SyntaxError.",
-        ),
-        "E0117": (
-            "nonlocal name %s found without binding",
-            "nonlocal-without-binding",
-            "Emitted when a nonlocal variable does not have an attached "
-            "name somewhere in the parent scopes",
-        ),
-        "E0118": (
-            "Name %r is used prior to global declaration",
-            "used-prior-global-declaration",
-            "Emitted when a name is used prior a global declaration, "
-            "which results in an error since Python 3.6.",
-            {"minversion": (3, 6)},
-        ),
-    }
-
-    @utils.check_messages("function-redefined")
-    def visit_classdef(self, node):
-        self._check_redefinition("class", node)
-
-    def _too_many_starred_for_tuple(self, assign_tuple):
-        starred_count = 0
-        for elem in assign_tuple.itered():
-            if isinstance(elem, astroid.Tuple):
-                return self._too_many_starred_for_tuple(elem)
-            if isinstance(elem, astroid.Starred):
-                starred_count += 1
-        return starred_count > 1
-
-    @utils.check_messages("too-many-star-expressions", "invalid-star-assignment-target")
-    def visit_assign(self, node):
-        # Check *a, *b = ...
-        assign_target = node.targets[0]
-        # Check *a = b
-        if isinstance(node.targets[0], astroid.Starred):
-            self.add_message("invalid-star-assignment-target", node=node)
-
-        if not isinstance(assign_target, astroid.Tuple):
-            return
-        if self._too_many_starred_for_tuple(assign_target):
-            self.add_message("too-many-star-expressions", node=node)
-
-    @utils.check_messages("star-needs-assignment-target")
-    def visit_starred(self, node):
-        """Check that a Starred expression is used in an assignment target."""
-        if isinstance(node.parent, astroid.Call):
-            # f(*args) is converted to Call(args=[Starred]), so ignore
-            # them for this check.
-            return
-        if isinstance(
-            node.parent, (astroid.List, astroid.Tuple, astroid.Set, astroid.Dict)
-        ):
-            # PEP 448 unpacking.
-            return
-
-        stmt = node.statement()
-        if not isinstance(stmt, astroid.Assign):
-            return
-
-        if stmt.value is node or stmt.value.parent_of(node):
-            self.add_message("star-needs-assignment-target", node=node)
-
-    @utils.check_messages(
-        "init-is-generator",
-        "return-in-init",
-        "function-redefined",
-        "return-arg-in-generator",
-        "duplicate-argument-name",
-        "nonlocal-and-global",
-        "used-prior-global-declaration",
-    )
-    def visit_functiondef(self, node):
-        self._check_nonlocal_and_global(node)
-        self._check_name_used_prior_global(node)
-        if not redefined_by_decorator(
-            node
-        ) and not utils.is_registered_in_singledispatch_function(node):
-            self._check_redefinition(node.is_method() and "method" or "function", node)
-        # checks for max returns, branch, return in __init__
-        returns = node.nodes_of_class(
-            astroid.Return, skip_klass=(astroid.FunctionDef, astroid.ClassDef)
-        )
-        if node.is_method() and node.name == "__init__":
-            if node.is_generator():
-                self.add_message("init-is-generator", node=node)
-            else:
-                values = [r.value for r in returns]
-                # Are we returning anything but None from constructors
-                if any(v for v in values if not utils.is_none(v)):
-                    self.add_message("return-in-init", node=node)
-        # Check for duplicate names by clustering args with same name for detailed report
-        arg_clusters = collections.defaultdict(list)
-        arguments = filter(None, [node.args.args, node.args.kwonlyargs])
-
-        for arg in itertools.chain.from_iterable(arguments):
-            arg_clusters[arg.name].append(arg)
-
-        # provide detailed report about each repeated argument
-        for argument_duplicates in arg_clusters.values():
-            if len(argument_duplicates) != 1:
-                for argument in argument_duplicates:
-                    self.add_message(
-                        "duplicate-argument-name",
-                        line=argument.lineno,
-                        node=argument,
-                        args=(argument.name,),
-                    )
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    def _check_name_used_prior_global(self, node):
-
-        scope_globals = {
-            name: child
-            for child in node.nodes_of_class(astroid.Global)
-            for name in child.names
-            if child.scope() is node
-        }
-
-        if not scope_globals:
-            return
-
-        for node_name in node.nodes_of_class(astroid.Name):
-            if node_name.scope() is not node:
-                continue
-
-            name = node_name.name
-            corresponding_global = scope_globals.get(name)
-            if not corresponding_global:
-                continue
-
-            global_lineno = corresponding_global.fromlineno
-            if global_lineno and global_lineno > node_name.fromlineno:
-                self.add_message(
-                    "used-prior-global-declaration", node=node_name, args=(name,)
-                )
-
-    def _check_nonlocal_and_global(self, node):
-        """Check that a name is both nonlocal and global."""
-
-        def same_scope(current):
-            return current.scope() is node
-
-        from_iter = itertools.chain.from_iterable
-        nonlocals = set(
-            from_iter(
-                child.names
-                for child in node.nodes_of_class(astroid.Nonlocal)
-                if same_scope(child)
-            )
-        )
-
-        if not nonlocals:
-            return
-
-        global_vars = set(
-            from_iter(
-                child.names
-                for child in node.nodes_of_class(astroid.Global)
-                if same_scope(child)
-            )
-        )
-        for name in nonlocals.intersection(global_vars):
-            self.add_message("nonlocal-and-global", args=(name,), node=node)
-
-    @utils.check_messages("return-outside-function")
-    def visit_return(self, node):
-        if not isinstance(node.frame(), astroid.FunctionDef):
-            self.add_message("return-outside-function", node=node)
-
-    @utils.check_messages("yield-outside-function")
-    def visit_yield(self, node):
-        self._check_yield_outside_func(node)
-
-    @utils.check_messages("yield-outside-function")
-    def visit_yieldfrom(self, node):
-        self._check_yield_outside_func(node)
-
-    @utils.check_messages("not-in-loop", "continue-in-finally")
-    def visit_continue(self, node):
-        self._check_in_loop(node, "continue")
-
-    @utils.check_messages("not-in-loop")
-    def visit_break(self, node):
-        self._check_in_loop(node, "break")
-
-    @utils.check_messages("useless-else-on-loop")
-    def visit_for(self, node):
-        self._check_else_on_loop(node)
-
-    @utils.check_messages("useless-else-on-loop")
-    def visit_while(self, node):
-        self._check_else_on_loop(node)
-
-    @utils.check_messages("nonexistent-operator")
-    def visit_unaryop(self, node):
-        """check use of the non-existent ++ and -- operator operator"""
-        if (
-            (node.op in "+-")
-            and isinstance(node.operand, astroid.UnaryOp)
-            and (node.operand.op == node.op)
-        ):
-            self.add_message("nonexistent-operator", node=node, args=node.op * 2)
-
-    def _check_nonlocal_without_binding(self, node, name):
-        current_scope = node.scope()
-        while True:
-            if current_scope.parent is None:
-                break
-
-            if not isinstance(current_scope, (astroid.ClassDef, astroid.FunctionDef)):
-                self.add_message("nonlocal-without-binding", args=(name,), node=node)
-                return
-
-            if name not in current_scope.locals:
-                current_scope = current_scope.parent.scope()
-                continue
-
-            # Okay, found it.
-            return
-
-        if not isinstance(current_scope, astroid.FunctionDef):
-            self.add_message("nonlocal-without-binding", args=(name,), node=node)
-
-    @utils.check_messages("nonlocal-without-binding")
-    def visit_nonlocal(self, node):
-        for name in node.names:
-            self._check_nonlocal_without_binding(node, name)
-
-    @utils.check_messages("abstract-class-instantiated")
-    def visit_call(self, node):
-        """ Check instantiating abstract class with
-        abc.ABCMeta as metaclass.
-        """
-        try:
-            for inferred in node.func.infer():
-                self._check_inferred_class_is_abstract(inferred, node)
-        except astroid.InferenceError:
-            return
-
-    def _check_inferred_class_is_abstract(self, inferred, node):
-        if not isinstance(inferred, astroid.ClassDef):
-            return
-
-        klass = utils.node_frame_class(node)
-        if klass is inferred:
-            # Don't emit the warning if the class is instantiated
-            # in its own body or if the call is not an instance
-            # creation. If the class is instantiated into its own
-            # body, we're expecting that it knows what it is doing.
-            return
-
-        # __init__ was called
-        abstract_methods = _has_abstract_methods(inferred)
-
-        if not abstract_methods:
-            return
-
-        metaclass = inferred.metaclass()
-
-        if metaclass is None:
-            # Python 3.4 has `abc.ABC`, which won't be detected
-            # by ClassNode.metaclass()
-            for ancestor in inferred.ancestors():
-                if ancestor.qname() == "abc.ABC":
-                    self.add_message(
-                        "abstract-class-instantiated", args=(inferred.name,), node=node
-                    )
-                    break
-
-            return
-
-        if metaclass.qname() in ABC_METACLASSES:
-            self.add_message(
-                "abstract-class-instantiated", args=(inferred.name,), node=node
-            )
-
-    def _check_yield_outside_func(self, node):
-        if not isinstance(node.frame(), (astroid.FunctionDef, astroid.Lambda)):
-            self.add_message("yield-outside-function", node=node)
-
-    def _check_else_on_loop(self, node):
-        """Check that any loop with an else clause has a break statement."""
-        if node.orelse and not _loop_exits_early(node):
-            self.add_message(
-                "useless-else-on-loop",
-                node=node,
-                # This is not optimal, but the line previous
-                # to the first statement in the else clause
-                # will usually be the one that contains the else:.
-                line=node.orelse[0].lineno - 1,
-            )
-
-    def _check_in_loop(self, node, node_name):
-        """check that a node is inside a for or while loop"""
-        _node = node.parent
-        while _node:
-            if isinstance(_node, (astroid.For, astroid.While)):
-                if node not in _node.orelse:
-                    return
-
-            if isinstance(_node, (astroid.ClassDef, astroid.FunctionDef)):
-                break
-            if (
-                isinstance(_node, astroid.TryFinally)
-                and node in _node.finalbody
-                and isinstance(node, astroid.Continue)
-            ):
-                self.add_message("continue-in-finally", node=node)
-
-            _node = _node.parent
-
-        self.add_message("not-in-loop", node=node, args=node_name)
-
-    def _check_redefinition(self, redeftype, node):
-        """check for redefinition of a function / method / class name"""
-        parent_frame = node.parent.frame()
-
-        # Ignore function stubs created for type information
-        redefinitions = parent_frame.locals[node.name]
-        defined_self = next(
-            (local for local in redefinitions if not utils.is_overload_stub(local)),
-            node,
-        )
-        if defined_self is not node and not astroid.are_exclusive(node, defined_self):
-
-            # Additional checks for methods which are not considered
-            # redefined, since they are already part of the base API.
-            if (
-                isinstance(parent_frame, astroid.ClassDef)
-                and node.name in REDEFINABLE_METHODS
-            ):
-                return
-
-            if utils.is_overload_stub(node):
-                return
-
-            # Check if we have forward references for this node.
-            try:
-                redefinition_index = redefinitions.index(node)
-            except ValueError:
-                pass
-            else:
-                for redefinition in redefinitions[:redefinition_index]:
-                    inferred = utils.safe_infer(redefinition)
-                    if (
-                        inferred
-                        and isinstance(inferred, astroid.Instance)
-                        and inferred.qname() == TYPING_FORWARD_REF_QNAME
-                    ):
-                        return
-
-            dummy_variables_rgx = lint_utils.get_global_option(
-                self, "dummy-variables-rgx", default=None
-            )
-            if dummy_variables_rgx and dummy_variables_rgx.match(node.name):
-                return
-            self.add_message(
-                "function-redefined",
-                node=node,
-                args=(redeftype, defined_self.fromlineno),
-            )
-
-
-class BasicChecker(_BasicChecker):
-    """checks for :
-    * doc strings
-    * number of arguments, local variables, branches, returns and statements in
-    functions, methods
-    * required module attributes
-    * dangerous default values as arguments
-    * redefinition of function / method / class
-    * uses of the global statement
-    """
-
-    __implements__ = interfaces.IAstroidChecker
-
-    name = "basic"
-    msgs = {
-        "W0101": (
-            "Unreachable code",
-            "unreachable",
-            'Used when there is some code behind a "return" or "raise" '
-            "statement, which will never be accessed.",
-        ),
-        "W0102": (
-            "Dangerous default value %s as argument",
-            "dangerous-default-value",
-            "Used when a mutable value as list or dictionary is detected in "
-            "a default value for an argument.",
-        ),
-        "W0104": (
-            "Statement seems to have no effect",
-            "pointless-statement",
-            "Used when a statement doesn't have (or at least seems to) any effect.",
-        ),
-        "W0105": (
-            "String statement has no effect",
-            "pointless-string-statement",
-            "Used when a string is used as a statement (which of course "
-            "has no effect). This is a particular case of W0104 with its "
-            "own message so you can easily disable it if you're using "
-            "those strings as documentation, instead of comments.",
-        ),
-        "W0106": (
-            'Expression "%s" is assigned to nothing',
-            "expression-not-assigned",
-            "Used when an expression that is not a function call is assigned "
-            "to nothing. Probably something else was intended.",
-        ),
-        "W0108": (
-            "Lambda may not be necessary",
-            "unnecessary-lambda",
-            "Used when the body of a lambda expression is a function call "
-            "on the same argument list as the lambda itself; such lambda "
-            "expressions are in all but a few cases replaceable with the "
-            "function being called in the body of the lambda.",
-        ),
-        "W0109": (
-            "Duplicate key %r in dictionary",
-            "duplicate-key",
-            "Used when a dictionary expression binds the same key multiple times.",
-        ),
-        "W0122": (
-            "Use of exec",
-            "exec-used",
-            'Used when you use the "exec" statement (function for Python '
-            "3), to discourage its usage. That doesn't "
-            "mean you cannot use it !",
-        ),
-        "W0123": (
-            "Use of eval",
-            "eval-used",
-            'Used when you use the "eval" function, to discourage its '
-            "usage. Consider using `ast.literal_eval` for safely evaluating "
-            "strings containing Python expressions "
-            "from untrusted sources. ",
-        ),
-        "W0150": (
-            "%s statement in finally block may swallow exception",
-            "lost-exception",
-            "Used when a break or a return statement is found inside the "
-            "finally clause of a try...finally block: the exceptions raised "
-            "in the try clause will be silently swallowed instead of being "
-            "re-raised.",
-        ),
-        "W0199": (
-            "Assert called on a 2-item-tuple. Did you mean 'assert x,y'?",
-            "assert-on-tuple",
-            "A call of assert on a tuple will always evaluate to true if "
-            "the tuple is not empty, and will always evaluate to false if "
-            "it is.",
-        ),
-        "W0124": (
-            'Following "as" with another context manager looks like a tuple.',
-            "confusing-with-statement",
-            "Emitted when a `with` statement component returns multiple values "
-            "and uses name binding with `as` only for a part of those values, "
-            "as in with ctx() as a, b. This can be misleading, since it's not "
-            "clear if the context manager returns a tuple or if the node without "
-            "a name binding is another context manager.",
-        ),
-        "W0125": (
-            "Using a conditional statement with a constant value",
-            "using-constant-test",
-            "Emitted when a conditional statement (If or ternary if) "
-            "uses a constant value for its test. This might not be what "
-            "the user intended to do.",
-        ),
-        "W0126": (
-            "Using a conditional statement with potentially wrong function or method call due to missing parentheses",
-            "missing-parentheses-for-call-in-test",
-            "Emitted when a conditional statement (If or ternary if) "
-            "seems to wrongly call a function due to missing parentheses",
-        ),
-        "W0127": (
-            "Assigning the same variable %r to itself",
-            "self-assigning-variable",
-            "Emitted when we detect that a variable is assigned to itself",
-        ),
-        "W0128": (
-            "Redeclared variable %r in assignment",
-            "redeclared-assigned-name",
-            "Emitted when we detect that a variable was redeclared in the same assignment.",
-        ),
-        "E0111": (
-            "The first reversed() argument is not a sequence",
-            "bad-reversed-sequence",
-            "Used when the first argument to reversed() builtin "
-            "isn't a sequence (does not implement __reversed__, "
-            "nor __getitem__ and __len__",
-        ),
-        "E0119": (
-            "format function is not called on str",
-            "misplaced-format-function",
-            "Emitted when format function is not called on str object. "
-            'e.g doing print("value: {}").format(123) instead of '
-            'print("value: {}".format(123)). This might not be what the user '
-            "intended to do.",
-        ),
-    }
-
-    reports = (("RP0101", "Statistics by type", report_by_type_stats),)
-
-    def __init__(self, linter):
-        _BasicChecker.__init__(self, linter)
-        self.stats = None
-        self._tryfinallys = None
-
-    def open(self):
-        """initialize visit variables and statistics
-        """
-        self._tryfinallys = []
-        self.stats = self.linter.add_stats(module=0, function=0, method=0, class_=0)
-
-    @utils.check_messages("using-constant-test", "missing-parentheses-for-call-in-test")
-    def visit_if(self, node):
-        self._check_using_constant_test(node, node.test)
-
-    @utils.check_messages("using-constant-test", "missing-parentheses-for-call-in-test")
-    def visit_ifexp(self, node):
-        self._check_using_constant_test(node, node.test)
-
-    @utils.check_messages("using-constant-test", "missing-parentheses-for-call-in-test")
-    def visit_comprehension(self, node):
-        if node.ifs:
-            for if_test in node.ifs:
-                self._check_using_constant_test(node, if_test)
-
-    def _check_using_constant_test(self, node, test):
-        const_nodes = (
-            astroid.Module,
-            astroid.scoped_nodes.GeneratorExp,
-            astroid.Lambda,
-            astroid.FunctionDef,
-            astroid.ClassDef,
-            astroid.bases.Generator,
-            astroid.UnboundMethod,
-            astroid.BoundMethod,
-            astroid.Module,
-        )
-        structs = (astroid.Dict, astroid.Tuple, astroid.Set)
-
-        # These nodes are excepted, since they are not constant
-        # values, requiring a computation to happen.
-        except_nodes = (
-            astroid.Call,
-            astroid.BinOp,
-            astroid.BoolOp,
-            astroid.UnaryOp,
-            astroid.Subscript,
-        )
-        inferred = None
-        emit = isinstance(test, (astroid.Const,) + structs + const_nodes)
-        if not isinstance(test, except_nodes):
-            inferred = utils.safe_infer(test)
-
-        if emit:
-            self.add_message("using-constant-test", node=node)
-        elif isinstance(inferred, const_nodes):
-            # If the constant node is a FunctionDef or Lambda then
-            #  it may be a illicit function call due to missing parentheses
-            call_inferred = None
-            if isinstance(inferred, astroid.FunctionDef):
-                call_inferred = inferred.infer_call_result()
-            elif isinstance(inferred, astroid.Lambda):
-                call_inferred = inferred.infer_call_result(node)
-            if call_inferred:
-                try:
-                    for inf_call in call_inferred:
-                        if inf_call != astroid.Uninferable:
-                            self.add_message(
-                                "missing-parentheses-for-call-in-test", node=node
-                            )
-                            break
-                except astroid.InferenceError:
-                    pass
-            self.add_message("using-constant-test", node=node)
-
-    def visit_module(self, _):
-        """check module name, docstring and required arguments
-        """
-        self.stats["module"] += 1
-
-    def visit_classdef(self, node):  # pylint: disable=unused-argument
-        """check module name, docstring and redefinition
-        increment branch counter
-        """
-        self.stats["class"] += 1
-
-    @utils.check_messages(
-        "pointless-statement", "pointless-string-statement", "expression-not-assigned"
-    )
-    def visit_expr(self, node):
-        """Check for various kind of statements without effect"""
-        expr = node.value
-        if isinstance(expr, astroid.Const) and isinstance(expr.value, str):
-            # treat string statement in a separated message
-            # Handle PEP-257 attribute docstrings.
-            # An attribute docstring is defined as being a string right after
-            # an assignment at the module level, class level or __init__ level.
-            scope = expr.scope()
-            if isinstance(
-                scope, (astroid.ClassDef, astroid.Module, astroid.FunctionDef)
-            ):
-                if isinstance(scope, astroid.FunctionDef) and scope.name != "__init__":
-                    pass
-                else:
-                    sibling = expr.previous_sibling()
-                    if (
-                        sibling is not None
-                        and sibling.scope() is scope
-                        and isinstance(sibling, (astroid.Assign, astroid.AnnAssign))
-                    ):
-                        return
-            self.add_message("pointless-string-statement", node=node)
-            return
-
-        # Ignore if this is :
-        # * a direct function call
-        # * the unique child of a try/except body
-        # * a yield statement
-        # * an ellipsis (which can be used on Python 3 instead of pass)
-        # warn W0106 if we have any underlying function call (we can't predict
-        # side effects), else pointless-statement
-        if (
-            isinstance(
-                expr, (astroid.Yield, astroid.Await, astroid.Ellipsis, astroid.Call)
-            )
-            or (
-                isinstance(node.parent, astroid.TryExcept)
-                and node.parent.body == [node]
-            )
-            or (isinstance(expr, astroid.Const) and expr.value is Ellipsis)
-        ):
-            return
-        if any(expr.nodes_of_class(astroid.Call)):
-            self.add_message(
-                "expression-not-assigned", node=node, args=expr.as_string()
-            )
-        else:
-            self.add_message("pointless-statement", node=node)
-
-    @staticmethod
-    def _filter_vararg(node, call_args):
-        # Return the arguments for the given call which are
-        # not passed as vararg.
-        for arg in call_args:
-            if isinstance(arg, astroid.Starred):
-                if (
-                    isinstance(arg.value, astroid.Name)
-                    and arg.value.name != node.args.vararg
-                ):
-                    yield arg
-            else:
-                yield arg
-
-    @staticmethod
-    def _has_variadic_argument(args, variadic_name):
-        if not args:
-            return True
-        for arg in args:
-            if isinstance(arg.value, astroid.Name):
-                if arg.value.name != variadic_name:
-                    return True
-            else:
-                return True
-        return False
-
-    @utils.check_messages("unnecessary-lambda")
-    def visit_lambda(self, node):
-        """check whether or not the lambda is suspicious
-        """
-        # if the body of the lambda is a call expression with the same
-        # argument list as the lambda itself, then the lambda is
-        # possibly unnecessary and at least suspicious.
-        if node.args.defaults:
-            # If the arguments of the lambda include defaults, then a
-            # judgment cannot be made because there is no way to check
-            # that the defaults defined by the lambda are the same as
-            # the defaults defined by the function called in the body
-            # of the lambda.
-            return
-        call = node.body
-        if not isinstance(call, astroid.Call):
-            # The body of the lambda must be a function call expression
-            # for the lambda to be unnecessary.
-            return
-        if isinstance(node.body.func, astroid.Attribute) and isinstance(
-            node.body.func.expr, astroid.Call
-        ):
-            # Chained call, the intermediate call might
-            # return something else (but we don't check that, yet).
-            return
-
-        call_site = CallSite.from_call(call)
-        ordinary_args = list(node.args.args)
-        new_call_args = list(self._filter_vararg(node, call.args))
-        if node.args.kwarg:
-            if self._has_variadic_argument(call.kwargs, node.args.kwarg):
-                return
-
-        if node.args.vararg:
-            if self._has_variadic_argument(call.starargs, node.args.vararg):
-                return
-        elif call.starargs:
-            return
-
-        if call.keywords:
-            # Look for additional keyword arguments that are not part
-            # of the lambda's signature
-            lambda_kwargs = {keyword.name for keyword in node.args.defaults}
-            if len(lambda_kwargs) != len(call_site.keyword_arguments):
-                # Different lengths, so probably not identical
-                return
-            if set(call_site.keyword_arguments).difference(lambda_kwargs):
-                return
-
-        # The "ordinary" arguments must be in a correspondence such that:
-        # ordinary_args[i].name == call.args[i].name.
-        if len(ordinary_args) != len(new_call_args):
-            return
-        for arg, passed_arg in zip(ordinary_args, new_call_args):
-            if not isinstance(passed_arg, astroid.Name):
-                return
-            if arg.name != passed_arg.name:
-                return
-
-        self.add_message("unnecessary-lambda", line=node.fromlineno, node=node)
-
-    @utils.check_messages("dangerous-default-value")
-    def visit_functiondef(self, node):
-        """check function name, docstring, arguments, redefinition,
-        variable names, max locals
-        """
-        self.stats["method" if node.is_method() else "function"] += 1
-        self._check_dangerous_default(node)
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    def _check_dangerous_default(self, node):
-        # check for dangerous default values as arguments
-        is_iterable = lambda n: isinstance(n, (astroid.List, astroid.Set, astroid.Dict))
-        for default in node.args.defaults:
-            try:
-                value = next(default.infer())
-            except astroid.InferenceError:
-                continue
-
-            if (
-                isinstance(value, astroid.Instance)
-                and value.qname() in DEFAULT_ARGUMENT_SYMBOLS
-            ):
-
-                if value is default:
-                    msg = DEFAULT_ARGUMENT_SYMBOLS[value.qname()]
-                elif isinstance(value, astroid.Instance) or is_iterable(value):
-                    # We are here in the following situation(s):
-                    #   * a dict/set/list/tuple call which wasn't inferred
-                    #     to a syntax node ({}, () etc.). This can happen
-                    #     when the arguments are invalid or unknown to
-                    #     the inference.
-                    #   * a variable from somewhere else, which turns out to be a list
-                    #     or a dict.
-                    if is_iterable(default):
-                        msg = value.pytype()
-                    elif isinstance(default, astroid.Call):
-                        msg = "%s() (%s)" % (value.name, value.qname())
-                    else:
-                        msg = "%s (%s)" % (default.as_string(), value.qname())
-                else:
-                    # this argument is a name
-                    msg = "%s (%s)" % (
-                        default.as_string(),
-                        DEFAULT_ARGUMENT_SYMBOLS[value.qname()],
-                    )
-                self.add_message("dangerous-default-value", node=node, args=(msg,))
-
-    @utils.check_messages("unreachable", "lost-exception")
-    def visit_return(self, node):
-        """1 - check is the node has a right sibling (if so, that's some
-        unreachable code)
-        2 - check is the node is inside the finally clause of a try...finally
-        block
-        """
-        self._check_unreachable(node)
-        # Is it inside final body of a try...finally bloc ?
-        self._check_not_in_finally(node, "return", (astroid.FunctionDef,))
-
-    @utils.check_messages("unreachable")
-    def visit_continue(self, node):
-        """check is the node has a right sibling (if so, that's some unreachable
-        code)
-        """
-        self._check_unreachable(node)
-
-    @utils.check_messages("unreachable", "lost-exception")
-    def visit_break(self, node):
-        """1 - check is the node has a right sibling (if so, that's some
-        unreachable code)
-        2 - check is the node is inside the finally clause of a try...finally
-        block
-        """
-        # 1 - Is it right sibling ?
-        self._check_unreachable(node)
-        # 2 - Is it inside final body of a try...finally bloc ?
-        self._check_not_in_finally(node, "break", (astroid.For, astroid.While))
-
-    @utils.check_messages("unreachable")
-    def visit_raise(self, node):
-        """check if the node has a right sibling (if so, that's some unreachable
-        code)
-        """
-        self._check_unreachable(node)
-
-    @utils.check_messages("exec-used")
-    def visit_exec(self, node):
-        """just print a warning on exec statements"""
-        self.add_message("exec-used", node=node)
-
-    def _check_misplaced_format_function(self, call_node):
-        if not isinstance(call_node.func, astroid.Attribute):
-            return
-        if call_node.func.attrname != "format":
-            return
-
-        expr = utils.safe_infer(call_node.func.expr)
-        if expr is astroid.Uninferable:
-            return
-        if not expr:
-            # we are doubtful on inferred type of node, so here just check if format
-            # was called on print()
-            call_expr = call_node.func.expr
-            if not isinstance(call_expr, astroid.Call):
-                return
-            if (
-                isinstance(call_expr.func, astroid.Name)
-                and call_expr.func.name == "print"
-            ):
-                self.add_message("misplaced-format-function", node=call_node)
-
-    @utils.check_messages(
-        "eval-used", "exec-used", "bad-reversed-sequence", "misplaced-format-function"
-    )
-    def visit_call(self, node):
-        """visit a Call node -> check if this is not a blacklisted builtin
-        call and check for * or ** use
-        """
-        self._check_misplaced_format_function(node)
-        if isinstance(node.func, astroid.Name):
-            name = node.func.name
-            # ignore the name if it's not a builtin (i.e. not defined in the
-            # locals nor globals scope)
-            if not (name in node.frame() or name in node.root()):
-                if name == "exec":
-                    self.add_message("exec-used", node=node)
-                elif name == "reversed":
-                    self._check_reversed(node)
-                elif name == "eval":
-                    self.add_message("eval-used", node=node)
-
-    @utils.check_messages("assert-on-tuple")
-    def visit_assert(self, node):
-        """check the use of an assert statement on a tuple."""
-        if (
-            node.fail is None
-            and isinstance(node.test, astroid.Tuple)
-            and len(node.test.elts) == 2
-        ):
-            self.add_message("assert-on-tuple", node=node)
-
-    @utils.check_messages("duplicate-key")
-    def visit_dict(self, node):
-        """check duplicate key in dictionary"""
-        keys = set()
-        for k, _ in node.items:
-            if isinstance(k, astroid.Const):
-                key = k.value
-                if key in keys:
-                    self.add_message("duplicate-key", node=node, args=key)
-                keys.add(key)
-
-    def visit_tryfinally(self, node):
-        """update try...finally flag"""
-        self._tryfinallys.append(node)
-
-    def leave_tryfinally(self, node):  # pylint: disable=unused-argument
-        """update try...finally flag"""
-        self._tryfinallys.pop()
-
-    def _check_unreachable(self, node):
-        """check unreachable code"""
-        unreach_stmt = node.next_sibling()
-        if unreach_stmt is not None:
-            self.add_message("unreachable", node=unreach_stmt)
-
-    def _check_not_in_finally(self, node, node_name, breaker_classes=()):
-        """check that a node is not inside a finally clause of a
-        try...finally statement.
-        If we found before a try...finally bloc a parent which its type is
-        in breaker_classes, we skip the whole check."""
-        # if self._tryfinallys is empty, we're not an in try...finally block
-        if not self._tryfinallys:
-            return
-        # the node could be a grand-grand...-children of the try...finally
-        _parent = node.parent
-        _node = node
-        while _parent and not isinstance(_parent, breaker_classes):
-            if hasattr(_parent, "finalbody") and _node in _parent.finalbody:
-                self.add_message("lost-exception", node=node, args=node_name)
-                return
-            _node = _parent
-            _parent = _node.parent
-
-    def _check_reversed(self, node):
-        """ check that the argument to `reversed` is a sequence """
-        try:
-            argument = utils.safe_infer(utils.get_argument_from_call(node, position=0))
-        except utils.NoSuchArgumentError:
-            pass
-        else:
-            if argument is astroid.Uninferable:
-                return
-            if argument is None:
-                # Nothing was inferred.
-                # Try to see if we have iter().
-                if isinstance(node.args[0], astroid.Call):
-                    try:
-                        func = next(node.args[0].func.infer())
-                    except astroid.InferenceError:
-                        return
-                    if getattr(
-                        func, "name", None
-                    ) == "iter" and utils.is_builtin_object(func):
-                        self.add_message("bad-reversed-sequence", node=node)
-                return
-
-            if isinstance(argument, (astroid.List, astroid.Tuple)):
-                return
-
-            if isinstance(argument, astroid.Instance):
-                if argument._proxied.name == "dict" and utils.is_builtin_object(
-                    argument._proxied
-                ):
-                    self.add_message("bad-reversed-sequence", node=node)
-                    return
-                if any(
-                    ancestor.name == "dict" and utils.is_builtin_object(ancestor)
-                    for ancestor in argument._proxied.ancestors()
-                ):
-                    # Mappings aren't accepted by reversed(), unless
-                    # they provide explicitly a __reversed__ method.
-                    try:
-                        argument.locals[REVERSED_PROTOCOL_METHOD]
-                    except KeyError:
-                        self.add_message("bad-reversed-sequence", node=node)
-                    return
-
-            if hasattr(argument, "getattr"):
-                # everything else is not a proper sequence for reversed()
-                for methods in REVERSED_METHODS:
-                    for meth in methods:
-                        try:
-                            argument.getattr(meth)
-                        except astroid.NotFoundError:
-                            break
-                    else:
-                        break
-                else:
-                    self.add_message("bad-reversed-sequence", node=node)
-            else:
-                self.add_message("bad-reversed-sequence", node=node)
-
-    @utils.check_messages("confusing-with-statement")
-    def visit_with(self, node):
-        # a "with" statement with multiple managers coresponds
-        # to one AST "With" node with multiple items
-        pairs = node.items
-        if pairs:
-            for prev_pair, pair in zip(pairs, pairs[1:]):
-                if isinstance(prev_pair[1], astroid.AssignName) and (
-                    pair[1] is None and not isinstance(pair[0], astroid.Call)
-                ):
-                    # Don't emit a message if the second is a function call
-                    # there's no way that can be mistaken for a name assignment.
-                    # If the line number doesn't match
-                    # we assume it's a nested "with".
-                    self.add_message("confusing-with-statement", node=node)
-
-    def _check_self_assigning_variable(self, node):
-        # Detect assigning to the same variable.
-
-        scope = node.scope()
-        scope_locals = scope.locals
-
-        rhs_names = []
-        targets = node.targets
-        if isinstance(targets[0], astroid.Tuple):
-            if len(targets) != 1:
-                # A complex assignment, so bail out early.
-                return
-            targets = targets[0].elts
-
-        if isinstance(node.value, astroid.Name):
-            if len(targets) != 1:
-                return
-            rhs_names = [node.value]
-        elif isinstance(node.value, astroid.Tuple):
-            rhs_count = len(node.value.elts)
-            if len(targets) != rhs_count or rhs_count == 1:
-                return
-            rhs_names = node.value.elts
-
-        for target, lhs_name in zip(targets, rhs_names):
-            if not isinstance(lhs_name, astroid.Name):
-                continue
-            if not isinstance(target, astroid.AssignName):
-                continue
-            if isinstance(scope, astroid.ClassDef) and target.name in scope_locals:
-                # Check that the scope is different than a class level, which is usually
-                # a pattern to expose module level attributes as class level ones.
-                continue
-            if target.name == lhs_name.name:
-                self.add_message(
-                    "self-assigning-variable", args=(target.name,), node=target
-                )
-
-    def _check_redeclared_assign_name(self, targets):
-        for target in targets:
-            if not isinstance(target, astroid.Tuple):
-                continue
-
-            found_names = []
-            for element in target.elts:
-                if isinstance(element, astroid.Tuple):
-                    self._check_redeclared_assign_name([element])
-                elif isinstance(element, astroid.AssignName) and element.name != "_":
-                    found_names.append(element.name)
-
-            names = collections.Counter(found_names)
-            for name, count in names.most_common():
-                if count > 1:
-                    self.add_message(
-                        "redeclared-assigned-name", args=(name,), node=target
-                    )
-
-    @utils.check_messages("self-assigning-variable", "redeclared-assigned-name")
-    def visit_assign(self, node):
-        self._check_self_assigning_variable(node)
-        self._check_redeclared_assign_name(node.targets)
-
-    @utils.check_messages("redeclared-assigned-name")
-    def visit_for(self, node):
-        self._check_redeclared_assign_name([node.target])
-
-
-KNOWN_NAME_TYPES = {
-    "module",
-    "const",
-    "class",
-    "function",
-    "method",
-    "attr",
-    "argument",
-    "variable",
-    "class_attribute",
-    "inlinevar",
-}
-
-
-HUMAN_READABLE_TYPES = {
-    "module": "module",
-    "const": "constant",
-    "class": "class",
-    "function": "function",
-    "method": "method",
-    "attr": "attribute",
-    "argument": "argument",
-    "variable": "variable",
-    "class_attribute": "class attribute",
-    "inlinevar": "inline iteration",
-}
-
-DEFAULT_NAMING_STYLES = {
-    "module": "snake_case",
-    "const": "UPPER_CASE",
-    "class": "PascalCase",
-    "function": "snake_case",
-    "method": "snake_case",
-    "attr": "snake_case",
-    "argument": "snake_case",
-    "variable": "snake_case",
-    "class_attribute": "any",
-    "inlinevar": "any",
-}
-
-
-def _create_naming_options():
-    name_options = []
-    for name_type in sorted(KNOWN_NAME_TYPES):
-        human_readable_name = HUMAN_READABLE_TYPES[name_type]
-        default_style = DEFAULT_NAMING_STYLES[name_type]
-        name_type = name_type.replace("_", "-")
-        name_options.append(
-            (
-                "%s-naming-style" % (name_type,),
-                {
-                    "default": default_style,
-                    "type": "choice",
-                    "choices": list(NAMING_STYLES.keys()),
-                    "metavar": "<style>",
-                    "help": "Naming style matching correct %s names."
-                    % (human_readable_name,),
-                },
-            )
-        )
-        name_options.append(
-            (
-                "%s-rgx" % (name_type,),
-                {
-                    "default": None,
-                    "type": "regexp",
-                    "metavar": "<regexp>",
-                    "help": "Regular expression matching correct %s names. Overrides %s-naming-style."
-                    % (human_readable_name, name_type),
-                },
-            )
-        )
-    return tuple(name_options)
-
-
-class NameChecker(_BasicChecker):
-
-    msgs = {
-        "C0102": (
-            'Black listed name "%s"',
-            "blacklisted-name",
-            "Used when the name is listed in the black list (unauthorized names).",
-        ),
-        "C0103": (
-            '%s name "%s" doesn\'t conform to %s',
-            "invalid-name",
-            "Used when the name doesn't conform to naming rules "
-            "associated to its type (constant, variable, class...).",
-        ),
-        "W0111": (
-            "Name %s will become a keyword in Python %s",
-            "assign-to-new-keyword",
-            "Used when assignment will become invalid in future "
-            "Python release due to introducing new keyword.",
-        ),
-    }
-
-    options = (
-        (
-            "good-names",
-            {
-                "default": ("i", "j", "k", "ex", "Run", "_"),
-                "type": "csv",
-                "metavar": "<names>",
-                "help": "Good variable names which should always be accepted,"
-                " separated by a comma.",
-            },
-        ),
-        (
-            "bad-names",
-            {
-                "default": ("foo", "bar", "baz", "toto", "tutu", "tata"),
-                "type": "csv",
-                "metavar": "<names>",
-                "help": "Bad variable names which should always be refused, "
-                "separated by a comma.",
-            },
-        ),
-        (
-            "name-group",
-            {
-                "default": (),
-                "type": "csv",
-                "metavar": "<name1:name2>",
-                "help": (
-                    "Colon-delimited sets of names that determine each"
-                    " other's naming style when the name regexes"
-                    " allow several styles."
-                ),
-            },
-        ),
-        (
-            "include-naming-hint",
-            {
-                "default": False,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "Include a hint for the correct naming format with invalid-name.",
-            },
-        ),
-        (
-            "property-classes",
-            {
-                "default": ("abc.abstractproperty",),
-                "type": "csv",
-                "metavar": "<decorator names>",
-                "help": "List of decorators that produce properties, such as "
-                "abc.abstractproperty. Add to this list to register "
-                "other decorators that produce valid properties. "
-                "These decorators are taken in consideration only for invalid-name.",
-            },
-        ),
-    ) + _create_naming_options()
-
-    KEYWORD_ONSET = {(3, 7): {"async", "await"}}
-
-    def __init__(self, linter):
-        _BasicChecker.__init__(self, linter)
-        self._name_category = {}
-        self._name_group = {}
-        self._bad_names = {}
-        self._name_regexps = {}
-        self._name_hints = {}
-
-    def open(self):
-        self.stats = self.linter.add_stats(
-            badname_module=0,
-            badname_class=0,
-            badname_function=0,
-            badname_method=0,
-            badname_attr=0,
-            badname_const=0,
-            badname_variable=0,
-            badname_inlinevar=0,
-            badname_argument=0,
-            badname_class_attribute=0,
-        )
-        for group in self.config.name_group:
-            for name_type in group.split(":"):
-                self._name_group[name_type] = "group_%s" % (group,)
-
-        regexps, hints = self._create_naming_rules()
-        self._name_regexps = regexps
-        self._name_hints = hints
-
-    def _create_naming_rules(self):
-        regexps = {}
-        hints = {}
-
-        for name_type in KNOWN_NAME_TYPES:
-            naming_style_option_name = "%s_naming_style" % (name_type,)
-            naming_style_name = getattr(self.config, naming_style_option_name)
-
-            regexps[name_type] = NAMING_STYLES[naming_style_name].get_regex(name_type)
-
-            custom_regex_setting_name = "%s_rgx" % (name_type,)
-            custom_regex = getattr(self.config, custom_regex_setting_name, None)
-            if custom_regex is not None:
-                regexps[name_type] = custom_regex
-
-            if custom_regex is not None:
-                hints[name_type] = "%r pattern" % custom_regex.pattern
-            else:
-                hints[name_type] = "%s naming style" % naming_style_name
-
-        return regexps, hints
-
-    @utils.check_messages("blacklisted-name", "invalid-name")
-    def visit_module(self, node):
-        self._check_name("module", node.name.split(".")[-1], node)
-        self._bad_names = {}
-
-    def leave_module(self, node):  # pylint: disable=unused-argument
-        for all_groups in self._bad_names.values():
-            if len(all_groups) < 2:
-                continue
-            groups = collections.defaultdict(list)
-            min_warnings = sys.maxsize
-            for group in all_groups.values():
-                groups[len(group)].append(group)
-                min_warnings = min(len(group), min_warnings)
-            if len(groups[min_warnings]) > 1:
-                by_line = sorted(
-                    groups[min_warnings],
-                    key=lambda group: min(warning[0].lineno for warning in group),
-                )
-                warnings = itertools.chain(*by_line[1:])
-            else:
-                warnings = groups[min_warnings][0]
-            for args in warnings:
-                self._raise_name_warning(*args)
-
-    @utils.check_messages("blacklisted-name", "invalid-name", "assign-to-new-keyword")
-    def visit_classdef(self, node):
-        self._check_assign_to_new_keyword_violation(node.name, node)
-        self._check_name("class", node.name, node)
-        for attr, anodes in node.instance_attrs.items():
-            if not any(node.instance_attr_ancestors(attr)):
-                self._check_name("attr", attr, anodes[0])
-
-    @utils.check_messages("blacklisted-name", "invalid-name", "assign-to-new-keyword")
-    def visit_functiondef(self, node):
-        # Do not emit any warnings if the method is just an implementation
-        # of a base class method.
-        self._check_assign_to_new_keyword_violation(node.name, node)
-        confidence = interfaces.HIGH
-        if node.is_method():
-            if utils.overrides_a_method(node.parent.frame(), node.name):
-                return
-            confidence = (
-                interfaces.INFERENCE
-                if utils.has_known_bases(node.parent.frame())
-                else interfaces.INFERENCE_FAILURE
-            )
-
-        self._check_name(
-            _determine_function_name_type(node, config=self.config),
-            node.name,
-            node,
-            confidence,
-        )
-        # Check argument names
-        args = node.args.args
-        if args is not None:
-            self._recursive_check_names(args, node)
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    @utils.check_messages("blacklisted-name", "invalid-name")
-    def visit_global(self, node):
-        for name in node.names:
-            self._check_name("const", name, node)
-
-    @utils.check_messages("blacklisted-name", "invalid-name", "assign-to-new-keyword")
-    def visit_assignname(self, node):
-        """check module level assigned names"""
-        self._check_assign_to_new_keyword_violation(node.name, node)
-        frame = node.frame()
-        assign_type = node.assign_type()
-        if isinstance(assign_type, astroid.Comprehension):
-            self._check_name("inlinevar", node.name, node)
-        elif isinstance(frame, astroid.Module):
-            if isinstance(assign_type, astroid.Assign) and not in_loop(assign_type):
-                if isinstance(utils.safe_infer(assign_type.value), astroid.ClassDef):
-                    self._check_name("class", node.name, node)
-                else:
-                    if not _redefines_import(node):
-                        # Don't emit if the name redefines an import
-                        # in an ImportError except handler.
-                        self._check_name("const", node.name, node)
-            elif isinstance(assign_type, astroid.ExceptHandler):
-                self._check_name("variable", node.name, node)
-        elif isinstance(frame, astroid.FunctionDef):
-            # global introduced variable aren't in the function locals
-            if node.name in frame and node.name not in frame.argnames():
-                if not _redefines_import(node):
-                    self._check_name("variable", node.name, node)
-        elif isinstance(frame, astroid.ClassDef):
-            if not list(frame.local_attr_ancestors(node.name)):
-                self._check_name("class_attribute", node.name, node)
-
-    def _recursive_check_names(self, args, node):
-        """check names in a possibly recursive list <arg>"""
-        for arg in args:
-            if isinstance(arg, astroid.AssignName):
-                self._check_name("argument", arg.name, node)
-            else:
-                self._recursive_check_names(arg.elts, node)
-
-    def _find_name_group(self, node_type):
-        return self._name_group.get(node_type, node_type)
-
-    def _raise_name_warning(self, node, node_type, name, confidence):
-        type_label = HUMAN_READABLE_TYPES[node_type]
-        hint = self._name_hints[node_type]
-        if self.config.include_naming_hint:
-            hint += " (%r pattern)" % self._name_regexps[node_type].pattern
-        args = (type_label.capitalize(), name, hint)
-
-        self.add_message("invalid-name", node=node, args=args, confidence=confidence)
-        self.stats["badname_" + node_type] += 1
-
-    def _check_name(self, node_type, name, node, confidence=interfaces.HIGH):
-        """check for a name using the type's regexp"""
-
-        def _should_exempt_from_invalid_name(node):
-            if node_type == "variable":
-                inferred = utils.safe_infer(node)
-                if isinstance(inferred, astroid.ClassDef):
-                    return True
-            return False
-
-        if utils.is_inside_except(node):
-            clobbering, _ = utils.clobber_in_except(node)
-            if clobbering:
-                return
-        if name in self.config.good_names:
-            return
-        if name in self.config.bad_names:
-            self.stats["badname_" + node_type] += 1
-            self.add_message("blacklisted-name", node=node, args=name)
-            return
-        regexp = self._name_regexps[node_type]
-        match = regexp.match(name)
-
-        if _is_multi_naming_match(match, node_type, confidence):
-            name_group = self._find_name_group(node_type)
-            bad_name_group = self._bad_names.setdefault(name_group, {})
-            warnings = bad_name_group.setdefault(match.lastgroup, [])
-            warnings.append((node, node_type, name, confidence))
-
-        if match is None and not _should_exempt_from_invalid_name(node):
-            self._raise_name_warning(node, node_type, name, confidence)
-
-    def _check_assign_to_new_keyword_violation(self, name, node):
-        keyword_first_version = self._name_became_keyword_in_version(
-            name, self.KEYWORD_ONSET
-        )
-        if keyword_first_version is not None:
-            self.add_message(
-                "assign-to-new-keyword",
-                node=node,
-                args=(name, keyword_first_version),
-                confidence=interfaces.HIGH,
-            )
-
-    @staticmethod
-    def _name_became_keyword_in_version(name, rules):
-        for version, keywords in rules.items():
-            if name in keywords and sys.version_info < version:
-                return ".".join(map(str, version))
-        return None
-
-
-class DocStringChecker(_BasicChecker):
-    msgs = {
-        "C0112": (
-            "Empty %s docstring",
-            "empty-docstring",
-            "Used when a module, function, class or method has an empty "
-            "docstring (it would be too easy ;).",
-            {"old_names": [("W0132", "old-empty-docstring")]},
-        ),
-        "C0114": (
-            "Missing module docstring",
-            "missing-module-docstring",
-            "Used when a module has no docstring."
-            "Empty modules do not require a docstring.",
-            {"old_names": [("C0111", "missing-docstring")]},
-        ),
-        "C0115": (
-            "Missing class docstring",
-            "missing-class-docstring",
-            "Used when a class has no docstring."
-            "Even an empty class must have a docstring.",
-            {"old_names": [("C0111", "missing-docstring")]},
-        ),
-        "C0116": (
-            "Missing function or method docstring",
-            "missing-function-docstring",
-            "Used when a function or method has no docstring."
-            "Some special methods like __init__ do not require a "
-            "docstring.",
-            {"old_names": [("C0111", "missing-docstring")]},
-        ),
-    }
-    options = (
-        (
-            "no-docstring-rgx",
-            {
-                "default": NO_REQUIRED_DOC_RGX,
-                "type": "regexp",
-                "metavar": "<regexp>",
-                "help": "Regular expression which should only match "
-                "function or class names that do not require a "
-                "docstring.",
-            },
-        ),
-        (
-            "docstring-min-length",
-            {
-                "default": -1,
-                "type": "int",
-                "metavar": "<int>",
-                "help": (
-                    "Minimum line length for functions/classes that"
-                    " require docstrings, shorter ones are exempt."
-                ),
-            },
-        ),
-    )
-
-    def open(self):
-        self.stats = self.linter.add_stats(
-            undocumented_module=0,
-            undocumented_function=0,
-            undocumented_method=0,
-            undocumented_class=0,
-        )
-
-    @utils.check_messages("missing-docstring", "empty-docstring")
-    def visit_module(self, node):
-        self._check_docstring("module", node)
-
-    @utils.check_messages("missing-docstring", "empty-docstring")
-    def visit_classdef(self, node):
-        if self.config.no_docstring_rgx.match(node.name) is None:
-            self._check_docstring("class", node)
-
-    @utils.check_messages("missing-docstring", "empty-docstring")
-    def visit_functiondef(self, node):
-        if self.config.no_docstring_rgx.match(node.name) is None:
-            ftype = "method" if node.is_method() else "function"
-            if is_property_setter_or_deleter(node):
-                return
-
-            if isinstance(node.parent.frame(), astroid.ClassDef):
-                overridden = False
-                confidence = (
-                    interfaces.INFERENCE
-                    if utils.has_known_bases(node.parent.frame())
-                    else interfaces.INFERENCE_FAILURE
-                )
-                # check if node is from a method overridden by its ancestor
-                for ancestor in node.parent.frame().ancestors():
-                    if node.name in ancestor and isinstance(
-                        ancestor[node.name], astroid.FunctionDef
-                    ):
-                        overridden = True
-                        break
-                self._check_docstring(
-                    ftype, node, report_missing=not overridden, confidence=confidence
-                )
-            elif isinstance(node.parent.frame(), astroid.Module):
-                self._check_docstring(ftype, node)
-            else:
-                return
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    def _check_docstring(
-        self, node_type, node, report_missing=True, confidence=interfaces.HIGH
-    ):
-        """check the node has a non empty docstring"""
-        docstring = node.doc
-        if docstring is None:
-            if not report_missing:
-                return
-            lines = utils.get_node_last_lineno(node) - node.lineno
-
-            if node_type == "module" and not lines:
-                # If the module has no body, there's no reason
-                # to require a docstring.
-                return
-            max_lines = self.config.docstring_min_length
-
-            if node_type != "module" and max_lines > -1 and lines < max_lines:
-                return
-            self.stats["undocumented_" + node_type] += 1
-            if (
-                node.body
-                and isinstance(node.body[0], astroid.Expr)
-                and isinstance(node.body[0].value, astroid.Call)
-            ):
-                # Most likely a string with a format call. Let's see.
-                func = utils.safe_infer(node.body[0].value.func)
-                if isinstance(func, astroid.BoundMethod) and isinstance(
-                    func.bound, astroid.Instance
-                ):
-                    # Strings.
-                    if func.bound.name == "str":
-                        return
-                    if func.bound.name in ("str", "unicode", "bytes"):
-                        return
-            if node_type == "module":
-                message = "missing-module-docstring"
-            elif node_type == "class":
-                message = "missing-class-docstring"
-            else:
-                message = "missing-function-docstring"
-            self.add_message(message, node=node, confidence=confidence)
-        elif not docstring.strip():
-            self.stats["undocumented_" + node_type] += 1
-            self.add_message(
-                "empty-docstring", node=node, args=(node_type,), confidence=confidence
-            )
-
-
-class PassChecker(_BasicChecker):
-    """check if the pass statement is really necessary"""
-
-    msgs = {
-        "W0107": (
-            "Unnecessary pass statement",
-            "unnecessary-pass",
-            'Used when a "pass" statement that can be avoided is encountered.',
-        )
-    }
-
-    @utils.check_messages("unnecessary-pass")
-    def visit_pass(self, node):
-        if len(node.parent.child_sequence(node)) > 1 or (
-            isinstance(node.parent, (astroid.ClassDef, astroid.FunctionDef))
-            and (node.parent.doc is not None)
-        ):
-            self.add_message("unnecessary-pass", node=node)
-
-
-def _is_one_arg_pos_call(call):
-    """Is this a call with exactly 1 argument,
-    where that argument is positional?
-    """
-    return isinstance(call, astroid.Call) and len(call.args) == 1 and not call.keywords
-
-
-class ComparisonChecker(_BasicChecker):
-    """Checks for comparisons
-
-    - singleton comparison: 'expr == True', 'expr == False' and 'expr == None'
-    - yoda condition: 'const "comp" right' where comp can be '==', '!=', '<',
-      '<=', '>' or '>=', and right can be a variable, an attribute, a method or
-      a function
-    """
-
-    msgs = {
-        "C0121": (
-            "Comparison to %s should be %s",
-            "singleton-comparison",
-            "Used when an expression is compared to singleton "
-            "values like True, False or None.",
-        ),
-        "C0122": (
-            "Comparison should be %s",
-            "misplaced-comparison-constant",
-            "Used when the constant is placed on the left side "
-            "of a comparison. It is usually clearer in intent to "
-            "place it in the right hand side of the comparison.",
-        ),
-        "C0123": (
-            "Using type() instead of isinstance() for a typecheck.",
-            "unidiomatic-typecheck",
-            "The idiomatic way to perform an explicit typecheck in "
-            "Python is to use isinstance(x, Y) rather than "
-            "type(x) == Y, type(x) is Y. Though there are unusual "
-            "situations where these give different results.",
-            {"old_names": [("W0154", "old-unidiomatic-typecheck")]},
-        ),
-        "R0123": (
-            "Comparison to literal",
-            "literal-comparison",
-            "Used when comparing an object to a literal, which is usually "
-            "what you do not want to do, since you can compare to a different "
-            "literal than what was expected altogether.",
-        ),
-        "R0124": (
-            "Redundant comparison - %s",
-            "comparison-with-itself",
-            "Used when something is compared against itself.",
-        ),
-        "W0143": (
-            "Comparing against a callable, did you omit the parenthesis?",
-            "comparison-with-callable",
-            "This message is emitted when pylint detects that a comparison with a "
-            "callable was made, which might suggest that some parenthesis were omitted, "
-            "resulting in potential unwanted behaviour.",
-        ),
-    }
-
-    def _check_singleton_comparison(self, singleton, root_node, negative_check=False):
-        if singleton.value is True:
-            if not negative_check:
-                suggestion = "just 'expr'"
-            else:
-                suggestion = "just 'not expr'"
-            self.add_message(
-                "singleton-comparison", node=root_node, args=(True, suggestion)
-            )
-        elif singleton.value is False:
-            if not negative_check:
-                suggestion = "'not expr'"
-            else:
-                suggestion = "'expr'"
-            self.add_message(
-                "singleton-comparison", node=root_node, args=(False, suggestion)
-            )
-        elif singleton.value is None:
-            if not negative_check:
-                suggestion = "'expr is None'"
-            else:
-                suggestion = "'expr is not None'"
-            self.add_message(
-                "singleton-comparison", node=root_node, args=(None, suggestion)
-            )
-
-    def _check_literal_comparison(self, literal, node):
-        """Check if we compare to a literal, which is usually what we do not want to do."""
-        nodes = (astroid.List, astroid.Tuple, astroid.Dict, astroid.Set)
-        is_other_literal = isinstance(literal, nodes)
-        is_const = False
-        if isinstance(literal, astroid.Const):
-            if isinstance(literal.value, bool) or literal.value is None:
-                # Not interested in this values.
-                return
-            is_const = isinstance(literal.value, (bytes, str, int, float))
-
-        if is_const or is_other_literal:
-            self.add_message("literal-comparison", node=node)
-
-    def _check_misplaced_constant(self, node, left, right, operator):
-        if isinstance(right, astroid.Const):
-            return
-        operator = REVERSED_COMPS.get(operator, operator)
-        suggestion = "%s %s %r" % (right.as_string(), operator, left.value)
-        self.add_message("misplaced-comparison-constant", node=node, args=(suggestion,))
-
-    def _check_logical_tautology(self, node):
-        """Check if identifier is compared against itself.
-        :param node: Compare node
-        :type node: astroid.node_classes.Compare
-        :Example:
-        val = 786
-        if val == val:  # [comparison-with-itself]
-            pass
-        """
-        left_operand = node.left
-        right_operand = node.ops[0][1]
-        operator = node.ops[0][0]
-        if isinstance(left_operand, astroid.Const) and isinstance(
-            right_operand, astroid.Const
-        ):
-            left_operand = left_operand.value
-            right_operand = right_operand.value
-        elif isinstance(left_operand, astroid.Name) and isinstance(
-            right_operand, astroid.Name
-        ):
-            left_operand = left_operand.name
-            right_operand = right_operand.name
-
-        if left_operand == right_operand:
-            suggestion = "%s %s %s" % (left_operand, operator, right_operand)
-            self.add_message("comparison-with-itself", node=node, args=(suggestion,))
-
-    def _check_callable_comparison(self, node):
-        operator = node.ops[0][0]
-        if operator not in COMPARISON_OPERATORS:
-            return
-
-        bare_callables = (astroid.FunctionDef, astroid.BoundMethod)
-        left_operand, right_operand = node.left, node.ops[0][1]
-        # this message should be emitted only when there is comparison of bare callable
-        # with non bare callable.
-        if (
-            sum(
-                1
-                for operand in (left_operand, right_operand)
-                if isinstance(utils.safe_infer(operand), bare_callables)
-            )
-            == 1
-        ):
-            self.add_message("comparison-with-callable", node=node)
-
-    @utils.check_messages(
-        "singleton-comparison",
-        "misplaced-comparison-constant",
-        "unidiomatic-typecheck",
-        "literal-comparison",
-        "comparison-with-itself",
-        "comparison-with-callable",
-    )
-    def visit_compare(self, node):
-        self._check_callable_comparison(node)
-        self._check_logical_tautology(node)
-        self._check_unidiomatic_typecheck(node)
-        # NOTE: this checker only works with binary comparisons like 'x == 42'
-        # but not 'x == y == 42'
-        if len(node.ops) != 1:
-            return
-
-        left = node.left
-        operator, right = node.ops[0]
-        if operator in COMPARISON_OPERATORS and isinstance(left, astroid.Const):
-            self._check_misplaced_constant(node, left, right, operator)
-
-        if operator == "==":
-            if isinstance(left, astroid.Const):
-                self._check_singleton_comparison(left, node)
-            elif isinstance(right, astroid.Const):
-                self._check_singleton_comparison(right, node)
-        if operator == "!=":
-            if isinstance(right, astroid.Const):
-                self._check_singleton_comparison(right, node, negative_check=True)
-        if operator in ("is", "is not"):
-            self._check_literal_comparison(right, node)
-
-    def _check_unidiomatic_typecheck(self, node):
-        operator, right = node.ops[0]
-        if operator in TYPECHECK_COMPARISON_OPERATORS:
-            left = node.left
-            if _is_one_arg_pos_call(left):
-                self._check_type_x_is_y(node, left, operator, right)
-
-    def _check_type_x_is_y(self, node, left, operator, right):
-        """Check for expressions like type(x) == Y."""
-        left_func = utils.safe_infer(left.func)
-        if not (
-            isinstance(left_func, astroid.ClassDef) and left_func.qname() == TYPE_QNAME
-        ):
-            return
-
-        if operator in ("is", "is not") and _is_one_arg_pos_call(right):
-            right_func = utils.safe_infer(right.func)
-            if (
-                isinstance(right_func, astroid.ClassDef)
-                and right_func.qname() == TYPE_QNAME
-            ):
-                # type(x) == type(a)
-                right_arg = utils.safe_infer(right.args[0])
-                if not isinstance(right_arg, LITERAL_NODE_TYPES):
-                    # not e.g. type(x) == type([])
-                    return
-        self.add_message("unidiomatic-typecheck", node=node)
-
-
-def register(linter):
-    """required method to auto register this checker"""
-    linter.register_checker(BasicErrorChecker(linter))
-    linter.register_checker(BasicChecker(linter))
-    linter.register_checker(NameChecker(linter))
-    linter.register_checker(DocStringChecker(linter))
-    linter.register_checker(PassChecker(linter))
-    linter.register_checker(ComparisonChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/base_checker.py b/venv/Lib/site-packages/pylint/checkers/base_checker.py
deleted file mode 100644
index f2ae4e5..0000000
--- a/venv/Lib/site-packages/pylint/checkers/base_checker.py
+++ /dev/null
@@ -1,187 +0,0 @@
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2013 buck@yelp.com <buck@yelp.com>
-# Copyright (c) 2014-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2017-2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-from inspect import cleandoc
-from typing import Any
-
-from pylint.config import OptionsProviderMixIn
-from pylint.constants import _MSG_ORDER, WarningScope
-from pylint.exceptions import InvalidMessageError
-from pylint.interfaces import UNDEFINED, IRawChecker, ITokenChecker, implements
-from pylint.message.message_definition import MessageDefinition
-from pylint.utils import get_rst_section, get_rst_title
-
-
-class BaseChecker(OptionsProviderMixIn):
-
-    # checker name (you may reuse an existing one)
-    name = None  # type: str
-    # options level (0 will be displaying in --help, 1 in --long-help)
-    level = 1
-    # ordered list of options to control the checker behaviour
-    options = ()  # type: Any
-    # messages issued by this checker
-    msgs = {}  # type: Any
-    # reports issued by this checker
-    reports = ()  # type: Any
-    # mark this checker as enabled or not.
-    enabled = True
-
-    def __init__(self, linter=None):
-        """checker instances should have the linter as argument
-
-        :param ILinter linter: is an object implementing ILinter."""
-        if self.name is not None:
-            self.name = self.name.lower()
-        OptionsProviderMixIn.__init__(self)
-        self.linter = linter
-
-    def __gt__(self, other):
-        """Permit to sort a list of Checker by name."""
-        return "{}{}".format(self.name, self.msgs).__gt__(
-            "{}{}".format(other.name, other.msgs)
-        )
-
-    def __repr__(self):
-        status = "Checker" if self.enabled else "Disabled checker"
-        return "{} '{}' (responsible for '{}')".format(
-            status, self.name, "', '".join(self.msgs.keys())
-        )
-
-    def __str__(self):
-        """This might be incomplete because multiple class inheriting BaseChecker
-        can have the same name. Cf MessageHandlerMixIn.get_full_documentation()"""
-        return self.get_full_documentation(
-            msgs=self.msgs, options=self.options_and_values(), reports=self.reports
-        )
-
-    def get_full_documentation(self, msgs, options, reports, doc=None, module=None):
-        result = ""
-        checker_title = "%s checker" % (self.name.replace("_", " ").title())
-        if module:
-            # Provide anchor to link against
-            result += ".. _%s:\n\n" % module
-        result += "%s\n" % get_rst_title(checker_title, "~")
-        if module:
-            result += "This checker is provided by ``%s``.\n" % module
-        result += "Verbatim name of the checker is ``%s``.\n\n" % self.name
-        if doc:
-            # Provide anchor to link against
-            result += get_rst_title("{} Documentation".format(checker_title), "^")
-            result += "%s\n\n" % cleandoc(doc)
-        # options might be an empty generator and not be False when casted to boolean
-        options = list(options)
-        if options:
-            result += get_rst_title("{} Options".format(checker_title), "^")
-            result += "%s\n" % get_rst_section(None, options)
-        if msgs:
-            result += get_rst_title("{} Messages".format(checker_title), "^")
-            for msgid, msg in sorted(
-                msgs.items(), key=lambda kv: (_MSG_ORDER.index(kv[0][0]), kv[1])
-            ):
-                msg = self.create_message_definition_from_tuple(msgid, msg)
-                result += "%s\n" % msg.format_help(checkerref=False)
-            result += "\n"
-        if reports:
-            result += get_rst_title("{} Reports".format(checker_title), "^")
-            for report in reports:
-                result += ":%s: %s\n" % report[:2]
-            result += "\n"
-        result += "\n"
-        return result
-
-    def add_message(
-        self, msgid, line=None, node=None, args=None, confidence=None, col_offset=None
-    ):
-        if not confidence:
-            confidence = UNDEFINED
-        self.linter.add_message(msgid, line, node, args, confidence, col_offset)
-
-    def check_consistency(self):
-        """Check the consistency of msgid.
-
-        msg ids for a checker should be a string of len 4, where the two first
-        characters are the checker id and the two last the msg id in this
-        checker.
-
-        :raises InvalidMessageError: If the checker id in the messages are not
-        always the same. """
-        checker_id = None
-        existing_ids = []
-        for message in self.messages:
-            if checker_id is not None and checker_id != message.msgid[1:3]:
-                error_msg = "Inconsistent checker part in message id "
-                error_msg += "'{}' (expected 'x{checker_id}xx' ".format(
-                    message.msgid, checker_id=checker_id
-                )
-                error_msg += "because we already had {existing_ids}).".format(
-                    existing_ids=existing_ids
-                )
-                raise InvalidMessageError(error_msg)
-            checker_id = message.msgid[1:3]
-            existing_ids.append(message.msgid)
-
-    def create_message_definition_from_tuple(self, msgid, msg_tuple):
-        if implements(self, (IRawChecker, ITokenChecker)):
-            default_scope = WarningScope.LINE
-        else:
-            default_scope = WarningScope.NODE
-        options = {}
-        if len(msg_tuple) > 3:
-            (msg, symbol, descr, options) = msg_tuple
-        elif len(msg_tuple) > 2:
-            (msg, symbol, descr) = msg_tuple
-        else:
-            error_msg = """Messages should have a msgid and a symbol. Something like this :
-
-"W1234": (
-    "message",
-    "message-symbol",
-    "Message description with detail.",
-    ...
-),
-"""
-            raise InvalidMessageError(error_msg)
-        options.setdefault("scope", default_scope)
-        return MessageDefinition(self, msgid, msg, descr, symbol, **options)
-
-    @property
-    def messages(self) -> list:
-        return [
-            self.create_message_definition_from_tuple(msgid, msg_tuple)
-            for msgid, msg_tuple in sorted(self.msgs.items())
-        ]
-
-    # dummy methods implementing the IChecker interface
-
-    def get_message_definition(self, msgid):
-        for message_definition in self.messages:
-            if message_definition.msgid == msgid:
-                return message_definition
-        error_msg = "MessageDefinition for '{}' does not exists. ".format(msgid)
-        error_msg += "Choose from {}.".format([m.msgid for m in self.messages])
-        raise InvalidMessageError(error_msg)
-
-    def open(self):
-        """called before visiting project (i.e set of modules)"""
-
-    def close(self):
-        """called after visiting project (i.e set of modules)"""
-
-
-class BaseTokenChecker(BaseChecker):
-    """Base class for checkers that want to have access to the token stream."""
-
-    def process_tokens(self, tokens):
-        """Should be overridden by subclasses."""
-        raise NotImplementedError()
diff --git a/venv/Lib/site-packages/pylint/checkers/classes.py b/venv/Lib/site-packages/pylint/checkers/classes.py
deleted file mode 100644
index 9f5d099..0000000
--- a/venv/Lib/site-packages/pylint/checkers/classes.py
+++ /dev/null
@@ -1,1844 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2016 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Maarten ter Huurne <maarten@treewalker.org>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2014 David Pursehouse <david.pursehouse@gmail.com>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016-2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2016 Anthony Foglia <afoglia@users.noreply.github.com>
-# Copyright (c) 2016 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 Ben Green <benhgreen@icloud.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""classes checker for Python code
-"""
-import collections
-from itertools import chain, zip_longest
-
-import astroid
-from astroid import decorators, objects
-from astroid.bases import BUILTINS, Generator
-from astroid.exceptions import DuplicateBasesError, InconsistentMroError
-from astroid.scoped_nodes import function_to_method
-
-from pylint.checkers import BaseChecker
-from pylint.checkers.utils import (
-    PYMETHODS,
-    SPECIAL_METHODS_PARAMS,
-    check_messages,
-    class_is_abstract,
-    decorated_with,
-    decorated_with_property,
-    has_known_bases,
-    is_attr_private,
-    is_attr_protected,
-    is_builtin_object,
-    is_comprehension,
-    is_iterable,
-    is_property_setter,
-    is_property_setter_or_deleter,
-    is_protocol_class,
-    node_frame_class,
-    overrides_a_method,
-    safe_infer,
-    unimplemented_abstract_methods,
-)
-from pylint.interfaces import IAstroidChecker
-from pylint.utils import get_global_option
-
-NEXT_METHOD = "__next__"
-INVALID_BASE_CLASSES = {"bool", "range", "slice", "memoryview"}
-BUILTIN_DECORATORS = {"builtins.property", "builtins.classmethod"}
-
-# Dealing with useless override detection, with regard
-# to parameters vs arguments
-
-_CallSignature = collections.namedtuple(
-    "_CallSignature", "args kws starred_args starred_kws"
-)
-_ParameterSignature = collections.namedtuple(
-    "_ParameterSignature", "args kwonlyargs varargs kwargs"
-)
-
-
-def _signature_from_call(call):
-    kws = {}
-    args = []
-    starred_kws = []
-    starred_args = []
-    for keyword in call.keywords or []:
-        arg, value = keyword.arg, keyword.value
-        if arg is None and isinstance(value, astroid.Name):
-            # Starred node and we are interested only in names,
-            # otherwise some transformation might occur for the parameter.
-            starred_kws.append(value.name)
-        elif isinstance(value, astroid.Name):
-            kws[arg] = value.name
-        else:
-            kws[arg] = None
-
-    for arg in call.args:
-        if isinstance(arg, astroid.Starred) and isinstance(arg.value, astroid.Name):
-            # Positional variadic and a name, otherwise some transformation
-            # might have occurred.
-            starred_args.append(arg.value.name)
-        elif isinstance(arg, astroid.Name):
-            args.append(arg.name)
-        else:
-            args.append(None)
-
-    return _CallSignature(args, kws, starred_args, starred_kws)
-
-
-def _signature_from_arguments(arguments):
-    kwarg = arguments.kwarg
-    vararg = arguments.vararg
-    args = [arg.name for arg in arguments.args if arg.name != "self"]
-    kwonlyargs = [arg.name for arg in arguments.kwonlyargs]
-    return _ParameterSignature(args, kwonlyargs, vararg, kwarg)
-
-
-def _definition_equivalent_to_call(definition, call):
-    """Check if a definition signature is equivalent to a call."""
-    if definition.kwargs:
-        same_kw_variadics = definition.kwargs in call.starred_kws
-    else:
-        same_kw_variadics = not call.starred_kws
-    if definition.varargs:
-        same_args_variadics = definition.varargs in call.starred_args
-    else:
-        same_args_variadics = not call.starred_args
-    same_kwonlyargs = all(kw in call.kws for kw in definition.kwonlyargs)
-    same_args = definition.args == call.args
-
-    no_additional_kwarg_arguments = True
-    if call.kws:
-        for keyword in call.kws:
-            is_arg = keyword in call.args
-            is_kwonly = keyword in definition.kwonlyargs
-            if not is_arg and not is_kwonly:
-                # Maybe this argument goes into **kwargs,
-                # or it is an extraneous argument.
-                # In any case, the signature is different than
-                # the call site, which stops our search.
-                no_additional_kwarg_arguments = False
-                break
-
-    return all(
-        (
-            same_args,
-            same_kwonlyargs,
-            same_args_variadics,
-            same_kw_variadics,
-            no_additional_kwarg_arguments,
-        )
-    )
-
-
-# Deal with parameters overridding in two methods.
-
-
-def _positional_parameters(method):
-    positional = method.args.args
-    if method.type in ("classmethod", "method"):
-        positional = positional[1:]
-    return positional
-
-
-def _get_node_type(node, potential_types):
-    """
-    Return the type of the node if it exists in potential_types.
-
-    Args:
-        node (astroid.node): node to get the type of.
-        potential_types (tuple): potential types of the node.
-
-    Returns:
-        type: type of the node or None.
-    """
-    for potential_type in potential_types:
-        if isinstance(node, potential_type):
-            return potential_type
-    return None
-
-
-def _check_arg_equality(node_a, node_b, attr_name):
-    """
-    Check equality of nodes based on the comparison of their attributes named attr_name.
-
-    Args:
-        node_a (astroid.node): first node to compare.
-        node_b (astroid.node): second node to compare.
-        attr_name (str): name of the nodes attribute to use for comparison.
-
-    Returns:
-        bool: True if node_a.attr_name == node_b.attr_name, False otherwise.
-    """
-    return getattr(node_a, attr_name) == getattr(node_b, attr_name)
-
-
-def _has_different_parameters_default_value(original, overridden):
-    """
-    Check if original and overridden methods arguments have different default values
-
-    Return True if one of the overridden arguments has a default
-    value different from the default value of the original argument
-    If one of the method doesn't have argument (.args is None)
-    return False
-    """
-    if original.args is None or overridden.args is None:
-        return False
-
-    all_args = chain(original.args, original.kwonlyargs)
-    original_param_names = [param.name for param in all_args]
-    default_missing = object()
-    for param_name in original_param_names:
-        try:
-            original_default = original.default_value(param_name)
-        except astroid.exceptions.NoDefault:
-            original_default = default_missing
-        try:
-            overridden_default = overridden.default_value(param_name)
-        except astroid.exceptions.NoDefault:
-            overridden_default = default_missing
-
-        default_list = [
-            arg == default_missing for arg in (original_default, overridden_default)
-        ]
-        if any(default_list) and not all(default_list):
-            # Only one arg has no default value
-            return True
-
-        astroid_type_compared_attr = {
-            astroid.Const: "value",
-            astroid.ClassDef: "name",
-            astroid.Tuple: "elts",
-            astroid.List: "elts",
-        }
-        handled_types = tuple(
-            astroid_type for astroid_type in astroid_type_compared_attr
-        )
-        original_type = _get_node_type(original_default, handled_types)
-        if original_type:
-            #  We handle only astroid types that are inside the dict astroid_type_compared_attr
-            if not isinstance(overridden_default, original_type):
-                #  Two args with same name but different types
-                return True
-            if not _check_arg_equality(
-                original_default,
-                overridden_default,
-                astroid_type_compared_attr[original_type],
-            ):
-                # Two args with same type but different values
-                return True
-    return False
-
-
-def _has_different_parameters(original, overridden, dummy_parameter_regex):
-    zipped = zip_longest(original, overridden)
-    for original_param, overridden_param in zipped:
-        params = (original_param, overridden_param)
-        if not all(params):
-            return True
-
-        names = [param.name for param in params]
-        if any(map(dummy_parameter_regex.match, names)):
-            continue
-        if original_param.name != overridden_param.name:
-            return True
-    return False
-
-
-def _different_parameters(original, overridden, dummy_parameter_regex):
-    """Determine if the two methods have different parameters
-
-    They are considered to have different parameters if:
-
-       * they have different positional parameters, including different names
-
-       * one of the methods is having variadics, while the other is not
-
-       * they have different keyword only parameters.
-
-    """
-    original_parameters = _positional_parameters(original)
-    overridden_parameters = _positional_parameters(overridden)
-
-    different_positional = _has_different_parameters(
-        original_parameters, overridden_parameters, dummy_parameter_regex
-    )
-    different_kwonly = _has_different_parameters(
-        original.args.kwonlyargs, overridden.args.kwonlyargs, dummy_parameter_regex
-    )
-    if original.name in PYMETHODS:
-        # Ignore the difference for special methods. If the parameter
-        # numbers are different, then that is going to be caught by
-        # unexpected-special-method-signature.
-        # If the names are different, it doesn't matter, since they can't
-        # be used as keyword arguments anyway.
-        different_positional = different_kwonly = False
-
-    # Both or none should have extra variadics, otherwise the method
-    # loses or gains capabilities that are not reflected into the parent method,
-    # leading to potential inconsistencies in the code.
-    different_kwarg = (
-        sum(1 for param in (original.args.kwarg, overridden.args.kwarg) if not param)
-        == 1
-    )
-    different_vararg = (
-        sum(1 for param in (original.args.vararg, overridden.args.vararg) if not param)
-        == 1
-    )
-
-    return any(
-        (different_positional, different_kwarg, different_vararg, different_kwonly)
-    )
-
-
-def _is_invalid_base_class(cls):
-    return cls.name in INVALID_BASE_CLASSES and is_builtin_object(cls)
-
-
-def _has_data_descriptor(cls, attr):
-    attributes = cls.getattr(attr)
-    for attribute in attributes:
-        try:
-            for inferred in attribute.infer():
-                if isinstance(inferred, astroid.Instance):
-                    try:
-                        inferred.getattr("__get__")
-                        inferred.getattr("__set__")
-                    except astroid.NotFoundError:
-                        continue
-                    else:
-                        return True
-        except astroid.InferenceError:
-            # Can't infer, avoid emitting a false positive in this case.
-            return True
-    return False
-
-
-def _called_in_methods(func, klass, methods):
-    """ Check if the func was called in any of the given methods,
-    belonging to the *klass*. Returns True if so, False otherwise.
-    """
-    if not isinstance(func, astroid.FunctionDef):
-        return False
-    for method in methods:
-        try:
-            inferred = klass.getattr(method)
-        except astroid.NotFoundError:
-            continue
-        for infer_method in inferred:
-            for call in infer_method.nodes_of_class(astroid.Call):
-                try:
-                    bound = next(call.func.infer())
-                except (astroid.InferenceError, StopIteration):
-                    continue
-                if not isinstance(bound, astroid.BoundMethod):
-                    continue
-                func_obj = bound._proxied
-                if isinstance(func_obj, astroid.UnboundMethod):
-                    func_obj = func_obj._proxied
-                if func_obj.name == func.name:
-                    return True
-    return False
-
-
-def _is_attribute_property(name, klass):
-    """ Check if the given attribute *name* is a property
-    in the given *klass*.
-
-    It will look for `property` calls or for functions
-    with the given name, decorated by `property` or `property`
-    subclasses.
-    Returns ``True`` if the name is a property in the given klass,
-    ``False`` otherwise.
-    """
-
-    try:
-        attributes = klass.getattr(name)
-    except astroid.NotFoundError:
-        return False
-    property_name = "{}.property".format(BUILTINS)
-    for attr in attributes:
-        if attr is astroid.Uninferable:
-            continue
-        try:
-            inferred = next(attr.infer())
-        except astroid.InferenceError:
-            continue
-        if isinstance(inferred, astroid.FunctionDef) and decorated_with_property(
-            inferred
-        ):
-            return True
-        if inferred.pytype() == property_name:
-            return True
-    return False
-
-
-def _has_bare_super_call(fundef_node):
-    for call in fundef_node.nodes_of_class(astroid.Call):
-        func = call.func
-        if isinstance(func, astroid.Name) and func.name == "super" and not call.args:
-            return True
-    return False
-
-
-def _safe_infer_call_result(node, caller, context=None):
-    """
-    Safely infer the return value of a function.
-
-    Returns None if inference failed or if there is some ambiguity (more than
-    one node has been inferred). Otherwise returns inferred value.
-    """
-    try:
-        inferit = node.infer_call_result(caller, context=context)
-        value = next(inferit)
-    except astroid.InferenceError:
-        return None  # inference failed
-    except StopIteration:
-        return None  # no values inferred
-    try:
-        next(inferit)
-        return None  # there is ambiguity on the inferred node
-    except astroid.InferenceError:
-        return None  # there is some kind of ambiguity
-    except StopIteration:
-        return value
-
-
-def _has_same_layout_slots(slots, assigned_value):
-    inferred = next(assigned_value.infer())
-    if isinstance(inferred, astroid.ClassDef):
-        other_slots = inferred.slots()
-        if all(
-            first_slot and second_slot and first_slot.value == second_slot.value
-            for (first_slot, second_slot) in zip_longest(slots, other_slots)
-        ):
-            return True
-    return False
-
-
-MSGS = {
-    "F0202": (
-        "Unable to check methods signature (%s / %s)",
-        "method-check-failed",
-        "Used when Pylint has been unable to check methods signature "
-        "compatibility for an unexpected reason. Please report this kind "
-        "if you don't make sense of it.",
-    ),
-    "E0202": (
-        "An attribute defined in %s line %s hides this method",
-        "method-hidden",
-        "Used when a class defines a method which is hidden by an "
-        "instance attribute from an ancestor class or set by some "
-        "client code.",
-    ),
-    "E0203": (
-        "Access to member %r before its definition line %s",
-        "access-member-before-definition",
-        "Used when an instance member is accessed before it's actually assigned.",
-    ),
-    "W0201": (
-        "Attribute %r defined outside __init__",
-        "attribute-defined-outside-init",
-        "Used when an instance attribute is defined outside the __init__ method.",
-    ),
-    "W0212": (
-        "Access to a protected member %s of a client class",  # E0214
-        "protected-access",
-        "Used when a protected member (i.e. class member with a name "
-        "beginning with an underscore) is access outside the class or a "
-        "descendant of the class where it's defined.",
-    ),
-    "E0211": (
-        "Method has no argument",
-        "no-method-argument",
-        "Used when a method which should have the bound instance as "
-        "first argument has no argument defined.",
-    ),
-    "E0213": (
-        'Method should have "self" as first argument',
-        "no-self-argument",
-        'Used when a method has an attribute different the "self" as '
-        "first argument. This is considered as an error since this is "
-        "a so common convention that you shouldn't break it!",
-    ),
-    "C0202": (
-        "Class method %s should have %s as first argument",
-        "bad-classmethod-argument",
-        "Used when a class method has a first argument named differently "
-        "than the value specified in valid-classmethod-first-arg option "
-        '(default to "cls"), recommended to easily differentiate them '
-        "from regular instance methods.",
-    ),
-    "C0203": (
-        "Metaclass method %s should have %s as first argument",
-        "bad-mcs-method-argument",
-        "Used when a metaclass method has a first argument named "
-        "differently than the value specified in valid-classmethod-first"
-        '-arg option (default to "cls"), recommended to easily '
-        "differentiate them from regular instance methods.",
-    ),
-    "C0204": (
-        "Metaclass class method %s should have %s as first argument",
-        "bad-mcs-classmethod-argument",
-        "Used when a metaclass class method has a first argument named "
-        "differently than the value specified in valid-metaclass-"
-        'classmethod-first-arg option (default to "mcs"), recommended to '
-        "easily differentiate them from regular instance methods.",
-    ),
-    "W0211": (
-        "Static method with %r as first argument",
-        "bad-staticmethod-argument",
-        'Used when a static method has "self" or a value specified in '
-        "valid-classmethod-first-arg option or "
-        "valid-metaclass-classmethod-first-arg option as first argument.",
-    ),
-    "R0201": (
-        "Method could be a function",
-        "no-self-use",
-        "Used when a method doesn't use its bound instance, and so could "
-        "be written as a function.",
-    ),
-    "W0221": (
-        "Parameters differ from %s %r method",
-        "arguments-differ",
-        "Used when a method has a different number of arguments than in "
-        "the implemented interface or in an overridden method.",
-    ),
-    "W0222": (
-        "Signature differs from %s %r method",
-        "signature-differs",
-        "Used when a method signature is different than in the "
-        "implemented interface or in an overridden method.",
-    ),
-    "W0223": (
-        "Method %r is abstract in class %r but is not overridden",
-        "abstract-method",
-        "Used when an abstract method (i.e. raise NotImplementedError) is "
-        "not overridden in concrete class.",
-    ),
-    "W0231": (
-        "__init__ method from base class %r is not called",
-        "super-init-not-called",
-        "Used when an ancestor class method has an __init__ method "
-        "which is not called by a derived class.",
-    ),
-    "W0232": (
-        "Class has no __init__ method",
-        "no-init",
-        "Used when a class has no __init__ method, neither its parent classes.",
-    ),
-    "W0233": (
-        "__init__ method from a non direct base class %r is called",
-        "non-parent-init-called",
-        "Used when an __init__ method is called on a class which is not "
-        "in the direct ancestors for the analysed class.",
-    ),
-    "W0235": (
-        "Useless super delegation in method %r",
-        "useless-super-delegation",
-        "Used whenever we can detect that an overridden method is useless, "
-        "relying on super() delegation to do the same thing as another method "
-        "from the MRO.",
-    ),
-    "W0236": (
-        "Method %r was expected to be %r, found it instead as %r",
-        "invalid-overridden-method",
-        "Used when we detect that a method was overridden as a property "
-        "or the other way around, which could result in potential bugs at "
-        "runtime.",
-    ),
-    "E0236": (
-        "Invalid object %r in __slots__, must contain only non empty strings",
-        "invalid-slots-object",
-        "Used when an invalid (non-string) object occurs in __slots__.",
-    ),
-    "E0237": (
-        "Assigning to attribute %r not defined in class slots",
-        "assigning-non-slot",
-        "Used when assigning to an attribute not defined in the class slots.",
-    ),
-    "E0238": (
-        "Invalid __slots__ object",
-        "invalid-slots",
-        "Used when an invalid __slots__ is found in class. "
-        "Only a string, an iterable or a sequence is permitted.",
-    ),
-    "E0239": (
-        "Inheriting %r, which is not a class.",
-        "inherit-non-class",
-        "Used when a class inherits from something which is not a class.",
-    ),
-    "E0240": (
-        "Inconsistent method resolution order for class %r",
-        "inconsistent-mro",
-        "Used when a class has an inconsistent method resolution order.",
-    ),
-    "E0241": (
-        "Duplicate bases for class %r",
-        "duplicate-bases",
-        "Used when a class has duplicate bases.",
-    ),
-    "E0242": (
-        "Value %r in slots conflicts with class variable",
-        "class-variable-slots-conflict",
-        "Used when a value in __slots__ conflicts with a class variable, property or method.",
-    ),
-    "R0202": (
-        "Consider using a decorator instead of calling classmethod",
-        "no-classmethod-decorator",
-        "Used when a class method is defined without using the decorator syntax.",
-    ),
-    "R0203": (
-        "Consider using a decorator instead of calling staticmethod",
-        "no-staticmethod-decorator",
-        "Used when a static method is defined without using the decorator syntax.",
-    ),
-    "C0205": (
-        "Class __slots__ should be a non-string iterable",
-        "single-string-used-for-slots",
-        "Used when a class __slots__ is a simple string, rather than an iterable.",
-    ),
-    "R0205": (
-        "Class %r inherits from object, can be safely removed from bases in python3",
-        "useless-object-inheritance",
-        "Used when a class inherit from object, which under python3 is implicit, "
-        "hence can be safely removed from bases.",
-    ),
-    "R0206": (
-        "Cannot have defined parameters for properties",
-        "property-with-parameters",
-        "Used when we detect that a property also has parameters, which are useless, "
-        "given that properties cannot be called with additional arguments.",
-    ),
-}
-
-
-class ScopeAccessMap:
-    """Store the accessed variables per scope."""
-
-    def __init__(self):
-        self._scopes = collections.defaultdict(lambda: collections.defaultdict(list))
-
-    def set_accessed(self, node):
-        """Set the given node as accessed."""
-
-        frame = node_frame_class(node)
-        if frame is None:
-            # The node does not live in a class.
-            return
-        self._scopes[frame][node.attrname].append(node)
-
-    def accessed(self, scope):
-        """Get the accessed variables for the given scope."""
-        return self._scopes.get(scope, {})
-
-
-class ClassChecker(BaseChecker):
-    """checks for :
-    * methods without self as first argument
-    * overridden methods signature
-    * access only to existent members via self
-    * attributes not defined in the __init__ method
-    * unreachable code
-    """
-
-    __implements__ = (IAstroidChecker,)
-
-    # configuration section name
-    name = "classes"
-    # messages
-    msgs = MSGS
-    priority = -2
-    # configuration options
-    options = (
-        (
-            "defining-attr-methods",
-            {
-                "default": ("__init__", "__new__", "setUp", "__post_init__"),
-                "type": "csv",
-                "metavar": "<method names>",
-                "help": "List of method names used to declare (i.e. assign) \
-instance attributes.",
-            },
-        ),
-        (
-            "valid-classmethod-first-arg",
-            {
-                "default": ("cls",),
-                "type": "csv",
-                "metavar": "<argument names>",
-                "help": "List of valid names for the first argument in \
-a class method.",
-            },
-        ),
-        (
-            "valid-metaclass-classmethod-first-arg",
-            {
-                "default": ("cls",),
-                "type": "csv",
-                "metavar": "<argument names>",
-                "help": "List of valid names for the first argument in \
-a metaclass class method.",
-            },
-        ),
-        (
-            "exclude-protected",
-            {
-                "default": (
-                    # namedtuple public API.
-                    "_asdict",
-                    "_fields",
-                    "_replace",
-                    "_source",
-                    "_make",
-                ),
-                "type": "csv",
-                "metavar": "<protected access exclusions>",
-                "help": (
-                    "List of member names, which should be excluded "
-                    "from the protected access warning."
-                ),
-            },
-        ),
-    )
-
-    def __init__(self, linter=None):
-        BaseChecker.__init__(self, linter)
-        self._accessed = ScopeAccessMap()
-        self._first_attrs = []
-        self._meth_could_be_func = None
-
-    @decorators.cachedproperty
-    def _dummy_rgx(self):
-        return get_global_option(self, "dummy-variables-rgx", default=None)
-
-    @decorators.cachedproperty
-    def _ignore_mixin(self):
-        return get_global_option(self, "ignore-mixin-members", default=True)
-
-    @check_messages(
-        "abstract-method",
-        "no-init",
-        "invalid-slots",
-        "single-string-used-for-slots",
-        "invalid-slots-object",
-        "class-variable-slots-conflict",
-        "inherit-non-class",
-        "useless-object-inheritance",
-        "inconsistent-mro",
-        "duplicate-bases",
-    )
-    def visit_classdef(self, node):
-        """init visit variable _accessed
-        """
-        self._check_bases_classes(node)
-        # if not an exception or a metaclass
-        if node.type == "class" and has_known_bases(node):
-            try:
-                node.local_attr("__init__")
-            except astroid.NotFoundError:
-                self.add_message("no-init", args=node, node=node)
-        self._check_slots(node)
-        self._check_proper_bases(node)
-        self._check_consistent_mro(node)
-
-    def _check_consistent_mro(self, node):
-        """Detect that a class has a consistent mro or duplicate bases."""
-        try:
-            node.mro()
-        except InconsistentMroError:
-            self.add_message("inconsistent-mro", args=node.name, node=node)
-        except DuplicateBasesError:
-            self.add_message("duplicate-bases", args=node.name, node=node)
-        except NotImplementedError:
-            # Old style class, there's no mro so don't do anything.
-            pass
-
-    def _check_proper_bases(self, node):
-        """
-        Detect that a class inherits something which is not
-        a class or a type.
-        """
-        for base in node.bases:
-            ancestor = safe_infer(base)
-            if ancestor in (astroid.Uninferable, None):
-                continue
-            if isinstance(ancestor, astroid.Instance) and ancestor.is_subtype_of(
-                "%s.type" % (BUILTINS,)
-            ):
-                continue
-
-            if not isinstance(ancestor, astroid.ClassDef) or _is_invalid_base_class(
-                ancestor
-            ):
-                self.add_message("inherit-non-class", args=base.as_string(), node=node)
-
-            if ancestor.name == object.__name__:
-                self.add_message(
-                    "useless-object-inheritance", args=node.name, node=node
-                )
-
-    def leave_classdef(self, cnode):
-        """close a class node:
-        check that instance attributes are defined in __init__ and check
-        access to existent members
-        """
-        # check access to existent members on non metaclass classes
-        if self._ignore_mixin and cnode.name[-5:].lower() == "mixin":
-            # We are in a mixin class. No need to try to figure out if
-            # something is missing, since it is most likely that it will
-            # miss.
-            return
-
-        accessed = self._accessed.accessed(cnode)
-        if cnode.type != "metaclass":
-            self._check_accessed_members(cnode, accessed)
-        # checks attributes are defined in an allowed method such as __init__
-        if not self.linter.is_message_enabled("attribute-defined-outside-init"):
-            return
-        defining_methods = self.config.defining_attr_methods
-        current_module = cnode.root()
-        for attr, nodes in cnode.instance_attrs.items():
-            # Exclude `__dict__` as it is already defined.
-            if attr == "__dict__":
-                continue
-
-            # Skip nodes which are not in the current module and it may screw up
-            # the output, while it's not worth it
-            nodes = [
-                n
-                for n in nodes
-                if not isinstance(n.statement(), (astroid.Delete, astroid.AugAssign))
-                and n.root() is current_module
-            ]
-            if not nodes:
-                continue  # error detected by typechecking
-
-            # Check if any method attr is defined in is a defining method
-            # or if we have the attribute defined in a setter.
-            frames = (node.frame() for node in nodes)
-            if any(
-                frame.name in defining_methods or is_property_setter(frame)
-                for frame in frames
-            ):
-                continue
-
-            # check attribute is defined in a parent's __init__
-            for parent in cnode.instance_attr_ancestors(attr):
-                attr_defined = False
-                # check if any parent method attr is defined in is a defining method
-                for node in parent.instance_attrs[attr]:
-                    if node.frame().name in defining_methods:
-                        attr_defined = True
-                if attr_defined:
-                    # we're done :)
-                    break
-            else:
-                # check attribute is defined as a class attribute
-                try:
-                    cnode.local_attr(attr)
-                except astroid.NotFoundError:
-                    for node in nodes:
-                        if node.frame().name not in defining_methods:
-                            # If the attribute was set by a call in any
-                            # of the defining methods, then don't emit
-                            # the warning.
-                            if _called_in_methods(
-                                node.frame(), cnode, defining_methods
-                            ):
-                                continue
-                            self.add_message(
-                                "attribute-defined-outside-init", args=attr, node=node
-                            )
-
-    def visit_functiondef(self, node):
-        """check method arguments, overriding"""
-        # ignore actual functions
-        if not node.is_method():
-            return
-
-        self._check_useless_super_delegation(node)
-        self._check_property_with_parameters(node)
-
-        klass = node.parent.frame()
-        self._meth_could_be_func = True
-        # check first argument is self if this is actually a method
-        self._check_first_arg_for_type(node, klass.type == "metaclass")
-        if node.name == "__init__":
-            self._check_init(node)
-            return
-        # check signature if the method overloads inherited method
-        for overridden in klass.local_attr_ancestors(node.name):
-            # get astroid for the searched method
-            try:
-                parent_function = overridden[node.name]
-            except KeyError:
-                # we have found the method but it's not in the local
-                # dictionary.
-                # This may happen with astroid build from living objects
-                continue
-            if not isinstance(parent_function, astroid.FunctionDef):
-                continue
-            self._check_signature(node, parent_function, "overridden", klass)
-            self._check_invalid_overridden_method(node, parent_function)
-            break
-
-        if node.decorators:
-            for decorator in node.decorators.nodes:
-                if isinstance(decorator, astroid.Attribute) and decorator.attrname in (
-                    "getter",
-                    "setter",
-                    "deleter",
-                ):
-                    # attribute affectation will call this method, not hiding it
-                    return
-                if isinstance(decorator, astroid.Name):
-                    if decorator.name == "property":
-                        # attribute affectation will either call a setter or raise
-                        # an attribute error, anyway not hiding the function
-                        return
-
-                # Infer the decorator and see if it returns something useful
-                inferred = safe_infer(decorator)
-                if not inferred:
-                    return
-                if isinstance(inferred, astroid.FunctionDef):
-                    # Okay, it's a decorator, let's see what it can infer.
-                    try:
-                        inferred = next(inferred.infer_call_result(inferred))
-                    except astroid.InferenceError:
-                        return
-                try:
-                    if (
-                        isinstance(inferred, (astroid.Instance, astroid.ClassDef))
-                        and inferred.getattr("__get__")
-                        and inferred.getattr("__set__")
-                    ):
-                        return
-                except astroid.AttributeInferenceError:
-                    pass
-
-        # check if the method is hidden by an attribute
-        try:
-            overridden = klass.instance_attr(node.name)[0]
-            overridden_frame = overridden.frame()
-            if (
-                isinstance(overridden_frame, astroid.FunctionDef)
-                and overridden_frame.type == "method"
-            ):
-                overridden_frame = overridden_frame.parent.frame()
-            if isinstance(overridden_frame, astroid.ClassDef) and klass.is_subtype_of(
-                overridden_frame.qname()
-            ):
-                args = (overridden.root().name, overridden.fromlineno)
-                self.add_message("method-hidden", args=args, node=node)
-        except astroid.NotFoundError:
-            pass
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    def _check_useless_super_delegation(self, function):
-        """Check if the given function node is an useless method override
-
-        We consider it *useless* if it uses the super() builtin, but having
-        nothing additional whatsoever than not implementing the method at all.
-        If the method uses super() to delegate an operation to the rest of the MRO,
-        and if the method called is the same as the current one, the arguments
-        passed to super() are the same as the parameters that were passed to
-        this method, then the method could be removed altogether, by letting
-        other implementation to take precedence.
-        """
-
-        if (
-            not function.is_method()
-            # With decorators is a change of use
-            or function.decorators
-        ):
-            return
-
-        body = function.body
-        if len(body) != 1:
-            # Multiple statements, which means this overridden method
-            # could do multiple things we are not aware of.
-            return
-
-        statement = body[0]
-        if not isinstance(statement, (astroid.Expr, astroid.Return)):
-            # Doing something else than what we are interested into.
-            return
-
-        call = statement.value
-        if (
-            not isinstance(call, astroid.Call)
-            # Not a super() attribute access.
-            or not isinstance(call.func, astroid.Attribute)
-        ):
-            return
-
-        # Should be a super call.
-        try:
-            super_call = next(call.func.expr.infer())
-        except astroid.InferenceError:
-            return
-        else:
-            if not isinstance(super_call, objects.Super):
-                return
-
-        # The name should be the same.
-        if call.func.attrname != function.name:
-            return
-
-        # Should be a super call with the MRO pointer being the
-        # current class and the type being the current instance.
-        current_scope = function.parent.scope()
-        if (
-            super_call.mro_pointer != current_scope
-            or not isinstance(super_call.type, astroid.Instance)
-            or super_call.type.name != current_scope.name
-        ):
-            return
-
-        #  Check values of default args
-        klass = function.parent.frame()
-        meth_node = None
-        for overridden in klass.local_attr_ancestors(function.name):
-            # get astroid for the searched method
-            try:
-                meth_node = overridden[function.name]
-            except KeyError:
-                # we have found the method but it's not in the local
-                # dictionary.
-                # This may happen with astroid build from living objects
-                continue
-            if (
-                not isinstance(meth_node, astroid.FunctionDef)
-                # If the method have an ancestor which is not a
-                # function then it is legitimate to redefine it
-                or _has_different_parameters_default_value(
-                    meth_node.args, function.args
-                )
-            ):
-                return
-            break
-
-        # Detect if the parameters are the same as the call's arguments.
-        params = _signature_from_arguments(function.args)
-        args = _signature_from_call(call)
-
-        if meth_node is not None:
-
-            def form_annotations(annotations):
-                return [
-                    annotation.as_string() for annotation in filter(None, annotations)
-                ]
-
-            called_annotations = form_annotations(function.args.annotations)
-            overridden_annotations = form_annotations(meth_node.args.annotations)
-            if called_annotations and overridden_annotations:
-                if called_annotations != overridden_annotations:
-                    return
-
-        if _definition_equivalent_to_call(params, args):
-            self.add_message(
-                "useless-super-delegation", node=function, args=(function.name,)
-            )
-
-    def _check_property_with_parameters(self, node):
-        if node.args.args and len(node.args.args) > 1 and decorated_with_property(node):
-            self.add_message("property-with-parameters", node=node)
-
-    def _check_invalid_overridden_method(self, function_node, parent_function_node):
-        parent_is_property = decorated_with_property(
-            parent_function_node
-        ) or is_property_setter_or_deleter(parent_function_node)
-        current_is_property = decorated_with_property(
-            function_node
-        ) or is_property_setter_or_deleter(function_node)
-        if parent_is_property and not current_is_property:
-            self.add_message(
-                "invalid-overridden-method",
-                args=(function_node.name, "property", function_node.type),
-                node=function_node,
-            )
-        elif not parent_is_property and current_is_property:
-            self.add_message(
-                "invalid-overridden-method",
-                args=(function_node.name, "method", "property"),
-                node=function_node,
-            )
-
-    def _check_slots(self, node):
-        if "__slots__" not in node.locals:
-            return
-        for slots in node.igetattr("__slots__"):
-            # check if __slots__ is a valid type
-            if slots is astroid.Uninferable:
-                continue
-            if not is_iterable(slots) and not is_comprehension(slots):
-                self.add_message("invalid-slots", node=node)
-                continue
-
-            if isinstance(slots, astroid.Const):
-                # a string, ignore the following checks
-                self.add_message("single-string-used-for-slots", node=node)
-                continue
-            if not hasattr(slots, "itered"):
-                # we can't obtain the values, maybe a .deque?
-                continue
-
-            if isinstance(slots, astroid.Dict):
-                values = [item[0] for item in slots.items]
-            else:
-                values = slots.itered()
-            if values is astroid.Uninferable:
-                return
-            for elt in values:
-                try:
-                    self._check_slots_elt(elt, node)
-                except astroid.InferenceError:
-                    continue
-
-    def _check_slots_elt(self, elt, node):
-        for inferred in elt.infer():
-            if inferred is astroid.Uninferable:
-                continue
-            if not isinstance(inferred, astroid.Const) or not isinstance(
-                inferred.value, str
-            ):
-                self.add_message(
-                    "invalid-slots-object", args=inferred.as_string(), node=elt
-                )
-                continue
-            if not inferred.value:
-                self.add_message(
-                    "invalid-slots-object", args=inferred.as_string(), node=elt
-                )
-
-            # Check if we have a conflict with a class variable.
-            class_variable = node.locals.get(inferred.value)
-            if class_variable:
-                # Skip annotated assignments which don't conflict at all with slots.
-                if len(class_variable) == 1:
-                    parent = class_variable[0].parent
-                    if isinstance(parent, astroid.AnnAssign) and parent.value is None:
-                        return
-                self.add_message(
-                    "class-variable-slots-conflict", args=(inferred.value,), node=elt
-                )
-
-    def leave_functiondef(self, node):
-        """on method node, check if this method couldn't be a function
-
-        ignore class, static and abstract methods, initializer,
-        methods overridden from a parent class.
-        """
-        if node.is_method():
-            if node.args.args is not None:
-                self._first_attrs.pop()
-            if not self.linter.is_message_enabled("no-self-use"):
-                return
-            class_node = node.parent.frame()
-            if (
-                self._meth_could_be_func
-                and node.type == "method"
-                and node.name not in PYMETHODS
-                and not (
-                    node.is_abstract()
-                    or overrides_a_method(class_node, node.name)
-                    or decorated_with_property(node)
-                    or _has_bare_super_call(node)
-                    or is_protocol_class(class_node)
-                )
-            ):
-                self.add_message("no-self-use", node=node)
-
-    def visit_attribute(self, node):
-        """check if the getattr is an access to a class member
-        if so, register it. Also check for access to protected
-        class member from outside its class (but ignore __special__
-        methods)
-        """
-        # Check self
-        if self._uses_mandatory_method_param(node):
-            self._accessed.set_accessed(node)
-            return
-        if not self.linter.is_message_enabled("protected-access"):
-            return
-
-        self._check_protected_attribute_access(node)
-
-    def visit_assignattr(self, node):
-        if isinstance(
-            node.assign_type(), astroid.AugAssign
-        ) and self._uses_mandatory_method_param(node):
-            self._accessed.set_accessed(node)
-        self._check_in_slots(node)
-
-    def _check_in_slots(self, node):
-        """ Check that the given AssignAttr node
-        is defined in the class slots.
-        """
-        inferred = safe_infer(node.expr)
-        if not isinstance(inferred, astroid.Instance):
-            return
-
-        klass = inferred._proxied
-        if not has_known_bases(klass):
-            return
-        if "__slots__" not in klass.locals or not klass.newstyle:
-            return
-
-        slots = klass.slots()
-        if slots is None:
-            return
-        # If any ancestor doesn't use slots, the slots
-        # defined for this class are superfluous.
-        if any(
-            "__slots__" not in ancestor.locals and ancestor.name != "object"
-            for ancestor in klass.ancestors()
-        ):
-            return
-
-        if not any(slot.value == node.attrname for slot in slots):
-            # If we have a '__dict__' in slots, then
-            # assigning any name is valid.
-            if not any(slot.value == "__dict__" for slot in slots):
-                if _is_attribute_property(node.attrname, klass):
-                    # Properties circumvent the slots mechanism,
-                    # so we should not emit a warning for them.
-                    return
-                if node.attrname in klass.locals and _has_data_descriptor(
-                    klass, node.attrname
-                ):
-                    # Descriptors circumvent the slots mechanism as well.
-                    return
-                if node.attrname == "__class__" and _has_same_layout_slots(
-                    slots, node.parent.value
-                ):
-                    return
-                self.add_message("assigning-non-slot", args=(node.attrname,), node=node)
-
-    @check_messages(
-        "protected-access", "no-classmethod-decorator", "no-staticmethod-decorator"
-    )
-    def visit_assign(self, assign_node):
-        self._check_classmethod_declaration(assign_node)
-        node = assign_node.targets[0]
-        if not isinstance(node, astroid.AssignAttr):
-            return
-
-        if self._uses_mandatory_method_param(node):
-            return
-        self._check_protected_attribute_access(node)
-
-    def _check_classmethod_declaration(self, node):
-        """Checks for uses of classmethod() or staticmethod()
-
-        When a @classmethod or @staticmethod decorator should be used instead.
-        A message will be emitted only if the assignment is at a class scope
-        and only if the classmethod's argument belongs to the class where it
-        is defined.
-        `node` is an assign node.
-        """
-        if not isinstance(node.value, astroid.Call):
-            return
-
-        # check the function called is "classmethod" or "staticmethod"
-        func = node.value.func
-        if not isinstance(func, astroid.Name) or func.name not in (
-            "classmethod",
-            "staticmethod",
-        ):
-            return
-
-        msg = (
-            "no-classmethod-decorator"
-            if func.name == "classmethod"
-            else "no-staticmethod-decorator"
-        )
-        # assignment must be at a class scope
-        parent_class = node.scope()
-        if not isinstance(parent_class, astroid.ClassDef):
-            return
-
-        # Check if the arg passed to classmethod is a class member
-        classmeth_arg = node.value.args[0]
-        if not isinstance(classmeth_arg, astroid.Name):
-            return
-
-        method_name = classmeth_arg.name
-        if any(method_name == member.name for member in parent_class.mymethods()):
-            self.add_message(msg, node=node.targets[0])
-
-    def _check_protected_attribute_access(self, node):
-        """Given an attribute access node (set or get), check if attribute
-        access is legitimate. Call _check_first_attr with node before calling
-        this method. Valid cases are:
-        * self._attr in a method or cls._attr in a classmethod. Checked by
-        _check_first_attr.
-        * Klass._attr inside "Klass" class.
-        * Klass2._attr inside "Klass" class when Klass2 is a base class of
-            Klass.
-        """
-        attrname = node.attrname
-
-        if (
-            is_attr_protected(attrname)
-            and attrname not in self.config.exclude_protected
-        ):
-
-            klass = node_frame_class(node)
-
-            # In classes, check we are not getting a parent method
-            # through the class object or through super
-            callee = node.expr.as_string()
-
-            # We are not in a class, no remaining valid case
-            if klass is None:
-                self.add_message("protected-access", node=node, args=attrname)
-                return
-
-            # If the expression begins with a call to super, that's ok.
-            if (
-                isinstance(node.expr, astroid.Call)
-                and isinstance(node.expr.func, astroid.Name)
-                and node.expr.func.name == "super"
-            ):
-                return
-
-            # If the expression begins with a call to type(self), that's ok.
-            if self._is_type_self_call(node.expr):
-                return
-
-            # We are in a class, one remaining valid cases, Klass._attr inside
-            # Klass
-            if not (callee == klass.name or callee in klass.basenames):
-                # Detect property assignments in the body of the class.
-                # This is acceptable:
-                #
-                # class A:
-                #     b = property(lambda: self._b)
-
-                stmt = node.parent.statement()
-                if (
-                    isinstance(stmt, astroid.Assign)
-                    and len(stmt.targets) == 1
-                    and isinstance(stmt.targets[0], astroid.AssignName)
-                ):
-                    name = stmt.targets[0].name
-                    if _is_attribute_property(name, klass):
-                        return
-
-                #  A licit use of protected member is inside a special method
-                if not attrname.startswith(
-                    "__"
-                ) and self._is_called_inside_special_method(node):
-                    return
-
-                self.add_message("protected-access", node=node, args=attrname)
-
-    @staticmethod
-    def _is_called_inside_special_method(node: astroid.node_classes.NodeNG) -> bool:
-        """
-        Returns true if the node is located inside a special (aka dunder) method
-        """
-        try:
-            frame_name = node.frame().name
-        except AttributeError:
-            return False
-        return frame_name and frame_name in PYMETHODS
-
-    def _is_type_self_call(self, expr):
-        return (
-            isinstance(expr, astroid.Call)
-            and isinstance(expr.func, astroid.Name)
-            and expr.func.name == "type"
-            and len(expr.args) == 1
-            and self._is_mandatory_method_param(expr.args[0])
-        )
-
-    def visit_name(self, node):
-        """check if the name handle an access to a class member
-        if so, register it
-        """
-        if self._first_attrs and (
-            node.name == self._first_attrs[-1] or not self._first_attrs[-1]
-        ):
-            self._meth_could_be_func = False
-
-    def _check_accessed_members(self, node, accessed):
-        """check that accessed members are defined"""
-        excs = ("AttributeError", "Exception", "BaseException")
-        for attr, nodes in accessed.items():
-            try:
-                # is it a class attribute ?
-                node.local_attr(attr)
-                # yes, stop here
-                continue
-            except astroid.NotFoundError:
-                pass
-            # is it an instance attribute of a parent class ?
-            try:
-                next(node.instance_attr_ancestors(attr))
-                # yes, stop here
-                continue
-            except StopIteration:
-                pass
-            # is it an instance attribute ?
-            try:
-                defstmts = node.instance_attr(attr)
-            except astroid.NotFoundError:
-                pass
-            else:
-                # filter out augment assignment nodes
-                defstmts = [stmt for stmt in defstmts if stmt not in nodes]
-                if not defstmts:
-                    # only augment assignment for this node, no-member should be
-                    # triggered by the typecheck checker
-                    continue
-                # filter defstmts to only pick the first one when there are
-                # several assignments in the same scope
-                scope = defstmts[0].scope()
-                defstmts = [
-                    stmt
-                    for i, stmt in enumerate(defstmts)
-                    if i == 0 or stmt.scope() is not scope
-                ]
-                # if there are still more than one, don't attempt to be smarter
-                # than we can be
-                if len(defstmts) == 1:
-                    defstmt = defstmts[0]
-                    # check that if the node is accessed in the same method as
-                    # it's defined, it's accessed after the initial assignment
-                    frame = defstmt.frame()
-                    lno = defstmt.fromlineno
-                    for _node in nodes:
-                        if (
-                            _node.frame() is frame
-                            and _node.fromlineno < lno
-                            and not astroid.are_exclusive(
-                                _node.statement(), defstmt, excs
-                            )
-                        ):
-                            self.add_message(
-                                "access-member-before-definition",
-                                node=_node,
-                                args=(attr, lno),
-                            )
-
-    def _check_first_arg_for_type(self, node, metaclass=0):
-        """check the name of first argument, expect:
-
-        * 'self' for a regular method
-        * 'cls' for a class method or a metaclass regular method (actually
-          valid-classmethod-first-arg value)
-        * 'mcs' for a metaclass class method (actually
-          valid-metaclass-classmethod-first-arg)
-        * not one of the above for a static method
-        """
-        # don't care about functions with unknown argument (builtins)
-        if node.args.args is None:
-            return
-        if node.args.args:
-            first_arg = node.argnames()[0]
-        elif node.args.posonlyargs:
-            first_arg = node.args.posonlyargs[0].name
-        else:
-            first_arg = None
-        self._first_attrs.append(first_arg)
-        first = self._first_attrs[-1]
-        # static method
-        if node.type == "staticmethod":
-            if (
-                first_arg == "self"
-                or first_arg in self.config.valid_classmethod_first_arg
-                or first_arg in self.config.valid_metaclass_classmethod_first_arg
-            ):
-                self.add_message("bad-staticmethod-argument", args=first, node=node)
-                return
-            self._first_attrs[-1] = None
-        # class / regular method with no args
-        elif not node.args.args and not node.args.posonlyargs:
-            self.add_message("no-method-argument", node=node)
-        # metaclass
-        elif metaclass:
-            # metaclass __new__ or classmethod
-            if node.type == "classmethod":
-                self._check_first_arg_config(
-                    first,
-                    self.config.valid_metaclass_classmethod_first_arg,
-                    node,
-                    "bad-mcs-classmethod-argument",
-                    node.name,
-                )
-            # metaclass regular method
-            else:
-                self._check_first_arg_config(
-                    first,
-                    self.config.valid_classmethod_first_arg,
-                    node,
-                    "bad-mcs-method-argument",
-                    node.name,
-                )
-        # regular class
-        else:
-            # class method
-            if node.type == "classmethod" or node.name == "__class_getitem__":
-                self._check_first_arg_config(
-                    first,
-                    self.config.valid_classmethod_first_arg,
-                    node,
-                    "bad-classmethod-argument",
-                    node.name,
-                )
-            # regular method without self as argument
-            elif first != "self":
-                self.add_message("no-self-argument", node=node)
-
-    def _check_first_arg_config(self, first, config, node, message, method_name):
-        if first not in config:
-            if len(config) == 1:
-                valid = repr(config[0])
-            else:
-                valid = ", ".join(repr(v) for v in config[:-1])
-                valid = "%s or %r" % (valid, config[-1])
-            self.add_message(message, args=(method_name, valid), node=node)
-
-    def _check_bases_classes(self, node):
-        """check that the given class node implements abstract methods from
-        base classes
-        """
-
-        def is_abstract(method):
-            return method.is_abstract(pass_is_abstract=False)
-
-        # check if this class abstract
-        if class_is_abstract(node):
-            return
-
-        methods = sorted(
-            unimplemented_abstract_methods(node, is_abstract).items(),
-            key=lambda item: item[0],
-        )
-        for name, method in methods:
-            owner = method.parent.frame()
-            if owner is node:
-                continue
-            # owner is not this class, it must be a parent class
-            # check that the ancestor's method is not abstract
-            if name in node.locals:
-                # it is redefined as an attribute or with a descriptor
-                continue
-            self.add_message("abstract-method", node=node, args=(name, owner.name))
-
-    def _check_init(self, node):
-        """check that the __init__ method call super or ancestors'__init__
-        method (unless it is used for type hinting with `typing.overload`)
-        """
-        if not self.linter.is_message_enabled(
-            "super-init-not-called"
-        ) and not self.linter.is_message_enabled("non-parent-init-called"):
-            return
-        klass_node = node.parent.frame()
-        to_call = _ancestors_to_call(klass_node)
-        not_called_yet = dict(to_call)
-        for stmt in node.nodes_of_class(astroid.Call):
-            expr = stmt.func
-            if not isinstance(expr, astroid.Attribute) or expr.attrname != "__init__":
-                continue
-            # skip the test if using super
-            if (
-                isinstance(expr.expr, astroid.Call)
-                and isinstance(expr.expr.func, astroid.Name)
-                and expr.expr.func.name == "super"
-            ):
-                return
-            try:
-                for klass in expr.expr.infer():
-                    if klass is astroid.Uninferable:
-                        continue
-                    # The inferred klass can be super(), which was
-                    # assigned to a variable and the `__init__`
-                    # was called later.
-                    #
-                    # base = super()
-                    # base.__init__(...)
-
-                    if (
-                        isinstance(klass, astroid.Instance)
-                        and isinstance(klass._proxied, astroid.ClassDef)
-                        and is_builtin_object(klass._proxied)
-                        and klass._proxied.name == "super"
-                    ):
-                        return
-                    if isinstance(klass, objects.Super):
-                        return
-                    try:
-                        del not_called_yet[klass]
-                    except KeyError:
-                        if klass not in to_call:
-                            self.add_message(
-                                "non-parent-init-called", node=expr, args=klass.name
-                            )
-            except astroid.InferenceError:
-                continue
-        for klass, method in not_called_yet.items():
-            if decorated_with(node, ["typing.overload"]):
-                continue
-            cls = node_frame_class(method)
-            if klass.name == "object" or (cls and cls.name == "object"):
-                continue
-            self.add_message("super-init-not-called", args=klass.name, node=node)
-
-    def _check_signature(self, method1, refmethod, class_type, cls):
-        """check that the signature of the two given methods match
-        """
-        if not (
-            isinstance(method1, astroid.FunctionDef)
-            and isinstance(refmethod, astroid.FunctionDef)
-        ):
-            self.add_message(
-                "method-check-failed", args=(method1, refmethod), node=method1
-            )
-            return
-
-        instance = cls.instantiate_class()
-        method1 = function_to_method(method1, instance)
-        refmethod = function_to_method(refmethod, instance)
-
-        # Don't care about functions with unknown argument (builtins).
-        if method1.args.args is None or refmethod.args.args is None:
-            return
-
-        # Ignore private to class methods.
-        if is_attr_private(method1.name):
-            return
-        # Ignore setters, they have an implicit extra argument,
-        # which shouldn't be taken in consideration.
-        if is_property_setter(method1):
-            return
-
-        if _different_parameters(
-            refmethod, method1, dummy_parameter_regex=self._dummy_rgx
-        ):
-            self.add_message(
-                "arguments-differ", args=(class_type, method1.name), node=method1
-            )
-        elif len(method1.args.defaults) < len(refmethod.args.defaults):
-            self.add_message(
-                "signature-differs", args=(class_type, method1.name), node=method1
-            )
-
-    def _uses_mandatory_method_param(self, node):
-        """Check that attribute lookup name use first attribute variable name
-
-        Name is `self` for method, `cls` for classmethod and `mcs` for metaclass.
-        """
-        return self._is_mandatory_method_param(node.expr)
-
-    def _is_mandatory_method_param(self, node):
-        """Check if astroid.Name corresponds to first attribute variable name
-
-        Name is `self` for method, `cls` for classmethod and `mcs` for metaclass.
-        """
-        return (
-            self._first_attrs
-            and isinstance(node, astroid.Name)
-            and node.name == self._first_attrs[-1]
-        )
-
-
-class SpecialMethodsChecker(BaseChecker):
-    """Checker which verifies that special methods
-    are implemented correctly.
-    """
-
-    __implements__ = (IAstroidChecker,)
-    name = "classes"
-    msgs = {
-        "E0301": (
-            "__iter__ returns non-iterator",
-            "non-iterator-returned",
-            "Used when an __iter__ method returns something which is not an "
-            "iterable (i.e. has no `%s` method)" % NEXT_METHOD,
-            {
-                "old_names": [
-                    ("W0234", "old-non-iterator-returned-1"),
-                    ("E0234", "old-non-iterator-returned-2"),
-                ]
-            },
-        ),
-        "E0302": (
-            "The special method %r expects %s param(s), %d %s given",
-            "unexpected-special-method-signature",
-            "Emitted when a special method was defined with an "
-            "invalid number of parameters. If it has too few or "
-            "too many, it might not work at all.",
-            {"old_names": [("E0235", "bad-context-manager")]},
-        ),
-        "E0303": (
-            "__len__ does not return non-negative integer",
-            "invalid-length-returned",
-            "Used when a __len__ method returns something which is not a "
-            "non-negative integer",
-            {},
-        ),
-    }
-    priority = -2
-
-    @check_messages(
-        "unexpected-special-method-signature",
-        "non-iterator-returned",
-        "invalid-length-returned",
-    )
-    def visit_functiondef(self, node):
-        if not node.is_method():
-            return
-        if node.name == "__iter__":
-            self._check_iter(node)
-        if node.name == "__len__":
-            self._check_len(node)
-        if node.name in PYMETHODS:
-            self._check_unexpected_method_signature(node)
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    def _check_unexpected_method_signature(self, node):
-        expected_params = SPECIAL_METHODS_PARAMS[node.name]
-
-        if expected_params is None:
-            # This can support a variable number of parameters.
-            return
-        if not node.args.args and not node.args.vararg:
-            # Method has no parameter, will be caught
-            # by no-method-argument.
-            return
-
-        if decorated_with(node, [BUILTINS + ".staticmethod"]):
-            # We expect to not take in consideration self.
-            all_args = node.args.args
-        else:
-            all_args = node.args.args[1:]
-        mandatory = len(all_args) - len(node.args.defaults)
-        optional = len(node.args.defaults)
-        current_params = mandatory + optional
-
-        if isinstance(expected_params, tuple):
-            # The expected number of parameters can be any value from this
-            # tuple, although the user should implement the method
-            # to take all of them in consideration.
-            emit = mandatory not in expected_params
-            expected_params = "between %d or %d" % expected_params
-        else:
-            # If the number of mandatory parameters doesn't
-            # suffice, the expected parameters for this
-            # function will be deduced from the optional
-            # parameters.
-            rest = expected_params - mandatory
-            if rest == 0:
-                emit = False
-            elif rest < 0:
-                emit = True
-            elif rest > 0:
-                emit = not ((optional - rest) >= 0 or node.args.vararg)
-
-        if emit:
-            verb = "was" if current_params <= 1 else "were"
-            self.add_message(
-                "unexpected-special-method-signature",
-                args=(node.name, expected_params, current_params, verb),
-                node=node,
-            )
-
-    @staticmethod
-    def _is_iterator(node):
-        if node is astroid.Uninferable:
-            # Just ignore Uninferable objects.
-            return True
-        if isinstance(node, Generator):
-            # Generators can be itered.
-            return True
-
-        if isinstance(node, astroid.Instance):
-            try:
-                node.local_attr(NEXT_METHOD)
-                return True
-            except astroid.NotFoundError:
-                pass
-        elif isinstance(node, astroid.ClassDef):
-            metaclass = node.metaclass()
-            if metaclass and isinstance(metaclass, astroid.ClassDef):
-                try:
-                    metaclass.local_attr(NEXT_METHOD)
-                    return True
-                except astroid.NotFoundError:
-                    pass
-        return False
-
-    def _check_iter(self, node):
-        inferred = _safe_infer_call_result(node, node)
-        if inferred is not None:
-            if not self._is_iterator(inferred):
-                self.add_message("non-iterator-returned", node=node)
-
-    def _check_len(self, node):
-        inferred = _safe_infer_call_result(node, node)
-        if not inferred or inferred is astroid.Uninferable:
-            return
-
-        if (
-            isinstance(inferred, astroid.Instance)
-            and inferred.name == "int"
-            and not isinstance(inferred, astroid.Const)
-        ):
-            # Assume it's good enough, since the int() call might wrap
-            # something that's uninferable for us
-            return
-
-        if not isinstance(inferred, astroid.Const):
-            self.add_message("invalid-length-returned", node=node)
-            return
-
-        value = inferred.value
-        if not isinstance(value, int) or value < 0:
-            self.add_message("invalid-length-returned", node=node)
-
-
-def _ancestors_to_call(klass_node, method="__init__"):
-    """return a dictionary where keys are the list of base classes providing
-    the queried method, and so that should/may be called from the method node
-    """
-    to_call = {}
-    for base_node in klass_node.ancestors(recurs=False):
-        try:
-            to_call[base_node] = next(base_node.igetattr(method))
-        except astroid.InferenceError:
-            continue
-    return to_call
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(ClassChecker(linter))
-    linter.register_checker(SpecialMethodsChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/design_analysis.py b/venv/Lib/site-packages/pylint/checkers/design_analysis.py
deleted file mode 100644
index 50d8eaa..0000000
--- a/venv/Lib/site-packages/pylint/checkers/design_analysis.py
+++ /dev/null
@@ -1,496 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006, 2009-2010, 2012-2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012, 2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 ahirnish <ahirnish@gmail.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 Mark Miller <725mrm@gmail.com>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-# Copyright (c) 2018 Jakub Wilk <jwilk@jwilk.net>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""check for signs of poor design"""
-
-import re
-from collections import defaultdict
-
-import astroid
-from astroid import BoolOp, If, decorators
-
-from pylint import utils
-from pylint.checkers import BaseChecker
-from pylint.checkers.utils import check_messages
-from pylint.interfaces import IAstroidChecker
-
-MSGS = {
-    "R0901": (
-        "Too many ancestors (%s/%s)",
-        "too-many-ancestors",
-        "Used when class has too many parent classes, try to reduce "
-        "this to get a simpler (and so easier to use) class.",
-    ),
-    "R0902": (
-        "Too many instance attributes (%s/%s)",
-        "too-many-instance-attributes",
-        "Used when class has too many instance attributes, try to reduce "
-        "this to get a simpler (and so easier to use) class.",
-    ),
-    "R0903": (
-        "Too few public methods (%s/%s)",
-        "too-few-public-methods",
-        "Used when class has too few public methods, so be sure it's "
-        "really worth it.",
-    ),
-    "R0904": (
-        "Too many public methods (%s/%s)",
-        "too-many-public-methods",
-        "Used when class has too many public methods, try to reduce "
-        "this to get a simpler (and so easier to use) class.",
-    ),
-    "R0911": (
-        "Too many return statements (%s/%s)",
-        "too-many-return-statements",
-        "Used when a function or method has too many return statement, "
-        "making it hard to follow.",
-    ),
-    "R0912": (
-        "Too many branches (%s/%s)",
-        "too-many-branches",
-        "Used when a function or method has too many branches, "
-        "making it hard to follow.",
-    ),
-    "R0913": (
-        "Too many arguments (%s/%s)",
-        "too-many-arguments",
-        "Used when a function or method takes too many arguments.",
-    ),
-    "R0914": (
-        "Too many local variables (%s/%s)",
-        "too-many-locals",
-        "Used when a function or method has too many local variables.",
-    ),
-    "R0915": (
-        "Too many statements (%s/%s)",
-        "too-many-statements",
-        "Used when a function or method has too many statements. You "
-        "should then split it in smaller functions / methods.",
-    ),
-    "R0916": (
-        "Too many boolean expressions in if statement (%s/%s)",
-        "too-many-boolean-expressions",
-        "Used when an if statement contains too many boolean expressions.",
-    ),
-}
-SPECIAL_OBJ = re.compile("^_{2}[a-z]+_{2}$")
-DATACLASSES_DECORATORS = frozenset({"dataclass", "attrs"})
-DATACLASS_IMPORT = "dataclasses"
-TYPING_NAMEDTUPLE = "typing.NamedTuple"
-
-
-def _is_exempt_from_public_methods(node: astroid.ClassDef) -> bool:
-    """Check if a class is exempt from too-few-public-methods"""
-
-    # If it's a typing.Namedtuple or an Enum
-    for ancestor in node.ancestors():
-        if ancestor.name == "Enum" and ancestor.root().name == "enum":
-            return True
-        if ancestor.qname() == TYPING_NAMEDTUPLE:
-            return True
-
-    # Or if it's a dataclass
-    if not node.decorators:
-        return False
-
-    root_locals = set(node.root().locals)
-    for decorator in node.decorators.nodes:
-        if isinstance(decorator, astroid.Call):
-            decorator = decorator.func
-        if not isinstance(decorator, (astroid.Name, astroid.Attribute)):
-            continue
-        if isinstance(decorator, astroid.Name):
-            name = decorator.name
-        else:
-            name = decorator.attrname
-        if name in DATACLASSES_DECORATORS and (
-            root_locals.intersection(DATACLASSES_DECORATORS)
-            or DATACLASS_IMPORT in root_locals
-        ):
-            return True
-    return False
-
-
-def _count_boolean_expressions(bool_op):
-    """Counts the number of boolean expressions in BoolOp `bool_op` (recursive)
-
-    example: a and (b or c or (d and e)) ==> 5 boolean expressions
-    """
-    nb_bool_expr = 0
-    for bool_expr in bool_op.get_children():
-        if isinstance(bool_expr, BoolOp):
-            nb_bool_expr += _count_boolean_expressions(bool_expr)
-        else:
-            nb_bool_expr += 1
-    return nb_bool_expr
-
-
-def _count_methods_in_class(node):
-    all_methods = sum(1 for method in node.methods() if not method.name.startswith("_"))
-    # Special methods count towards the number of public methods,
-    # but don't count towards there being too many methods.
-    for method in node.mymethods():
-        if SPECIAL_OBJ.search(method.name) and method.name != "__init__":
-            all_methods += 1
-    return all_methods
-
-
-class MisdesignChecker(BaseChecker):
-    """checks for sign of poor/misdesign:
-    * number of methods, attributes, local variables...
-    * size, complexity of functions, methods
-    """
-
-    __implements__ = (IAstroidChecker,)
-
-    # configuration section name
-    name = "design"
-    # messages
-    msgs = MSGS
-    priority = -2
-    # configuration options
-    options = (
-        (
-            "max-args",
-            {
-                "default": 5,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of arguments for function / method.",
-            },
-        ),
-        (
-            "max-locals",
-            {
-                "default": 15,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of locals for function / method body.",
-            },
-        ),
-        (
-            "max-returns",
-            {
-                "default": 6,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of return / yield for function / "
-                "method body.",
-            },
-        ),
-        (
-            "max-branches",
-            {
-                "default": 12,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of branch for function / method body.",
-            },
-        ),
-        (
-            "max-statements",
-            {
-                "default": 50,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of statements in function / method " "body.",
-            },
-        ),
-        (
-            "max-parents",
-            {
-                "default": 7,
-                "type": "int",
-                "metavar": "<num>",
-                "help": "Maximum number of parents for a class (see R0901).",
-            },
-        ),
-        (
-            "max-attributes",
-            {
-                "default": 7,
-                "type": "int",
-                "metavar": "<num>",
-                "help": "Maximum number of attributes for a class \
-(see R0902).",
-            },
-        ),
-        (
-            "min-public-methods",
-            {
-                "default": 2,
-                "type": "int",
-                "metavar": "<num>",
-                "help": "Minimum number of public methods for a class \
-(see R0903).",
-            },
-        ),
-        (
-            "max-public-methods",
-            {
-                "default": 20,
-                "type": "int",
-                "metavar": "<num>",
-                "help": "Maximum number of public methods for a class \
-(see R0904).",
-            },
-        ),
-        (
-            "max-bool-expr",
-            {
-                "default": 5,
-                "type": "int",
-                "metavar": "<num>",
-                "help": "Maximum number of boolean expressions in an if "
-                "statement (see R0916).",
-            },
-        ),
-    )
-
-    def __init__(self, linter=None):
-        BaseChecker.__init__(self, linter)
-        self.stats = None
-        self._returns = None
-        self._branches = None
-        self._stmts = None
-
-    def open(self):
-        """initialize visit variables"""
-        self.stats = self.linter.add_stats()
-        self._returns = []
-        self._branches = defaultdict(int)
-        self._stmts = []
-
-    def _inc_all_stmts(self, amount):
-        for i in range(len(self._stmts)):
-            self._stmts[i] += amount
-
-    @decorators.cachedproperty
-    def _ignored_argument_names(self):
-        return utils.get_global_option(self, "ignored-argument-names", default=None)
-
-    @check_messages(
-        "too-many-ancestors",
-        "too-many-instance-attributes",
-        "too-few-public-methods",
-        "too-many-public-methods",
-    )
-    def visit_classdef(self, node):
-        """check size of inheritance hierarchy and number of instance attributes
-        """
-        nb_parents = len(list(node.ancestors()))
-        if nb_parents > self.config.max_parents:
-            self.add_message(
-                "too-many-ancestors",
-                node=node,
-                args=(nb_parents, self.config.max_parents),
-            )
-
-        if len(node.instance_attrs) > self.config.max_attributes:
-            self.add_message(
-                "too-many-instance-attributes",
-                node=node,
-                args=(len(node.instance_attrs), self.config.max_attributes),
-            )
-
-    @check_messages("too-few-public-methods", "too-many-public-methods")
-    def leave_classdef(self, node):
-        """check number of public methods"""
-        my_methods = sum(
-            1 for method in node.mymethods() if not method.name.startswith("_")
-        )
-
-        # Does the class contain less than n public methods ?
-        # This checks only the methods defined in the current class,
-        # since the user might not have control over the classes
-        # from the ancestors. It avoids some false positives
-        # for classes such as unittest.TestCase, which provides
-        # a lot of assert methods. It doesn't make sense to warn
-        # when the user subclasses TestCase to add his own tests.
-        if my_methods > self.config.max_public_methods:
-            self.add_message(
-                "too-many-public-methods",
-                node=node,
-                args=(my_methods, self.config.max_public_methods),
-            )
-
-        # Stop here for exception, metaclass, interface classes and other
-        # classes for which we don't need to count the methods.
-        if node.type != "class" or _is_exempt_from_public_methods(node):
-            return
-
-        # Does the class contain more than n public methods ?
-        # This checks all the methods defined by ancestors and
-        # by the current class.
-        all_methods = _count_methods_in_class(node)
-        if all_methods < self.config.min_public_methods:
-            self.add_message(
-                "too-few-public-methods",
-                node=node,
-                args=(all_methods, self.config.min_public_methods),
-            )
-
-    @check_messages(
-        "too-many-return-statements",
-        "too-many-branches",
-        "too-many-arguments",
-        "too-many-locals",
-        "too-many-statements",
-        "keyword-arg-before-vararg",
-    )
-    def visit_functiondef(self, node):
-        """check function name, docstring, arguments, redefinition,
-        variable names, max locals
-        """
-        # init branch and returns counters
-        self._returns.append(0)
-        # check number of arguments
-        args = node.args.args
-        ignored_argument_names = self._ignored_argument_names
-        if args is not None:
-            ignored_args_num = 0
-            if ignored_argument_names:
-                ignored_args_num = sum(
-                    1 for arg in args if ignored_argument_names.match(arg.name)
-                )
-
-            argnum = len(args) - ignored_args_num
-            if argnum > self.config.max_args:
-                self.add_message(
-                    "too-many-arguments",
-                    node=node,
-                    args=(len(args), self.config.max_args),
-                )
-        else:
-            ignored_args_num = 0
-        # check number of local variables
-        locnum = len(node.locals) - ignored_args_num
-        if locnum > self.config.max_locals:
-            self.add_message(
-                "too-many-locals", node=node, args=(locnum, self.config.max_locals)
-            )
-        # init new statements counter
-        self._stmts.append(1)
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    @check_messages(
-        "too-many-return-statements",
-        "too-many-branches",
-        "too-many-arguments",
-        "too-many-locals",
-        "too-many-statements",
-    )
-    def leave_functiondef(self, node):
-        """most of the work is done here on close:
-        checks for max returns, branch, return in __init__
-        """
-        returns = self._returns.pop()
-        if returns > self.config.max_returns:
-            self.add_message(
-                "too-many-return-statements",
-                node=node,
-                args=(returns, self.config.max_returns),
-            )
-        branches = self._branches[node]
-        if branches > self.config.max_branches:
-            self.add_message(
-                "too-many-branches",
-                node=node,
-                args=(branches, self.config.max_branches),
-            )
-        # check number of statements
-        stmts = self._stmts.pop()
-        if stmts > self.config.max_statements:
-            self.add_message(
-                "too-many-statements",
-                node=node,
-                args=(stmts, self.config.max_statements),
-            )
-
-    leave_asyncfunctiondef = leave_functiondef
-
-    def visit_return(self, _):
-        """count number of returns"""
-        if not self._returns:
-            return  # return outside function, reported by the base checker
-        self._returns[-1] += 1
-
-    def visit_default(self, node):
-        """default visit method -> increments the statements counter if
-        necessary
-        """
-        if node.is_statement:
-            self._inc_all_stmts(1)
-
-    def visit_tryexcept(self, node):
-        """increments the branches counter"""
-        branches = len(node.handlers)
-        if node.orelse:
-            branches += 1
-        self._inc_branch(node, branches)
-        self._inc_all_stmts(branches)
-
-    def visit_tryfinally(self, node):
-        """increments the branches counter"""
-        self._inc_branch(node, 2)
-        self._inc_all_stmts(2)
-
-    @check_messages("too-many-boolean-expressions")
-    def visit_if(self, node):
-        """increments the branches counter and checks boolean expressions"""
-        self._check_boolean_expressions(node)
-        branches = 1
-        # don't double count If nodes coming from some 'elif'
-        if node.orelse and (len(node.orelse) > 1 or not isinstance(node.orelse[0], If)):
-            branches += 1
-        self._inc_branch(node, branches)
-        self._inc_all_stmts(branches)
-
-    def _check_boolean_expressions(self, node):
-        """Go through "if" node `node` and counts its boolean expressions
-
-        if the "if" node test is a BoolOp node
-        """
-        condition = node.test
-        if not isinstance(condition, BoolOp):
-            return
-        nb_bool_expr = _count_boolean_expressions(condition)
-        if nb_bool_expr > self.config.max_bool_expr:
-            self.add_message(
-                "too-many-boolean-expressions",
-                node=condition,
-                args=(nb_bool_expr, self.config.max_bool_expr),
-            )
-
-    def visit_while(self, node):
-        """increments the branches counter"""
-        branches = 1
-        if node.orelse:
-            branches += 1
-        self._inc_branch(node, branches)
-
-    visit_for = visit_while
-
-    def _inc_branch(self, node, branchesnum=1):
-        """increments the branches counter"""
-        self._branches[node.scope()] += branchesnum
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(MisdesignChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/exceptions.py b/venv/Lib/site-packages/pylint/checkers/exceptions.py
deleted file mode 100644
index 360e1d1..0000000
--- a/venv/Lib/site-packages/pylint/checkers/exceptions.py
+++ /dev/null
@@ -1,546 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2011-2014 Google, Inc.
-# Copyright (c) 2012 Tim Hatch <tim@timhatch.com>
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Rene Zhang <rz99@cornell.edu>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Steven Myint <hg@stevenmyint.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Erik <erik.eriksson@yahoo.com>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 Martin von Gagern <gagern@google.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Checks for various exception related errors."""
-import builtins
-import inspect
-import typing
-
-import astroid
-from astroid.node_classes import NodeNG
-
-from pylint import checkers, interfaces
-from pylint.checkers import utils
-
-
-def _builtin_exceptions():
-    def predicate(obj):
-        return isinstance(obj, type) and issubclass(obj, BaseException)
-
-    members = inspect.getmembers(builtins, predicate)
-    return {exc.__name__ for (_, exc) in members}
-
-
-def _annotated_unpack_infer(stmt, context=None):
-    """
-    Recursively generate nodes inferred by the given statement.
-    If the inferred value is a list or a tuple, recurse on the elements.
-    Returns an iterator which yields tuples in the format
-    ('original node', 'inferred node').
-    """
-    if isinstance(stmt, (astroid.List, astroid.Tuple)):
-        for elt in stmt.elts:
-            inferred = utils.safe_infer(elt)
-            if inferred and inferred is not astroid.Uninferable:
-                yield elt, inferred
-        return
-    for inferred in stmt.infer(context):
-        if inferred is astroid.Uninferable:
-            continue
-        yield stmt, inferred
-
-
-def _is_raising(body: typing.List) -> bool:
-    """Return true if the given statement node raise an exception"""
-    for node in body:
-        if isinstance(node, astroid.Raise):
-            return True
-    return False
-
-
-OVERGENERAL_EXCEPTIONS = ("BaseException", "Exception")
-BUILTINS_NAME = builtins.__name__
-
-MSGS = {
-    "E0701": (
-        "Bad except clauses order (%s)",
-        "bad-except-order",
-        "Used when except clauses are not in the correct order (from the "
-        "more specific to the more generic). If you don't fix the order, "
-        "some exceptions may not be caught by the most specific handler.",
-    ),
-    "E0702": (
-        "Raising %s while only classes or instances are allowed",
-        "raising-bad-type",
-        "Used when something which is neither a class, an instance or a "
-        "string is raised (i.e. a `TypeError` will be raised).",
-    ),
-    "E0703": (
-        "Exception context set to something which is not an exception, nor None",
-        "bad-exception-context",
-        'Used when using the syntax "raise ... from ...", '
-        "where the exception context is not an exception, "
-        "nor None.",
-    ),
-    "E0704": (
-        "The raise statement is not inside an except clause",
-        "misplaced-bare-raise",
-        "Used when a bare raise is not used inside an except clause. "
-        "This generates an error, since there are no active exceptions "
-        "to be reraised. An exception to this rule is represented by "
-        "a bare raise inside a finally clause, which might work, as long "
-        "as an exception is raised inside the try block, but it is "
-        "nevertheless a code smell that must not be relied upon.",
-    ),
-    "E0710": (
-        "Raising a new style class which doesn't inherit from BaseException",
-        "raising-non-exception",
-        "Used when a new style class which doesn't inherit from "
-        "BaseException is raised.",
-    ),
-    "E0711": (
-        "NotImplemented raised - should raise NotImplementedError",
-        "notimplemented-raised",
-        "Used when NotImplemented is raised instead of NotImplementedError",
-    ),
-    "E0712": (
-        "Catching an exception which doesn't inherit from Exception: %s",
-        "catching-non-exception",
-        "Used when a class which doesn't inherit from "
-        "Exception is used as an exception in an except clause.",
-    ),
-    "W0702": (
-        "No exception type(s) specified",
-        "bare-except",
-        "Used when an except clause doesn't specify exceptions type to catch.",
-    ),
-    "W0703": (
-        "Catching too general exception %s",
-        "broad-except",
-        "Used when an except catches a too general exception, "
-        "possibly burying unrelated errors.",
-    ),
-    "W0705": (
-        "Catching previously caught exception type %s",
-        "duplicate-except",
-        "Used when an except catches a type that was already caught by "
-        "a previous handler.",
-    ),
-    "W0706": (
-        "The except handler raises immediately",
-        "try-except-raise",
-        "Used when an except handler uses raise as its first or only "
-        "operator. This is useless because it raises back the exception "
-        "immediately. Remove the raise operator or the entire "
-        "try-except-raise block!",
-    ),
-    "W0711": (
-        'Exception to catch is the result of a binary "%s" operation',
-        "binary-op-exception",
-        "Used when the exception to catch is of the form "
-        '"except A or B:".  If intending to catch multiple, '
-        'rewrite as "except (A, B):"',
-    ),
-    "W0715": (
-        "Exception arguments suggest string formatting might be intended",
-        "raising-format-tuple",
-        "Used when passing multiple arguments to an exception "
-        "constructor, the first of them a string literal containing what "
-        "appears to be placeholders intended for formatting",
-    ),
-    "W0716": (
-        "Invalid exception operation. %s",
-        "wrong-exception-operation",
-        "Used when an operation is done against an exception, but the operation "
-        "is not valid for the exception in question. Usually emitted when having "
-        "binary operations between exceptions in except handlers.",
-    ),
-}
-
-
-class BaseVisitor:
-    """Base class for visitors defined in this module."""
-
-    def __init__(self, checker, node):
-        self._checker = checker
-        self._node = node
-
-    def visit(self, node):
-        name = node.__class__.__name__.lower()
-        dispatch_meth = getattr(self, "visit_" + name, None)
-        if dispatch_meth:
-            dispatch_meth(node)
-        else:
-            self.visit_default(node)
-
-    def visit_default(self, node):  # pylint: disable=unused-argument
-        """Default implementation for all the nodes."""
-
-
-class ExceptionRaiseRefVisitor(BaseVisitor):
-    """Visit references (anything that is not an AST leaf)."""
-
-    def visit_name(self, name):
-        if name.name == "NotImplemented":
-            self._checker.add_message("notimplemented-raised", node=self._node)
-
-    def visit_call(self, call):
-        if isinstance(call.func, astroid.Name):
-            self.visit_name(call.func)
-        if (
-            len(call.args) > 1
-            and isinstance(call.args[0], astroid.Const)
-            and isinstance(call.args[0].value, str)
-        ):
-            msg = call.args[0].value
-            if "%" in msg or ("{" in msg and "}" in msg):
-                self._checker.add_message("raising-format-tuple", node=self._node)
-
-
-class ExceptionRaiseLeafVisitor(BaseVisitor):
-    """Visitor for handling leaf kinds of a raise value."""
-
-    def visit_const(self, const):
-        if not isinstance(const.value, str):
-            # raising-string will be emitted from python3 porting checker.
-            self._checker.add_message(
-                "raising-bad-type", node=self._node, args=const.value.__class__.__name__
-            )
-
-    def visit_instance(self, instance):
-        # pylint: disable=protected-access
-        cls = instance._proxied
-        self.visit_classdef(cls)
-
-    # Exception instances have a particular class type
-    visit_exceptioninstance = visit_instance
-
-    def visit_classdef(self, cls):
-        if not utils.inherit_from_std_ex(cls) and utils.has_known_bases(cls):
-            if cls.newstyle:
-                self._checker.add_message("raising-non-exception", node=self._node)
-
-    def visit_tuple(self, _):
-        self._checker.add_message("raising-bad-type", node=self._node, args="tuple")
-
-    def visit_default(self, node):
-        name = getattr(node, "name", node.__class__.__name__)
-        self._checker.add_message("raising-bad-type", node=self._node, args=name)
-
-
-class ExceptionsChecker(checkers.BaseChecker):
-    """Exception related checks."""
-
-    __implements__ = interfaces.IAstroidChecker
-
-    name = "exceptions"
-    msgs = MSGS
-    priority = -4
-    options = (
-        (
-            "overgeneral-exceptions",
-            {
-                "default": OVERGENERAL_EXCEPTIONS,
-                "type": "csv",
-                "metavar": "<comma-separated class names>",
-                "help": "Exceptions that will emit a warning "
-                'when being caught. Defaults to "%s".'
-                % (", ".join(OVERGENERAL_EXCEPTIONS),),
-            },
-        ),
-    )
-
-    def open(self):
-        self._builtin_exceptions = _builtin_exceptions()
-        super(ExceptionsChecker, self).open()
-
-    @utils.check_messages(
-        "misplaced-bare-raise",
-        "raising-bad-type",
-        "raising-non-exception",
-        "notimplemented-raised",
-        "bad-exception-context",
-        "raising-format-tuple",
-    )
-    def visit_raise(self, node):
-        if node.exc is None:
-            self._check_misplaced_bare_raise(node)
-            return
-
-        if node.cause:
-            self._check_bad_exception_context(node)
-
-        expr = node.exc
-        ExceptionRaiseRefVisitor(self, node).visit(expr)
-
-        try:
-            inferred_value = expr.inferred()[-1]
-        except astroid.InferenceError:
-            pass
-        else:
-            if inferred_value:
-                ExceptionRaiseLeafVisitor(self, node).visit(inferred_value)
-
-    def _check_misplaced_bare_raise(self, node):
-        # Filter out if it's present in __exit__.
-        scope = node.scope()
-        if (
-            isinstance(scope, astroid.FunctionDef)
-            and scope.is_method()
-            and scope.name == "__exit__"
-        ):
-            return
-
-        current = node
-        # Stop when a new scope is generated or when the raise
-        # statement is found inside a TryFinally.
-        ignores = (astroid.ExceptHandler, astroid.FunctionDef)
-        while current and not isinstance(current.parent, ignores):
-            current = current.parent
-
-        expected = (astroid.ExceptHandler,)
-        if not current or not isinstance(current.parent, expected):
-            self.add_message("misplaced-bare-raise", node=node)
-
-    def _check_bad_exception_context(self, node):
-        """Verify that the exception context is properly set.
-
-        An exception context can be only `None` or an exception.
-        """
-        cause = utils.safe_infer(node.cause)
-        if cause in (astroid.Uninferable, None):
-            return
-
-        if isinstance(cause, astroid.Const):
-            if cause.value is not None:
-                self.add_message("bad-exception-context", node=node)
-        elif not isinstance(cause, astroid.ClassDef) and not utils.inherit_from_std_ex(
-            cause
-        ):
-            self.add_message("bad-exception-context", node=node)
-
-    def _check_catching_non_exception(self, handler, exc, part):
-        if isinstance(exc, astroid.Tuple):
-            # Check if it is a tuple of exceptions.
-            inferred = [utils.safe_infer(elt) for elt in exc.elts]
-            if any(node is astroid.Uninferable for node in inferred):
-                # Don't emit if we don't know every component.
-                return
-            if all(
-                node
-                and (utils.inherit_from_std_ex(node) or not utils.has_known_bases(node))
-                for node in inferred
-            ):
-                return
-
-        if not isinstance(exc, astroid.ClassDef):
-            # Don't emit the warning if the inferred stmt
-            # is None, but the exception handler is something else,
-            # maybe it was redefined.
-            if isinstance(exc, astroid.Const) and exc.value is None:
-                if (
-                    isinstance(handler.type, astroid.Const)
-                    and handler.type.value is None
-                ) or handler.type.parent_of(exc):
-                    # If the exception handler catches None or
-                    # the exception component, which is None, is
-                    # defined by the entire exception handler, then
-                    # emit a warning.
-                    self.add_message(
-                        "catching-non-exception",
-                        node=handler.type,
-                        args=(part.as_string(),),
-                    )
-            else:
-                self.add_message(
-                    "catching-non-exception",
-                    node=handler.type,
-                    args=(part.as_string(),),
-                )
-            return
-
-        if (
-            not utils.inherit_from_std_ex(exc)
-            and exc.name not in self._builtin_exceptions
-        ):
-            if utils.has_known_bases(exc):
-                self.add_message(
-                    "catching-non-exception", node=handler.type, args=(exc.name,)
-                )
-
-    def _check_try_except_raise(self, node):
-        def gather_exceptions_from_handler(
-            handler
-        ) -> typing.Optional[typing.List[NodeNG]]:
-            exceptions = []  # type: typing.List[NodeNG]
-            if handler.type:
-                exceptions_in_handler = utils.safe_infer(handler.type)
-                if isinstance(exceptions_in_handler, astroid.Tuple):
-                    exceptions = list(
-                        {
-                            exception
-                            for exception in exceptions_in_handler.elts
-                            if isinstance(exception, astroid.Name)
-                        }
-                    )
-                elif exceptions_in_handler:
-                    exceptions = [exceptions_in_handler]
-                else:
-                    # Break when we cannot infer anything reliably.
-                    return None
-            return exceptions
-
-        bare_raise = False
-        handler_having_bare_raise = None
-        excs_in_bare_handler = []
-        for handler in node.handlers:
-            if bare_raise:
-                # check that subsequent handler is not parent of handler which had bare raise.
-                # since utils.safe_infer can fail for bare except, check it before.
-                # also break early if bare except is followed by bare except.
-
-                excs_in_current_handler = gather_exceptions_from_handler(handler)
-
-                if not excs_in_current_handler:
-                    bare_raise = False
-                    break
-                if excs_in_bare_handler is None:
-                    # It can be `None` when the inference failed
-                    break
-
-                for exc_in_current_handler in excs_in_current_handler:
-                    inferred_current = utils.safe_infer(exc_in_current_handler)
-                    if any(
-                        utils.is_subclass_of(
-                            utils.safe_infer(exc_in_bare_handler), inferred_current
-                        )
-                        for exc_in_bare_handler in excs_in_bare_handler
-                    ):
-                        bare_raise = False
-                        break
-
-            # `raise` as the first operator inside the except handler
-            if _is_raising([handler.body[0]]):
-                # flags when there is a bare raise
-                if handler.body[0].exc is None:
-                    bare_raise = True
-                    handler_having_bare_raise = handler
-                    excs_in_bare_handler = gather_exceptions_from_handler(handler)
-        else:
-            if bare_raise:
-                self.add_message("try-except-raise", node=handler_having_bare_raise)
-
-    @utils.check_messages("wrong-exception-operation")
-    def visit_binop(self, node):
-        if isinstance(node.parent, astroid.ExceptHandler):
-            # except (V | A)
-            suggestion = "Did you mean '(%s, %s)' instead?" % (
-                node.left.as_string(),
-                node.right.as_string(),
-            )
-            self.add_message("wrong-exception-operation", node=node, args=(suggestion,))
-
-    @utils.check_messages("wrong-exception-operation")
-    def visit_compare(self, node):
-        if isinstance(node.parent, astroid.ExceptHandler):
-            # except (V < A)
-            suggestion = "Did you mean '(%s, %s)' instead?" % (
-                node.left.as_string(),
-                ", ".join(operand.as_string() for _, operand in node.ops),
-            )
-            self.add_message("wrong-exception-operation", node=node, args=(suggestion,))
-
-    @utils.check_messages(
-        "bare-except",
-        "broad-except",
-        "try-except-raise",
-        "binary-op-exception",
-        "bad-except-order",
-        "catching-non-exception",
-        "duplicate-except",
-    )
-    def visit_tryexcept(self, node):
-        """check for empty except"""
-        self._check_try_except_raise(node)
-        exceptions_classes = []
-        nb_handlers = len(node.handlers)
-        for index, handler in enumerate(node.handlers):
-            if handler.type is None:
-                if not _is_raising(handler.body):
-                    self.add_message("bare-except", node=handler)
-
-                # check if an "except:" is followed by some other
-                # except
-                if index < (nb_handlers - 1):
-                    msg = "empty except clause should always appear last"
-                    self.add_message("bad-except-order", node=node, args=msg)
-
-            elif isinstance(handler.type, astroid.BoolOp):
-                self.add_message(
-                    "binary-op-exception", node=handler, args=handler.type.op
-                )
-            else:
-                try:
-                    excs = list(_annotated_unpack_infer(handler.type))
-                except astroid.InferenceError:
-                    continue
-
-                for part, exc in excs:
-                    if exc is astroid.Uninferable:
-                        continue
-                    if isinstance(exc, astroid.Instance) and utils.inherit_from_std_ex(
-                        exc
-                    ):
-                        # pylint: disable=protected-access
-                        exc = exc._proxied
-
-                    self._check_catching_non_exception(handler, exc, part)
-
-                    if not isinstance(exc, astroid.ClassDef):
-                        continue
-
-                    exc_ancestors = [
-                        anc
-                        for anc in exc.ancestors()
-                        if isinstance(anc, astroid.ClassDef)
-                    ]
-
-                    for previous_exc in exceptions_classes:
-                        if previous_exc in exc_ancestors:
-                            msg = "%s is an ancestor class of %s" % (
-                                previous_exc.name,
-                                exc.name,
-                            )
-                            self.add_message(
-                                "bad-except-order", node=handler.type, args=msg
-                            )
-                    if (
-                        exc.name in self.config.overgeneral_exceptions
-                        and exc.root().name == utils.EXCEPTIONS_MODULE
-                        and not _is_raising(handler.body)
-                    ):
-                        self.add_message(
-                            "broad-except", args=exc.name, node=handler.type
-                        )
-
-                    if exc in exceptions_classes:
-                        self.add_message(
-                            "duplicate-except", args=exc.name, node=handler.type
-                        )
-
-                exceptions_classes += [exc for _, exc in excs]
-
-
-def register(linter):
-    """required method to auto register this checker"""
-    linter.register_checker(ExceptionsChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/format.py b/venv/Lib/site-packages/pylint/checkers/format.py
deleted file mode 100644
index c4cad31..0000000
--- a/venv/Lib/site-packages/pylint/checkers/format.py
+++ /dev/null
@@ -1,1332 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012-2015 Google, Inc.
-# Copyright (c) 2013 moxian <aleftmail@inbox.ru>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 frost-nzcr4 <frost.nzcr4@jagmort.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Mike Frysinger <vapier@gentoo.org>
-# Copyright (c) 2015 Fabio Natali <me@fabionatali.com>
-# Copyright (c) 2015 Harut <yes@harutune.name>
-# Copyright (c) 2015 Mihai Balint <balint.mihai@gmail.com>
-# Copyright (c) 2015 Pavel Roskin <proski@gnu.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Petr Pulc <petrpulc@gmail.com>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017-2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Krzysztof Czapla <k.czapla68@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 James M. Allen <james.m.allen@gmail.com>
-# Copyright (c) 2017 vinnyrose <vinnyrose@users.noreply.github.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.guinta@protonmail.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 Fureigh <rhys.fureigh@gsa.gov>
-# Copyright (c) 2018 Pierre Sassoulas <pierre.sassoulas@wisebim.fr>
-# Copyright (c) 2018 Andreas Freimuth <andreas.freimuth@united-bits.de>
-# Copyright (c) 2018 Jakub Wilk <jwilk@jwilk.net>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Python code format's checker.
-
-By default try to follow Guido's style guide :
-
-https://www.python.org/doc/essays/styleguide/
-
-Some parts of the process_token method is based from The Tab Nanny std module.
-"""
-
-import keyword
-import tokenize
-from functools import reduce  # pylint: disable=redefined-builtin
-
-from astroid import nodes
-
-from pylint.checkers import BaseTokenChecker
-from pylint.checkers.utils import check_messages
-from pylint.constants import OPTION_RGX, WarningScope
-from pylint.interfaces import IAstroidChecker, IRawChecker, ITokenChecker
-
-_ASYNC_TOKEN = "async"
-_CONTINUATION_BLOCK_OPENERS = [
-    "elif",
-    "except",
-    "for",
-    "if",
-    "while",
-    "def",
-    "class",
-    "with",
-]
-_KEYWORD_TOKENS = [
-    "assert",
-    "del",
-    "elif",
-    "except",
-    "for",
-    "if",
-    "in",
-    "not",
-    "raise",
-    "return",
-    "while",
-    "yield",
-    "with",
-]
-
-_SPACED_OPERATORS = [
-    "==",
-    "<",
-    ">",
-    "!=",
-    "<>",
-    "<=",
-    ">=",
-    "+=",
-    "-=",
-    "*=",
-    "**=",
-    "/=",
-    "//=",
-    "&=",
-    "|=",
-    "^=",
-    "%=",
-    ">>=",
-    "<<=",
-]
-_OPENING_BRACKETS = ["(", "[", "{"]
-_CLOSING_BRACKETS = [")", "]", "}"]
-_TAB_LENGTH = 8
-
-_EOL = frozenset([tokenize.NEWLINE, tokenize.NL, tokenize.COMMENT])
-_JUNK_TOKENS = (tokenize.COMMENT, tokenize.NL)
-
-# Whitespace checking policy constants
-_MUST = 0
-_MUST_NOT = 1
-_IGNORE = 2
-
-# Whitespace checking config constants
-_DICT_SEPARATOR = "dict-separator"
-_TRAILING_COMMA = "trailing-comma"
-_EMPTY_LINE = "empty-line"
-_NO_SPACE_CHECK_CHOICES = [_TRAILING_COMMA, _DICT_SEPARATOR, _EMPTY_LINE]
-_DEFAULT_NO_SPACE_CHECK_CHOICES = [_TRAILING_COMMA, _DICT_SEPARATOR]
-
-MSGS = {
-    "C0301": (
-        "Line too long (%s/%s)",
-        "line-too-long",
-        "Used when a line is longer than a given number of characters.",
-    ),
-    "C0302": (
-        "Too many lines in module (%s/%s)",  # was W0302
-        "too-many-lines",
-        "Used when a module has too many lines, reducing its readability.",
-    ),
-    "C0303": (
-        "Trailing whitespace",
-        "trailing-whitespace",
-        "Used when there is whitespace between the end of a line and the newline.",
-    ),
-    "C0304": (
-        "Final newline missing",
-        "missing-final-newline",
-        "Used when the last line in a file is missing a newline.",
-    ),
-    "C0305": (
-        "Trailing newlines",
-        "trailing-newlines",
-        "Used when there are trailing blank lines in a file.",
-    ),
-    "W0311": (
-        "Bad indentation. Found %s %s, expected %s",
-        "bad-indentation",
-        "Used when an unexpected number of indentation's tabulations or "
-        "spaces has been found.",
-    ),
-    "C0330": ("Wrong %s indentation%s%s.\n%s%s", "bad-continuation", "TODO"),
-    "W0312": (
-        "Found indentation with %ss instead of %ss",
-        "mixed-indentation",
-        "Used when there are some mixed tabs and spaces in a module.",
-    ),
-    "W0301": (
-        "Unnecessary semicolon",  # was W0106
-        "unnecessary-semicolon",
-        'Used when a statement is ended by a semi-colon (";"), which '
-        "isn't necessary (that's python, not C ;).",
-    ),
-    "C0321": (
-        "More than one statement on a single line",
-        "multiple-statements",
-        "Used when more than on statement are found on the same line.",
-        {"scope": WarningScope.NODE},
-    ),
-    "C0325": (
-        "Unnecessary parens after %r keyword",
-        "superfluous-parens",
-        "Used when a single item in parentheses follows an if, for, or "
-        "other keyword.",
-    ),
-    "C0326": (
-        "%s space %s %s %s\n%s",
-        "bad-whitespace",
-        (
-            "Used when a wrong number of spaces is used around an operator, "
-            "bracket or block opener."
-        ),
-        {
-            "old_names": [
-                ("C0323", "no-space-after-operator"),
-                ("C0324", "no-space-after-comma"),
-                ("C0322", "no-space-before-operator"),
-            ]
-        },
-    ),
-    "C0327": (
-        "Mixed line endings LF and CRLF",
-        "mixed-line-endings",
-        "Used when there are mixed (LF and CRLF) newline signs in a file.",
-    ),
-    "C0328": (
-        "Unexpected line ending format. There is '%s' while it should be '%s'.",
-        "unexpected-line-ending-format",
-        "Used when there is different newline than expected.",
-    ),
-}
-
-
-def _underline_token(token):
-    length = token[3][1] - token[2][1]
-    offset = token[2][1]
-    referenced_line = token[4]
-    # If the referenced line does not end with a newline char, fix it
-    if referenced_line[-1] != "\n":
-        referenced_line += "\n"
-    return referenced_line + (" " * offset) + ("^" * length)
-
-
-def _column_distance(token1, token2):
-    if token1 == token2:
-        return 0
-    if token2[3] < token1[3]:
-        token1, token2 = token2, token1
-    if token1[3][0] != token2[2][0]:
-        return None
-    return token2[2][1] - token1[3][1]
-
-
-def _last_token_on_line_is(tokens, line_end, token):
-    return (
-        line_end > 0
-        and tokens.token(line_end - 1) == token
-        or line_end > 1
-        and tokens.token(line_end - 2) == token
-        and tokens.type(line_end - 1) == tokenize.COMMENT
-    )
-
-
-def _token_followed_by_eol(tokens, position):
-    return (
-        tokens.type(position + 1) == tokenize.NL
-        or tokens.type(position + 1) == tokenize.COMMENT
-        and tokens.type(position + 2) == tokenize.NL
-    )
-
-
-def _get_indent_string(line):
-    """Return the indention string of the given line."""
-    result = ""
-    for char in line:
-        if char in " \t":
-            result += char
-        else:
-            break
-    return result
-
-
-def _get_indent_length(line):
-    """Return the length of the indentation on the given token's line."""
-    result = 0
-    for char in line:
-        if char == " ":
-            result += 1
-        elif char == "\t":
-            result += _TAB_LENGTH
-        else:
-            break
-    return result
-
-
-def _get_indent_hint_line(bar_positions, bad_position):
-    """Return a line with |s for each of the positions in the given lists."""
-    if not bar_positions:
-        return "", ""
-
-    bar_positions = [_get_indent_length(indent) for indent in bar_positions]
-    bad_position = _get_indent_length(bad_position)
-    delta_message = ""
-    markers = [(pos, "|") for pos in bar_positions]
-    if len(markers) == 1:
-        # if we have only one marker we'll provide an extra hint on how to fix
-        expected_position = markers[0][0]
-        delta = abs(expected_position - bad_position)
-        direction = "add" if expected_position > bad_position else "remove"
-        delta_message = _CONTINUATION_HINT_MESSAGE % (
-            direction,
-            delta,
-            "s" if delta > 1 else "",
-        )
-    markers.append((bad_position, "^"))
-    markers.sort()
-    line = [" "] * (markers[-1][0] + 1)
-    for position, marker in markers:
-        line[position] = marker
-    return "".join(line), delta_message
-
-
-class _ContinuedIndent:
-    __slots__ = (
-        "valid_outdent_strings",
-        "valid_continuation_strings",
-        "context_type",
-        "token",
-        "position",
-    )
-
-    def __init__(
-        self,
-        context_type,
-        token,
-        position,
-        valid_outdent_strings,
-        valid_continuation_strings,
-    ):
-        self.valid_outdent_strings = valid_outdent_strings
-        self.valid_continuation_strings = valid_continuation_strings
-        self.context_type = context_type
-        self.position = position
-        self.token = token
-
-
-# The contexts for hanging indents.
-# A hanging indented dictionary value after :
-HANGING_DICT_VALUE = "dict-value"
-# Hanging indentation in an expression.
-HANGING = "hanging"
-# Hanging indentation in a block header.
-HANGING_BLOCK = "hanging-block"
-# Continued indentation inside an expression.
-CONTINUED = "continued"
-# Continued indentation in a block header.
-CONTINUED_BLOCK = "continued-block"
-
-SINGLE_LINE = "single"
-WITH_BODY = "multi"
-
-_CONTINUATION_MSG_PARTS = {
-    HANGING_DICT_VALUE: ("hanging", " in dict value"),
-    HANGING: ("hanging", ""),
-    HANGING_BLOCK: ("hanging", " before block"),
-    CONTINUED: ("continued", ""),
-    CONTINUED_BLOCK: ("continued", " before block"),
-}
-
-_CONTINUATION_HINT_MESSAGE = " (%s %d space%s)"  # Ex: (remove 2 spaces)
-
-
-def _Indentations(*args):
-    """Valid indentation strings for a continued line."""
-    return {a: None for a in args}
-
-
-def _BeforeBlockIndentations(single, with_body):
-    """Valid alternative indentation strings for continued lines before blocks.
-
-    :param int single: Valid indentation string for statements on a single logical line.
-    :param int with_body: Valid indentation string for statements on several lines.
-
-    :returns: A dictionary mapping indent offsets to a string representing
-        whether the indent if for a line or block.
-    :rtype: dict
-    """
-    return {single: SINGLE_LINE, with_body: WITH_BODY}
-
-
-class TokenWrapper:
-    """A wrapper for readable access to token information."""
-
-    def __init__(self, tokens):
-        self._tokens = tokens
-
-    def token(self, idx):
-        return self._tokens[idx][1]
-
-    def type(self, idx):
-        return self._tokens[idx][0]
-
-    def start_line(self, idx):
-        return self._tokens[idx][2][0]
-
-    def start_col(self, idx):
-        return self._tokens[idx][2][1]
-
-    def line(self, idx):
-        return self._tokens[idx][4]
-
-    def line_indent(self, idx):
-        """Get the string of TABs and Spaces used for indentation of the line of this token"""
-        return _get_indent_string(self.line(idx))
-
-    def token_indent(self, idx):
-        """Get an indentation string for hanging indentation, consisting of the line-indent plus
-        a number of spaces to fill up to the column of this token.
-
-        e.g. the token indent for foo
-        in "<TAB><TAB>print(foo)"
-        is "<TAB><TAB>      "
-        """
-        line_indent = self.line_indent(idx)
-        return line_indent + " " * (self.start_col(idx) - len(line_indent))
-
-
-class ContinuedLineState:
-    """Tracker for continued indentation inside a logical line."""
-
-    def __init__(self, tokens, config):
-        self._line_start = -1
-        self._cont_stack = []
-        self._is_block_opener = False
-        self.retained_warnings = []
-        self._config = config
-        self._tokens = TokenWrapper(tokens)
-
-    @property
-    def has_content(self):
-        return bool(self._cont_stack)
-
-    @property
-    def _block_indent_string(self):
-        return self._config.indent_string.replace("\\t", "\t")
-
-    @property
-    def _continuation_string(self):
-        return self._block_indent_string[0] * self._config.indent_after_paren
-
-    @property
-    def _continuation_size(self):
-        return self._config.indent_after_paren
-
-    def handle_line_start(self, pos):
-        """Record the first non-junk token at the start of a line."""
-        if self._line_start > -1:
-            return
-
-        check_token_position = pos
-        if self._tokens.token(pos) == _ASYNC_TOKEN:
-            check_token_position += 1
-        self._is_block_opener = (
-            self._tokens.token(check_token_position) in _CONTINUATION_BLOCK_OPENERS
-        )
-        self._line_start = pos
-
-    def next_physical_line(self):
-        """Prepares the tracker for a new physical line (NL)."""
-        self._line_start = -1
-        self._is_block_opener = False
-
-    def next_logical_line(self):
-        """Prepares the tracker for a new logical line (NEWLINE).
-
-        A new logical line only starts with block indentation.
-        """
-        self.next_physical_line()
-        self.retained_warnings = []
-        self._cont_stack = []
-
-    def add_block_warning(self, token_position, state, valid_indentations):
-        self.retained_warnings.append((token_position, state, valid_indentations))
-
-    def get_valid_indentations(self, idx):
-        """Returns the valid offsets for the token at the given position."""
-        # The closing brace on a dict or the 'for' in a dict comprehension may
-        # reset two indent levels because the dict value is ended implicitly
-        stack_top = -1
-        if (
-            self._tokens.token(idx) in ("}", "for")
-            and self._cont_stack[-1].token == ":"
-        ):
-            stack_top = -2
-        indent = self._cont_stack[stack_top]
-        if self._tokens.token(idx) in _CLOSING_BRACKETS:
-            valid_indentations = indent.valid_outdent_strings
-        else:
-            valid_indentations = indent.valid_continuation_strings
-        return indent, valid_indentations.copy()
-
-    def _hanging_indent_after_bracket(self, bracket, position):
-        """Extracts indentation information for a hanging indent
-
-        Case of hanging indent after a bracket (including parenthesis)
-
-        :param str bracket: bracket in question
-        :param int position: Position of bracket in self._tokens
-
-        :returns: the state and valid positions for hanging indentation
-        :rtype: _ContinuedIndent
-        """
-        indentation = self._tokens.line_indent(position)
-        if (
-            self._is_block_opener
-            and self._continuation_string == self._block_indent_string
-        ):
-            return _ContinuedIndent(
-                HANGING_BLOCK,
-                bracket,
-                position,
-                _Indentations(indentation + self._continuation_string, indentation),
-                _BeforeBlockIndentations(
-                    indentation + self._continuation_string,
-                    indentation + self._continuation_string * 2,
-                ),
-            )
-        if bracket == ":":
-            # If the dict key was on the same line as the open brace, the new
-            # correct indent should be relative to the key instead of the
-            # current indent level
-            paren_align = self._cont_stack[-1].valid_outdent_strings
-            next_align = self._cont_stack[-1].valid_continuation_strings.copy()
-            next_align_keys = list(next_align.keys())
-            next_align[next_align_keys[0] + self._continuation_string] = True
-            # Note that the continuation of
-            # d = {
-            #       'a': 'b'
-            #            'c'
-            # }
-            # is handled by the special-casing for hanging continued string indents.
-            return _ContinuedIndent(
-                HANGING_DICT_VALUE, bracket, position, paren_align, next_align
-            )
-        return _ContinuedIndent(
-            HANGING,
-            bracket,
-            position,
-            _Indentations(indentation, indentation + self._continuation_string),
-            _Indentations(indentation + self._continuation_string),
-        )
-
-    def _continuation_inside_bracket(self, bracket, position):
-        """Extracts indentation information for a continued indent."""
-        indentation = self._tokens.line_indent(position)
-        token_indent = self._tokens.token_indent(position)
-        next_token_indent = self._tokens.token_indent(position + 1)
-        if (
-            self._is_block_opener
-            and next_token_indent == indentation + self._block_indent_string
-        ):
-            return _ContinuedIndent(
-                CONTINUED_BLOCK,
-                bracket,
-                position,
-                _Indentations(token_indent),
-                _BeforeBlockIndentations(
-                    next_token_indent, next_token_indent + self._continuation_string
-                ),
-            )
-        return _ContinuedIndent(
-            CONTINUED,
-            bracket,
-            position,
-            _Indentations(token_indent, next_token_indent),
-            _Indentations(next_token_indent),
-        )
-
-    def pop_token(self):
-        self._cont_stack.pop()
-
-    def push_token(self, token, position):
-        """Pushes a new token for continued indentation on the stack.
-
-        Tokens that can modify continued indentation offsets are:
-          * opening brackets
-          * 'lambda'
-          * : inside dictionaries
-
-        push_token relies on the caller to filter out those
-        interesting tokens.
-
-        :param int token: The concrete token
-        :param int position: The position of the token in the stream.
-        """
-        if _token_followed_by_eol(self._tokens, position):
-            self._cont_stack.append(self._hanging_indent_after_bracket(token, position))
-        else:
-            self._cont_stack.append(self._continuation_inside_bracket(token, position))
-
-
-class FormatChecker(BaseTokenChecker):
-    """checks for :
-    * unauthorized constructions
-    * strict indentation
-    * line length
-    """
-
-    __implements__ = (ITokenChecker, IAstroidChecker, IRawChecker)
-
-    # configuration section name
-    name = "format"
-    # messages
-    msgs = MSGS
-    # configuration options
-    # for available dict keys/values see the optik parser 'add_option' method
-    options = (
-        (
-            "max-line-length",
-            {
-                "default": 100,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of characters on a single line.",
-            },
-        ),
-        (
-            "ignore-long-lines",
-            {
-                "type": "regexp",
-                "metavar": "<regexp>",
-                "default": r"^\s*(# )?<?https?://\S+>?$",
-                "help": (
-                    "Regexp for a line that is allowed to be longer than " "the limit."
-                ),
-            },
-        ),
-        (
-            "single-line-if-stmt",
-            {
-                "default": False,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": (
-                    "Allow the body of an if to be on the same "
-                    "line as the test if there is no else."
-                ),
-            },
-        ),
-        (
-            "single-line-class-stmt",
-            {
-                "default": False,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": (
-                    "Allow the body of a class to be on the same "
-                    "line as the declaration if body contains "
-                    "single statement."
-                ),
-            },
-        ),
-        (
-            "no-space-check",
-            {
-                "default": ",".join(_DEFAULT_NO_SPACE_CHECK_CHOICES),
-                "metavar": ",".join(_NO_SPACE_CHECK_CHOICES),
-                "type": "multiple_choice",
-                "choices": _NO_SPACE_CHECK_CHOICES,
-                "help": (
-                    "List of optional constructs for which whitespace "
-                    "checking is disabled. "
-                    "`" + _DICT_SEPARATOR + "` is used to allow tabulation "
-                    "in dicts, etc.: {1  : 1,\\n222: 2}. "
-                    "`" + _TRAILING_COMMA + "` allows a space between comma "
-                    "and closing bracket: (a, ). "
-                    "`" + _EMPTY_LINE + "` allows space-only lines."
-                ),
-            },
-        ),
-        (
-            "max-module-lines",
-            {
-                "default": 1000,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of lines in a module.",
-            },
-        ),
-        (
-            "indent-string",
-            {
-                "default": "    ",
-                "type": "non_empty_string",
-                "metavar": "<string>",
-                "help": "String used as indentation unit. This is usually "
-                '"    " (4 spaces) or "\\t" (1 tab).',
-            },
-        ),
-        (
-            "indent-after-paren",
-            {
-                "type": "int",
-                "metavar": "<int>",
-                "default": 4,
-                "help": "Number of spaces of indent required inside a hanging "
-                "or continued line.",
-            },
-        ),
-        (
-            "expected-line-ending-format",
-            {
-                "type": "choice",
-                "metavar": "<empty or LF or CRLF>",
-                "default": "",
-                "choices": ["", "LF", "CRLF"],
-                "help": (
-                    "Expected format of line ending, "
-                    "e.g. empty (any line ending), LF or CRLF."
-                ),
-            },
-        ),
-    )
-
-    def __init__(self, linter=None):
-        BaseTokenChecker.__init__(self, linter)
-        self._lines = None
-        self._visited_lines = None
-        self._bracket_stack = [None]
-
-    def _pop_token(self):
-        self._bracket_stack.pop()
-        self._current_line.pop_token()
-
-    def _push_token(self, token, idx):
-        self._bracket_stack.append(token)
-        self._current_line.push_token(token, idx)
-
-    def new_line(self, tokens, line_end, line_start):
-        """a new line has been encountered, process it if necessary"""
-        if _last_token_on_line_is(tokens, line_end, ";"):
-            self.add_message("unnecessary-semicolon", line=tokens.start_line(line_end))
-
-        line_num = tokens.start_line(line_start)
-        line = tokens.line(line_start)
-        if tokens.type(line_start) not in _JUNK_TOKENS:
-            self._lines[line_num] = line.split("\n")[0]
-        self.check_lines(line, line_num)
-
-    def process_module(self, _module):
-        self._keywords_with_parens = set()
-
-    def _check_keyword_parentheses(self, tokens, start):
-        """Check that there are not unnecessary parens after a keyword.
-
-        Parens are unnecessary if there is exactly one balanced outer pair on a
-        line, and it is followed by a colon, and contains no commas (i.e. is not a
-        tuple).
-
-        Args:
-        tokens: list of Tokens; the entire list of Tokens.
-        start: int; the position of the keyword in the token list.
-        """
-        # If the next token is not a paren, we're fine.
-        if self._inside_brackets(":") and tokens[start][1] == "for":
-            self._pop_token()
-        if tokens[start + 1][1] != "(":
-            return
-
-        found_and_or = False
-        depth = 0
-        keyword_token = str(tokens[start][1])
-        line_num = tokens[start][2][0]
-
-        for i in range(start, len(tokens) - 1):
-            token = tokens[i]
-
-            # If we hit a newline, then assume any parens were for continuation.
-            if token[0] == tokenize.NL:
-                return
-
-            if token[1] == "(":
-                depth += 1
-            elif token[1] == ")":
-                depth -= 1
-                if depth:
-                    continue
-                # ')' can't happen after if (foo), since it would be a syntax error.
-                if tokens[i + 1][1] in (":", ")", "]", "}", "in") or tokens[i + 1][
-                    0
-                ] in (tokenize.NEWLINE, tokenize.ENDMARKER, tokenize.COMMENT):
-                    # The empty tuple () is always accepted.
-                    if i == start + 2:
-                        return
-                    if keyword_token == "not":
-                        if not found_and_or:
-                            self.add_message(
-                                "superfluous-parens", line=line_num, args=keyword_token
-                            )
-                    elif keyword_token in ("return", "yield"):
-                        self.add_message(
-                            "superfluous-parens", line=line_num, args=keyword_token
-                        )
-                    elif keyword_token not in self._keywords_with_parens:
-                        if not found_and_or:
-                            self.add_message(
-                                "superfluous-parens", line=line_num, args=keyword_token
-                            )
-                return
-            elif depth == 1:
-                # This is a tuple, which is always acceptable.
-                if token[1] == ",":
-                    return
-                # 'and' and 'or' are the only boolean operators with lower precedence
-                # than 'not', so parens are only required when they are found.
-                if token[1] in ("and", "or"):
-                    found_and_or = True
-                # A yield inside an expression must always be in parentheses,
-                # quit early without error.
-                elif token[1] == "yield":
-                    return
-                # A generator expression always has a 'for' token in it, and
-                # the 'for' token is only legal inside parens when it is in a
-                # generator expression.  The parens are necessary here, so bail
-                # without an error.
-                elif token[1] == "for":
-                    return
-
-    def _opening_bracket(self, tokens, i):
-        self._push_token(tokens[i][1], i)
-        # Special case: ignore slices
-        if tokens[i][1] == "[" and tokens[i + 1][1] == ":":
-            return
-
-        if i > 0 and (
-            tokens[i - 1][0] == tokenize.NAME
-            and not (keyword.iskeyword(tokens[i - 1][1]))
-            or tokens[i - 1][1] in _CLOSING_BRACKETS
-        ):
-            self._check_space(tokens, i, (_MUST_NOT, _MUST_NOT))
-        else:
-            self._check_space(tokens, i, (_IGNORE, _MUST_NOT))
-
-    def _closing_bracket(self, tokens, i):
-        if self._inside_brackets(":"):
-            self._pop_token()
-        self._pop_token()
-        # Special case: ignore slices
-        if tokens[i - 1][1] == ":" and tokens[i][1] == "]":
-            return
-        policy_before = _MUST_NOT
-        if tokens[i][1] in _CLOSING_BRACKETS and tokens[i - 1][1] == ",":
-            if _TRAILING_COMMA in self.config.no_space_check:
-                policy_before = _IGNORE
-
-        self._check_space(tokens, i, (policy_before, _IGNORE))
-
-    def _has_valid_type_annotation(self, tokens, i):
-        """Extended check of PEP-484 type hint presence"""
-        if not self._inside_brackets("("):
-            return False
-        # token_info
-        # type string start end line
-        #  0      1     2    3    4
-        bracket_level = 0
-        for token in tokens[i - 1 :: -1]:
-            if token[1] == ":":
-                return True
-            if token[1] == "(":
-                return False
-            if token[1] == "]":
-                bracket_level += 1
-            elif token[1] == "[":
-                bracket_level -= 1
-            elif token[1] == ",":
-                if not bracket_level:
-                    return False
-            elif token[1] in (".", "..."):
-                continue
-            elif token[0] not in (tokenize.NAME, tokenize.STRING, tokenize.NL):
-                return False
-        return False
-
-    def _check_equals_spacing(self, tokens, i):
-        """Check the spacing of a single equals sign."""
-        if self._has_valid_type_annotation(tokens, i):
-            self._check_space(tokens, i, (_MUST, _MUST))
-        elif self._inside_brackets("(") or self._inside_brackets("lambda"):
-            self._check_space(tokens, i, (_MUST_NOT, _MUST_NOT))
-        else:
-            self._check_space(tokens, i, (_MUST, _MUST))
-
-    def _open_lambda(self, tokens, i):  # pylint:disable=unused-argument
-        self._push_token("lambda", i)
-
-    def _handle_colon(self, tokens, i):
-        # Special case: ignore slices
-        if self._inside_brackets("["):
-            return
-        if self._inside_brackets("{") and _DICT_SEPARATOR in self.config.no_space_check:
-            policy = (_IGNORE, _IGNORE)
-        else:
-            policy = (_MUST_NOT, _MUST)
-        self._check_space(tokens, i, policy)
-
-        if self._inside_brackets("lambda"):
-            self._pop_token()
-        elif self._inside_brackets("{"):
-            self._push_token(":", i)
-
-    def _handle_comma(self, tokens, i):
-        # Only require a following whitespace if this is
-        # not a hanging comma before a closing bracket.
-        if tokens[i + 1][1] in _CLOSING_BRACKETS:
-            self._check_space(tokens, i, (_MUST_NOT, _IGNORE))
-        else:
-            self._check_space(tokens, i, (_MUST_NOT, _MUST))
-        if self._inside_brackets(":"):
-            self._pop_token()
-
-    def _check_surrounded_by_space(self, tokens, i):
-        """Check that a binary operator is surrounded by exactly one space."""
-        self._check_space(tokens, i, (_MUST, _MUST))
-
-    def _check_space(self, tokens, i, policies):
-        def _policy_string(policy):
-            if policy == _MUST:
-                return "Exactly one", "required"
-            return "No", "allowed"
-
-        def _name_construct(token):
-            if token[1] == ",":
-                return "comma"
-            if token[1] == ":":
-                return ":"
-            if token[1] in "()[]{}":
-                return "bracket"
-            if token[1] in ("<", ">", "<=", ">=", "!=", "=="):
-                return "comparison"
-            if self._inside_brackets("("):
-                return "keyword argument assignment"
-            return "assignment"
-
-        good_space = [True, True]
-        token = tokens[i]
-        pairs = [(tokens[i - 1], token), (token, tokens[i + 1])]
-
-        for other_idx, (policy, token_pair) in enumerate(zip(policies, pairs)):
-            if token_pair[other_idx][0] in _EOL or policy == _IGNORE:
-                continue
-
-            distance = _column_distance(*token_pair)
-            if distance is None:
-                continue
-            good_space[other_idx] = (policy == _MUST and distance == 1) or (
-                policy == _MUST_NOT and distance == 0
-            )
-
-        warnings = []
-        if not any(good_space) and policies[0] == policies[1]:
-            warnings.append((policies[0], "around"))
-        else:
-            for ok, policy, position in zip(good_space, policies, ("before", "after")):
-                if not ok:
-                    warnings.append((policy, position))
-        for policy, position in warnings:
-            construct = _name_construct(token)
-            count, state = _policy_string(policy)
-            self.add_message(
-                "bad-whitespace",
-                line=token[2][0],
-                args=(count, state, position, construct, _underline_token(token)),
-                col_offset=token[2][1],
-            )
-
-    def _inside_brackets(self, left):
-        return self._bracket_stack[-1] == left
-
-    def _prepare_token_dispatcher(self):
-        raw = [
-            (_KEYWORD_TOKENS, self._check_keyword_parentheses),
-            (_OPENING_BRACKETS, self._opening_bracket),
-            (_CLOSING_BRACKETS, self._closing_bracket),
-            (["="], self._check_equals_spacing),
-            (_SPACED_OPERATORS, self._check_surrounded_by_space),
-            ([","], self._handle_comma),
-            ([":"], self._handle_colon),
-            (["lambda"], self._open_lambda),
-        ]
-
-        dispatch = {}
-        for tokens, handler in raw:
-            for token in tokens:
-                dispatch[token] = handler
-        return dispatch
-
-    def process_tokens(self, tokens):
-        """process tokens and search for :
-
-         _ non strict indentation (i.e. not always using the <indent> parameter as
-           indent unit)
-         _ too long lines (i.e. longer than <max_chars>)
-         _ optionally bad construct (if given, bad_construct must be a compiled
-           regular expression).
-        """
-        self._bracket_stack = [None]
-        indents = [0]
-        check_equal = False
-        line_num = 0
-        self._lines = {}
-        self._visited_lines = {}
-        token_handlers = self._prepare_token_dispatcher()
-        self._last_line_ending = None
-        last_blank_line_num = 0
-
-        self._current_line = ContinuedLineState(tokens, self.config)
-        for idx, (tok_type, token, start, _, line) in enumerate(tokens):
-            if start[0] != line_num:
-                line_num = start[0]
-                # A tokenizer oddity: if an indented line contains a multi-line
-                # docstring, the line member of the INDENT token does not contain
-                # the full line; therefore we check the next token on the line.
-                if tok_type == tokenize.INDENT:
-                    self.new_line(TokenWrapper(tokens), idx - 1, idx + 1)
-                else:
-                    self.new_line(TokenWrapper(tokens), idx - 1, idx)
-
-            if tok_type == tokenize.NEWLINE:
-                # a program statement, or ENDMARKER, will eventually follow,
-                # after some (possibly empty) run of tokens of the form
-                #     (NL | COMMENT)* (INDENT | DEDENT+)?
-                # If an INDENT appears, setting check_equal is wrong, and will
-                # be undone when we see the INDENT.
-                check_equal = True
-                self._process_retained_warnings(TokenWrapper(tokens), idx)
-                self._current_line.next_logical_line()
-                self._check_line_ending(token, line_num)
-            elif tok_type == tokenize.INDENT:
-                check_equal = False
-                self.check_indent_level(token, indents[-1] + 1, line_num)
-                indents.append(indents[-1] + 1)
-            elif tok_type == tokenize.DEDENT:
-                # there's nothing we need to check here!  what's important is
-                # that when the run of DEDENTs ends, the indentation of the
-                # program statement (or ENDMARKER) that triggered the run is
-                # equal to what's left at the top of the indents stack
-                check_equal = True
-                if len(indents) > 1:
-                    del indents[-1]
-            elif tok_type == tokenize.NL:
-                if not line.strip("\r\n"):
-                    last_blank_line_num = line_num
-                self._check_continued_indentation(TokenWrapper(tokens), idx + 1)
-                self._current_line.next_physical_line()
-            elif tok_type not in (tokenize.COMMENT, tokenize.ENCODING):
-                self._current_line.handle_line_start(idx)
-                # This is the first concrete token following a NEWLINE, so it
-                # must be the first token of the next program statement, or an
-                # ENDMARKER; the "line" argument exposes the leading whitespace
-                # for this statement; in the case of ENDMARKER, line is an empty
-                # string, so will properly match the empty string with which the
-                # "indents" stack was seeded
-                if check_equal:
-                    check_equal = False
-                    self.check_indent_level(line, indents[-1], line_num)
-
-            if tok_type == tokenize.NUMBER and token.endswith("l"):
-                self.add_message("lowercase-l-suffix", line=line_num)
-
-            try:
-                handler = token_handlers[token]
-            except KeyError:
-                pass
-            else:
-                handler(tokens, idx)
-
-        line_num -= 1  # to be ok with "wc -l"
-        if line_num > self.config.max_module_lines:
-            # Get the line where the too-many-lines (or its message id)
-            # was disabled or default to 1.
-            message_definition = self.linter.msgs_store.get_message_definitions(
-                "too-many-lines"
-            )[0]
-            names = (message_definition.msgid, "too-many-lines")
-            line = next(filter(None, map(self.linter._pragma_lineno.get, names)), 1)
-            self.add_message(
-                "too-many-lines",
-                args=(line_num, self.config.max_module_lines),
-                line=line,
-            )
-
-        # See if there are any trailing lines.  Do not complain about empty
-        # files like __init__.py markers.
-        if line_num == last_blank_line_num and line_num > 0:
-            self.add_message("trailing-newlines", line=line_num)
-
-    def _check_line_ending(self, line_ending, line_num):
-        # check if line endings are mixed
-        if self._last_line_ending is not None:
-            # line_ending == "" indicates a synthetic newline added at
-            # the end of a file that does not, in fact, end with a
-            # newline.
-            if line_ending and line_ending != self._last_line_ending:
-                self.add_message("mixed-line-endings", line=line_num)
-
-        self._last_line_ending = line_ending
-
-        # check if line ending is as expected
-        expected = self.config.expected_line_ending_format
-        if expected:
-            # reduce multiple \n\n\n\n to one \n
-            line_ending = reduce(lambda x, y: x + y if x != y else x, line_ending, "")
-            line_ending = "LF" if line_ending == "\n" else "CRLF"
-            if line_ending != expected:
-                self.add_message(
-                    "unexpected-line-ending-format",
-                    args=(line_ending, expected),
-                    line=line_num,
-                )
-
-    def _process_retained_warnings(self, tokens, current_pos):
-        single_line_block_stmt = not _last_token_on_line_is(tokens, current_pos, ":")
-
-        for indent_pos, state, indentations in self._current_line.retained_warnings:
-            block_type = indentations[tokens.token_indent(indent_pos)]
-            hints = {k: v for k, v in indentations.items() if v != block_type}
-            if single_line_block_stmt and block_type == WITH_BODY:
-                self._add_continuation_message(state, hints, tokens, indent_pos)
-            elif not single_line_block_stmt and block_type == SINGLE_LINE:
-                self._add_continuation_message(state, hints, tokens, indent_pos)
-
-    def _check_continued_indentation(self, tokens, next_idx):
-        def same_token_around_nl(token_type):
-            return (
-                tokens.type(next_idx) == token_type
-                and tokens.type(next_idx - 2) == token_type
-            )
-
-        # Do not issue any warnings if the next line is empty.
-        if not self._current_line.has_content or tokens.type(next_idx) == tokenize.NL:
-            return
-
-        state, valid_indentations = self._current_line.get_valid_indentations(next_idx)
-        # Special handling for hanging comments and strings. If the last line ended
-        # with a comment (string) and the new line contains only a comment, the line
-        # may also be indented to the start of the previous token.
-        if same_token_around_nl(tokenize.COMMENT) or same_token_around_nl(
-            tokenize.STRING
-        ):
-            valid_indentations[tokens.token_indent(next_idx - 2)] = True
-
-        # We can only decide if the indentation of a continued line before opening
-        # a new block is valid once we know of the body of the block is on the
-        # same line as the block opener. Since the token processing is single-pass,
-        # emitting those warnings is delayed until the block opener is processed.
-        if (
-            state.context_type in (HANGING_BLOCK, CONTINUED_BLOCK)
-            and tokens.token_indent(next_idx) in valid_indentations
-        ):
-            self._current_line.add_block_warning(next_idx, state, valid_indentations)
-        elif tokens.token_indent(next_idx) not in valid_indentations:
-            length_indentation = len(tokens.token_indent(next_idx))
-            if not any(
-                length_indentation == 2 * len(indentation)
-                for indentation in valid_indentations
-            ):
-                self._add_continuation_message(
-                    state, valid_indentations, tokens, next_idx
-                )
-
-    def _add_continuation_message(self, state, indentations, tokens, position):
-        readable_type, readable_position = _CONTINUATION_MSG_PARTS[state.context_type]
-        hint_line, delta_message = _get_indent_hint_line(
-            indentations, tokens.token_indent(position)
-        )
-        self.add_message(
-            "bad-continuation",
-            line=tokens.start_line(position),
-            args=(
-                readable_type,
-                readable_position,
-                delta_message,
-                tokens.line(position),
-                hint_line,
-            ),
-        )
-
-    @check_messages("multiple-statements")
-    def visit_default(self, node):
-        """check the node line number and check it if not yet done"""
-        if not node.is_statement:
-            return
-        if not node.root().pure_python:
-            return
-        prev_sibl = node.previous_sibling()
-        if prev_sibl is not None:
-            prev_line = prev_sibl.fromlineno
-        else:
-            # The line on which a finally: occurs in a try/finally
-            # is not directly represented in the AST. We infer it
-            # by taking the last line of the body and adding 1, which
-            # should be the line of finally:
-            if (
-                isinstance(node.parent, nodes.TryFinally)
-                and node in node.parent.finalbody
-            ):
-                prev_line = node.parent.body[0].tolineno + 1
-            else:
-                prev_line = node.parent.statement().fromlineno
-        line = node.fromlineno
-        assert line, node
-        if prev_line == line and self._visited_lines.get(line) != 2:
-            self._check_multi_statement_line(node, line)
-            return
-        if line in self._visited_lines:
-            return
-        try:
-            tolineno = node.blockstart_tolineno
-        except AttributeError:
-            tolineno = node.tolineno
-        assert tolineno, node
-        lines = []
-        for line in range(line, tolineno + 1):
-            self._visited_lines[line] = 1
-            try:
-                lines.append(self._lines[line].rstrip())
-            except KeyError:
-                lines.append("")
-
-    def _check_multi_statement_line(self, node, line):
-        """Check for lines containing multiple statements."""
-        # Do not warn about multiple nested context managers
-        # in with statements.
-        if isinstance(node, nodes.With):
-            return
-        # For try... except... finally..., the two nodes
-        # appear to be on the same line due to how the AST is built.
-        if isinstance(node, nodes.TryExcept) and isinstance(
-            node.parent, nodes.TryFinally
-        ):
-            return
-        if (
-            isinstance(node.parent, nodes.If)
-            and not node.parent.orelse
-            and self.config.single_line_if_stmt
-        ):
-            return
-        if (
-            isinstance(node.parent, nodes.ClassDef)
-            and len(node.parent.body) == 1
-            and self.config.single_line_class_stmt
-        ):
-            return
-        self.add_message("multiple-statements", node=node)
-        self._visited_lines[line] = 2
-
-    def check_lines(self, lines, i):
-        """check lines have less than a maximum number of characters
-        """
-        max_chars = self.config.max_line_length
-        ignore_long_line = self.config.ignore_long_lines
-
-        def check_line(line, i):
-            if not line.endswith("\n"):
-                self.add_message("missing-final-newline", line=i)
-            else:
-                # exclude \f (formfeed) from the rstrip
-                stripped_line = line.rstrip("\t\n\r\v ")
-                if not stripped_line and _EMPTY_LINE in self.config.no_space_check:
-                    # allow empty lines
-                    pass
-                elif line[len(stripped_line) :] not in ("\n", "\r\n"):
-                    self.add_message(
-                        "trailing-whitespace", line=i, col_offset=len(stripped_line)
-                    )
-                # Don't count excess whitespace in the line length.
-                line = stripped_line
-            mobj = OPTION_RGX.search(line)
-            if mobj and "=" in line:
-                front_of_equal, _, back_of_equal = mobj.group(1).partition("=")
-                if front_of_equal.strip() == "disable":
-                    if "line-too-long" in {
-                        _msg_id.strip() for _msg_id in back_of_equal.split(",")
-                    }:
-                        return None
-                    line = line.rsplit("#", 1)[0].rstrip()
-
-            if len(line) > max_chars and not ignore_long_line.search(line):
-                self.add_message("line-too-long", line=i, args=(len(line), max_chars))
-            return i + 1
-
-        unsplit_ends = {
-            "\v",
-            "\x0b",
-            "\f",
-            "\x0c",
-            "\x1c",
-            "\x1d",
-            "\x1e",
-            "\x85",
-            "\u2028",
-            "\u2029",
-        }
-        unsplit = []
-        for line in lines.splitlines(True):
-            if line[-1] in unsplit_ends:
-                unsplit.append(line)
-                continue
-
-            if unsplit:
-                unsplit.append(line)
-                line = "".join(unsplit)
-                unsplit = []
-
-            i = check_line(line, i)
-            if i is None:
-                break
-
-        if unsplit:
-            check_line("".join(unsplit), i)
-
-    def check_indent_level(self, string, expected, line_num):
-        """return the indent level of the string
-        """
-        indent = self.config.indent_string
-        if indent == "\\t":  # \t is not interpreted in the configuration file
-            indent = "\t"
-        level = 0
-        unit_size = len(indent)
-        while string[:unit_size] == indent:
-            string = string[unit_size:]
-            level += 1
-        suppl = ""
-        while string and string[0] in " \t":
-            if string[0] != indent[0]:
-                if string[0] == "\t":
-                    args = ("tab", "space")
-                else:
-                    args = ("space", "tab")
-                self.add_message("mixed-indentation", args=args, line=line_num)
-                return level
-            suppl += string[0]
-            string = string[1:]
-        if level != expected or suppl:
-            i_type = "spaces"
-            if indent[0] == "\t":
-                i_type = "tabs"
-            self.add_message(
-                "bad-indentation",
-                line=line_num,
-                args=(level * unit_size + len(suppl), i_type, expected * unit_size),
-            )
-        return None
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(FormatChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/imports.py b/venv/Lib/site-packages/pylint/checkers/imports.py
deleted file mode 100644
index 42d4362..0000000
--- a/venv/Lib/site-packages/pylint/checkers/imports.py
+++ /dev/null
@@ -1,981 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2013 buck@yelp.com <buck@yelp.com>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2015 Cezar <celnazli@bitdefender.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Noam Yorav-Raphael <noamraph@gmail.com>
-# Copyright (c) 2015 James Morgensen <james.morgensen@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Jared Garst <cultofjared@gmail.com>
-# Copyright (c) 2016 Maik Röder <maikroeder@gmail.com>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Michka Popoff <michkapopoff@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 Erik Wright <erik.wright@shopify.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Marianna Polatoglou <mpolatoglou@bloomberg.net>
-# Copyright (c) 2019 Paul Renvoise <renvoisepaul@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""imports checkers for Python code"""
-
-import collections
-import copy
-import os
-import sys
-from distutils import sysconfig
-
-import astroid
-import isort
-from astroid import modutils
-from astroid.decorators import cached
-
-from pylint.checkers import BaseChecker
-from pylint.checkers.utils import (
-    check_messages,
-    is_from_fallback_block,
-    node_ignores_exception,
-)
-from pylint.exceptions import EmptyReportError
-from pylint.graph import DotBackend, get_cycles
-from pylint.interfaces import IAstroidChecker
-from pylint.reporters.ureports.nodes import Paragraph, VerbatimText
-from pylint.utils import get_global_option
-
-
-def _qualified_names(modname):
-    """Split the names of the given module into subparts
-
-    For example,
-        _qualified_names('pylint.checkers.ImportsChecker')
-    returns
-        ['pylint', 'pylint.checkers', 'pylint.checkers.ImportsChecker']
-    """
-    names = modname.split(".")
-    return [".".join(names[0 : i + 1]) for i in range(len(names))]
-
-
-def _get_import_name(importnode, modname):
-    """Get a prepared module name from the given import node
-
-    In the case of relative imports, this will return the
-    absolute qualified module name, which might be useful
-    for debugging. Otherwise, the initial module name
-    is returned unchanged.
-    """
-    if isinstance(importnode, astroid.ImportFrom):
-        if importnode.level:
-            root = importnode.root()
-            if isinstance(root, astroid.Module):
-                modname = root.relative_to_absolute_name(
-                    modname, level=importnode.level
-                )
-    return modname
-
-
-def _get_first_import(node, context, name, base, level, alias):
-    """return the node where [base.]<name> is imported or None if not found
-    """
-    fullname = "%s.%s" % (base, name) if base else name
-
-    first = None
-    found = False
-    for first in context.body:
-        if first is node:
-            continue
-        if first.scope() is node.scope() and first.fromlineno > node.fromlineno:
-            continue
-        if isinstance(first, astroid.Import):
-            if any(fullname == iname[0] for iname in first.names):
-                found = True
-                break
-        elif isinstance(first, astroid.ImportFrom):
-            if level == first.level:
-                for imported_name, imported_alias in first.names:
-                    if fullname == "%s.%s" % (first.modname, imported_name):
-                        found = True
-                        break
-                    if (
-                        name != "*"
-                        and name == imported_name
-                        and not (alias or imported_alias)
-                    ):
-                        found = True
-                        break
-                if found:
-                    break
-    if found and not astroid.are_exclusive(first, node):
-        return first
-    return None
-
-
-def _ignore_import_failure(node, modname, ignored_modules):
-    for submodule in _qualified_names(modname):
-        if submodule in ignored_modules:
-            return True
-
-    return node_ignores_exception(node, ImportError)
-
-
-# utilities to represents import dependencies as tree and dot graph ###########
-
-
-def _make_tree_defs(mod_files_list):
-    """get a list of 2-uple (module, list_of_files_which_import_this_module),
-    it will return a dictionary to represent this as a tree
-    """
-    tree_defs = {}
-    for mod, files in mod_files_list:
-        node = (tree_defs, ())
-        for prefix in mod.split("."):
-            node = node[0].setdefault(prefix, [{}, []])
-        node[1] += files
-    return tree_defs
-
-
-def _repr_tree_defs(data, indent_str=None):
-    """return a string which represents imports as a tree"""
-    lines = []
-    nodes = data.items()
-    for i, (mod, (sub, files)) in enumerate(sorted(nodes, key=lambda x: x[0])):
-        if not files:
-            files = ""
-        else:
-            files = "(%s)" % ",".join(sorted(files))
-        if indent_str is None:
-            lines.append("%s %s" % (mod, files))
-            sub_indent_str = "  "
-        else:
-            lines.append(r"%s\-%s %s" % (indent_str, mod, files))
-            if i == len(nodes) - 1:
-                sub_indent_str = "%s  " % indent_str
-            else:
-                sub_indent_str = "%s| " % indent_str
-        if sub:
-            lines.append(_repr_tree_defs(sub, sub_indent_str))
-    return "\n".join(lines)
-
-
-def _dependencies_graph(filename, dep_info):
-    """write dependencies as a dot (graphviz) file
-    """
-    done = {}
-    printer = DotBackend(filename[:-4], rankdir="LR")
-    printer.emit('URL="." node[shape="box"]')
-    for modname, dependencies in sorted(dep_info.items()):
-        done[modname] = 1
-        printer.emit_node(modname)
-        for depmodname in dependencies:
-            if depmodname not in done:
-                done[depmodname] = 1
-                printer.emit_node(depmodname)
-    for depmodname, dependencies in sorted(dep_info.items()):
-        for modname in dependencies:
-            printer.emit_edge(modname, depmodname)
-    printer.generate(filename)
-
-
-def _make_graph(filename, dep_info, sect, gtype):
-    """generate a dependencies graph and add some information about it in the
-    report's section
-    """
-    _dependencies_graph(filename, dep_info)
-    sect.append(Paragraph("%simports graph has been written to %s" % (gtype, filename)))
-
-
-# the import checker itself ###################################################
-
-MSGS = {
-    "E0401": (
-        "Unable to import %s",
-        "import-error",
-        "Used when pylint has been unable to import a module.",
-        {"old_names": [("F0401", "old-import-error")]},
-    ),
-    "E0402": (
-        "Attempted relative import beyond top-level package",
-        "relative-beyond-top-level",
-        "Used when a relative import tries to access too many levels "
-        "in the current package.",
-    ),
-    "R0401": (
-        "Cyclic import (%s)",
-        "cyclic-import",
-        "Used when a cyclic import between two or more modules is detected.",
-    ),
-    "W0401": (
-        "Wildcard import %s",
-        "wildcard-import",
-        "Used when `from module import *` is detected.",
-    ),
-    "W0402": (
-        "Uses of a deprecated module %r",
-        "deprecated-module",
-        "Used a module marked as deprecated is imported.",
-    ),
-    "W0404": (
-        "Reimport %r (imported line %s)",
-        "reimported",
-        "Used when a module is reimported multiple times.",
-    ),
-    "W0406": (
-        "Module import itself",
-        "import-self",
-        "Used when a module is importing itself.",
-    ),
-    "W0407": (
-        "Prefer importing %r instead of %r",
-        "preferred-module",
-        "Used when a module imported has a preferred replacement module.",
-    ),
-    "W0410": (
-        "__future__ import is not the first non docstring statement",
-        "misplaced-future",
-        "Python 2.5 and greater require __future__ import to be the "
-        "first non docstring statement in the module.",
-    ),
-    "C0410": (
-        "Multiple imports on one line (%s)",
-        "multiple-imports",
-        "Used when import statement importing multiple modules is detected.",
-    ),
-    "C0411": (
-        "%s should be placed before %s",
-        "wrong-import-order",
-        "Used when PEP8 import order is not respected (standard imports "
-        "first, then third-party libraries, then local imports)",
-    ),
-    "C0412": (
-        "Imports from package %s are not grouped",
-        "ungrouped-imports",
-        "Used when imports are not grouped by packages",
-    ),
-    "C0413": (
-        'Import "%s" should be placed at the top of the module',
-        "wrong-import-position",
-        "Used when code and imports are mixed",
-    ),
-    "C0414": (
-        "Import alias does not rename original package",
-        "useless-import-alias",
-        "Used when an import alias is same as original package."
-        "e.g using import numpy as numpy instead of import numpy as np",
-    ),
-    "C0415": (
-        "Import outside toplevel (%s)",
-        "import-outside-toplevel",
-        "Used when an import statement is used anywhere other than the module "
-        "toplevel. Move this import to the top of the file.",
-    ),
-}
-
-
-DEFAULT_STANDARD_LIBRARY = ()
-DEFAULT_KNOWN_THIRD_PARTY = ("enchant",)
-DEFAULT_PREFERRED_MODULES = ()
-
-
-class ImportsChecker(BaseChecker):
-    """checks for
-    * external modules dependencies
-    * relative / wildcard imports
-    * cyclic imports
-    * uses of deprecated modules
-    * uses of modules instead of preferred modules
-    """
-
-    __implements__ = IAstroidChecker
-
-    name = "imports"
-    msgs = MSGS
-    priority = -2
-    deprecated_modules = ("optparse", "tkinter.tix")
-
-    options = (
-        (
-            "deprecated-modules",
-            {
-                "default": deprecated_modules,
-                "type": "csv",
-                "metavar": "<modules>",
-                "help": "Deprecated modules which should not be used,"
-                " separated by a comma.",
-            },
-        ),
-        (
-            "preferred-modules",
-            {
-                "default": DEFAULT_PREFERRED_MODULES,
-                "type": "csv",
-                "metavar": "<module:preferred-module>",
-                "help": "Couples of modules and preferred modules,"
-                " separated by a comma.",
-            },
-        ),
-        (
-            "import-graph",
-            {
-                "default": "",
-                "type": "string",
-                "metavar": "<file.dot>",
-                "help": "Create a graph of every (i.e. internal and"
-                " external) dependencies in the given file"
-                " (report RP0402 must not be disabled).",
-            },
-        ),
-        (
-            "ext-import-graph",
-            {
-                "default": "",
-                "type": "string",
-                "metavar": "<file.dot>",
-                "help": "Create a graph of external dependencies in the"
-                " given file (report RP0402 must not be disabled).",
-            },
-        ),
-        (
-            "int-import-graph",
-            {
-                "default": "",
-                "type": "string",
-                "metavar": "<file.dot>",
-                "help": "Create a graph of internal dependencies in the"
-                " given file (report RP0402 must not be disabled).",
-            },
-        ),
-        (
-            "known-standard-library",
-            {
-                "default": DEFAULT_STANDARD_LIBRARY,
-                "type": "csv",
-                "metavar": "<modules>",
-                "help": "Force import order to recognize a module as part of "
-                "the standard compatibility libraries.",
-            },
-        ),
-        (
-            "known-third-party",
-            {
-                "default": DEFAULT_KNOWN_THIRD_PARTY,
-                "type": "csv",
-                "metavar": "<modules>",
-                "help": "Force import order to recognize a module as part of "
-                "a third party library.",
-            },
-        ),
-        (
-            "allow-any-import-level",
-            {
-                "default": (),
-                "type": "csv",
-                "metavar": "<modules>",
-                "help": (
-                    "List of modules that can be imported at any level, not just "
-                    "the top level one."
-                ),
-            },
-        ),
-        (
-            "analyse-fallback-blocks",
-            {
-                "default": False,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "Analyse import fallback blocks. This can be used to "
-                "support both Python 2 and 3 compatible code, which "
-                "means that the block might have code that exists "
-                "only in one or another interpreter, leading to false "
-                "positives when analysed.",
-            },
-        ),
-        (
-            "allow-wildcard-with-all",
-            {
-                "default": False,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "Allow wildcard imports from modules that define __all__.",
-            },
-        ),
-    )
-
-    def __init__(self, linter=None):
-        BaseChecker.__init__(self, linter)
-        self.stats = None
-        self.import_graph = None
-        self._imports_stack = []
-        self._first_non_import_node = None
-        self._module_pkg = {}  # mapping of modules to the pkg they belong in
-        self._allow_any_import_level = set()
-        self.reports = (
-            ("RP0401", "External dependencies", self._report_external_dependencies),
-            ("RP0402", "Modules dependencies graph", self._report_dependencies_graph),
-        )
-
-        self._site_packages = self._compute_site_packages()
-
-    @staticmethod
-    def _compute_site_packages():
-        def _normalized_path(path):
-            return os.path.normcase(os.path.abspath(path))
-
-        paths = set()
-        real_prefix = getattr(sys, "real_prefix", None)
-        for prefix in filter(None, (real_prefix, sys.prefix)):
-            path = sysconfig.get_python_lib(prefix=prefix)
-            path = _normalized_path(path)
-            paths.add(path)
-
-        # Handle Debian's derivatives /usr/local.
-        if os.path.isfile("/etc/debian_version"):
-            for prefix in filter(None, (real_prefix, sys.prefix)):
-                libpython = os.path.join(
-                    prefix,
-                    "local",
-                    "lib",
-                    "python" + sysconfig.get_python_version(),
-                    "dist-packages",
-                )
-                paths.add(libpython)
-        return paths
-
-    def open(self):
-        """called before visiting project (i.e set of modules)"""
-        self.linter.add_stats(dependencies={})
-        self.linter.add_stats(cycles=[])
-        self.stats = self.linter.stats
-        self.import_graph = collections.defaultdict(set)
-        self._module_pkg = {}  # mapping of modules to the pkg they belong in
-        self._excluded_edges = collections.defaultdict(set)
-        self._ignored_modules = get_global_option(self, "ignored-modules", default=[])
-        # Build a mapping {'module': 'preferred-module'}
-        self.preferred_modules = dict(
-            module.split(":")
-            for module in self.config.preferred_modules
-            if ":" in module
-        )
-        self._allow_any_import_level = set(self.config.allow_any_import_level)
-
-    def _import_graph_without_ignored_edges(self):
-        filtered_graph = copy.deepcopy(self.import_graph)
-        for node in filtered_graph:
-            filtered_graph[node].difference_update(self._excluded_edges[node])
-        return filtered_graph
-
-    def close(self):
-        """called before visiting project (i.e set of modules)"""
-        if self.linter.is_message_enabled("cyclic-import"):
-            graph = self._import_graph_without_ignored_edges()
-            vertices = list(graph)
-            for cycle in get_cycles(graph, vertices=vertices):
-                self.add_message("cyclic-import", args=" -> ".join(cycle))
-
-    @check_messages(*MSGS)
-    def visit_import(self, node):
-        """triggered when an import statement is seen"""
-        self._check_reimport(node)
-        self._check_import_as_rename(node)
-        self._check_toplevel(node)
-
-        names = [name for name, _ in node.names]
-        if len(names) >= 2:
-            self.add_message("multiple-imports", args=", ".join(names), node=node)
-
-        for name in names:
-            self._check_deprecated_module(node, name)
-            self._check_preferred_module(node, name)
-            imported_module = self._get_imported_module(node, name)
-            if isinstance(node.parent, astroid.Module):
-                # Allow imports nested
-                self._check_position(node)
-            if isinstance(node.scope(), astroid.Module):
-                self._record_import(node, imported_module)
-
-            if imported_module is None:
-                continue
-
-            self._add_imported_module(node, imported_module.name)
-
-    @check_messages(*MSGS)
-    def visit_importfrom(self, node):
-        """triggered when a from statement is seen"""
-        basename = node.modname
-        imported_module = self._get_imported_module(node, basename)
-
-        self._check_import_as_rename(node)
-        self._check_misplaced_future(node)
-        self._check_deprecated_module(node, basename)
-        self._check_preferred_module(node, basename)
-        self._check_wildcard_imports(node, imported_module)
-        self._check_same_line_imports(node)
-        self._check_reimport(node, basename=basename, level=node.level)
-        self._check_toplevel(node)
-
-        if isinstance(node.parent, astroid.Module):
-            # Allow imports nested
-            self._check_position(node)
-        if isinstance(node.scope(), astroid.Module):
-            self._record_import(node, imported_module)
-        if imported_module is None:
-            return
-        for name, _ in node.names:
-            if name != "*":
-                self._add_imported_module(node, "%s.%s" % (imported_module.name, name))
-            else:
-                self._add_imported_module(node, imported_module.name)
-
-    @check_messages(*MSGS)
-    def leave_module(self, node):
-        # Check imports are grouped by category (standard, 3rd party, local)
-        std_imports, ext_imports, loc_imports = self._check_imports_order(node)
-
-        # Check that imports are grouped by package within a given category
-        met_import = set()  #  set for 'import x' style
-        met_from = set()  #  set for 'from x import y' style
-        current_package = None
-        for import_node, import_name in std_imports + ext_imports + loc_imports:
-            if not self.linter.is_message_enabled(
-                "ungrouped-imports", import_node.fromlineno
-            ):
-                continue
-            if isinstance(import_node, astroid.node_classes.ImportFrom):
-                met = met_from
-            else:
-                met = met_import
-            package, _, _ = import_name.partition(".")
-            if current_package and current_package != package and package in met:
-                self.add_message("ungrouped-imports", node=import_node, args=package)
-            current_package = package
-            met.add(package)
-
-        self._imports_stack = []
-        self._first_non_import_node = None
-
-    def compute_first_non_import_node(self, node):
-        if not self.linter.is_message_enabled("wrong-import-position", node.fromlineno):
-            return
-        # if the node does not contain an import instruction, and if it is the
-        # first node of the module, keep a track of it (all the import positions
-        # of the module will be compared to the position of this first
-        # instruction)
-        if self._first_non_import_node:
-            return
-        if not isinstance(node.parent, astroid.Module):
-            return
-        nested_allowed = [astroid.TryExcept, astroid.TryFinally]
-        is_nested_allowed = [
-            allowed for allowed in nested_allowed if isinstance(node, allowed)
-        ]
-        if is_nested_allowed and any(
-            node.nodes_of_class((astroid.Import, astroid.ImportFrom))
-        ):
-            return
-        if isinstance(node, astroid.Assign):
-            # Add compatibility for module level dunder names
-            # https://www.python.org/dev/peps/pep-0008/#module-level-dunder-names
-            valid_targets = [
-                isinstance(target, astroid.AssignName)
-                and target.name.startswith("__")
-                and target.name.endswith("__")
-                for target in node.targets
-            ]
-            if all(valid_targets):
-                return
-        self._first_non_import_node = node
-
-    visit_tryfinally = (
-        visit_tryexcept
-    ) = (
-        visit_assignattr
-    ) = (
-        visit_assign
-    ) = (
-        visit_ifexp
-    ) = visit_comprehension = visit_expr = visit_if = compute_first_non_import_node
-
-    def visit_functiondef(self, node):
-        if not self.linter.is_message_enabled("wrong-import-position", node.fromlineno):
-            return
-        # If it is the first non import instruction of the module, record it.
-        if self._first_non_import_node:
-            return
-
-        # Check if the node belongs to an `If` or a `Try` block. If they
-        # contain imports, skip recording this node.
-        if not isinstance(node.parent.scope(), astroid.Module):
-            return
-
-        root = node
-        while not isinstance(root.parent, astroid.Module):
-            root = root.parent
-
-        if isinstance(root, (astroid.If, astroid.TryFinally, astroid.TryExcept)):
-            if any(root.nodes_of_class((astroid.Import, astroid.ImportFrom))):
-                return
-
-        self._first_non_import_node = node
-
-    visit_classdef = visit_for = visit_while = visit_functiondef
-
-    def _check_misplaced_future(self, node):
-        basename = node.modname
-        if basename == "__future__":
-            # check if this is the first non-docstring statement in the module
-            prev = node.previous_sibling()
-            if prev:
-                # consecutive future statements are possible
-                if not (
-                    isinstance(prev, astroid.ImportFrom)
-                    and prev.modname == "__future__"
-                ):
-                    self.add_message("misplaced-future", node=node)
-            return
-
-    def _check_same_line_imports(self, node):
-        # Detect duplicate imports on the same line.
-        names = (name for name, _ in node.names)
-        counter = collections.Counter(names)
-        for name, count in counter.items():
-            if count > 1:
-                self.add_message("reimported", node=node, args=(name, node.fromlineno))
-
-    def _check_position(self, node):
-        """Check `node` import or importfrom node position is correct
-
-        Send a message  if `node` comes before another instruction
-        """
-        # if a first non-import instruction has already been encountered,
-        # it means the import comes after it and therefore is not well placed
-        if self._first_non_import_node:
-            self.add_message("wrong-import-position", node=node, args=node.as_string())
-
-    def _record_import(self, node, importedmodnode):
-        """Record the package `node` imports from"""
-        if isinstance(node, astroid.ImportFrom):
-            importedname = node.modname
-        else:
-            importedname = importedmodnode.name if importedmodnode else None
-        if not importedname:
-            importedname = node.names[0][0].split(".")[0]
-
-        if isinstance(node, astroid.ImportFrom) and (node.level or 0) >= 1:
-            # We need the importedname with first point to detect local package
-            # Example of node:
-            #  'from .my_package1 import MyClass1'
-            #  the output should be '.my_package1' instead of 'my_package1'
-            # Example of node:
-            #  'from . import my_package2'
-            #  the output should be '.my_package2' instead of '{pyfile}'
-            importedname = "." + importedname
-
-        self._imports_stack.append((node, importedname))
-
-    @staticmethod
-    def _is_fallback_import(node, imports):
-        imports = [import_node for (import_node, _) in imports]
-        return any(astroid.are_exclusive(import_node, node) for import_node in imports)
-
-    def _check_imports_order(self, _module_node):
-        """Checks imports of module `node` are grouped by category
-
-        Imports must follow this order: standard, 3rd party, local
-        """
-        std_imports = []
-        third_party_imports = []
-        first_party_imports = []
-        # need of a list that holds third or first party ordered import
-        external_imports = []
-        local_imports = []
-        third_party_not_ignored = []
-        first_party_not_ignored = []
-        local_not_ignored = []
-        isort_obj = isort.SortImports(
-            file_contents="",
-            known_third_party=self.config.known_third_party,
-            known_standard_library=self.config.known_standard_library,
-        )
-        for node, modname in self._imports_stack:
-            if modname.startswith("."):
-                package = "." + modname.split(".")[1]
-            else:
-                package = modname.split(".")[0]
-            nested = not isinstance(node.parent, astroid.Module)
-            ignore_for_import_order = not self.linter.is_message_enabled(
-                "wrong-import-order", node.fromlineno
-            )
-            import_category = isort_obj.place_module(package)
-            node_and_package_import = (node, package)
-            if import_category in ("FUTURE", "STDLIB"):
-                std_imports.append(node_and_package_import)
-                wrong_import = (
-                    third_party_not_ignored
-                    or first_party_not_ignored
-                    or local_not_ignored
-                )
-                if self._is_fallback_import(node, wrong_import):
-                    continue
-                if wrong_import and not nested:
-                    self.add_message(
-                        "wrong-import-order",
-                        node=node,
-                        args=(
-                            'standard import "%s"' % node.as_string(),
-                            '"%s"' % wrong_import[0][0].as_string(),
-                        ),
-                    )
-            elif import_category == "THIRDPARTY":
-                third_party_imports.append(node_and_package_import)
-                external_imports.append(node_and_package_import)
-                if not nested and not ignore_for_import_order:
-                    third_party_not_ignored.append(node_and_package_import)
-                wrong_import = first_party_not_ignored or local_not_ignored
-                if wrong_import and not nested:
-                    self.add_message(
-                        "wrong-import-order",
-                        node=node,
-                        args=(
-                            'third party import "%s"' % node.as_string(),
-                            '"%s"' % wrong_import[0][0].as_string(),
-                        ),
-                    )
-            elif import_category == "FIRSTPARTY":
-                first_party_imports.append(node_and_package_import)
-                external_imports.append(node_and_package_import)
-                if not nested and not ignore_for_import_order:
-                    first_party_not_ignored.append(node_and_package_import)
-                wrong_import = local_not_ignored
-                if wrong_import and not nested:
-                    self.add_message(
-                        "wrong-import-order",
-                        node=node,
-                        args=(
-                            'first party import "%s"' % node.as_string(),
-                            '"%s"' % wrong_import[0][0].as_string(),
-                        ),
-                    )
-            elif import_category == "LOCALFOLDER":
-                local_imports.append((node, package))
-                if not nested and not ignore_for_import_order:
-                    local_not_ignored.append((node, package))
-        return std_imports, external_imports, local_imports
-
-    def _get_imported_module(self, importnode, modname):
-        try:
-            return importnode.do_import_module(modname)
-        except astroid.TooManyLevelsError:
-            if _ignore_import_failure(importnode, modname, self._ignored_modules):
-                return None
-
-            self.add_message("relative-beyond-top-level", node=importnode)
-        except astroid.AstroidSyntaxError as exc:
-            message = "Cannot import {!r} due to syntax error {!r}".format(
-                modname, str(exc.error)  # pylint: disable=no-member; false positive
-            )
-            self.add_message("syntax-error", line=importnode.lineno, args=message)
-
-        except astroid.AstroidBuildingException:
-            if not self.linter.is_message_enabled("import-error"):
-                return None
-            if _ignore_import_failure(importnode, modname, self._ignored_modules):
-                return None
-            if not self.config.analyse_fallback_blocks and is_from_fallback_block(
-                importnode
-            ):
-                return None
-
-            dotted_modname = _get_import_name(importnode, modname)
-            self.add_message("import-error", args=repr(dotted_modname), node=importnode)
-
-    def _add_imported_module(self, node, importedmodname):
-        """notify an imported module, used to analyze dependencies"""
-        module_file = node.root().file
-        context_name = node.root().name
-        base = os.path.splitext(os.path.basename(module_file))[0]
-
-        try:
-            importedmodname = modutils.get_module_part(importedmodname, module_file)
-        except ImportError:
-            pass
-
-        if context_name == importedmodname:
-            self.add_message("import-self", node=node)
-
-        elif not modutils.is_standard_module(importedmodname):
-            # if this is not a package __init__ module
-            if base != "__init__" and context_name not in self._module_pkg:
-                # record the module's parent, or the module itself if this is
-                # a top level module, as the package it belongs to
-                self._module_pkg[context_name] = context_name.rsplit(".", 1)[0]
-
-            # handle dependencies
-            importedmodnames = self.stats["dependencies"].setdefault(
-                importedmodname, set()
-            )
-            if context_name not in importedmodnames:
-                importedmodnames.add(context_name)
-
-            # update import graph
-            self.import_graph[context_name].add(importedmodname)
-            if not self.linter.is_message_enabled("cyclic-import", line=node.lineno):
-                self._excluded_edges[context_name].add(importedmodname)
-
-    def _check_deprecated_module(self, node, mod_path):
-        """check if the module is deprecated"""
-        for mod_name in self.config.deprecated_modules:
-            if mod_path == mod_name or mod_path.startswith(mod_name + "."):
-                self.add_message("deprecated-module", node=node, args=mod_path)
-
-    def _check_preferred_module(self, node, mod_path):
-        """check if the module has a preferred replacement"""
-        if mod_path in self.preferred_modules:
-            self.add_message(
-                "preferred-module",
-                node=node,
-                args=(self.preferred_modules[mod_path], mod_path),
-            )
-
-    def _check_import_as_rename(self, node):
-        names = node.names
-        for name in names:
-            if not all(name):
-                return
-
-            real_name = name[0]
-            splitted_packages = real_name.rsplit(".")
-            real_name = splitted_packages[-1]
-            imported_name = name[1]
-            # consider only following cases
-            # import x as x
-            # and ignore following
-            # import x.y.z as z
-            if real_name == imported_name and len(splitted_packages) == 1:
-                self.add_message("useless-import-alias", node=node)
-
-    def _check_reimport(self, node, basename=None, level=None):
-        """check if the import is necessary (i.e. not already done)"""
-        if not self.linter.is_message_enabled("reimported"):
-            return
-
-        frame = node.frame()
-        root = node.root()
-        contexts = [(frame, level)]
-        if root is not frame:
-            contexts.append((root, None))
-
-        for known_context, known_level in contexts:
-            for name, alias in node.names:
-                first = _get_first_import(
-                    node, known_context, name, basename, known_level, alias
-                )
-                if first is not None:
-                    self.add_message(
-                        "reimported", node=node, args=(name, first.fromlineno)
-                    )
-
-    def _report_external_dependencies(self, sect, _, _dummy):
-        """return a verbatim layout for displaying dependencies"""
-        dep_info = _make_tree_defs(self._external_dependencies_info().items())
-        if not dep_info:
-            raise EmptyReportError()
-        tree_str = _repr_tree_defs(dep_info)
-        sect.append(VerbatimText(tree_str))
-
-    def _report_dependencies_graph(self, sect, _, _dummy):
-        """write dependencies as a dot (graphviz) file"""
-        dep_info = self.stats["dependencies"]
-        if not dep_info or not (
-            self.config.import_graph
-            or self.config.ext_import_graph
-            or self.config.int_import_graph
-        ):
-            raise EmptyReportError()
-        filename = self.config.import_graph
-        if filename:
-            _make_graph(filename, dep_info, sect, "")
-        filename = self.config.ext_import_graph
-        if filename:
-            _make_graph(filename, self._external_dependencies_info(), sect, "external ")
-        filename = self.config.int_import_graph
-        if filename:
-            _make_graph(filename, self._internal_dependencies_info(), sect, "internal ")
-
-    def _filter_dependencies_graph(self, internal):
-        """build the internal or the external dependency graph"""
-        graph = collections.defaultdict(set)
-        for importee, importers in self.stats["dependencies"].items():
-            for importer in importers:
-                package = self._module_pkg.get(importer, importer)
-                is_inside = importee.startswith(package)
-                if is_inside and internal or not is_inside and not internal:
-                    graph[importee].add(importer)
-        return graph
-
-    @cached
-    def _external_dependencies_info(self):
-        """return cached external dependencies information or build and
-        cache them
-        """
-        return self._filter_dependencies_graph(internal=False)
-
-    @cached
-    def _internal_dependencies_info(self):
-        """return cached internal dependencies information or build and
-        cache them
-        """
-        return self._filter_dependencies_graph(internal=True)
-
-    def _check_wildcard_imports(self, node, imported_module):
-        if node.root().package:
-            # Skip the check if in __init__.py issue #2026
-            return
-
-        wildcard_import_is_allowed = self._wildcard_import_is_allowed(imported_module)
-        for name, _ in node.names:
-            if name == "*" and not wildcard_import_is_allowed:
-                self.add_message("wildcard-import", args=node.modname, node=node)
-
-    def _wildcard_import_is_allowed(self, imported_module):
-        return (
-            self.config.allow_wildcard_with_all
-            and imported_module is not None
-            and "__all__" in imported_module.locals
-        )
-
-    def _check_toplevel(self, node):
-        """Check whether the import is made outside the module toplevel.
-        """
-        # If the scope of the import is a module, then obviously it is
-        # not outside the module toplevel.
-        if isinstance(node.scope(), astroid.Module):
-            return
-
-        if isinstance(node, astroid.ImportFrom):
-            module_names = [node.modname]
-        else:
-            module_names = [name[0] for name in node.names]
-
-        # Get the full names of all the imports that are not whitelisted.
-        scoped_imports = [
-            name for name in module_names if name not in self._allow_any_import_level
-        ]
-
-        if scoped_imports:
-            self.add_message(
-                "import-outside-toplevel", args=", ".join(scoped_imports), node=node
-            )
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(ImportsChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/logging.py b/venv/Lib/site-packages/pylint/checkers/logging.py
deleted file mode 100644
index 5ad0e76..0000000
--- a/venv/Lib/site-packages/pylint/checkers/logging.py
+++ /dev/null
@@ -1,384 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2009-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2009, 2012, 2014 Google, Inc.
-# Copyright (c) 2012 Mike Bryant <leachim@leachim.info>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Chris Murray <chris@chrismurray.scot>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017 guillaume2 <guillaume.peillex@gmail.col>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 Mariatta Wijaya <mariatta@python.org>
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""checker for use of Python logging
-"""
-import string
-
-import astroid
-
-from pylint import checkers, interfaces
-from pylint.checkers import utils
-from pylint.checkers.utils import check_messages
-
-MSGS = {
-    "W1201": (
-        "Specify string format arguments as logging function parameters",
-        "logging-not-lazy",
-        "Used when a logging statement has a call form of "
-        '"logging.<logging method>(format_string % (format_args...))". '
-        "Such calls should leave string interpolation to the logging "
-        "method itself and be written "
-        '"logging.<logging method>(format_string, format_args...)" '
-        "so that the program may avoid incurring the cost of the "
-        "interpolation in those cases in which no message will be "
-        "logged. For more, see "
-        "http://www.python.org/dev/peps/pep-0282/.",
-    ),
-    "W1202": (
-        "Use %s formatting in logging functions%s",
-        "logging-format-interpolation",
-        "Used when a logging statement has a call form of "
-        '"logging.<logging method>(<string formatting>)".'
-        " with invalid string formatting. "
-        "Use another way for format the string instead.",
-    ),
-    "E1200": (
-        "Unsupported logging format character %r (%#02x) at index %d",
-        "logging-unsupported-format",
-        "Used when an unsupported format character is used in a logging "
-        "statement format string.",
-    ),
-    "E1201": (
-        "Logging format string ends in middle of conversion specifier",
-        "logging-format-truncated",
-        "Used when a logging statement format string terminates before "
-        "the end of a conversion specifier.",
-    ),
-    "E1205": (
-        "Too many arguments for logging format string",
-        "logging-too-many-args",
-        "Used when a logging format string is given too many arguments.",
-    ),
-    "E1206": (
-        "Not enough arguments for logging format string",
-        "logging-too-few-args",
-        "Used when a logging format string is given too few arguments.",
-    ),
-}
-
-
-CHECKED_CONVENIENCE_FUNCTIONS = {
-    "critical",
-    "debug",
-    "error",
-    "exception",
-    "fatal",
-    "info",
-    "warn",
-    "warning",
-}
-
-
-def is_method_call(func, types=(), methods=()):
-    """Determines if a BoundMethod node represents a method call.
-
-    Args:
-      func (astroid.BoundMethod): The BoundMethod AST node to check.
-      types (Optional[String]): Optional sequence of caller type names to restrict check.
-      methods (Optional[String]): Optional sequence of method names to restrict check.
-
-    Returns:
-      bool: true if the node represents a method call for the given type and
-      method names, False otherwise.
-    """
-    return (
-        isinstance(func, astroid.BoundMethod)
-        and isinstance(func.bound, astroid.Instance)
-        and (func.bound.name in types if types else True)
-        and (func.name in methods if methods else True)
-    )
-
-
-class LoggingChecker(checkers.BaseChecker):
-    """Checks use of the logging module."""
-
-    __implements__ = interfaces.IAstroidChecker
-    name = "logging"
-    msgs = MSGS
-
-    options = (
-        (
-            "logging-modules",
-            {
-                "default": ("logging",),
-                "type": "csv",
-                "metavar": "<comma separated list>",
-                "help": "Logging modules to check that the string format "
-                "arguments are in logging function parameter format.",
-            },
-        ),
-        (
-            "logging-format-style",
-            {
-                "default": "old",
-                "type": "choice",
-                "metavar": "<old (%) or new ({) or fstr (f'')>",
-                "choices": ["old", "new", "fstr"],
-                "help": "Format style used to check logging format string. "
-                "`old` means using % formatting, `new` is for `{}` formatting,"
-                "and `fstr` is for f-strings.",
-            },
-        ),
-    )
-
-    def visit_module(self, node):  # pylint: disable=unused-argument
-        """Clears any state left in this checker from last module checked."""
-        # The code being checked can just as easily "import logging as foo",
-        # so it is necessary to process the imports and store in this field
-        # what name the logging module is actually given.
-        self._logging_names = set()
-        logging_mods = self.config.logging_modules
-
-        self._format_style = self.config.logging_format_style
-        format_styles = {"old": "%", "new": "{", "fstr": "f-string"}
-        format_style_help = ""
-        if self._format_style == "old":
-            format_style_help = " and pass the % parameters as arguments"
-
-        self._format_style_args = (format_styles[self._format_style], format_style_help)
-
-        self._logging_modules = set(logging_mods)
-        self._from_imports = {}
-        for logging_mod in logging_mods:
-            parts = logging_mod.rsplit(".", 1)
-            if len(parts) > 1:
-                self._from_imports[parts[0]] = parts[1]
-
-    def visit_importfrom(self, node):
-        """Checks to see if a module uses a non-Python logging module."""
-        try:
-            logging_name = self._from_imports[node.modname]
-            for module, as_name in node.names:
-                if module == logging_name:
-                    self._logging_names.add(as_name or module)
-        except KeyError:
-            pass
-
-    def visit_import(self, node):
-        """Checks to see if this module uses Python's built-in logging."""
-        for module, as_name in node.names:
-            if module in self._logging_modules:
-                self._logging_names.add(as_name or module)
-
-    @check_messages(*MSGS)
-    def visit_call(self, node):
-        """Checks calls to logging methods."""
-
-        def is_logging_name():
-            return (
-                isinstance(node.func, astroid.Attribute)
-                and isinstance(node.func.expr, astroid.Name)
-                and node.func.expr.name in self._logging_names
-            )
-
-        def is_logger_class():
-            try:
-                for inferred in node.func.infer():
-                    if isinstance(inferred, astroid.BoundMethod):
-                        parent = inferred._proxied.parent
-                        if isinstance(parent, astroid.ClassDef) and (
-                            parent.qname() == "logging.Logger"
-                            or any(
-                                ancestor.qname() == "logging.Logger"
-                                for ancestor in parent.ancestors()
-                            )
-                        ):
-                            return True, inferred._proxied.name
-            except astroid.exceptions.InferenceError:
-                pass
-            return False, None
-
-        if is_logging_name():
-            name = node.func.attrname
-        else:
-            result, name = is_logger_class()
-            if not result:
-                return
-        self._check_log_method(node, name)
-
-    def _check_log_method(self, node, name):
-        """Checks calls to logging.log(level, format, *format_args)."""
-        if name == "log":
-            if node.starargs or node.kwargs or len(node.args) < 2:
-                # Either a malformed call, star args, or double-star args. Beyond
-                # the scope of this checker.
-                return
-            format_pos = 1
-        elif name in CHECKED_CONVENIENCE_FUNCTIONS:
-            if node.starargs or node.kwargs or not node.args:
-                # Either no args, star args, or double-star args. Beyond the
-                # scope of this checker.
-                return
-            format_pos = 0
-        else:
-            return
-
-        if isinstance(node.args[format_pos], astroid.BinOp):
-            binop = node.args[format_pos]
-            emit = binop.op == "%"
-            if binop.op == "+":
-                total_number_of_strings = sum(
-                    1
-                    for operand in (binop.left, binop.right)
-                    if self._is_operand_literal_str(utils.safe_infer(operand))
-                )
-                emit = total_number_of_strings > 0
-            if emit:
-                self.add_message("logging-not-lazy", node=node)
-        elif isinstance(node.args[format_pos], astroid.Call):
-            self._check_call_func(node.args[format_pos])
-        elif isinstance(node.args[format_pos], astroid.Const):
-            self._check_format_string(node, format_pos)
-        elif isinstance(
-            node.args[format_pos], (astroid.FormattedValue, astroid.JoinedStr)
-        ):
-            if self._format_style != "fstr":
-                self.add_message(
-                    "logging-format-interpolation",
-                    node=node,
-                    args=self._format_style_args,
-                )
-
-    @staticmethod
-    def _is_operand_literal_str(operand):
-        """
-        Return True if the operand in argument is a literal string
-        """
-        return isinstance(operand, astroid.Const) and operand.name == "str"
-
-    def _check_call_func(self, node):
-        """Checks that function call is not format_string.format().
-
-        Args:
-          node (astroid.node_classes.Call):
-            Call AST node to be checked.
-        """
-        func = utils.safe_infer(node.func)
-        types = ("str", "unicode")
-        methods = ("format",)
-        if is_method_call(func, types, methods) and not is_complex_format_str(
-            func.bound
-        ):
-            self.add_message(
-                "logging-format-interpolation", node=node, args=self._format_style_args
-            )
-
-    def _check_format_string(self, node, format_arg):
-        """Checks that format string tokens match the supplied arguments.
-
-        Args:
-          node (astroid.node_classes.NodeNG): AST node to be checked.
-          format_arg (int): Index of the format string in the node arguments.
-        """
-        num_args = _count_supplied_tokens(node.args[format_arg + 1 :])
-        if not num_args:
-            # If no args were supplied the string is not interpolated and can contain
-            # formatting characters - it's used verbatim. Don't check any further.
-            return
-
-        format_string = node.args[format_arg].value
-        required_num_args = 0
-        if isinstance(format_string, bytes):
-            format_string = format_string.decode()
-        if isinstance(format_string, str):
-            try:
-                if self._format_style == "old":
-                    keyword_args, required_num_args, _, _ = utils.parse_format_string(
-                        format_string
-                    )
-                    if keyword_args:
-                        # Keyword checking on logging strings is complicated by
-                        # special keywords - out of scope.
-                        return
-                elif self._format_style == "new":
-                    keyword_arguments, implicit_pos_args, explicit_pos_args = utils.parse_format_method_string(
-                        format_string
-                    )
-
-                    keyword_args_cnt = len(
-                        set(k for k, l in keyword_arguments if not isinstance(k, int))
-                    )
-                    required_num_args = (
-                        keyword_args_cnt + implicit_pos_args + explicit_pos_args
-                    )
-                else:
-                    self.add_message(
-                        "logging-format-interpolation",
-                        node=node,
-                        args=self._format_style_args,
-                    )
-            except utils.UnsupportedFormatCharacter as ex:
-                char = format_string[ex.index]
-                self.add_message(
-                    "logging-unsupported-format",
-                    node=node,
-                    args=(char, ord(char), ex.index),
-                )
-                return
-            except utils.IncompleteFormatString:
-                self.add_message("logging-format-truncated", node=node)
-                return
-        if num_args > required_num_args:
-            self.add_message("logging-too-many-args", node=node)
-        elif num_args < required_num_args:
-            self.add_message("logging-too-few-args", node=node)
-
-
-def is_complex_format_str(node):
-    """Checks if node represents a string with complex formatting specs.
-
-    Args:
-        node (astroid.node_classes.NodeNG): AST node to check
-    Returns:
-        bool: True if inferred string uses complex formatting, False otherwise
-    """
-    inferred = utils.safe_infer(node)
-    if inferred is None or not (
-        isinstance(inferred, astroid.Const) and isinstance(inferred.value, str)
-    ):
-        return True
-    try:
-        parsed = list(string.Formatter().parse(inferred.value))
-    except ValueError:
-        # This format string is invalid
-        return False
-    for _, _, format_spec, _ in parsed:
-        if format_spec:
-            return True
-    return False
-
-
-def _count_supplied_tokens(args):
-    """Counts the number of tokens in an args list.
-
-    The Python log functions allow for special keyword arguments: func,
-    exc_info and extra. To handle these cases correctly, we only count
-    arguments that aren't keywords.
-
-    Args:
-      args (list): AST nodes that are arguments for a log format string.
-
-    Returns:
-      int: Number of AST nodes that aren't keywords.
-    """
-    return sum(1 for arg in args if not isinstance(arg, astroid.Keyword))
-
-
-def register(linter):
-    """Required method to auto-register this checker."""
-    linter.register_checker(LoggingChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/misc.py b/venv/Lib/site-packages/pylint/checkers/misc.py
deleted file mode 100644
index dcf7a3e..0000000
--- a/venv/Lib/site-packages/pylint/checkers/misc.py
+++ /dev/null
@@ -1,171 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006, 2009-2013 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Alexandru Coman <fcoman@bitdefender.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 glegoux <gilles.legoux@gmail.com>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Mikhail Fesenko <proggga@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@iki.fi>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-
-"""Check source code is ascii only or has an encoding declaration (PEP 263)"""
-
-import re
-import tokenize
-
-from pylint.checkers import BaseChecker
-from pylint.constants import OPTION_RGX
-from pylint.interfaces import IRawChecker, ITokenChecker
-from pylint.message import MessagesHandlerMixIn
-
-
-class ByIdManagedMessagesChecker(BaseChecker):
-
-    """checks for messages that are enabled or disabled by id instead of symbol."""
-
-    __implements__ = IRawChecker
-
-    # configuration section name
-    name = "miscellaneous"
-    msgs = {
-        "I0023": (
-            "%s",
-            "use-symbolic-message-instead",
-            "Used when a message is enabled or disabled by id.",
-        )
-    }
-
-    options = ()
-
-    def process_module(self, module):
-        """inspect the source file to find messages activated or deactivated by id."""
-        managed_msgs = MessagesHandlerMixIn.get_by_id_managed_msgs()
-        for (mod_name, msg_id, msg_symbol, lineno, is_disabled) in managed_msgs:
-            if mod_name == module.name:
-                if is_disabled:
-                    txt = "Id '{ident}' is used to disable '{symbol}' message emission".format(
-                        ident=msg_id, symbol=msg_symbol
-                    )
-                else:
-                    txt = "Id '{ident}' is used to enable '{symbol}' message emission".format(
-                        ident=msg_id, symbol=msg_symbol
-                    )
-                self.add_message("use-symbolic-message-instead", line=lineno, args=txt)
-        MessagesHandlerMixIn.clear_by_id_managed_msgs()
-
-
-class EncodingChecker(BaseChecker):
-
-    """checks for:
-    * warning notes in the code like FIXME, XXX
-    * encoding issues.
-    """
-
-    __implements__ = (IRawChecker, ITokenChecker)
-
-    # configuration section name
-    name = "miscellaneous"
-    msgs = {
-        "W0511": (
-            "%s",
-            "fixme",
-            "Used when a warning note as FIXME or XXX is detected.",
-        )
-    }
-
-    options = (
-        (
-            "notes",
-            {
-                "type": "csv",
-                "metavar": "<comma separated values>",
-                "default": ("FIXME", "XXX", "TODO"),
-                "help": (
-                    "List of note tags to take in consideration, "
-                    "separated by a comma."
-                ),
-            },
-        ),
-    )
-
-    def open(self):
-        super().open()
-        self._fixme_pattern = re.compile(
-            r"#\s*(%s)\b" % "|".join(map(re.escape, self.config.notes)), re.I
-        )
-
-    def _check_encoding(self, lineno, line, file_encoding):
-        try:
-            return line.decode(file_encoding)
-        except UnicodeDecodeError:
-            pass
-        except LookupError:
-            if line.startswith("#") and "coding" in line and file_encoding in line:
-                self.add_message(
-                    "syntax-error",
-                    line=lineno,
-                    args='Cannot decode using encoding "{}",'
-                    " bad encoding".format(file_encoding),
-                )
-
-    def process_module(self, module):
-        """inspect the source file to find encoding problem"""
-        if module.file_encoding:
-            encoding = module.file_encoding
-        else:
-            encoding = "ascii"
-
-        with module.stream() as stream:
-            for lineno, line in enumerate(stream):
-                self._check_encoding(lineno + 1, line, encoding)
-
-    def process_tokens(self, tokens):
-        """inspect the source to find fixme problems"""
-        if not self.config.notes:
-            return
-        comments = (
-            token_info for token_info in tokens if token_info.type == tokenize.COMMENT
-        )
-        for comment in comments:
-            comment_text = comment.string[1:].lstrip()  # trim '#' and whitespaces
-
-            # handle pylint disable clauses
-            disable_option_match = OPTION_RGX.search(comment_text)
-            if disable_option_match:
-                try:
-                    _, value = disable_option_match.group(1).split("=", 1)
-                    values = [_val.strip().upper() for _val in value.split(",")]
-                    if set(values) & set(self.config.notes):
-                        continue
-                except ValueError:
-                    self.add_message(
-                        "bad-inline-option",
-                        args=disable_option_match.group(1).strip(),
-                        line=comment.start[0],
-                    )
-                    continue
-
-            # emit warnings if necessary
-            match = self._fixme_pattern.search("#" + comment_text.lower())
-            if match:
-                note = match.group(1)
-                self.add_message(
-                    "fixme",
-                    col_offset=comment.string.lower().index(note.lower()),
-                    args=comment_text,
-                    line=comment.start[0],
-                )
-
-
-def register(linter):
-    """required method to auto register this checker"""
-    linter.register_checker(EncodingChecker(linter))
-    linter.register_checker(ByIdManagedMessagesChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/newstyle.py b/venv/Lib/site-packages/pylint/checkers/newstyle.py
deleted file mode 100644
index 46f4e4e..0000000
--- a/venv/Lib/site-packages/pylint/checkers/newstyle.py
+++ /dev/null
@@ -1,127 +0,0 @@
-# Copyright (c) 2006, 2008-2011, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""check for new / old style related problems
-"""
-import astroid
-
-from pylint.checkers import BaseChecker
-from pylint.checkers.utils import check_messages, has_known_bases, node_frame_class
-from pylint.interfaces import IAstroidChecker
-
-MSGS = {
-    "E1003": (
-        "Bad first argument %r given to super()",
-        "bad-super-call",
-        "Used when another argument than the current class is given as "
-        "first argument of the super builtin.",
-    )
-}
-
-
-class NewStyleConflictChecker(BaseChecker):
-    """checks for usage of new style capabilities on old style classes and
-    other new/old styles conflicts problems
-    * use of property, __slots__, super
-    * "super" usage
-    """
-
-    __implements__ = (IAstroidChecker,)
-
-    # configuration section name
-    name = "newstyle"
-    # messages
-    msgs = MSGS
-    priority = -2
-    # configuration options
-    options = ()
-
-    @check_messages("bad-super-call")
-    def visit_functiondef(self, node):
-        """check use of super"""
-        # ignore actual functions or method within a new style class
-        if not node.is_method():
-            return
-        klass = node.parent.frame()
-        for stmt in node.nodes_of_class(astroid.Call):
-            if node_frame_class(stmt) != node_frame_class(node):
-                # Don't look down in other scopes.
-                continue
-
-            expr = stmt.func
-            if not isinstance(expr, astroid.Attribute):
-                continue
-
-            call = expr.expr
-            # skip the test if using super
-            if not (
-                isinstance(call, astroid.Call)
-                and isinstance(call.func, astroid.Name)
-                and call.func.name == "super"
-            ):
-                continue
-
-            # super should not be used on an old style class
-            if klass.newstyle or not has_known_bases(klass):
-                # super first arg should not be the class
-                if not call.args:
-                    continue
-
-                # calling super(type(self), self) can lead to recursion loop
-                # in derived classes
-                arg0 = call.args[0]
-                if (
-                    isinstance(arg0, astroid.Call)
-                    and isinstance(arg0.func, astroid.Name)
-                    and arg0.func.name == "type"
-                ):
-                    self.add_message("bad-super-call", node=call, args=("type",))
-                    continue
-
-                # calling super(self.__class__, self) can lead to recursion loop
-                # in derived classes
-                if (
-                    len(call.args) >= 2
-                    and isinstance(call.args[1], astroid.Name)
-                    and call.args[1].name == "self"
-                    and isinstance(arg0, astroid.Attribute)
-                    and arg0.attrname == "__class__"
-                ):
-                    self.add_message(
-                        "bad-super-call", node=call, args=("self.__class__",)
-                    )
-                    continue
-
-                try:
-                    supcls = call.args and next(call.args[0].infer(), None)
-                except astroid.InferenceError:
-                    continue
-
-                if klass is not supcls:
-                    name = None
-                    # if supcls is not Uninferable, then supcls was inferred
-                    # and use its name. Otherwise, try to look
-                    # for call.args[0].name
-                    if supcls:
-                        name = supcls.name
-                    elif call.args and hasattr(call.args[0], "name"):
-                        name = call.args[0].name
-                    if name:
-                        self.add_message("bad-super-call", node=call, args=(name,))
-
-    visit_asyncfunctiondef = visit_functiondef
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(NewStyleConflictChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/python3.py b/venv/Lib/site-packages/pylint/checkers/python3.py
deleted file mode 100644
index 583b1c2..0000000
--- a/venv/Lib/site-packages/pylint/checkers/python3.py
+++ /dev/null
@@ -1,1398 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014-2015 Brett Cannon <brett@python.org>
-# Copyright (c) 2015 Simu Toni <simutoni@gmail.com>
-# Copyright (c) 2015 Pavel Roskin <proski@gnu.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2015 Cosmin Poieana <cmin@ropython.org>
-# Copyright (c) 2015 Viorel Stirbu <viorels@gmail.com>
-# Copyright (c) 2016, 2018 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016-2017 Roy Williams <roy.williams.iii@gmail.com>
-# Copyright (c) 2016 Roy Williams <rwilliams@lyft.com>
-# Copyright (c) 2016 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Erik <erik.eriksson@yahoo.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2017 Daniel Miller <millerdev@gmail.com>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 ahirnish <ahirnish@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-# Copyright (c) 2018 gaurikholkar <f2013002@goa.bits-pilani.ac.in>
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Check Python 2 code for Python 2/3 source-compatible issues."""
-import re
-import tokenize
-from collections import namedtuple
-
-import astroid
-from astroid import bases
-
-from pylint import checkers, interfaces
-from pylint.checkers import utils
-from pylint.checkers.utils import find_try_except_wrapper_node, node_ignores_exception
-from pylint.constants import WarningScope
-from pylint.interfaces import INFERENCE, INFERENCE_FAILURE
-
-_ZERO = re.compile("^0+$")
-
-
-def _is_old_octal(literal):
-    if _ZERO.match(literal):
-        return False
-    if re.match(r"0\d+", literal):
-        try:
-            int(literal, 8)
-        except ValueError:
-            return False
-        return True
-    return None
-
-
-def _inferred_value_is_dict(value):
-    if isinstance(value, astroid.Dict):
-        return True
-    return isinstance(value, astroid.Instance) and "dict" in value.basenames
-
-
-def _is_builtin(node):
-    return getattr(node, "name", None) in ("__builtin__", "builtins")
-
-
-_ACCEPTS_ITERATOR = {
-    "iter",
-    "list",
-    "tuple",
-    "sorted",
-    "set",
-    "sum",
-    "any",
-    "all",
-    "enumerate",
-    "dict",
-    "filter",
-    "reversed",
-    "max",
-    "min",
-    "frozenset",
-    "OrderedDict",
-}
-ATTRIBUTES_ACCEPTS_ITERATOR = {"join", "from_iterable"}
-_BUILTIN_METHOD_ACCEPTS_ITERATOR = {
-    "builtins.list.extend",
-    "builtins.dict.update",
-    "builtins.set.update",
-}
-DICT_METHODS = {"items", "keys", "values"}
-
-
-def _in_iterating_context(node):
-    """Check if the node is being used as an iterator.
-
-    Definition is taken from lib2to3.fixer_util.in_special_context().
-    """
-    parent = node.parent
-    # Since a call can't be the loop variant we only need to know if the node's
-    # parent is a 'for' loop to know it's being used as the iterator for the
-    # loop.
-    if isinstance(parent, astroid.For):
-        return True
-    # Need to make sure the use of the node is in the iterator part of the
-    # comprehension.
-    if isinstance(parent, astroid.Comprehension):
-        if parent.iter == node:
-            return True
-    # Various built-ins can take in an iterable or list and lead to the same
-    # value.
-    elif isinstance(parent, astroid.Call):
-        if isinstance(parent.func, astroid.Name):
-            if parent.func.name in _ACCEPTS_ITERATOR:
-                return True
-        elif isinstance(parent.func, astroid.Attribute):
-            if parent.func.attrname in ATTRIBUTES_ACCEPTS_ITERATOR:
-                return True
-
-        inferred = utils.safe_infer(parent.func)
-        if inferred:
-            if inferred.qname() in _BUILTIN_METHOD_ACCEPTS_ITERATOR:
-                return True
-            root = inferred.root()
-            if root and root.name == "itertools":
-                return True
-    # If the call is in an unpacking, there's no need to warn,
-    # since it can be considered iterating.
-    elif isinstance(parent, astroid.Assign) and isinstance(
-        parent.targets[0], (astroid.List, astroid.Tuple)
-    ):
-        if len(parent.targets[0].elts) > 1:
-            return True
-    # If the call is in a containment check, we consider that to
-    # be an iterating context
-    elif (
-        isinstance(parent, astroid.Compare)
-        and len(parent.ops) == 1
-        and parent.ops[0][0] == "in"
-    ):
-        return True
-    # Also if it's an `yield from`, that's fair
-    elif isinstance(parent, astroid.YieldFrom):
-        return True
-    if isinstance(parent, astroid.Starred):
-        return True
-    return False
-
-
-def _is_conditional_import(node):
-    """Checks if an import node is in the context of a conditional.
-    """
-    parent = node.parent
-    return isinstance(
-        parent, (astroid.TryExcept, astroid.ExceptHandler, astroid.If, astroid.IfExp)
-    )
-
-
-Branch = namedtuple("Branch", ["node", "is_py2_only"])
-
-
-class Python3Checker(checkers.BaseChecker):
-
-    __implements__ = interfaces.IAstroidChecker
-    enabled = False
-    name = "python3"
-
-    msgs = {
-        # Errors for what will syntactically break in Python 3, warnings for
-        # everything else.
-        "E1601": (
-            "print statement used",
-            "print-statement",
-            "Used when a print statement is used "
-            "(`print` is a function in Python 3)",
-        ),
-        "E1602": (
-            "Parameter unpacking specified",
-            "parameter-unpacking",
-            "Used when parameter unpacking is specified for a function"
-            "(Python 3 doesn't allow it)",
-        ),
-        "E1603": (
-            "Implicit unpacking of exceptions is not supported in Python 3",
-            "unpacking-in-except",
-            "Python3 will not allow implicit unpacking of "
-            "exceptions in except clauses. "
-            "See http://www.python.org/dev/peps/pep-3110/",
-            {"old_names": [("W0712", "old-unpacking-in-except")]},
-        ),
-        "E1604": (
-            "Use raise ErrorClass(args) instead of raise ErrorClass, args.",
-            "old-raise-syntax",
-            "Used when the alternate raise syntax "
-            "'raise foo, bar' is used "
-            "instead of 'raise foo(bar)'.",
-            {"old_names": [("W0121", "old-old-raise-syntax")]},
-        ),
-        "E1605": (
-            "Use of the `` operator",
-            "backtick",
-            'Used when the deprecated "``" (backtick) operator is used '
-            "instead  of the str() function.",
-            {"scope": WarningScope.NODE, "old_names": [("W0333", "old-backtick")]},
-        ),
-        "E1609": (
-            "Import * only allowed at module level",
-            "import-star-module-level",
-            "Used when the import star syntax is used somewhere "
-            "else than the module level.",
-            {"maxversion": (3, 0)},
-        ),
-        "W1601": (
-            "apply built-in referenced",
-            "apply-builtin",
-            "Used when the apply built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1602": (
-            "basestring built-in referenced",
-            "basestring-builtin",
-            "Used when the basestring built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1603": (
-            "buffer built-in referenced",
-            "buffer-builtin",
-            "Used when the buffer built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1604": (
-            "cmp built-in referenced",
-            "cmp-builtin",
-            "Used when the cmp built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1605": (
-            "coerce built-in referenced",
-            "coerce-builtin",
-            "Used when the coerce built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1606": (
-            "execfile built-in referenced",
-            "execfile-builtin",
-            "Used when the execfile built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1607": (
-            "file built-in referenced",
-            "file-builtin",
-            "Used when the file built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1608": (
-            "long built-in referenced",
-            "long-builtin",
-            "Used when the long built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1609": (
-            "raw_input built-in referenced",
-            "raw_input-builtin",
-            "Used when the raw_input built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1610": (
-            "reduce built-in referenced",
-            "reduce-builtin",
-            "Used when the reduce built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1611": (
-            "StandardError built-in referenced",
-            "standarderror-builtin",
-            "Used when the StandardError built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1612": (
-            "unicode built-in referenced",
-            "unicode-builtin",
-            "Used when the unicode built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1613": (
-            "xrange built-in referenced",
-            "xrange-builtin",
-            "Used when the xrange built-in function is referenced "
-            "(missing from Python 3)",
-        ),
-        "W1614": (
-            "__coerce__ method defined",
-            "coerce-method",
-            "Used when a __coerce__ method is defined "
-            "(method is not used by Python 3)",
-        ),
-        "W1615": (
-            "__delslice__ method defined",
-            "delslice-method",
-            "Used when a __delslice__ method is defined "
-            "(method is not used by Python 3)",
-        ),
-        "W1616": (
-            "__getslice__ method defined",
-            "getslice-method",
-            "Used when a __getslice__ method is defined "
-            "(method is not used by Python 3)",
-        ),
-        "W1617": (
-            "__setslice__ method defined",
-            "setslice-method",
-            "Used when a __setslice__ method is defined "
-            "(method is not used by Python 3)",
-        ),
-        "W1618": (
-            "import missing `from __future__ import absolute_import`",
-            "no-absolute-import",
-            "Used when an import is not accompanied by "
-            "``from __future__ import absolute_import`` "
-            "(default behaviour in Python 3)",
-        ),
-        "W1619": (
-            "division w/o __future__ statement",
-            "old-division",
-            "Used for non-floor division w/o a float literal or "
-            "``from __future__ import division`` "
-            "(Python 3 returns a float for int division unconditionally)",
-        ),
-        "W1620": (
-            "Calling a dict.iter*() method",
-            "dict-iter-method",
-            "Used for calls to dict.iterkeys(), itervalues() or iteritems() "
-            "(Python 3 lacks these methods)",
-        ),
-        "W1621": (
-            "Calling a dict.view*() method",
-            "dict-view-method",
-            "Used for calls to dict.viewkeys(), viewvalues() or viewitems() "
-            "(Python 3 lacks these methods)",
-        ),
-        "W1622": (
-            "Called a next() method on an object",
-            "next-method-called",
-            "Used when an object's next() method is called "
-            "(Python 3 uses the next() built-in function)",
-        ),
-        "W1623": (
-            "Assigning to a class's __metaclass__ attribute",
-            "metaclass-assignment",
-            "Used when a metaclass is specified by assigning to __metaclass__ "
-            "(Python 3 specifies the metaclass as a class statement argument)",
-        ),
-        "W1624": (
-            "Indexing exceptions will not work on Python 3",
-            "indexing-exception",
-            "Indexing exceptions will not work on Python 3. Use "
-            "`exception.args[index]` instead.",
-            {"old_names": [("W0713", "old-indexing-exception")]},
-        ),
-        "W1625": (
-            "Raising a string exception",
-            "raising-string",
-            "Used when a string exception is raised. This will not "
-            "work on Python 3.",
-            {"old_names": [("W0701", "old-raising-string")]},
-        ),
-        "W1626": (
-            "reload built-in referenced",
-            "reload-builtin",
-            "Used when the reload built-in function is referenced "
-            "(missing from Python 3). You can use instead imp.reload "
-            "or importlib.reload.",
-        ),
-        "W1627": (
-            "__oct__ method defined",
-            "oct-method",
-            "Used when an __oct__ method is defined "
-            "(method is not used by Python 3)",
-        ),
-        "W1628": (
-            "__hex__ method defined",
-            "hex-method",
-            "Used when a __hex__ method is defined (method is not used by Python 3)",
-        ),
-        "W1629": (
-            "__nonzero__ method defined",
-            "nonzero-method",
-            "Used when a __nonzero__ method is defined "
-            "(method is not used by Python 3)",
-        ),
-        "W1630": (
-            "__cmp__ method defined",
-            "cmp-method",
-            "Used when a __cmp__ method is defined (method is not used by Python 3)",
-        ),
-        # 'W1631': replaced by W1636
-        "W1632": (
-            "input built-in referenced",
-            "input-builtin",
-            "Used when the input built-in is referenced "
-            "(backwards-incompatible semantics in Python 3)",
-        ),
-        "W1633": (
-            "round built-in referenced",
-            "round-builtin",
-            "Used when the round built-in is referenced "
-            "(backwards-incompatible semantics in Python 3)",
-        ),
-        "W1634": (
-            "intern built-in referenced",
-            "intern-builtin",
-            "Used when the intern built-in is referenced "
-            "(Moved to sys.intern in Python 3)",
-        ),
-        "W1635": (
-            "unichr built-in referenced",
-            "unichr-builtin",
-            "Used when the unichr built-in is referenced (Use chr in Python 3)",
-        ),
-        "W1636": (
-            "map built-in referenced when not iterating",
-            "map-builtin-not-iterating",
-            "Used when the map built-in is referenced in a non-iterating "
-            "context (returns an iterator in Python 3)",
-            {"old_names": [("W1631", "implicit-map-evaluation")]},
-        ),
-        "W1637": (
-            "zip built-in referenced when not iterating",
-            "zip-builtin-not-iterating",
-            "Used when the zip built-in is referenced in a non-iterating "
-            "context (returns an iterator in Python 3)",
-        ),
-        "W1638": (
-            "range built-in referenced when not iterating",
-            "range-builtin-not-iterating",
-            "Used when the range built-in is referenced in a non-iterating "
-            "context (returns a range in Python 3)",
-        ),
-        "W1639": (
-            "filter built-in referenced when not iterating",
-            "filter-builtin-not-iterating",
-            "Used when the filter built-in is referenced in a non-iterating "
-            "context (returns an iterator in Python 3)",
-        ),
-        "W1640": (
-            "Using the cmp argument for list.sort / sorted",
-            "using-cmp-argument",
-            "Using the cmp argument for list.sort or the sorted "
-            "builtin should be avoided, since it was removed in "
-            "Python 3. Using either `key` or `functools.cmp_to_key` "
-            "should be preferred.",
-        ),
-        "W1641": (
-            "Implementing __eq__ without also implementing __hash__",
-            "eq-without-hash",
-            "Used when a class implements __eq__ but not __hash__.  In Python 2, objects "
-            "get object.__hash__ as the default implementation, in Python 3 objects get "
-            "None as their default __hash__ implementation if they also implement __eq__.",
-        ),
-        "W1642": (
-            "__div__ method defined",
-            "div-method",
-            "Used when a __div__ method is defined.  Using `__truediv__` and setting"
-            "__div__ = __truediv__ should be preferred."
-            "(method is not used by Python 3)",
-        ),
-        "W1643": (
-            "__idiv__ method defined",
-            "idiv-method",
-            "Used when an __idiv__ method is defined.  Using `__itruediv__` and setting"
-            "__idiv__ = __itruediv__ should be preferred."
-            "(method is not used by Python 3)",
-        ),
-        "W1644": (
-            "__rdiv__ method defined",
-            "rdiv-method",
-            "Used when a __rdiv__ method is defined.  Using `__rtruediv__` and setting"
-            "__rdiv__ = __rtruediv__ should be preferred."
-            "(method is not used by Python 3)",
-        ),
-        "W1645": (
-            "Exception.message removed in Python 3",
-            "exception-message-attribute",
-            "Used when the message attribute is accessed on an Exception.  Use "
-            "str(exception) instead.",
-        ),
-        "W1646": (
-            "non-text encoding used in str.decode",
-            "invalid-str-codec",
-            "Used when using str.encode or str.decode with a non-text encoding.  Use "
-            "codecs module to handle arbitrary codecs.",
-        ),
-        "W1647": (
-            "sys.maxint removed in Python 3",
-            "sys-max-int",
-            "Used when accessing sys.maxint.  Use sys.maxsize instead.",
-        ),
-        "W1648": (
-            "Module moved in Python 3",
-            "bad-python3-import",
-            "Used when importing a module that no longer exists in Python 3.",
-        ),
-        "W1649": (
-            "Accessing a deprecated function on the string module",
-            "deprecated-string-function",
-            "Used when accessing a string function that has been deprecated in Python 3.",
-        ),
-        "W1650": (
-            "Using str.translate with deprecated deletechars parameters",
-            "deprecated-str-translate-call",
-            "Used when using the deprecated deletechars parameters from str.translate.  Use "
-            "re.sub to remove the desired characters ",
-        ),
-        "W1651": (
-            "Accessing a deprecated function on the itertools module",
-            "deprecated-itertools-function",
-            "Used when accessing a function on itertools that has been removed in Python 3.",
-        ),
-        "W1652": (
-            "Accessing a deprecated fields on the types module",
-            "deprecated-types-field",
-            "Used when accessing a field on types that has been removed in Python 3.",
-        ),
-        "W1653": (
-            "next method defined",
-            "next-method-defined",
-            "Used when a next method is defined that would be an iterator in Python 2 but "
-            "is treated as a normal function in Python 3.",
-        ),
-        "W1654": (
-            "dict.items referenced when not iterating",
-            "dict-items-not-iterating",
-            "Used when dict.items is referenced in a non-iterating "
-            "context (returns an iterator in Python 3)",
-        ),
-        "W1655": (
-            "dict.keys referenced when not iterating",
-            "dict-keys-not-iterating",
-            "Used when dict.keys is referenced in a non-iterating "
-            "context (returns an iterator in Python 3)",
-        ),
-        "W1656": (
-            "dict.values referenced when not iterating",
-            "dict-values-not-iterating",
-            "Used when dict.values is referenced in a non-iterating "
-            "context (returns an iterator in Python 3)",
-        ),
-        "W1657": (
-            "Accessing a removed attribute on the operator module",
-            "deprecated-operator-function",
-            "Used when accessing a field on operator module that has been "
-            "removed in Python 3.",
-        ),
-        "W1658": (
-            "Accessing a removed attribute on the urllib module",
-            "deprecated-urllib-function",
-            "Used when accessing a field on urllib module that has been "
-            "removed or moved in Python 3.",
-        ),
-        "W1659": (
-            "Accessing a removed xreadlines attribute",
-            "xreadlines-attribute",
-            "Used when accessing the xreadlines() function on a file stream, "
-            "removed in Python 3.",
-        ),
-        "W1660": (
-            "Accessing a removed attribute on the sys module",
-            "deprecated-sys-function",
-            "Used when accessing a field on sys module that has been "
-            "removed in Python 3.",
-        ),
-        "W1661": (
-            "Using an exception object that was bound by an except handler",
-            "exception-escape",
-            "Emitted when using an exception, that was bound in an except "
-            "handler, outside of the except handler. On Python 3 these "
-            "exceptions will be deleted once they get out "
-            "of the except handler.",
-        ),
-        "W1662": (
-            "Using a variable that was bound inside a comprehension",
-            "comprehension-escape",
-            "Emitted when using a variable, that was bound in a comprehension "
-            "handler, outside of the comprehension itself. On Python 3 these "
-            "variables will be deleted outside of the "
-            "comprehension.",
-        ),
-    }
-
-    _bad_builtins = frozenset(
-        [
-            "apply",
-            "basestring",
-            "buffer",
-            "cmp",
-            "coerce",
-            "execfile",
-            "file",
-            "input",  # Not missing, but incompatible semantics
-            "intern",
-            "long",
-            "raw_input",
-            "reduce",
-            "round",  # Not missing, but incompatible semantics
-            "StandardError",
-            "unichr",
-            "unicode",
-            "xrange",
-            "reload",
-        ]
-    )
-
-    _unused_magic_methods = frozenset(
-        [
-            "__coerce__",
-            "__delslice__",
-            "__getslice__",
-            "__setslice__",
-            "__oct__",
-            "__hex__",
-            "__nonzero__",
-            "__cmp__",
-            "__div__",
-            "__idiv__",
-            "__rdiv__",
-        ]
-    )
-
-    _invalid_encodings = frozenset(
-        [
-            "base64_codec",
-            "base64",
-            "base_64",
-            "bz2_codec",
-            "bz2",
-            "hex_codec",
-            "hex",
-            "quopri_codec",
-            "quopri",
-            "quotedprintable",
-            "quoted_printable",
-            "uu_codec",
-            "uu",
-            "zlib_codec",
-            "zlib",
-            "zip",
-            "rot13",
-            "rot_13",
-        ]
-    )
-
-    _bad_python3_module_map = {
-        "sys-max-int": {"sys": frozenset(["maxint"])},
-        "deprecated-itertools-function": {
-            "itertools": frozenset(
-                ["izip", "ifilter", "imap", "izip_longest", "ifilterfalse"]
-            )
-        },
-        "deprecated-types-field": {
-            "types": frozenset(
-                [
-                    "EllipsisType",
-                    "XRangeType",
-                    "ComplexType",
-                    "StringType",
-                    "TypeType",
-                    "LongType",
-                    "UnicodeType",
-                    "ClassType",
-                    "BufferType",
-                    "StringTypes",
-                    "NotImplementedType",
-                    "NoneType",
-                    "InstanceType",
-                    "FloatType",
-                    "SliceType",
-                    "UnboundMethodType",
-                    "ObjectType",
-                    "IntType",
-                    "TupleType",
-                    "ListType",
-                    "DictType",
-                    "FileType",
-                    "DictionaryType",
-                    "BooleanType",
-                    "DictProxyType",
-                ]
-            )
-        },
-        "bad-python3-import": frozenset(
-            [
-                "anydbm",
-                "BaseHTTPServer",
-                "__builtin__",
-                "CGIHTTPServer",
-                "ConfigParser",
-                "copy_reg",
-                "cPickle",
-                "cStringIO",
-                "Cookie",
-                "cookielib",
-                "dbhash",
-                "dumbdbm",
-                "dumbdb",
-                "Dialog",
-                "DocXMLRPCServer",
-                "FileDialog",
-                "FixTk",
-                "gdbm",
-                "htmlentitydefs",
-                "HTMLParser",
-                "httplib",
-                "markupbase",
-                "Queue",
-                "repr",
-                "robotparser",
-                "ScrolledText",
-                "SimpleDialog",
-                "SimpleHTTPServer",
-                "SimpleXMLRPCServer",
-                "StringIO",
-                "dummy_thread",
-                "SocketServer",
-                "test.test_support",
-                "Tkinter",
-                "Tix",
-                "Tkconstants",
-                "tkColorChooser",
-                "tkCommonDialog",
-                "Tkdnd",
-                "tkFileDialog",
-                "tkFont",
-                "tkMessageBox",
-                "tkSimpleDialog",
-                "UserList",
-                "UserString",
-                "whichdb",
-                "_winreg",
-                "xmlrpclib",
-                "audiodev",
-                "Bastion",
-                "bsddb185",
-                "bsddb3",
-                "Canvas",
-                "cfmfile",
-                "cl",
-                "commands",
-                "compiler",
-                "dircache",
-                "dl",
-                "exception",
-                "fpformat",
-                "htmllib",
-                "ihooks",
-                "imageop",
-                "imputil",
-                "linuxaudiodev",
-                "md5",
-                "mhlib",
-                "mimetools",
-                "MimeWriter",
-                "mimify",
-                "multifile",
-                "mutex",
-                "new",
-                "popen2",
-                "posixfile",
-                "pure",
-                "rexec",
-                "rfc822",
-                "sets",
-                "sha",
-                "sgmllib",
-                "sre",
-                "stringold",
-                "sunaudio",
-                "sv",
-                "test.testall",
-                "thread",
-                "timing",
-                "toaiff",
-                "user",
-                "urllib2",
-                "urlparse",
-            ]
-        ),
-        "deprecated-string-function": {
-            "string": frozenset(
-                [
-                    "maketrans",
-                    "atof",
-                    "atoi",
-                    "atol",
-                    "capitalize",
-                    "expandtabs",
-                    "find",
-                    "rfind",
-                    "index",
-                    "rindex",
-                    "count",
-                    "lower",
-                    "letters",
-                    "split",
-                    "rsplit",
-                    "splitfields",
-                    "join",
-                    "joinfields",
-                    "lstrip",
-                    "rstrip",
-                    "strip",
-                    "swapcase",
-                    "translate",
-                    "upper",
-                    "ljust",
-                    "rjust",
-                    "center",
-                    "zfill",
-                    "replace",
-                    "lowercase",
-                    "letters",
-                    "uppercase",
-                    "atol_error",
-                    "atof_error",
-                    "atoi_error",
-                    "index_error",
-                ]
-            )
-        },
-        "deprecated-operator-function": {"operator": frozenset({"div"})},
-        "deprecated-urllib-function": {
-            "urllib": frozenset(
-                {
-                    "addbase",
-                    "addclosehook",
-                    "addinfo",
-                    "addinfourl",
-                    "always_safe",
-                    "basejoin",
-                    "ftpcache",
-                    "ftperrors",
-                    "ftpwrapper",
-                    "getproxies",
-                    "getproxies_environment",
-                    "getproxies_macosx_sysconf",
-                    "main",
-                    "noheaders",
-                    "pathname2url",
-                    "proxy_bypass",
-                    "proxy_bypass_environment",
-                    "proxy_bypass_macosx_sysconf",
-                    "quote",
-                    "quote_plus",
-                    "reporthook",
-                    "splitattr",
-                    "splithost",
-                    "splitnport",
-                    "splitpasswd",
-                    "splitport",
-                    "splitquery",
-                    "splittag",
-                    "splittype",
-                    "splituser",
-                    "splitvalue",
-                    "unquote",
-                    "unquote_plus",
-                    "unwrap",
-                    "url2pathname",
-                    "urlcleanup",
-                    "urlencode",
-                    "urlopen",
-                    "urlretrieve",
-                }
-            )
-        },
-        "deprecated-sys-function": {"sys": frozenset({"exc_clear"})},
-    }
-
-    _python_2_tests = frozenset(
-        [
-            astroid.extract_node(x).repr_tree()
-            for x in [
-                "sys.version_info[0] == 2",
-                "sys.version_info[0] < 3",
-                "sys.version_info == (2, 7)",
-                "sys.version_info <= (2, 7)",
-                "sys.version_info < (3, 0)",
-            ]
-        ]
-    )
-
-    def __init__(self, *args, **kwargs):
-        self._future_division = False
-        self._future_absolute_import = False
-        self._modules_warned_about = set()
-        self._branch_stack = []
-        super(Python3Checker, self).__init__(*args, **kwargs)
-
-    # pylint: disable=keyword-arg-before-vararg, arguments-differ
-    def add_message(self, msg_id, always_warn=False, *args, **kwargs):
-        if always_warn or not (
-            self._branch_stack and self._branch_stack[-1].is_py2_only
-        ):
-            super(Python3Checker, self).add_message(msg_id, *args, **kwargs)
-
-    def _is_py2_test(self, node):
-        if isinstance(node.test, astroid.Attribute) and isinstance(
-            node.test.expr, astroid.Name
-        ):
-            if node.test.expr.name == "six" and node.test.attrname == "PY2":
-                return True
-        elif (
-            isinstance(node.test, astroid.Compare)
-            and node.test.repr_tree() in self._python_2_tests
-        ):
-            return True
-        return False
-
-    def visit_if(self, node):
-        self._branch_stack.append(Branch(node, self._is_py2_test(node)))
-
-    def leave_if(self, node):
-        assert self._branch_stack.pop().node == node
-
-    def visit_ifexp(self, node):
-        self._branch_stack.append(Branch(node, self._is_py2_test(node)))
-
-    def leave_ifexp(self, node):
-        assert self._branch_stack.pop().node == node
-
-    def visit_module(self, node):  # pylint: disable=unused-argument
-        """Clear checker state after previous module."""
-        self._future_division = False
-        self._future_absolute_import = False
-
-    def visit_functiondef(self, node):
-        if node.is_method():
-            if node.name in self._unused_magic_methods:
-                method_name = node.name
-                if node.name.startswith("__"):
-                    method_name = node.name[2:-2]
-                self.add_message(method_name + "-method", node=node)
-            elif node.name == "next":
-                # If there is a method named `next` declared, if it is invokable
-                # with zero arguments then it implements the Iterator protocol.
-                # This means if the method is an instance method or a
-                # classmethod 1 argument should cause a failure, if it is a
-                # staticmethod 0 arguments should cause a failure.
-                failing_arg_count = 1
-                if utils.decorated_with(node, [bases.BUILTINS + ".staticmethod"]):
-                    failing_arg_count = 0
-                if len(node.args.args) == failing_arg_count:
-                    self.add_message("next-method-defined", node=node)
-
-    @utils.check_messages("parameter-unpacking")
-    def visit_arguments(self, node):
-        for arg in node.args:
-            if isinstance(arg, astroid.Tuple):
-                self.add_message("parameter-unpacking", node=arg)
-
-    @utils.check_messages("comprehension-escape")
-    def visit_listcomp(self, node):
-        names = {
-            generator.target.name
-            for generator in node.generators
-            if isinstance(generator.target, astroid.AssignName)
-        }
-        scope = node.parent.scope()
-        scope_names = scope.nodes_of_class(astroid.Name, skip_klass=astroid.FunctionDef)
-        has_redefined_assign_name = any(
-            assign_name
-            for assign_name in scope.nodes_of_class(
-                astroid.AssignName, skip_klass=astroid.FunctionDef
-            )
-            if assign_name.name in names and assign_name.lineno > node.lineno
-        )
-        if has_redefined_assign_name:
-            return
-
-        emitted_for_names = set()
-        scope_names = list(scope_names)
-        for scope_name in scope_names:
-            if (
-                scope_name.name not in names
-                or scope_name.lineno <= node.lineno
-                or scope_name.name in emitted_for_names
-                or scope_name.scope() == node
-            ):
-                continue
-
-            emitted_for_names.add(scope_name.name)
-            self.add_message("comprehension-escape", node=scope_name)
-
-    def visit_name(self, node):
-        """Detect when a "bad" built-in is referenced."""
-        found_node, _ = node.lookup(node.name)
-        if not _is_builtin(found_node):
-            return
-        if node.name not in self._bad_builtins:
-            return
-        if node_ignores_exception(node) or isinstance(
-            find_try_except_wrapper_node(node), astroid.ExceptHandler
-        ):
-            return
-
-        message = node.name.lower() + "-builtin"
-        self.add_message(message, node=node)
-
-    @utils.check_messages("print-statement")
-    def visit_print(self, node):
-        self.add_message("print-statement", node=node, always_warn=True)
-
-    def _warn_if_deprecated(self, node, module, attributes, report_on_modules=True):
-        for message, module_map in self._bad_python3_module_map.items():
-            if module in module_map and module not in self._modules_warned_about:
-                if isinstance(module_map, frozenset):
-                    if report_on_modules:
-                        self._modules_warned_about.add(module)
-                        self.add_message(message, node=node)
-                elif attributes and module_map[module].intersection(attributes):
-                    self.add_message(message, node=node)
-
-    def visit_importfrom(self, node):
-        if node.modname == "__future__":
-            for name, _ in node.names:
-                if name == "division":
-                    self._future_division = True
-                elif name == "absolute_import":
-                    self._future_absolute_import = True
-        else:
-            if not self._future_absolute_import:
-                if self.linter.is_message_enabled("no-absolute-import"):
-                    self.add_message("no-absolute-import", node=node)
-                    self._future_absolute_import = True
-            if not _is_conditional_import(node) and not node.level:
-                self._warn_if_deprecated(node, node.modname, {x[0] for x in node.names})
-
-        if node.names[0][0] == "*":
-            if self.linter.is_message_enabled("import-star-module-level"):
-                if not isinstance(node.scope(), astroid.Module):
-                    self.add_message("import-star-module-level", node=node)
-
-    def visit_import(self, node):
-        if not self._future_absolute_import:
-            if self.linter.is_message_enabled("no-absolute-import"):
-                self.add_message("no-absolute-import", node=node)
-                self._future_absolute_import = True
-        if not _is_conditional_import(node):
-            for name, _ in node.names:
-                self._warn_if_deprecated(node, name, None)
-
-    @utils.check_messages("metaclass-assignment")
-    def visit_classdef(self, node):
-        if "__metaclass__" in node.locals:
-            self.add_message("metaclass-assignment", node=node)
-        locals_and_methods = set(node.locals).union(x.name for x in node.mymethods())
-        if "__eq__" in locals_and_methods and "__hash__" not in locals_and_methods:
-            self.add_message("eq-without-hash", node=node)
-
-    @utils.check_messages("old-division")
-    def visit_binop(self, node):
-        if not self._future_division and node.op == "/":
-            for arg in (node.left, node.right):
-                inferred = utils.safe_infer(arg)
-                # If we can infer the object and that object is not an int, bail out.
-                if inferred and not (
-                    (
-                        isinstance(inferred, astroid.Const)
-                        and isinstance(inferred.value, int)
-                    )
-                    or (
-                        isinstance(inferred, astroid.Instance)
-                        and inferred.name == "int"
-                    )
-                ):
-                    break
-            else:
-                self.add_message("old-division", node=node)
-
-    def _check_cmp_argument(self, node):
-        # Check that the `cmp` argument is used
-        kwargs = []
-        if isinstance(node.func, astroid.Attribute) and node.func.attrname == "sort":
-            inferred = utils.safe_infer(node.func.expr)
-            if not inferred:
-                return
-
-            builtins_list = "{}.list".format(bases.BUILTINS)
-            if isinstance(inferred, astroid.List) or inferred.qname() == builtins_list:
-                kwargs = node.keywords
-
-        elif isinstance(node.func, astroid.Name) and node.func.name == "sorted":
-            inferred = utils.safe_infer(node.func)
-            if not inferred:
-                return
-
-            builtins_sorted = "{}.sorted".format(bases.BUILTINS)
-            if inferred.qname() == builtins_sorted:
-                kwargs = node.keywords
-
-        for kwarg in kwargs or []:
-            if kwarg.arg == "cmp":
-                self.add_message("using-cmp-argument", node=node)
-                return
-
-    @staticmethod
-    def _is_constant_string_or_name(node):
-        if isinstance(node, astroid.Const):
-            return isinstance(node.value, str)
-        return isinstance(node, astroid.Name)
-
-    @staticmethod
-    def _is_none(node):
-        return isinstance(node, astroid.Const) and node.value is None
-
-    @staticmethod
-    def _has_only_n_positional_args(node, number_of_args):
-        return len(node.args) == number_of_args and all(node.args) and not node.keywords
-
-    @staticmethod
-    def _could_be_string(inferred_types):
-        confidence = INFERENCE if inferred_types else INFERENCE_FAILURE
-        for inferred_type in inferred_types:
-            if inferred_type is astroid.Uninferable:
-                confidence = INFERENCE_FAILURE
-            elif not (
-                isinstance(inferred_type, astroid.Const)
-                and isinstance(inferred_type.value, str)
-            ):
-                return None
-        return confidence
-
-    def visit_call(self, node):
-        self._check_cmp_argument(node)
-
-        if isinstance(node.func, astroid.Attribute):
-            inferred_types = set()
-            try:
-                for inferred_receiver in node.func.expr.infer():
-                    if inferred_receiver is astroid.Uninferable:
-                        continue
-                    inferred_types.add(inferred_receiver)
-                    if isinstance(inferred_receiver, astroid.Module):
-                        self._warn_if_deprecated(
-                            node,
-                            inferred_receiver.name,
-                            {node.func.attrname},
-                            report_on_modules=False,
-                        )
-                    if (
-                        _inferred_value_is_dict(inferred_receiver)
-                        and node.func.attrname in DICT_METHODS
-                    ):
-                        if not _in_iterating_context(node):
-                            checker = "dict-{}-not-iterating".format(node.func.attrname)
-                            self.add_message(checker, node=node)
-            except astroid.InferenceError:
-                pass
-            if node.args:
-                is_str_confidence = self._could_be_string(inferred_types)
-                if is_str_confidence:
-                    if (
-                        node.func.attrname in ("encode", "decode")
-                        and len(node.args) >= 1
-                        and node.args[0]
-                    ):
-                        first_arg = node.args[0]
-                        self._validate_encoding(first_arg, node)
-                    if (
-                        node.func.attrname == "translate"
-                        and self._has_only_n_positional_args(node, 2)
-                        and self._is_none(node.args[0])
-                        and self._is_constant_string_or_name(node.args[1])
-                    ):
-                        # The above statement looking for calls of the form:
-                        #
-                        # foo.translate(None, 'abc123')
-                        #
-                        # or
-                        #
-                        # foo.translate(None, some_variable)
-                        #
-                        # This check is somewhat broad and _may_ have some false positives, but
-                        # after checking several large codebases it did not have any false
-                        # positives while finding several real issues.  This call pattern seems
-                        # rare enough that the trade off is worth it.
-                        self.add_message(
-                            "deprecated-str-translate-call",
-                            node=node,
-                            confidence=is_str_confidence,
-                        )
-                return
-            if node.keywords:
-                return
-            if node.func.attrname == "next":
-                self.add_message("next-method-called", node=node)
-            else:
-                if node.func.attrname in ("iterkeys", "itervalues", "iteritems"):
-                    self.add_message("dict-iter-method", node=node)
-                elif node.func.attrname in ("viewkeys", "viewvalues", "viewitems"):
-                    self.add_message("dict-view-method", node=node)
-        elif isinstance(node.func, astroid.Name):
-            found_node = node.func.lookup(node.func.name)[0]
-            if _is_builtin(found_node):
-                if node.func.name in ("filter", "map", "range", "zip"):
-                    if not _in_iterating_context(node):
-                        checker = "{}-builtin-not-iterating".format(node.func.name)
-                        self.add_message(checker, node=node)
-                if node.func.name == "open" and node.keywords:
-                    kwargs = node.keywords
-                    for kwarg in kwargs or []:
-                        if kwarg.arg == "encoding":
-                            self._validate_encoding(kwarg.value, node)
-                            break
-
-    def _validate_encoding(self, encoding, node):
-        if isinstance(encoding, astroid.Const):
-            value = encoding.value
-            if value in self._invalid_encodings:
-                self.add_message("invalid-str-codec", node=node)
-
-    @utils.check_messages("indexing-exception")
-    def visit_subscript(self, node):
-        """ Look for indexing exceptions. """
-        try:
-            for inferred in node.value.infer():
-                if not isinstance(inferred, astroid.Instance):
-                    continue
-                if utils.inherit_from_std_ex(inferred):
-                    self.add_message("indexing-exception", node=node)
-        except astroid.InferenceError:
-            return
-
-    def visit_assignattr(self, node):
-        if isinstance(node.assign_type(), astroid.AugAssign):
-            self.visit_attribute(node)
-
-    def visit_delattr(self, node):
-        self.visit_attribute(node)
-
-    @utils.check_messages("exception-message-attribute", "xreadlines-attribute")
-    def visit_attribute(self, node):
-        """Look for removed attributes"""
-        if node.attrname == "xreadlines":
-            self.add_message("xreadlines-attribute", node=node)
-            return
-
-        exception_message = "message"
-        try:
-            for inferred in node.expr.infer():
-                if isinstance(inferred, astroid.Instance) and utils.inherit_from_std_ex(
-                    inferred
-                ):
-                    if node.attrname == exception_message:
-
-                        # Exceptions with .message clearly defined are an exception
-                        if exception_message in inferred.instance_attrs:
-                            continue
-                        self.add_message("exception-message-attribute", node=node)
-                if isinstance(inferred, astroid.Module):
-                    self._warn_if_deprecated(
-                        node, inferred.name, {node.attrname}, report_on_modules=False
-                    )
-        except astroid.InferenceError:
-            return
-
-    @utils.check_messages("unpacking-in-except", "comprehension-escape")
-    def visit_excepthandler(self, node):
-        """Visit an except handler block and check for exception unpacking."""
-
-        def _is_used_in_except_block(node):
-            scope = node.scope()
-            current = node
-            while (
-                current
-                and current != scope
-                and not isinstance(current, astroid.ExceptHandler)
-            ):
-                current = current.parent
-            return isinstance(current, astroid.ExceptHandler) and current.type != node
-
-        if isinstance(node.name, (astroid.Tuple, astroid.List)):
-            self.add_message("unpacking-in-except", node=node)
-            return
-
-        if not node.name:
-            return
-
-        # Find any names
-        scope = node.parent.scope()
-        scope_names = scope.nodes_of_class(astroid.Name, skip_klass=astroid.FunctionDef)
-        scope_names = list(scope_names)
-        potential_leaked_names = [
-            scope_name
-            for scope_name in scope_names
-            if scope_name.name == node.name.name
-            and scope_name.lineno > node.lineno
-            and not _is_used_in_except_block(scope_name)
-        ]
-        reassignments_for_same_name = {
-            assign_name.lineno
-            for assign_name in scope.nodes_of_class(
-                astroid.AssignName, skip_klass=astroid.FunctionDef
-            )
-            if assign_name.name == node.name.name
-        }
-        for leaked_name in potential_leaked_names:
-            if any(
-                node.lineno < elem < leaked_name.lineno
-                for elem in reassignments_for_same_name
-            ):
-                continue
-            self.add_message("exception-escape", node=leaked_name)
-
-    @utils.check_messages("backtick")
-    def visit_repr(self, node):
-        self.add_message("backtick", node=node)
-
-    @utils.check_messages("raising-string", "old-raise-syntax")
-    def visit_raise(self, node):
-        """Visit a raise statement and check for raising
-        strings or old-raise-syntax.
-        """
-
-        # Ignore empty raise.
-        if node.exc is None:
-            return
-        expr = node.exc
-        if self._check_raise_value(node, expr):
-            return
-        try:
-            value = next(astroid.unpack_infer(expr))
-        except astroid.InferenceError:
-            return
-        self._check_raise_value(node, value)
-
-    def _check_raise_value(self, node, expr):
-        if isinstance(expr, astroid.Const):
-            value = expr.value
-            if isinstance(value, str):
-                self.add_message("raising-string", node=node)
-                return True
-        return None
-
-
-class Python3TokenChecker(checkers.BaseTokenChecker):
-    __implements__ = interfaces.ITokenChecker
-    name = "python3"
-    enabled = False
-
-    msgs = {
-        "E1606": (
-            "Use of long suffix",
-            "long-suffix",
-            'Used when "l" or "L" is used to mark a long integer. '
-            "This will not work in Python 3, since `int` and `long` "
-            "types have merged.",
-            {"maxversion": (3, 0)},
-        ),
-        "E1607": (
-            "Use of the <> operator",
-            "old-ne-operator",
-            'Used when the deprecated "<>" operator is used instead '
-            'of "!=". This is removed in Python 3.',
-            {"maxversion": (3, 0), "old_names": [("W0331", "old-old-ne-operator")]},
-        ),
-        "E1608": (
-            "Use of old octal literal",
-            "old-octal-literal",
-            "Used when encountering the old octal syntax, "
-            "removed in Python 3. To use the new syntax, "
-            "prepend 0o on the number.",
-            {"maxversion": (3, 0)},
-        ),
-        "E1610": (
-            "Non-ascii bytes literals not supported in 3.x",
-            "non-ascii-bytes-literal",
-            "Used when non-ascii bytes literals are found in a program. "
-            "They are no longer supported in Python 3.",
-            {"maxversion": (3, 0)},
-        ),
-    }
-
-    def process_tokens(self, tokens):
-        for idx, (tok_type, token, start, _, _) in enumerate(tokens):
-            if tok_type == tokenize.NUMBER:
-                if token.lower().endswith("l"):
-                    # This has a different semantic than lowercase-l-suffix.
-                    self.add_message("long-suffix", line=start[0])
-                elif _is_old_octal(token):
-                    self.add_message("old-octal-literal", line=start[0])
-            if tokens[idx][1] == "<>":
-                self.add_message("old-ne-operator", line=tokens[idx][2][0])
-            if tok_type == tokenize.STRING and token.startswith("b"):
-                if any(elem for elem in token if ord(elem) > 127):
-                    self.add_message("non-ascii-bytes-literal", line=start[0])
-
-
-def register(linter):
-    linter.register_checker(Python3Checker(linter))
-    linter.register_checker(Python3TokenChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/raw_metrics.py b/venv/Lib/site-packages/pylint/checkers/raw_metrics.py
deleted file mode 100644
index 0564398..0000000
--- a/venv/Lib/site-packages/pylint/checkers/raw_metrics.py
+++ /dev/null
@@ -1,119 +0,0 @@
-# Copyright (c) 2007, 2010, 2013, 2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013 Google, Inc.
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Mike Frysinger <vapier@gentoo.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-""" Copyright (c) 2003-2010 LOGILAB S.A. (Paris, FRANCE).
- http://www.logilab.fr/ -- mailto:contact@logilab.fr
-
-Raw metrics checker
-"""
-
-import tokenize
-from typing import Any
-
-from pylint.checkers import BaseTokenChecker
-from pylint.exceptions import EmptyReportError
-from pylint.interfaces import ITokenChecker
-from pylint.reporters.ureports.nodes import Table
-
-
-def report_raw_stats(sect, stats, _):
-    """calculate percentage of code / doc / comment / empty
-    """
-    total_lines = stats["total_lines"]
-    if not total_lines:
-        raise EmptyReportError()
-    sect.description = "%s lines have been analyzed" % total_lines
-    lines = ("type", "number", "%", "previous", "difference")
-    for node_type in ("code", "docstring", "comment", "empty"):
-        key = node_type + "_lines"
-        total = stats[key]
-        percent = float(total * 100) / total_lines
-        lines += (node_type, str(total), "%.2f" % percent, "NC", "NC")
-    sect.append(Table(children=lines, cols=5, rheaders=1))
-
-
-class RawMetricsChecker(BaseTokenChecker):
-    """does not check anything but gives some raw metrics :
-    * total number of lines
-    * total number of code lines
-    * total number of docstring lines
-    * total number of comments lines
-    * total number of empty lines
-    """
-
-    __implements__ = (ITokenChecker,)
-
-    # configuration section name
-    name = "metrics"
-    # configuration options
-    options = ()
-    # messages
-    msgs = {}  # type: Any
-    # reports
-    reports = (("RP0701", "Raw metrics", report_raw_stats),)
-
-    def __init__(self, linter):
-        BaseTokenChecker.__init__(self, linter)
-        self.stats = None
-
-    def open(self):
-        """init statistics"""
-        self.stats = self.linter.add_stats(
-            total_lines=0,
-            code_lines=0,
-            empty_lines=0,
-            docstring_lines=0,
-            comment_lines=0,
-        )
-
-    def process_tokens(self, tokens):
-        """update stats"""
-        i = 0
-        tokens = list(tokens)
-        while i < len(tokens):
-            i, lines_number, line_type = get_type(tokens, i)
-            self.stats["total_lines"] += lines_number
-            self.stats[line_type] += lines_number
-
-
-JUNK = (tokenize.NL, tokenize.INDENT, tokenize.NEWLINE, tokenize.ENDMARKER)
-
-
-def get_type(tokens, start_index):
-    """return the line type : docstring, comment, code, empty"""
-    i = start_index
-    tok_type = tokens[i][0]
-    start = tokens[i][2]
-    pos = start
-    line_type = None
-    while i < len(tokens) and tokens[i][2][0] == start[0]:
-        tok_type = tokens[i][0]
-        pos = tokens[i][3]
-        if line_type is None:
-            if tok_type == tokenize.STRING:
-                line_type = "docstring_lines"
-            elif tok_type == tokenize.COMMENT:
-                line_type = "comment_lines"
-            elif tok_type in JUNK:
-                pass
-            else:
-                line_type = "code_lines"
-        i += 1
-    if line_type is None:
-        line_type = "empty_lines"
-    elif i < len(tokens) and tokens[i][0] == tokenize.NEWLINE:
-        i += 1
-    return i, pos[0] - start[0] + 1, line_type
-
-
-def register(linter):
-    """ required method to auto register this checker """
-    linter.register_checker(RawMetricsChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/refactoring.py b/venv/Lib/site-packages/pylint/checkers/refactoring.py
deleted file mode 100644
index 2831343..0000000
--- a/venv/Lib/site-packages/pylint/checkers/refactoring.py
+++ /dev/null
@@ -1,1510 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016-2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2017-2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2017 Hugo <hugovk@users.noreply.github.com>
-# Copyright (c) 2017 Łukasz Sznuk <ls@rdprojekt.pl>
-# Copyright (c) 2017 Alex Hearn <alex.d.hearn@gmail.com>
-# Copyright (c) 2017 Antonio Ossa <aaossa@uc.cl>
-# Copyright (c) 2018 Konstantin Manna <Konstantin@Manna.uno>
-# Copyright (c) 2018 Konstantin <Github@pheanex.de>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Matej Marušák <marusak.matej@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-# Copyright (c) 2018 Mr. Senko <atodorov@mrsenko.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Looks for code which can be refactored."""
-import builtins
-import collections
-import itertools
-import tokenize
-from functools import reduce
-
-import astroid
-from astroid import decorators
-
-from pylint import checkers, interfaces
-from pylint import utils as lint_utils
-from pylint.checkers import utils
-
-KNOWN_INFINITE_ITERATORS = {"itertools.count"}
-BUILTIN_EXIT_FUNCS = frozenset(("quit", "exit"))
-
-
-def _if_statement_is_always_returning(if_node, returning_node_class):
-    for node in if_node.body:
-        if isinstance(node, returning_node_class):
-            return True
-    return False
-
-
-def _is_len_call(node):
-    """Checks if node is len(SOMETHING)."""
-    return (
-        isinstance(node, astroid.Call)
-        and isinstance(node.func, astroid.Name)
-        and node.func.name == "len"
-    )
-
-
-def _is_constant_zero(node):
-    return isinstance(node, astroid.Const) and node.value == 0
-
-
-def _node_is_test_condition(node):
-    """ Checks if node is an if, while, assert or if expression statement."""
-    return isinstance(node, (astroid.If, astroid.While, astroid.Assert, astroid.IfExp))
-
-
-def _is_trailing_comma(tokens, index):
-    """Check if the given token is a trailing comma
-
-    :param tokens: Sequence of modules tokens
-    :type tokens: list[tokenize.TokenInfo]
-    :param int index: Index of token under check in tokens
-    :returns: True if the token is a comma which trails an expression
-    :rtype: bool
-    """
-    token = tokens[index]
-    if token.exact_type != tokenize.COMMA:
-        return False
-    # Must have remaining tokens on the same line such as NEWLINE
-    left_tokens = itertools.islice(tokens, index + 1, None)
-    same_line_remaining_tokens = list(
-        itertools.takewhile(
-            lambda other_token, _token=token: other_token.start[0] == _token.start[0],
-            left_tokens,
-        )
-    )
-    # Note: If the newline is tokenize.NEWLINE and not tokenize.NL
-    # then the newline denotes the end of expression
-    is_last_element = all(
-        other_token.type in (tokenize.NEWLINE, tokenize.COMMENT)
-        for other_token in same_line_remaining_tokens
-    )
-    if not same_line_remaining_tokens or not is_last_element:
-        return False
-
-    def get_curline_index_start():
-        """Get the index denoting the start of the current line"""
-        for subindex, token in enumerate(reversed(tokens[:index])):
-            # See Lib/tokenize.py and Lib/token.py in cpython for more info
-            if token.type in (tokenize.NEWLINE, tokenize.NL):
-                return index - subindex
-        return 0
-
-    curline_start = get_curline_index_start()
-    expected_tokens = {"return", "yield"}
-    for prevtoken in tokens[curline_start:index]:
-        if "=" in prevtoken.string or prevtoken.string in expected_tokens:
-            return True
-    return False
-
-
-class RefactoringChecker(checkers.BaseTokenChecker):
-    """Looks for code which can be refactored
-
-    This checker also mixes the astroid and the token approaches
-    in order to create knowledge about whether an "else if" node
-    is a true "else if" node, or an "elif" node.
-    """
-
-    __implements__ = (interfaces.ITokenChecker, interfaces.IAstroidChecker)
-
-    name = "refactoring"
-
-    msgs = {
-        "R1701": (
-            "Consider merging these isinstance calls to isinstance(%s, (%s))",
-            "consider-merging-isinstance",
-            "Used when multiple consecutive isinstance calls can be merged into one.",
-        ),
-        "R1706": (
-            "Consider using ternary (%s)",
-            "consider-using-ternary",
-            "Used when one of known pre-python 2.5 ternary syntax is used.",
-        ),
-        "R1709": (
-            "Boolean expression may be simplified to %s",
-            "simplify-boolean-expression",
-            "Emitted when redundant pre-python 2.5 ternary syntax is used.",
-        ),
-        "R1702": (
-            "Too many nested blocks (%s/%s)",
-            "too-many-nested-blocks",
-            "Used when a function or a method has too many nested "
-            "blocks. This makes the code less understandable and "
-            "maintainable.",
-            {"old_names": [("R0101", "old-too-many-nested-blocks")]},
-        ),
-        "R1703": (
-            "The if statement can be replaced with %s",
-            "simplifiable-if-statement",
-            "Used when an if statement can be replaced with 'bool(test)'. ",
-            {"old_names": [("R0102", "old-simplifiable-if-statement")]},
-        ),
-        "R1704": (
-            "Redefining argument with the local name %r",
-            "redefined-argument-from-local",
-            "Used when a local name is redefining an argument, which might "
-            "suggest a potential error. This is taken in account only for "
-            "a handful of name binding operations, such as for iteration, "
-            "with statement assignment and exception handler assignment.",
-        ),
-        "R1705": (
-            'Unnecessary "%s" after "return"',
-            "no-else-return",
-            "Used in order to highlight an unnecessary block of "
-            "code following an if containing a return statement. "
-            "As such, it will warn when it encounters an else "
-            "following a chain of ifs, all of them containing a "
-            "return statement.",
-        ),
-        "R1707": (
-            "Disallow trailing comma tuple",
-            "trailing-comma-tuple",
-            "In Python, a tuple is actually created by the comma symbol, "
-            "not by the parentheses. Unfortunately, one can actually create a "
-            "tuple by misplacing a trailing comma, which can lead to potential "
-            "weird bugs in your code. You should always use parentheses "
-            "explicitly for creating a tuple.",
-        ),
-        "R1708": (
-            "Do not raise StopIteration in generator, use return statement instead",
-            "stop-iteration-return",
-            "According to PEP479, the raise of StopIteration to end the loop of "
-            "a generator may lead to hard to find bugs. This PEP specify that "
-            "raise StopIteration has to be replaced by a simple return statement",
-        ),
-        "R1710": (
-            "Either all return statements in a function should return an expression, "
-            "or none of them should.",
-            "inconsistent-return-statements",
-            "According to PEP8, if any return statement returns an expression, "
-            "any return statements where no value is returned should explicitly "
-            "state this as return None, and an explicit return statement "
-            "should be present at the end of the function (if reachable)",
-        ),
-        "R1711": (
-            "Useless return at end of function or method",
-            "useless-return",
-            'Emitted when a single "return" or "return None" statement is found '
-            "at the end of function or method definition. This statement can safely be "
-            "removed because Python will implicitly return None",
-        ),
-        "R1712": (
-            "Consider using tuple unpacking for swapping variables",
-            "consider-swap-variables",
-            "You do not have to use a temporary variable in order to "
-            'swap variables. Using "tuple unpacking" to directly swap '
-            "variables makes the intention more clear.",
-        ),
-        "R1713": (
-            "Consider using str.join(sequence) for concatenating "
-            "strings from an iterable",
-            "consider-using-join",
-            "Using str.join(sequence) is faster, uses less memory "
-            "and increases readability compared to for-loop iteration.",
-        ),
-        "R1714": (
-            'Consider merging these comparisons with "in" to %r',
-            "consider-using-in",
-            "To check if a variable is equal to one of many values,"
-            'combine the values into a tuple and check if the variable is contained "in" it '
-            "instead of checking for equality against each of the values."
-            "This is faster and less verbose.",
-        ),
-        "R1715": (
-            "Consider using dict.get for getting values from a dict "
-            "if a key is present or a default if not",
-            "consider-using-get",
-            "Using the builtin dict.get for getting a value from a dictionary "
-            "if a key is present or a default if not, is simpler and considered "
-            "more idiomatic, although sometimes a bit slower",
-        ),
-        "R1716": (
-            "Simplify chained comparison between the operands",
-            "chained-comparison",
-            "This message is emitted when pylint encounters boolean operation like"
-            '"a < b and b < c", suggesting instead to refactor it to "a < b < c"',
-        ),
-        "R1717": (
-            "Consider using a dictionary comprehension",
-            "consider-using-dict-comprehension",
-            "Emitted when we detect the creation of a dictionary "
-            "using the dict() callable and a transient list. "
-            "Although there is nothing syntactically wrong with this code, "
-            "it is hard to read and can be simplified to a dict comprehension."
-            "Also it is faster since you don't need to create another "
-            "transient list",
-        ),
-        "R1718": (
-            "Consider using a set comprehension",
-            "consider-using-set-comprehension",
-            "Although there is nothing syntactically wrong with this code, "
-            "it is hard to read and can be simplified to a set comprehension."
-            "Also it is faster since you don't need to create another "
-            "transient list",
-        ),
-        "R1719": (
-            "The if expression can be replaced with %s",
-            "simplifiable-if-expression",
-            "Used when an if expression can be replaced with 'bool(test)'. ",
-        ),
-        "R1720": (
-            'Unnecessary "%s" after "raise"',
-            "no-else-raise",
-            "Used in order to highlight an unnecessary block of "
-            "code following an if containing a raise statement. "
-            "As such, it will warn when it encounters an else "
-            "following a chain of ifs, all of them containing a "
-            "raise statement.",
-        ),
-        "R1721": (
-            "Unnecessary use of a comprehension",
-            "unnecessary-comprehension",
-            "Instead of using an identitiy comprehension, "
-            "consider using the list, dict or set constructor. "
-            "It is faster and simpler.",
-        ),
-        "R1722": (
-            "Consider using sys.exit()",
-            "consider-using-sys-exit",
-            "Instead of using exit() or quit(), consider using the sys.exit().",
-        ),
-        "R1723": (
-            'Unnecessary "%s" after "break"',
-            "no-else-break",
-            "Used in order to highlight an unnecessary block of "
-            "code following an if containing a break statement. "
-            "As such, it will warn when it encounters an else "
-            "following a chain of ifs, all of them containing a "
-            "break statement.",
-        ),
-        "R1724": (
-            'Unnecessary "%s" after "continue"',
-            "no-else-continue",
-            "Used in order to highlight an unnecessary block of "
-            "code following an if containing a continue statement. "
-            "As such, it will warn when it encounters an else "
-            "following a chain of ifs, all of them containing a "
-            "continue statement.",
-        ),
-    }
-    options = (
-        (
-            "max-nested-blocks",
-            {
-                "default": 5,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of nested blocks for function / method body",
-            },
-        ),
-        (
-            "never-returning-functions",
-            {
-                "default": ("sys.exit",),
-                "type": "csv",
-                "help": "Complete name of functions that never returns. When checking "
-                "for inconsistent-return-statements if a never returning function is "
-                "called then it will be considered as an explicit return statement "
-                "and no message will be printed.",
-            },
-        ),
-    )
-
-    priority = 0
-
-    def __init__(self, linter=None):
-        checkers.BaseTokenChecker.__init__(self, linter)
-        self._return_nodes = {}
-        self._init()
-        self._never_returning_functions = None
-
-    def _init(self):
-        self._nested_blocks = []
-        self._elifs = []
-        self._nested_blocks_msg = None
-        self._reported_swap_nodes = set()
-
-    def open(self):
-        # do this in open since config not fully initialized in __init__
-        self._never_returning_functions = set(self.config.never_returning_functions)
-
-    @decorators.cachedproperty
-    def _dummy_rgx(self):
-        return lint_utils.get_global_option(self, "dummy-variables-rgx", default=None)
-
-    @staticmethod
-    def _is_bool_const(node):
-        return isinstance(node.value, astroid.Const) and isinstance(
-            node.value.value, bool
-        )
-
-    def _is_actual_elif(self, node):
-        """Check if the given node is an actual elif
-
-        This is a problem we're having with the builtin ast module,
-        which splits `elif` branches into a separate if statement.
-        Unfortunately we need to know the exact type in certain
-        cases.
-        """
-        if isinstance(node.parent, astroid.If):
-            orelse = node.parent.orelse
-            # current if node must directly follow an "else"
-            if orelse and orelse == [node]:
-                if (node.lineno, node.col_offset) in self._elifs:
-                    return True
-        return False
-
-    def _check_simplifiable_if(self, node):
-        """Check if the given if node can be simplified.
-
-        The if statement can be reduced to a boolean expression
-        in some cases. For instance, if there are two branches
-        and both of them return a boolean value that depends on
-        the result of the statement's test, then this can be reduced
-        to `bool(test)` without losing any functionality.
-        """
-
-        if self._is_actual_elif(node):
-            # Not interested in if statements with multiple branches.
-            return
-        if len(node.orelse) != 1 or len(node.body) != 1:
-            return
-
-        # Check if both branches can be reduced.
-        first_branch = node.body[0]
-        else_branch = node.orelse[0]
-        if isinstance(first_branch, astroid.Return):
-            if not isinstance(else_branch, astroid.Return):
-                return
-            first_branch_is_bool = self._is_bool_const(first_branch)
-            else_branch_is_bool = self._is_bool_const(else_branch)
-            reduced_to = "'return bool(test)'"
-        elif isinstance(first_branch, astroid.Assign):
-            if not isinstance(else_branch, astroid.Assign):
-                return
-
-            # Check if we assign to the same value
-            first_branch_targets = [
-                target.name
-                for target in first_branch.targets
-                if isinstance(target, astroid.AssignName)
-            ]
-            else_branch_targets = [
-                target.name
-                for target in else_branch.targets
-                if isinstance(target, astroid.AssignName)
-            ]
-            if not first_branch_targets or not else_branch_targets:
-                return
-            if sorted(first_branch_targets) != sorted(else_branch_targets):
-                return
-
-            first_branch_is_bool = self._is_bool_const(first_branch)
-            else_branch_is_bool = self._is_bool_const(else_branch)
-            reduced_to = "'var = bool(test)'"
-        else:
-            return
-
-        if not first_branch_is_bool or not else_branch_is_bool:
-            return
-        if not first_branch.value.value:
-            # This is a case that can't be easily simplified and
-            # if it can be simplified, it will usually result in a
-            # code that's harder to understand and comprehend.
-            # Let's take for instance `arg and arg <= 3`. This could theoretically be
-            # reduced to `not arg or arg > 3`, but the net result is that now the
-            # condition is harder to understand, because it requires understanding of
-            # an extra clause:
-            #   * first, there is the negation of truthness with `not arg`
-            #   * the second clause is `arg > 3`, which occurs when arg has a
-            #     a truth value, but it implies that `arg > 3` is equivalent
-            #     with `arg and arg > 3`, which means that the user must
-            #     think about this assumption when evaluating `arg > 3`.
-            #     The original form is easier to grasp.
-            return
-
-        self.add_message("simplifiable-if-statement", node=node, args=(reduced_to,))
-
-    def process_tokens(self, tokens):
-        # Process tokens and look for 'if' or 'elif'
-        for index, token in enumerate(tokens):
-            token_string = token[1]
-            if token_string == "elif":
-                # AST exists by the time process_tokens is called, so
-                # it's safe to assume tokens[index+1]
-                # exists. tokens[index+1][2] is the elif's position as
-                # reported by CPython and PyPy,
-                # tokens[index][2] is the actual position and also is
-                # reported by IronPython.
-                self._elifs.extend([tokens[index][2], tokens[index + 1][2]])
-            elif _is_trailing_comma(tokens, index):
-                if self.linter.is_message_enabled("trailing-comma-tuple"):
-                    self.add_message("trailing-comma-tuple", line=token.start[0])
-
-    def leave_module(self, _):
-        self._init()
-
-    @utils.check_messages("too-many-nested-blocks")
-    def visit_tryexcept(self, node):
-        self._check_nested_blocks(node)
-
-    visit_tryfinally = visit_tryexcept
-    visit_while = visit_tryexcept
-
-    def _check_redefined_argument_from_local(self, name_node):
-        if self._dummy_rgx and self._dummy_rgx.match(name_node.name):
-            return
-        if not name_node.lineno:
-            # Unknown position, maybe it is a manually built AST?
-            return
-
-        scope = name_node.scope()
-        if not isinstance(scope, astroid.FunctionDef):
-            return
-
-        for defined_argument in scope.args.nodes_of_class(
-            astroid.AssignName, skip_klass=(astroid.Lambda,)
-        ):
-            if defined_argument.name == name_node.name:
-                self.add_message(
-                    "redefined-argument-from-local",
-                    node=name_node,
-                    args=(name_node.name,),
-                )
-
-    @utils.check_messages("redefined-argument-from-local", "too-many-nested-blocks")
-    def visit_for(self, node):
-        self._check_nested_blocks(node)
-
-        for name in node.target.nodes_of_class(astroid.AssignName):
-            self._check_redefined_argument_from_local(name)
-
-    @utils.check_messages("redefined-argument-from-local")
-    def visit_excepthandler(self, node):
-        if node.name and isinstance(node.name, astroid.AssignName):
-            self._check_redefined_argument_from_local(node.name)
-
-    @utils.check_messages("redefined-argument-from-local")
-    def visit_with(self, node):
-        for _, names in node.items:
-            if not names:
-                continue
-            for name in names.nodes_of_class(astroid.AssignName):
-                self._check_redefined_argument_from_local(name)
-
-    def _check_superfluous_else(self, node, msg_id, returning_node_class):
-        if not node.orelse:
-            # Not interested in if statements without else.
-            return
-
-        if self._is_actual_elif(node):
-            # Not interested in elif nodes; only if
-            return
-
-        if _if_statement_is_always_returning(node, returning_node_class):
-            orelse = node.orelse[0]
-            followed_by_elif = (orelse.lineno, orelse.col_offset) in self._elifs
-            self.add_message(
-                msg_id, node=node, args="elif" if followed_by_elif else "else"
-            )
-
-    def _check_superfluous_else_return(self, node):
-        return self._check_superfluous_else(
-            node, msg_id="no-else-return", returning_node_class=astroid.Return
-        )
-
-    def _check_superfluous_else_raise(self, node):
-        return self._check_superfluous_else(
-            node, msg_id="no-else-raise", returning_node_class=astroid.Raise
-        )
-
-    def _check_superfluous_else_break(self, node):
-        return self._check_superfluous_else(
-            node, msg_id="no-else-break", returning_node_class=astroid.Break
-        )
-
-    def _check_superfluous_else_continue(self, node):
-        return self._check_superfluous_else(
-            node, msg_id="no-else-continue", returning_node_class=astroid.Continue
-        )
-
-    def _check_consider_get(self, node):
-        def type_and_name_are_equal(node_a, node_b):
-            for _type in [astroid.Name, astroid.AssignName]:
-                if all(isinstance(_node, _type) for _node in [node_a, node_b]):
-                    return node_a.name == node_b.name
-            if all(isinstance(_node, astroid.Const) for _node in [node_a, node_b]):
-                return node_a.value == node_b.value
-            return False
-
-        if_block_ok = (
-            isinstance(node.test, astroid.Compare)
-            and len(node.body) == 1
-            and isinstance(node.body[0], astroid.Assign)
-            and isinstance(node.body[0].value, astroid.Subscript)
-            and type_and_name_are_equal(node.body[0].value.value, node.test.ops[0][1])
-            and isinstance(node.body[0].value.slice, astroid.Index)
-            and type_and_name_are_equal(node.body[0].value.slice.value, node.test.left)
-            and len(node.body[0].targets) == 1
-            and isinstance(node.body[0].targets[0], astroid.AssignName)
-            and isinstance(utils.safe_infer(node.test.ops[0][1]), astroid.Dict)
-        )
-
-        if if_block_ok and not node.orelse:
-            self.add_message("consider-using-get", node=node)
-        elif (
-            if_block_ok
-            and len(node.orelse) == 1
-            and isinstance(node.orelse[0], astroid.Assign)
-            and type_and_name_are_equal(
-                node.orelse[0].targets[0], node.body[0].targets[0]
-            )
-            and len(node.orelse[0].targets) == 1
-        ):
-            self.add_message("consider-using-get", node=node)
-
-    @utils.check_messages(
-        "too-many-nested-blocks",
-        "simplifiable-if-statement",
-        "no-else-return",
-        "no-else-raise",
-        "no-else-break",
-        "no-else-continue",
-        "consider-using-get",
-    )
-    def visit_if(self, node):
-        self._check_simplifiable_if(node)
-        self._check_nested_blocks(node)
-        self._check_superfluous_else_return(node)
-        self._check_superfluous_else_raise(node)
-        self._check_superfluous_else_break(node)
-        self._check_superfluous_else_continue(node)
-        self._check_consider_get(node)
-
-    @utils.check_messages("simplifiable-if-expression")
-    def visit_ifexp(self, node):
-        self._check_simplifiable_ifexp(node)
-
-    def _check_simplifiable_ifexp(self, node):
-        if not isinstance(node.body, astroid.Const) or not isinstance(
-            node.orelse, astroid.Const
-        ):
-            return
-
-        if not isinstance(node.body.value, bool) or not isinstance(
-            node.orelse.value, bool
-        ):
-            return
-
-        if isinstance(node.test, astroid.Compare):
-            test_reduced_to = "test"
-        else:
-            test_reduced_to = "bool(test)"
-
-        if (node.body.value, node.orelse.value) == (True, False):
-            reduced_to = "'{}'".format(test_reduced_to)
-        elif (node.body.value, node.orelse.value) == (False, True):
-            reduced_to = "'not test'"
-        else:
-            return
-
-        self.add_message("simplifiable-if-expression", node=node, args=(reduced_to,))
-
-    @utils.check_messages(
-        "too-many-nested-blocks", "inconsistent-return-statements", "useless-return"
-    )
-    def leave_functiondef(self, node):
-        # check left-over nested blocks stack
-        self._emit_nested_blocks_message_if_needed(self._nested_blocks)
-        # new scope = reinitialize the stack of nested blocks
-        self._nested_blocks = []
-        #  check consistent return statements
-        self._check_consistent_returns(node)
-        # check for single return or return None at the end
-        self._check_return_at_the_end(node)
-        self._return_nodes[node.name] = []
-
-    @utils.check_messages("stop-iteration-return")
-    def visit_raise(self, node):
-        self._check_stop_iteration_inside_generator(node)
-
-    def _check_stop_iteration_inside_generator(self, node):
-        """Check if an exception of type StopIteration is raised inside a generator"""
-        frame = node.frame()
-        if not isinstance(frame, astroid.FunctionDef) or not frame.is_generator():
-            return
-        if utils.node_ignores_exception(node, StopIteration):
-            return
-        if not node.exc:
-            return
-        exc = utils.safe_infer(node.exc)
-        if exc is None or exc is astroid.Uninferable:
-            return
-        if self._check_exception_inherit_from_stopiteration(exc):
-            self.add_message("stop-iteration-return", node=node)
-
-    @staticmethod
-    def _check_exception_inherit_from_stopiteration(exc):
-        """Return True if the exception node in argument inherit from StopIteration"""
-        stopiteration_qname = "{}.StopIteration".format(utils.EXCEPTIONS_MODULE)
-        return any(_class.qname() == stopiteration_qname for _class in exc.mro())
-
-    def _check_consider_using_comprehension_constructor(self, node):
-        if (
-            isinstance(node.func, astroid.Name)
-            and node.args
-            and isinstance(node.args[0], astroid.ListComp)
-        ):
-            if node.func.name == "dict" and not isinstance(
-                node.args[0].elt, astroid.Call
-            ):
-                message_name = "consider-using-dict-comprehension"
-                self.add_message(message_name, node=node)
-            elif node.func.name == "set":
-                message_name = "consider-using-set-comprehension"
-                self.add_message(message_name, node=node)
-
-    @utils.check_messages(
-        "stop-iteration-return",
-        "consider-using-dict-comprehension",
-        "consider-using-set-comprehension",
-        "consider-using-sys-exit",
-    )
-    def visit_call(self, node):
-        self._check_raising_stopiteration_in_generator_next_call(node)
-        self._check_consider_using_comprehension_constructor(node)
-        self._check_quit_exit_call(node)
-
-    @staticmethod
-    def _has_exit_in_scope(scope):
-        exit_func = scope.locals.get("exit")
-        return bool(
-            exit_func and isinstance(exit_func[0], (astroid.ImportFrom, astroid.Import))
-        )
-
-    def _check_quit_exit_call(self, node):
-
-        if isinstance(node.func, astroid.Name) and node.func.name in BUILTIN_EXIT_FUNCS:
-            # If we have `exit` imported from `sys` in the current or global scope, exempt this instance.
-            local_scope = node.scope()
-            if self._has_exit_in_scope(local_scope) or self._has_exit_in_scope(
-                node.root()
-            ):
-                return
-            self.add_message("consider-using-sys-exit", node=node)
-
-    def _check_raising_stopiteration_in_generator_next_call(self, node):
-        """Check if a StopIteration exception is raised by the call to next function
-
-        If the next value has a default value, then do not add message.
-
-        :param node: Check to see if this Call node is a next function
-        :type node: :class:`astroid.node_classes.Call`
-        """
-
-        def _looks_like_infinite_iterator(param):
-            inferred = utils.safe_infer(param)
-            if inferred:
-                return inferred.qname() in KNOWN_INFINITE_ITERATORS
-            return False
-
-        if isinstance(node.func, astroid.Attribute):
-            # A next() method, which is now what we want.
-            return
-
-        inferred = utils.safe_infer(node.func)
-        if getattr(inferred, "name", "") == "next":
-            frame = node.frame()
-            # The next builtin can only have up to two
-            # positional arguments and no keyword arguments
-            has_sentinel_value = len(node.args) > 1
-            if (
-                isinstance(frame, astroid.FunctionDef)
-                and frame.is_generator()
-                and not has_sentinel_value
-                and not utils.node_ignores_exception(node, StopIteration)
-                and not _looks_like_infinite_iterator(node.args[0])
-            ):
-                self.add_message("stop-iteration-return", node=node)
-
-    def _check_nested_blocks(self, node):
-        """Update and check the number of nested blocks
-        """
-        # only check block levels inside functions or methods
-        if not isinstance(node.scope(), astroid.FunctionDef):
-            return
-        # messages are triggered on leaving the nested block. Here we save the
-        # stack in case the current node isn't nested in the previous one
-        nested_blocks = self._nested_blocks[:]
-        if node.parent == node.scope():
-            self._nested_blocks = [node]
-        else:
-            # go through ancestors from the most nested to the less
-            for ancestor_node in reversed(self._nested_blocks):
-                if ancestor_node == node.parent:
-                    break
-                self._nested_blocks.pop()
-            # if the node is an elif, this should not be another nesting level
-            if isinstance(node, astroid.If) and self._is_actual_elif(node):
-                if self._nested_blocks:
-                    self._nested_blocks.pop()
-            self._nested_blocks.append(node)
-
-        # send message only once per group of nested blocks
-        if len(nested_blocks) > len(self._nested_blocks):
-            self._emit_nested_blocks_message_if_needed(nested_blocks)
-
-    def _emit_nested_blocks_message_if_needed(self, nested_blocks):
-        if len(nested_blocks) > self.config.max_nested_blocks:
-            self.add_message(
-                "too-many-nested-blocks",
-                node=nested_blocks[0],
-                args=(len(nested_blocks), self.config.max_nested_blocks),
-            )
-
-    @staticmethod
-    def _duplicated_isinstance_types(node):
-        """Get the duplicated types from the underlying isinstance calls.
-
-        :param astroid.BoolOp node: Node which should contain a bunch of isinstance calls.
-        :returns: Dictionary of the comparison objects from the isinstance calls,
-                  to duplicate values from consecutive calls.
-        :rtype: dict
-        """
-        duplicated_objects = set()
-        all_types = collections.defaultdict(set)
-
-        for call in node.values:
-            if not isinstance(call, astroid.Call) or len(call.args) != 2:
-                continue
-
-            inferred = utils.safe_infer(call.func)
-            if not inferred or not utils.is_builtin_object(inferred):
-                continue
-
-            if inferred.name != "isinstance":
-                continue
-
-            isinstance_object = call.args[0].as_string()
-            isinstance_types = call.args[1]
-
-            if isinstance_object in all_types:
-                duplicated_objects.add(isinstance_object)
-
-            if isinstance(isinstance_types, astroid.Tuple):
-                elems = [
-                    class_type.as_string() for class_type in isinstance_types.itered()
-                ]
-            else:
-                elems = [isinstance_types.as_string()]
-            all_types[isinstance_object].update(elems)
-
-        # Remove all keys which not duplicated
-        return {
-            key: value for key, value in all_types.items() if key in duplicated_objects
-        }
-
-    def _check_consider_merging_isinstance(self, node):
-        """Check isinstance calls which can be merged together."""
-        if node.op != "or":
-            return
-
-        first_args = self._duplicated_isinstance_types(node)
-        for duplicated_name, class_names in first_args.items():
-            names = sorted(name for name in class_names)
-            self.add_message(
-                "consider-merging-isinstance",
-                node=node,
-                args=(duplicated_name, ", ".join(names)),
-            )
-
-    def _check_consider_using_in(self, node):
-        allowed_ops = {"or": "==", "and": "!="}
-
-        if node.op not in allowed_ops or len(node.values) < 2:
-            return
-
-        for value in node.values:
-            if (
-                not isinstance(value, astroid.Compare)
-                or len(value.ops) != 1
-                or value.ops[0][0] not in allowed_ops[node.op]
-            ):
-                return
-            for comparable in value.left, value.ops[0][1]:
-                if isinstance(comparable, astroid.Call):
-                    return
-
-        # Gather variables and values from comparisons
-        variables, values = [], []
-        for value in node.values:
-            variable_set = set()
-            for comparable in value.left, value.ops[0][1]:
-                if isinstance(comparable, astroid.Name):
-                    variable_set.add(comparable.as_string())
-                values.append(comparable.as_string())
-            variables.append(variable_set)
-
-        # Look for (common-)variables that occur in all comparisons
-        common_variables = reduce(lambda a, b: a.intersection(b), variables)
-
-        if not common_variables:
-            return
-
-        # Gather information for the suggestion
-        common_variable = sorted(list(common_variables))[0]
-        comprehension = "in" if node.op == "or" else "not in"
-        values = list(collections.OrderedDict.fromkeys(values))
-        values.remove(common_variable)
-        values_string = ", ".join(values) if len(values) != 1 else values[0] + ","
-        suggestion = "%s %s (%s)" % (common_variable, comprehension, values_string)
-
-        self.add_message("consider-using-in", node=node, args=(suggestion,))
-
-    def _check_chained_comparison(self, node):
-        """Check if there is any chained comparison in the expression.
-
-        Add a refactoring message if a boolOp contains comparison like a < b and b < c,
-        which can be chained as a < b < c.
-
-        Care is taken to avoid simplifying a < b < c and b < d.
-        """
-        if node.op != "and" or len(node.values) < 2:
-            return
-
-        def _find_lower_upper_bounds(comparison_node, uses):
-            left_operand = comparison_node.left
-            for operator, right_operand in comparison_node.ops:
-                for operand in (left_operand, right_operand):
-                    value = None
-                    if isinstance(operand, astroid.Name):
-                        value = operand.name
-                    elif isinstance(operand, astroid.Const):
-                        value = operand.value
-
-                    if value is None:
-                        continue
-
-                    if operator in ("<", "<="):
-                        if operand is left_operand:
-                            uses[value]["lower_bound"].add(comparison_node)
-                        elif operand is right_operand:
-                            uses[value]["upper_bound"].add(comparison_node)
-                    elif operator in (">", ">="):
-                        if operand is left_operand:
-                            uses[value]["upper_bound"].add(comparison_node)
-                        elif operand is right_operand:
-                            uses[value]["lower_bound"].add(comparison_node)
-                left_operand = right_operand
-
-        uses = collections.defaultdict(
-            lambda: {"lower_bound": set(), "upper_bound": set()}
-        )
-        for comparison_node in node.values:
-            if isinstance(comparison_node, astroid.Compare):
-                _find_lower_upper_bounds(comparison_node, uses)
-
-        for _, bounds in uses.items():
-            num_shared = len(bounds["lower_bound"].intersection(bounds["upper_bound"]))
-            num_lower_bounds = len(bounds["lower_bound"])
-            num_upper_bounds = len(bounds["upper_bound"])
-            if num_shared < num_lower_bounds and num_shared < num_upper_bounds:
-                self.add_message("chained-comparison", node=node)
-                break
-
-    @utils.check_messages(
-        "consider-merging-isinstance", "consider-using-in", "chained-comparison"
-    )
-    def visit_boolop(self, node):
-        self._check_consider_merging_isinstance(node)
-        self._check_consider_using_in(node)
-        self._check_chained_comparison(node)
-
-    @staticmethod
-    def _is_simple_assignment(node):
-        return (
-            isinstance(node, astroid.Assign)
-            and len(node.targets) == 1
-            and isinstance(node.targets[0], astroid.node_classes.AssignName)
-            and isinstance(node.value, astroid.node_classes.Name)
-        )
-
-    def _check_swap_variables(self, node):
-        if not node.next_sibling() or not node.next_sibling().next_sibling():
-            return
-        assignments = [node, node.next_sibling(), node.next_sibling().next_sibling()]
-        if not all(self._is_simple_assignment(node) for node in assignments):
-            return
-        if any(node in self._reported_swap_nodes for node in assignments):
-            return
-        left = [node.targets[0].name for node in assignments]
-        right = [node.value.name for node in assignments]
-        if left[0] == right[-1] and left[1:] == right[:-1]:
-            self._reported_swap_nodes.update(assignments)
-            message = "consider-swap-variables"
-            self.add_message(message, node=node)
-
-    @utils.check_messages(
-        "simplify-boolean-expression",
-        "consider-using-ternary",
-        "consider-swap-variables",
-    )
-    def visit_assign(self, node):
-        self._check_swap_variables(node)
-        if self._is_and_or_ternary(node.value):
-            cond, truth_value, false_value = self._and_or_ternary_arguments(node.value)
-        else:
-            return
-
-        if all(
-            isinstance(value, astroid.Compare) for value in (truth_value, false_value)
-        ):
-            return
-
-        inferred_truth_value = utils.safe_infer(truth_value)
-        if inferred_truth_value in (None, astroid.Uninferable):
-            truth_boolean_value = True
-        else:
-            truth_boolean_value = truth_value.bool_value()
-
-        if truth_boolean_value is False:
-            message = "simplify-boolean-expression"
-            suggestion = false_value.as_string()
-        else:
-            message = "consider-using-ternary"
-            suggestion = "{truth} if {cond} else {false}".format(
-                truth=truth_value.as_string(),
-                cond=cond.as_string(),
-                false=false_value.as_string(),
-            )
-        self.add_message(message, node=node, args=(suggestion,))
-
-    visit_return = visit_assign
-
-    def _check_consider_using_join(self, aug_assign):
-        """
-        We start with the augmented assignment and work our way upwards.
-        Names of variables for nodes if match successful:
-        result = ''  # assign
-        for number in ['1', '2', '3']  # for_loop
-            result += number  # aug_assign
-        """
-        for_loop = aug_assign.parent
-        if not isinstance(for_loop, astroid.For) or len(for_loop.body) > 1:
-            return
-        assign = for_loop.previous_sibling()
-        if not isinstance(assign, astroid.Assign):
-            return
-        result_assign_names = {
-            target.name
-            for target in assign.targets
-            if isinstance(target, astroid.AssignName)
-        }
-
-        is_concat_loop = (
-            aug_assign.op == "+="
-            and isinstance(aug_assign.target, astroid.AssignName)
-            and len(for_loop.body) == 1
-            and aug_assign.target.name in result_assign_names
-            and isinstance(assign.value, astroid.Const)
-            and isinstance(assign.value.value, str)
-            and isinstance(aug_assign.value, astroid.Name)
-            and aug_assign.value.name == for_loop.target.name
-        )
-        if is_concat_loop:
-            self.add_message("consider-using-join", node=aug_assign)
-
-    @utils.check_messages("consider-using-join")
-    def visit_augassign(self, node):
-        self._check_consider_using_join(node)
-
-    @utils.check_messages("unnecessary-comprehension")
-    def visit_comprehension(self, node):
-        self._check_unnecessary_comprehension(node)
-
-    def _check_unnecessary_comprehension(self, node):
-        if (
-            isinstance(node.parent, astroid.GeneratorExp)
-            or len(node.ifs) != 0
-            or len(node.parent.generators) != 1
-            or node.is_async
-        ):
-            return
-
-        if (
-            isinstance(node.parent, astroid.DictComp)
-            and isinstance(node.parent.key, astroid.Name)
-            and isinstance(node.parent.value, astroid.Name)
-            and isinstance(node.target, astroid.Tuple)
-            and all(isinstance(elt, astroid.AssignName) for elt in node.target.elts)
-        ):
-            expr_list = [node.parent.key.name, node.parent.value.name]
-            target_list = [elt.name for elt in node.target.elts]
-
-        elif isinstance(node.parent, (astroid.ListComp, astroid.SetComp)):
-            expr = node.parent.elt
-            if isinstance(expr, astroid.Name):
-                expr_list = expr.name
-            elif isinstance(expr, astroid.Tuple):
-                if any(not isinstance(elt, astroid.Name) for elt in expr.elts):
-                    return
-                expr_list = [elt.name for elt in expr.elts]
-            else:
-                expr_list = []
-            target = node.parent.generators[0].target
-            target_list = (
-                target.name
-                if isinstance(target, astroid.AssignName)
-                else (
-                    [
-                        elt.name
-                        for elt in target.elts
-                        if isinstance(elt, astroid.AssignName)
-                    ]
-                    if isinstance(target, astroid.Tuple)
-                    else []
-                )
-            )
-        else:
-            return
-        if expr_list == target_list != []:
-            self.add_message("unnecessary-comprehension", node=node)
-
-    @staticmethod
-    def _is_and_or_ternary(node):
-        """
-        Returns true if node is 'condition and true_value or false_value' form.
-
-        All of: condition, true_value and false_value should not be a complex boolean expression
-        """
-        return (
-            isinstance(node, astroid.BoolOp)
-            and node.op == "or"
-            and len(node.values) == 2
-            and isinstance(node.values[0], astroid.BoolOp)
-            and not isinstance(node.values[1], astroid.BoolOp)
-            and node.values[0].op == "and"
-            and not isinstance(node.values[0].values[1], astroid.BoolOp)
-            and len(node.values[0].values) == 2
-        )
-
-    @staticmethod
-    def _and_or_ternary_arguments(node):
-        false_value = node.values[1]
-        condition, true_value = node.values[0].values
-        return condition, true_value, false_value
-
-    def visit_functiondef(self, node):
-        self._return_nodes[node.name] = list(
-            node.nodes_of_class(astroid.Return, skip_klass=astroid.FunctionDef)
-        )
-
-    def _check_consistent_returns(self, node):
-        """Check that all return statements inside a function are consistent.
-
-        Return statements are consistent if:
-            - all returns are explicit and if there is no implicit return;
-            - all returns are empty and if there is, possibly, an implicit return.
-
-        Args:
-            node (astroid.FunctionDef): the function holding the return statements.
-
-        """
-        # explicit return statements are those with a not None value
-        explicit_returns = [
-            _node for _node in self._return_nodes[node.name] if _node.value is not None
-        ]
-        if not explicit_returns:
-            return
-        if len(explicit_returns) == len(
-            self._return_nodes[node.name]
-        ) and self._is_node_return_ended(node):
-            return
-        self.add_message("inconsistent-return-statements", node=node)
-
-    def _is_node_return_ended(self, node):
-        """Check if the node ends with an explicit return statement.
-
-        Args:
-            node (astroid.NodeNG): node to be checked.
-
-        Returns:
-            bool: True if the node ends with an explicit statement, False otherwise.
-
-        """
-        #  Recursion base case
-        if isinstance(node, astroid.Return):
-            return True
-        if isinstance(node, astroid.Call):
-            try:
-                funcdef_node = node.func.inferred()[0]
-                if self._is_function_def_never_returning(funcdef_node):
-                    return True
-            except astroid.InferenceError:
-                pass
-        # Avoid the check inside while loop as we don't know
-        #  if they will be completed
-        if isinstance(node, astroid.While):
-            return True
-        if isinstance(node, astroid.Raise):
-            # a Raise statement doesn't need to end with a return statement
-            # but if the exception raised is handled, then the handler has to
-            # ends with a return statement
-            if not node.exc:
-                # Ignore bare raises
-                return True
-            if not utils.is_node_inside_try_except(node):
-                # If the raise statement is not inside a try/except statement
-                #  then the exception is raised and cannot be caught. No need
-                #  to infer it.
-                return True
-            exc = utils.safe_infer(node.exc)
-            if exc is None or exc is astroid.Uninferable:
-                return False
-            exc_name = exc.pytype().split(".")[-1]
-            handlers = utils.get_exception_handlers(node, exc_name)
-            handlers = list(handlers) if handlers is not None else []
-            if handlers:
-                # among all the handlers handling the exception at least one
-                # must end with a return statement
-                return any(
-                    self._is_node_return_ended(_handler) for _handler in handlers
-                )
-            # if no handlers handle the exception then it's ok
-            return True
-        if isinstance(node, astroid.If):
-            # if statement is returning if there are exactly two return statements in its
-            #  children : one for the body part, the other for the orelse part
-            # Do not check if inner function definition are return ended.
-            is_orelse_returning = any(
-                self._is_node_return_ended(_ore)
-                for _ore in node.orelse
-                if not isinstance(_ore, astroid.FunctionDef)
-            )
-            is_if_returning = any(
-                self._is_node_return_ended(_ifn)
-                for _ifn in node.body
-                if not isinstance(_ifn, astroid.FunctionDef)
-            )
-            return is_if_returning and is_orelse_returning
-        #  recurses on the children of the node except for those which are except handler
-        # because one cannot be sure that the handler will really be used
-        return any(
-            self._is_node_return_ended(_child)
-            for _child in node.get_children()
-            if not isinstance(_child, astroid.ExceptHandler)
-        )
-
-    def _is_function_def_never_returning(self, node):
-        """Return True if the function never returns. False otherwise.
-
-        Args:
-            node (astroid.FunctionDef): function definition node to be analyzed.
-
-        Returns:
-            bool: True if the function never returns, False otherwise.
-        """
-        try:
-            return node.qname() in self._never_returning_functions
-        except TypeError:
-            return False
-
-    def _check_return_at_the_end(self, node):
-        """Check for presence of a *single* return statement at the end of a
-        function. "return" or "return None" are useless because None is the
-        default return type if they are missing.
-
-        NOTE: produces a message only if there is a single return statement
-        in the function body. Otherwise _check_consistent_returns() is called!
-        Per its implementation and PEP8 we can have a "return None" at the end
-        of the function body if there are other return statements before that!
-        """
-        if len(self._return_nodes[node.name]) > 1:
-            return
-        if len(node.body) <= 1:
-            return
-
-        last = node.body[-1]
-        if isinstance(last, astroid.Return):
-            # e.g. "return"
-            if last.value is None:
-                self.add_message("useless-return", node=node)
-            # return None"
-            elif isinstance(last.value, astroid.Const) and (last.value.value is None):
-                self.add_message("useless-return", node=node)
-
-
-class RecommandationChecker(checkers.BaseChecker):
-    __implements__ = (interfaces.IAstroidChecker,)
-    name = "refactoring"
-    msgs = {
-        "C0200": (
-            "Consider using enumerate instead of iterating with range and len",
-            "consider-using-enumerate",
-            "Emitted when code that iterates with range and len is "
-            "encountered. Such code can be simplified by using the "
-            "enumerate builtin.",
-        ),
-        "C0201": (
-            "Consider iterating the dictionary directly instead of calling .keys()",
-            "consider-iterating-dictionary",
-            "Emitted when the keys of a dictionary are iterated through the .keys() "
-            "method. It is enough to just iterate through the dictionary itself, as "
-            'in "for key in dictionary".',
-        ),
-    }
-
-    @staticmethod
-    def _is_builtin(node, function):
-        inferred = utils.safe_infer(node)
-        if not inferred:
-            return False
-        return utils.is_builtin_object(inferred) and inferred.name == function
-
-    @utils.check_messages("consider-iterating-dictionary")
-    def visit_call(self, node):
-        if not isinstance(node.func, astroid.Attribute):
-            return
-        if node.func.attrname != "keys":
-            return
-        if not isinstance(node.parent, (astroid.For, astroid.Comprehension)):
-            return
-
-        inferred = utils.safe_infer(node.func)
-        if not isinstance(inferred, astroid.BoundMethod) or not isinstance(
-            inferred.bound, astroid.Dict
-        ):
-            return
-
-        if isinstance(node.parent, (astroid.For, astroid.Comprehension)):
-            self.add_message("consider-iterating-dictionary", node=node)
-
-    @utils.check_messages("consider-using-enumerate")
-    def visit_for(self, node):
-        """Emit a convention whenever range and len are used for indexing."""
-        # Verify that we have a `range([start], len(...), [stop])` call and
-        # that the object which is iterated is used as a subscript in the
-        # body of the for.
-
-        # Is it a proper range call?
-        if not isinstance(node.iter, astroid.Call):
-            return
-        if not self._is_builtin(node.iter.func, "range"):
-            return
-        if len(node.iter.args) == 2 and not _is_constant_zero(node.iter.args[0]):
-            return
-        if len(node.iter.args) > 2:
-            return
-
-        # Is it a proper len call?
-        if not isinstance(node.iter.args[-1], astroid.Call):
-            return
-        second_func = node.iter.args[-1].func
-        if not self._is_builtin(second_func, "len"):
-            return
-        len_args = node.iter.args[-1].args
-        if not len_args or len(len_args) != 1:
-            return
-        iterating_object = len_args[0]
-        if not isinstance(iterating_object, astroid.Name):
-            return
-        # If we're defining __iter__ on self, enumerate won't work
-        scope = node.scope()
-        if iterating_object.name == "self" and scope.name == "__iter__":
-            return
-
-        # Verify that the body of the for loop uses a subscript
-        # with the object that was iterated. This uses some heuristics
-        # in order to make sure that the same object is used in the
-        # for body.
-        for child in node.body:
-            for subscript in child.nodes_of_class(astroid.Subscript):
-                if not isinstance(subscript.value, astroid.Name):
-                    continue
-                if not isinstance(subscript.slice, astroid.Index):
-                    continue
-                if not isinstance(subscript.slice.value, astroid.Name):
-                    continue
-                if subscript.slice.value.name != node.target.name:
-                    continue
-                if iterating_object.name != subscript.value.name:
-                    continue
-                if subscript.value.scope() != node.scope():
-                    # Ignore this subscript if it's not in the same
-                    # scope. This means that in the body of the for
-                    # loop, another scope was created, where the same
-                    # name for the iterating object was used.
-                    continue
-                self.add_message("consider-using-enumerate", node=node)
-                return
-
-
-class NotChecker(checkers.BaseChecker):
-    """checks for too many not in comparison expressions
-
-    - "not not" should trigger a warning
-    - "not" followed by a comparison should trigger a warning
-    """
-
-    __implements__ = (interfaces.IAstroidChecker,)
-    msgs = {
-        "C0113": (
-            'Consider changing "%s" to "%s"',
-            "unneeded-not",
-            "Used when a boolean expression contains an unneeded negation.",
-        )
-    }
-    name = "refactoring"
-    reverse_op = {
-        "<": ">=",
-        "<=": ">",
-        ">": "<=",
-        ">=": "<",
-        "==": "!=",
-        "!=": "==",
-        "in": "not in",
-        "is": "is not",
-    }
-    # sets are not ordered, so for example "not set(LEFT_VALS) <= set(RIGHT_VALS)" is
-    # not equivalent to "set(LEFT_VALS) > set(RIGHT_VALS)"
-    skipped_nodes = (astroid.Set,)
-    # 'builtins' py3, '__builtin__' py2
-    skipped_classnames = [
-        "%s.%s" % (builtins.__name__, qname) for qname in ("set", "frozenset")
-    ]
-
-    @utils.check_messages("unneeded-not")
-    def visit_unaryop(self, node):
-        if node.op != "not":
-            return
-        operand = node.operand
-
-        if isinstance(operand, astroid.UnaryOp) and operand.op == "not":
-            self.add_message(
-                "unneeded-not",
-                node=node,
-                args=(node.as_string(), operand.operand.as_string()),
-            )
-        elif isinstance(operand, astroid.Compare):
-            left = operand.left
-            # ignore multiple comparisons
-            if len(operand.ops) > 1:
-                return
-            operator, right = operand.ops[0]
-            if operator not in self.reverse_op:
-                return
-            # Ignore __ne__ as function of __eq__
-            frame = node.frame()
-            if frame.name == "__ne__" and operator == "==":
-                return
-            for _type in (utils.node_type(left), utils.node_type(right)):
-                if not _type:
-                    return
-                if isinstance(_type, self.skipped_nodes):
-                    return
-                if (
-                    isinstance(_type, astroid.Instance)
-                    and _type.qname() in self.skipped_classnames
-                ):
-                    return
-            suggestion = "%s %s %s" % (
-                left.as_string(),
-                self.reverse_op[operator],
-                right.as_string(),
-            )
-            self.add_message(
-                "unneeded-not", node=node, args=(node.as_string(), suggestion)
-            )
-
-
-class LenChecker(checkers.BaseChecker):
-    """Checks for incorrect usage of len() inside conditions.
-    Pep8 states:
-    For sequences, (strings, lists, tuples), use the fact that empty sequences are false.
-
-        Yes: if not seq:
-             if seq:
-
-        No: if len(seq):
-            if not len(seq):
-
-    Problems detected:
-    * if len(sequence):
-    * if not len(sequence):
-    * elif len(sequence):
-    * elif not len(sequence):
-    * while len(sequence):
-    * while not len(sequence):
-    * assert len(sequence):
-    * assert not len(sequence):
-    """
-
-    __implements__ = (interfaces.IAstroidChecker,)
-
-    # configuration section name
-    name = "refactoring"
-    msgs = {
-        "C1801": (
-            "Do not use `len(SEQUENCE)` without comparison to determine if a sequence is empty",
-            "len-as-condition",
-            "Used when Pylint detects that len(sequence) is being used "
-            "without explicit comparison inside a condition to determine if a sequence is empty. "
-            "Instead of coercing the length to a boolean, either "
-            "rely on the fact that empty sequences are false or "
-            "compare the length against a scalar.",
-        )
-    }
-
-    priority = -2
-    options = ()
-
-    @utils.check_messages("len-as-condition")
-    def visit_call(self, node):
-        # a len(S) call is used inside a test condition
-        # could be if, while, assert or if expression statement
-        # e.g. `if len(S):`
-        if _is_len_call(node):
-            # the len() call could also be nested together with other
-            # boolean operations, e.g. `if z or len(x):`
-            parent = node.parent
-            while isinstance(parent, astroid.BoolOp):
-                parent = parent.parent
-
-            # we're finally out of any nested boolean operations so check if
-            # this len() call is part of a test condition
-            if not _node_is_test_condition(parent):
-                return
-            if not (node is parent.test or parent.test.parent_of(node)):
-                return
-            self.add_message("len-as-condition", node=node)
-
-    @utils.check_messages("len-as-condition")
-    def visit_unaryop(self, node):
-        """`not len(S)` must become `not S` regardless if the parent block
-        is a test condition or something else (boolean expression)
-        e.g. `if not len(S):`"""
-        if (
-            isinstance(node, astroid.UnaryOp)
-            and node.op == "not"
-            and _is_len_call(node.operand)
-        ):
-            self.add_message("len-as-condition", node=node)
-
-
-def register(linter):
-    """Required method to auto register this checker."""
-    linter.register_checker(RefactoringChecker(linter))
-    linter.register_checker(NotChecker(linter))
-    linter.register_checker(RecommandationChecker(linter))
-    linter.register_checker(LenChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/similar.py b/venv/Lib/site-packages/pylint/checkers/similar.py
deleted file mode 100644
index 019b55f..0000000
--- a/venv/Lib/site-packages/pylint/checkers/similar.py
+++ /dev/null
@@ -1,452 +0,0 @@
-# Copyright (c) 2006, 2008-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012 Ry4an Brase <ry4an-hg@ry4an.org>
-# Copyright (c) 2012 Google, Inc.
-# Copyright (c) 2012 Anthony VEREZ <anthony.verez.external@cassidian.com>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2017 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2017 Mikhail Fesenko <proggga@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-# pylint: disable=redefined-builtin
-"""a similarities / code duplication command line tool and pylint checker
-"""
-
-import sys
-from collections import defaultdict
-from getopt import getopt
-from itertools import groupby
-
-import astroid
-
-from pylint.checkers import BaseChecker, table_lines_from_stats
-from pylint.interfaces import IRawChecker
-from pylint.reporters.ureports.nodes import Table
-from pylint.utils import decoding_stream
-
-
-class Similar:
-    """finds copy-pasted lines of code in a project"""
-
-    def __init__(
-        self,
-        min_lines=4,
-        ignore_comments=False,
-        ignore_docstrings=False,
-        ignore_imports=False,
-    ):
-        self.min_lines = min_lines
-        self.ignore_comments = ignore_comments
-        self.ignore_docstrings = ignore_docstrings
-        self.ignore_imports = ignore_imports
-        self.linesets = []
-
-    def append_stream(self, streamid, stream, encoding=None):
-        """append a file to search for similarities"""
-        if encoding is None:
-            readlines = stream.readlines
-        else:
-            readlines = decoding_stream(stream, encoding).readlines
-        try:
-            self.linesets.append(
-                LineSet(
-                    streamid,
-                    readlines(),
-                    self.ignore_comments,
-                    self.ignore_docstrings,
-                    self.ignore_imports,
-                )
-            )
-        except UnicodeDecodeError:
-            pass
-
-    def run(self):
-        """start looking for similarities and display results on stdout"""
-        self._display_sims(self._compute_sims())
-
-    def _compute_sims(self):
-        """compute similarities in appended files"""
-        no_duplicates = defaultdict(list)
-        for num, lineset1, idx1, lineset2, idx2 in self._iter_sims():
-            duplicate = no_duplicates[num]
-            for couples in duplicate:
-                if (lineset1, idx1) in couples or (lineset2, idx2) in couples:
-                    couples.add((lineset1, idx1))
-                    couples.add((lineset2, idx2))
-                    break
-            else:
-                duplicate.append({(lineset1, idx1), (lineset2, idx2)})
-        sims = []
-        for num, ensembles in no_duplicates.items():
-            for couples in ensembles:
-                sims.append((num, couples))
-        sims.sort()
-        sims.reverse()
-        return sims
-
-    def _display_sims(self, sims):
-        """display computed similarities on stdout"""
-        nb_lignes_dupliquees = 0
-        for num, couples in sims:
-            print()
-            print(num, "similar lines in", len(couples), "files")
-            couples = sorted(couples)
-            lineset = idx = None
-            for lineset, idx in couples:
-                print("==%s:%s" % (lineset.name, idx))
-            if lineset:
-                for line in lineset._real_lines[idx : idx + num]:
-                    print("  ", line.rstrip())
-            nb_lignes_dupliquees += num * (len(couples) - 1)
-        nb_total_lignes = sum([len(lineset) for lineset in self.linesets])
-        print(
-            "TOTAL lines=%s duplicates=%s percent=%.2f"
-            % (
-                nb_total_lignes,
-                nb_lignes_dupliquees,
-                nb_lignes_dupliquees * 100.0 / nb_total_lignes,
-            )
-        )
-
-    def _find_common(self, lineset1, lineset2):
-        """find similarities in the two given linesets"""
-        lines1 = lineset1.enumerate_stripped
-        lines2 = lineset2.enumerate_stripped
-        find = lineset2.find
-        index1 = 0
-        min_lines = self.min_lines
-        while index1 < len(lineset1):
-            skip = 1
-            num = 0
-            for index2 in find(lineset1[index1]):
-                non_blank = 0
-                for num, ((_, line1), (_, line2)) in enumerate(
-                    zip(lines1(index1), lines2(index2))
-                ):
-                    if line1 != line2:
-                        if non_blank > min_lines:
-                            yield num, lineset1, index1, lineset2, index2
-                        skip = max(skip, num)
-                        break
-                    if line1:
-                        non_blank += 1
-                else:
-                    # we may have reach the end
-                    num += 1
-                    if non_blank > min_lines:
-                        yield num, lineset1, index1, lineset2, index2
-                    skip = max(skip, num)
-            index1 += skip
-
-    def _iter_sims(self):
-        """iterate on similarities among all files, by making a cartesian
-        product
-        """
-        for idx, lineset in enumerate(self.linesets[:-1]):
-            for lineset2 in self.linesets[idx + 1 :]:
-                for sim in self._find_common(lineset, lineset2):
-                    yield sim
-
-
-def stripped_lines(lines, ignore_comments, ignore_docstrings, ignore_imports):
-    """return lines with leading/trailing whitespace and any ignored code
-    features removed
-    """
-    if ignore_imports:
-        tree = astroid.parse("".join(lines))
-        node_is_import_by_lineno = (
-            (node.lineno, isinstance(node, (astroid.Import, astroid.ImportFrom)))
-            for node in tree.body
-        )
-        line_begins_import = {
-            lineno: all(is_import for _, is_import in node_is_import_group)
-            for lineno, node_is_import_group in groupby(
-                node_is_import_by_lineno, key=lambda x: x[0]
-            )
-        }
-        current_line_is_import = False
-
-    strippedlines = []
-    docstring = None
-    for lineno, line in enumerate(lines, start=1):
-        line = line.strip()
-        if ignore_docstrings:
-            if not docstring and any(
-                line.startswith(i) for i in ['"""', "'''", 'r"""', "r'''"]
-            ):
-                docstring = line[:3]
-                line = line[3:]
-            if docstring:
-                if line.endswith(docstring):
-                    docstring = None
-                line = ""
-        if ignore_imports:
-            current_line_is_import = line_begins_import.get(
-                lineno, current_line_is_import
-            )
-            if current_line_is_import:
-                line = ""
-        if ignore_comments:
-            line = line.split("#", 1)[0].strip()
-        strippedlines.append(line)
-    return strippedlines
-
-
-class LineSet:
-    """Holds and indexes all the lines of a single source file"""
-
-    def __init__(
-        self,
-        name,
-        lines,
-        ignore_comments=False,
-        ignore_docstrings=False,
-        ignore_imports=False,
-    ):
-        self.name = name
-        self._real_lines = lines
-        self._stripped_lines = stripped_lines(
-            lines, ignore_comments, ignore_docstrings, ignore_imports
-        )
-        self._index = self._mk_index()
-
-    def __str__(self):
-        return "<Lineset for %s>" % self.name
-
-    def __len__(self):
-        return len(self._real_lines)
-
-    def __getitem__(self, index):
-        return self._stripped_lines[index]
-
-    def __lt__(self, other):
-        return self.name < other.name
-
-    def __hash__(self):
-        return id(self)
-
-    def enumerate_stripped(self, start_at=0):
-        """return an iterator on stripped lines, starting from a given index
-        if specified, else 0
-        """
-        idx = start_at
-        if start_at:
-            lines = self._stripped_lines[start_at:]
-        else:
-            lines = self._stripped_lines
-        for line in lines:
-            # if line:
-            yield idx, line
-            idx += 1
-
-    def find(self, stripped_line):
-        """return positions of the given stripped line in this set"""
-        return self._index.get(stripped_line, ())
-
-    def _mk_index(self):
-        """create the index for this set"""
-        index = defaultdict(list)
-        for line_no, line in enumerate(self._stripped_lines):
-            if line:
-                index[line].append(line_no)
-        return index
-
-
-MSGS = {
-    "R0801": (
-        "Similar lines in %s files\n%s",
-        "duplicate-code",
-        "Indicates that a set of similar lines has been detected "
-        "among multiple file. This usually means that the code should "
-        "be refactored to avoid this duplication.",
-    )
-}
-
-
-def report_similarities(sect, stats, old_stats):
-    """make a layout with some stats about duplication"""
-    lines = ["", "now", "previous", "difference"]
-    lines += table_lines_from_stats(
-        stats, old_stats, ("nb_duplicated_lines", "percent_duplicated_lines")
-    )
-    sect.append(Table(children=lines, cols=4, rheaders=1, cheaders=1))
-
-
-# wrapper to get a pylint checker from the similar class
-class SimilarChecker(BaseChecker, Similar):
-    """checks for similarities and duplicated code. This computation may be
-    memory / CPU intensive, so you should disable it if you experiment some
-    problems.
-    """
-
-    __implements__ = (IRawChecker,)
-    # configuration section name
-    name = "similarities"
-    # messages
-    msgs = MSGS
-    # configuration options
-    # for available dict keys/values see the optik parser 'add_option' method
-    options = (
-        (
-            "min-similarity-lines",  # type: ignore
-            {
-                "default": 4,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Minimum lines number of a similarity.",
-            },
-        ),
-        (
-            "ignore-comments",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y or n>",
-                "help": "Ignore comments when computing similarities.",
-            },
-        ),
-        (
-            "ignore-docstrings",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y or n>",
-                "help": "Ignore docstrings when computing similarities.",
-            },
-        ),
-        (
-            "ignore-imports",
-            {
-                "default": False,
-                "type": "yn",
-                "metavar": "<y or n>",
-                "help": "Ignore imports when computing similarities.",
-            },
-        ),
-    )
-    # reports
-    reports = (("RP0801", "Duplication", report_similarities),)  # type: ignore
-
-    def __init__(self, linter=None):
-        BaseChecker.__init__(self, linter)
-        Similar.__init__(
-            self, min_lines=4, ignore_comments=True, ignore_docstrings=True
-        )
-        self.stats = None
-
-    def set_option(self, optname, value, action=None, optdict=None):
-        """method called to set an option (registered in the options list)
-
-        overridden to report options setting to Similar
-        """
-        BaseChecker.set_option(self, optname, value, action, optdict)
-        if optname == "min-similarity-lines":
-            self.min_lines = self.config.min_similarity_lines
-        elif optname == "ignore-comments":
-            self.ignore_comments = self.config.ignore_comments
-        elif optname == "ignore-docstrings":
-            self.ignore_docstrings = self.config.ignore_docstrings
-        elif optname == "ignore-imports":
-            self.ignore_imports = self.config.ignore_imports
-
-    def open(self):
-        """init the checkers: reset linesets and statistics information"""
-        self.linesets = []
-        self.stats = self.linter.add_stats(
-            nb_duplicated_lines=0, percent_duplicated_lines=0
-        )
-
-    def process_module(self, node):
-        """process a module
-
-        the module's content is accessible via the stream object
-
-        stream must implement the readlines method
-        """
-        with node.stream() as stream:
-            self.append_stream(self.linter.current_name, stream, node.file_encoding)
-
-    def close(self):
-        """compute and display similarities on closing (i.e. end of parsing)"""
-        total = sum(len(lineset) for lineset in self.linesets)
-        duplicated = 0
-        stats = self.stats
-        for num, couples in self._compute_sims():
-            msg = []
-            lineset = idx = None
-            for lineset, idx in couples:
-                msg.append("==%s:%s" % (lineset.name, idx))
-            msg.sort()
-
-            if lineset:
-                for line in lineset._real_lines[idx : idx + num]:
-                    msg.append(line.rstrip())
-
-            self.add_message("R0801", args=(len(couples), "\n".join(msg)))
-            duplicated += num * (len(couples) - 1)
-        stats["nb_duplicated_lines"] = duplicated
-        stats["percent_duplicated_lines"] = total and duplicated * 100.0 / total
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(SimilarChecker(linter))
-
-
-def usage(status=0):
-    """display command line usage information"""
-    print("finds copy pasted blocks in a set of files")
-    print()
-    print(
-        "Usage: symilar [-d|--duplicates min_duplicated_lines] \
-[-i|--ignore-comments] [--ignore-docstrings] [--ignore-imports] file1..."
-    )
-    sys.exit(status)
-
-
-def Run(argv=None):
-    """standalone command line access point"""
-    if argv is None:
-        argv = sys.argv[1:]
-
-    s_opts = "hdi"
-    l_opts = (
-        "help",
-        "duplicates=",
-        "ignore-comments",
-        "ignore-imports",
-        "ignore-docstrings",
-    )
-    min_lines = 4
-    ignore_comments = False
-    ignore_docstrings = False
-    ignore_imports = False
-    opts, args = getopt(argv, s_opts, l_opts)
-    for opt, val in opts:
-        if opt in ("-d", "--duplicates"):
-            min_lines = int(val)
-        elif opt in ("-h", "--help"):
-            usage()
-        elif opt in ("-i", "--ignore-comments"):
-            ignore_comments = True
-        elif opt in ("--ignore-docstrings",):
-            ignore_docstrings = True
-        elif opt in ("--ignore-imports",):
-            ignore_imports = True
-    if not args:
-        usage(1)
-    sim = Similar(min_lines, ignore_comments, ignore_docstrings, ignore_imports)
-    for filename in args:
-        with open(filename) as stream:
-            sim.append_stream(filename, stream)
-    sim.run()
-    sys.exit(0)
-
-
-if __name__ == "__main__":
-    Run()
diff --git a/venv/Lib/site-packages/pylint/checkers/spelling.py b/venv/Lib/site-packages/pylint/checkers/spelling.py
deleted file mode 100644
index b1a5334..0000000
--- a/venv/Lib/site-packages/pylint/checkers/spelling.py
+++ /dev/null
@@ -1,411 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2014-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2015 Pavel Roskin <proski@gnu.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016-2017 Pedro Algarvio <pedro@algarvio.me>
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 Mikhail Fesenko <proggga@gmail.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Checker for spelling errors in comments and docstrings.
-"""
-
-import os
-import re
-import tokenize
-
-from pylint.checkers import BaseTokenChecker
-from pylint.checkers.utils import check_messages
-from pylint.interfaces import IAstroidChecker, ITokenChecker
-
-try:
-    import enchant
-    from enchant.tokenize import (  # type: ignore
-        get_tokenizer,
-        Chunker,
-        Filter,
-        EmailFilter,
-        URLFilter,
-        WikiWordFilter,
-    )
-except ImportError:
-    enchant = None
-    # pylint: disable=no-init
-    class Filter:  # type: ignore
-        def _skip(self, word):
-            raise NotImplementedError
-
-    class Chunker:  # type: ignore
-        pass
-
-
-if enchant is not None:
-    br = enchant.Broker()
-    dicts = br.list_dicts()
-    dict_choices = [""] + [d[0] for d in dicts]
-    dicts = ["%s (%s)" % (d[0], d[1].name) for d in dicts]
-    dicts = ", ".join(dicts)
-    instr = ""
-else:
-    dicts = "none"
-    dict_choices = [""]
-    instr = " To make it work, install the python-enchant package."
-
-
-class WordsWithDigigtsFilter(Filter):
-    """Skips words with digits.
-    """
-
-    def _skip(self, word):
-        for char in word:
-            if char.isdigit():
-                return True
-        return False
-
-
-class WordsWithUnderscores(Filter):
-    """Skips words with underscores.
-
-    They are probably function parameter names.
-    """
-
-    def _skip(self, word):
-        return "_" in word
-
-
-class CamelCasedWord(Filter):
-    r"""Filter skipping over camelCasedWords.
-    This filter skips any words matching the following regular expression:
-
-           ^([a-z]\w+[A-Z]+\w+)
-
-    That is, any words that are camelCasedWords.
-    """
-    _pattern = re.compile(r"^([a-z]+([\d]|[A-Z])(?:\w+)?)")
-
-    def _skip(self, word):
-        return bool(self._pattern.match(word))
-
-
-class SphinxDirectives(Filter):
-    r"""Filter skipping over Sphinx Directives.
-    This filter skips any words matching the following regular expression:
-
-           ^:([a-z]+):`([^`]+)(`)?
-
-    That is, for example, :class:`BaseQuery`
-    """
-    # The final ` in the pattern is optional because enchant strips it out
-    _pattern = re.compile(r"^:([a-z]+):`([^`]+)(`)?")
-
-    def _skip(self, word):
-        return bool(self._pattern.match(word))
-
-
-class ForwardSlashChunkder(Chunker):
-    """
-    This chunker allows splitting words like 'before/after' into 'before' and 'after'
-    """
-
-    def next(self):
-        while True:
-            if not self._text:
-                raise StopIteration()
-            if "/" not in self._text:
-                text = self._text
-                self._offset = 0
-                self._text = ""
-                return (text, 0)
-            pre_text, post_text = self._text.split("/", 1)
-            self._text = post_text
-            self._offset = 0
-            if (
-                not pre_text
-                or not post_text
-                or not pre_text[-1].isalpha()
-                or not post_text[0].isalpha()
-            ):
-                self._text = ""
-                self._offset = 0
-                return (pre_text + "/" + post_text, 0)
-            return (pre_text, 0)
-
-    def _next(self):
-        while True:
-            if "/" not in self._text:
-                return (self._text, 0)
-            pre_text, post_text = self._text.split("/", 1)
-            if not pre_text or not post_text:
-                break
-            if not pre_text[-1].isalpha() or not post_text[0].isalpha():
-                raise StopIteration()
-            self._text = pre_text + " " + post_text
-        raise StopIteration()
-
-
-class SpellingChecker(BaseTokenChecker):
-    """Check spelling in comments and docstrings"""
-
-    __implements__ = (ITokenChecker, IAstroidChecker)
-    name = "spelling"
-    msgs = {
-        "C0401": (
-            "Wrong spelling of a word '%s' in a comment:\n%s\n"
-            "%s\nDid you mean: '%s'?",
-            "wrong-spelling-in-comment",
-            "Used when a word in comment is not spelled correctly.",
-        ),
-        "C0402": (
-            "Wrong spelling of a word '%s' in a docstring:\n%s\n"
-            "%s\nDid you mean: '%s'?",
-            "wrong-spelling-in-docstring",
-            "Used when a word in docstring is not spelled correctly.",
-        ),
-        "C0403": (
-            "Invalid characters %r in a docstring",
-            "invalid-characters-in-docstring",
-            "Used when a word in docstring cannot be checked by enchant.",
-        ),
-    }
-    options = (
-        (
-            "spelling-dict",
-            {
-                "default": "",
-                "type": "choice",
-                "metavar": "<dict name>",
-                "choices": dict_choices,
-                "help": "Spelling dictionary name. "
-                "Available dictionaries: %s.%s" % (dicts, instr),
-            },
-        ),
-        (
-            "spelling-ignore-words",
-            {
-                "default": "",
-                "type": "string",
-                "metavar": "<comma separated words>",
-                "help": "List of comma separated words that " "should not be checked.",
-            },
-        ),
-        (
-            "spelling-private-dict-file",
-            {
-                "default": "",
-                "type": "string",
-                "metavar": "<path to file>",
-                "help": "A path to a file that contains the private "
-                "dictionary; one word per line.",
-            },
-        ),
-        (
-            "spelling-store-unknown-words",
-            {
-                "default": "n",
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "Tells whether to store unknown words to the "
-                "private dictionary (see the "
-                "--spelling-private-dict-file option) instead of "
-                "raising a message.",
-            },
-        ),
-        (
-            "max-spelling-suggestions",
-            {
-                "default": 4,
-                "type": "int",
-                "metavar": "N",
-                "help": "Limits count of emitted suggestions for " "spelling mistakes.",
-            },
-        ),
-    )
-
-    def open(self):
-        self.initialized = False
-        self.private_dict_file = None
-
-        if enchant is None:
-            return
-        dict_name = self.config.spelling_dict
-        if not dict_name:
-            return
-
-        self.ignore_list = [
-            w.strip() for w in self.config.spelling_ignore_words.split(",")
-        ]
-        # "param" appears in docstring in param description and
-        # "pylint" appears in comments in pylint pragmas.
-        self.ignore_list.extend(["param", "pylint"])
-
-        # Expand tilde to allow e.g. spelling-private-dict-file = ~/.pylintdict
-        if self.config.spelling_private_dict_file:
-            self.config.spelling_private_dict_file = os.path.expanduser(
-                self.config.spelling_private_dict_file
-            )
-
-        if self.config.spelling_private_dict_file:
-            self.spelling_dict = enchant.DictWithPWL(
-                dict_name, self.config.spelling_private_dict_file
-            )
-            self.private_dict_file = open(self.config.spelling_private_dict_file, "a")
-        else:
-            self.spelling_dict = enchant.Dict(dict_name)
-
-        if self.config.spelling_store_unknown_words:
-            self.unknown_words = set()
-
-        self.tokenizer = get_tokenizer(
-            dict_name,
-            chunkers=[ForwardSlashChunkder],
-            filters=[
-                EmailFilter,
-                URLFilter,
-                WikiWordFilter,
-                WordsWithDigigtsFilter,
-                WordsWithUnderscores,
-                CamelCasedWord,
-                SphinxDirectives,
-            ],
-        )
-        self.initialized = True
-
-    def close(self):
-        if self.private_dict_file:
-            self.private_dict_file.close()
-
-    def _check_spelling(self, msgid, line, line_num):
-        original_line = line
-        try:
-            initial_space = re.search(r"^[^\S]\s*", line).regs[0][1]
-        except (IndexError, AttributeError):
-            initial_space = 0
-        if line.strip().startswith("#"):
-            line = line.strip()[1:]
-            starts_with_comment = True
-        else:
-            starts_with_comment = False
-        for word, word_start_at in self.tokenizer(line.strip()):
-            word_start_at += initial_space
-            lower_cased_word = word.casefold()
-
-            # Skip words from ignore list.
-            if word in self.ignore_list or lower_cased_word in self.ignore_list:
-                continue
-
-            # Strip starting u' from unicode literals and r' from raw strings.
-            if word.startswith(("u'", 'u"', "r'", 'r"')) and len(word) > 2:
-                word = word[2:]
-                lower_cased_word = lower_cased_word[2:]
-
-            # If it is a known word, then continue.
-            try:
-                if self.spelling_dict.check(lower_cased_word):
-                    # The lower cased version of word passed spell checking
-                    continue
-
-                # If we reached this far, it means there was a spelling mistake.
-                # Let's retry with the original work because 'unicode' is a
-                # spelling mistake but 'Unicode' is not
-                if self.spelling_dict.check(word):
-                    continue
-            except enchant.errors.Error:
-                self.add_message(
-                    "invalid-characters-in-docstring", line=line_num, args=(word,)
-                )
-                continue
-
-            # Store word to private dict or raise a message.
-            if self.config.spelling_store_unknown_words:
-                if lower_cased_word not in self.unknown_words:
-                    self.private_dict_file.write("%s\n" % lower_cased_word)
-                    self.unknown_words.add(lower_cased_word)
-            else:
-                # Present up to N suggestions.
-                suggestions = self.spelling_dict.suggest(word)
-                del suggestions[self.config.max_spelling_suggestions :]
-
-                line_segment = line[word_start_at:]
-                match = re.search(r"(\W|^)(%s)(\W|$)" % word, line_segment)
-                if match:
-                    # Start position of second group in regex.
-                    col = match.regs[2][0]
-                else:
-                    col = line_segment.index(word)
-
-                col += word_start_at
-
-                if starts_with_comment:
-                    col += 1
-                indicator = (" " * col) + ("^" * len(word))
-
-                self.add_message(
-                    msgid,
-                    line=line_num,
-                    args=(
-                        word,
-                        original_line,
-                        indicator,
-                        "'{}'".format("' or '".join(suggestions)),
-                    ),
-                )
-
-    def process_tokens(self, tokens):
-        if not self.initialized:
-            return
-
-        # Process tokens and look for comments.
-        for (tok_type, token, (start_row, _), _, _) in tokens:
-            if tok_type == tokenize.COMMENT:
-                if start_row == 1 and token.startswith("#!/"):
-                    # Skip shebang lines
-                    continue
-                if token.startswith("# pylint:"):
-                    # Skip pylint enable/disable comments
-                    continue
-                self._check_spelling("wrong-spelling-in-comment", token, start_row)
-
-    @check_messages("wrong-spelling-in-docstring")
-    def visit_module(self, node):
-        if not self.initialized:
-            return
-        self._check_docstring(node)
-
-    @check_messages("wrong-spelling-in-docstring")
-    def visit_classdef(self, node):
-        if not self.initialized:
-            return
-        self._check_docstring(node)
-
-    @check_messages("wrong-spelling-in-docstring")
-    def visit_functiondef(self, node):
-        if not self.initialized:
-            return
-        self._check_docstring(node)
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    def _check_docstring(self, node):
-        """check the node has any spelling errors"""
-        docstring = node.doc
-        if not docstring:
-            return
-
-        start_line = node.lineno + 1
-
-        # Go through lines of docstring
-        for idx, line in enumerate(docstring.splitlines()):
-            self._check_spelling("wrong-spelling-in-docstring", line, start_line + idx)
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(SpellingChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/stdlib.py b/venv/Lib/site-packages/pylint/checkers/stdlib.py
deleted file mode 100644
index a945107..0000000
--- a/venv/Lib/site-packages/pylint/checkers/stdlib.py
+++ /dev/null
@@ -1,452 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Cosmin Poieana <cmin@ropython.org>
-# Copyright (c) 2014 Vlad Temian <vladtemian@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Cezar <celnazli@bitdefender.com>
-# Copyright (c) 2015 Chris Rebert <code@rebertia.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Jared Garst <cultofjared@gmail.com>
-# Copyright (c) 2017 Renat Galimov <renat2017@gmail.com>
-# Copyright (c) 2017 Martin <MartinBasti@users.noreply.github.com>
-# Copyright (c) 2017 Christopher Zurcher <zurcher@users.noreply.github.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 Banjamin Freeman <befreeman@users.noreply.github.com>
-# Copyright (c) 2018 Ioana Tagirta <ioana.tagirta@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Checkers for various standard library functions."""
-
-import sys
-
-import astroid
-from astroid.bases import Instance
-from astroid.node_classes import Const
-
-from pylint.checkers import BaseChecker, utils
-from pylint.interfaces import IAstroidChecker
-
-OPEN_FILES = {"open", "file"}
-UNITTEST_CASE = "unittest.case"
-THREADING_THREAD = "threading.Thread"
-COPY_COPY = "copy.copy"
-OS_ENVIRON = "os._Environ"
-ENV_GETTERS = {"os.getenv"}
-SUBPROCESS_POPEN = "subprocess.Popen"
-SUBPROCESS_RUN = "subprocess.run"
-OPEN_MODULE = "_io"
-
-
-def _check_mode_str(mode):
-    # check type
-    if not isinstance(mode, str):
-        return False
-    # check syntax
-    modes = set(mode)
-    _mode = "rwatb+Ux"
-    creating = "x" in modes
-    if modes - set(_mode) or len(mode) > len(modes):
-        return False
-    # check logic
-    reading = "r" in modes
-    writing = "w" in modes
-    appending = "a" in modes
-    text = "t" in modes
-    binary = "b" in modes
-    if "U" in modes:
-        if writing or appending or creating:
-            return False
-        reading = True
-    if text and binary:
-        return False
-    total = reading + writing + appending + creating
-    if total > 1:
-        return False
-    if not (reading or writing or appending or creating):
-        return False
-    return True
-
-
-class StdlibChecker(BaseChecker):
-    __implements__ = (IAstroidChecker,)
-    name = "stdlib"
-
-    msgs = {
-        "W1501": (
-            '"%s" is not a valid mode for open.',
-            "bad-open-mode",
-            "Python supports: r, w, a[, x] modes with b, +, "
-            "and U (only with r) options. "
-            "See http://docs.python.org/2/library/functions.html#open",
-        ),
-        "W1502": (
-            "Using datetime.time in a boolean context.",
-            "boolean-datetime",
-            "Using datetime.time in a boolean context can hide "
-            "subtle bugs when the time they represent matches "
-            "midnight UTC. This behaviour was fixed in Python 3.5. "
-            "See http://bugs.python.org/issue13936 for reference.",
-            {"maxversion": (3, 5)},
-        ),
-        "W1503": (
-            "Redundant use of %s with constant value %r",
-            "redundant-unittest-assert",
-            "The first argument of assertTrue and assertFalse is "
-            "a condition. If a constant is passed as parameter, that "
-            "condition will be always true. In this case a warning "
-            "should be emitted.",
-        ),
-        "W1505": (
-            "Using deprecated method %s()",
-            "deprecated-method",
-            "The method is marked as deprecated and will be removed in "
-            "a future version of Python. Consider looking for an "
-            "alternative in the documentation.",
-        ),
-        "W1506": (
-            "threading.Thread needs the target function",
-            "bad-thread-instantiation",
-            "The warning is emitted when a threading.Thread class "
-            "is instantiated without the target function being passed. "
-            "By default, the first parameter is the group param, not the target param. ",
-        ),
-        "W1507": (
-            "Using copy.copy(os.environ). Use os.environ.copy() instead. ",
-            "shallow-copy-environ",
-            "os.environ is not a dict object but proxy object, so "
-            "shallow copy has still effects on original object. "
-            "See https://bugs.python.org/issue15373 for reference. ",
-        ),
-        "E1507": (
-            "%s does not support %s type argument",
-            "invalid-envvar-value",
-            "Env manipulation functions support only string type arguments. "
-            "See https://docs.python.org/3/library/os.html#os.getenv. ",
-        ),
-        "W1508": (
-            "%s default type is %s. Expected str or None.",
-            "invalid-envvar-default",
-            "Env manipulation functions return None or str values. "
-            "Supplying anything different as a default may cause bugs. "
-            "See https://docs.python.org/3/library/os.html#os.getenv. ",
-        ),
-        "W1509": (
-            "Using preexec_fn keyword which may be unsafe in the presence "
-            "of threads",
-            "subprocess-popen-preexec-fn",
-            "The preexec_fn parameter is not safe to use in the presence "
-            "of threads in your application. The child process could "
-            "deadlock before exec is called. If you must use it, keep it "
-            "trivial! Minimize the number of libraries you call into."
-            "https://docs.python.org/3/library/subprocess.html#popen-constructor",
-        ),
-        "W1510": (
-            "Using subprocess.run without explicitly set `check` is not recommended.",
-            "subprocess-run-check",
-            "The check parameter should always be used with explicitly set "
-            "`check` keyword to make clear what the error-handling behavior is."
-            "https://docs.python.org/3/library/subprocess.html#subprocess.runs",
-        ),
-    }
-
-    deprecated = {
-        0: {
-            "cgi.parse_qs",
-            "cgi.parse_qsl",
-            "ctypes.c_buffer",
-            "distutils.command.register.register.check_metadata",
-            "distutils.command.sdist.sdist.check_metadata",
-            "tkinter.Misc.tk_menuBar",
-            "tkinter.Menu.tk_bindForTraversal",
-        },
-        2: {
-            (2, 6, 0): {
-                "commands.getstatus",
-                "os.popen2",
-                "os.popen3",
-                "os.popen4",
-                "macostools.touched",
-            },
-            (2, 7, 0): {
-                "unittest.case.TestCase.assertEquals",
-                "unittest.case.TestCase.assertNotEquals",
-                "unittest.case.TestCase.assertAlmostEquals",
-                "unittest.case.TestCase.assertNotAlmostEquals",
-                "unittest.case.TestCase.assert_",
-                "xml.etree.ElementTree.Element.getchildren",
-                "xml.etree.ElementTree.Element.getiterator",
-                "xml.etree.ElementTree.XMLParser.getiterator",
-                "xml.etree.ElementTree.XMLParser.doctype",
-            },
-        },
-        3: {
-            (3, 0, 0): {
-                "inspect.getargspec",
-                "failUnlessEqual",
-                "assertEquals",
-                "failIfEqual",
-                "assertNotEquals",
-                "failUnlessAlmostEqual",
-                "assertAlmostEquals",
-                "failIfAlmostEqual",
-                "assertNotAlmostEquals",
-                "failUnless",
-                "assert_",
-                "failUnlessRaises",
-                "failIf",
-                "assertRaisesRegexp",
-                "assertRegexpMatches",
-                "assertNotRegexpMatches",
-            },
-            (3, 1, 0): {
-                "base64.encodestring",
-                "base64.decodestring",
-                "ntpath.splitunc",
-            },
-            (3, 2, 0): {
-                "cgi.escape",
-                "configparser.RawConfigParser.readfp",
-                "xml.etree.ElementTree.Element.getchildren",
-                "xml.etree.ElementTree.Element.getiterator",
-                "xml.etree.ElementTree.XMLParser.getiterator",
-                "xml.etree.ElementTree.XMLParser.doctype",
-            },
-            (3, 3, 0): {
-                "inspect.getmoduleinfo",
-                "logging.warn",
-                "logging.Logger.warn",
-                "logging.LoggerAdapter.warn",
-                "nntplib._NNTPBase.xpath",
-                "platform.popen",
-            },
-            (3, 4, 0): {
-                "importlib.find_loader",
-                "plistlib.readPlist",
-                "plistlib.writePlist",
-                "plistlib.readPlistFromBytes",
-                "plistlib.writePlistToBytes",
-            },
-            (3, 4, 4): {"asyncio.tasks.async"},
-            (3, 5, 0): {
-                "fractions.gcd",
-                "inspect.getargvalues",
-                "inspect.formatargspec",
-                "inspect.formatargvalues",
-                "inspect.getcallargs",
-                "platform.linux_distribution",
-                "platform.dist",
-            },
-            (3, 6, 0): {"importlib._bootstrap_external.FileLoader.load_module"},
-        },
-    }
-
-    def _check_bad_thread_instantiation(self, node):
-        if not node.kwargs and not node.keywords and len(node.args) <= 1:
-            self.add_message("bad-thread-instantiation", node=node)
-
-    def _check_for_preexec_fn_in_popen(self, node):
-        if node.keywords:
-            for keyword in node.keywords:
-                if keyword.arg == "preexec_fn":
-                    self.add_message("subprocess-popen-preexec-fn", node=node)
-
-    def _check_for_check_kw_in_run(self, node):
-        kwargs = {keyword.arg for keyword in (node.keywords or ())}
-        if "check" not in kwargs:
-            self.add_message("subprocess-run-check", node=node)
-
-    def _check_shallow_copy_environ(self, node):
-        arg = utils.get_argument_from_call(node, position=0)
-        for inferred in arg.inferred():
-            if inferred.qname() == OS_ENVIRON:
-                self.add_message("shallow-copy-environ", node=node)
-                break
-
-    @utils.check_messages(
-        "bad-open-mode",
-        "redundant-unittest-assert",
-        "deprecated-method",
-        "bad-thread-instantiation",
-        "shallow-copy-environ",
-        "invalid-envvar-value",
-        "invalid-envvar-default",
-        "subprocess-popen-preexec-fn",
-        "subprocess-run-check",
-    )
-    def visit_call(self, node):
-        """Visit a Call node."""
-        try:
-            for inferred in node.func.infer():
-                if inferred is astroid.Uninferable:
-                    continue
-                if inferred.root().name == OPEN_MODULE:
-                    if getattr(node.func, "name", None) in OPEN_FILES:
-                        self._check_open_mode(node)
-                elif inferred.root().name == UNITTEST_CASE:
-                    self._check_redundant_assert(node, inferred)
-                elif isinstance(inferred, astroid.ClassDef):
-                    if inferred.qname() == THREADING_THREAD:
-                        self._check_bad_thread_instantiation(node)
-                    elif inferred.qname() == SUBPROCESS_POPEN:
-                        self._check_for_preexec_fn_in_popen(node)
-                elif isinstance(inferred, astroid.FunctionDef):
-                    name = inferred.qname()
-                    if name == COPY_COPY:
-                        self._check_shallow_copy_environ(node)
-                    elif name in ENV_GETTERS:
-                        self._check_env_function(node, inferred)
-                    elif name == SUBPROCESS_RUN:
-                        self._check_for_check_kw_in_run(node)
-                self._check_deprecated_method(node, inferred)
-        except astroid.InferenceError:
-            return
-
-    @utils.check_messages("boolean-datetime")
-    def visit_unaryop(self, node):
-        if node.op == "not":
-            self._check_datetime(node.operand)
-
-    @utils.check_messages("boolean-datetime")
-    def visit_if(self, node):
-        self._check_datetime(node.test)
-
-    @utils.check_messages("boolean-datetime")
-    def visit_ifexp(self, node):
-        self._check_datetime(node.test)
-
-    @utils.check_messages("boolean-datetime")
-    def visit_boolop(self, node):
-        for value in node.values:
-            self._check_datetime(value)
-
-    def _check_deprecated_method(self, node, inferred):
-        py_vers = sys.version_info[0]
-
-        if isinstance(node.func, astroid.Attribute):
-            func_name = node.func.attrname
-        elif isinstance(node.func, astroid.Name):
-            func_name = node.func.name
-        else:
-            # Not interested in other nodes.
-            return
-
-        # Reject nodes which aren't of interest to us.
-        acceptable_nodes = (
-            astroid.BoundMethod,
-            astroid.UnboundMethod,
-            astroid.FunctionDef,
-        )
-        if not isinstance(inferred, acceptable_nodes):
-            return
-
-        qname = inferred.qname()
-        if any(name in self.deprecated[0] for name in (qname, func_name)):
-            self.add_message("deprecated-method", node=node, args=(func_name,))
-        else:
-            for since_vers, func_list in self.deprecated[py_vers].items():
-                if since_vers <= sys.version_info and any(
-                    name in func_list for name in (qname, func_name)
-                ):
-                    self.add_message("deprecated-method", node=node, args=(func_name,))
-                    break
-
-    def _check_redundant_assert(self, node, infer):
-        if (
-            isinstance(infer, astroid.BoundMethod)
-            and node.args
-            and isinstance(node.args[0], astroid.Const)
-            and infer.name in ["assertTrue", "assertFalse"]
-        ):
-            self.add_message(
-                "redundant-unittest-assert",
-                args=(infer.name, node.args[0].value),
-                node=node,
-            )
-
-    def _check_datetime(self, node):
-        """ Check that a datetime was inferred.
-        If so, emit boolean-datetime warning.
-        """
-        try:
-            inferred = next(node.infer())
-        except astroid.InferenceError:
-            return
-        if isinstance(inferred, Instance) and inferred.qname() == "datetime.time":
-            self.add_message("boolean-datetime", node=node)
-
-    def _check_open_mode(self, node):
-        """Check that the mode argument of an open or file call is valid."""
-        try:
-            mode_arg = utils.get_argument_from_call(node, position=1, keyword="mode")
-        except utils.NoSuchArgumentError:
-            return
-        if mode_arg:
-            mode_arg = utils.safe_infer(mode_arg)
-            if isinstance(mode_arg, astroid.Const) and not _check_mode_str(
-                mode_arg.value
-            ):
-                self.add_message("bad-open-mode", node=node, args=mode_arg.value)
-
-    def _check_env_function(self, node, infer):
-        env_name_kwarg = "key"
-        env_value_kwarg = "default"
-        if node.keywords:
-            kwargs = {keyword.arg: keyword.value for keyword in node.keywords}
-        else:
-            kwargs = None
-        if node.args:
-            env_name_arg = node.args[0]
-        elif kwargs and env_name_kwarg in kwargs:
-            env_name_arg = kwargs[env_name_kwarg]
-        else:
-            env_name_arg = None
-
-        if env_name_arg:
-            self._check_invalid_envvar_value(
-                node=node,
-                message="invalid-envvar-value",
-                call_arg=utils.safe_infer(env_name_arg),
-                infer=infer,
-                allow_none=False,
-            )
-
-        if len(node.args) == 2:
-            env_value_arg = node.args[1]
-        elif kwargs and env_value_kwarg in kwargs:
-            env_value_arg = kwargs[env_value_kwarg]
-        else:
-            env_value_arg = None
-
-        if env_value_arg:
-            self._check_invalid_envvar_value(
-                node=node,
-                infer=infer,
-                message="invalid-envvar-default",
-                call_arg=utils.safe_infer(env_value_arg),
-                allow_none=True,
-            )
-
-    def _check_invalid_envvar_value(self, node, infer, message, call_arg, allow_none):
-        if call_arg in (astroid.Uninferable, None):
-            return
-
-        name = infer.qname()
-        if isinstance(call_arg, Const):
-            emit = False
-            if call_arg.value is None:
-                emit = not allow_none
-            elif not isinstance(call_arg.value, str):
-                emit = True
-            if emit:
-                self.add_message(message, node=node, args=(name, call_arg.pytype()))
-        else:
-            self.add_message(message, node=node, args=(name, call_arg.pytype()))
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(StdlibChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/strings.py b/venv/Lib/site-packages/pylint/checkers/strings.py
deleted file mode 100644
index 9470f46..0000000
--- a/venv/Lib/site-packages/pylint/checkers/strings.py
+++ /dev/null
@@ -1,755 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2009 Charles Hebert <charles.hebert@logilab.fr>
-# Copyright (c) 2010-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Rene Zhang <rz99@cornell.edu>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016, 2018 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016 Peter Dawyndt <Peter.Dawyndt@UGent.be>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Checker for string formatting operations.
-"""
-
-import builtins
-import numbers
-import tokenize
-from collections import Counter
-
-import astroid
-from astroid.arguments import CallSite
-from astroid.node_classes import Const
-
-from pylint.checkers import BaseChecker, BaseTokenChecker, utils
-from pylint.checkers.utils import check_messages
-from pylint.interfaces import IAstroidChecker, IRawChecker, ITokenChecker
-
-_AST_NODE_STR_TYPES = ("__builtin__.unicode", "__builtin__.str", "builtins.str")
-
-MSGS = {
-    "E1300": (
-        "Unsupported format character %r (%#02x) at index %d",
-        "bad-format-character",
-        "Used when an unsupported format character is used in a format string.",
-    ),
-    "E1301": (
-        "Format string ends in middle of conversion specifier",
-        "truncated-format-string",
-        "Used when a format string terminates before the end of a "
-        "conversion specifier.",
-    ),
-    "E1302": (
-        "Mixing named and unnamed conversion specifiers in format string",
-        "mixed-format-string",
-        "Used when a format string contains both named (e.g. '%(foo)d') "
-        "and unnamed (e.g. '%d') conversion specifiers.  This is also "
-        "used when a named conversion specifier contains * for the "
-        "minimum field width and/or precision.",
-    ),
-    "E1303": (
-        "Expected mapping for format string, not %s",
-        "format-needs-mapping",
-        "Used when a format string that uses named conversion specifiers "
-        "is used with an argument that is not a mapping.",
-    ),
-    "W1300": (
-        "Format string dictionary key should be a string, not %s",
-        "bad-format-string-key",
-        "Used when a format string that uses named conversion specifiers "
-        "is used with a dictionary whose keys are not all strings.",
-    ),
-    "W1301": (
-        "Unused key %r in format string dictionary",
-        "unused-format-string-key",
-        "Used when a format string that uses named conversion specifiers "
-        "is used with a dictionary that contains keys not required by the "
-        "format string.",
-    ),
-    "E1304": (
-        "Missing key %r in format string dictionary",
-        "missing-format-string-key",
-        "Used when a format string that uses named conversion specifiers "
-        "is used with a dictionary that doesn't contain all the keys "
-        "required by the format string.",
-    ),
-    "E1305": (
-        "Too many arguments for format string",
-        "too-many-format-args",
-        "Used when a format string that uses unnamed conversion "
-        "specifiers is given too many arguments.",
-    ),
-    "E1306": (
-        "Not enough arguments for format string",
-        "too-few-format-args",
-        "Used when a format string that uses unnamed conversion "
-        "specifiers is given too few arguments",
-    ),
-    "E1307": (
-        "Argument %r does not match format type %r",
-        "bad-string-format-type",
-        "Used when a type required by format string "
-        "is not suitable for actual argument type",
-    ),
-    "E1310": (
-        "Suspicious argument in %s.%s call",
-        "bad-str-strip-call",
-        "The argument to a str.{l,r,}strip call contains a duplicate character, ",
-    ),
-    "W1302": (
-        "Invalid format string",
-        "bad-format-string",
-        "Used when a PEP 3101 format string is invalid.",
-    ),
-    "W1303": (
-        "Missing keyword argument %r for format string",
-        "missing-format-argument-key",
-        "Used when a PEP 3101 format string that uses named fields "
-        "doesn't receive one or more required keywords.",
-    ),
-    "W1304": (
-        "Unused format argument %r",
-        "unused-format-string-argument",
-        "Used when a PEP 3101 format string that uses named "
-        "fields is used with an argument that "
-        "is not required by the format string.",
-    ),
-    "W1305": (
-        "Format string contains both automatic field numbering "
-        "and manual field specification",
-        "format-combined-specification",
-        "Used when a PEP 3101 format string contains both automatic "
-        "field numbering (e.g. '{}') and manual field "
-        "specification (e.g. '{0}').",
-    ),
-    "W1306": (
-        "Missing format attribute %r in format specifier %r",
-        "missing-format-attribute",
-        "Used when a PEP 3101 format string uses an "
-        "attribute specifier ({0.length}), but the argument "
-        "passed for formatting doesn't have that attribute.",
-    ),
-    "W1307": (
-        "Using invalid lookup key %r in format specifier %r",
-        "invalid-format-index",
-        "Used when a PEP 3101 format string uses a lookup specifier "
-        "({a[1]}), but the argument passed for formatting "
-        "doesn't contain or doesn't have that key as an attribute.",
-    ),
-    "W1308": (
-        "Duplicate string formatting argument %r, consider passing as named argument",
-        "duplicate-string-formatting-argument",
-        "Used when we detect that a string formatting is "
-        "repeating an argument instead of using named string arguments",
-    ),
-}
-
-OTHER_NODES = (
-    astroid.Const,
-    astroid.List,
-    astroid.Lambda,
-    astroid.FunctionDef,
-    astroid.ListComp,
-    astroid.SetComp,
-    astroid.GeneratorExp,
-)
-
-BUILTINS_STR = builtins.__name__ + ".str"
-BUILTINS_FLOAT = builtins.__name__ + ".float"
-BUILTINS_INT = builtins.__name__ + ".int"
-
-
-def get_access_path(key, parts):
-    """ Given a list of format specifiers, returns
-    the final access path (e.g. a.b.c[0][1]).
-    """
-    path = []
-    for is_attribute, specifier in parts:
-        if is_attribute:
-            path.append(".{}".format(specifier))
-        else:
-            path.append("[{!r}]".format(specifier))
-    return str(key) + "".join(path)
-
-
-def arg_matches_format_type(arg_type, format_type):
-    if format_type in "sr":
-        # All types can be printed with %s and %r
-        return True
-    if isinstance(arg_type, astroid.Instance):
-        arg_type = arg_type.pytype()
-        if arg_type == BUILTINS_STR:
-            return format_type == "c"
-        if arg_type == BUILTINS_FLOAT:
-            return format_type in "deEfFgGn%"
-        if arg_type == BUILTINS_INT:
-            # Integers allow all types
-            return True
-        return False
-    return True
-
-
-class StringFormatChecker(BaseChecker):
-    """Checks string formatting operations to ensure that the format string
-    is valid and the arguments match the format string.
-    """
-
-    __implements__ = (IAstroidChecker,)
-    name = "string"
-    msgs = MSGS
-
-    # pylint: disable=too-many-branches
-    @check_messages(*MSGS)
-    def visit_binop(self, node):
-        if node.op != "%":
-            return
-        left = node.left
-        args = node.right
-
-        if not (isinstance(left, astroid.Const) and isinstance(left.value, str)):
-            return
-        format_string = left.value
-        try:
-            required_keys, required_num_args, required_key_types, required_arg_types = utils.parse_format_string(
-                format_string
-            )
-        except utils.UnsupportedFormatCharacter as exc:
-            formatted = format_string[exc.index]
-            self.add_message(
-                "bad-format-character",
-                node=node,
-                args=(formatted, ord(formatted), exc.index),
-            )
-            return
-        except utils.IncompleteFormatString:
-            self.add_message("truncated-format-string", node=node)
-            return
-        if required_keys and required_num_args:
-            # The format string uses both named and unnamed format
-            # specifiers.
-            self.add_message("mixed-format-string", node=node)
-        elif required_keys:
-            # The format string uses only named format specifiers.
-            # Check that the RHS of the % operator is a mapping object
-            # that contains precisely the set of keys required by the
-            # format string.
-            if isinstance(args, astroid.Dict):
-                keys = set()
-                unknown_keys = False
-                for k, _ in args.items:
-                    if isinstance(k, astroid.Const):
-                        key = k.value
-                        if isinstance(key, str):
-                            keys.add(key)
-                        else:
-                            self.add_message(
-                                "bad-format-string-key", node=node, args=key
-                            )
-                    else:
-                        # One of the keys was something other than a
-                        # constant.  Since we can't tell what it is,
-                        # suppress checks for missing keys in the
-                        # dictionary.
-                        unknown_keys = True
-                if not unknown_keys:
-                    for key in required_keys:
-                        if key not in keys:
-                            self.add_message(
-                                "missing-format-string-key", node=node, args=key
-                            )
-                for key in keys:
-                    if key not in required_keys:
-                        self.add_message(
-                            "unused-format-string-key", node=node, args=key
-                        )
-                for key, arg in args.items:
-                    if not isinstance(key, astroid.Const):
-                        continue
-                    format_type = required_key_types.get(key.value, None)
-                    arg_type = utils.safe_infer(arg)
-                    if (
-                        format_type is not None
-                        and arg_type not in (None, astroid.Uninferable)
-                        and not arg_matches_format_type(arg_type, format_type)
-                    ):
-                        self.add_message(
-                            "bad-string-format-type",
-                            node=node,
-                            args=(arg_type.pytype(), format_type),
-                        )
-            elif isinstance(args, (OTHER_NODES, astroid.Tuple)):
-                type_name = type(args).__name__
-                self.add_message("format-needs-mapping", node=node, args=type_name)
-            # else:
-            # The RHS of the format specifier is a name or
-            # expression.  It may be a mapping object, so
-            # there's nothing we can check.
-        else:
-            # The format string uses only unnamed format specifiers.
-            # Check that the number of arguments passed to the RHS of
-            # the % operator matches the number required by the format
-            # string.
-            args_elts = ()
-            if isinstance(args, astroid.Tuple):
-                rhs_tuple = utils.safe_infer(args)
-                num_args = None
-                if hasattr(rhs_tuple, "elts"):
-                    args_elts = rhs_tuple.elts
-                    num_args = len(args_elts)
-            elif isinstance(args, (OTHER_NODES, (astroid.Dict, astroid.DictComp))):
-                args_elts = [args]
-                num_args = 1
-            else:
-                # The RHS of the format specifier is a name or
-                # expression.  It could be a tuple of unknown size, so
-                # there's nothing we can check.
-                num_args = None
-            if num_args is not None:
-                if num_args > required_num_args:
-                    self.add_message("too-many-format-args", node=node)
-                elif num_args < required_num_args:
-                    self.add_message("too-few-format-args", node=node)
-                for arg, format_type in zip(args_elts, required_arg_types):
-                    if not arg:
-                        continue
-                    arg_type = utils.safe_infer(arg)
-                    if arg_type not in (
-                        None,
-                        astroid.Uninferable,
-                    ) and not arg_matches_format_type(arg_type, format_type):
-                        self.add_message(
-                            "bad-string-format-type",
-                            node=node,
-                            args=(arg_type.pytype(), format_type),
-                        )
-
-    @check_messages(*MSGS)
-    def visit_call(self, node):
-        func = utils.safe_infer(node.func)
-        if (
-            isinstance(func, astroid.BoundMethod)
-            and isinstance(func.bound, astroid.Instance)
-            and func.bound.name in ("str", "unicode", "bytes")
-        ):
-            if func.name in ("strip", "lstrip", "rstrip") and node.args:
-                arg = utils.safe_infer(node.args[0])
-                if not isinstance(arg, astroid.Const) or not isinstance(arg.value, str):
-                    return
-                if len(arg.value) != len(set(arg.value)):
-                    self.add_message(
-                        "bad-str-strip-call",
-                        node=node,
-                        args=(func.bound.name, func.name),
-                    )
-            elif func.name == "format":
-                self._check_new_format(node, func)
-
-    def _detect_vacuous_formatting(self, node, positional_arguments):
-        counter = Counter(
-            arg.name for arg in positional_arguments if isinstance(arg, astroid.Name)
-        )
-        for name, count in counter.items():
-            if count == 1:
-                continue
-            self.add_message(
-                "duplicate-string-formatting-argument", node=node, args=(name,)
-            )
-
-    def _check_new_format(self, node, func):
-        """Check the new string formatting. """
-        # Skip ormat nodes which don't have an explicit string on the
-        # left side of the format operation.
-        # We do this because our inference engine can't properly handle
-        # redefinitions of the original string.
-        # Note that there may not be any left side at all, if the format method
-        # has been assigned to another variable. See issue 351. For example:
-        #
-        #    fmt = 'some string {}'.format
-        #    fmt('arg')
-        if isinstance(node.func, astroid.Attribute) and not isinstance(
-            node.func.expr, astroid.Const
-        ):
-            return
-        if node.starargs or node.kwargs:
-            return
-        try:
-            strnode = next(func.bound.infer())
-        except astroid.InferenceError:
-            return
-        if not (isinstance(strnode, astroid.Const) and isinstance(strnode.value, str)):
-            return
-        try:
-            call_site = CallSite.from_call(node)
-        except astroid.InferenceError:
-            return
-
-        try:
-            fields, num_args, manual_pos = utils.parse_format_method_string(
-                strnode.value
-            )
-        except utils.IncompleteFormatString:
-            self.add_message("bad-format-string", node=node)
-            return
-
-        positional_arguments = call_site.positional_arguments
-        named_arguments = call_site.keyword_arguments
-        named_fields = {field[0] for field in fields if isinstance(field[0], str)}
-        if num_args and manual_pos:
-            self.add_message("format-combined-specification", node=node)
-            return
-
-        check_args = False
-        # Consider "{[0]} {[1]}" as num_args.
-        num_args += sum(1 for field in named_fields if field == "")
-        if named_fields:
-            for field in named_fields:
-                if field and field not in named_arguments:
-                    self.add_message(
-                        "missing-format-argument-key", node=node, args=(field,)
-                    )
-            for field in named_arguments:
-                if field not in named_fields:
-                    self.add_message(
-                        "unused-format-string-argument", node=node, args=(field,)
-                    )
-            # num_args can be 0 if manual_pos is not.
-            num_args = num_args or manual_pos
-            if positional_arguments or num_args:
-                empty = any(True for field in named_fields if field == "")
-                if named_arguments or empty:
-                    # Verify the required number of positional arguments
-                    # only if the .format got at least one keyword argument.
-                    # This means that the format strings accepts both
-                    # positional and named fields and we should warn
-                    # when one of the them is missing or is extra.
-                    check_args = True
-        else:
-            check_args = True
-        if check_args:
-            # num_args can be 0 if manual_pos is not.
-            num_args = num_args or manual_pos
-            if len(positional_arguments) > num_args:
-                self.add_message("too-many-format-args", node=node)
-            elif len(positional_arguments) < num_args:
-                self.add_message("too-few-format-args", node=node)
-
-        self._detect_vacuous_formatting(node, positional_arguments)
-        self._check_new_format_specifiers(node, fields, named_arguments)
-
-    def _check_new_format_specifiers(self, node, fields, named):
-        """
-        Check attribute and index access in the format
-        string ("{0.a}" and "{0[a]}").
-        """
-        for key, specifiers in fields:
-            # Obtain the argument. If it can't be obtained
-            # or inferred, skip this check.
-            if key == "":
-                # {[0]} will have an unnamed argument, defaulting
-                # to 0. It will not be present in `named`, so use the value
-                # 0 for it.
-                key = 0
-            if isinstance(key, numbers.Number):
-                try:
-                    argname = utils.get_argument_from_call(node, key)
-                except utils.NoSuchArgumentError:
-                    continue
-            else:
-                if key not in named:
-                    continue
-                argname = named[key]
-            if argname in (astroid.Uninferable, None):
-                continue
-            try:
-                argument = utils.safe_infer(argname)
-            except astroid.InferenceError:
-                continue
-            if not specifiers or not argument:
-                # No need to check this key if it doesn't
-                # use attribute / item access
-                continue
-            if argument.parent and isinstance(argument.parent, astroid.Arguments):
-                # Ignore any object coming from an argument,
-                # because we can't infer its value properly.
-                continue
-            previous = argument
-            parsed = []
-            for is_attribute, specifier in specifiers:
-                if previous is astroid.Uninferable:
-                    break
-                parsed.append((is_attribute, specifier))
-                if is_attribute:
-                    try:
-                        previous = previous.getattr(specifier)[0]
-                    except astroid.NotFoundError:
-                        if (
-                            hasattr(previous, "has_dynamic_getattr")
-                            and previous.has_dynamic_getattr()
-                        ):
-                            # Don't warn if the object has a custom __getattr__
-                            break
-                        path = get_access_path(key, parsed)
-                        self.add_message(
-                            "missing-format-attribute",
-                            args=(specifier, path),
-                            node=node,
-                        )
-                        break
-                else:
-                    warn_error = False
-                    if hasattr(previous, "getitem"):
-                        try:
-                            previous = previous.getitem(astroid.Const(specifier))
-                        except (
-                            astroid.AstroidIndexError,
-                            astroid.AstroidTypeError,
-                            astroid.AttributeInferenceError,
-                        ):
-                            warn_error = True
-                        except astroid.InferenceError:
-                            break
-                        if previous is astroid.Uninferable:
-                            break
-                    else:
-                        try:
-                            # Lookup __getitem__ in the current node,
-                            # but skip further checks, because we can't
-                            # retrieve the looked object
-                            previous.getattr("__getitem__")
-                            break
-                        except astroid.NotFoundError:
-                            warn_error = True
-                    if warn_error:
-                        path = get_access_path(key, parsed)
-                        self.add_message(
-                            "invalid-format-index", args=(specifier, path), node=node
-                        )
-                        break
-
-                try:
-                    previous = next(previous.infer())
-                except astroid.InferenceError:
-                    # can't check further if we can't infer it
-                    break
-
-
-class StringConstantChecker(BaseTokenChecker):
-    """Check string literals"""
-
-    __implements__ = (IAstroidChecker, ITokenChecker, IRawChecker)
-    name = "string"
-    msgs = {
-        "W1401": (
-            "Anomalous backslash in string: '%s'. "
-            "String constant might be missing an r prefix.",
-            "anomalous-backslash-in-string",
-            "Used when a backslash is in a literal string but not as an escape.",
-        ),
-        "W1402": (
-            "Anomalous Unicode escape in byte string: '%s'. "
-            "String constant might be missing an r or u prefix.",
-            "anomalous-unicode-escape-in-string",
-            "Used when an escape like \\u is encountered in a byte "
-            "string where it has no effect.",
-        ),
-        "W1403": (
-            "Implicit string concatenation found in %s",
-            "implicit-str-concat-in-sequence",
-            "String literals are implicitly concatenated in a "
-            "literal iterable definition : "
-            "maybe a comma is missing ?",
-        ),
-    }
-    options = (
-        (
-            "check-str-concat-over-line-jumps",
-            {
-                "default": False,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "This flag controls whether the "
-                "implicit-str-concat-in-sequence should generate a warning "
-                "on implicit string concatenation in sequences defined over "
-                "several lines.",
-            },
-        ),
-    )
-
-    # Characters that have a special meaning after a backslash in either
-    # Unicode or byte strings.
-    ESCAPE_CHARACTERS = "abfnrtvx\n\r\t\\'\"01234567"
-
-    # Characters that have a special meaning after a backslash but only in
-    # Unicode strings.
-    UNICODE_ESCAPE_CHARACTERS = "uUN"
-
-    def __init__(self, *args, **kwargs):
-        super(StringConstantChecker, self).__init__(*args, **kwargs)
-        self.string_tokens = {}  # token position -> (token value, next token)
-
-    def process_module(self, module):
-        self._unicode_literals = "unicode_literals" in module.future_imports
-
-    def process_tokens(self, tokens):
-        encoding = "ascii"
-        for i, (tok_type, token, start, _, line) in enumerate(tokens):
-            if tok_type == tokenize.ENCODING:
-                # this is always the first token processed
-                encoding = token
-            elif tok_type == tokenize.STRING:
-                # 'token' is the whole un-parsed token; we can look at the start
-                # of it to see whether it's a raw or unicode string etc.
-                self.process_string_token(token, start[0])
-                # We figure the next token, ignoring comments & newlines:
-                j = i + 1
-                while j < len(tokens) and tokens[j].type in (
-                    tokenize.NEWLINE,
-                    tokenize.NL,
-                    tokenize.COMMENT,
-                ):
-                    j += 1
-                next_token = tokens[j] if j < len(tokens) else None
-                if encoding != "ascii":
-                    # We convert `tokenize` character count into a byte count,
-                    # to match with astroid `.col_offset`
-                    start = (start[0], len(line[: start[1]].encode(encoding)))
-                self.string_tokens[start] = (str_eval(token), next_token)
-
-    @check_messages(*(msgs.keys()))
-    def visit_list(self, node):
-        self.check_for_concatenated_strings(node, "list")
-
-    @check_messages(*(msgs.keys()))
-    def visit_set(self, node):
-        self.check_for_concatenated_strings(node, "set")
-
-    @check_messages(*(msgs.keys()))
-    def visit_tuple(self, node):
-        self.check_for_concatenated_strings(node, "tuple")
-
-    def check_for_concatenated_strings(self, iterable_node, iterable_type):
-        for elt in iterable_node.elts:
-            if isinstance(elt, Const) and elt.pytype() in _AST_NODE_STR_TYPES:
-                if elt.col_offset < 0:
-                    # This can happen in case of escaped newlines
-                    continue
-                if (elt.lineno, elt.col_offset) not in self.string_tokens:
-                    # This may happen with Latin1 encoding
-                    # cf. https://github.com/PyCQA/pylint/issues/2610
-                    continue
-                matching_token, next_token = self.string_tokens[
-                    (elt.lineno, elt.col_offset)
-                ]
-                # We detect string concatenation: the AST Const is the
-                # combination of 2 string tokens
-                if matching_token != elt.value and next_token is not None:
-                    if next_token.type == tokenize.STRING and (
-                        next_token.start[0] == elt.lineno
-                        or self.config.check_str_concat_over_line_jumps
-                    ):
-                        self.add_message(
-                            "implicit-str-concat-in-sequence",
-                            line=elt.lineno,
-                            args=(iterable_type,),
-                        )
-
-    def process_string_token(self, token, start_row):
-        quote_char = None
-        index = None
-        for index, char in enumerate(token):
-            if char in "'\"":
-                quote_char = char
-                break
-        if quote_char is None:
-            return
-
-        prefix = token[:index].lower()  # markers like u, b, r.
-        after_prefix = token[index:]
-        if after_prefix[:3] == after_prefix[-3:] == 3 * quote_char:
-            string_body = after_prefix[3:-3]
-        else:
-            string_body = after_prefix[1:-1]  # Chop off quotes
-        # No special checks on raw strings at the moment.
-        if "r" not in prefix:
-            self.process_non_raw_string_token(prefix, string_body, start_row)
-
-    def process_non_raw_string_token(self, prefix, string_body, start_row):
-        """check for bad escapes in a non-raw string.
-
-        prefix: lowercase string of eg 'ur' string prefix markers.
-        string_body: the un-parsed body of the string, not including the quote
-        marks.
-        start_row: integer line number in the source.
-        """
-        # Walk through the string; if we see a backslash then escape the next
-        # character, and skip over it.  If we see a non-escaped character,
-        # alert, and continue.
-        #
-        # Accept a backslash when it escapes a backslash, or a quote, or
-        # end-of-line, or one of the letters that introduce a special escape
-        # sequence <http://docs.python.org/reference/lexical_analysis.html>
-        #
-        index = 0
-        while True:
-            index = string_body.find("\\", index)
-            if index == -1:
-                break
-            # There must be a next character; having a backslash at the end
-            # of the string would be a SyntaxError.
-            next_char = string_body[index + 1]
-            match = string_body[index : index + 2]
-            if next_char in self.UNICODE_ESCAPE_CHARACTERS:
-                if "u" in prefix:
-                    pass
-                elif "b" not in prefix:
-                    pass  # unicode by default
-                else:
-                    self.add_message(
-                        "anomalous-unicode-escape-in-string",
-                        line=start_row,
-                        args=(match,),
-                        col_offset=index,
-                    )
-            elif next_char not in self.ESCAPE_CHARACTERS:
-                self.add_message(
-                    "anomalous-backslash-in-string",
-                    line=start_row,
-                    args=(match,),
-                    col_offset=index,
-                )
-            # Whether it was a valid escape or not, backslash followed by
-            # another character can always be consumed whole: the second
-            # character can never be the start of a new backslash escape.
-            index += 2
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(StringFormatChecker(linter))
-    linter.register_checker(StringConstantChecker(linter))
-
-
-def str_eval(token):
-    """
-    Mostly replicate `ast.literal_eval(token)` manually to avoid any performance hit.
-    This supports f-strings, contrary to `ast.literal_eval`.
-    We have to support all string literal notations:
-    https://docs.python.org/3/reference/lexical_analysis.html#string-and-bytes-literals
-    """
-    if token[0:2].lower() in ("fr", "rf"):
-        token = token[2:]
-    elif token[0].lower() in ("r", "u", "f"):
-        token = token[1:]
-    if token[0:3] in ('"""', "'''"):
-        return token[3:-3]
-    return token[1:-1]
diff --git a/venv/Lib/site-packages/pylint/checkers/typecheck.py b/venv/Lib/site-packages/pylint/checkers/typecheck.py
deleted file mode 100644
index a288f49..0000000
--- a/venv/Lib/site-packages/pylint/checkers/typecheck.py
+++ /dev/null
@@ -1,1770 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2009 James Lingard <jchl@aristanetworks.com>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 David Shea <dshea@redhat.com>
-# Copyright (c) 2014 Steven Myint <hg@stevenmyint.com>
-# Copyright (c) 2014 Holger Peters <email@holger-peters.de>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Anentropic <ego@anentropic.com>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2015 Rene Zhang <rz99@cornell.edu>
-# Copyright (c) 2015 Radu Ciorba <radu@devrandom.ro>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016 Jürgen Hermann <jh@web.de>
-# Copyright (c) 2016 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016 Filipe Brandenburger <filbranden@google.com>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2017 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 Ben Green <benhgreen@icloud.com>
-# Copyright (c) 2018 Konstantin <Github@pheanex.de>
-# Copyright (c) 2018 Justin Li <justinnhli@users.noreply.github.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""try to find more bugs in the code using astroid inference capabilities
-"""
-
-import builtins
-import fnmatch
-import heapq
-import itertools
-import operator
-import re
-import shlex
-import sys
-import types
-from collections import deque
-from collections.abc import Sequence
-from functools import singledispatch
-
-import astroid
-import astroid.arguments
-import astroid.context
-import astroid.nodes
-from astroid import bases, decorators, exceptions, modutils, objects
-from astroid.interpreter import dunder_lookup
-
-from pylint.checkers import BaseChecker
-from pylint.checkers.utils import (
-    check_messages,
-    decorated_with,
-    decorated_with_property,
-    has_known_bases,
-    is_builtin_object,
-    is_comprehension,
-    is_inside_abstract_class,
-    is_iterable,
-    is_mapping,
-    is_overload_stub,
-    is_super,
-    node_ignores_exception,
-    safe_infer,
-    supports_delitem,
-    supports_getitem,
-    supports_membership_test,
-    supports_setitem,
-)
-from pylint.interfaces import INFERENCE, IAstroidChecker
-from pylint.utils import get_global_option
-
-BUILTINS = builtins.__name__
-STR_FORMAT = {"%s.str.format" % BUILTINS}
-ASYNCIO_COROUTINE = "asyncio.coroutines.coroutine"
-
-
-def _unflatten(iterable):
-    for index, elem in enumerate(iterable):
-        if isinstance(elem, Sequence) and not isinstance(elem, str):
-            for single_elem in _unflatten(elem):
-                yield single_elem
-        elif elem and not index:
-            # We're interested only in the first element.
-            yield elem
-
-
-def _flatten_container(iterable):
-    # Flatten nested containers into a single iterable
-    for item in iterable:
-        if isinstance(item, (list, tuple, types.GeneratorType)):
-            yield from _flatten_container(item)
-        else:
-            yield item
-
-
-def _is_owner_ignored(owner, attrname, ignored_classes, ignored_modules):
-    """Check if the given owner should be ignored
-
-    This will verify if the owner's module is in *ignored_modules*
-    or the owner's module fully qualified name is in *ignored_modules*
-    or if the *ignored_modules* contains a pattern which catches
-    the fully qualified name of the module.
-
-    Also, similar checks are done for the owner itself, if its name
-    matches any name from the *ignored_classes* or if its qualified
-    name can be found in *ignored_classes*.
-    """
-    ignored_modules = set(ignored_modules)
-    module_name = owner.root().name
-    module_qname = owner.root().qname()
-
-    for ignore in ignored_modules:
-        # Try to match the module name / fully qualified name directly
-        if module_qname in ignored_modules or module_name in ignored_modules:
-            return True
-
-        # Try to see if the ignores pattern match against the module name.
-        if fnmatch.fnmatch(module_qname, ignore):
-            return True
-
-        # Otherwise we might have a root module name being ignored,
-        # and the qualified owner has more levels of depth.
-        parts = deque(module_name.split("."))
-        current_module = ""
-
-        while parts:
-            part = parts.popleft()
-            if not current_module:
-                current_module = part
-            else:
-                current_module += ".{}".format(part)
-            if current_module in ignored_modules:
-                return True
-
-    # Match against ignored classes.
-    ignored_classes = set(ignored_classes)
-    if hasattr(owner, "qname"):
-        qname = owner.qname()
-    else:
-        qname = ""
-    return any(ignore in (attrname, qname) for ignore in ignored_classes)
-
-
-@singledispatch
-def _node_names(node):
-    if not hasattr(node, "locals"):
-        return []
-    return node.locals.keys()
-
-
-@_node_names.register(astroid.ClassDef)
-@_node_names.register(astroid.Instance)
-def _(node):
-    values = itertools.chain(node.instance_attrs.keys(), node.locals.keys())
-
-    try:
-        mro = node.mro()[1:]
-    except (NotImplementedError, TypeError):
-        mro = node.ancestors()
-
-    other_values = [value for cls in mro for value in _node_names(cls)]
-    return itertools.chain(values, other_values)
-
-
-def _string_distance(seq1, seq2):
-    seq2_length = len(seq2)
-
-    row = list(range(1, seq2_length + 1)) + [0]
-    for seq1_index, seq1_char in enumerate(seq1):
-        last_row = row
-        row = [0] * seq2_length + [seq1_index + 1]
-
-        for seq2_index, seq2_char in enumerate(seq2):
-            row[seq2_index] = min(
-                last_row[seq2_index] + 1,
-                row[seq2_index - 1] + 1,
-                last_row[seq2_index - 1] + (seq1_char != seq2_char),
-            )
-
-    return row[seq2_length - 1]
-
-
-def _similar_names(owner, attrname, distance_threshold, max_choices):
-    """Given an owner and a name, try to find similar names
-
-    The similar names are searched given a distance metric and only
-    a given number of choices will be returned.
-    """
-    possible_names = []
-    names = _node_names(owner)
-
-    for name in names:
-        if name == attrname:
-            continue
-
-        distance = _string_distance(attrname, name)
-        if distance <= distance_threshold:
-            possible_names.append((name, distance))
-
-    # Now get back the values with a minimum, up to the given
-    # limit or choices.
-    picked = [
-        name
-        for (name, _) in heapq.nsmallest(
-            max_choices, possible_names, key=operator.itemgetter(1)
-        )
-    ]
-    return sorted(picked)
-
-
-def _missing_member_hint(owner, attrname, distance_threshold, max_choices):
-    names = _similar_names(owner, attrname, distance_threshold, max_choices)
-    if not names:
-        # No similar name.
-        return ""
-
-    names = list(map(repr, names))
-    if len(names) == 1:
-        names = ", ".join(names)
-    else:
-        names = "one of {} or {}".format(", ".join(names[:-1]), names[-1])
-
-    return "; maybe {}?".format(names)
-
-
-MSGS = {
-    "E1101": (
-        "%s %r has no %r member%s",
-        "no-member",
-        "Used when a variable is accessed for an unexistent member.",
-        {"old_names": [("E1103", "maybe-no-member")]},
-    ),
-    "I1101": (
-        "%s %r has no %r member%s, but source is unavailable. Consider "
-        "adding this module to extension-pkg-whitelist if you want "
-        "to perform analysis based on run-time introspection of living objects.",
-        "c-extension-no-member",
-        "Used when a variable is accessed for non-existent member of C "
-        "extension. Due to unavailability of source static analysis is impossible, "
-        "but it may be performed by introspecting living objects in run-time.",
-    ),
-    "E1102": (
-        "%s is not callable",
-        "not-callable",
-        "Used when an object being called has been inferred to a non "
-        "callable object.",
-    ),
-    "E1111": (
-        "Assigning result of a function call, where the function has no return",
-        "assignment-from-no-return",
-        "Used when an assignment is done on a function call but the "
-        "inferred function doesn't return anything.",
-    ),
-    "E1120": (
-        "No value for argument %s in %s call",
-        "no-value-for-parameter",
-        "Used when a function call passes too few arguments.",
-    ),
-    "E1121": (
-        "Too many positional arguments for %s call",
-        "too-many-function-args",
-        "Used when a function call passes too many positional arguments.",
-    ),
-    "E1123": (
-        "Unexpected keyword argument %r in %s call",
-        "unexpected-keyword-arg",
-        "Used when a function call passes a keyword argument that "
-        "doesn't correspond to one of the function's parameter names.",
-    ),
-    "E1124": (
-        "Argument %r passed by position and keyword in %s call",
-        "redundant-keyword-arg",
-        "Used when a function call would result in assigning multiple "
-        "values to a function parameter, one value from a positional "
-        "argument and one from a keyword argument.",
-    ),
-    "E1125": (
-        "Missing mandatory keyword argument %r in %s call",
-        "missing-kwoa",
-        (
-            "Used when a function call does not pass a mandatory"
-            " keyword-only argument."
-        ),
-    ),
-    "E1126": (
-        "Sequence index is not an int, slice, or instance with __index__",
-        "invalid-sequence-index",
-        "Used when a sequence type is indexed with an invalid type. "
-        "Valid types are ints, slices, and objects with an __index__ "
-        "method.",
-    ),
-    "E1127": (
-        "Slice index is not an int, None, or instance with __index__",
-        "invalid-slice-index",
-        "Used when a slice index is not an integer, None, or an object "
-        "with an __index__ method.",
-    ),
-    "E1128": (
-        "Assigning result of a function call, where the function returns None",
-        "assignment-from-none",
-        "Used when an assignment is done on a function call but the "
-        "inferred function returns nothing but None.",
-        {"old_names": [("W1111", "old-assignment-from-none")]},
-    ),
-    "E1129": (
-        "Context manager '%s' doesn't implement __enter__ and __exit__.",
-        "not-context-manager",
-        "Used when an instance in a with statement doesn't implement "
-        "the context manager protocol(__enter__/__exit__).",
-    ),
-    "E1130": (
-        "%s",
-        "invalid-unary-operand-type",
-        "Emitted when a unary operand is used on an object which does not "
-        "support this type of operation.",
-    ),
-    "E1131": (
-        "%s",
-        "unsupported-binary-operation",
-        "Emitted when a binary arithmetic operation between two "
-        "operands is not supported.",
-    ),
-    "E1132": (
-        "Got multiple values for keyword argument %r in function call",
-        "repeated-keyword",
-        "Emitted when a function call got multiple values for a keyword.",
-    ),
-    "E1135": (
-        "Value '%s' doesn't support membership test",
-        "unsupported-membership-test",
-        "Emitted when an instance in membership test expression doesn't "
-        "implement membership protocol (__contains__/__iter__/__getitem__).",
-    ),
-    "E1136": (
-        "Value '%s' is unsubscriptable",
-        "unsubscriptable-object",
-        "Emitted when a subscripted value doesn't support subscription "
-        "(i.e. doesn't define __getitem__ method or __class_getitem__ for a class).",
-    ),
-    "E1137": (
-        "%r does not support item assignment",
-        "unsupported-assignment-operation",
-        "Emitted when an object does not support item assignment "
-        "(i.e. doesn't define __setitem__ method).",
-    ),
-    "E1138": (
-        "%r does not support item deletion",
-        "unsupported-delete-operation",
-        "Emitted when an object does not support item deletion "
-        "(i.e. doesn't define __delitem__ method).",
-    ),
-    "E1139": (
-        "Invalid metaclass %r used",
-        "invalid-metaclass",
-        "Emitted whenever we can detect that a class is using, "
-        "as a metaclass, something which might be invalid for using as "
-        "a metaclass.",
-    ),
-    "E1140": (
-        "Dict key is unhashable",
-        "unhashable-dict-key",
-        "Emitted when a dict key is not hashable "
-        "(i.e. doesn't define __hash__ method).",
-    ),
-    "E1141": (
-        "Unpacking a dictionary in iteration without calling .items()",
-        "dict-iter-missing-items",
-        "Emitted when trying to iterate through a dict without calling .items()",
-    ),
-    "W1113": (
-        "Keyword argument before variable positional arguments list "
-        "in the definition of %s function",
-        "keyword-arg-before-vararg",
-        "When defining a keyword argument before variable positional arguments, one can "
-        "end up in having multiple values passed for the aforementioned parameter in "
-        "case the method is called with keyword arguments.",
-    ),
-    "W1114": (
-        "Positional arguments appear to be out of order",
-        "arguments-out-of-order",
-        "Emitted  when the caller's argument names fully match the parameter "
-        "names in the function signature but do not have the same order.",
-    ),
-}
-
-# builtin sequence types in Python 2 and 3.
-SEQUENCE_TYPES = {
-    "str",
-    "unicode",
-    "list",
-    "tuple",
-    "bytearray",
-    "xrange",
-    "range",
-    "bytes",
-    "memoryview",
-}
-
-
-def _emit_no_member(node, owner, owner_name, ignored_mixins=True, ignored_none=True):
-    """Try to see if no-member should be emitted for the given owner.
-
-    The following cases are ignored:
-
-        * the owner is a function and it has decorators.
-        * the owner is an instance and it has __getattr__, __getattribute__ implemented
-        * the module is explicitly ignored from no-member checks
-        * the owner is a class and the name can be found in its metaclass.
-        * The access node is protected by an except handler, which handles
-          AttributeError, Exception or bare except.
-    """
-    # pylint: disable=too-many-return-statements
-    if node_ignores_exception(node, AttributeError):
-        return False
-    if ignored_none and isinstance(owner, astroid.Const) and owner.value is None:
-        return False
-    if is_super(owner) or getattr(owner, "type", None) == "metaclass":
-        return False
-    if owner_name and ignored_mixins and owner_name[-5:].lower() == "mixin":
-        return False
-    if isinstance(owner, astroid.FunctionDef) and owner.decorators:
-        return False
-    if isinstance(owner, (astroid.Instance, astroid.ClassDef)):
-        if owner.has_dynamic_getattr():
-            # Issue #2565: Don't ignore enums, as they have a `__getattr__` but it's not
-            # invoked at this point.
-            try:
-                metaclass = owner.metaclass()
-            except exceptions.MroError:
-                return False
-            if metaclass:
-                return metaclass.qname() == "enum.EnumMeta"
-            return False
-        if not has_known_bases(owner):
-            return False
-
-        # Exclude typed annotations, since these might actually exist
-        # at some point during the runtime of the program.
-        attribute = owner.locals.get(node.attrname, [None])[0]
-        if (
-            attribute
-            and isinstance(attribute, astroid.AssignName)
-            and isinstance(attribute.parent, astroid.AnnAssign)
-        ):
-            return False
-    if isinstance(owner, objects.Super):
-        # Verify if we are dealing with an invalid Super object.
-        # If it is invalid, then there's no point in checking that
-        # it has the required attribute. Also, don't fail if the
-        # MRO is invalid.
-        try:
-            owner.super_mro()
-        except (exceptions.MroError, exceptions.SuperError):
-            return False
-        if not all(map(has_known_bases, owner.type.mro())):
-            return False
-    if isinstance(owner, astroid.Module):
-        try:
-            owner.getattr("__getattr__")
-            return False
-        except astroid.NotFoundError:
-            pass
-    if owner_name and node.attrname.startswith("_" + owner_name):
-        # Test if an attribute has been mangled ('private' attribute)
-        unmangled_name = node.attrname.split("_" + owner_name)[-1]
-        try:
-            if owner.getattr(unmangled_name, context=None) is not None:
-                return False
-        except astroid.NotFoundError:
-            return True
-    return True
-
-
-def _determine_callable(callable_obj):
-    # Ordering is important, since BoundMethod is a subclass of UnboundMethod,
-    # and Function inherits Lambda.
-    parameters = 0
-    if hasattr(callable_obj, "implicit_parameters"):
-        parameters = callable_obj.implicit_parameters()
-    if isinstance(callable_obj, astroid.BoundMethod):
-        # Bound methods have an extra implicit 'self' argument.
-        return callable_obj, parameters, callable_obj.type
-    if isinstance(callable_obj, astroid.UnboundMethod):
-        return callable_obj, parameters, "unbound method"
-    if isinstance(callable_obj, astroid.FunctionDef):
-        return callable_obj, parameters, callable_obj.type
-    if isinstance(callable_obj, astroid.Lambda):
-        return callable_obj, parameters, "lambda"
-    if isinstance(callable_obj, astroid.ClassDef):
-        # Class instantiation, lookup __new__ instead.
-        # If we only find object.__new__, we can safely check __init__
-        # instead. If __new__ belongs to builtins, then we look
-        # again for __init__ in the locals, since we won't have
-        # argument information for the builtin __new__ function.
-        try:
-            # Use the last definition of __new__.
-            new = callable_obj.local_attr("__new__")[-1]
-        except exceptions.NotFoundError:
-            new = None
-
-        from_object = new and new.parent.scope().name == "object"
-        from_builtins = new and new.root().name in sys.builtin_module_names
-
-        if not new or from_object or from_builtins:
-            try:
-                # Use the last definition of __init__.
-                callable_obj = callable_obj.local_attr("__init__")[-1]
-            except exceptions.NotFoundError:
-                # do nothing, covered by no-init.
-                raise ValueError
-        else:
-            callable_obj = new
-
-        if not isinstance(callable_obj, astroid.FunctionDef):
-            raise ValueError
-        # both have an extra implicit 'cls'/'self' argument.
-        return callable_obj, parameters, "constructor"
-
-    raise ValueError
-
-
-def _has_parent_of_type(node, node_type, statement):
-    """Check if the given node has a parent of the given type."""
-    parent = node.parent
-    while not isinstance(parent, node_type) and statement.parent_of(parent):
-        parent = parent.parent
-    return isinstance(parent, node_type)
-
-
-def _no_context_variadic_keywords(node, scope):
-    statement = node.statement()
-    variadics = ()
-
-    if isinstance(scope, astroid.Lambda) and not isinstance(scope, astroid.FunctionDef):
-        variadics = list(node.keywords or []) + node.kwargs
-    else:
-        if isinstance(statement, (astroid.Return, astroid.Expr)) and isinstance(
-            statement.value, astroid.Call
-        ):
-            call = statement.value
-            variadics = list(call.keywords or []) + call.kwargs
-
-    return _no_context_variadic(node, scope.args.kwarg, astroid.Keyword, variadics)
-
-
-def _no_context_variadic_positional(node, scope):
-    variadics = ()
-    if isinstance(scope, astroid.Lambda) and not isinstance(scope, astroid.FunctionDef):
-        variadics = node.starargs + node.kwargs
-    else:
-        statement = node.statement()
-        if isinstance(statement, (astroid.Expr, astroid.Return)) and isinstance(
-            statement.value, astroid.Call
-        ):
-            call = statement.value
-            variadics = call.starargs + call.kwargs
-
-    return _no_context_variadic(node, scope.args.vararg, astroid.Starred, variadics)
-
-
-def _no_context_variadic(node, variadic_name, variadic_type, variadics):
-    """Verify if the given call node has variadic nodes without context
-
-    This is a workaround for handling cases of nested call functions
-    which don't have the specific call context at hand.
-    Variadic arguments (variable positional arguments and variable
-    keyword arguments) are inferred, inherently wrong, by astroid
-    as a Tuple, respectively a Dict with empty elements.
-    This can lead pylint to believe that a function call receives
-    too few arguments.
-    """
-    scope = node.scope()
-    is_in_lambda_scope = not isinstance(scope, astroid.FunctionDef) and isinstance(
-        scope, astroid.Lambda
-    )
-    statement = node.statement()
-    for name in statement.nodes_of_class(astroid.Name):
-        if name.name != variadic_name:
-            continue
-
-        inferred = safe_infer(name)
-        if isinstance(inferred, (astroid.List, astroid.Tuple)):
-            length = len(inferred.elts)
-        elif isinstance(inferred, astroid.Dict):
-            length = len(inferred.items)
-        else:
-            continue
-
-        if is_in_lambda_scope and isinstance(inferred.parent, astroid.Arguments):
-            # The statement of the variadic will be the assignment itself,
-            # so we need to go the lambda instead
-            inferred_statement = inferred.parent.parent
-        else:
-            inferred_statement = inferred.statement()
-
-        if not length and isinstance(inferred_statement, astroid.Lambda):
-            is_in_starred_context = _has_parent_of_type(node, variadic_type, statement)
-            used_as_starred_argument = any(
-                variadic.value == name or variadic.value.parent_of(name)
-                for variadic in variadics
-            )
-            if is_in_starred_context or used_as_starred_argument:
-                return True
-    return False
-
-
-def _is_invalid_metaclass(metaclass):
-    try:
-        mro = metaclass.mro()
-    except NotImplementedError:
-        # Cannot have a metaclass which is not a newstyle class.
-        return True
-    else:
-        if not any(is_builtin_object(cls) and cls.name == "type" for cls in mro):
-            return True
-    return False
-
-
-def _infer_from_metaclass_constructor(cls, func):
-    """Try to infer what the given *func* constructor is building
-
-    :param astroid.FunctionDef func:
-        A metaclass constructor. Metaclass definitions can be
-        functions, which should accept three arguments, the name of
-        the class, the bases of the class and the attributes.
-        The function could return anything, but usually it should
-        be a proper metaclass.
-    :param astroid.ClassDef cls:
-        The class for which the *func* parameter should generate
-        a metaclass.
-    :returns:
-        The class generated by the function or None,
-        if we couldn't infer it.
-    :rtype: astroid.ClassDef
-    """
-    context = astroid.context.InferenceContext()
-
-    class_bases = astroid.List()
-    class_bases.postinit(elts=cls.bases)
-
-    attrs = astroid.Dict()
-    local_names = [(name, values[-1]) for name, values in cls.locals.items()]
-    attrs.postinit(local_names)
-
-    builder_args = astroid.Tuple()
-    builder_args.postinit([cls.name, class_bases, attrs])
-
-    context.callcontext = astroid.context.CallContext(builder_args)
-    try:
-        inferred = next(func.infer_call_result(func, context), None)
-    except astroid.InferenceError:
-        return None
-    return inferred or None
-
-
-def _is_c_extension(module_node):
-    return (
-        not modutils.is_standard_module(module_node.name)
-        and not module_node.fully_defined()
-    )
-
-
-class TypeChecker(BaseChecker):
-    """try to find bugs in the code using type inference
-    """
-
-    __implements__ = (IAstroidChecker,)
-
-    # configuration section name
-    name = "typecheck"
-    # messages
-    msgs = MSGS
-    priority = -1
-    # configuration options
-    options = (
-        (
-            "ignore-on-opaque-inference",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "This flag controls whether pylint should warn about "
-                "no-member and similar checks whenever an opaque object "
-                "is returned when inferring. The inference can return "
-                "multiple potential results while evaluating a Python object, "
-                "but some branches might not be evaluated, which results in "
-                "partial inference. In that case, it might be useful to still emit "
-                "no-member and other checks for the rest of the inferred objects.",
-            },
-        ),
-        (
-            "ignore-mixin-members",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": 'Tells whether missing members accessed in mixin \
-class should be ignored. A mixin class is detected if its name ends with \
-"mixin" (case insensitive).',
-            },
-        ),
-        (
-            "ignore-none",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "Tells whether to warn about missing members when the owner "
-                "of the attribute is inferred to be None.",
-            },
-        ),
-        (
-            "ignored-modules",
-            {
-                "default": (),
-                "type": "csv",
-                "metavar": "<module names>",
-                "help": "List of module names for which member attributes "
-                "should not be checked (useful for modules/projects "
-                "where namespaces are manipulated during runtime and "
-                "thus existing member attributes cannot be "
-                "deduced by static analysis). It supports qualified "
-                "module names, as well as Unix pattern matching.",
-            },
-        ),
-        # the defaults here are *stdlib* names that (almost) always
-        # lead to false positives, since their idiomatic use is
-        # 'too dynamic' for pylint to grok.
-        (
-            "ignored-classes",
-            {
-                "default": ("optparse.Values", "thread._local", "_thread._local"),
-                "type": "csv",
-                "metavar": "<members names>",
-                "help": "List of class names for which member attributes "
-                "should not be checked (useful for classes with "
-                "dynamically set attributes). This supports "
-                "the use of qualified names.",
-            },
-        ),
-        (
-            "generated-members",
-            {
-                "default": (),
-                "type": "string",
-                "metavar": "<members names>",
-                "help": "List of members which are set dynamically and \
-missed by pylint inference system, and so shouldn't trigger E1101 when \
-accessed. Python regular expressions are accepted.",
-            },
-        ),
-        (
-            "contextmanager-decorators",
-            {
-                "default": ["contextlib.contextmanager"],
-                "type": "csv",
-                "metavar": "<decorator names>",
-                "help": "List of decorators that produce context managers, "
-                "such as contextlib.contextmanager. Add to this list "
-                "to register other decorators that produce valid "
-                "context managers.",
-            },
-        ),
-        (
-            "missing-member-hint-distance",
-            {
-                "default": 1,
-                "type": "int",
-                "metavar": "<member hint edit distance>",
-                "help": "The minimum edit distance a name should have in order "
-                "to be considered a similar match for a missing member name.",
-            },
-        ),
-        (
-            "missing-member-max-choices",
-            {
-                "default": 1,
-                "type": "int",
-                "metavar": "<member hint max choices>",
-                "help": "The total number of similar names that should be taken in "
-                "consideration when showing a hint for a missing member.",
-            },
-        ),
-        (
-            "missing-member-hint",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<missing member hint>",
-                "help": "Show a hint with possible names when a member name was not "
-                "found. The aspect of finding the hint is based on edit distance.",
-            },
-        ),
-        (
-            "signature-mutators",
-            {
-                "default": [],
-                "type": "csv",
-                "metavar": "<decorator names>",
-                "help": "List of decorators that change the signature of "
-                "a decorated function.",
-            },
-        ),
-    )
-
-    @decorators.cachedproperty
-    def _suggestion_mode(self):
-        return get_global_option(self, "suggestion-mode", default=True)
-
-    def open(self):
-        # do this in open since config not fully initialized in __init__
-        # generated_members may contain regular expressions
-        # (surrounded by quote `"` and followed by a comma `,`)
-        # REQUEST,aq_parent,"[a-zA-Z]+_set{1,2}"' =>
-        # ('REQUEST', 'aq_parent', '[a-zA-Z]+_set{1,2}')
-        if isinstance(self.config.generated_members, str):
-            gen = shlex.shlex(self.config.generated_members)
-            gen.whitespace += ","
-            gen.wordchars += r"[]-+\.*?()|"
-            self.config.generated_members = tuple(tok.strip('"') for tok in gen)
-
-    @check_messages("keyword-arg-before-vararg")
-    def visit_functiondef(self, node):
-        # check for keyword arg before varargs
-        if node.args.vararg and node.args.defaults:
-            self.add_message("keyword-arg-before-vararg", node=node, args=(node.name))
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    @check_messages("invalid-metaclass")
-    def visit_classdef(self, node):
-        def _metaclass_name(metaclass):
-            if isinstance(metaclass, (astroid.ClassDef, astroid.FunctionDef)):
-                return metaclass.name
-            return metaclass.as_string()
-
-        metaclass = node.declared_metaclass()
-        if not metaclass:
-            return
-
-        if isinstance(metaclass, astroid.FunctionDef):
-            # Try to infer the result.
-            metaclass = _infer_from_metaclass_constructor(node, metaclass)
-            if not metaclass:
-                # Don't do anything if we cannot infer the result.
-                return
-
-        if isinstance(metaclass, astroid.ClassDef):
-            if _is_invalid_metaclass(metaclass):
-                self.add_message(
-                    "invalid-metaclass", node=node, args=(_metaclass_name(metaclass),)
-                )
-        else:
-            self.add_message(
-                "invalid-metaclass", node=node, args=(_metaclass_name(metaclass),)
-            )
-
-    def visit_assignattr(self, node):
-        if isinstance(node.assign_type(), astroid.AugAssign):
-            self.visit_attribute(node)
-
-    def visit_delattr(self, node):
-        self.visit_attribute(node)
-
-    @check_messages("no-member", "c-extension-no-member")
-    def visit_attribute(self, node):
-        """check that the accessed attribute exists
-
-        to avoid too much false positives for now, we'll consider the code as
-        correct if a single of the inferred nodes has the accessed attribute.
-
-        function/method, super call and metaclasses are ignored
-        """
-        for pattern in self.config.generated_members:
-            # attribute is marked as generated, stop here
-            if re.match(pattern, node.attrname):
-                return
-            if re.match(pattern, node.as_string()):
-                return
-
-        try:
-            inferred = list(node.expr.infer())
-        except exceptions.InferenceError:
-            return
-
-        # list of (node, nodename) which are missing the attribute
-        missingattr = set()
-
-        non_opaque_inference_results = [
-            owner
-            for owner in inferred
-            if owner is not astroid.Uninferable
-            and not isinstance(owner, astroid.nodes.Unknown)
-        ]
-        if (
-            len(non_opaque_inference_results) != len(inferred)
-            and self.config.ignore_on_opaque_inference
-        ):
-            # There is an ambiguity in the inference. Since we can't
-            # make sure that we won't emit a false positive, we just stop
-            # whenever the inference returns an opaque inference object.
-            return
-        for owner in non_opaque_inference_results:
-            name = getattr(owner, "name", None)
-            if _is_owner_ignored(
-                owner, name, self.config.ignored_classes, self.config.ignored_modules
-            ):
-                continue
-
-            try:
-                if not [
-                    n
-                    for n in owner.getattr(node.attrname)
-                    if not isinstance(n.statement(), astroid.AugAssign)
-                ]:
-                    missingattr.add((owner, name))
-                    continue
-            except AttributeError:
-                continue
-            except exceptions.NotFoundError:
-                # This can't be moved before the actual .getattr call,
-                # because there can be more values inferred and we are
-                # stopping after the first one which has the attribute in question.
-                # The problem is that if the first one has the attribute,
-                # but we continue to the next values which doesn't have the
-                # attribute, then we'll have a false positive.
-                # So call this only after the call has been made.
-                if not _emit_no_member(
-                    node,
-                    owner,
-                    name,
-                    ignored_mixins=self.config.ignore_mixin_members,
-                    ignored_none=self.config.ignore_none,
-                ):
-                    continue
-                missingattr.add((owner, name))
-                continue
-            # stop on the first found
-            break
-        else:
-            # we have not found any node with the attributes, display the
-            # message for inferred nodes
-            done = set()
-            for owner, name in missingattr:
-                if isinstance(owner, astroid.Instance):
-                    actual = owner._proxied
-                else:
-                    actual = owner
-                if actual in done:
-                    continue
-                done.add(actual)
-
-                msg, hint = self._get_nomember_msgid_hint(node, owner)
-                self.add_message(
-                    msg,
-                    node=node,
-                    args=(owner.display_type(), name, node.attrname, hint),
-                    confidence=INFERENCE,
-                )
-
-    def _get_nomember_msgid_hint(self, node, owner):
-        suggestions_are_possible = self._suggestion_mode and isinstance(
-            owner, astroid.Module
-        )
-        if suggestions_are_possible and _is_c_extension(owner):
-            msg = "c-extension-no-member"
-            hint = ""
-        else:
-            msg = "no-member"
-            if self.config.missing_member_hint:
-                hint = _missing_member_hint(
-                    owner,
-                    node.attrname,
-                    self.config.missing_member_hint_distance,
-                    self.config.missing_member_max_choices,
-                )
-            else:
-                hint = ""
-        return msg, hint
-
-    @check_messages("assignment-from-no-return", "assignment-from-none")
-    def visit_assign(self, node):
-        """check that if assigning to a function call, the function is
-        possibly returning something valuable
-        """
-        if not isinstance(node.value, astroid.Call):
-            return
-
-        function_node = safe_infer(node.value.func)
-        funcs = (astroid.FunctionDef, astroid.UnboundMethod, astroid.BoundMethod)
-        if not isinstance(function_node, funcs):
-            return
-
-        # Unwrap to get the actual function object
-        if isinstance(function_node, astroid.BoundMethod) and isinstance(
-            function_node._proxied, astroid.UnboundMethod
-        ):
-            function_node = function_node._proxied._proxied
-
-        # Make sure that it's a valid function that we can analyze.
-        # Ordered from less expensive to more expensive checks.
-        # pylint: disable=too-many-boolean-expressions
-        if (
-            not function_node.is_function
-            or isinstance(function_node, astroid.AsyncFunctionDef)
-            or function_node.decorators
-            or function_node.is_generator()
-            or function_node.is_abstract(pass_is_abstract=False)
-            or not function_node.root().fully_defined()
-        ):
-            return
-
-        returns = list(
-            function_node.nodes_of_class(astroid.Return, skip_klass=astroid.FunctionDef)
-        )
-        if not returns:
-            self.add_message("assignment-from-no-return", node=node)
-        else:
-            for rnode in returns:
-                if not (
-                    isinstance(rnode.value, astroid.Const)
-                    and rnode.value.value is None
-                    or rnode.value is None
-                ):
-                    break
-            else:
-                self.add_message("assignment-from-none", node=node)
-
-    def _check_uninferable_call(self, node):
-        """
-        Check that the given uninferable Call node does not
-        call an actual function.
-        """
-        if not isinstance(node.func, astroid.Attribute):
-            return
-
-        # Look for properties. First, obtain
-        # the lhs of the Attribute node and search the attribute
-        # there. If that attribute is a property or a subclass of properties,
-        # then most likely it's not callable.
-
-        expr = node.func.expr
-        klass = safe_infer(expr)
-        if (
-            klass is None
-            or klass is astroid.Uninferable
-            or not isinstance(klass, astroid.Instance)
-        ):
-            return
-
-        try:
-            attrs = klass._proxied.getattr(node.func.attrname)
-        except exceptions.NotFoundError:
-            return
-
-        for attr in attrs:
-            if attr is astroid.Uninferable:
-                continue
-            if not isinstance(attr, astroid.FunctionDef):
-                continue
-
-            # Decorated, see if it is decorated with a property.
-            # Also, check the returns and see if they are callable.
-            if decorated_with_property(attr):
-
-                try:
-                    all_returns_are_callable = all(
-                        return_node.callable() or return_node is astroid.Uninferable
-                        for return_node in attr.infer_call_result(node)
-                    )
-                except astroid.InferenceError:
-                    continue
-
-                if not all_returns_are_callable:
-                    self.add_message(
-                        "not-callable", node=node, args=node.func.as_string()
-                    )
-                    break
-
-    def _check_argument_order(self, node, call_site, called, called_param_names):
-        """Match the supplied argument names against the function parameters.
-        Warn if some argument names are not in the same order as they are in
-        the function signature.
-        """
-        # Check for called function being an object instance function
-        # If so, ignore the initial 'self' argument in the signature
-        try:
-            is_classdef = isinstance(called.parent, astroid.scoped_nodes.ClassDef)
-            if is_classdef and called_param_names[0] == "self":
-                called_param_names = called_param_names[1:]
-        except IndexError:
-            return
-
-        try:
-            # extract argument names, if they have names
-            calling_parg_names = [p.name for p in call_site.positional_arguments]
-
-            # Additionally get names of keyword arguments to use in a full match
-            # against parameters
-            calling_kwarg_names = [
-                arg.name for arg in call_site.keyword_arguments.values()
-            ]
-        except AttributeError:
-            # the type of arg does not provide a `.name`. In this case we
-            # stop checking for out-of-order arguments because it is only relevant
-            # for named variables.
-            return
-
-        # Don't check for ordering if there is an unmatched arg or param
-        arg_set = set(calling_parg_names) | set(calling_kwarg_names)
-        param_set = set(called_param_names)
-        if arg_set != param_set:
-            return
-
-        # Warn based on the equality of argument ordering
-        if calling_parg_names != called_param_names[: len(calling_parg_names)]:
-            self.add_message("arguments-out-of-order", node=node, args=())
-
-    # pylint: disable=too-many-branches,too-many-locals
-    @check_messages(*(list(MSGS.keys())))
-    def visit_call(self, node):
-        """check that called functions/methods are inferred to callable objects,
-        and that the arguments passed to the function match the parameters in
-        the inferred function's definition
-        """
-        called = safe_infer(node.func)
-        # only function, generator and object defining __call__ are allowed
-        # Ignore instances of descriptors since astroid cannot properly handle them
-        # yet
-        if called and not called.callable():
-            if isinstance(called, astroid.Instance) and (
-                not has_known_bases(called)
-                or (
-                    called.parent is not None
-                    and isinstance(called.scope(), astroid.ClassDef)
-                    and "__get__" in called.locals
-                )
-            ):
-                # Don't emit if we can't make sure this object is callable.
-                pass
-            else:
-                self.add_message("not-callable", node=node, args=node.func.as_string())
-
-        self._check_uninferable_call(node)
-        try:
-            called, implicit_args, callable_name = _determine_callable(called)
-        except ValueError:
-            # Any error occurred during determining the function type, most of
-            # those errors are handled by different warnings.
-            return
-
-        if called.args.args is None:
-            # Built-in functions have no argument information.
-            return
-
-        if len(called.argnames()) != len(set(called.argnames())):
-            # Duplicate parameter name (see duplicate-argument).  We can't really
-            # make sense of the function call in this case, so just return.
-            return
-
-        # Build the set of keyword arguments, checking for duplicate keywords,
-        # and count the positional arguments.
-        call_site = astroid.arguments.CallSite.from_call(node)
-
-        # Warn about duplicated keyword arguments, such as `f=24, **{'f': 24}`
-        for keyword in call_site.duplicated_keywords:
-            self.add_message("repeated-keyword", node=node, args=(keyword,))
-
-        if call_site.has_invalid_arguments() or call_site.has_invalid_keywords():
-            # Can't make sense of this.
-            return
-
-        # Has the function signature changed in ways we cannot reliably detect?
-        if hasattr(called, "decorators") and decorated_with(
-            called, self.config.signature_mutators
-        ):
-            return
-
-        num_positional_args = len(call_site.positional_arguments)
-        keyword_args = list(call_site.keyword_arguments.keys())
-        overload_function = is_overload_stub(called)
-
-        # Determine if we don't have a context for our call and we use variadics.
-        node_scope = node.scope()
-        if isinstance(node_scope, (astroid.Lambda, astroid.FunctionDef)):
-            has_no_context_positional_variadic = _no_context_variadic_positional(
-                node, node_scope
-            )
-            has_no_context_keywords_variadic = _no_context_variadic_keywords(
-                node, node_scope
-            )
-        else:
-            has_no_context_positional_variadic = (
-                has_no_context_keywords_variadic
-            ) = False
-
-        # These are coming from the functools.partial implementation in astroid
-        already_filled_positionals = getattr(called, "filled_positionals", 0)
-        already_filled_keywords = getattr(called, "filled_keywords", {})
-
-        keyword_args += list(already_filled_keywords)
-        num_positional_args += implicit_args + already_filled_positionals
-
-        # Analyze the list of formal parameters.
-        args = list(itertools.chain(called.args.posonlyargs or (), called.args.args))
-        num_mandatory_parameters = len(args) - len(called.args.defaults)
-        parameters = []
-        parameter_name_to_index = {}
-        for i, arg in enumerate(args):
-            if isinstance(arg, astroid.Tuple):
-                name = None
-                # Don't store any parameter names within the tuple, since those
-                # are not assignable from keyword arguments.
-            else:
-                assert isinstance(arg, astroid.AssignName)
-                # This occurs with:
-                #    def f( (a), (b) ): pass
-                name = arg.name
-                parameter_name_to_index[name] = i
-            if i >= num_mandatory_parameters:
-                defval = called.args.defaults[i - num_mandatory_parameters]
-            else:
-                defval = None
-            parameters.append([(name, defval), False])
-
-        kwparams = {}
-        for i, arg in enumerate(called.args.kwonlyargs):
-            if isinstance(arg, astroid.Keyword):
-                name = arg.arg
-            else:
-                assert isinstance(arg, astroid.AssignName)
-                name = arg.name
-            kwparams[name] = [called.args.kw_defaults[i], False]
-
-        self._check_argument_order(
-            node, call_site, called, [p[0][0] for p in parameters]
-        )
-
-        # 1. Match the positional arguments.
-        for i in range(num_positional_args):
-            if i < len(parameters):
-                parameters[i][1] = True
-            elif called.args.vararg is not None:
-                # The remaining positional arguments get assigned to the *args
-                # parameter.
-                break
-            else:
-                if not overload_function:
-                    # Too many positional arguments.
-                    self.add_message(
-                        "too-many-function-args", node=node, args=(callable_name,)
-                    )
-                    break
-
-        # 2. Match the keyword arguments.
-        for keyword in keyword_args:
-            if keyword in parameter_name_to_index:
-                i = parameter_name_to_index[keyword]
-                if parameters[i][1]:
-                    # Duplicate definition of function parameter.
-
-                    # Might be too hardcoded, but this can actually
-                    # happen when using str.format and `self` is passed
-                    # by keyword argument, as in `.format(self=self)`.
-                    # It's perfectly valid to so, so we're just skipping
-                    # it if that's the case.
-                    if not (keyword == "self" and called.qname() in STR_FORMAT):
-                        self.add_message(
-                            "redundant-keyword-arg",
-                            node=node,
-                            args=(keyword, callable_name),
-                        )
-                else:
-                    parameters[i][1] = True
-            elif keyword in kwparams:
-                if kwparams[keyword][1]:
-                    # Duplicate definition of function parameter.
-                    self.add_message(
-                        "redundant-keyword-arg",
-                        node=node,
-                        args=(keyword, callable_name),
-                    )
-                else:
-                    kwparams[keyword][1] = True
-            elif called.args.kwarg is not None:
-                # The keyword argument gets assigned to the **kwargs parameter.
-                pass
-            elif not overload_function:
-                # Unexpected keyword argument.
-                self.add_message(
-                    "unexpected-keyword-arg", node=node, args=(keyword, callable_name)
-                )
-
-        # 3. Match the **kwargs, if any.
-        if node.kwargs:
-            for i, [(name, defval), assigned] in enumerate(parameters):
-                # Assume that *kwargs provides values for all remaining
-                # unassigned named parameters.
-                if name is not None:
-                    parameters[i][1] = True
-                else:
-                    # **kwargs can't assign to tuples.
-                    pass
-
-        # Check that any parameters without a default have been assigned
-        # values.
-        for [(name, defval), assigned] in parameters:
-            if (defval is None) and not assigned:
-                if name is None:
-                    display_name = "<tuple>"
-                else:
-                    display_name = repr(name)
-                if not has_no_context_positional_variadic and not overload_function:
-                    self.add_message(
-                        "no-value-for-parameter",
-                        node=node,
-                        args=(display_name, callable_name),
-                    )
-
-        for name in kwparams:
-            defval, assigned = kwparams[name]
-            if defval is None and not assigned and not has_no_context_keywords_variadic:
-                self.add_message("missing-kwoa", node=node, args=(name, callable_name))
-
-    @check_messages("invalid-sequence-index")
-    def visit_extslice(self, node):
-        # Check extended slice objects as if they were used as a sequence
-        # index to check if the object being sliced can support them
-        return self.visit_index(node)
-
-    @check_messages("invalid-sequence-index")
-    def visit_index(self, node):
-        if not node.parent or not hasattr(node.parent, "value"):
-            return None
-        # Look for index operations where the parent is a sequence type.
-        # If the types can be determined, only allow indices to be int,
-        # slice or instances with __index__.
-        parent_type = safe_infer(node.parent.value)
-        if not isinstance(
-            parent_type, (astroid.ClassDef, astroid.Instance)
-        ) or not has_known_bases(parent_type):
-            return None
-
-        # Determine what method on the parent this index will use
-        # The parent of this node will be a Subscript, and the parent of that
-        # node determines if the Subscript is a get, set, or delete operation.
-        if node.parent.ctx is astroid.Store:
-            methodname = "__setitem__"
-        elif node.parent.ctx is astroid.Del:
-            methodname = "__delitem__"
-        else:
-            methodname = "__getitem__"
-
-        # Check if this instance's __getitem__, __setitem__, or __delitem__, as
-        # appropriate to the statement, is implemented in a builtin sequence
-        # type. This way we catch subclasses of sequence types but skip classes
-        # that override __getitem__ and which may allow non-integer indices.
-        try:
-            methods = dunder_lookup.lookup(parent_type, methodname)
-            if methods is astroid.Uninferable:
-                return None
-            itemmethod = methods[0]
-        except (
-            exceptions.NotFoundError,
-            exceptions.AttributeInferenceError,
-            IndexError,
-        ):
-            return None
-
-        if (
-            not isinstance(itemmethod, astroid.FunctionDef)
-            or itemmethod.root().name != BUILTINS
-            or not itemmethod.parent
-            or itemmethod.parent.name not in SEQUENCE_TYPES
-        ):
-            return None
-
-        # For ExtSlice objects coming from visit_extslice, no further
-        # inference is necessary, since if we got this far the ExtSlice
-        # is an error.
-        if isinstance(node, astroid.ExtSlice):
-            index_type = node
-        else:
-            index_type = safe_infer(node)
-        if index_type is None or index_type is astroid.Uninferable:
-            return None
-        # Constants must be of type int
-        if isinstance(index_type, astroid.Const):
-            if isinstance(index_type.value, int):
-                return None
-        # Instance values must be int, slice, or have an __index__ method
-        elif isinstance(index_type, astroid.Instance):
-            if index_type.pytype() in (BUILTINS + ".int", BUILTINS + ".slice"):
-                return None
-            try:
-                index_type.getattr("__index__")
-                return None
-            except exceptions.NotFoundError:
-                pass
-        elif isinstance(index_type, astroid.Slice):
-            # Delegate to visit_slice. A slice can be present
-            # here after inferring the index node, which could
-            # be a `slice(...)` call for instance.
-            return self.visit_slice(index_type)
-
-        # Anything else is an error
-        self.add_message("invalid-sequence-index", node=node)
-        return None
-
-    @check_messages("invalid-slice-index")
-    def visit_slice(self, node):
-        # Check the type of each part of the slice
-        invalid_slices = 0
-        for index in (node.lower, node.upper, node.step):
-            if index is None:
-                continue
-
-            index_type = safe_infer(index)
-            if index_type is None or index_type is astroid.Uninferable:
-                continue
-
-            # Constants must of type int or None
-            if isinstance(index_type, astroid.Const):
-                if isinstance(index_type.value, (int, type(None))):
-                    continue
-            # Instance values must be of type int, None or an object
-            # with __index__
-            elif isinstance(index_type, astroid.Instance):
-                if index_type.pytype() in (BUILTINS + ".int", BUILTINS + ".NoneType"):
-                    continue
-
-                try:
-                    index_type.getattr("__index__")
-                    return
-                except exceptions.NotFoundError:
-                    pass
-            invalid_slices += 1
-
-        if not invalid_slices:
-            return
-
-        # Anything else is an error, unless the object that is indexed
-        # is a custom object, which knows how to handle this kind of slices
-        parent = node.parent
-        if isinstance(parent, astroid.ExtSlice):
-            parent = parent.parent
-        if isinstance(parent, astroid.Subscript):
-            inferred = safe_infer(parent.value)
-            if inferred is None or inferred is astroid.Uninferable:
-                # Don't know what this is
-                return
-            known_objects = (
-                astroid.List,
-                astroid.Dict,
-                astroid.Tuple,
-                astroid.objects.FrozenSet,
-                astroid.Set,
-            )
-            if not isinstance(inferred, known_objects):
-                # Might be an instance that knows how to handle this slice object
-                return
-        for _ in range(invalid_slices):
-            self.add_message("invalid-slice-index", node=node)
-
-    @check_messages("not-context-manager")
-    def visit_with(self, node):
-        for ctx_mgr, _ in node.items:
-            context = astroid.context.InferenceContext()
-            inferred = safe_infer(ctx_mgr, context=context)
-            if inferred is None or inferred is astroid.Uninferable:
-                continue
-
-            if isinstance(inferred, bases.Generator):
-                # Check if we are dealing with a function decorated
-                # with contextlib.contextmanager.
-                if decorated_with(
-                    inferred.parent, self.config.contextmanager_decorators
-                ):
-                    continue
-                # If the parent of the generator is not the context manager itself,
-                # that means that it could have been returned from another
-                # function which was the real context manager.
-                # The following approach is more of a hack rather than a real
-                # solution: walk all the inferred statements for the
-                # given *ctx_mgr* and if you find one function scope
-                # which is decorated, consider it to be the real
-                # manager and give up, otherwise emit not-context-manager.
-                # See the test file for not_context_manager for a couple
-                # of self explaining tests.
-
-                # Retrieve node from all previusly visited nodes in the the inference history
-                context_path_names = filter(None, _unflatten(context.path))
-                inferred_paths = _flatten_container(
-                    safe_infer(path) for path in context_path_names
-                )
-                for inferred_path in inferred_paths:
-                    if not inferred_path:
-                        continue
-                    scope = inferred_path.scope()
-                    if not isinstance(scope, astroid.FunctionDef):
-                        continue
-                    if decorated_with(scope, self.config.contextmanager_decorators):
-                        break
-                else:
-                    self.add_message(
-                        "not-context-manager", node=node, args=(inferred.name,)
-                    )
-            else:
-                try:
-                    inferred.getattr("__enter__")
-                    inferred.getattr("__exit__")
-                except exceptions.NotFoundError:
-                    if isinstance(inferred, astroid.Instance):
-                        # If we do not know the bases of this class,
-                        # just skip it.
-                        if not has_known_bases(inferred):
-                            continue
-                        # Just ignore mixin classes.
-                        if self.config.ignore_mixin_members:
-                            if inferred.name[-5:].lower() == "mixin":
-                                continue
-
-                    self.add_message(
-                        "not-context-manager", node=node, args=(inferred.name,)
-                    )
-
-    @check_messages("invalid-unary-operand-type")
-    def visit_unaryop(self, node):
-        """Detect TypeErrors for unary operands."""
-
-        for error in node.type_errors():
-            # Let the error customize its output.
-            self.add_message("invalid-unary-operand-type", args=str(error), node=node)
-
-    @check_messages("unsupported-binary-operation")
-    def _visit_binop(self, node):
-        """Detect TypeErrors for binary arithmetic operands."""
-        self._check_binop_errors(node)
-
-    @check_messages("unsupported-binary-operation")
-    def _visit_augassign(self, node):
-        """Detect TypeErrors for augmented binary arithmetic operands."""
-        self._check_binop_errors(node)
-
-    def _check_binop_errors(self, node):
-        for error in node.type_errors():
-            # Let the error customize its output.
-            if any(
-                isinstance(obj, astroid.ClassDef) and not has_known_bases(obj)
-                for obj in (error.left_type, error.right_type)
-            ):
-                continue
-            self.add_message("unsupported-binary-operation", args=str(error), node=node)
-
-    def _check_membership_test(self, node):
-        if is_inside_abstract_class(node):
-            return
-        if is_comprehension(node):
-            return
-        inferred = safe_infer(node)
-        if inferred is None or inferred is astroid.Uninferable:
-            return
-        if not supports_membership_test(inferred):
-            self.add_message(
-                "unsupported-membership-test", args=node.as_string(), node=node
-            )
-
-    @check_messages("unsupported-membership-test")
-    def visit_compare(self, node):
-        if len(node.ops) != 1:
-            return
-
-        op, right = node.ops[0]
-        if op in ["in", "not in"]:
-            self._check_membership_test(right)
-
-    @check_messages(
-        "unsubscriptable-object",
-        "unsupported-assignment-operation",
-        "unsupported-delete-operation",
-        "unhashable-dict-key",
-    )
-    def visit_subscript(self, node):
-        supported_protocol = None
-        if isinstance(node.value, (astroid.ListComp, astroid.DictComp)):
-            return
-
-        if isinstance(node.value, astroid.Dict):
-            # Assert dict key is hashable
-            inferred = safe_infer(node.slice.value)
-            if inferred not in (None, astroid.Uninferable):
-                try:
-                    hash_fn = next(inferred.igetattr("__hash__"))
-                except astroid.InferenceError:
-                    pass
-                else:
-                    if getattr(hash_fn, "value", True) is None:
-                        self.add_message("unhashable-dict-key", node=node.value)
-
-        if node.ctx == astroid.Load:
-            supported_protocol = supports_getitem
-            msg = "unsubscriptable-object"
-        elif node.ctx == astroid.Store:
-            supported_protocol = supports_setitem
-            msg = "unsupported-assignment-operation"
-        elif node.ctx == astroid.Del:
-            supported_protocol = supports_delitem
-            msg = "unsupported-delete-operation"
-
-        if isinstance(node.value, astroid.SetComp):
-            self.add_message(msg, args=node.value.as_string(), node=node.value)
-            return
-
-        if is_inside_abstract_class(node):
-            return
-
-        inferred = safe_infer(node.value)
-        if inferred is None or inferred is astroid.Uninferable:
-            return
-
-        if not supported_protocol(inferred):
-            self.add_message(msg, args=node.value.as_string(), node=node.value)
-
-    @check_messages("dict-items-missing-iter")
-    def visit_for(self, node):
-        if not isinstance(node.target, astroid.node_classes.Tuple):
-            # target is not a tuple
-            return
-        if not len(node.target.elts) == 2:
-            # target is not a tuple of two elements
-            return
-
-        iterable = node.iter
-        if not isinstance(iterable, astroid.node_classes.Name):
-            # it's not a bare variable
-            return
-
-        inferred = safe_infer(iterable)
-        if not inferred:
-            return
-        if not isinstance(inferred, astroid.node_classes.Dict):
-            # the iterable is not a dict
-            return
-
-        self.add_message("dict-iter-missing-items", node=node)
-
-
-class IterableChecker(BaseChecker):
-    """
-    Checks for non-iterables used in an iterable context.
-    Contexts include:
-    - for-statement
-    - starargs in function call
-    - `yield from`-statement
-    - list, dict and set comprehensions
-    - generator expressions
-    Also checks for non-mappings in function call kwargs.
-    """
-
-    __implements__ = (IAstroidChecker,)
-    name = "typecheck"
-
-    msgs = {
-        "E1133": (
-            "Non-iterable value %s is used in an iterating context",
-            "not-an-iterable",
-            "Used when a non-iterable value is used in place where "
-            "iterable is expected",
-        ),
-        "E1134": (
-            "Non-mapping value %s is used in a mapping context",
-            "not-a-mapping",
-            "Used when a non-mapping value is used in place where "
-            "mapping is expected",
-        ),
-    }
-
-    @staticmethod
-    def _is_asyncio_coroutine(node):
-        if not isinstance(node, astroid.Call):
-            return False
-
-        inferred_func = safe_infer(node.func)
-        if not isinstance(inferred_func, astroid.FunctionDef):
-            return False
-        if not inferred_func.decorators:
-            return False
-        for decorator in inferred_func.decorators.nodes:
-            inferred_decorator = safe_infer(decorator)
-            if not isinstance(inferred_decorator, astroid.FunctionDef):
-                continue
-            if inferred_decorator.qname() != ASYNCIO_COROUTINE:
-                continue
-            return True
-        return False
-
-    def _check_iterable(self, node, check_async=False):
-        if is_inside_abstract_class(node) or is_comprehension(node):
-            return
-        inferred = safe_infer(node)
-        if not inferred:
-            return
-        if not is_iterable(inferred, check_async=check_async):
-            self.add_message("not-an-iterable", args=node.as_string(), node=node)
-
-    def _check_mapping(self, node):
-        if is_inside_abstract_class(node):
-            return
-        if isinstance(node, astroid.DictComp):
-            return
-        inferred = safe_infer(node)
-        if inferred is None or inferred is astroid.Uninferable:
-            return
-        if not is_mapping(inferred):
-            self.add_message("not-a-mapping", args=node.as_string(), node=node)
-
-    @check_messages("not-an-iterable")
-    def visit_for(self, node):
-        self._check_iterable(node.iter)
-
-    @check_messages("not-an-iterable")
-    def visit_asyncfor(self, node):
-        self._check_iterable(node.iter, check_async=True)
-
-    @check_messages("not-an-iterable")
-    def visit_yieldfrom(self, node):
-        if self._is_asyncio_coroutine(node.value):
-            return
-        self._check_iterable(node.value)
-
-    @check_messages("not-an-iterable", "not-a-mapping")
-    def visit_call(self, node):
-        for stararg in node.starargs:
-            self._check_iterable(stararg.value)
-        for kwarg in node.kwargs:
-            self._check_mapping(kwarg.value)
-
-    @check_messages("not-an-iterable")
-    def visit_listcomp(self, node):
-        for gen in node.generators:
-            self._check_iterable(gen.iter, check_async=gen.is_async)
-
-    @check_messages("not-an-iterable")
-    def visit_dictcomp(self, node):
-        for gen in node.generators:
-            self._check_iterable(gen.iter, check_async=gen.is_async)
-
-    @check_messages("not-an-iterable")
-    def visit_setcomp(self, node):
-        for gen in node.generators:
-            self._check_iterable(gen.iter, check_async=gen.is_async)
-
-    @check_messages("not-an-iterable")
-    def visit_generatorexp(self, node):
-        for gen in node.generators:
-            self._check_iterable(gen.iter, check_async=gen.is_async)
-
-
-def register(linter):
-    """required method to auto register this checker """
-    linter.register_checker(TypeChecker(linter))
-    linter.register_checker(IterableChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/checkers/utils.py b/venv/Lib/site-packages/pylint/checkers/utils.py
deleted file mode 100644
index 2a6820a..0000000
--- a/venv/Lib/site-packages/pylint/checkers/utils.py
+++ /dev/null
@@ -1,1253 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2007, 2009-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2009 Mads Kiilerich <mads@kiilerich.com>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Ricardo Gemignani <ricardo.gemignani@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Radu Ciorba <radu@devrandom.ro>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016, 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016-2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016-2017 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2016 Brian C. Lane <bcl@redhat.com>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 ttenhoeve-aa <ttenhoeve@appannie.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.guinta@protonmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-# Copyright (c) 2018 Brian Shaginaw <brian.shaginaw@warbyparker.com>
-# Copyright (c) 2018 Caio Carrara <ccarrara@redhat.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""some functions that may be useful for various checkers
-"""
-import builtins
-import itertools
-import numbers
-import re
-import string
-from functools import lru_cache, partial
-from typing import Callable, Dict, Iterable, List, Match, Optional, Set, Tuple, Union
-
-import astroid
-from astroid import bases as _bases
-from astroid import helpers, scoped_nodes
-from astroid.exceptions import _NonDeducibleTypeHierarchy
-
-import _string  # pylint: disable=wrong-import-position, wrong-import-order
-
-BUILTINS_NAME = builtins.__name__
-COMP_NODE_TYPES = (
-    astroid.ListComp,
-    astroid.SetComp,
-    astroid.DictComp,
-    astroid.GeneratorExp,
-)
-EXCEPTIONS_MODULE = "builtins"
-ABC_METHODS = {
-    "abc.abstractproperty",
-    "abc.abstractmethod",
-    "abc.abstractclassmethod",
-    "abc.abstractstaticmethod",
-}
-TYPING_PROTOCOLS = frozenset({"typing.Protocol", "typing_extensions.Protocol"})
-ITER_METHOD = "__iter__"
-AITER_METHOD = "__aiter__"
-NEXT_METHOD = "__next__"
-GETITEM_METHOD = "__getitem__"
-CLASS_GETITEM_METHOD = "__class_getitem__"
-SETITEM_METHOD = "__setitem__"
-DELITEM_METHOD = "__delitem__"
-CONTAINS_METHOD = "__contains__"
-KEYS_METHOD = "keys"
-
-# Dictionary which maps the number of expected parameters a
-# special method can have to a set of special methods.
-# The following keys are used to denote the parameters restrictions:
-#
-# * None: variable number of parameters
-# * number: exactly that number of parameters
-# * tuple: this are the odd ones. Basically it means that the function
-#          can work with any number of arguments from that tuple,
-#          although it's best to implement it in order to accept
-#          all of them.
-_SPECIAL_METHODS_PARAMS = {
-    None: ("__new__", "__init__", "__call__"),
-    0: (
-        "__del__",
-        "__repr__",
-        "__str__",
-        "__bytes__",
-        "__hash__",
-        "__bool__",
-        "__dir__",
-        "__len__",
-        "__length_hint__",
-        "__iter__",
-        "__reversed__",
-        "__neg__",
-        "__pos__",
-        "__abs__",
-        "__invert__",
-        "__complex__",
-        "__int__",
-        "__float__",
-        "__neg__",
-        "__pos__",
-        "__abs__",
-        "__complex__",
-        "__int__",
-        "__float__",
-        "__index__",
-        "__enter__",
-        "__aenter__",
-        "__getnewargs_ex__",
-        "__getnewargs__",
-        "__getstate__",
-        "__reduce__",
-        "__copy__",
-        "__unicode__",
-        "__nonzero__",
-        "__await__",
-        "__aiter__",
-        "__anext__",
-        "__fspath__",
-    ),
-    1: (
-        "__format__",
-        "__lt__",
-        "__le__",
-        "__eq__",
-        "__ne__",
-        "__gt__",
-        "__ge__",
-        "__getattr__",
-        "__getattribute__",
-        "__delattr__",
-        "__delete__",
-        "__instancecheck__",
-        "__subclasscheck__",
-        "__getitem__",
-        "__missing__",
-        "__delitem__",
-        "__contains__",
-        "__add__",
-        "__sub__",
-        "__mul__",
-        "__truediv__",
-        "__floordiv__",
-        "__rfloordiv__",
-        "__mod__",
-        "__divmod__",
-        "__lshift__",
-        "__rshift__",
-        "__and__",
-        "__xor__",
-        "__or__",
-        "__radd__",
-        "__rsub__",
-        "__rmul__",
-        "__rtruediv__",
-        "__rmod__",
-        "__rdivmod__",
-        "__rpow__",
-        "__rlshift__",
-        "__rrshift__",
-        "__rand__",
-        "__rxor__",
-        "__ror__",
-        "__iadd__",
-        "__isub__",
-        "__imul__",
-        "__itruediv__",
-        "__ifloordiv__",
-        "__imod__",
-        "__ilshift__",
-        "__irshift__",
-        "__iand__",
-        "__ixor__",
-        "__ior__",
-        "__ipow__",
-        "__setstate__",
-        "__reduce_ex__",
-        "__deepcopy__",
-        "__cmp__",
-        "__matmul__",
-        "__rmatmul__",
-        "__div__",
-    ),
-    2: ("__setattr__", "__get__", "__set__", "__setitem__", "__set_name__"),
-    3: ("__exit__", "__aexit__"),
-    (0, 1): ("__round__",),
-}
-
-SPECIAL_METHODS_PARAMS = {
-    name: params
-    for params, methods in _SPECIAL_METHODS_PARAMS.items()
-    for name in methods  # type: ignore
-}
-PYMETHODS = set(SPECIAL_METHODS_PARAMS)
-
-
-class NoSuchArgumentError(Exception):
-    pass
-
-
-def is_inside_except(node):
-    """Returns true if node is inside the name of an except handler."""
-    current = node
-    while current and not isinstance(current.parent, astroid.ExceptHandler):
-        current = current.parent
-
-    return current and current is current.parent.name
-
-
-def is_inside_lambda(node: astroid.node_classes.NodeNG) -> bool:
-    """Return true if given node is inside lambda"""
-    parent = node.parent
-    while parent is not None:
-        if isinstance(parent, astroid.Lambda):
-            return True
-        parent = parent.parent
-    return False
-
-
-def get_all_elements(
-    node: astroid.node_classes.NodeNG
-) -> Iterable[astroid.node_classes.NodeNG]:
-    """Recursively returns all atoms in nested lists and tuples."""
-    if isinstance(node, (astroid.Tuple, astroid.List)):
-        for child in node.elts:
-            yield from get_all_elements(child)
-    else:
-        yield node
-
-
-def clobber_in_except(
-    node: astroid.node_classes.NodeNG
-) -> Tuple[bool, Optional[Tuple[str, str]]]:
-    """Checks if an assignment node in an except handler clobbers an existing
-    variable.
-
-    Returns (True, args for W0623) if assignment clobbers an existing variable,
-    (False, None) otherwise.
-    """
-    if isinstance(node, astroid.AssignAttr):
-        return True, (node.attrname, "object %r" % (node.expr.as_string(),))
-    if isinstance(node, astroid.AssignName):
-        name = node.name
-        if is_builtin(name):
-            return True, (name, "builtins")
-
-        stmts = node.lookup(name)[1]
-        if stmts and not isinstance(
-            stmts[0].assign_type(),
-            (astroid.Assign, astroid.AugAssign, astroid.ExceptHandler),
-        ):
-            return True, (name, "outer scope (line %s)" % stmts[0].fromlineno)
-    return False, None
-
-
-def is_super(node: astroid.node_classes.NodeNG) -> bool:
-    """return True if the node is referencing the "super" builtin function
-    """
-    if getattr(node, "name", None) == "super" and node.root().name == BUILTINS_NAME:
-        return True
-    return False
-
-
-def is_error(node: astroid.node_classes.NodeNG) -> bool:
-    """return true if the function does nothing but raising an exception"""
-    raises = False
-    returns = False
-    for child_node in node.nodes_of_class((astroid.Raise, astroid.Return)):
-        if isinstance(child_node, astroid.Raise):
-            raises = True
-        if isinstance(child_node, astroid.Return):
-            returns = True
-    return raises and not returns
-
-
-builtins = builtins.__dict__.copy()  # type: ignore
-SPECIAL_BUILTINS = ("__builtins__",)  # '__path__', '__file__')
-
-
-def is_builtin_object(node: astroid.node_classes.NodeNG) -> bool:
-    """Returns True if the given node is an object from the __builtin__ module."""
-    return node and node.root().name == BUILTINS_NAME
-
-
-def is_builtin(name: str) -> bool:
-    """return true if <name> could be considered as a builtin defined by python
-    """
-    return name in builtins or name in SPECIAL_BUILTINS  # type: ignore
-
-
-def is_defined_in_scope(
-    var_node: astroid.node_classes.NodeNG,
-    varname: str,
-    scope: astroid.node_classes.NodeNG,
-) -> bool:
-    if isinstance(scope, astroid.If):
-        for node in scope.body:
-            if (
-                isinstance(node, astroid.Assign)
-                and any(
-                    isinstance(target, astroid.AssignName) and target.name == varname
-                    for target in node.targets
-                )
-            ) or (isinstance(node, astroid.Nonlocal) and varname in node.names):
-                return True
-    elif isinstance(scope, (COMP_NODE_TYPES, astroid.For)):
-        for ass_node in scope.nodes_of_class(astroid.AssignName):
-            if ass_node.name == varname:
-                return True
-    elif isinstance(scope, astroid.With):
-        for expr, ids in scope.items:
-            if expr.parent_of(var_node):
-                break
-            if ids and isinstance(ids, astroid.AssignName) and ids.name == varname:
-                return True
-    elif isinstance(scope, (astroid.Lambda, astroid.FunctionDef)):
-        if scope.args.is_argument(varname):
-            # If the name is found inside a default value
-            # of a function, then let the search continue
-            # in the parent's tree.
-            if scope.args.parent_of(var_node):
-                try:
-                    scope.args.default_value(varname)
-                    scope = scope.parent
-                    is_defined_in_scope(var_node, varname, scope)
-                except astroid.NoDefault:
-                    pass
-            return True
-        if getattr(scope, "name", None) == varname:
-            return True
-    elif isinstance(scope, astroid.ExceptHandler):
-        if isinstance(scope.name, astroid.AssignName):
-            ass_node = scope.name
-            if ass_node.name == varname:
-                return True
-    return False
-
-
-def is_defined_before(var_node: astroid.node_classes.NodeNG) -> bool:
-    """return True if the variable node is defined by a parent node (list,
-    set, dict, or generator comprehension, lambda) or in a previous sibling
-    node on the same line (statement_defining ; statement_using)
-    """
-    varname = var_node.name
-    _node = var_node.parent
-    while _node:
-        if is_defined_in_scope(var_node, varname, _node):
-            return True
-        _node = _node.parent
-    # possibly multiple statements on the same line using semi colon separator
-    stmt = var_node.statement()
-    _node = stmt.previous_sibling()
-    lineno = stmt.fromlineno
-    while _node and _node.fromlineno == lineno:
-        for assign_node in _node.nodes_of_class(astroid.AssignName):
-            if assign_node.name == varname:
-                return True
-        for imp_node in _node.nodes_of_class((astroid.ImportFrom, astroid.Import)):
-            if varname in [name[1] or name[0] for name in imp_node.names]:
-                return True
-        _node = _node.previous_sibling()
-    return False
-
-
-def is_default_argument(node: astroid.node_classes.NodeNG) -> bool:
-    """return true if the given Name node is used in function or lambda
-    default argument's value
-    """
-    parent = node.scope()
-    if isinstance(parent, (astroid.FunctionDef, astroid.Lambda)):
-        for default_node in parent.args.defaults:
-            for default_name_node in default_node.nodes_of_class(astroid.Name):
-                if default_name_node is node:
-                    return True
-    return False
-
-
-def is_func_decorator(node: astroid.node_classes.NodeNG) -> bool:
-    """return true if the name is used in function decorator"""
-    parent = node.parent
-    while parent is not None:
-        if isinstance(parent, astroid.Decorators):
-            return True
-        if parent.is_statement or isinstance(
-            parent,
-            (astroid.Lambda, scoped_nodes.ComprehensionScope, scoped_nodes.ListComp),
-        ):
-            break
-        parent = parent.parent
-    return False
-
-
-def is_ancestor_name(
-    frame: astroid.node_classes.NodeNG, node: astroid.node_classes.NodeNG
-) -> bool:
-    """return True if `frame` is an astroid.Class node with `node` in the
-    subtree of its bases attribute
-    """
-    try:
-        bases = frame.bases
-    except AttributeError:
-        return False
-    for base in bases:
-        if node in base.nodes_of_class(astroid.Name):
-            return True
-    return False
-
-
-def assign_parent(node: astroid.node_classes.NodeNG) -> astroid.node_classes.NodeNG:
-    """return the higher parent which is not an AssignName, Tuple or List node
-    """
-    while node and isinstance(node, (astroid.AssignName, astroid.Tuple, astroid.List)):
-        node = node.parent
-    return node
-
-
-def overrides_a_method(class_node: astroid.node_classes.NodeNG, name: str) -> bool:
-    """return True if <name> is a method overridden from an ancestor"""
-    for ancestor in class_node.ancestors():
-        if name in ancestor and isinstance(ancestor[name], astroid.FunctionDef):
-            return True
-    return False
-
-
-def check_messages(*messages: str) -> Callable:
-    """decorator to store messages that are handled by a checker method"""
-
-    def store_messages(func):
-        func.checks_msgs = messages
-        return func
-
-    return store_messages
-
-
-class IncompleteFormatString(Exception):
-    """A format string ended in the middle of a format specifier."""
-
-
-class UnsupportedFormatCharacter(Exception):
-    """A format character in a format string is not one of the supported
-    format characters."""
-
-    def __init__(self, index):
-        Exception.__init__(self, index)
-        self.index = index
-
-
-def parse_format_string(
-    format_string: str
-) -> Tuple[Set[str], int, Dict[str, str], List[str]]:
-    """Parses a format string, returning a tuple of (keys, num_args), where keys
-    is the set of mapping keys in the format string, and num_args is the number
-    of arguments required by the format string.  Raises
-    IncompleteFormatString or UnsupportedFormatCharacter if a
-    parse error occurs."""
-    keys = set()
-    key_types = dict()
-    pos_types = []
-    num_args = 0
-
-    def next_char(i):
-        i += 1
-        if i == len(format_string):
-            raise IncompleteFormatString
-        return (i, format_string[i])
-
-    i = 0
-    while i < len(format_string):
-        char = format_string[i]
-        if char == "%":
-            i, char = next_char(i)
-            # Parse the mapping key (optional).
-            key = None
-            if char == "(":
-                depth = 1
-                i, char = next_char(i)
-                key_start = i
-                while depth != 0:
-                    if char == "(":
-                        depth += 1
-                    elif char == ")":
-                        depth -= 1
-                    i, char = next_char(i)
-                key_end = i - 1
-                key = format_string[key_start:key_end]
-
-            # Parse the conversion flags (optional).
-            while char in "#0- +":
-                i, char = next_char(i)
-            # Parse the minimum field width (optional).
-            if char == "*":
-                num_args += 1
-                i, char = next_char(i)
-            else:
-                while char in string.digits:
-                    i, char = next_char(i)
-            # Parse the precision (optional).
-            if char == ".":
-                i, char = next_char(i)
-                if char == "*":
-                    num_args += 1
-                    i, char = next_char(i)
-                else:
-                    while char in string.digits:
-                        i, char = next_char(i)
-            # Parse the length modifier (optional).
-            if char in "hlL":
-                i, char = next_char(i)
-            # Parse the conversion type (mandatory).
-            flags = "diouxXeEfFgGcrs%a"
-            if char not in flags:
-                raise UnsupportedFormatCharacter(i)
-            if key:
-                keys.add(key)
-                key_types[key] = char
-            elif char != "%":
-                num_args += 1
-                pos_types.append(char)
-        i += 1
-    return keys, num_args, key_types, pos_types
-
-
-def split_format_field_names(format_string) -> Tuple[str, Iterable[Tuple[bool, str]]]:
-    try:
-        return _string.formatter_field_name_split(format_string)
-    except ValueError:
-        raise IncompleteFormatString()
-
-
-def collect_string_fields(format_string) -> Iterable[Optional[str]]:
-    """ Given a format string, return an iterator
-    of all the valid format fields. It handles nested fields
-    as well.
-    """
-    formatter = string.Formatter()
-    try:
-        parseiterator = formatter.parse(format_string)
-        for result in parseiterator:
-            if all(item is None for item in result[1:]):
-                # not a replacement format
-                continue
-            name = result[1]
-            nested = result[2]
-            yield name
-            if nested:
-                for field in collect_string_fields(nested):
-                    yield field
-    except ValueError as exc:
-        # Probably the format string is invalid.
-        if exc.args[0].startswith("cannot switch from manual"):
-            # On Jython, parsing a string with both manual
-            # and automatic positions will fail with a ValueError,
-            # while on CPython it will simply return the fields,
-            # the validation being done in the interpreter (?).
-            # We're just returning two mixed fields in order
-            # to trigger the format-combined-specification check.
-            yield ""
-            yield "1"
-            return
-        raise IncompleteFormatString(format_string)
-
-
-def parse_format_method_string(
-    format_string: str
-) -> Tuple[List[Tuple[str, List[Tuple[bool, str]]]], int, int]:
-    """
-    Parses a PEP 3101 format string, returning a tuple of
-    (keyword_arguments, implicit_pos_args_cnt, explicit_pos_args),
-    where keyword_arguments is the set of mapping keys in the format string, implicit_pos_args_cnt
-    is the number of arguments required by the format string and
-    explicit_pos_args is the number of arguments passed with the position.
-    """
-    keyword_arguments = []
-    implicit_pos_args_cnt = 0
-    explicit_pos_args = set()
-    for name in collect_string_fields(format_string):
-        if name and str(name).isdigit():
-            explicit_pos_args.add(str(name))
-        elif name:
-            keyname, fielditerator = split_format_field_names(name)
-            if isinstance(keyname, numbers.Number):
-                # In Python 2 it will return long which will lead
-                # to different output between 2 and 3
-                explicit_pos_args.add(str(keyname))
-                keyname = int(keyname)
-            try:
-                keyword_arguments.append((keyname, list(fielditerator)))
-            except ValueError:
-                raise IncompleteFormatString()
-        else:
-            implicit_pos_args_cnt += 1
-    return keyword_arguments, implicit_pos_args_cnt, len(explicit_pos_args)
-
-
-def is_attr_protected(attrname: str) -> bool:
-    """return True if attribute name is protected (start with _ and some other
-    details), False otherwise.
-    """
-    return (
-        attrname[0] == "_"
-        and attrname != "_"
-        and not (attrname.startswith("__") and attrname.endswith("__"))
-    )
-
-
-def node_frame_class(node: astroid.node_classes.NodeNG) -> Optional[astroid.ClassDef]:
-    """Return the class that is wrapping the given node
-
-    The function returns a class for a method node (or a staticmethod or a
-    classmethod), otherwise it returns `None`.
-    """
-    klass = node.frame()
-
-    while klass is not None and not isinstance(klass, astroid.ClassDef):
-        if klass.parent is None:
-            klass = None
-        else:
-            klass = klass.parent.frame()
-
-    return klass
-
-
-def is_attr_private(attrname: str) -> Optional[Match[str]]:
-    """Check that attribute name is private (at least two leading underscores,
-    at most one trailing underscore)
-    """
-    regex = re.compile("^_{2,}.*[^_]+_?$")
-    return regex.match(attrname)
-
-
-def get_argument_from_call(
-    call_node: astroid.Call, position: int = None, keyword: str = None
-) -> astroid.Name:
-    """Returns the specified argument from a function call.
-
-    :param astroid.Call call_node: Node representing a function call to check.
-    :param int position: position of the argument.
-    :param str keyword: the keyword of the argument.
-
-    :returns: The node representing the argument, None if the argument is not found.
-    :rtype: astroid.Name
-    :raises ValueError: if both position and keyword are None.
-    :raises NoSuchArgumentError: if no argument at the provided position or with
-    the provided keyword.
-    """
-    if position is None and keyword is None:
-        raise ValueError("Must specify at least one of: position or keyword.")
-    if position is not None:
-        try:
-            return call_node.args[position]
-        except IndexError:
-            pass
-    if keyword and call_node.keywords:
-        for arg in call_node.keywords:
-            if arg.arg == keyword:
-                return arg.value
-
-    raise NoSuchArgumentError
-
-
-def inherit_from_std_ex(node: astroid.node_classes.NodeNG) -> bool:
-    """
-    Return true if the given class node is subclass of
-    exceptions.Exception.
-    """
-    ancestors = node.ancestors() if hasattr(node, "ancestors") else []
-    for ancestor in itertools.chain([node], ancestors):
-        if (
-            ancestor.name in ("Exception", "BaseException")
-            and ancestor.root().name == EXCEPTIONS_MODULE
-        ):
-            return True
-    return False
-
-
-def error_of_type(handler: astroid.ExceptHandler, error_type) -> bool:
-    """
-    Check if the given exception handler catches
-    the given error_type.
-
-    The *handler* parameter is a node, representing an ExceptHandler node.
-    The *error_type* can be an exception, such as AttributeError,
-    the name of an exception, or it can be a tuple of errors.
-    The function will return True if the handler catches any of the
-    given errors.
-    """
-
-    def stringify_error(error):
-        if not isinstance(error, str):
-            return error.__name__
-        return error
-
-    if not isinstance(error_type, tuple):
-        error_type = (error_type,)  # type: ignore
-    expected_errors = {stringify_error(error) for error in error_type}  # type: ignore
-    if not handler.type:
-        return True
-    return handler.catch(expected_errors)
-
-
-def decorated_with_property(node: astroid.FunctionDef) -> bool:
-    """Detect if the given function node is decorated with a property. """
-    if not node.decorators:
-        return False
-    for decorator in node.decorators.nodes:
-        try:
-            if _is_property_decorator(decorator):
-                return True
-        except astroid.InferenceError:
-            pass
-    return False
-
-
-def _is_property_kind(node, *kinds):
-    if not isinstance(node, (astroid.UnboundMethod, astroid.FunctionDef)):
-        return False
-    if node.decorators:
-        for decorator in node.decorators.nodes:
-            if isinstance(decorator, astroid.Attribute) and decorator.attrname in kinds:
-                return True
-    return False
-
-
-def is_property_setter(node: astroid.FunctionDef) -> bool:
-    """Check if the given node is a property setter"""
-    return _is_property_kind(node, "setter")
-
-
-def is_property_setter_or_deleter(node: astroid.FunctionDef) -> bool:
-    """Check if the given node is either a property setter or a deleter"""
-    return _is_property_kind(node, "setter", "deleter")
-
-
-def _is_property_decorator(decorator: astroid.Name) -> bool:
-    for inferred in decorator.infer():
-        if isinstance(inferred, astroid.ClassDef):
-            if inferred.root().name == BUILTINS_NAME and inferred.name == "property":
-                return True
-            for ancestor in inferred.ancestors():
-                if (
-                    ancestor.name == "property"
-                    and ancestor.root().name == BUILTINS_NAME
-                ):
-                    return True
-    return False
-
-
-def decorated_with(
-    func: Union[astroid.FunctionDef, astroid.BoundMethod, astroid.UnboundMethod],
-    qnames: Iterable[str],
-) -> bool:
-    """Determine if the `func` node has a decorator with the qualified name `qname`."""
-    decorators = func.decorators.nodes if func.decorators else []
-    for decorator_node in decorators:
-        if isinstance(decorator_node, astroid.Call):
-            # We only want to infer the function name
-            decorator_node = decorator_node.func
-        try:
-            if any(
-                i is not None and i.qname() in qnames or i.name in qnames
-                for i in decorator_node.infer()
-            ):
-                return True
-        except astroid.InferenceError:
-            continue
-    return False
-
-
-@lru_cache(maxsize=1024)
-def unimplemented_abstract_methods(
-    node: astroid.node_classes.NodeNG, is_abstract_cb: astroid.FunctionDef = None
-) -> Dict[str, astroid.node_classes.NodeNG]:
-    """
-    Get the unimplemented abstract methods for the given *node*.
-
-    A method can be considered abstract if the callback *is_abstract_cb*
-    returns a ``True`` value. The check defaults to verifying that
-    a method is decorated with abstract methods.
-    The function will work only for new-style classes. For old-style
-    classes, it will simply return an empty dictionary.
-    For the rest of them, it will return a dictionary of abstract method
-    names and their inferred objects.
-    """
-    if is_abstract_cb is None:
-        is_abstract_cb = partial(decorated_with, qnames=ABC_METHODS)
-    visited = {}  # type: Dict[str, astroid.node_classes.NodeNG]
-    try:
-        mro = reversed(node.mro())
-    except NotImplementedError:
-        # Old style class, it will not have a mro.
-        return {}
-    except astroid.ResolveError:
-        # Probably inconsistent hierarchy, don'try
-        # to figure this out here.
-        return {}
-    for ancestor in mro:
-        for obj in ancestor.values():
-            inferred = obj
-            if isinstance(obj, astroid.AssignName):
-                inferred = safe_infer(obj)
-                if not inferred:
-                    # Might be an abstract function,
-                    # but since we don't have enough information
-                    # in order to take this decision, we're taking
-                    # the *safe* decision instead.
-                    if obj.name in visited:
-                        del visited[obj.name]
-                    continue
-                if not isinstance(inferred, astroid.FunctionDef):
-                    if obj.name in visited:
-                        del visited[obj.name]
-            if isinstance(inferred, astroid.FunctionDef):
-                # It's critical to use the original name,
-                # since after inferring, an object can be something
-                # else than expected, as in the case of the
-                # following assignment.
-                #
-                # class A:
-                #     def keys(self): pass
-                #     __iter__ = keys
-                abstract = is_abstract_cb(inferred)
-                if abstract:
-                    visited[obj.name] = inferred
-                elif not abstract and obj.name in visited:
-                    del visited[obj.name]
-    return visited
-
-
-def find_try_except_wrapper_node(
-    node: astroid.node_classes.NodeNG
-) -> Union[astroid.ExceptHandler, astroid.TryExcept]:
-    """Return the ExceptHandler or the TryExcept node in which the node is."""
-    current = node
-    ignores = (astroid.ExceptHandler, astroid.TryExcept)
-    while current and not isinstance(current.parent, ignores):
-        current = current.parent
-
-    if current and isinstance(current.parent, ignores):
-        return current.parent
-    return None
-
-
-def is_from_fallback_block(node: astroid.node_classes.NodeNG) -> bool:
-    """Check if the given node is from a fallback import block."""
-    context = find_try_except_wrapper_node(node)
-    if not context:
-        return False
-
-    if isinstance(context, astroid.ExceptHandler):
-        other_body = context.parent.body
-        handlers = context.parent.handlers
-    else:
-        other_body = itertools.chain.from_iterable(
-            handler.body for handler in context.handlers
-        )
-        handlers = context.handlers
-
-    has_fallback_imports = any(
-        isinstance(import_node, (astroid.ImportFrom, astroid.Import))
-        for import_node in other_body
-    )
-    ignores_import_error = _except_handlers_ignores_exception(handlers, ImportError)
-    return ignores_import_error or has_fallback_imports
-
-
-def _except_handlers_ignores_exception(
-    handlers: astroid.ExceptHandler, exception
-) -> bool:
-    func = partial(error_of_type, error_type=(exception,))
-    return any(map(func, handlers))
-
-
-def get_exception_handlers(
-    node: astroid.node_classes.NodeNG, exception=Exception
-) -> Optional[List[astroid.ExceptHandler]]:
-    """Return the collections of handlers handling the exception in arguments.
-
-    Args:
-        node (astroid.NodeNG): A node that is potentially wrapped in a try except.
-        exception (builtin.Exception or str): exception or name of the exception.
-
-    Returns:
-        list: the collection of handlers that are handling the exception or None.
-
-    """
-    context = find_try_except_wrapper_node(node)
-    if isinstance(context, astroid.TryExcept):
-        return [
-            handler for handler in context.handlers if error_of_type(handler, exception)
-        ]
-    return []
-
-
-def is_node_inside_try_except(node: astroid.Raise) -> bool:
-    """Check if the node is directly under a Try/Except statement.
-    (but not under an ExceptHandler!)
-
-    Args:
-        node (astroid.Raise): the node raising the exception.
-
-    Returns:
-        bool: True if the node is inside a try/except statement, False otherwise.
-    """
-    context = find_try_except_wrapper_node(node)
-    return isinstance(context, astroid.TryExcept)
-
-
-def node_ignores_exception(
-    node: astroid.node_classes.NodeNG, exception=Exception
-) -> bool:
-    """Check if the node is in a TryExcept which handles the given exception.
-
-    If the exception is not given, the function is going to look for bare
-    excepts.
-    """
-    managing_handlers = get_exception_handlers(node, exception)
-    if not managing_handlers:
-        return False
-    return any(managing_handlers)
-
-
-def class_is_abstract(node: astroid.ClassDef) -> bool:
-    """return true if the given class node should be considered as an abstract
-    class
-    """
-    for method in node.methods():
-        if method.parent.frame() is node:
-            if method.is_abstract(pass_is_abstract=False):
-                return True
-    return False
-
-
-def _supports_protocol_method(value: astroid.node_classes.NodeNG, attr: str) -> bool:
-    try:
-        attributes = value.getattr(attr)
-    except astroid.NotFoundError:
-        return False
-
-    first = attributes[0]
-    if isinstance(first, astroid.AssignName):
-        if isinstance(first.parent.value, astroid.Const):
-            return False
-    return True
-
-
-def is_comprehension(node: astroid.node_classes.NodeNG) -> bool:
-    comprehensions = (
-        astroid.ListComp,
-        astroid.SetComp,
-        astroid.DictComp,
-        astroid.GeneratorExp,
-    )
-    return isinstance(node, comprehensions)
-
-
-def _supports_mapping_protocol(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol_method(
-        value, GETITEM_METHOD
-    ) and _supports_protocol_method(value, KEYS_METHOD)
-
-
-def _supports_membership_test_protocol(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol_method(value, CONTAINS_METHOD)
-
-
-def _supports_iteration_protocol(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol_method(value, ITER_METHOD) or _supports_protocol_method(
-        value, GETITEM_METHOD
-    )
-
-
-def _supports_async_iteration_protocol(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol_method(value, AITER_METHOD)
-
-
-def _supports_getitem_protocol(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol_method(value, GETITEM_METHOD)
-
-
-def _supports_setitem_protocol(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol_method(value, SETITEM_METHOD)
-
-
-def _supports_delitem_protocol(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol_method(value, DELITEM_METHOD)
-
-
-def _is_abstract_class_name(name: str) -> bool:
-    lname = name.lower()
-    is_mixin = lname.endswith("mixin")
-    is_abstract = lname.startswith("abstract")
-    is_base = lname.startswith("base") or lname.endswith("base")
-    return is_mixin or is_abstract or is_base
-
-
-def is_inside_abstract_class(node: astroid.node_classes.NodeNG) -> bool:
-    while node is not None:
-        if isinstance(node, astroid.ClassDef):
-            if class_is_abstract(node):
-                return True
-            name = getattr(node, "name", None)
-            if name is not None and _is_abstract_class_name(name):
-                return True
-        node = node.parent
-    return False
-
-
-def _supports_protocol(
-    value: astroid.node_classes.NodeNG, protocol_callback: astroid.FunctionDef
-) -> bool:
-    if isinstance(value, astroid.ClassDef):
-        if not has_known_bases(value):
-            return True
-        # classobj can only be iterable if it has an iterable metaclass
-        meta = value.metaclass()
-        if meta is not None:
-            if protocol_callback(meta):
-                return True
-    if isinstance(value, astroid.BaseInstance):
-        if not has_known_bases(value):
-            return True
-        if value.has_dynamic_getattr():
-            return True
-        if protocol_callback(value):
-            return True
-
-    if (
-        isinstance(value, _bases.Proxy)
-        and isinstance(value._proxied, astroid.BaseInstance)
-        and has_known_bases(value._proxied)
-    ):
-        value = value._proxied
-        return protocol_callback(value)
-
-    return False
-
-
-def is_iterable(value: astroid.node_classes.NodeNG, check_async: bool = False) -> bool:
-    if check_async:
-        protocol_check = _supports_async_iteration_protocol
-    else:
-        protocol_check = _supports_iteration_protocol
-    return _supports_protocol(value, protocol_check)
-
-
-def is_mapping(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol(value, _supports_mapping_protocol)
-
-
-def supports_membership_test(value: astroid.node_classes.NodeNG) -> bool:
-    supported = _supports_protocol(value, _supports_membership_test_protocol)
-    return supported or is_iterable(value)
-
-
-def supports_getitem(value: astroid.node_classes.NodeNG) -> bool:
-    if isinstance(value, astroid.ClassDef):
-        if _supports_protocol_method(value, CLASS_GETITEM_METHOD):
-            return True
-    return _supports_protocol(value, _supports_getitem_protocol)
-
-
-def supports_setitem(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol(value, _supports_setitem_protocol)
-
-
-def supports_delitem(value: astroid.node_classes.NodeNG) -> bool:
-    return _supports_protocol(value, _supports_delitem_protocol)
-
-
-@lru_cache(maxsize=1024)
-def safe_infer(
-    node: astroid.node_classes.NodeNG, context=None
-) -> Optional[astroid.node_classes.NodeNG]:
-    """Return the inferred value for the given node.
-
-    Return None if inference failed or if there is some ambiguity (more than
-    one node has been inferred).
-    """
-    try:
-        inferit = node.infer(context=context)
-        value = next(inferit)
-    except astroid.InferenceError:
-        return None
-    try:
-        next(inferit)
-        return None  # None if there is ambiguity on the inferred node
-    except astroid.InferenceError:
-        return None  # there is some kind of ambiguity
-    except StopIteration:
-        return value
-
-
-def has_known_bases(klass: astroid.ClassDef, context=None) -> bool:
-    """Return true if all base classes of a class could be inferred."""
-    try:
-        return klass._all_bases_known
-    except AttributeError:
-        pass
-    for base in klass.bases:
-        result = safe_infer(base, context=context)
-        if (
-            not isinstance(result, astroid.ClassDef)
-            or result is klass
-            or not has_known_bases(result, context=context)
-        ):
-            klass._all_bases_known = False
-            return False
-    klass._all_bases_known = True
-    return True
-
-
-def is_none(node: astroid.node_classes.NodeNG) -> bool:
-    return (
-        node is None
-        or (isinstance(node, astroid.Const) and node.value is None)
-        or (isinstance(node, astroid.Name) and node.name == "None")
-    )
-
-
-def node_type(node: astroid.node_classes.NodeNG) -> Optional[type]:
-    """Return the inferred type for `node`
-
-    If there is more than one possible type, or if inferred type is Uninferable or None,
-    return None
-    """
-    # check there is only one possible type for the assign node. Else we
-    # don't handle it for now
-    types = set()
-    try:
-        for var_type in node.infer():
-            if var_type == astroid.Uninferable or is_none(var_type):
-                continue
-            types.add(var_type)
-            if len(types) > 1:
-                return None
-    except astroid.InferenceError:
-        return None
-    return types.pop() if types else None
-
-
-def is_registered_in_singledispatch_function(node: astroid.FunctionDef) -> bool:
-    """Check if the given function node is a singledispatch function."""
-
-    singledispatch_qnames = (
-        "functools.singledispatch",
-        "singledispatch.singledispatch",
-    )
-
-    if not isinstance(node, astroid.FunctionDef):
-        return False
-
-    decorators = node.decorators.nodes if node.decorators else []
-    for decorator in decorators:
-        # func.register are function calls
-        if not isinstance(decorator, astroid.Call):
-            continue
-
-        func = decorator.func
-        if not isinstance(func, astroid.Attribute) or func.attrname != "register":
-            continue
-
-        try:
-            func_def = next(func.expr.infer())
-        except astroid.InferenceError:
-            continue
-
-        if isinstance(func_def, astroid.FunctionDef):
-            # pylint: disable=redundant-keyword-arg; some flow inference goes wrong here
-            return decorated_with(func_def, singledispatch_qnames)
-
-    return False
-
-
-def get_node_last_lineno(node: astroid.node_classes.NodeNG) -> int:
-    """
-    Get the last lineno of the given node. For a simple statement this will just be node.lineno,
-    but for a node that has child statements (e.g. a method) this will be the lineno of the last
-    child statement recursively.
-    """
-    # 'finalbody' is always the last clause in a try statement, if present
-    if getattr(node, "finalbody", False):
-        return get_node_last_lineno(node.finalbody[-1])
-    # For if, while, and for statements 'orelse' is always the last clause.
-    # For try statements 'orelse' is the last in the absence of a 'finalbody'
-    if getattr(node, "orelse", False):
-        return get_node_last_lineno(node.orelse[-1])
-    # try statements have the 'handlers' last if there is no 'orelse' or 'finalbody'
-    if getattr(node, "handlers", False):
-        return get_node_last_lineno(node.handlers[-1])
-    # All compound statements have a 'body'
-    if getattr(node, "body", False):
-        return get_node_last_lineno(node.body[-1])
-    # Not a compound statement
-    return node.lineno
-
-
-def is_postponed_evaluation_enabled(node: astroid.node_classes.NodeNG) -> bool:
-    """Check if the postponed evaluation of annotations is enabled"""
-    name = "annotations"
-    module = node.root()
-    stmt = module.locals.get(name)
-    return (
-        stmt
-        and isinstance(stmt[0], astroid.ImportFrom)
-        and stmt[0].modname == "__future__"
-    )
-
-
-def is_subclass_of(child: astroid.ClassDef, parent: astroid.ClassDef) -> bool:
-    """
-    Check if first node is a subclass of second node.
-    :param child: Node to check for subclass.
-    :param parent: Node to check for superclass.
-    :returns: True if child is derived from parent. False otherwise.
-    """
-    if not all(isinstance(node, astroid.ClassDef) for node in (child, parent)):
-        return False
-
-    for ancestor in child.ancestors():
-        try:
-            if helpers.is_subtype(ancestor, parent):
-                return True
-        except _NonDeducibleTypeHierarchy:
-            continue
-    return False
-
-
-@lru_cache(maxsize=1024)
-def is_overload_stub(node: astroid.node_classes.NodeNG) -> bool:
-    """Check if a node if is a function stub decorated with typing.overload.
-
-    :param node: Node to check.
-    :returns: True if node is an overload function stub. False otherwise.
-    """
-    decorators = getattr(node, "decorators", None)
-    return bool(decorators and decorated_with(node, ["typing.overload", "overload"]))
-
-
-def is_protocol_class(cls: astroid.node_classes.NodeNG) -> bool:
-    """Check if the given node represents a protocol class
-
-    :param cls: The node to check
-    :returns: True if the node is a typing protocol class, false otherwise.
-    """
-    if not isinstance(cls, astroid.ClassDef):
-        return False
-
-    # Use .ancestors() since not all protocol classes can have
-    # their mro deduced.
-    return any(parent.qname() in TYPING_PROTOCOLS for parent in cls.ancestors())
diff --git a/venv/Lib/site-packages/pylint/checkers/variables.py b/venv/Lib/site-packages/pylint/checkers/variables.py
deleted file mode 100644
index e13f9b5..0000000
--- a/venv/Lib/site-packages/pylint/checkers/variables.py
+++ /dev/null
@@ -1,1987 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2009 Mads Kiilerich <mads@kiilerich.com>
-# Copyright (c) 2010 Daniel Harding <dharding@gmail.com>
-# Copyright (c) 2011-2014, 2017 Google, Inc.
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2013-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Ricardo Gemignani <ricardo.gemignani@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Dmitry Pribysh <dmand@yandex.ru>
-# Copyright (c) 2015 Radu Ciorba <radu@devrandom.ro>
-# Copyright (c) 2015 Simu Toni <simutoni@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016, 2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016, 2018 Jakub Wilk <jwilk@jwilk.net>
-# Copyright (c) 2016-2017 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2016-2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Grant Welch <gwelch925+github@gmail.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Dan Garrette <dhgarrette@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.guinta@protonmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Marianna Polatoglou <mpolatoglou@bloomberg.net>
-# Copyright (c) 2018 mar-chi-pan <mar.polatoglou@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""variables checkers for Python code
-"""
-import collections
-import copy
-import itertools
-import os
-import re
-from functools import lru_cache
-
-import astroid
-from astroid import decorators, modutils, objects
-from astroid.context import InferenceContext
-
-from pylint.checkers import BaseChecker, utils
-from pylint.checkers.utils import is_postponed_evaluation_enabled
-from pylint.interfaces import HIGH, INFERENCE, INFERENCE_FAILURE, IAstroidChecker
-from pylint.utils import get_global_option
-
-SPECIAL_OBJ = re.compile("^_{2}[a-z]+_{2}$")
-FUTURE = "__future__"
-# regexp for ignored argument name
-IGNORED_ARGUMENT_NAMES = re.compile("_.*|^ignored_|^unused_")
-# In Python 3.7 abc has a Python implementation which is preferred
-# by astroid. Unfortunately this also messes up our explicit checks
-# for `abc`
-METACLASS_NAME_TRANSFORMS = {"_py_abc": "abc"}
-TYPING_TYPE_CHECKS_GUARDS = frozenset({"typing.TYPE_CHECKING", "TYPE_CHECKING"})
-BUILTIN_RANGE = "builtins.range"
-TYPING_MODULE = "typing"
-TYPING_NAMES = frozenset(
-    {
-        "Any",
-        "Callable",
-        "ClassVar",
-        "Generic",
-        "Optional",
-        "Tuple",
-        "Type",
-        "TypeVar",
-        "Union",
-        "AbstractSet",
-        "ByteString",
-        "Container",
-        "ContextManager",
-        "Hashable",
-        "ItemsView",
-        "Iterable",
-        "Iterator",
-        "KeysView",
-        "Mapping",
-        "MappingView",
-        "MutableMapping",
-        "MutableSequence",
-        "MutableSet",
-        "Sequence",
-        "Sized",
-        "ValuesView",
-        "Awaitable",
-        "AsyncIterator",
-        "AsyncIterable",
-        "Coroutine",
-        "Collection",
-        "AsyncGenerator",
-        "AsyncContextManager",
-        "Reversible",
-        "SupportsAbs",
-        "SupportsBytes",
-        "SupportsComplex",
-        "SupportsFloat",
-        "SupportsInt",
-        "SupportsRound",
-        "Counter",
-        "Deque",
-        "Dict",
-        "DefaultDict",
-        "List",
-        "Set",
-        "FrozenSet",
-        "NamedTuple",
-        "Generator",
-        "AnyStr",
-        "Text",
-        "Pattern",
-    }
-)
-
-
-def _is_from_future_import(stmt, name):
-    """Check if the name is a future import from another module."""
-    try:
-        module = stmt.do_import_module(stmt.modname)
-    except astroid.AstroidBuildingException:
-        return None
-
-    for local_node in module.locals.get(name, []):
-        if isinstance(local_node, astroid.ImportFrom) and local_node.modname == FUTURE:
-            return True
-    return None
-
-
-def in_for_else_branch(parent, stmt):
-    """Returns True if stmt in inside the else branch for a parent For stmt."""
-    return isinstance(parent, astroid.For) and any(
-        else_stmt.parent_of(stmt) or else_stmt == stmt for else_stmt in parent.orelse
-    )
-
-
-@lru_cache(maxsize=1000)
-def overridden_method(klass, name):
-    """get overridden method if any"""
-    try:
-        parent = next(klass.local_attr_ancestors(name))
-    except (StopIteration, KeyError):
-        return None
-    try:
-        meth_node = parent[name]
-    except KeyError:
-        # We have found an ancestor defining <name> but it's not in the local
-        # dictionary. This may happen with astroid built from living objects.
-        return None
-    if isinstance(meth_node, astroid.FunctionDef):
-        return meth_node
-    return None
-
-
-def _get_unpacking_extra_info(node, inferred):
-    """return extra information to add to the message for unpacking-non-sequence
-    and unbalanced-tuple-unpacking errors
-    """
-    more = ""
-    inferred_module = inferred.root().name
-    if node.root().name == inferred_module:
-        if node.lineno == inferred.lineno:
-            more = " %s" % inferred.as_string()
-        elif inferred.lineno:
-            more = " defined at line %s" % inferred.lineno
-    elif inferred.lineno:
-        more = " defined at line %s of %s" % (inferred.lineno, inferred_module)
-    return more
-
-
-def _detect_global_scope(node, frame, defframe):
-    """ Detect that the given frames shares a global
-    scope.
-
-    Two frames shares a global scope when neither
-    of them are hidden under a function scope, as well
-    as any of parent scope of them, until the root scope.
-    In this case, depending from something defined later on
-    will not work, because it is still undefined.
-
-    Example:
-        class A:
-            # B has the same global scope as `C`, leading to a NameError.
-            class B(C): ...
-        class C: ...
-
-    """
-    def_scope = scope = None
-    if frame and frame.parent:
-        scope = frame.parent.scope()
-    if defframe and defframe.parent:
-        def_scope = defframe.parent.scope()
-    if isinstance(frame, astroid.FunctionDef):
-        # If the parent of the current node is a
-        # function, then it can be under its scope
-        # (defined in, which doesn't concern us) or
-        # the `->` part of annotations. The same goes
-        # for annotations of function arguments, they'll have
-        # their parent the Arguments node.
-        if not isinstance(node.parent, (astroid.FunctionDef, astroid.Arguments)):
-            return False
-    elif any(
-        not isinstance(f, (astroid.ClassDef, astroid.Module)) for f in (frame, defframe)
-    ):
-        # Not interested in other frames, since they are already
-        # not in a global scope.
-        return False
-
-    break_scopes = []
-    for current_scope in (scope, def_scope):
-        # Look for parent scopes. If there is anything different
-        # than a module or a class scope, then they frames don't
-        # share a global scope.
-        parent_scope = current_scope
-        while parent_scope:
-            if not isinstance(parent_scope, (astroid.ClassDef, astroid.Module)):
-                break_scopes.append(parent_scope)
-                break
-            if parent_scope.parent:
-                parent_scope = parent_scope.parent.scope()
-            else:
-                break
-    if break_scopes and len(set(break_scopes)) != 1:
-        # Store different scopes than expected.
-        # If the stored scopes are, in fact, the very same, then it means
-        # that the two frames (frame and defframe) shares the same scope,
-        # and we could apply our lineno analysis over them.
-        # For instance, this works when they are inside a function, the node
-        # that uses a definition and the definition itself.
-        return False
-    # At this point, we are certain that frame and defframe shares a scope
-    # and the definition of the first depends on the second.
-    return frame.lineno < defframe.lineno
-
-
-def _infer_name_module(node, name):
-    context = InferenceContext()
-    context.lookupname = name
-    return node.infer(context, asname=False)
-
-
-def _fix_dot_imports(not_consumed):
-    """ Try to fix imports with multiple dots, by returning a dictionary
-    with the import names expanded. The function unflattens root imports,
-    like 'xml' (when we have both 'xml.etree' and 'xml.sax'), to 'xml.etree'
-    and 'xml.sax' respectively.
-    """
-    names = {}
-    for name, stmts in not_consumed.items():
-        if any(
-            isinstance(stmt, astroid.AssignName)
-            and isinstance(stmt.assign_type(), astroid.AugAssign)
-            for stmt in stmts
-        ):
-            continue
-        for stmt in stmts:
-            if not isinstance(stmt, (astroid.ImportFrom, astroid.Import)):
-                continue
-            for imports in stmt.names:
-                second_name = None
-                import_module_name = imports[0]
-                if import_module_name == "*":
-                    # In case of wildcard imports,
-                    # pick the name from inside the imported module.
-                    second_name = name
-                else:
-                    name_matches_dotted_import = False
-                    if (
-                        import_module_name.startswith(name)
-                        and import_module_name.find(".") > -1
-                    ):
-                        name_matches_dotted_import = True
-
-                    if name_matches_dotted_import or name in imports:
-                        # Most likely something like 'xml.etree',
-                        # which will appear in the .locals as 'xml'.
-                        # Only pick the name if it wasn't consumed.
-                        second_name = import_module_name
-                if second_name and second_name not in names:
-                    names[second_name] = stmt
-    return sorted(names.items(), key=lambda a: a[1].fromlineno)
-
-
-def _find_frame_imports(name, frame):
-    """
-    Detect imports in the frame, with the required
-    *name*. Such imports can be considered assignments.
-    Returns True if an import for the given name was found.
-    """
-    imports = frame.nodes_of_class((astroid.Import, astroid.ImportFrom))
-    for import_node in imports:
-        for import_name, import_alias in import_node.names:
-            # If the import uses an alias, check only that.
-            # Otherwise, check only the import name.
-            if import_alias:
-                if import_alias == name:
-                    return True
-            elif import_name and import_name == name:
-                return True
-    return None
-
-
-def _import_name_is_global(stmt, global_names):
-    for import_name, import_alias in stmt.names:
-        # If the import uses an alias, check only that.
-        # Otherwise, check only the import name.
-        if import_alias:
-            if import_alias in global_names:
-                return True
-        elif import_name in global_names:
-            return True
-    return False
-
-
-def _flattened_scope_names(iterator):
-    values = (set(stmt.names) for stmt in iterator)
-    return set(itertools.chain.from_iterable(values))
-
-
-def _assigned_locally(name_node):
-    """
-    Checks if name_node has corresponding assign statement in same scope
-    """
-    assign_stmts = name_node.scope().nodes_of_class(astroid.AssignName)
-    return any(a.name == name_node.name for a in assign_stmts)
-
-
-def _is_type_checking_import(node):
-    parent = node.parent
-    if not isinstance(parent, astroid.If):
-        return False
-    test = parent.test
-    return test.as_string() in TYPING_TYPE_CHECKS_GUARDS
-
-
-def _has_locals_call_after_node(stmt, scope):
-    skip_nodes = (
-        astroid.FunctionDef,
-        astroid.ClassDef,
-        astroid.Import,
-        astroid.ImportFrom,
-    )
-    for call in scope.nodes_of_class(astroid.Call, skip_klass=skip_nodes):
-        inferred = utils.safe_infer(call.func)
-        if (
-            utils.is_builtin_object(inferred)
-            and getattr(inferred, "name", None) == "locals"
-        ):
-            if stmt.lineno < call.lineno:
-                return True
-    return False
-
-
-MSGS = {
-    "E0601": (
-        "Using variable %r before assignment",
-        "used-before-assignment",
-        "Used when a local variable is accessed before its assignment.",
-    ),
-    "E0602": (
-        "Undefined variable %r",
-        "undefined-variable",
-        "Used when an undefined variable is accessed.",
-    ),
-    "E0603": (
-        "Undefined variable name %r in __all__",
-        "undefined-all-variable",
-        "Used when an undefined variable name is referenced in __all__.",
-    ),
-    "E0604": (
-        "Invalid object %r in __all__, must contain only strings",
-        "invalid-all-object",
-        "Used when an invalid (non-string) object occurs in __all__.",
-    ),
-    "E0611": (
-        "No name %r in module %r",
-        "no-name-in-module",
-        "Used when a name cannot be found in a module.",
-    ),
-    "W0601": (
-        "Global variable %r undefined at the module level",
-        "global-variable-undefined",
-        'Used when a variable is defined through the "global" statement '
-        "but the variable is not defined in the module scope.",
-    ),
-    "W0602": (
-        "Using global for %r but no assignment is done",
-        "global-variable-not-assigned",
-        'Used when a variable is defined through the "global" statement '
-        "but no assignment to this variable is done.",
-    ),
-    "W0603": (
-        "Using the global statement",  # W0121
-        "global-statement",
-        'Used when you use the "global" statement to update a global '
-        "variable. Pylint just try to discourage this "
-        "usage. That doesn't mean you cannot use it !",
-    ),
-    "W0604": (
-        "Using the global statement at the module level",  # W0103
-        "global-at-module-level",
-        'Used when you use the "global" statement at the module level '
-        "since it has no effect",
-    ),
-    "W0611": (
-        "Unused %s",
-        "unused-import",
-        "Used when an imported module or variable is not used.",
-    ),
-    "W0612": (
-        "Unused variable %r",
-        "unused-variable",
-        "Used when a variable is defined but not used.",
-    ),
-    "W0613": (
-        "Unused argument %r",
-        "unused-argument",
-        "Used when a function or method argument is not used.",
-    ),
-    "W0614": (
-        "Unused import %s from wildcard import",
-        "unused-wildcard-import",
-        "Used when an imported module or variable is not used from a "
-        "`'from X import *'` style import.",
-    ),
-    "W0621": (
-        "Redefining name %r from outer scope (line %s)",
-        "redefined-outer-name",
-        "Used when a variable's name hides a name defined in the outer scope.",
-    ),
-    "W0622": (
-        "Redefining built-in %r",
-        "redefined-builtin",
-        "Used when a variable or function override a built-in.",
-    ),
-    "W0623": (
-        "Redefining name %r from %s in exception handler",
-        "redefine-in-handler",
-        "Used when an exception handler assigns the exception to an existing name",
-    ),
-    "W0631": (
-        "Using possibly undefined loop variable %r",
-        "undefined-loop-variable",
-        "Used when a loop variable (i.e. defined by a for loop or "
-        "a list comprehension or a generator expression) is used outside "
-        "the loop.",
-    ),
-    "W0632": (
-        "Possible unbalanced tuple unpacking with "
-        "sequence%s: "
-        "left side has %d label(s), right side has %d value(s)",
-        "unbalanced-tuple-unpacking",
-        "Used when there is an unbalanced tuple unpacking in assignment",
-        {"old_names": [("E0632", "old-unbalanced-tuple-unpacking")]},
-    ),
-    "E0633": (
-        "Attempting to unpack a non-sequence%s",
-        "unpacking-non-sequence",
-        "Used when something which is not "
-        "a sequence is used in an unpack assignment",
-        {"old_names": [("W0633", "old-unpacking-non-sequence")]},
-    ),
-    "W0640": (
-        "Cell variable %s defined in loop",
-        "cell-var-from-loop",
-        "A variable used in a closure is defined in a loop. "
-        "This will result in all closures using the same value for "
-        "the closed-over variable.",
-    ),
-    "W0641": (
-        "Possibly unused variable %r",
-        "possibly-unused-variable",
-        "Used when a variable is defined but might not be used. "
-        "The possibility comes from the fact that locals() might be used, "
-        "which could consume or not the said variable",
-    ),
-    "W0642": (
-        "Invalid assignment to %s in method",
-        "self-cls-assignment",
-        "Invalid assignment to self or cls in instance or class method "
-        "respectively.",
-    ),
-}
-
-
-ScopeConsumer = collections.namedtuple(
-    "ScopeConsumer", "to_consume consumed scope_type"
-)
-
-
-class NamesConsumer:
-    """
-    A simple class to handle consumed, to consume and scope type info of node locals
-    """
-
-    def __init__(self, node, scope_type):
-        self._atomic = ScopeConsumer(copy.copy(node.locals), {}, scope_type)
-
-    def __repr__(self):
-        msg = "\nto_consume : {:s}\n".format(
-            ", ".join(
-                [
-                    "{}->{}".format(key, val)
-                    for key, val in self._atomic.to_consume.items()
-                ]
-            )
-        )
-        msg += "consumed : {:s}\n".format(
-            ", ".join(
-                [
-                    "{}->{}".format(key, val)
-                    for key, val in self._atomic.consumed.items()
-                ]
-            )
-        )
-        msg += "scope_type : {:s}\n".format(self._atomic.scope_type)
-        return msg
-
-    def __iter__(self):
-        return iter(self._atomic)
-
-    @property
-    def to_consume(self):
-        return self._atomic.to_consume
-
-    @property
-    def consumed(self):
-        return self._atomic.consumed
-
-    @property
-    def scope_type(self):
-        return self._atomic.scope_type
-
-    def mark_as_consumed(self, name, new_node):
-        """
-        Mark the name as consumed and delete it from
-        the to_consume dictionary
-        """
-        self.consumed[name] = new_node
-        del self.to_consume[name]
-
-    def get_next_to_consume(self, node):
-        # mark the name as consumed if it's defined in this scope
-        name = node.name
-        parent_node = node.parent
-        found_node = self.to_consume.get(name)
-        if (
-            found_node
-            and isinstance(parent_node, astroid.Assign)
-            and parent_node == found_node[0].parent
-        ):
-            lhs = found_node[0].parent.targets[0]
-            if lhs.name == name:  # this name is defined in this very statement
-                found_node = None
-        return found_node
-
-
-# pylint: disable=too-many-public-methods
-class VariablesChecker(BaseChecker):
-    """checks for
-    * unused variables / imports
-    * undefined variables
-    * redefinition of variable from builtins or from an outer scope
-    * use of variable before assignment
-    * __all__ consistency
-    * self/cls assignment
-    """
-
-    __implements__ = IAstroidChecker
-
-    name = "variables"
-    msgs = MSGS
-    priority = -1
-    options = (
-        (
-            "init-import",
-            {
-                "default": 0,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "Tells whether we should check for unused import in "
-                "__init__ files.",
-            },
-        ),
-        (
-            "dummy-variables-rgx",
-            {
-                "default": "_+$|(_[a-zA-Z0-9_]*[a-zA-Z0-9]+?$)|dummy|^ignored_|^unused_",
-                "type": "regexp",
-                "metavar": "<regexp>",
-                "help": "A regular expression matching the name of dummy "
-                "variables (i.e. expected to not be used).",
-            },
-        ),
-        (
-            "additional-builtins",
-            {
-                "default": (),
-                "type": "csv",
-                "metavar": "<comma separated list>",
-                "help": "List of additional names supposed to be defined in "
-                "builtins. Remember that you should avoid defining new builtins "
-                "when possible.",
-            },
-        ),
-        (
-            "callbacks",
-            {
-                "default": ("cb_", "_cb"),
-                "type": "csv",
-                "metavar": "<callbacks>",
-                "help": "List of strings which can identify a callback "
-                "function by name. A callback name must start or "
-                "end with one of those strings.",
-            },
-        ),
-        (
-            "redefining-builtins-modules",
-            {
-                "default": (
-                    "six.moves",
-                    "past.builtins",
-                    "future.builtins",
-                    "builtins",
-                    "io",
-                ),
-                "type": "csv",
-                "metavar": "<comma separated list>",
-                "help": "List of qualified module names which can have objects "
-                "that can redefine builtins.",
-            },
-        ),
-        (
-            "ignored-argument-names",
-            {
-                "default": IGNORED_ARGUMENT_NAMES,
-                "type": "regexp",
-                "metavar": "<regexp>",
-                "help": "Argument names that match this expression will be "
-                "ignored. Default to name with leading underscore.",
-            },
-        ),
-        (
-            "allow-global-unused-variables",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y_or_n>",
-                "help": "Tells whether unused global variables should be treated as a violation.",
-            },
-        ),
-    )
-
-    def __init__(self, linter=None):
-        BaseChecker.__init__(self, linter)
-        self._to_consume = (
-            None
-        )  # list of tuples: (to_consume:dict, consumed:dict, scope_type:str)
-        self._checking_mod_attr = None
-        self._loop_variables = []
-        self._type_annotation_names = []
-        self._postponed_evaluation_enabled = False
-
-    @utils.check_messages("redefined-outer-name")
-    def visit_for(self, node):
-        assigned_to = [
-            var.name for var in node.target.nodes_of_class(astroid.AssignName)
-        ]
-
-        # Only check variables that are used
-        dummy_rgx = self.config.dummy_variables_rgx
-        assigned_to = [var for var in assigned_to if not dummy_rgx.match(var)]
-
-        for variable in assigned_to:
-            for outer_for, outer_variables in self._loop_variables:
-                if variable in outer_variables and not in_for_else_branch(
-                    outer_for, node
-                ):
-                    self.add_message(
-                        "redefined-outer-name",
-                        args=(variable, outer_for.fromlineno),
-                        node=node,
-                    )
-                    break
-
-        self._loop_variables.append((node, assigned_to))
-
-    @utils.check_messages("redefined-outer-name")
-    def leave_for(self, node):
-        self._loop_variables.pop()
-        self._store_type_annotation_names(node)
-
-    def visit_module(self, node):
-        """visit module : update consumption analysis variable
-        checks globals doesn't overrides builtins
-        """
-        self._to_consume = [NamesConsumer(node, "module")]
-        self._postponed_evaluation_enabled = is_postponed_evaluation_enabled(node)
-
-        for name, stmts in node.locals.items():
-            if utils.is_builtin(name) and not utils.is_inside_except(stmts[0]):
-                if self._should_ignore_redefined_builtin(stmts[0]) or name == "__doc__":
-                    continue
-                self.add_message("redefined-builtin", args=name, node=stmts[0])
-
-    @utils.check_messages(
-        "unused-import",
-        "unused-wildcard-import",
-        "redefined-builtin",
-        "undefined-all-variable",
-        "invalid-all-object",
-        "unused-variable",
-    )
-    def leave_module(self, node):
-        """leave module: check globals
-        """
-        assert len(self._to_consume) == 1
-
-        self._check_metaclasses(node)
-        not_consumed = self._to_consume.pop().to_consume
-        # attempt to check for __all__ if defined
-        if "__all__" in node.locals:
-            self._check_all(node, not_consumed)
-
-        # check for unused globals
-        self._check_globals(not_consumed)
-
-        # don't check unused imports in __init__ files
-        if not self.config.init_import and node.package:
-            return
-
-        self._check_imports(not_consumed)
-
-    def visit_classdef(self, node):
-        """visit class: update consumption analysis variable
-        """
-        self._to_consume.append(NamesConsumer(node, "class"))
-
-    def leave_classdef(self, _):
-        """leave class: update consumption analysis variable
-        """
-        # do not check for not used locals here (no sense)
-        self._to_consume.pop()
-
-    def visit_lambda(self, node):
-        """visit lambda: update consumption analysis variable
-        """
-        self._to_consume.append(NamesConsumer(node, "lambda"))
-
-    def leave_lambda(self, _):
-        """leave lambda: update consumption analysis variable
-        """
-        # do not check for not used locals here
-        self._to_consume.pop()
-
-    def visit_generatorexp(self, node):
-        """visit genexpr: update consumption analysis variable
-        """
-        self._to_consume.append(NamesConsumer(node, "comprehension"))
-
-    def leave_generatorexp(self, _):
-        """leave genexpr: update consumption analysis variable
-        """
-        # do not check for not used locals here
-        self._to_consume.pop()
-
-    def visit_dictcomp(self, node):
-        """visit dictcomp: update consumption analysis variable
-        """
-        self._to_consume.append(NamesConsumer(node, "comprehension"))
-
-    def leave_dictcomp(self, _):
-        """leave dictcomp: update consumption analysis variable
-        """
-        # do not check for not used locals here
-        self._to_consume.pop()
-
-    def visit_setcomp(self, node):
-        """visit setcomp: update consumption analysis variable
-        """
-        self._to_consume.append(NamesConsumer(node, "comprehension"))
-
-    def leave_setcomp(self, _):
-        """leave setcomp: update consumption analysis variable
-        """
-        # do not check for not used locals here
-        self._to_consume.pop()
-
-    def visit_functiondef(self, node):
-        """visit function: update consumption analysis variable and check locals
-        """
-        self._to_consume.append(NamesConsumer(node, "function"))
-        if not (
-            self.linter.is_message_enabled("redefined-outer-name")
-            or self.linter.is_message_enabled("redefined-builtin")
-        ):
-            return
-        globs = node.root().globals
-        for name, stmt in node.items():
-            if utils.is_inside_except(stmt):
-                continue
-            if name in globs and not isinstance(stmt, astroid.Global):
-                definition = globs[name][0]
-                if (
-                    isinstance(definition, astroid.ImportFrom)
-                    and definition.modname == FUTURE
-                ):
-                    # It is a __future__ directive, not a symbol.
-                    continue
-
-                # Do not take in account redefined names for the purpose
-                # of type checking.:
-                if any(
-                    isinstance(definition.parent, astroid.If)
-                    and definition.parent.test.as_string() in TYPING_TYPE_CHECKS_GUARDS
-                    for definition in globs[name]
-                ):
-                    continue
-
-                line = definition.fromlineno
-                if not self._is_name_ignored(stmt, name):
-                    self.add_message(
-                        "redefined-outer-name", args=(name, line), node=stmt
-                    )
-
-            elif utils.is_builtin(name) and not self._should_ignore_redefined_builtin(
-                stmt
-            ):
-                # do not print Redefining builtin for additional builtins
-                self.add_message("redefined-builtin", args=name, node=stmt)
-
-    def leave_functiondef(self, node):
-        """leave function: check function's locals are consumed"""
-        self._check_metaclasses(node)
-
-        if node.type_comment_returns:
-            self._store_type_annotation_node(node.type_comment_returns)
-        if node.type_comment_args:
-            for argument_annotation in node.type_comment_args:
-                self._store_type_annotation_node(argument_annotation)
-
-        not_consumed = self._to_consume.pop().to_consume
-        if not (
-            self.linter.is_message_enabled("unused-variable")
-            or self.linter.is_message_enabled("possibly-unused-variable")
-            or self.linter.is_message_enabled("unused-argument")
-        ):
-            return
-
-        # Don't check arguments of function which are only raising an exception.
-        if utils.is_error(node):
-            return
-
-        # Don't check arguments of abstract methods or within an interface.
-        is_method = node.is_method()
-        if is_method and node.is_abstract():
-            return
-
-        global_names = _flattened_scope_names(node.nodes_of_class(astroid.Global))
-        nonlocal_names = _flattened_scope_names(node.nodes_of_class(astroid.Nonlocal))
-        for name, stmts in not_consumed.items():
-            self._check_is_unused(name, node, stmts[0], global_names, nonlocal_names)
-
-    visit_asyncfunctiondef = visit_functiondef
-    leave_asyncfunctiondef = leave_functiondef
-
-    @utils.check_messages(
-        "global-variable-undefined",
-        "global-variable-not-assigned",
-        "global-statement",
-        "global-at-module-level",
-        "redefined-builtin",
-    )
-    def visit_global(self, node):
-        """check names imported exists in the global scope"""
-        frame = node.frame()
-        if isinstance(frame, astroid.Module):
-            self.add_message("global-at-module-level", node=node)
-            return
-
-        module = frame.root()
-        default_message = True
-        locals_ = node.scope().locals
-        for name in node.names:
-            try:
-                assign_nodes = module.getattr(name)
-            except astroid.NotFoundError:
-                # unassigned global, skip
-                assign_nodes = []
-
-            not_defined_locally_by_import = not any(
-                isinstance(local, astroid.node_classes.Import)
-                for local in locals_.get(name, ())
-            )
-            if not assign_nodes and not_defined_locally_by_import:
-                self.add_message("global-variable-not-assigned", args=name, node=node)
-                default_message = False
-                continue
-
-            for anode in assign_nodes:
-                if (
-                    isinstance(anode, astroid.AssignName)
-                    and anode.name in module.special_attributes
-                ):
-                    self.add_message("redefined-builtin", args=name, node=node)
-                    break
-                if anode.frame() is module:
-                    # module level assignment
-                    break
-            else:
-                if not_defined_locally_by_import:
-                    # global undefined at the module scope
-                    self.add_message("global-variable-undefined", args=name, node=node)
-                    default_message = False
-
-        if default_message:
-            self.add_message("global-statement", node=node)
-
-    def visit_assignname(self, node):
-        if isinstance(node.assign_type(), astroid.AugAssign):
-            self.visit_name(node)
-
-    def visit_delname(self, node):
-        self.visit_name(node)
-
-    @utils.check_messages(*MSGS)
-    def visit_name(self, node):
-        """check that a name is defined if the current scope and doesn't
-        redefine a built-in
-        """
-        stmt = node.statement()
-        if stmt.fromlineno is None:
-            # name node from an astroid built from live code, skip
-            assert not stmt.root().file.endswith(".py")
-            return
-
-        name = node.name
-        frame = stmt.scope()
-        # if the name node is used as a function default argument's value or as
-        # a decorator, then start from the parent frame of the function instead
-        # of the function frame - and thus open an inner class scope
-        if (
-            utils.is_default_argument(node)
-            or utils.is_func_decorator(node)
-            or utils.is_ancestor_name(frame, node)
-        ):
-            start_index = len(self._to_consume) - 2
-        else:
-            start_index = len(self._to_consume) - 1
-        # iterates through parent scopes, from the inner to the outer
-        base_scope_type = self._to_consume[start_index].scope_type
-        # pylint: disable=too-many-nested-blocks; refactoring this block is a pain.
-        for i in range(start_index, -1, -1):
-            current_consumer = self._to_consume[i]
-            # if the current scope is a class scope but it's not the inner
-            # scope, ignore it. This prevents to access this scope instead of
-            # the globals one in function members when there are some common
-            # names. The only exception is when the starting scope is a
-            # comprehension and its direct outer scope is a class
-            if (
-                current_consumer.scope_type == "class"
-                and i != start_index
-                and not (base_scope_type == "comprehension" and i == start_index - 1)
-            ):
-                if self._ignore_class_scope(node):
-                    continue
-
-            # the name has already been consumed, only check it's not a loop
-            # variable used outside the loop
-            # avoid the case where there are homonyms inside function scope and
-            #  comprehension current scope (avoid bug #1731)
-            if name in current_consumer.consumed and not (
-                current_consumer.scope_type == "comprehension"
-                and self._has_homonym_in_upper_function_scope(node, i)
-            ):
-                defnode = utils.assign_parent(current_consumer.consumed[name][0])
-                self._check_late_binding_closure(node, defnode)
-                self._loopvar_name(node, name)
-                break
-
-            found_node = current_consumer.get_next_to_consume(node)
-            if found_node is None:
-                continue
-
-            # checks for use before assignment
-            defnode = utils.assign_parent(current_consumer.to_consume[name][0])
-
-            if defnode is not None:
-                self._check_late_binding_closure(node, defnode)
-                defstmt = defnode.statement()
-                defframe = defstmt.frame()
-                # The class reuses itself in the class scope.
-                recursive_klass = (
-                    frame is defframe
-                    and defframe.parent_of(node)
-                    and isinstance(defframe, astroid.ClassDef)
-                    and node.name == defframe.name
-                )
-
-                if (
-                    recursive_klass
-                    and utils.is_inside_lambda(node)
-                    and (
-                        not utils.is_default_argument(node)
-                        or node.scope().parent.scope() is not defframe
-                    )
-                ):
-                    # Self-referential class references are fine in lambda's --
-                    # As long as they are not part of the default argument directly
-                    # under the scope of the parent self-referring class.
-                    # Example of valid default argument:
-                    # class MyName3:
-                    #     myattr = 1
-                    #     mylambda3 = lambda: lambda a=MyName3: a
-                    # Example of invalid default argument:
-                    # class MyName4:
-                    #     myattr = 1
-                    #     mylambda4 = lambda a=MyName4: lambda: a
-
-                    # If the above conditional is True,
-                    # there is no possibility of undefined-variable
-                    # Also do not consume class name
-                    # (since consuming blocks subsequent checks)
-                    # -- quit
-                    break
-
-                maybee0601, annotation_return, use_outer_definition = self._is_variable_violation(
-                    node,
-                    name,
-                    defnode,
-                    stmt,
-                    defstmt,
-                    frame,
-                    defframe,
-                    base_scope_type,
-                    recursive_klass,
-                )
-
-                if use_outer_definition:
-                    continue
-
-                if (
-                    maybee0601
-                    and not utils.is_defined_before(node)
-                    and not astroid.are_exclusive(stmt, defstmt, ("NameError",))
-                ):
-
-                    # Used and defined in the same place, e.g `x += 1` and `del x`
-                    defined_by_stmt = defstmt is stmt and isinstance(
-                        node, (astroid.DelName, astroid.AssignName)
-                    )
-                    if (
-                        recursive_klass
-                        or defined_by_stmt
-                        or annotation_return
-                        or isinstance(defstmt, astroid.Delete)
-                    ):
-                        if not utils.node_ignores_exception(node, NameError):
-
-                            # Handle postponed evaluation of annotations
-                            if not (
-                                self._postponed_evaluation_enabled
-                                and isinstance(
-                                    stmt,
-                                    (
-                                        astroid.AnnAssign,
-                                        astroid.FunctionDef,
-                                        astroid.Arguments,
-                                    ),
-                                )
-                                and name in node.root().locals
-                            ):
-                                self.add_message(
-                                    "undefined-variable", args=name, node=node
-                                )
-                    elif base_scope_type != "lambda":
-                        # E0601 may *not* occurs in lambda scope.
-
-                        # Handle postponed evaluation of annotations
-                        if not (
-                            self._postponed_evaluation_enabled
-                            and isinstance(
-                                stmt, (astroid.AnnAssign, astroid.FunctionDef)
-                            )
-                        ):
-                            self.add_message(
-                                "used-before-assignment", args=name, node=node
-                            )
-                    elif base_scope_type == "lambda":
-                        # E0601 can occur in class-level scope in lambdas, as in
-                        # the following example:
-                        #   class A:
-                        #      x = lambda attr: f + attr
-                        #      f = 42
-                        if isinstance(frame, astroid.ClassDef) and name in frame.locals:
-                            if isinstance(node.parent, astroid.Arguments):
-                                if stmt.fromlineno <= defstmt.fromlineno:
-                                    # Doing the following is fine:
-                                    #   class A:
-                                    #      x = 42
-                                    #      y = lambda attr=x: attr
-                                    self.add_message(
-                                        "used-before-assignment", args=name, node=node
-                                    )
-                            else:
-                                self.add_message(
-                                    "undefined-variable", args=name, node=node
-                                )
-                        elif current_consumer.scope_type == "lambda":
-                            self.add_message("undefined-variable", node=node, args=name)
-
-            current_consumer.mark_as_consumed(name, found_node)
-            # check it's not a loop variable used outside the loop
-            self._loopvar_name(node, name)
-            break
-        else:
-            # we have not found the name, if it isn't a builtin, that's an
-            # undefined name !
-            if not (
-                name in astroid.Module.scope_attrs
-                or utils.is_builtin(name)
-                or name in self.config.additional_builtins
-            ):
-                if not utils.node_ignores_exception(node, NameError):
-                    self.add_message("undefined-variable", args=name, node=node)
-
-    @utils.check_messages("no-name-in-module")
-    def visit_import(self, node):
-        """check modules attribute accesses"""
-        if not self._analyse_fallback_blocks and utils.is_from_fallback_block(node):
-            # No need to verify this, since ImportError is already
-            # handled by the client code.
-            return
-
-        for name, _ in node.names:
-            parts = name.split(".")
-            try:
-                module = next(_infer_name_module(node, parts[0]))
-            except astroid.ResolveError:
-                continue
-            self._check_module_attrs(node, module, parts[1:])
-
-    @utils.check_messages("no-name-in-module")
-    def visit_importfrom(self, node):
-        """check modules attribute accesses"""
-        if not self._analyse_fallback_blocks and utils.is_from_fallback_block(node):
-            # No need to verify this, since ImportError is already
-            # handled by the client code.
-            return
-
-        name_parts = node.modname.split(".")
-        try:
-            module = node.do_import_module(name_parts[0])
-        except astroid.AstroidBuildingException:
-            return
-        module = self._check_module_attrs(node, module, name_parts[1:])
-        if not module:
-            return
-        for name, _ in node.names:
-            if name == "*":
-                continue
-            self._check_module_attrs(node, module, name.split("."))
-
-    @utils.check_messages(
-        "unbalanced-tuple-unpacking", "unpacking-non-sequence", "self-cls-assignment"
-    )
-    def visit_assign(self, node):
-        """Check unbalanced tuple unpacking for assignments
-        and unpacking non-sequences as well as in case self/cls
-        get assigned.
-        """
-        self._check_self_cls_assign(node)
-        if not isinstance(node.targets[0], (astroid.Tuple, astroid.List)):
-            return
-
-        targets = node.targets[0].itered()
-        try:
-            inferred = utils.safe_infer(node.value)
-            if inferred is not None:
-                self._check_unpacking(inferred, node, targets)
-        except astroid.InferenceError:
-            return
-
-    # listcomp have now also their scope
-    def visit_listcomp(self, node):
-        """visit dictcomp: update consumption analysis variable
-        """
-        self._to_consume.append(NamesConsumer(node, "comprehension"))
-
-    def leave_listcomp(self, _):
-        """leave dictcomp: update consumption analysis variable
-        """
-        # do not check for not used locals here
-        self._to_consume.pop()
-
-    def leave_assign(self, node):
-        self._store_type_annotation_names(node)
-
-    def leave_with(self, node):
-        self._store_type_annotation_names(node)
-
-    def visit_arguments(self, node):
-        for annotation in node.type_comment_args:
-            self._store_type_annotation_node(annotation)
-
-    # Relying on other checker's options, which might not have been initialized yet.
-    @decorators.cachedproperty
-    def _analyse_fallback_blocks(self):
-        return get_global_option(self, "analyse-fallback-blocks", default=False)
-
-    @decorators.cachedproperty
-    def _ignored_modules(self):
-        return get_global_option(self, "ignored-modules", default=[])
-
-    @decorators.cachedproperty
-    def _allow_global_unused_variables(self):
-        return get_global_option(self, "allow-global-unused-variables", default=True)
-
-    @staticmethod
-    def _defined_in_function_definition(node, frame):
-        in_annotation_or_default = False
-        if isinstance(frame, astroid.FunctionDef) and node.statement() is frame:
-            in_annotation_or_default = (
-                node in frame.args.annotations
-                or node in frame.args.kwonlyargs_annotations
-                or node is frame.args.varargannotation
-                or node is frame.args.kwargannotation
-            ) or frame.args.parent_of(node)
-        return in_annotation_or_default
-
-    @staticmethod
-    def _is_variable_violation(
-        node,
-        name,
-        defnode,
-        stmt,
-        defstmt,
-        frame,
-        defframe,
-        base_scope_type,
-        recursive_klass,
-    ):
-        # pylint: disable=too-many-nested-blocks
-        # node: Node to check for violation
-        # name: name of node to check violation for
-        # frame: Scope of statement of node
-        # base_scope_type: local scope type
-        maybee0601 = True
-        annotation_return = False
-        use_outer_definition = False
-        if frame is not defframe:
-            maybee0601 = _detect_global_scope(node, frame, defframe)
-        elif defframe.parent is None:
-            # we are at the module level, check the name is not
-            # defined in builtins
-            if name in defframe.scope_attrs or astroid.builtin_lookup(name)[1]:
-                maybee0601 = False
-        else:
-            # we are in a local scope, check the name is not
-            # defined in global or builtin scope
-            # skip this lookup if name is assigned later in function scope/lambda
-            # Note: the node.frame() is not the same as the `frame` argument which is
-            # equivalent to frame.statement().scope()
-            forbid_lookup = (
-                isinstance(frame, astroid.FunctionDef)
-                or isinstance(node.frame(), astroid.Lambda)
-            ) and _assigned_locally(node)
-            if not forbid_lookup and defframe.root().lookup(name)[1]:
-                maybee0601 = False
-                use_outer_definition = stmt == defstmt and not isinstance(
-                    defnode, astroid.node_classes.Comprehension
-                )
-            else:
-                # check if we have a nonlocal
-                if name in defframe.locals:
-                    maybee0601 = not any(
-                        isinstance(child, astroid.Nonlocal) and name in child.names
-                        for child in defframe.get_children()
-                    )
-
-        if (
-            base_scope_type == "lambda"
-            and isinstance(frame, astroid.ClassDef)
-            and name in frame.locals
-        ):
-
-            # This rule verifies that if the definition node of the
-            # checked name is an Arguments node and if the name
-            # is used a default value in the arguments defaults
-            # and the actual definition of the variable label
-            # is happening before the Arguments definition.
-            #
-            # bar = None
-            # foo = lambda bar=bar: bar
-            #
-            # In this case, maybee0601 should be False, otherwise
-            # it should be True.
-            maybee0601 = not (
-                isinstance(defnode, astroid.Arguments)
-                and node in defnode.defaults
-                and frame.locals[name][0].fromlineno < defstmt.fromlineno
-            )
-        elif isinstance(defframe, astroid.ClassDef) and isinstance(
-            frame, astroid.FunctionDef
-        ):
-            # Special rule for function return annotations,
-            # which uses the same name as the class where
-            # the function lives.
-            if node is frame.returns and defframe.parent_of(frame.returns):
-                maybee0601 = annotation_return = True
-
-            if (
-                maybee0601
-                and defframe.name in defframe.locals
-                and defframe.locals[name][0].lineno < frame.lineno
-            ):
-                # Detect class assignments with the same
-                # name as the class. In this case, no warning
-                # should be raised.
-                maybee0601 = False
-            if isinstance(node.parent, astroid.Arguments):
-                maybee0601 = stmt.fromlineno <= defstmt.fromlineno
-        elif recursive_klass:
-            maybee0601 = True
-        else:
-            maybee0601 = maybee0601 and stmt.fromlineno <= defstmt.fromlineno
-            if maybee0601 and stmt.fromlineno == defstmt.fromlineno:
-                if (
-                    isinstance(defframe, astroid.FunctionDef)
-                    and frame is defframe
-                    and defframe.parent_of(node)
-                    and stmt is not defstmt
-                ):
-                    # Single statement function, with the statement on the
-                    # same line as the function definition
-                    maybee0601 = False
-
-            # Look for type checking definitions inside a type checking guard.
-            if isinstance(defstmt, (astroid.Import, astroid.ImportFrom)):
-                defstmt_parent = defstmt.parent
-
-                if (
-                    isinstance(defstmt_parent, astroid.If)
-                    and defstmt_parent.test.as_string() in TYPING_TYPE_CHECKS_GUARDS
-                ):
-                    # Exempt those definitions that are used inside the type checking
-                    # guard or that are defined in both type checking guard branches.
-                    used_in_branch = defstmt_parent.parent_of(node)
-                    defined_in_or_else = False
-
-                    for definition in defstmt_parent.orelse:
-                        if isinstance(definition, astroid.Assign):
-                            defined_in_or_else = any(
-                                target.name == name for target in definition.targets
-                            )
-                            if defined_in_or_else:
-                                break
-
-                    if not used_in_branch and not defined_in_or_else:
-                        maybee0601 = True
-
-        return maybee0601, annotation_return, use_outer_definition
-
-    def _ignore_class_scope(self, node):
-        """
-        Return True if the node is in a local class scope, as an assignment.
-
-        :param node: Node considered
-        :type node: astroid.Node
-        :return: True if the node is in a local class scope, as an assignment. False otherwise.
-        :rtype: bool
-        """
-        # Detect if we are in a local class scope, as an assignment.
-        # For example, the following is fair game.
-        #
-        # class A:
-        #    b = 1
-        #    c = lambda b=b: b * b
-        #
-        # class B:
-        #    tp = 1
-        #    def func(self, arg: tp):
-        #        ...
-        # class C:
-        #    tp = 2
-        #    def func(self, arg=tp):
-        #        ...
-
-        name = node.name
-        frame = node.statement().scope()
-        in_annotation_or_default = self._defined_in_function_definition(node, frame)
-        if in_annotation_or_default:
-            frame_locals = frame.parent.scope().locals
-        else:
-            frame_locals = frame.locals
-        return not (
-            (isinstance(frame, astroid.ClassDef) or in_annotation_or_default)
-            and name in frame_locals
-        )
-
-    def _loopvar_name(self, node, name):
-        # filter variables according to node's scope
-        if not self.linter.is_message_enabled("undefined-loop-variable"):
-            return
-        astmts = [stmt for stmt in node.lookup(name)[1] if hasattr(stmt, "assign_type")]
-        # If this variable usage exists inside a function definition
-        # that exists in the same loop,
-        # the usage is safe because the function will not be defined either if
-        # the variable is not defined.
-        scope = node.scope()
-        if isinstance(scope, astroid.FunctionDef) and any(
-            asmt.statement().parent_of(scope) for asmt in astmts
-        ):
-            return
-
-        # filter variables according their respective scope test is_statement
-        # and parent to avoid #74747. This is not a total fix, which would
-        # introduce a mechanism similar to special attribute lookup in
-        # modules. Also, in order to get correct inference in this case, the
-        # scope lookup rules would need to be changed to return the initial
-        # assignment (which does not exist in code per se) as well as any later
-        # modifications.
-        if (
-            not astmts
-            or (astmts[0].is_statement or astmts[0].parent)
-            and astmts[0].statement().parent_of(node)
-        ):
-            _astmts = []
-        else:
-            _astmts = astmts[:1]
-        for i, stmt in enumerate(astmts[1:]):
-            if astmts[i].statement().parent_of(stmt) and not in_for_else_branch(
-                astmts[i].statement(), stmt
-            ):
-                continue
-            _astmts.append(stmt)
-        astmts = _astmts
-        if len(astmts) != 1:
-            return
-
-        assign = astmts[0].assign_type()
-        if not (
-            isinstance(
-                assign, (astroid.For, astroid.Comprehension, astroid.GeneratorExp)
-            )
-            and assign.statement() is not node.statement()
-        ):
-            return
-
-        # For functions we can do more by inferring the length of the itered object
-        if not isinstance(assign, astroid.For):
-            self.add_message("undefined-loop-variable", args=name, node=node)
-            return
-
-        try:
-            inferred = next(assign.iter.infer())
-        except astroid.InferenceError:
-            self.add_message("undefined-loop-variable", args=name, node=node)
-        else:
-            if (
-                isinstance(inferred, astroid.Instance)
-                and inferred.qname() == BUILTIN_RANGE
-            ):
-                # Consider range() objects safe, even if they might not yield any results.
-                return
-
-            # Consider sequences.
-            sequences = (
-                astroid.List,
-                astroid.Tuple,
-                astroid.Dict,
-                astroid.Set,
-                objects.FrozenSet,
-            )
-            if not isinstance(inferred, sequences):
-                self.add_message("undefined-loop-variable", args=name, node=node)
-                return
-
-            elements = getattr(inferred, "elts", getattr(inferred, "items", []))
-            if not elements:
-                self.add_message("undefined-loop-variable", args=name, node=node)
-
-    def _check_is_unused(self, name, node, stmt, global_names, nonlocal_names):
-        # pylint: disable=too-many-branches
-        # Ignore some special names specified by user configuration.
-        if self._is_name_ignored(stmt, name):
-            return
-        # Ignore names that were added dynamically to the Function scope
-        if (
-            isinstance(node, astroid.FunctionDef)
-            and name == "__class__"
-            and len(node.locals["__class__"]) == 1
-            and isinstance(node.locals["__class__"][0], astroid.ClassDef)
-        ):
-            return
-
-        # Ignore names imported by the global statement.
-        if isinstance(stmt, (astroid.Global, astroid.Import, astroid.ImportFrom)):
-            # Detect imports, assigned to global statements.
-            if global_names and _import_name_is_global(stmt, global_names):
-                return
-
-        argnames = list(
-            itertools.chain(node.argnames(), [arg.name for arg in node.args.kwonlyargs])
-        )
-        # Care about functions with unknown argument (builtins)
-        if name in argnames:
-            self._check_unused_arguments(name, node, stmt, argnames)
-        else:
-            if stmt.parent and isinstance(
-                stmt.parent, (astroid.Assign, astroid.AnnAssign)
-            ):
-                if name in nonlocal_names:
-                    return
-
-            qname = asname = None
-            if isinstance(stmt, (astroid.Import, astroid.ImportFrom)):
-                # Need the complete name, which we don't have in .locals.
-                if len(stmt.names) > 1:
-                    import_names = next(
-                        (names for names in stmt.names if name in names), None
-                    )
-                else:
-                    import_names = stmt.names[0]
-                if import_names:
-                    qname, asname = import_names
-                    name = asname or qname
-
-            if _has_locals_call_after_node(stmt, node.scope()):
-                message_name = "possibly-unused-variable"
-            else:
-                if isinstance(stmt, astroid.Import):
-                    if asname is not None:
-                        msg = "%s imported as %s" % (qname, asname)
-                    else:
-                        msg = "import %s" % name
-                    self.add_message("unused-import", args=msg, node=stmt)
-                    return
-                if isinstance(stmt, astroid.ImportFrom):
-                    if asname is not None:
-                        msg = "%s imported from %s as %s" % (
-                            qname,
-                            stmt.modname,
-                            asname,
-                        )
-                    else:
-                        msg = "%s imported from %s" % (name, stmt.modname)
-                    self.add_message("unused-import", args=msg, node=stmt)
-                    return
-                message_name = "unused-variable"
-
-            # Don't check function stubs created only for type information
-            if utils.is_overload_stub(node):
-                return
-
-            self.add_message(message_name, args=name, node=stmt)
-
-    def _is_name_ignored(self, stmt, name):
-        authorized_rgx = self.config.dummy_variables_rgx
-        if (
-            isinstance(stmt, astroid.AssignName)
-            and isinstance(stmt.parent, astroid.Arguments)
-            or isinstance(stmt, astroid.Arguments)
-        ):
-            regex = self.config.ignored_argument_names
-        else:
-            regex = authorized_rgx
-        return regex and regex.match(name)
-
-    def _check_unused_arguments(self, name, node, stmt, argnames):
-        is_method = node.is_method()
-        klass = node.parent.frame()
-        if is_method and isinstance(klass, astroid.ClassDef):
-            confidence = (
-                INFERENCE if utils.has_known_bases(klass) else INFERENCE_FAILURE
-            )
-        else:
-            confidence = HIGH
-
-        if is_method:
-            # Don't warn for the first argument of a (non static) method
-            if node.type != "staticmethod" and name == argnames[0]:
-                return
-            # Don't warn for argument of an overridden method
-            overridden = overridden_method(klass, node.name)
-            if overridden is not None and name in overridden.argnames():
-                return
-            if node.name in utils.PYMETHODS and node.name not in (
-                "__init__",
-                "__new__",
-            ):
-                return
-        # Don't check callback arguments
-        if any(
-            node.name.startswith(cb) or node.name.endswith(cb)
-            for cb in self.config.callbacks
-        ):
-            return
-        # Don't check arguments of singledispatch.register function.
-        if utils.is_registered_in_singledispatch_function(node):
-            return
-
-        # Don't check function stubs created only for type information
-        if utils.is_overload_stub(node):
-            return
-
-        # Don't check protocol classes
-        if utils.is_protocol_class(klass):
-            return
-
-        self.add_message("unused-argument", args=name, node=stmt, confidence=confidence)
-
-    def _check_late_binding_closure(self, node, assignment_node):
-        def _is_direct_lambda_call():
-            return (
-                isinstance(node_scope.parent, astroid.Call)
-                and node_scope.parent.func is node_scope
-            )
-
-        node_scope = node.scope()
-        if not isinstance(node_scope, (astroid.Lambda, astroid.FunctionDef)):
-            return
-        if isinstance(node.parent, astroid.Arguments):
-            return
-
-        if isinstance(assignment_node, astroid.Comprehension):
-            if assignment_node.parent.parent_of(node.scope()):
-                self.add_message("cell-var-from-loop", node=node, args=node.name)
-        else:
-            assign_scope = assignment_node.scope()
-            maybe_for = assignment_node
-            while not isinstance(maybe_for, astroid.For):
-                if maybe_for is assign_scope:
-                    break
-                maybe_for = maybe_for.parent
-            else:
-                if (
-                    maybe_for.parent_of(node_scope)
-                    and not _is_direct_lambda_call()
-                    and not isinstance(node_scope.statement(), astroid.Return)
-                ):
-                    self.add_message("cell-var-from-loop", node=node, args=node.name)
-
-    def _should_ignore_redefined_builtin(self, stmt):
-        if not isinstance(stmt, astroid.ImportFrom):
-            return False
-        return stmt.modname in self.config.redefining_builtins_modules
-
-    def _has_homonym_in_upper_function_scope(self, node, index):
-        """
-        Return True if there is a node with the same name in the to_consume dict of an upper scope
-        and if that scope is a function
-
-        :param node: node to check for
-        :type node: astroid.Node
-        :param index: index of the current consumer inside self._to_consume
-        :type index: int
-        :return: True if there is a node with the same name in the to_consume dict of an upper scope
-                 and if that scope is a function
-        :rtype: bool
-        """
-        for _consumer in self._to_consume[index - 1 :: -1]:
-            if _consumer.scope_type == "function" and node.name in _consumer.to_consume:
-                return True
-        return False
-
-    def _store_type_annotation_node(self, type_annotation):
-        """Given a type annotation, store all the name nodes it refers to"""
-        if isinstance(type_annotation, astroid.Name):
-            self._type_annotation_names.append(type_annotation.name)
-            return
-
-        if not isinstance(type_annotation, astroid.Subscript):
-            return
-
-        if (
-            isinstance(type_annotation.value, astroid.Attribute)
-            and isinstance(type_annotation.value.expr, astroid.Name)
-            and type_annotation.value.expr.name == TYPING_MODULE
-        ):
-            self._type_annotation_names.append(TYPING_MODULE)
-            return
-
-        self._type_annotation_names.extend(
-            annotation.name
-            for annotation in type_annotation.nodes_of_class(astroid.Name)
-        )
-
-    def _store_type_annotation_names(self, node):
-        type_annotation = node.type_annotation
-        if not type_annotation:
-            return
-        self._store_type_annotation_node(node.type_annotation)
-
-    def _check_self_cls_assign(self, node):
-        """Check that self/cls don't get assigned"""
-        assign_names = {
-            target.name
-            for target in node.targets
-            if isinstance(target, astroid.AssignName)
-        }
-        scope = node.scope()
-        nonlocals_with_same_name = any(
-            child
-            for child in scope.body
-            if isinstance(child, astroid.Nonlocal) and assign_names & set(child.names)
-        )
-        if nonlocals_with_same_name:
-            scope = node.scope().parent.scope()
-
-        if not (
-            isinstance(scope, astroid.scoped_nodes.FunctionDef)
-            and scope.is_method()
-            and "builtins.staticmethod" not in scope.decoratornames()
-        ):
-            return
-        argument_names = scope.argnames()
-        if not argument_names:
-            return
-        self_cls_name = argument_names[0]
-        target_assign_names = (
-            target.name
-            for target in node.targets
-            if isinstance(target, astroid.node_classes.AssignName)
-        )
-        if self_cls_name in target_assign_names:
-            self.add_message("self-cls-assignment", node=node, args=(self_cls_name))
-
-    def _check_unpacking(self, inferred, node, targets):
-        """ Check for unbalanced tuple unpacking
-        and unpacking non sequences.
-        """
-        if utils.is_inside_abstract_class(node):
-            return
-        if utils.is_comprehension(node):
-            return
-        if inferred is astroid.Uninferable:
-            return
-        if (
-            isinstance(inferred.parent, astroid.Arguments)
-            and isinstance(node.value, astroid.Name)
-            and node.value.name == inferred.parent.vararg
-        ):
-            # Variable-length argument, we can't determine the length.
-            return
-        if isinstance(inferred, (astroid.Tuple, astroid.List)):
-            # attempt to check unpacking is properly balanced
-            values = inferred.itered()
-            if len(targets) != len(values):
-                # Check if we have starred nodes.
-                if any(isinstance(target, astroid.Starred) for target in targets):
-                    return
-                self.add_message(
-                    "unbalanced-tuple-unpacking",
-                    node=node,
-                    args=(
-                        _get_unpacking_extra_info(node, inferred),
-                        len(targets),
-                        len(values),
-                    ),
-                )
-        # attempt to check unpacking may be possible (ie RHS is iterable)
-        else:
-            if not utils.is_iterable(inferred):
-                self.add_message(
-                    "unpacking-non-sequence",
-                    node=node,
-                    args=(_get_unpacking_extra_info(node, inferred),),
-                )
-
-    def _check_module_attrs(self, node, module, module_names):
-        """check that module_names (list of string) are accessible through the
-        given module
-        if the latest access name corresponds to a module, return it
-        """
-        assert isinstance(module, astroid.Module), module
-        while module_names:
-            name = module_names.pop(0)
-            if name == "__dict__":
-                module = None
-                break
-            try:
-                module = next(module.getattr(name)[0].infer())
-                if module is astroid.Uninferable:
-                    return None
-            except astroid.NotFoundError:
-                if module.name in self._ignored_modules:
-                    return None
-                self.add_message(
-                    "no-name-in-module", args=(name, module.name), node=node
-                )
-                return None
-            except astroid.InferenceError:
-                return None
-        if module_names:
-            modname = module.name if module else "__dict__"
-            self.add_message(
-                "no-name-in-module", node=node, args=(".".join(module_names), modname)
-            )
-            return None
-        if isinstance(module, astroid.Module):
-            return module
-        return None
-
-    def _check_all(self, node, not_consumed):
-        assigned = next(node.igetattr("__all__"))
-        if assigned is astroid.Uninferable:
-            return
-
-        for elt in getattr(assigned, "elts", ()):
-            try:
-                elt_name = next(elt.infer())
-            except astroid.InferenceError:
-                continue
-            if elt_name is astroid.Uninferable:
-                continue
-            if not elt_name.parent:
-                continue
-
-            if not isinstance(elt_name, astroid.Const) or not isinstance(
-                elt_name.value, str
-            ):
-                self.add_message("invalid-all-object", args=elt.as_string(), node=elt)
-                continue
-
-            elt_name = elt_name.value
-            # If elt is in not_consumed, remove it from not_consumed
-            if elt_name in not_consumed:
-                del not_consumed[elt_name]
-                continue
-
-            if elt_name not in node.locals:
-                if not node.package:
-                    self.add_message(
-                        "undefined-all-variable", args=(elt_name,), node=elt
-                    )
-                else:
-                    basename = os.path.splitext(node.file)[0]
-                    if os.path.basename(basename) == "__init__":
-                        name = node.name + "." + elt_name
-                        try:
-                            modutils.file_from_modpath(name.split("."))
-                        except ImportError:
-                            self.add_message(
-                                "undefined-all-variable", args=(elt_name,), node=elt
-                            )
-                        except SyntaxError:
-                            # don't yield a syntax-error warning,
-                            # because it will be later yielded
-                            # when the file will be checked
-                            pass
-
-    def _check_globals(self, not_consumed):
-        if self._allow_global_unused_variables:
-            return
-        for name, nodes in not_consumed.items():
-            for node in nodes:
-                self.add_message("unused-variable", args=(name,), node=node)
-
-    def _check_imports(self, not_consumed):
-        local_names = _fix_dot_imports(not_consumed)
-        checked = set()
-        for name, stmt in local_names:
-            for imports in stmt.names:
-                real_name = imported_name = imports[0]
-                if imported_name == "*":
-                    real_name = name
-                as_name = imports[1]
-                if real_name in checked:
-                    continue
-                if name not in (real_name, as_name):
-                    continue
-                checked.add(real_name)
-
-                if isinstance(stmt, astroid.Import) or (
-                    isinstance(stmt, astroid.ImportFrom) and not stmt.modname
-                ):
-                    if isinstance(stmt, astroid.ImportFrom) and SPECIAL_OBJ.search(
-                        imported_name
-                    ):
-                        # Filter special objects (__doc__, __all__) etc.,
-                        # because they can be imported for exporting.
-                        continue
-
-                    if imported_name in self._type_annotation_names:
-                        # Most likely a typing import if it wasn't used so far.
-                        continue
-
-                    if as_name == "_":
-                        continue
-                    if as_name is None:
-                        msg = "import %s" % imported_name
-                    else:
-                        msg = "%s imported as %s" % (imported_name, as_name)
-                    if not _is_type_checking_import(stmt):
-                        self.add_message("unused-import", args=msg, node=stmt)
-                elif isinstance(stmt, astroid.ImportFrom) and stmt.modname != FUTURE:
-                    if SPECIAL_OBJ.search(imported_name):
-                        # Filter special objects (__doc__, __all__) etc.,
-                        # because they can be imported for exporting.
-                        continue
-
-                    if _is_from_future_import(stmt, name):
-                        # Check if the name is in fact loaded from a
-                        # __future__ import in another module.
-                        continue
-
-                    if imported_name in self._type_annotation_names:
-                        # Most likely a typing import if it wasn't used so far.
-                        continue
-
-                    if imported_name == "*":
-                        self.add_message("unused-wildcard-import", args=name, node=stmt)
-                    else:
-                        if as_name is None:
-                            msg = "%s imported from %s" % (imported_name, stmt.modname)
-                        else:
-                            fields = (imported_name, stmt.modname, as_name)
-                            msg = "%s imported from %s as %s" % fields
-                        if not _is_type_checking_import(stmt):
-                            self.add_message("unused-import", args=msg, node=stmt)
-        del self._to_consume
-
-    def _check_metaclasses(self, node):
-        """ Update consumption analysis for metaclasses. """
-        consumed = []  # [(scope_locals, consumed_key)]
-
-        for child_node in node.get_children():
-            if isinstance(child_node, astroid.ClassDef):
-                consumed.extend(self._check_classdef_metaclasses(child_node, node))
-
-        # Pop the consumed items, in order to avoid having
-        # unused-import and unused-variable false positives
-        for scope_locals, name in consumed:
-            scope_locals.pop(name, None)
-
-    def _check_classdef_metaclasses(self, klass, parent_node):
-        if not klass._metaclass:
-            # Skip if this class doesn't use explicitly a metaclass, but inherits it from ancestors
-            return []
-
-        consumed = []  # [(scope_locals, consumed_key)]
-        metaclass = klass.metaclass()
-
-        name = None
-        if isinstance(klass._metaclass, astroid.Name):
-            name = klass._metaclass.name
-        elif metaclass:
-            name = metaclass.root().name
-
-        found = None
-        name = METACLASS_NAME_TRANSFORMS.get(name, name)
-        if name:
-            # check enclosing scopes starting from most local
-            for scope_locals, _, _ in self._to_consume[::-1]:
-                found = scope_locals.get(name)
-                if found:
-                    consumed.append((scope_locals, name))
-                    break
-
-        if found is None and not metaclass:
-            name = None
-            if isinstance(klass._metaclass, astroid.Name):
-                name = klass._metaclass.name
-            elif isinstance(klass._metaclass, astroid.Attribute):
-                name = klass._metaclass.as_string()
-
-            if name is not None:
-                if not (
-                    name in astroid.Module.scope_attrs
-                    or utils.is_builtin(name)
-                    or name in self.config.additional_builtins
-                    or name in parent_node.locals
-                ):
-                    self.add_message("undefined-variable", node=klass, args=(name,))
-
-        return consumed
-
-
-def register(linter):
-    """required method to auto register this checker"""
-    linter.register_checker(VariablesChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/config.py b/venv/Lib/site-packages/pylint/config.py
deleted file mode 100644
index 0925575..0000000
--- a/venv/Lib/site-packages/pylint/config.py
+++ /dev/null
@@ -1,913 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2010, 2012-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2008 pyves@crater.logilab.fr <pyves@crater.logilab.fr>
-# Copyright (c) 2010 Julien Jehannet <julien.jehannet@logilab.fr>
-# Copyright (c) 2013 Google, Inc.
-# Copyright (c) 2013 John McGehee <jmcgehee@altera.com>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Aru Sahni <arusahni@gmail.com>
-# Copyright (c) 2015 John Kirkham <jakirkham@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Erik <erik.eriksson@yahoo.com>
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2017-2018 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 ahirnish <ahirnish@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 Gary Tyler McLeod <mail@garytyler.com>
-# Copyright (c) 2018 Konstantin <Github@pheanex.de>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""utilities for Pylint configuration :
-
-* pylintrc
-* pylint.d (PYLINTHOME)
-"""
-import collections
-import configparser
-import contextlib
-import copy
-import io
-import optparse
-import os
-import pickle
-import re
-import sys
-import time
-from typing import Any, Dict, Tuple
-
-from pylint import utils
-
-USER_HOME = os.path.expanduser("~")
-if "PYLINTHOME" in os.environ:
-    PYLINT_HOME = os.environ["PYLINTHOME"]
-    if USER_HOME == "~":
-        USER_HOME = os.path.dirname(PYLINT_HOME)
-elif USER_HOME == "~":
-    PYLINT_HOME = ".pylint.d"
-else:
-    PYLINT_HOME = os.path.join(USER_HOME, ".pylint.d")
-
-
-def _get_pdata_path(base_name, recurs):
-    base_name = base_name.replace(os.sep, "_")
-    return os.path.join(PYLINT_HOME, "%s%s%s" % (base_name, recurs, ".stats"))
-
-
-def load_results(base):
-    data_file = _get_pdata_path(base, 1)
-    try:
-        with open(data_file, "rb") as stream:
-            return pickle.load(stream)
-    except Exception:  # pylint: disable=broad-except
-        return {}
-
-
-def save_results(results, base):
-    if not os.path.exists(PYLINT_HOME):
-        try:
-            os.mkdir(PYLINT_HOME)
-        except OSError:
-            print("Unable to create directory %s" % PYLINT_HOME, file=sys.stderr)
-    data_file = _get_pdata_path(base, 1)
-    try:
-        with open(data_file, "wb") as stream:
-            pickle.dump(results, stream)
-    except (IOError, OSError) as ex:
-        print("Unable to create file %s: %s" % (data_file, ex), file=sys.stderr)
-
-
-def find_pylintrc():
-    """search the pylint rc file and return its path if it find it, else None
-    """
-    # is there a pylint rc file in the current directory ?
-    if os.path.exists("pylintrc"):
-        return os.path.abspath("pylintrc")
-    if os.path.exists(".pylintrc"):
-        return os.path.abspath(".pylintrc")
-    if os.path.isfile("__init__.py"):
-        curdir = os.path.abspath(os.getcwd())
-        while os.path.isfile(os.path.join(curdir, "__init__.py")):
-            curdir = os.path.abspath(os.path.join(curdir, ".."))
-            if os.path.isfile(os.path.join(curdir, "pylintrc")):
-                return os.path.join(curdir, "pylintrc")
-            if os.path.isfile(os.path.join(curdir, ".pylintrc")):
-                return os.path.join(curdir, ".pylintrc")
-    if "PYLINTRC" in os.environ and os.path.exists(os.environ["PYLINTRC"]):
-        pylintrc = os.environ["PYLINTRC"]
-    else:
-        user_home = os.path.expanduser("~")
-        if user_home in ("~", "/root"):
-            pylintrc = ".pylintrc"
-        else:
-            pylintrc = os.path.join(user_home, ".pylintrc")
-            if not os.path.isfile(pylintrc):
-                pylintrc = os.path.join(user_home, ".config", "pylintrc")
-    if not os.path.isfile(pylintrc):
-        if os.path.isfile("/etc/pylintrc"):
-            pylintrc = "/etc/pylintrc"
-        else:
-            pylintrc = None
-    return pylintrc
-
-
-PYLINTRC = find_pylintrc()
-
-ENV_HELP = (
-    """
-The following environment variables are used:
-    * PYLINTHOME
-    Path to the directory where persistent data for the run will be stored. If
-not found, it defaults to ~/.pylint.d/ or .pylint.d (in the current working
-directory).
-    * PYLINTRC
-    Path to the configuration file. See the documentation for the method used
-to search for configuration file.
-"""
-    % globals()  # type: ignore
-)
-
-
-class UnsupportedAction(Exception):
-    """raised by set_option when it doesn't know what to do for an action"""
-
-
-def _multiple_choice_validator(choices, name, value):
-    values = utils._check_csv(value)
-    for csv_value in values:
-        if csv_value not in choices:
-            msg = "option %s: invalid value: %r, should be in %s"
-            raise optparse.OptionValueError(msg % (name, csv_value, choices))
-    return values
-
-
-def _choice_validator(choices, name, value):
-    if value not in choices:
-        msg = "option %s: invalid value: %r, should be in %s"
-        raise optparse.OptionValueError(msg % (name, value, choices))
-    return value
-
-
-# pylint: disable=unused-argument
-def _csv_validator(_, name, value):
-    return utils._check_csv(value)
-
-
-# pylint: disable=unused-argument
-def _regexp_validator(_, name, value):
-    if hasattr(value, "pattern"):
-        return value
-    return re.compile(value)
-
-
-# pylint: disable=unused-argument
-def _regexp_csv_validator(_, name, value):
-    return [_regexp_validator(_, name, val) for val in _csv_validator(_, name, value)]
-
-
-def _yn_validator(opt, _, value):
-    if isinstance(value, int):
-        return bool(value)
-    if value in ("y", "yes"):
-        return True
-    if value in ("n", "no"):
-        return False
-    msg = "option %s: invalid yn value %r, should be in (y, yes, n, no)"
-    raise optparse.OptionValueError(msg % (opt, value))
-
-
-def _non_empty_string_validator(opt, _, value):
-    if not value:
-        msg = "indent string can't be empty."
-        raise optparse.OptionValueError(msg)
-    return utils._unquote(value)
-
-
-VALIDATORS = {
-    "string": utils._unquote,
-    "int": int,
-    "regexp": re.compile,
-    "regexp_csv": _regexp_csv_validator,
-    "csv": _csv_validator,
-    "yn": _yn_validator,
-    "choice": lambda opt, name, value: _choice_validator(opt["choices"], name, value),
-    "multiple_choice": lambda opt, name, value: _multiple_choice_validator(
-        opt["choices"], name, value
-    ),
-    "non_empty_string": _non_empty_string_validator,
-}
-
-
-def _call_validator(opttype, optdict, option, value):
-    if opttype not in VALIDATORS:
-        raise Exception('Unsupported type "%s"' % opttype)
-    try:
-        return VALIDATORS[opttype](optdict, option, value)
-    except TypeError:
-        try:
-            return VALIDATORS[opttype](value)
-        except Exception:
-            raise optparse.OptionValueError(
-                "%s value (%r) should be of type %s" % (option, value, opttype)
-            )
-
-
-def _validate(value, optdict, name=""):
-    """return a validated value for an option according to its type
-
-    optional argument name is only used for error message formatting
-    """
-    try:
-        _type = optdict["type"]
-    except KeyError:
-        return value
-    return _call_validator(_type, optdict, name, value)
-
-
-def _level_options(group, outputlevel):
-    return [
-        option
-        for option in group.option_list
-        if (getattr(option, "level", 0) or 0) <= outputlevel
-        and option.help is not optparse.SUPPRESS_HELP
-    ]
-
-
-def _expand_default(self, option):
-    """Patch OptionParser.expand_default with custom behaviour
-
-    This will handle defaults to avoid overriding values in the
-    configuration file.
-    """
-    if self.parser is None or not self.default_tag:
-        return option.help
-    optname = option._long_opts[0][2:]
-    try:
-        provider = self.parser.options_manager._all_options[optname]
-    except KeyError:
-        value = None
-    else:
-        optdict = provider.get_option_def(optname)
-        optname = provider.option_attrname(optname, optdict)
-        value = getattr(provider.config, optname, optdict)
-        value = utils._format_option_value(optdict, value)
-    if value is optparse.NO_DEFAULT or not value:
-        value = self.NO_DEFAULT_VALUE
-    return option.help.replace(self.default_tag, str(value))
-
-
-@contextlib.contextmanager
-def _patch_optparse():
-    orig_default = optparse.HelpFormatter
-    try:
-        optparse.HelpFormatter.expand_default = _expand_default
-        yield
-    finally:
-        optparse.HelpFormatter.expand_default = orig_default
-
-
-def _multiple_choices_validating_option(opt, name, value):
-    return _multiple_choice_validator(opt.choices, name, value)
-
-
-# pylint: disable=no-member
-class Option(optparse.Option):
-    TYPES = optparse.Option.TYPES + (
-        "regexp",
-        "regexp_csv",
-        "csv",
-        "yn",
-        "multiple_choice",
-        "non_empty_string",
-    )
-    ATTRS = optparse.Option.ATTRS + ["hide", "level"]
-    TYPE_CHECKER = copy.copy(optparse.Option.TYPE_CHECKER)
-    TYPE_CHECKER["regexp"] = _regexp_validator
-    TYPE_CHECKER["regexp_csv"] = _regexp_csv_validator
-    TYPE_CHECKER["csv"] = _csv_validator
-    TYPE_CHECKER["yn"] = _yn_validator
-    TYPE_CHECKER["multiple_choice"] = _multiple_choices_validating_option
-    TYPE_CHECKER["non_empty_string"] = _non_empty_string_validator
-
-    def __init__(self, *opts, **attrs):
-        optparse.Option.__init__(self, *opts, **attrs)
-        if hasattr(self, "hide") and self.hide:
-            self.help = optparse.SUPPRESS_HELP
-
-    def _check_choice(self):
-        if self.type in ("choice", "multiple_choice"):
-            if self.choices is None:
-                raise optparse.OptionError(
-                    "must supply a list of choices for type 'choice'", self
-                )
-            if not isinstance(self.choices, (tuple, list)):
-                raise optparse.OptionError(
-                    "choices must be a list of strings ('%s' supplied)"
-                    % str(type(self.choices)).split("'")[1],
-                    self,
-                )
-        elif self.choices is not None:
-            raise optparse.OptionError(
-                "must not supply choices for type %r" % self.type, self
-            )
-
-    # pylint: disable=unsupported-assignment-operation
-    optparse.Option.CHECK_METHODS[2] = _check_choice  # type: ignore
-
-    def process(self, opt, value, values, parser):
-        # First, convert the value(s) to the right type.  Howl if any
-        # value(s) are bogus.
-        value = self.convert_value(opt, value)
-        if self.type == "named":
-            existent = getattr(values, self.dest)
-            if existent:
-                existent.update(value)
-                value = existent
-        # And then take whatever action is expected of us.
-        # This is a separate method to make life easier for
-        # subclasses to add new actions.
-        return self.take_action(self.action, self.dest, opt, value, values, parser)
-
-
-class OptionParser(optparse.OptionParser):
-    def __init__(self, option_class, *args, **kwargs):
-        optparse.OptionParser.__init__(self, option_class=Option, *args, **kwargs)
-
-    def format_option_help(self, formatter=None):
-        if formatter is None:
-            formatter = self.formatter
-        outputlevel = getattr(formatter, "output_level", 0)
-        formatter.store_option_strings(self)
-        result = []
-        result.append(formatter.format_heading("Options"))
-        formatter.indent()
-        if self.option_list:
-            result.append(optparse.OptionContainer.format_option_help(self, formatter))
-            result.append("\n")
-        for group in self.option_groups:
-            if group.level <= outputlevel and (
-                group.description or _level_options(group, outputlevel)
-            ):
-                result.append(group.format_help(formatter))
-                result.append("\n")
-        formatter.dedent()
-        # Drop the last "\n", or the header if no options or option groups:
-        return "".join(result[:-1])
-
-    def _match_long_opt(self, opt):
-        """Disable abbreviations."""
-        if opt not in self._long_opt:
-            raise optparse.BadOptionError(opt)
-        return opt
-
-
-# pylint: disable=abstract-method; by design?
-class _ManHelpFormatter(optparse.HelpFormatter):
-    def __init__(
-        self, indent_increment=0, max_help_position=24, width=79, short_first=0
-    ):
-        optparse.HelpFormatter.__init__(
-            self, indent_increment, max_help_position, width, short_first
-        )
-
-    def format_heading(self, heading):
-        return ".SH %s\n" % heading.upper()
-
-    def format_description(self, description):
-        return description
-
-    def format_option(self, option):
-        try:
-            optstring = option.option_strings
-        except AttributeError:
-            optstring = self.format_option_strings(option)
-        if option.help:
-            help_text = self.expand_default(option)
-            help_string = " ".join([l.strip() for l in help_text.splitlines()])
-            help_string = help_string.replace("\\", "\\\\")
-            help_string = help_string.replace("[current:", "[default:")
-        else:
-            help_string = ""
-        return """.IP "%s"
-%s
-""" % (
-            optstring,
-            help_string,
-        )
-
-    def format_head(self, optparser, pkginfo, section=1):
-        long_desc = ""
-        try:
-            pgm = optparser._get_prog_name()
-        except AttributeError:
-            # py >= 2.4.X (dunno which X exactly, at least 2)
-            pgm = optparser.get_prog_name()
-        short_desc = self.format_short_description(pgm, pkginfo.description)
-        if hasattr(pkginfo, "long_desc"):
-            long_desc = self.format_long_description(pgm, pkginfo.long_desc)
-        return "%s\n%s\n%s\n%s" % (
-            self.format_title(pgm, section),
-            short_desc,
-            self.format_synopsis(pgm),
-            long_desc,
-        )
-
-    @staticmethod
-    def format_title(pgm, section):
-        date = "%d-%02d-%02d" % time.localtime()[:3]
-        return '.TH %s %s "%s" %s' % (pgm, section, date, pgm)
-
-    @staticmethod
-    def format_short_description(pgm, short_desc):
-        return """.SH NAME
-.B %s
-\\- %s
-""" % (
-            pgm,
-            short_desc.strip(),
-        )
-
-    @staticmethod
-    def format_synopsis(pgm):
-        return (
-            """.SH SYNOPSIS
-.B  %s
-[
-.I OPTIONS
-] [
-.I <arguments>
-]
-"""
-            % pgm
-        )
-
-    @staticmethod
-    def format_long_description(pgm, long_desc):
-        long_desc = "\n".join(line.lstrip() for line in long_desc.splitlines())
-        long_desc = long_desc.replace("\n.\n", "\n\n")
-        if long_desc.lower().startswith(pgm):
-            long_desc = long_desc[len(pgm) :]
-        return """.SH DESCRIPTION
-.B %s
-%s
-""" % (
-            pgm,
-            long_desc.strip(),
-        )
-
-    @staticmethod
-    def format_tail(pkginfo):
-        tail = """.SH SEE ALSO
-/usr/share/doc/pythonX.Y-%s/
-
-.SH BUGS
-Please report bugs on the project\'s mailing list:
-%s
-
-.SH AUTHOR
-%s <%s>
-""" % (
-            getattr(pkginfo, "debian_name", pkginfo.modname),
-            pkginfo.mailinglist,
-            pkginfo.author,
-            pkginfo.author_email,
-        )
-
-        if hasattr(pkginfo, "copyright"):
-            tail += (
-                """
-.SH COPYRIGHT
-%s
-"""
-                % pkginfo.copyright
-            )
-
-        return tail
-
-
-class OptionsManagerMixIn:
-    """Handle configuration from both a configuration file and command line options"""
-
-    def __init__(self, usage, config_file=None, version=None):
-        self.config_file = config_file
-        self.reset_parsers(usage, version=version)
-        # list of registered options providers
-        self.options_providers = []
-        # dictionary associating option name to checker
-        self._all_options = collections.OrderedDict()
-        self._short_options = {}
-        self._nocallback_options = {}
-        self._mygroups = {}
-        # verbosity
-        self._maxlevel = 0
-
-    def reset_parsers(self, usage="", version=None):
-        # configuration file parser
-        self.cfgfile_parser = configparser.ConfigParser(
-            inline_comment_prefixes=("#", ";")
-        )
-        # command line parser
-        self.cmdline_parser = OptionParser(Option, usage=usage, version=version)
-        self.cmdline_parser.options_manager = self
-        self._optik_option_attrs = set(self.cmdline_parser.option_class.ATTRS)
-
-    def register_options_provider(self, provider, own_group=True):
-        """register an options provider"""
-        assert provider.priority <= 0, "provider's priority can't be >= 0"
-        for i in range(len(self.options_providers)):
-            if provider.priority > self.options_providers[i].priority:
-                self.options_providers.insert(i, provider)
-                break
-        else:
-            self.options_providers.append(provider)
-        non_group_spec_options = [
-            option for option in provider.options if "group" not in option[1]
-        ]
-        groups = getattr(provider, "option_groups", ())
-        if own_group and non_group_spec_options:
-            self.add_option_group(
-                provider.name.upper(),
-                provider.__doc__,
-                non_group_spec_options,
-                provider,
-            )
-        else:
-            for opt, optdict in non_group_spec_options:
-                self.add_optik_option(provider, self.cmdline_parser, opt, optdict)
-        for gname, gdoc in groups:
-            gname = gname.upper()
-            goptions = [
-                option
-                for option in provider.options
-                if option[1].get("group", "").upper() == gname
-            ]
-            self.add_option_group(gname, gdoc, goptions, provider)
-
-    def add_option_group(self, group_name, _, options, provider):
-        # add option group to the command line parser
-        if group_name in self._mygroups:
-            group = self._mygroups[group_name]
-        else:
-            group = optparse.OptionGroup(
-                self.cmdline_parser, title=group_name.capitalize()
-            )
-            self.cmdline_parser.add_option_group(group)
-            group.level = provider.level
-            self._mygroups[group_name] = group
-            # add section to the config file
-            if (
-                group_name != "DEFAULT"
-                and group_name not in self.cfgfile_parser._sections
-            ):
-                self.cfgfile_parser.add_section(group_name)
-        # add provider's specific options
-        for opt, optdict in options:
-            self.add_optik_option(provider, group, opt, optdict)
-
-    def add_optik_option(self, provider, optikcontainer, opt, optdict):
-        args, optdict = self.optik_option(provider, opt, optdict)
-        option = optikcontainer.add_option(*args, **optdict)
-        self._all_options[opt] = provider
-        self._maxlevel = max(self._maxlevel, option.level or 0)
-
-    def optik_option(self, provider, opt, optdict):
-        """get our personal option definition and return a suitable form for
-        use with optik/optparse
-        """
-        optdict = copy.copy(optdict)
-        if "action" in optdict:
-            self._nocallback_options[provider] = opt
-        else:
-            optdict["action"] = "callback"
-            optdict["callback"] = self.cb_set_provider_option
-        # default is handled here and *must not* be given to optik if you
-        # want the whole machinery to work
-        if "default" in optdict:
-            if (
-                "help" in optdict
-                and optdict.get("default") is not None
-                and optdict["action"] not in ("store_true", "store_false")
-            ):
-                optdict["help"] += " [current: %default]"
-            del optdict["default"]
-        args = ["--" + str(opt)]
-        if "short" in optdict:
-            self._short_options[optdict["short"]] = opt
-            args.append("-" + optdict["short"])
-            del optdict["short"]
-        # cleanup option definition dict before giving it to optik
-        for key in list(optdict.keys()):
-            if key not in self._optik_option_attrs:
-                optdict.pop(key)
-        return args, optdict
-
-    def cb_set_provider_option(self, option, opt, value, parser):
-        """optik callback for option setting"""
-        if opt.startswith("--"):
-            # remove -- on long option
-            opt = opt[2:]
-        else:
-            # short option, get its long equivalent
-            opt = self._short_options[opt[1:]]
-        # trick since we can't set action='store_true' on options
-        if value is None:
-            value = 1
-        self.global_set_option(opt, value)
-
-    def global_set_option(self, opt, value):
-        """set option on the correct option provider"""
-        self._all_options[opt].set_option(opt, value)
-
-    def generate_config(self, stream=None, skipsections=(), encoding=None):
-        """write a configuration file according to the current configuration
-        into the given stream or stdout
-        """
-        options_by_section = {}
-        sections = []
-        for provider in self.options_providers:
-            for section, options in provider.options_by_section():
-                if section is None:
-                    section = provider.name
-                if section in skipsections:
-                    continue
-                options = [
-                    (n, d, v)
-                    for (n, d, v) in options
-                    if d.get("type") is not None and not d.get("deprecated")
-                ]
-                if not options:
-                    continue
-                if section not in sections:
-                    sections.append(section)
-                alloptions = options_by_section.setdefault(section, [])
-                alloptions += options
-        stream = stream or sys.stdout
-        printed = False
-        for section in sections:
-            if printed:
-                print("\n", file=stream)
-            utils.format_section(
-                stream, section.upper(), sorted(options_by_section[section])
-            )
-            printed = True
-
-    def generate_manpage(self, pkginfo, section=1, stream=None):
-        with _patch_optparse():
-            _generate_manpage(
-                self.cmdline_parser,
-                pkginfo,
-                section,
-                stream=stream or sys.stdout,
-                level=self._maxlevel,
-            )
-
-    def load_provider_defaults(self):
-        """initialize configuration using default values"""
-        for provider in self.options_providers:
-            provider.load_defaults()
-
-    def read_config_file(self, config_file=None, verbose=None):
-        """read the configuration file but do not load it (i.e. dispatching
-        values to each options provider)
-        """
-        helplevel = 1
-        while helplevel <= self._maxlevel:
-            opt = "-".join(["long"] * helplevel) + "-help"
-            if opt in self._all_options:
-                break  # already processed
-            # pylint: disable=unused-argument
-            def helpfunc(option, opt, val, p, level=helplevel):
-                print(self.help(level))
-                sys.exit(0)
-
-            helpmsg = "%s verbose help." % " ".join(["more"] * helplevel)
-            optdict = {"action": "callback", "callback": helpfunc, "help": helpmsg}
-            provider = self.options_providers[0]
-            self.add_optik_option(provider, self.cmdline_parser, opt, optdict)
-            provider.options += ((opt, optdict),)
-            helplevel += 1
-        if config_file is None:
-            config_file = self.config_file
-        if config_file is not None:
-            config_file = os.path.expanduser(config_file)
-            if not os.path.exists(config_file):
-                raise IOError("The config file {:s} doesn't exist!".format(config_file))
-
-        use_config_file = config_file and os.path.exists(config_file)
-        if use_config_file:
-            parser = self.cfgfile_parser
-
-            # Use this encoding in order to strip the BOM marker, if any.
-            with io.open(config_file, "r", encoding="utf_8_sig") as fp:
-                parser.read_file(fp)
-
-            # normalize sections'title
-            for sect, values in list(parser._sections.items()):
-                if not sect.isupper() and values:
-                    parser._sections[sect.upper()] = values
-
-        if not verbose:
-            return
-
-        if use_config_file:
-            msg = "Using config file {}".format(os.path.abspath(config_file))
-        else:
-            msg = "No config file found, using default configuration"
-        print(msg, file=sys.stderr)
-
-    def load_config_file(self):
-        """dispatch values previously read from a configuration file to each
-        options provider)
-        """
-        parser = self.cfgfile_parser
-        for section in parser.sections():
-            for option, value in parser.items(section):
-                try:
-                    self.global_set_option(option, value)
-                except (KeyError, optparse.OptionError):
-                    continue
-
-    def load_configuration(self, **kwargs):
-        """override configuration according to given parameters"""
-        return self.load_configuration_from_config(kwargs)
-
-    def load_configuration_from_config(self, config):
-        for opt, opt_value in config.items():
-            opt = opt.replace("_", "-")
-            provider = self._all_options[opt]
-            provider.set_option(opt, opt_value)
-
-    def load_command_line_configuration(self, args=None):
-        """Override configuration according to command line parameters
-
-        return additional arguments
-        """
-        with _patch_optparse():
-            if args is None:
-                args = sys.argv[1:]
-            else:
-                args = list(args)
-            (options, args) = self.cmdline_parser.parse_args(args=args)
-            for provider in self._nocallback_options:
-                config = provider.config
-                for attr in config.__dict__.keys():
-                    value = getattr(options, attr, None)
-                    if value is None:
-                        continue
-                    setattr(config, attr, value)
-            return args
-
-    def add_help_section(self, title, description, level=0):
-        """add a dummy option section for help purpose """
-        group = optparse.OptionGroup(
-            self.cmdline_parser, title=title.capitalize(), description=description
-        )
-        group.level = level
-        self._maxlevel = max(self._maxlevel, level)
-        self.cmdline_parser.add_option_group(group)
-
-    def help(self, level=0):
-        """return the usage string for available options """
-        self.cmdline_parser.formatter.output_level = level
-        with _patch_optparse():
-            return self.cmdline_parser.format_help()
-
-
-class OptionsProviderMixIn:
-    """Mixin to provide options to an OptionsManager"""
-
-    # those attributes should be overridden
-    priority = -1
-    name = "default"
-    options = ()  # type: Tuple[Tuple[str, Dict[str, Any]], ...]
-    level = 0
-
-    def __init__(self):
-        self.config = optparse.Values()
-        self.load_defaults()
-
-    def load_defaults(self):
-        """initialize the provider using default values"""
-        for opt, optdict in self.options:
-            action = optdict.get("action")
-            if action != "callback":
-                # callback action have no default
-                if optdict is None:
-                    optdict = self.get_option_def(opt)
-                default = optdict.get("default")
-                self.set_option(opt, default, action, optdict)
-
-    def option_attrname(self, opt, optdict=None):
-        """get the config attribute corresponding to opt"""
-        if optdict is None:
-            optdict = self.get_option_def(opt)
-        return optdict.get("dest", opt.replace("-", "_"))
-
-    def option_value(self, opt):
-        """get the current value for the given option"""
-        return getattr(self.config, self.option_attrname(opt), None)
-
-    def set_option(self, optname, value, action=None, optdict=None):
-        """method called to set an option (registered in the options list)"""
-        if optdict is None:
-            optdict = self.get_option_def(optname)
-        if value is not None:
-            value = _validate(value, optdict, optname)
-        if action is None:
-            action = optdict.get("action", "store")
-        if action == "store":
-            setattr(self.config, self.option_attrname(optname, optdict), value)
-        elif action in ("store_true", "count"):
-            setattr(self.config, self.option_attrname(optname, optdict), 0)
-        elif action == "store_false":
-            setattr(self.config, self.option_attrname(optname, optdict), 1)
-        elif action == "append":
-            optname = self.option_attrname(optname, optdict)
-            _list = getattr(self.config, optname, None)
-            if _list is None:
-                if isinstance(value, (list, tuple)):
-                    _list = value
-                elif value is not None:
-                    _list = []
-                    _list.append(value)
-                setattr(self.config, optname, _list)
-            elif isinstance(_list, tuple):
-                setattr(self.config, optname, _list + (value,))
-            else:
-                _list.append(value)
-        elif action == "callback":
-            optdict["callback"](None, optname, value, None)
-        else:
-            raise UnsupportedAction(action)
-
-    def get_option_def(self, opt):
-        """return the dictionary defining an option given its name"""
-        assert self.options
-        for option in self.options:
-            if option[0] == opt:
-                return option[1]
-        raise optparse.OptionError(
-            "no such option %s in section %r" % (opt, self.name), opt
-        )
-
-    def options_by_section(self):
-        """return an iterator on options grouped by section
-
-        (section, [list of (optname, optdict, optvalue)])
-        """
-        sections = {}
-        for optname, optdict in self.options:
-            sections.setdefault(optdict.get("group"), []).append(
-                (optname, optdict, self.option_value(optname))
-            )
-        if None in sections:
-            yield None, sections.pop(None)
-        for section, options in sorted(sections.items()):
-            yield section.upper(), options
-
-    def options_and_values(self, options=None):
-        if options is None:
-            options = self.options
-        for optname, optdict in options:
-            yield (optname, optdict, self.option_value(optname))
-
-
-class ConfigurationMixIn(OptionsManagerMixIn, OptionsProviderMixIn):
-    """basic mixin for simple configurations which don't need the
-    manager / providers model
-    """
-
-    def __init__(self, *args, **kwargs):
-        if not args:
-            kwargs.setdefault("usage", "")
-        OptionsManagerMixIn.__init__(self, *args, **kwargs)
-        OptionsProviderMixIn.__init__(self)
-        if not getattr(self, "option_groups", None):
-            self.option_groups = []
-            for _, optdict in self.options:
-                try:
-                    gdef = (optdict["group"].upper(), "")
-                except KeyError:
-                    continue
-                if gdef not in self.option_groups:
-                    self.option_groups.append(gdef)
-        self.register_options_provider(self, own_group=False)
-
-
-def _generate_manpage(optparser, pkginfo, section=1, stream=sys.stdout, level=0):
-    formatter = _ManHelpFormatter()
-    formatter.output_level = level
-    formatter.parser = optparser
-    print(formatter.format_head(optparser, pkginfo, section), file=stream)
-    print(optparser.format_option_help(formatter), file=stream)
-    print(formatter.format_tail(pkginfo), file=stream)
diff --git a/venv/Lib/site-packages/pylint/constants.py b/venv/Lib/site-packages/pylint/constants.py
deleted file mode 100644
index 852fc15..0000000
--- a/venv/Lib/site-packages/pylint/constants.py
+++ /dev/null
@@ -1,43 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import re
-
-# Allow stopping after the first semicolon/hash encountered,
-# so that an option can be continued with the reasons
-# why it is active or disabled.
-OPTION_RGX = re.compile(r"\s*#.*\bpylint:\s*([^;#]+)[;#]{0,1}")
-
-PY_EXTS = (".py", ".pyc", ".pyo", ".pyw", ".so", ".dll")
-
-MSG_STATE_CONFIDENCE = 2
-_MSG_ORDER = "EWRCIF"
-MSG_STATE_SCOPE_CONFIG = 0
-MSG_STATE_SCOPE_MODULE = 1
-
-# The line/node distinction does not apply to fatal errors and reports.
-_SCOPE_EXEMPT = "FR"
-
-MSG_TYPES = {
-    "I": "info",
-    "C": "convention",
-    "R": "refactor",
-    "W": "warning",
-    "E": "error",
-    "F": "fatal",
-}
-MSG_TYPES_LONG = {v: k for k, v in MSG_TYPES.items()}
-
-MSG_TYPES_STATUS = {"I": 0, "C": 16, "R": 8, "W": 4, "E": 2, "F": 1}
-
-# You probably don't want to change the MAIN_CHECKER_NAME
-# This would affect rcfile generation and retro-compatibility
-# on all project using [MASTER] in their rcfile.
-MAIN_CHECKER_NAME = "master"
-
-
-class WarningScope:
-    LINE = "line-based-msg"
-    NODE = "node-based-msg"
diff --git a/venv/Lib/site-packages/pylint/epylint.py b/venv/Lib/site-packages/pylint/epylint.py
deleted file mode 100644
index 85f1c86..0000000
--- a/venv/Lib/site-packages/pylint/epylint.py
+++ /dev/null
@@ -1,197 +0,0 @@
-# -*- coding: utf-8;
-# mode: python; tab-width: 4; indent-tabs-mode: nil; c-basic-offset: 4
-# -*- vim:fenc=utf-8:ft=python:et:sw=4:ts=4:sts=4
-
-# Copyright (c) 2008-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Jakob Normark <jakobnormark@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Manuel Vázquez Acosta <mva.led@gmail.com>
-# Copyright (c) 2014 Derek Harland <derek.harland@finq.co.nz>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Mihai Balint <balint.mihai@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Daniela Plascencia <daplascen@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Ryan McGuire <ryan@enigmacurry.com>
-# Copyright (c) 2018 thernstig <30827238+thernstig@users.noreply.github.com>
-# Copyright (c) 2018 Radostin Stoyanov <rst0git@users.noreply.github.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Emacs and Flymake compatible Pylint.
-
-This script is for integration with emacs and is compatible with flymake mode.
-
-epylint walks out of python packages before invoking pylint. This avoids
-reporting import errors that occur when a module within a package uses the
-absolute import path to get another module within this package.
-
-For example:
-    - Suppose a package is structured as
-
-        a/__init__.py
-        a/b/x.py
-        a/c/y.py
-
-   - Then if y.py imports x as "from a.b import x" the following produces pylint
-     errors
-
-       cd a/c; pylint y.py
-
-   - The following obviously doesn't
-
-       pylint a/c/y.py
-
-   - As this script will be invoked by emacs within the directory of the file
-     we are checking we need to go out of it to avoid these false positives.
-
-
-You may also use py_run to run pylint with desired options and get back (or not)
-its output.
-"""
-import os
-import os.path as osp
-import shlex
-import sys
-from io import StringIO
-from subprocess import PIPE, Popen
-
-
-def _get_env():
-    """Extracts the environment PYTHONPATH and appends the current sys.path to
-    those."""
-    env = dict(os.environ)
-    env["PYTHONPATH"] = os.pathsep.join(sys.path)
-    return env
-
-
-def lint(filename, options=()):
-    """Pylint the given file.
-
-    When run from emacs we will be in the directory of a file, and passed its
-    filename.  If this file is part of a package and is trying to import other
-    modules from within its own package or another package rooted in a directory
-    below it, pylint will classify it as a failed import.
-
-    To get around this, we traverse down the directory tree to find the root of
-    the package this module is in.  We then invoke pylint from this directory.
-
-    Finally, we must correct the filenames in the output generated by pylint so
-    Emacs doesn't become confused (it will expect just the original filename,
-    while pylint may extend it with extra directories if we've traversed down
-    the tree)
-    """
-    # traverse downwards until we are out of a python package
-    full_path = osp.abspath(filename)
-    parent_path = osp.dirname(full_path)
-    child_path = osp.basename(full_path)
-
-    while parent_path != "/" and osp.exists(osp.join(parent_path, "__init__.py")):
-        child_path = osp.join(osp.basename(parent_path), child_path)
-        parent_path = osp.dirname(parent_path)
-
-    # Start pylint
-    # Ensure we use the python and pylint associated with the running epylint
-    run_cmd = "import sys; from pylint.lint import Run; Run(sys.argv[1:])"
-    cmd = (
-        [sys.executable, "-c", run_cmd]
-        + [
-            "--msg-template",
-            "{path}:{line}: {category} ({msg_id}, {symbol}, {obj}) {msg}",
-            "-r",
-            "n",
-            child_path,
-        ]
-        + list(options)
-    )
-    process = Popen(
-        cmd, stdout=PIPE, cwd=parent_path, env=_get_env(), universal_newlines=True
-    )
-
-    for line in process.stdout:
-        # remove pylintrc warning
-        if line.startswith("No config file found"):
-            continue
-
-        # modify the file name thats output to reverse the path traversal we made
-        parts = line.split(":")
-        if parts and parts[0] == child_path:
-            line = ":".join([filename] + parts[1:])
-        print(line, end=" ")
-
-    process.wait()
-    return process.returncode
-
-
-def py_run(command_options="", return_std=False, stdout=None, stderr=None):
-    """Run pylint from python
-
-    ``command_options`` is a string containing ``pylint`` command line options;
-    ``return_std`` (boolean) indicates return of created standard output
-    and error (see below);
-    ``stdout`` and ``stderr`` are 'file-like' objects in which standard output
-    could be written.
-
-    Calling agent is responsible for stdout/err management (creation, close).
-    Default standard output and error are those from sys,
-    or standalone ones (``subprocess.PIPE``) are used
-    if they are not set and ``return_std``.
-
-    If ``return_std`` is set to ``True``, this function returns a 2-uple
-    containing standard output and error related to created process,
-    as follows: ``(stdout, stderr)``.
-
-    To silently run Pylint on a module, and get its standard output and error:
-        >>> (pylint_stdout, pylint_stderr) = py_run( 'module_name.py', True)
-    """
-    # Detect if we use Python as executable or not, else default to `python`
-    executable = sys.executable if "python" in sys.executable else "python"
-
-    # Create command line to call pylint
-    epylint_part = [executable, "-c", "from pylint import epylint;epylint.Run()"]
-    options = shlex.split(command_options, posix=not sys.platform.startswith("win"))
-    cli = epylint_part + options
-
-    # Providing standard output and/or error if not set
-    if stdout is None:
-        if return_std:
-            stdout = PIPE
-        else:
-            stdout = sys.stdout
-    if stderr is None:
-        if return_std:
-            stderr = PIPE
-        else:
-            stderr = sys.stderr
-    # Call pylint in a subprocess
-    process = Popen(
-        cli,
-        shell=False,
-        stdout=stdout,
-        stderr=stderr,
-        env=_get_env(),
-        universal_newlines=True,
-    )
-    proc_stdout, proc_stderr = process.communicate()
-    # Return standard output and error
-    if return_std:
-        return StringIO(proc_stdout), StringIO(proc_stderr)
-    return None
-
-
-def Run():
-    if len(sys.argv) == 1:
-        print("Usage: %s <filename> [options]" % sys.argv[0])
-        sys.exit(1)
-    elif not osp.exists(sys.argv[1]):
-        print("%s does not exist" % sys.argv[1])
-        sys.exit(1)
-    else:
-        sys.exit(lint(sys.argv[1], sys.argv[2:]))
-
-
-if __name__ == "__main__":
-    Run()
diff --git a/venv/Lib/site-packages/pylint/exceptions.py b/venv/Lib/site-packages/pylint/exceptions.py
deleted file mode 100644
index d5dd17f..0000000
--- a/venv/Lib/site-packages/pylint/exceptions.py
+++ /dev/null
@@ -1,29 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Exception classes raised by various operations within pylint."""
-
-
-class InvalidMessageError(Exception):
-    """raised when a message creation, registration or addition is rejected"""
-
-
-class UnknownMessageError(Exception):
-    """raised when an unregistered message id is encountered"""
-
-
-class EmptyReportError(Exception):
-    """raised when a report is empty and so should not be displayed"""
-
-
-class InvalidReporterError(Exception):
-    """raised when selected reporter is invalid (e.g. not found)"""
-
-
-class InvalidArgsError(ValueError):
-    """raised when passed arguments are invalid, e.g., have the wrong length"""
diff --git a/venv/Lib/site-packages/pylint/extensions/__init__.py b/venv/Lib/site-packages/pylint/extensions/__init__.py
deleted file mode 100644
index e69de29..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__init__.py
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 03323e7..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/_check_docs_utils.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/_check_docs_utils.cpython-37.pyc
deleted file mode 100644
index 271e216..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/_check_docs_utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/bad_builtin.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/bad_builtin.cpython-37.pyc
deleted file mode 100644
index bb50903..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/bad_builtin.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/broad_try_clause.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/broad_try_clause.cpython-37.pyc
deleted file mode 100644
index cd3cd71..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/broad_try_clause.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/check_docs.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/check_docs.cpython-37.pyc
deleted file mode 100644
index 9730100..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/check_docs.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/check_elif.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/check_elif.cpython-37.pyc
deleted file mode 100644
index 030378b..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/check_elif.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/comparetozero.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/comparetozero.cpython-37.pyc
deleted file mode 100644
index 83eaae3..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/comparetozero.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/docparams.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/docparams.cpython-37.pyc
deleted file mode 100644
index 3d447e1..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/docparams.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/docstyle.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/docstyle.cpython-37.pyc
deleted file mode 100644
index e6d0d7d..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/docstyle.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/emptystring.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/emptystring.cpython-37.pyc
deleted file mode 100644
index f5f4892..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/emptystring.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/mccabe.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/mccabe.cpython-37.pyc
deleted file mode 100644
index cb64a4d..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/mccabe.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/overlapping_exceptions.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/overlapping_exceptions.cpython-37.pyc
deleted file mode 100644
index f099683..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/overlapping_exceptions.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/__pycache__/redefined_variable_type.cpython-37.pyc b/venv/Lib/site-packages/pylint/extensions/__pycache__/redefined_variable_type.cpython-37.pyc
deleted file mode 100644
index eb897a3..0000000
--- a/venv/Lib/site-packages/pylint/extensions/__pycache__/redefined_variable_type.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/extensions/_check_docs_utils.py b/venv/Lib/site-packages/pylint/extensions/_check_docs_utils.py
deleted file mode 100644
index fe1603f..0000000
--- a/venv/Lib/site-packages/pylint/extensions/_check_docs_utils.py
+++ /dev/null
@@ -1,792 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016-2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Yuri Bochkarev <baltazar.bz@gmail.com>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Mitar <mitar.github@tnode.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 Mitchell T.H. Young <mitchelly@gmail.com>
-# Copyright (c) 2018 Adrian Chirieac <chirieacam@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Utility methods for docstring checking."""
-
-import re
-
-import astroid
-
-from pylint.checkers import utils
-
-
-def space_indentation(s):
-    """The number of leading spaces in a string
-
-    :param str s: input string
-
-    :rtype: int
-    :return: number of leading spaces
-    """
-    return len(s) - len(s.lstrip(" "))
-
-
-def get_setters_property_name(node):
-    """Get the name of the property that the given node is a setter for.
-
-    :param node: The node to get the property name for.
-    :type node: str
-
-    :rtype: str or None
-    :returns: The name of the property that the node is a setter for,
-        or None if one could not be found.
-    """
-    decorators = node.decorators.nodes if node.decorators else []
-    for decorator in decorators:
-        if (
-            isinstance(decorator, astroid.Attribute)
-            and decorator.attrname == "setter"
-            and isinstance(decorator.expr, astroid.Name)
-        ):
-            return decorator.expr.name
-    return None
-
-
-def get_setters_property(node):
-    """Get the property node for the given setter node.
-
-    :param node: The node to get the property for.
-    :type node: astroid.FunctionDef
-
-    :rtype: astroid.FunctionDef or None
-    :returns: The node relating to the property of the given setter node,
-        or None if one could not be found.
-    """
-    property_ = None
-
-    property_name = get_setters_property_name(node)
-    class_node = utils.node_frame_class(node)
-    if property_name and class_node:
-        class_attrs = class_node.getattr(node.name)
-        for attr in class_attrs:
-            if utils.decorated_with_property(attr):
-                property_ = attr
-                break
-
-    return property_
-
-
-def returns_something(return_node):
-    """Check if a return node returns a value other than None.
-
-    :param return_node: The return node to check.
-    :type return_node: astroid.Return
-
-    :rtype: bool
-    :return: True if the return node returns a value other than None,
-        False otherwise.
-    """
-    returns = return_node.value
-
-    if returns is None:
-        return False
-
-    return not (isinstance(returns, astroid.Const) and returns.value is None)
-
-
-def _get_raise_target(node):
-    if isinstance(node.exc, astroid.Call):
-        func = node.exc.func
-        if isinstance(func, (astroid.Name, astroid.Attribute)):
-            return utils.safe_infer(func)
-    return None
-
-
-def possible_exc_types(node):
-    """
-    Gets all of the possible raised exception types for the given raise node.
-
-    .. note::
-
-        Caught exception types are ignored.
-
-
-    :param node: The raise node to find exception types for.
-    :type node: astroid.node_classes.NodeNG
-
-    :returns: A list of exception types possibly raised by :param:`node`.
-    :rtype: set(str)
-    """
-    excs = []
-    if isinstance(node.exc, astroid.Name):
-        inferred = utils.safe_infer(node.exc)
-        if inferred:
-            excs = [inferred.name]
-    elif node.exc is None:
-        handler = node.parent
-        while handler and not isinstance(handler, astroid.ExceptHandler):
-            handler = handler.parent
-
-        if handler and handler.type:
-            inferred_excs = astroid.unpack_infer(handler.type)
-            excs = (exc.name for exc in inferred_excs if exc is not astroid.Uninferable)
-    else:
-        target = _get_raise_target(node)
-        if isinstance(target, astroid.ClassDef):
-            excs = [target.name]
-        elif isinstance(target, astroid.FunctionDef):
-            for ret in target.nodes_of_class(astroid.Return):
-                if ret.frame() != target:
-                    # return from inner function - ignore it
-                    continue
-
-                val = utils.safe_infer(ret.value)
-                if (
-                    val
-                    and isinstance(val, (astroid.Instance, astroid.ClassDef))
-                    and utils.inherit_from_std_ex(val)
-                ):
-                    excs.append(val.name)
-
-    try:
-        return {exc for exc in excs if not utils.node_ignores_exception(node, exc)}
-    except astroid.InferenceError:
-        return set()
-
-
-def docstringify(docstring, default_type="default"):
-    for docstring_type in [
-        SphinxDocstring,
-        EpytextDocstring,
-        GoogleDocstring,
-        NumpyDocstring,
-    ]:
-        instance = docstring_type(docstring)
-        if instance.is_valid():
-            return instance
-
-    docstring_type = DOCSTRING_TYPES.get(default_type, Docstring)
-    return docstring_type(docstring)
-
-
-class Docstring:
-    re_for_parameters_see = re.compile(
-        r"""
-        For\s+the\s+(other)?\s*parameters\s*,\s+see
-        """,
-        re.X | re.S,
-    )
-
-    supports_yields = None
-    """True if the docstring supports a "yield" section.
-
-    False if the docstring uses the returns section to document generators.
-    """
-
-    # These methods are designed to be overridden
-    # pylint: disable=no-self-use
-    def __init__(self, doc):
-        doc = doc or ""
-        self.doc = doc.expandtabs()
-
-    def is_valid(self):
-        return False
-
-    def exceptions(self):
-        return set()
-
-    def has_params(self):
-        return False
-
-    def has_returns(self):
-        return False
-
-    def has_rtype(self):
-        return False
-
-    def has_property_returns(self):
-        return False
-
-    def has_property_type(self):
-        return False
-
-    def has_yields(self):
-        return False
-
-    def has_yields_type(self):
-        return False
-
-    def match_param_docs(self):
-        return set(), set()
-
-    def params_documented_elsewhere(self):
-        return self.re_for_parameters_see.search(self.doc) is not None
-
-
-class SphinxDocstring(Docstring):
-    re_type = r"""
-        [~!.]?               # Optional link style prefix
-        \w(?:\w|\.[^\.])*    # Valid python name
-        """
-
-    re_simple_container_type = r"""
-        {type}                        # a container type
-        [\(\[] [^\n\s]+ [\)\]]        # with the contents of the container
-    """.format(
-        type=re_type
-    )
-
-    re_xref = r"""
-        (?::\w+:)?                    # optional tag
-        `{}`                         # what to reference
-        """.format(
-        re_type
-    )
-
-    re_param_raw = r"""
-        :                       # initial colon
-        (?:                     # Sphinx keywords
-        param|parameter|
-        arg|argument|
-        key|keyword
-        )
-        \s+                     # whitespace
-
-        (?:                     # optional type declaration
-        ({type}|{container_type})
-        \s+
-        )?
-
-        (\w+)                   # Parameter name
-        \s*                     # whitespace
-        :                       # final colon
-        """.format(
-        type=re_type, container_type=re_simple_container_type
-    )
-    re_param_in_docstring = re.compile(re_param_raw, re.X | re.S)
-
-    re_type_raw = r"""
-        :type                   # Sphinx keyword
-        \s+                     # whitespace
-        ({type})                # Parameter name
-        \s*                     # whitespace
-        :                       # final colon
-        """.format(
-        type=re_type
-    )
-    re_type_in_docstring = re.compile(re_type_raw, re.X | re.S)
-
-    re_property_type_raw = r"""
-        :type:                  # Sphinx keyword
-        \s+                     # whitespace
-        {type}                  # type declaration
-        """.format(
-        type=re_type
-    )
-    re_property_type_in_docstring = re.compile(re_property_type_raw, re.X | re.S)
-
-    re_raise_raw = r"""
-        :                       # initial colon
-        (?:                     # Sphinx keyword
-        raises?|
-        except|exception
-        )
-        \s+                     # whitespace
-        ({type})                # exception type
-        \s*                     # whitespace
-        :                       # final colon
-        """.format(
-        type=re_type
-    )
-    re_raise_in_docstring = re.compile(re_raise_raw, re.X | re.S)
-
-    re_rtype_in_docstring = re.compile(r":rtype:")
-
-    re_returns_in_docstring = re.compile(r":returns?:")
-
-    supports_yields = False
-
-    def is_valid(self):
-        return bool(
-            self.re_param_in_docstring.search(self.doc)
-            or self.re_raise_in_docstring.search(self.doc)
-            or self.re_rtype_in_docstring.search(self.doc)
-            or self.re_returns_in_docstring.search(self.doc)
-            or self.re_property_type_in_docstring.search(self.doc)
-        )
-
-    def exceptions(self):
-        types = set()
-
-        for match in re.finditer(self.re_raise_in_docstring, self.doc):
-            raise_type = match.group(1)
-            types.add(raise_type)
-
-        return types
-
-    def has_params(self):
-        if not self.doc:
-            return False
-
-        return self.re_param_in_docstring.search(self.doc) is not None
-
-    def has_returns(self):
-        if not self.doc:
-            return False
-
-        return bool(self.re_returns_in_docstring.search(self.doc))
-
-    def has_rtype(self):
-        if not self.doc:
-            return False
-
-        return bool(self.re_rtype_in_docstring.search(self.doc))
-
-    def has_property_returns(self):
-        if not self.doc:
-            return False
-
-        # The summary line is the return doc,
-        # so the first line must not be a known directive.
-        return not self.doc.lstrip().startswith(":")
-
-    def has_property_type(self):
-        if not self.doc:
-            return False
-
-        return bool(self.re_property_type_in_docstring.search(self.doc))
-
-    def match_param_docs(self):
-        params_with_doc = set()
-        params_with_type = set()
-
-        for match in re.finditer(self.re_param_in_docstring, self.doc):
-            name = match.group(2)
-            params_with_doc.add(name)
-            param_type = match.group(1)
-            if param_type is not None:
-                params_with_type.add(name)
-
-        params_with_type.update(re.findall(self.re_type_in_docstring, self.doc))
-        return params_with_doc, params_with_type
-
-
-class EpytextDocstring(SphinxDocstring):
-    """
-    Epytext is similar to Sphinx. See the docs:
-        http://epydoc.sourceforge.net/epytext.html
-        http://epydoc.sourceforge.net/fields.html#fields
-
-    It's used in PyCharm:
-        https://www.jetbrains.com/help/pycharm/2016.1/creating-documentation-comments.html#d848203e314
-        https://www.jetbrains.com/help/pycharm/2016.1/using-docstrings-to-specify-types.html
-    """
-
-    re_param_in_docstring = re.compile(
-        SphinxDocstring.re_param_raw.replace(":", "@", 1), re.X | re.S
-    )
-
-    re_type_in_docstring = re.compile(
-        SphinxDocstring.re_type_raw.replace(":", "@", 1), re.X | re.S
-    )
-
-    re_property_type_in_docstring = re.compile(
-        SphinxDocstring.re_property_type_raw.replace(":", "@", 1), re.X | re.S
-    )
-
-    re_raise_in_docstring = re.compile(
-        SphinxDocstring.re_raise_raw.replace(":", "@", 1), re.X | re.S
-    )
-
-    re_rtype_in_docstring = re.compile(
-        r"""
-        @                       # initial "at" symbol
-        (?:                     # Epytext keyword
-        rtype|returntype
-        )
-        :                       # final colon
-        """,
-        re.X | re.S,
-    )
-
-    re_returns_in_docstring = re.compile(r"@returns?:")
-
-    def has_property_returns(self):
-        if not self.doc:
-            return False
-
-        # If this is a property docstring, the summary is the return doc.
-        if self.has_property_type():
-            # The summary line is the return doc,
-            # so the first line must not be a known directive.
-            return not self.doc.lstrip().startswith("@")
-
-        return False
-
-
-class GoogleDocstring(Docstring):
-    re_type = SphinxDocstring.re_type
-
-    re_xref = SphinxDocstring.re_xref
-
-    re_container_type = r"""
-        (?:{type}|{xref})             # a container type
-        [\(\[] [^\n]+ [\)\]]          # with the contents of the container
-    """.format(
-        type=re_type, xref=re_xref
-    )
-
-    re_multiple_type = r"""
-        (?:{container_type}|{type}|{xref})
-        (?:\s+(?:of|or)\s+(?:{container_type}|{type}|{xref}))*
-    """.format(
-        type=re_type, xref=re_xref, container_type=re_container_type
-    )
-
-    _re_section_template = r"""
-        ^([ ]*)   {0} \s*:   \s*$     # Google parameter header
-        (  .* )                       # section
-        """
-
-    re_param_section = re.compile(
-        _re_section_template.format(r"(?:Args|Arguments|Parameters)"),
-        re.X | re.S | re.M,
-    )
-
-    re_keyword_param_section = re.compile(
-        _re_section_template.format(r"Keyword\s(?:Args|Arguments|Parameters)"),
-        re.X | re.S | re.M,
-    )
-
-    re_param_line = re.compile(
-        r"""
-        \s*  \*{{0,2}}(\w+)             # identifier potentially with asterisks
-        \s*  ( [(]
-            {type}
-            (?:,\s+optional)?
-            [)] )? \s* :                # optional type declaration
-        \s*  (.*)                       # beginning of optional description
-    """.format(
-            type=re_multiple_type
-        ),
-        re.X | re.S | re.M,
-    )
-
-    re_raise_section = re.compile(
-        _re_section_template.format(r"Raises"), re.X | re.S | re.M
-    )
-
-    re_raise_line = re.compile(
-        r"""
-        \s*  ({type}) \s* :              # identifier
-        \s*  (.*)                        # beginning of optional description
-    """.format(
-            type=re_type
-        ),
-        re.X | re.S | re.M,
-    )
-
-    re_returns_section = re.compile(
-        _re_section_template.format(r"Returns?"), re.X | re.S | re.M
-    )
-
-    re_returns_line = re.compile(
-        r"""
-        \s* ({type}:)?                    # identifier
-        \s* (.*)                          # beginning of description
-    """.format(
-            type=re_multiple_type
-        ),
-        re.X | re.S | re.M,
-    )
-
-    re_property_returns_line = re.compile(
-        r"""
-        ^{type}:                       # indentifier
-        \s* (.*)                       # Summary line / description
-    """.format(
-            type=re_multiple_type
-        ),
-        re.X | re.S | re.M,
-    )
-
-    re_yields_section = re.compile(
-        _re_section_template.format(r"Yields?"), re.X | re.S | re.M
-    )
-
-    re_yields_line = re_returns_line
-
-    supports_yields = True
-
-    def is_valid(self):
-        return bool(
-            self.re_param_section.search(self.doc)
-            or self.re_raise_section.search(self.doc)
-            or self.re_returns_section.search(self.doc)
-            or self.re_yields_section.search(self.doc)
-            or self.re_property_returns_line.search(self._first_line())
-        )
-
-    def has_params(self):
-        if not self.doc:
-            return False
-
-        return self.re_param_section.search(self.doc) is not None
-
-    def has_returns(self):
-        if not self.doc:
-            return False
-
-        entries = self._parse_section(self.re_returns_section)
-        for entry in entries:
-            match = self.re_returns_line.match(entry)
-            if not match:
-                continue
-
-            return_desc = match.group(2)
-            if return_desc:
-                return True
-
-        return False
-
-    def has_rtype(self):
-        if not self.doc:
-            return False
-
-        entries = self._parse_section(self.re_returns_section)
-        for entry in entries:
-            match = self.re_returns_line.match(entry)
-            if not match:
-                continue
-
-            return_type = match.group(1)
-            if return_type:
-                return True
-
-        return False
-
-    def has_property_returns(self):
-        # The summary line is the return doc,
-        # so the first line must not be a known directive.
-        first_line = self._first_line()
-        return not bool(
-            self.re_param_section.search(first_line)
-            or self.re_raise_section.search(first_line)
-            or self.re_returns_section.search(first_line)
-            or self.re_yields_section.search(first_line)
-        )
-
-    def has_property_type(self):
-        if not self.doc:
-            return False
-
-        return bool(self.re_property_returns_line.match(self._first_line()))
-
-    def has_yields(self):
-        if not self.doc:
-            return False
-
-        entries = self._parse_section(self.re_yields_section)
-        for entry in entries:
-            match = self.re_yields_line.match(entry)
-            if not match:
-                continue
-
-            yield_desc = match.group(2)
-            if yield_desc:
-                return True
-
-        return False
-
-    def has_yields_type(self):
-        if not self.doc:
-            return False
-
-        entries = self._parse_section(self.re_yields_section)
-        for entry in entries:
-            match = self.re_yields_line.match(entry)
-            if not match:
-                continue
-
-            yield_type = match.group(1)
-            if yield_type:
-                return True
-
-        return False
-
-    def exceptions(self):
-        types = set()
-
-        entries = self._parse_section(self.re_raise_section)
-        for entry in entries:
-            match = self.re_raise_line.match(entry)
-            if not match:
-                continue
-
-            exc_type = match.group(1)
-            exc_desc = match.group(2)
-            if exc_desc:
-                types.add(exc_type)
-
-        return types
-
-    def match_param_docs(self):
-        params_with_doc = set()
-        params_with_type = set()
-
-        entries = self._parse_section(self.re_param_section)
-        entries.extend(self._parse_section(self.re_keyword_param_section))
-        for entry in entries:
-            match = self.re_param_line.match(entry)
-            if not match:
-                continue
-
-            param_name = match.group(1)
-            param_type = match.group(2)
-            param_desc = match.group(3)
-            if param_type:
-                params_with_type.add(param_name)
-
-            if param_desc:
-                params_with_doc.add(param_name)
-
-        return params_with_doc, params_with_type
-
-    def _first_line(self):
-        return self.doc.lstrip().split("\n", 1)[0]
-
-    @staticmethod
-    def min_section_indent(section_match):
-        return len(section_match.group(1)) + 1
-
-    @staticmethod
-    def _is_section_header(_):
-        # Google parsing does not need to detect section headers,
-        # because it works off of indentation level only
-        return False
-
-    def _parse_section(self, section_re):
-        section_match = section_re.search(self.doc)
-        if section_match is None:
-            return []
-
-        min_indentation = self.min_section_indent(section_match)
-
-        entries = []
-        entry = []
-        is_first = True
-        for line in section_match.group(2).splitlines():
-            if not line.strip():
-                continue
-            indentation = space_indentation(line)
-            if indentation < min_indentation:
-                break
-
-            # The first line after the header defines the minimum
-            # indentation.
-            if is_first:
-                min_indentation = indentation
-                is_first = False
-
-            if indentation == min_indentation:
-                if self._is_section_header(line):
-                    break
-                # Lines with minimum indentation must contain the beginning
-                # of a new parameter documentation.
-                if entry:
-                    entries.append("\n".join(entry))
-                    entry = []
-
-            entry.append(line)
-
-        if entry:
-            entries.append("\n".join(entry))
-
-        return entries
-
-
-class NumpyDocstring(GoogleDocstring):
-    _re_section_template = r"""
-        ^([ ]*)   {0}   \s*?$          # Numpy parameters header
-        \s*     [-=]+   \s*?$          # underline
-        (  .* )                        # section
-    """
-
-    re_param_section = re.compile(
-        _re_section_template.format(r"(?:Args|Arguments|Parameters)"),
-        re.X | re.S | re.M,
-    )
-
-    re_param_line = re.compile(
-        r"""
-        \s*  (\w+)                      # identifier
-        \s*  :
-        \s*  (?:({type})(?:,\s+optional)?)? # optional type declaration
-        \n                              # description starts on a new line
-        \s* (.*)                        # description
-    """.format(
-            type=GoogleDocstring.re_multiple_type
-        ),
-        re.X | re.S,
-    )
-
-    re_raise_section = re.compile(
-        _re_section_template.format(r"Raises"), re.X | re.S | re.M
-    )
-
-    re_raise_line = re.compile(
-        r"""
-        \s* ({type})$   # type declaration
-        \s* (.*)        # optional description
-    """.format(
-            type=GoogleDocstring.re_type
-        ),
-        re.X | re.S | re.M,
-    )
-
-    re_returns_section = re.compile(
-        _re_section_template.format(r"Returns?"), re.X | re.S | re.M
-    )
-
-    re_returns_line = re.compile(
-        r"""
-        \s* (?:\w+\s+:\s+)? # optional name
-        ({type})$                         # type declaration
-        \s* (.*)                          # optional description
-    """.format(
-            type=GoogleDocstring.re_multiple_type
-        ),
-        re.X | re.S | re.M,
-    )
-
-    re_yields_section = re.compile(
-        _re_section_template.format(r"Yields?"), re.X | re.S | re.M
-    )
-
-    re_yields_line = re_returns_line
-
-    supports_yields = True
-
-    @staticmethod
-    def min_section_indent(section_match):
-        return len(section_match.group(1))
-
-    @staticmethod
-    def _is_section_header(line):
-        return bool(re.match(r"\s*-+$", line))
-
-
-DOCSTRING_TYPES = {
-    "sphinx": SphinxDocstring,
-    "epytext": EpytextDocstring,
-    "google": GoogleDocstring,
-    "numpy": NumpyDocstring,
-    "default": Docstring,
-}
-"""A map of the name of the docstring type to its class.
-
-:type: dict(str, type)
-"""
diff --git a/venv/Lib/site-packages/pylint/extensions/bad_builtin.py b/venv/Lib/site-packages/pylint/extensions/bad_builtin.py
deleted file mode 100644
index 754c409..0000000
--- a/venv/Lib/site-packages/pylint/extensions/bad_builtin.py
+++ /dev/null
@@ -1,69 +0,0 @@
-# Copyright (c) 2016 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Checker for deprecated builtins."""
-import astroid
-
-from pylint.checkers import BaseChecker
-from pylint.checkers.utils import check_messages
-from pylint.interfaces import IAstroidChecker
-
-BAD_FUNCTIONS = ["map", "filter"]
-# Some hints regarding the use of bad builtins.
-BUILTIN_HINTS = {"map": "Using a list comprehension can be clearer."}
-BUILTIN_HINTS["filter"] = BUILTIN_HINTS["map"]
-
-
-class BadBuiltinChecker(BaseChecker):
-
-    __implements__ = (IAstroidChecker,)
-    name = "deprecated_builtins"
-    msgs = {
-        "W0141": (
-            "Used builtin function %s",
-            "bad-builtin",
-            "Used when a black listed builtin function is used (see the "
-            "bad-function option). Usual black listed functions are the ones "
-            "like map, or filter , where Python offers now some cleaner "
-            "alternative like list comprehension.",
-        )
-    }
-
-    options = (
-        (
-            "bad-functions",
-            {
-                "default": BAD_FUNCTIONS,
-                "type": "csv",
-                "metavar": "<builtin function names>",
-                "help": "List of builtins function names that should not be "
-                "used, separated by a comma",
-            },
-        ),
-    )
-
-    @check_messages("bad-builtin")
-    def visit_call(self, node):
-        if isinstance(node.func, astroid.Name):
-            name = node.func.name
-            # ignore the name if it's not a builtin (i.e. not defined in the
-            # locals nor globals scope)
-            if not (name in node.frame() or name in node.root()):
-                if name in self.config.bad_functions:
-                    hint = BUILTIN_HINTS.get(name)
-                    if hint:
-                        args = "%r. %s" % (name, hint)
-                    else:
-                        args = repr(name)
-                    self.add_message("bad-builtin", node=node, args=args)
-
-
-def register(linter):
-    """Required method to auto register this checker.
-
-    :param linter: Main interface object for Pylint plugins
-    :type linter: Pylint object
-    """
-    linter.register_checker(BadBuiltinChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/broad_try_clause.py b/venv/Lib/site-packages/pylint/extensions/broad_try_clause.py
deleted file mode 100644
index 9a61fb6..0000000
--- a/venv/Lib/site-packages/pylint/extensions/broad_try_clause.py
+++ /dev/null
@@ -1,59 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2019 Tyler N. Thieding <python@thieding.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Looks for try/except statements with too much code in the try clause."""
-
-from pylint import checkers, interfaces
-
-
-class BroadTryClauseChecker(checkers.BaseChecker):
-    """Checks for try clauses with too many lines.
-
-    According to PEP 8, ``try`` clauses shall contain the absolute minimum
-    amount of code. This checker enforces a maximum number of statements within
-    ``try`` clauses.
-
-    """
-
-    __implements__ = interfaces.IAstroidChecker
-
-    # configuration section name
-    name = "broad_try_clause"
-    msgs = {
-        "W0717": (
-            "%s",
-            "too-many-try-statements",
-            "Try clause contains too many statements.",
-        )
-    }
-
-    priority = -2
-    options = (
-        (
-            "max-try-statements",
-            {
-                "default": 1,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "Maximum number of statements allowed in a try clause",
-            },
-        ),
-    )
-
-    def visit_tryexcept(self, node):
-        try_clause_statements = len(node.body)
-        if try_clause_statements > self.config.max_try_statements:
-            msg = "try clause contains {0} statements, expected at most {1}".format(
-                try_clause_statements, self.config.max_try_statements
-            )
-            self.add_message(
-                "too-many-try-statements", node.lineno, node=node, args=msg
-            )
-
-
-def register(linter):
-    """Required method to auto register this checker."""
-    linter.register_checker(BroadTryClauseChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/check_docs.py b/venv/Lib/site-packages/pylint/extensions/check_docs.py
deleted file mode 100644
index 7f7f643..0000000
--- a/venv/Lib/site-packages/pylint/extensions/check_docs.py
+++ /dev/null
@@ -1,23 +0,0 @@
-# Copyright (c) 2014-2015 Bruno Daniel <bruno.daniel@blue-yonder.com>
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import warnings
-
-from pylint.extensions import docparams
-
-
-def register(linter):
-    """Required method to auto register this checker.
-
-    :param linter: Main interface object for Pylint plugins
-    :type linter: Pylint object
-    """
-    warnings.warn(
-        "This plugin is deprecated, use pylint.extensions.docparams instead.",
-        DeprecationWarning,
-    )
-    linter.register_checker(docparams.DocstringParameterChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/check_elif.py b/venv/Lib/site-packages/pylint/extensions/check_elif.py
deleted file mode 100644
index 67555b1..0000000
--- a/venv/Lib/site-packages/pylint/extensions/check_elif.py
+++ /dev/null
@@ -1,77 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Glenn Matthews <glmatthe@cisco.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import astroid
-
-from pylint.checkers import BaseTokenChecker
-from pylint.checkers.utils import check_messages
-from pylint.interfaces import IAstroidChecker, ITokenChecker
-
-
-class ElseifUsedChecker(BaseTokenChecker):
-    """Checks for use of "else if" when an "elif" could be used
-    """
-
-    __implements__ = (ITokenChecker, IAstroidChecker)
-    name = "else_if_used"
-    msgs = {
-        "R5501": (
-            'Consider using "elif" instead of "else if"',
-            "else-if-used",
-            "Used when an else statement is immediately followed by "
-            "an if statement and does not contain statements that "
-            "would be unrelated to it.",
-        )
-    }
-
-    def __init__(self, linter=None):
-        BaseTokenChecker.__init__(self, linter)
-        self._init()
-
-    def _init(self):
-        self._elifs = []
-        self._if_counter = 0
-
-    def process_tokens(self, tokens):
-        # Process tokens and look for 'if' or 'elif'
-        for _, token, _, _, _ in tokens:
-            if token == "elif":
-                self._elifs.append(True)
-            elif token == "if":
-                self._elifs.append(False)
-
-    def leave_module(self, _):
-        self._init()
-
-    def visit_ifexp(self, node):
-        if isinstance(node.parent, astroid.FormattedValue):
-            return
-        self._if_counter += 1
-
-    def visit_comprehension(self, node):
-        self._if_counter += len(node.ifs)
-
-    @check_messages("else-if-used")
-    def visit_if(self, node):
-        if isinstance(node.parent, astroid.If):
-            orelse = node.parent.orelse
-            # current if node must directly follow an "else"
-            if orelse and orelse == [node]:
-                if not self._elifs[self._if_counter]:
-                    self.add_message("else-if-used", node=node)
-        self._if_counter += 1
-
-
-def register(linter):
-    """Required method to auto register this checker.
-
-    :param linter: Main interface object for Pylint plugins
-    :type linter: Pylint object
-    """
-    linter.register_checker(ElseifUsedChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/comparetozero.py b/venv/Lib/site-packages/pylint/extensions/comparetozero.py
deleted file mode 100644
index e31f488..0000000
--- a/venv/Lib/site-packages/pylint/extensions/comparetozero.py
+++ /dev/null
@@ -1,74 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2017 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Looks for  comparisons to empty string."""
-
-import itertools
-
-import astroid
-
-from pylint import checkers, interfaces
-from pylint.checkers import utils
-
-
-def _is_constant_zero(node):
-    return isinstance(node, astroid.Const) and node.value == 0
-
-
-class CompareToZeroChecker(checkers.BaseChecker):
-    """Checks for comparisons to zero.
-    Most of the times you should use the fact that integers with a value of 0 are false.
-    An exception to this rule is when 0 is allowed in the program and has a
-    different meaning than None!
-    """
-
-    __implements__ = (interfaces.IAstroidChecker,)
-
-    # configuration section name
-    name = "compare-to-zero"
-    msgs = {
-        "C2001": (
-            "Avoid comparisons to zero",
-            "compare-to-zero",
-            "Used when Pylint detects comparison to a 0 constant.",
-        )
-    }
-
-    priority = -2
-    options = ()
-
-    @utils.check_messages("compare-to-zero")
-    def visit_compare(self, node):
-        _operators = ["!=", "==", "is not", "is"]
-        # note: astroid.Compare has the left most operand in node.left
-        # while the rest are a list of tuples in node.ops
-        # the format of the tuple is ('compare operator sign', node)
-        # here we squash everything into `ops` to make it easier for processing later
-        ops = [("", node.left)]
-        ops.extend(node.ops)
-        ops = list(itertools.chain(*ops))
-
-        for ops_idx in range(len(ops) - 2):
-            op_1 = ops[ops_idx]
-            op_2 = ops[ops_idx + 1]
-            op_3 = ops[ops_idx + 2]
-            error_detected = False
-
-            # 0 ?? X
-            if _is_constant_zero(op_1) and op_2 in _operators:
-                error_detected = True
-            # X ?? 0
-            elif op_2 in _operators and _is_constant_zero(op_3):
-                error_detected = True
-
-            if error_detected:
-                self.add_message("compare-to-zero", node=node)
-
-
-def register(linter):
-    """Required method to auto register this checker."""
-    linter.register_checker(CompareToZeroChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/docparams.py b/venv/Lib/site-packages/pylint/extensions/docparams.py
deleted file mode 100644
index d5a15a4..0000000
--- a/venv/Lib/site-packages/pylint/extensions/docparams.py
+++ /dev/null
@@ -1,536 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2014-2015 Bruno Daniel <bruno.daniel@blue-yonder.com>
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016-2018 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2016 Glenn Matthews <glmatthe@cisco.com>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2017 John Paraskevopoulos <io.paraskev@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Adam Dangoor <adamdangoor@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Pylint plugin for checking in Sphinx, Google, or Numpy style docstrings
-"""
-import astroid
-
-import pylint.extensions._check_docs_utils as utils
-from pylint.checkers import BaseChecker
-from pylint.checkers import utils as checker_utils
-from pylint.interfaces import IAstroidChecker
-
-
-class DocstringParameterChecker(BaseChecker):
-    """Checker for Sphinx, Google, or Numpy style docstrings
-
-    * Check that all function, method and constructor parameters are mentioned
-      in the params and types part of the docstring.  Constructor parameters
-      can be documented in either the class docstring or ``__init__`` docstring,
-      but not both.
-    * Check that there are no naming inconsistencies between the signature and
-      the documentation, i.e. also report documented parameters that are missing
-      in the signature. This is important to find cases where parameters are
-      renamed only in the code, not in the documentation.
-    * Check that all explicitly raised exceptions in a function are documented
-      in the function docstring. Caught exceptions are ignored.
-
-    Activate this checker by adding the line::
-
-        load-plugins=pylint.extensions.docparams
-
-    to the ``MASTER`` section of your ``.pylintrc``.
-
-    :param linter: linter object
-    :type linter: :class:`pylint.lint.PyLinter`
-    """
-
-    __implements__ = IAstroidChecker
-
-    name = "parameter_documentation"
-    msgs = {
-        "W9005": (
-            '"%s" has constructor parameters documented in class and __init__',
-            "multiple-constructor-doc",
-            "Please remove parameter declarations in the class or constructor.",
-        ),
-        "W9006": (
-            '"%s" not documented as being raised',
-            "missing-raises-doc",
-            "Please document exceptions for all raised exception types.",
-        ),
-        "W9008": (
-            "Redundant returns documentation",
-            "redundant-returns-doc",
-            "Please remove the return/rtype documentation from this method.",
-        ),
-        "W9010": (
-            "Redundant yields documentation",
-            "redundant-yields-doc",
-            "Please remove the yields documentation from this method.",
-        ),
-        "W9011": (
-            "Missing return documentation",
-            "missing-return-doc",
-            "Please add documentation about what this method returns.",
-            {"old_names": [("W9007", "old-missing-returns-doc")]},
-        ),
-        "W9012": (
-            "Missing return type documentation",
-            "missing-return-type-doc",
-            "Please document the type returned by this method.",
-            # we can't use the same old_name for two different warnings
-            # {'old_names': [('W9007', 'missing-returns-doc')]},
-        ),
-        "W9013": (
-            "Missing yield documentation",
-            "missing-yield-doc",
-            "Please add documentation about what this generator yields.",
-            {"old_names": [("W9009", "old-missing-yields-doc")]},
-        ),
-        "W9014": (
-            "Missing yield type documentation",
-            "missing-yield-type-doc",
-            "Please document the type yielded by this method.",
-            # we can't use the same old_name for two different warnings
-            # {'old_names': [('W9009', 'missing-yields-doc')]},
-        ),
-        "W9015": (
-            '"%s" missing in parameter documentation',
-            "missing-param-doc",
-            "Please add parameter declarations for all parameters.",
-            {"old_names": [("W9003", "old-missing-param-doc")]},
-        ),
-        "W9016": (
-            '"%s" missing in parameter type documentation',
-            "missing-type-doc",
-            "Please add parameter type declarations for all parameters.",
-            {"old_names": [("W9004", "old-missing-type-doc")]},
-        ),
-        "W9017": (
-            '"%s" differing in parameter documentation',
-            "differing-param-doc",
-            "Please check parameter names in declarations.",
-        ),
-        "W9018": (
-            '"%s" differing in parameter type documentation',
-            "differing-type-doc",
-            "Please check parameter names in type declarations.",
-        ),
-    }
-
-    options = (
-        (
-            "accept-no-param-doc",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y or n>",
-                "help": "Whether to accept totally missing parameter "
-                "documentation in the docstring of a function that has "
-                "parameters.",
-            },
-        ),
-        (
-            "accept-no-raise-doc",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y or n>",
-                "help": "Whether to accept totally missing raises "
-                "documentation in the docstring of a function that "
-                "raises an exception.",
-            },
-        ),
-        (
-            "accept-no-return-doc",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y or n>",
-                "help": "Whether to accept totally missing return "
-                "documentation in the docstring of a function that "
-                "returns a statement.",
-            },
-        ),
-        (
-            "accept-no-yields-doc",
-            {
-                "default": True,
-                "type": "yn",
-                "metavar": "<y or n>",
-                "help": "Whether to accept totally missing yields "
-                "documentation in the docstring of a generator.",
-            },
-        ),
-        (
-            "default-docstring-type",
-            {
-                "type": "choice",
-                "default": "default",
-                "choices": list(utils.DOCSTRING_TYPES),
-                "help": "If the docstring type cannot be guessed "
-                "the specified docstring type will be used.",
-            },
-        ),
-    )
-
-    priority = -2
-
-    constructor_names = {"__init__", "__new__"}
-    not_needed_param_in_docstring = {"self", "cls"}
-
-    def visit_functiondef(self, node):
-        """Called for function and method definitions (def).
-
-        :param node: Node for a function or method definition in the AST
-        :type node: :class:`astroid.scoped_nodes.Function`
-        """
-        node_doc = utils.docstringify(node.doc, self.config.default_docstring_type)
-        self.check_functiondef_params(node, node_doc)
-        self.check_functiondef_returns(node, node_doc)
-        self.check_functiondef_yields(node, node_doc)
-
-    def check_functiondef_params(self, node, node_doc):
-        node_allow_no_param = None
-        if node.name in self.constructor_names:
-            class_node = checker_utils.node_frame_class(node)
-            if class_node is not None:
-                class_doc = utils.docstringify(
-                    class_node.doc, self.config.default_docstring_type
-                )
-                self.check_single_constructor_params(class_doc, node_doc, class_node)
-
-                # __init__ or class docstrings can have no parameters documented
-                # as long as the other documents them.
-                node_allow_no_param = (
-                    class_doc.has_params()
-                    or class_doc.params_documented_elsewhere()
-                    or None
-                )
-                class_allow_no_param = (
-                    node_doc.has_params()
-                    or node_doc.params_documented_elsewhere()
-                    or None
-                )
-
-                self.check_arguments_in_docstring(
-                    class_doc, node.args, class_node, class_allow_no_param
-                )
-
-        self.check_arguments_in_docstring(
-            node_doc, node.args, node, node_allow_no_param
-        )
-
-    def check_functiondef_returns(self, node, node_doc):
-        if (not node_doc.supports_yields and node.is_generator()) or node.is_abstract():
-            return
-
-        return_nodes = node.nodes_of_class(astroid.Return)
-        if (node_doc.has_returns() or node_doc.has_rtype()) and not any(
-            utils.returns_something(ret_node) for ret_node in return_nodes
-        ):
-            self.add_message("redundant-returns-doc", node=node)
-
-    def check_functiondef_yields(self, node, node_doc):
-        if not node_doc.supports_yields or node.is_abstract():
-            return
-
-        if (
-            node_doc.has_yields() or node_doc.has_yields_type()
-        ) and not node.is_generator():
-            self.add_message("redundant-yields-doc", node=node)
-
-    def visit_raise(self, node):
-        func_node = node.frame()
-        if not isinstance(func_node, astroid.FunctionDef):
-            return
-
-        expected_excs = utils.possible_exc_types(node)
-
-        if not expected_excs:
-            return
-
-        if not func_node.doc:
-            # If this is a property setter,
-            # the property should have the docstring instead.
-            property_ = utils.get_setters_property(func_node)
-            if property_:
-                func_node = property_
-
-        doc = utils.docstringify(func_node.doc, self.config.default_docstring_type)
-        if not doc.is_valid():
-            if doc.doc:
-                self._handle_no_raise_doc(expected_excs, func_node)
-            return
-
-        found_excs_full_names = doc.exceptions()
-
-        # Extract just the class name, e.g. "error" from "re.error"
-        found_excs_class_names = {exc.split(".")[-1] for exc in found_excs_full_names}
-        missing_excs = expected_excs - found_excs_class_names
-        self._add_raise_message(missing_excs, func_node)
-
-    def visit_return(self, node):
-        if not utils.returns_something(node):
-            return
-
-        func_node = node.frame()
-        if not isinstance(func_node, astroid.FunctionDef):
-            return
-
-        doc = utils.docstringify(func_node.doc, self.config.default_docstring_type)
-        if not doc.is_valid() and self.config.accept_no_return_doc:
-            return
-
-        is_property = checker_utils.decorated_with_property(func_node)
-
-        if not (doc.has_returns() or (doc.has_property_returns() and is_property)):
-            self.add_message("missing-return-doc", node=func_node)
-
-        if func_node.returns:
-            return
-
-        if not (doc.has_rtype() or (doc.has_property_type() and is_property)):
-            self.add_message("missing-return-type-doc", node=func_node)
-
-    def visit_yield(self, node):
-        func_node = node.frame()
-        if not isinstance(func_node, astroid.FunctionDef):
-            return
-
-        doc = utils.docstringify(func_node.doc, self.config.default_docstring_type)
-        if not doc.is_valid() and self.config.accept_no_yields_doc:
-            return
-
-        if doc.supports_yields:
-            doc_has_yields = doc.has_yields()
-            doc_has_yields_type = doc.has_yields_type()
-        else:
-            doc_has_yields = doc.has_returns()
-            doc_has_yields_type = doc.has_rtype()
-
-        if not doc_has_yields:
-            self.add_message("missing-yield-doc", node=func_node)
-
-        if not (doc_has_yields_type or func_node.returns):
-            self.add_message("missing-yield-type-doc", node=func_node)
-
-    def visit_yieldfrom(self, node):
-        self.visit_yield(node)
-
-    def _compare_missing_args(
-        self,
-        found_argument_names,
-        message_id,
-        not_needed_names,
-        expected_argument_names,
-        warning_node,
-    ):
-        """Compare the found argument names with the expected ones and
-        generate a message if there are arguments missing.
-
-        :param set found_argument_names: argument names found in the
-            docstring
-
-        :param str message_id: pylint message id
-
-        :param not_needed_names: names that may be omitted
-        :type not_needed_names: set of str
-
-        :param set expected_argument_names: Expected argument names
-        :param NodeNG warning_node: The node to be analyzed
-        """
-        missing_argument_names = (
-            expected_argument_names - found_argument_names
-        ) - not_needed_names
-        if missing_argument_names:
-            self.add_message(
-                message_id,
-                args=(", ".join(sorted(missing_argument_names)),),
-                node=warning_node,
-            )
-
-    def _compare_different_args(
-        self,
-        found_argument_names,
-        message_id,
-        not_needed_names,
-        expected_argument_names,
-        warning_node,
-    ):
-        """Compare the found argument names with the expected ones and
-        generate a message if there are extra arguments found.
-
-        :param set found_argument_names: argument names found in the
-            docstring
-
-        :param str message_id: pylint message id
-
-        :param not_needed_names: names that may be omitted
-        :type not_needed_names: set of str
-
-        :param set expected_argument_names: Expected argument names
-        :param NodeNG warning_node: The node to be analyzed
-        """
-        differing_argument_names = (
-            (expected_argument_names ^ found_argument_names)
-            - not_needed_names
-            - expected_argument_names
-        )
-
-        if differing_argument_names:
-            self.add_message(
-                message_id,
-                args=(", ".join(sorted(differing_argument_names)),),
-                node=warning_node,
-            )
-
-    def check_arguments_in_docstring(
-        self, doc, arguments_node, warning_node, accept_no_param_doc=None
-    ):
-        """Check that all parameters in a function, method or class constructor
-        on the one hand and the parameters mentioned in the parameter
-        documentation (e.g. the Sphinx tags 'param' and 'type') on the other
-        hand are consistent with each other.
-
-        * Undocumented parameters except 'self' are noticed.
-        * Undocumented parameter types except for 'self' and the ``*<args>``
-          and ``**<kwargs>`` parameters are noticed.
-        * Parameters mentioned in the parameter documentation that don't or no
-          longer exist in the function parameter list are noticed.
-        * If the text "For the parameters, see" or "For the other parameters,
-          see" (ignoring additional whitespace) is mentioned in the docstring,
-          missing parameter documentation is tolerated.
-        * If there's no Sphinx style, Google style or NumPy style parameter
-          documentation at all, i.e. ``:param`` is never mentioned etc., the
-          checker assumes that the parameters are documented in another format
-          and the absence is tolerated.
-
-        :param doc: Docstring for the function, method or class.
-        :type doc: :class:`Docstring`
-
-        :param arguments_node: Arguments node for the function, method or
-            class constructor.
-        :type arguments_node: :class:`astroid.scoped_nodes.Arguments`
-
-        :param warning_node: The node to assign the warnings to
-        :type warning_node: :class:`astroid.scoped_nodes.Node`
-
-        :param accept_no_param_doc: Whether or not to allow no parameters
-            to be documented.
-            If None then this value is read from the configuration.
-        :type accept_no_param_doc: bool or None
-        """
-        # Tolerate missing param or type declarations if there is a link to
-        # another method carrying the same name.
-        if not doc.doc:
-            return
-
-        if accept_no_param_doc is None:
-            accept_no_param_doc = self.config.accept_no_param_doc
-        tolerate_missing_params = doc.params_documented_elsewhere()
-
-        # Collect the function arguments.
-        expected_argument_names = {arg.name for arg in arguments_node.args}
-        expected_argument_names.update(arg.name for arg in arguments_node.kwonlyargs)
-        not_needed_type_in_docstring = self.not_needed_param_in_docstring.copy()
-
-        if arguments_node.vararg is not None:
-            expected_argument_names.add(arguments_node.vararg)
-            not_needed_type_in_docstring.add(arguments_node.vararg)
-        if arguments_node.kwarg is not None:
-            expected_argument_names.add(arguments_node.kwarg)
-            not_needed_type_in_docstring.add(arguments_node.kwarg)
-        params_with_doc, params_with_type = doc.match_param_docs()
-
-        # Tolerate no parameter documentation at all.
-        if not params_with_doc and not params_with_type and accept_no_param_doc:
-            tolerate_missing_params = True
-
-        if not tolerate_missing_params:
-            self._compare_missing_args(
-                params_with_doc,
-                "missing-param-doc",
-                self.not_needed_param_in_docstring,
-                expected_argument_names,
-                warning_node,
-            )
-
-        for index, arg_name in enumerate(arguments_node.args):
-            if arguments_node.annotations[index]:
-                params_with_type.add(arg_name.name)
-        for index, arg_name in enumerate(arguments_node.kwonlyargs):
-            if arguments_node.kwonlyargs_annotations[index]:
-                params_with_type.add(arg_name.name)
-
-        if not tolerate_missing_params:
-            self._compare_missing_args(
-                params_with_type,
-                "missing-type-doc",
-                not_needed_type_in_docstring,
-                expected_argument_names,
-                warning_node,
-            )
-
-        self._compare_different_args(
-            params_with_doc,
-            "differing-param-doc",
-            self.not_needed_param_in_docstring,
-            expected_argument_names,
-            warning_node,
-        )
-        self._compare_different_args(
-            params_with_type,
-            "differing-type-doc",
-            not_needed_type_in_docstring,
-            expected_argument_names,
-            warning_node,
-        )
-
-    def check_single_constructor_params(self, class_doc, init_doc, class_node):
-        if class_doc.has_params() and init_doc.has_params():
-            self.add_message(
-                "multiple-constructor-doc", args=(class_node.name,), node=class_node
-            )
-
-    def _handle_no_raise_doc(self, excs, node):
-        if self.config.accept_no_raise_doc:
-            return
-
-        self._add_raise_message(excs, node)
-
-    def _add_raise_message(self, missing_excs, node):
-        """
-        Adds a message on :param:`node` for the missing exception type.
-
-        :param missing_excs: A list of missing exception types.
-        :type missing_excs: set(str)
-
-        :param node: The node show the message on.
-        :type node: astroid.node_classes.NodeNG
-        """
-        if node.is_abstract():
-            try:
-                missing_excs.remove("NotImplementedError")
-            except KeyError:
-                pass
-
-        if not missing_excs:
-            return
-
-        self.add_message(
-            "missing-raises-doc", args=(", ".join(sorted(missing_excs)),), node=node
-        )
-
-
-def register(linter):
-    """Required method to auto register this checker.
-
-    :param linter: Main interface object for Pylint plugins
-    :type linter: Pylint object
-    """
-    linter.register_checker(DocstringParameterChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/docstyle.py b/venv/Lib/site-packages/pylint/extensions/docstyle.py
deleted file mode 100644
index 36f506f..0000000
--- a/venv/Lib/site-packages/pylint/extensions/docstyle.py
+++ /dev/null
@@ -1,89 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Luis Escobar <lescobar@vauxoo.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import linecache
-
-from pylint import checkers
-from pylint.checkers.utils import check_messages
-from pylint.interfaces import HIGH, IAstroidChecker
-
-
-class DocStringStyleChecker(checkers.BaseChecker):
-    """Checks format of docstrings based on PEP 0257"""
-
-    __implements__ = IAstroidChecker
-    name = "docstyle"
-
-    msgs = {
-        "C0198": (
-            'Bad docstring quotes in %s, expected """, given %s',
-            "bad-docstring-quotes",
-            "Used when a docstring does not have triple double quotes.",
-        ),
-        "C0199": (
-            "First line empty in %s docstring",
-            "docstring-first-line-empty",
-            "Used when a blank line is found at the beginning of a docstring.",
-        ),
-    }
-
-    @check_messages("docstring-first-line-empty", "bad-docstring-quotes")
-    def visit_module(self, node):
-        self._check_docstring("module", node)
-
-    def visit_classdef(self, node):
-        self._check_docstring("class", node)
-
-    def visit_functiondef(self, node):
-        ftype = "method" if node.is_method() else "function"
-        self._check_docstring(ftype, node)
-
-    visit_asyncfunctiondef = visit_functiondef
-
-    def _check_docstring(self, node_type, node):
-        docstring = node.doc
-        if docstring and docstring[0] == "\n":
-            self.add_message(
-                "docstring-first-line-empty",
-                node=node,
-                args=(node_type,),
-                confidence=HIGH,
-            )
-
-        # Use "linecache", instead of node.as_string(), because the latter
-        # looses the original form of the docstrings.
-
-        if docstring:
-            lineno = node.fromlineno + 1
-            line = linecache.getline(node.root().file, lineno).lstrip()
-            if line and line.find('"""') == 0:
-                return
-            if line and "'''" in line:
-                quotes = "'''"
-            elif line and line[0] == '"':
-                quotes = '"'
-            elif line and line[0] == "'":
-                quotes = "'"
-            else:
-                quotes = False
-            if quotes:
-                self.add_message(
-                    "bad-docstring-quotes",
-                    node=node,
-                    args=(node_type, quotes),
-                    confidence=HIGH,
-                )
-
-
-def register(linter):
-    """Required method to auto register this checker.
-
-    :param linter: Main interface object for Pylint plugins
-    :type linter: Pylint object
-    """
-    linter.register_checker(DocStringStyleChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/emptystring.py b/venv/Lib/site-packages/pylint/extensions/emptystring.py
deleted file mode 100644
index 04021d5..0000000
--- a/venv/Lib/site-packages/pylint/extensions/emptystring.py
+++ /dev/null
@@ -1,74 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016 Alexander Todorov <atodorov@otb.bg>
-# Copyright (c) 2017 Claudiu Popa <pcmanticore@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Looks for  comparisons to empty string."""
-
-import itertools
-
-import astroid
-
-from pylint import checkers, interfaces
-from pylint.checkers import utils
-
-
-def _is_constant_empty_str(node):
-    return isinstance(node, astroid.Const) and node.value == ""
-
-
-class CompareToEmptyStringChecker(checkers.BaseChecker):
-    """Checks for comparisons to empty string.
-    Most of the times you should use the fact that empty strings are false.
-    An exception to this rule is when an empty string value is allowed in the program
-    and has a different meaning than None!
-    """
-
-    __implements__ = (interfaces.IAstroidChecker,)
-
-    # configuration section name
-    name = "compare-to-empty-string"
-    msgs = {
-        "C1901": (
-            "Avoid comparisons to empty string",
-            "compare-to-empty-string",
-            "Used when Pylint detects comparison to an empty string constant.",
-        )
-    }
-
-    priority = -2
-    options = ()
-
-    @utils.check_messages("compare-to-empty-string")
-    def visit_compare(self, node):
-        _operators = ["!=", "==", "is not", "is"]
-        # note: astroid.Compare has the left most operand in node.left
-        # while the rest are a list of tuples in node.ops
-        # the format of the tuple is ('compare operator sign', node)
-        # here we squash everything into `ops` to make it easier for processing later
-        ops = [("", node.left)]
-        ops.extend(node.ops)
-        ops = list(itertools.chain(*ops))
-
-        for ops_idx in range(len(ops) - 2):
-            op_1 = ops[ops_idx]
-            op_2 = ops[ops_idx + 1]
-            op_3 = ops[ops_idx + 2]
-            error_detected = False
-
-            # x ?? ""
-            if _is_constant_empty_str(op_1) and op_2 in _operators:
-                error_detected = True
-            # '' ?? X
-            elif op_2 in _operators and _is_constant_empty_str(op_3):
-                error_detected = True
-
-            if error_detected:
-                self.add_message("compare-to-empty-string", node=node)
-
-
-def register(linter):
-    """Required method to auto register this checker."""
-    linter.register_checker(CompareToEmptyStringChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/mccabe.py b/venv/Lib/site-packages/pylint/extensions/mccabe.py
deleted file mode 100644
index cafac97..0000000
--- a/venv/Lib/site-packages/pylint/extensions/mccabe.py
+++ /dev/null
@@ -1,196 +0,0 @@
-# Copyright (c) 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Module to add McCabe checker class for pylint. """
-
-from mccabe import PathGraph as Mccabe_PathGraph
-from mccabe import PathGraphingAstVisitor as Mccabe_PathGraphingAstVisitor
-
-from pylint import checkers
-from pylint.checkers.utils import check_messages
-from pylint.interfaces import HIGH, IAstroidChecker
-
-
-class PathGraph(Mccabe_PathGraph):
-    def __init__(self, node):
-        super(PathGraph, self).__init__(name="", entity="", lineno=1)
-        self.root = node
-
-
-class PathGraphingAstVisitor(Mccabe_PathGraphingAstVisitor):
-    def __init__(self):
-        super(PathGraphingAstVisitor, self).__init__()
-        self._bottom_counter = 0
-
-    def default(self, node, *args):
-        for child in node.get_children():
-            self.dispatch(child, *args)
-
-    def dispatch(self, node, *args):
-        self.node = node
-        klass = node.__class__
-        meth = self._cache.get(klass)
-        if meth is None:
-            class_name = klass.__name__
-            meth = getattr(self.visitor, "visit" + class_name, self.default)
-            self._cache[klass] = meth
-        return meth(node, *args)
-
-    def visitFunctionDef(self, node):
-        if self.graph is not None:
-            # closure
-            pathnode = self._append_node(node)
-            self.tail = pathnode
-            self.dispatch_list(node.body)
-            bottom = "%s" % self._bottom_counter
-            self._bottom_counter += 1
-            self.graph.connect(self.tail, bottom)
-            self.graph.connect(node, bottom)
-            self.tail = bottom
-        else:
-            self.graph = PathGraph(node)
-            self.tail = node
-            self.dispatch_list(node.body)
-            self.graphs["%s%s" % (self.classname, node.name)] = self.graph
-            self.reset()
-
-    visitAsyncFunctionDef = visitFunctionDef
-
-    def visitSimpleStatement(self, node):
-        self._append_node(node)
-
-    visitAssert = (
-        visitAssign
-    ) = (
-        visitAugAssign
-    ) = (
-        visitDelete
-    ) = (
-        visitPrint
-    ) = (
-        visitRaise
-    ) = (
-        visitYield
-    ) = (
-        visitImport
-    ) = (
-        visitCall
-    ) = (
-        visitSubscript
-    ) = (
-        visitPass
-    ) = (
-        visitContinue
-    ) = (
-        visitBreak
-    ) = visitGlobal = visitReturn = visitExpr = visitAwait = visitSimpleStatement
-
-    def visitWith(self, node):
-        self._append_node(node)
-        self.dispatch_list(node.body)
-
-    visitAsyncWith = visitWith
-
-    def _append_node(self, node):
-        if not self.tail:
-            return None
-        self.graph.connect(self.tail, node)
-        self.tail = node
-        return node
-
-    def _subgraph(self, node, name, extra_blocks=()):
-        """create the subgraphs representing any `if` and `for` statements"""
-        if self.graph is None:
-            # global loop
-            self.graph = PathGraph(node)
-            self._subgraph_parse(node, node, extra_blocks)
-            self.graphs["%s%s" % (self.classname, name)] = self.graph
-            self.reset()
-        else:
-            self._append_node(node)
-            self._subgraph_parse(node, node, extra_blocks)
-
-    def _subgraph_parse(self, node, pathnode, extra_blocks):
-        """parse the body and any `else` block of `if` and `for` statements"""
-        loose_ends = []
-        self.tail = node
-        self.dispatch_list(node.body)
-        loose_ends.append(self.tail)
-        for extra in extra_blocks:
-            self.tail = node
-            self.dispatch_list(extra.body)
-            loose_ends.append(self.tail)
-        if node.orelse:
-            self.tail = node
-            self.dispatch_list(node.orelse)
-            loose_ends.append(self.tail)
-        else:
-            loose_ends.append(node)
-        if node:
-            bottom = "%s" % self._bottom_counter
-            self._bottom_counter += 1
-            for end in loose_ends:
-                self.graph.connect(end, bottom)
-            self.tail = bottom
-
-
-class McCabeMethodChecker(checkers.BaseChecker):
-    """Checks McCabe complexity cyclomatic threshold in methods and functions
-    to validate a too complex code.
-    """
-
-    __implements__ = IAstroidChecker
-    name = "design"
-
-    msgs = {
-        "R1260": (
-            "%s is too complex. The McCabe rating is %d",
-            "too-complex",
-            "Used when a method or function is too complex based on "
-            "McCabe Complexity Cyclomatic",
-        )
-    }
-    options = (
-        (
-            "max-complexity",
-            {
-                "default": 10,
-                "type": "int",
-                "metavar": "<int>",
-                "help": "McCabe complexity cyclomatic threshold",
-            },
-        ),
-    )
-
-    @check_messages("too-complex")
-    def visit_module(self, node):
-        """visit an astroid.Module node to check too complex rating and
-        add message if is greather than max_complexity stored from options"""
-        visitor = PathGraphingAstVisitor()
-        for child in node.body:
-            visitor.preorder(child, visitor)
-        for graph in visitor.graphs.values():
-            complexity = graph.complexity()
-            node = graph.root
-            if hasattr(node, "name"):
-                node_name = "'%s'" % node.name
-            else:
-                node_name = "This '%s'" % node.__class__.__name__.lower()
-            if complexity <= self.config.max_complexity:
-                continue
-            self.add_message(
-                "too-complex", node=node, confidence=HIGH, args=(node_name, complexity)
-            )
-
-
-def register(linter):
-    """Required method to auto register this checker.
-
-    :param linter: Main interface object for Pylint plugins
-    :type linter: Pylint object
-    """
-    linter.register_checker(McCabeMethodChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/overlapping_exceptions.py b/venv/Lib/site-packages/pylint/extensions/overlapping_exceptions.py
deleted file mode 100644
index be2208c..0000000
--- a/venv/Lib/site-packages/pylint/extensions/overlapping_exceptions.py
+++ /dev/null
@@ -1,88 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Looks for overlapping exceptions."""
-
-import astroid
-
-from pylint import checkers, interfaces
-from pylint.checkers import utils
-from pylint.checkers.exceptions import _annotated_unpack_infer
-
-
-class OverlappingExceptionsChecker(checkers.BaseChecker):
-    """Checks for two or more exceptions in the same exception handler
-    clause that are identical or parts of the same inheritance hierarchy
-    (i.e. overlapping)."""
-
-    __implements__ = interfaces.IAstroidChecker
-
-    name = "overlap-except"
-    msgs = {
-        "W0714": (
-            "Overlapping exceptions (%s)",
-            "overlapping-except",
-            "Used when exceptions in handler overlap or are identical",
-        )
-    }
-    priority = -2
-    options = ()
-
-    @utils.check_messages("overlapping-except")
-    def visit_tryexcept(self, node):
-        """check for empty except"""
-        for handler in node.handlers:
-            if handler.type is None:
-                continue
-            if isinstance(handler.type, astroid.BoolOp):
-                continue
-            try:
-                excs = list(_annotated_unpack_infer(handler.type))
-            except astroid.InferenceError:
-                continue
-
-            handled_in_clause = []
-            for part, exc in excs:
-                if exc is astroid.Uninferable:
-                    continue
-                if isinstance(exc, astroid.Instance) and utils.inherit_from_std_ex(exc):
-                    # pylint: disable=protected-access
-                    exc = exc._proxied
-
-                if not isinstance(exc, astroid.ClassDef):
-                    continue
-
-                exc_ancestors = [
-                    anc for anc in exc.ancestors() if isinstance(anc, astroid.ClassDef)
-                ]
-
-                for prev_part, prev_exc in handled_in_clause:
-                    prev_exc_ancestors = [
-                        anc
-                        for anc in prev_exc.ancestors()
-                        if isinstance(anc, astroid.ClassDef)
-                    ]
-                    if exc == prev_exc:
-                        self.add_message(
-                            "overlapping-except",
-                            node=handler.type,
-                            args="%s and %s are the same"
-                            % (prev_part.as_string(), part.as_string()),
-                        )
-                    elif prev_exc in exc_ancestors or exc in prev_exc_ancestors:
-                        ancestor = part if exc in prev_exc_ancestors else prev_part
-                        descendant = part if prev_exc in exc_ancestors else prev_part
-                        self.add_message(
-                            "overlapping-except",
-                            node=handler.type,
-                            args="%s is an ancestor class of %s"
-                            % (ancestor.as_string(), descendant.as_string()),
-                        )
-                handled_in_clause += [(part, exc)]
-
-
-def register(linter):
-    """Required method to auto register this checker."""
-    linter.register_checker(OverlappingExceptionsChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/extensions/redefined_variable_type.py b/venv/Lib/site-packages/pylint/extensions/redefined_variable_type.py
deleted file mode 100644
index cfe4754..0000000
--- a/venv/Lib/site-packages/pylint/extensions/redefined_variable_type.py
+++ /dev/null
@@ -1,116 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2016-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2016 Glenn Matthews <glmatthe@cisco.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import astroid
-
-from pylint.checkers import BaseChecker
-from pylint.checkers.utils import check_messages, is_none, node_type
-from pylint.interfaces import IAstroidChecker
-
-BUILTINS = "builtins"
-
-
-class MultipleTypesChecker(BaseChecker):
-    """Checks for variable type redefinitions (NoneType excepted)
-
-    At a function, method, class or module scope
-
-    This rule could be improved:
-
-    - Currently, if an attribute is set to different types in 2 methods of a
-      same class, it won't be detected (see functional test)
-    - One could improve the support for inference on assignment with tuples,
-      ifexpr, etc. Also it would be great to have support for inference on
-      str.split()
-    """
-
-    __implements__ = IAstroidChecker
-
-    name = "multiple_types"
-    msgs = {
-        "R0204": (
-            "Redefinition of %s type from %s to %s",
-            "redefined-variable-type",
-            "Used when the type of a variable changes inside a "
-            "method or a function.",
-        )
-    }
-
-    def visit_classdef(self, _):
-        self._assigns.append({})
-
-    @check_messages("redefined-variable-type")
-    def leave_classdef(self, _):
-        self._check_and_add_messages()
-
-    visit_functiondef = visit_classdef
-    leave_functiondef = leave_module = leave_classdef
-
-    def visit_module(self, _):
-        self._assigns = [{}]
-
-    def _check_and_add_messages(self):
-        assigns = self._assigns.pop()
-        for name, args in assigns.items():
-            if len(args) <= 1:
-                continue
-            orig_node, orig_type = args[0]
-            # Check if there is a type in the following nodes that would be
-            # different from orig_type.
-            for redef_node, redef_type in args[1:]:
-                if redef_type == orig_type:
-                    continue
-                # if a variable is defined to several types in an if node,
-                # this is not actually redefining.
-                orig_parent = orig_node.parent
-                redef_parent = redef_node.parent
-                if isinstance(orig_parent, astroid.If):
-                    if orig_parent == redef_parent:
-                        if (
-                            redef_node in orig_parent.orelse
-                            and orig_node not in orig_parent.orelse
-                        ):
-                            orig_node, orig_type = redef_node, redef_type
-                            continue
-                    elif isinstance(
-                        redef_parent, astroid.If
-                    ) and redef_parent in orig_parent.nodes_of_class(astroid.If):
-                        orig_node, orig_type = redef_node, redef_type
-                        continue
-                orig_type = orig_type.replace(BUILTINS + ".", "")
-                redef_type = redef_type.replace(BUILTINS + ".", "")
-                self.add_message(
-                    "redefined-variable-type",
-                    node=redef_node,
-                    args=(name, orig_type, redef_type),
-                )
-                break
-
-    def visit_assign(self, node):
-        # we don't handle multiple assignment nor slice assignment
-        target = node.targets[0]
-        if isinstance(target, (astroid.Tuple, astroid.Subscript)):
-            return
-        # ignore NoneType
-        if is_none(node):
-            return
-        _type = node_type(node.value)
-        if _type:
-            self._assigns[-1].setdefault(target.as_string(), []).append(
-                (node, _type.pytype())
-            )
-
-
-def register(linter):
-    """Required method to auto register this checker.
-
-    :param linter: Main interface object for Pylint plugins
-    :type linter: Pylint object
-    """
-    linter.register_checker(MultipleTypesChecker(linter))
diff --git a/venv/Lib/site-packages/pylint/graph.py b/venv/Lib/site-packages/pylint/graph.py
deleted file mode 100644
index 0dc7a14..0000000
--- a/venv/Lib/site-packages/pylint/graph.py
+++ /dev/null
@@ -1,197 +0,0 @@
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Graph manipulation utilities.
-
-(dot generation adapted from pypy/translator/tool/make_dot.py)
-"""
-
-import codecs
-import os
-import os.path as osp
-import subprocess
-import sys
-import tempfile
-
-
-def target_info_from_filename(filename):
-    """Transforms /some/path/foo.png into ('/some/path', 'foo.png', 'png')."""
-    basename = osp.basename(filename)
-    storedir = osp.dirname(osp.abspath(filename))
-    target = filename.split(".")[-1]
-    return storedir, basename, target
-
-
-class DotBackend:
-    """Dot File backend."""
-
-    def __init__(
-        self,
-        graphname,
-        rankdir=None,
-        size=None,
-        ratio=None,
-        charset="utf-8",
-        renderer="dot",
-        additional_param=None,
-    ):
-        if additional_param is None:
-            additional_param = {}
-        self.graphname = graphname
-        self.renderer = renderer
-        self.lines = []
-        self._source = None
-        self.emit("digraph %s {" % normalize_node_id(graphname))
-        if rankdir:
-            self.emit("rankdir=%s" % rankdir)
-        if ratio:
-            self.emit("ratio=%s" % ratio)
-        if size:
-            self.emit('size="%s"' % size)
-        if charset:
-            assert charset.lower() in ("utf-8", "iso-8859-1", "latin1"), (
-                "unsupported charset %s" % charset
-            )
-            self.emit('charset="%s"' % charset)
-        for param in additional_param.items():
-            self.emit("=".join(param))
-
-    def get_source(self):
-        """returns self._source"""
-        if self._source is None:
-            self.emit("}\n")
-            self._source = "\n".join(self.lines)
-            del self.lines
-        return self._source
-
-    source = property(get_source)
-
-    def generate(self, outputfile=None, dotfile=None, mapfile=None):
-        """Generates a graph file.
-
-        :param str outputfile: filename and path [defaults to graphname.png]
-        :param str dotfile: filename and path [defaults to graphname.dot]
-        :param str mapfile: filename and path
-
-        :rtype: str
-        :return: a path to the generated file
-        """
-        name = self.graphname
-        if not dotfile:
-            # if 'outputfile' is a dot file use it as 'dotfile'
-            if outputfile and outputfile.endswith(".dot"):
-                dotfile = outputfile
-            else:
-                dotfile = "%s.dot" % name
-        if outputfile is not None:
-            storedir, _, target = target_info_from_filename(outputfile)
-            if target != "dot":
-                pdot, dot_sourcepath = tempfile.mkstemp(".dot", name)
-                os.close(pdot)
-            else:
-                dot_sourcepath = osp.join(storedir, dotfile)
-        else:
-            target = "png"
-            pdot, dot_sourcepath = tempfile.mkstemp(".dot", name)
-            ppng, outputfile = tempfile.mkstemp(".png", name)
-            os.close(pdot)
-            os.close(ppng)
-        pdot = codecs.open(dot_sourcepath, "w", encoding="utf8")
-        pdot.write(self.source)
-        pdot.close()
-        if target != "dot":
-            use_shell = sys.platform == "win32"
-            if mapfile:
-                subprocess.call(
-                    [
-                        self.renderer,
-                        "-Tcmapx",
-                        "-o",
-                        mapfile,
-                        "-T",
-                        target,
-                        dot_sourcepath,
-                        "-o",
-                        outputfile,
-                    ],
-                    shell=use_shell,
-                )
-            else:
-                subprocess.call(
-                    [self.renderer, "-T", target, dot_sourcepath, "-o", outputfile],
-                    shell=use_shell,
-                )
-            os.unlink(dot_sourcepath)
-        return outputfile
-
-    def emit(self, line):
-        """Adds <line> to final output."""
-        self.lines.append(line)
-
-    def emit_edge(self, name1, name2, **props):
-        """emit an edge from <name1> to <name2>.
-        edge properties: see http://www.graphviz.org/doc/info/attrs.html
-        """
-        attrs = ['%s="%s"' % (prop, value) for prop, value in props.items()]
-        n_from, n_to = normalize_node_id(name1), normalize_node_id(name2)
-        self.emit("%s -> %s [%s];" % (n_from, n_to, ", ".join(sorted(attrs))))
-
-    def emit_node(self, name, **props):
-        """emit a node with given properties.
-        node properties: see http://www.graphviz.org/doc/info/attrs.html
-        """
-        attrs = ['%s="%s"' % (prop, value) for prop, value in props.items()]
-        self.emit("%s [%s];" % (normalize_node_id(name), ", ".join(sorted(attrs))))
-
-
-def normalize_node_id(nid):
-    """Returns a suitable DOT node id for `nid`."""
-    return '"%s"' % nid
-
-
-def get_cycles(graph_dict, vertices=None):
-    """given a dictionary representing an ordered graph (i.e. key are vertices
-    and values is a list of destination vertices representing edges), return a
-    list of detected cycles
-    """
-    if not graph_dict:
-        return ()
-    result = []
-    if vertices is None:
-        vertices = graph_dict.keys()
-    for vertice in vertices:
-        _get_cycles(graph_dict, [], set(), result, vertice)
-    return result
-
-
-def _get_cycles(graph_dict, path, visited, result, vertice):
-    """recursive function doing the real work for get_cycles"""
-    if vertice in path:
-        cycle = [vertice]
-        for node in path[::-1]:
-            if node == vertice:
-                break
-            cycle.insert(0, node)
-        # make a canonical representation
-        start_from = min(cycle)
-        index = cycle.index(start_from)
-        cycle = cycle[index:] + cycle[0:index]
-        # append it to result if not already in
-        if cycle not in result:
-            result.append(cycle)
-        return
-    path.append(vertice)
-    try:
-        for node in graph_dict[vertice]:
-            # don't check already visited nodes again
-            if node not in visited:
-                _get_cycles(graph_dict, path, visited, result, node)
-                visited.add(node)
-    except KeyError:
-        pass
-    path.pop()
diff --git a/venv/Lib/site-packages/pylint/interfaces.py b/venv/Lib/site-packages/pylint/interfaces.py
deleted file mode 100644
index 378585c..0000000
--- a/venv/Lib/site-packages/pylint/interfaces.py
+++ /dev/null
@@ -1,102 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2009-2010, 2012-2013 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2014 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Interfaces for Pylint objects"""
-from collections import namedtuple
-
-Confidence = namedtuple("Confidence", ["name", "description"])
-# Warning Certainties
-HIGH = Confidence("HIGH", "No false positive possible.")
-INFERENCE = Confidence("INFERENCE", "Warning based on inference result.")
-INFERENCE_FAILURE = Confidence(
-    "INFERENCE_FAILURE", "Warning based on inference with failures."
-)
-UNDEFINED = Confidence("UNDEFINED", "Warning without any associated confidence level.")
-
-CONFIDENCE_LEVELS = [HIGH, INFERENCE, INFERENCE_FAILURE, UNDEFINED]
-
-
-class Interface:
-    """Base class for interfaces."""
-
-    @classmethod
-    def is_implemented_by(cls, instance):
-        return implements(instance, cls)
-
-
-def implements(obj, interface):
-    """Return true if the give object (maybe an instance or class) implements
-    the interface.
-    """
-    kimplements = getattr(obj, "__implements__", ())
-    if not isinstance(kimplements, (list, tuple)):
-        kimplements = (kimplements,)
-    for implementedinterface in kimplements:
-        if issubclass(implementedinterface, interface):
-            return True
-    return False
-
-
-class IChecker(Interface):
-    """This is a base interface, not designed to be used elsewhere than for
-    sub interfaces definition.
-    """
-
-    def open(self):
-        """called before visiting project (i.e set of modules)"""
-
-    def close(self):
-        """called after visiting project (i.e set of modules)"""
-
-
-class IRawChecker(IChecker):
-    """interface for checker which need to parse the raw file
-    """
-
-    def process_module(self, astroid):
-        """ process a module
-
-        the module's content is accessible via astroid.stream
-        """
-
-
-class ITokenChecker(IChecker):
-    """Interface for checkers that need access to the token list."""
-
-    def process_tokens(self, tokens):
-        """Process a module.
-
-        tokens is a list of all source code tokens in the file.
-        """
-
-
-class IAstroidChecker(IChecker):
-    """ interface for checker which prefers receive events according to
-    statement type
-    """
-
-
-class IReporter(Interface):
-    """ reporter collect messages and display results encapsulated in a layout
-    """
-
-    def handle_message(self, msg):
-        """Handle the given message object."""
-
-    def display_reports(self, layout):
-        """display results encapsulated in the layout tree
-        """
-
-
-__all__ = ("IRawChecker", "IAstroidChecker", "ITokenChecker", "IReporter")
diff --git a/venv/Lib/site-packages/pylint/lint.py b/venv/Lib/site-packages/pylint/lint.py
deleted file mode 100644
index a98970b..0000000
--- a/venv/Lib/site-packages/pylint/lint.py
+++ /dev/null
@@ -1,1817 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2015 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2008 Fabrice Douchant <Fabrice.Douchant@logilab.fr>
-# Copyright (c) 2009 Vincent
-# Copyright (c) 2009 Mads Kiilerich <mads@kiilerich.com>
-# Copyright (c) 2011-2014 Google, Inc.
-# Copyright (c) 2012 David Pursehouse <david.pursehouse@sonymobile.com>
-# Copyright (c) 2012 Kevin Jing Qiu <kevin.jing.qiu@gmail.com>
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2012 JT Olds <jtolds@xnet5.com>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014-2015 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Alexandru Coman <fcoman@bitdefender.com>
-# Copyright (c) 2014 Daniel Harding <dharding@living180.net>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2014 Dan Goldsmith <djgoldsmith@googlemail.com>
-# Copyright (c) 2015-2016 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Aru Sahni <arusahni@gmail.com>
-# Copyright (c) 2015 Steven Myint <hg@stevenmyint.com>
-# Copyright (c) 2015 Simu Toni <simutoni@gmail.com>
-# Copyright (c) 2015 Mihai Balint <balint.mihai@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016-2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2016 Alan Evangelista <alanoe@linux.vnet.ibm.com>
-# Copyright (c) 2017-2018 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Daniel Miller <millerdev@gmail.com>
-# Copyright (c) 2017 Roman Ivanov <me@roivanov.com>
-# Copyright (c) 2017 Ned Batchelder <ned@nedbatchelder.com>
-# Copyright (c) 2018 Randall Leeds <randall@bleeds.info>
-# Copyright (c) 2018 Mike Frysinger <vapier@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2018 Jason Owen <jason.a.owen@gmail.com>
-# Copyright (c) 2018 Gary Tyler McLeod <mail@garytyler.com>
-# Copyright (c) 2018 Yuval Langer <yuvallanger@mail.tau.ac.il>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-# Copyright (c) 2018 kapsh <kapsh@kap.sh>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-# pylint: disable=broad-except
-
-""" pylint [options] modules_or_packages
-
-  Check that module(s) satisfy a coding standard (and more !).
-
-    pylint --help
-
-  Display this help message and exit.
-
-    pylint --help-msg <msg-id>[,<msg-id>]
-
-  Display help messages about given message identifiers and exit.
-"""
-import collections
-import contextlib
-import operator
-import os
-import sys
-import tokenize
-import traceback
-import warnings
-from io import TextIOWrapper
-
-import astroid
-from astroid import modutils
-from astroid.__pkginfo__ import version as astroid_version
-from astroid.builder import AstroidBuilder
-
-from pylint import __pkginfo__, checkers, config, exceptions, interfaces, reporters
-from pylint.__pkginfo__ import version
-from pylint.constants import MAIN_CHECKER_NAME, MSG_TYPES, OPTION_RGX
-from pylint.message import Message, MessageDefinitionStore, MessagesHandlerMixIn
-from pylint.reporters.ureports import nodes as report_nodes
-from pylint.utils import ASTWalker, FileState, utils
-
-try:
-    import multiprocessing
-except ImportError:
-    multiprocessing = None  # type: ignore
-
-
-MANAGER = astroid.MANAGER
-
-
-def _ast_from_string(data, filepath, modname):
-    cached = MANAGER.astroid_cache.get(modname)
-    if cached and cached.file == filepath:
-        return cached
-
-    return AstroidBuilder(MANAGER).string_build(data, modname, filepath)
-
-
-def _read_stdin():
-    # https://mail.python.org/pipermail/python-list/2012-November/634424.html
-    sys.stdin = TextIOWrapper(sys.stdin.detach(), encoding="utf-8")
-    return sys.stdin.read()
-
-
-def _get_new_args(message):
-    location = (
-        message.abspath,
-        message.path,
-        message.module,
-        message.obj,
-        message.line,
-        message.column,
-    )
-    return (message.msg_id, message.symbol, location, message.msg, message.confidence)
-
-
-def _get_python_path(filepath):
-    dirname = os.path.realpath(os.path.expanduser(filepath))
-    if not os.path.isdir(dirname):
-        dirname = os.path.dirname(dirname)
-    while True:
-        if not os.path.exists(os.path.join(dirname, "__init__.py")):
-            return dirname
-        old_dirname = dirname
-        dirname = os.path.dirname(dirname)
-        if old_dirname == dirname:
-            return os.getcwd()
-    return None
-
-
-def _merge_stats(stats):
-    merged = {}
-    by_msg = collections.Counter()
-    for stat in stats:
-        message_stats = stat.pop("by_msg", {})
-        by_msg.update(message_stats)
-
-        for key, item in stat.items():
-            if key not in merged:
-                merged[key] = item
-            else:
-                if isinstance(item, dict):
-                    merged[key].update(item)
-                else:
-                    merged[key] = merged[key] + item
-
-    merged["by_msg"] = by_msg
-    return merged
-
-
-# Python Linter class #########################################################
-
-MSGS = {
-    "F0001": (
-        "%s",
-        "fatal",
-        "Used when an error occurred preventing the analysis of a \
-              module (unable to find it for instance).",
-    ),
-    "F0002": (
-        "%s: %s",
-        "astroid-error",
-        "Used when an unexpected error occurred while building the "
-        "Astroid  representation. This is usually accompanied by a "
-        "traceback. Please report such errors !",
-    ),
-    "F0010": (
-        "error while code parsing: %s",
-        "parse-error",
-        "Used when an exception occurred while building the Astroid "
-        "representation which could be handled by astroid.",
-    ),
-    "I0001": (
-        "Unable to run raw checkers on built-in module %s",
-        "raw-checker-failed",
-        "Used to inform that a built-in module has not been checked "
-        "using the raw checkers.",
-    ),
-    "I0010": (
-        "Unable to consider inline option %r",
-        "bad-inline-option",
-        "Used when an inline option is either badly formatted or can't "
-        "be used inside modules.",
-    ),
-    "I0011": (
-        "Locally disabling %s (%s)",
-        "locally-disabled",
-        "Used when an inline option disables a message or a messages category.",
-    ),
-    "I0013": (
-        "Ignoring entire file",
-        "file-ignored",
-        "Used to inform that the file will not be checked",
-    ),
-    "I0020": (
-        "Suppressed %s (from line %d)",
-        "suppressed-message",
-        "A message was triggered on a line, but suppressed explicitly "
-        "by a disable= comment in the file. This message is not "
-        "generated for messages that are ignored due to configuration "
-        "settings.",
-    ),
-    "I0021": (
-        "Useless suppression of %s",
-        "useless-suppression",
-        "Reported when a message is explicitly disabled for a line or "
-        "a block of code, but never triggered.",
-    ),
-    "I0022": (
-        'Pragma "%s" is deprecated, use "%s" instead',
-        "deprecated-pragma",
-        "Some inline pylint options have been renamed or reworked, "
-        "only the most recent form should be used. "
-        "NOTE:skip-all is only available with pylint >= 0.26",
-        {"old_names": [("I0014", "deprecated-disable-all")]},
-    ),
-    "E0001": ("%s", "syntax-error", "Used when a syntax error is raised for a module."),
-    "E0011": (
-        "Unrecognized file option %r",
-        "unrecognized-inline-option",
-        "Used when an unknown inline option is encountered.",
-    ),
-    "E0012": (
-        "Bad option value %r",
-        "bad-option-value",
-        "Used when a bad value for an inline option is encountered.",
-    ),
-}
-
-
-def _cpu_count() -> int:
-    """Use sched_affinity if available for virtualized or containerized environments."""
-    sched_getaffinity = getattr(os, "sched_getaffinity", None)
-    # pylint: disable=not-callable,using-constant-test
-    if sched_getaffinity:
-        return len(sched_getaffinity(0))
-    if multiprocessing:
-        return multiprocessing.cpu_count()
-    return 1
-
-
-if multiprocessing is not None:
-
-    class ChildLinter(multiprocessing.Process):
-        def run(self):
-            # pylint: disable=no-member, unbalanced-tuple-unpacking
-            tasks_queue, results_queue, self._config = self._args
-
-            self._config["jobs"] = 1  # Child does not parallelize any further.
-            self._python3_porting_mode = self._config.pop("python3_porting_mode", None)
-            self._plugins = self._config.pop("plugins", None)
-
-            # Run linter for received files/modules.
-            for file_or_module in iter(tasks_queue.get, "STOP"):
-                try:
-                    result = self._run_linter(file_or_module[0])
-                    results_queue.put(result)
-                except Exception as ex:
-                    print(
-                        "internal error with sending report for module %s"
-                        % file_or_module,
-                        file=sys.stderr,
-                    )
-                    print(ex, file=sys.stderr)
-                    results_queue.put({})
-
-        def _run_linter(self, file_or_module):
-            linter = PyLinter()
-
-            # Register standard checkers.
-            linter.load_default_plugins()
-            # Load command line plugins.
-            if self._plugins:
-                linter.load_plugin_modules(self._plugins)
-
-            linter.load_configuration_from_config(self._config)
-
-            # Load plugin specific configuration
-            linter.load_plugin_configuration()
-
-            linter.set_reporter(reporters.CollectingReporter())
-
-            # Enable the Python 3 checker mode. This option is
-            # passed down from the parent linter up to here, since
-            # the Python 3 porting flag belongs to the Run class,
-            # instead of the Linter class.
-            if self._python3_porting_mode:
-                linter.python3_porting_mode()
-
-            # Run the checks.
-            linter.check(file_or_module)
-
-            msgs = [_get_new_args(m) for m in linter.reporter.messages]
-            return (
-                file_or_module,
-                linter.file_state.base_name,
-                linter.current_name,
-                msgs,
-                linter.stats,
-                linter.msg_status,
-            )
-
-
-# pylint: disable=too-many-instance-attributes,too-many-public-methods
-class PyLinter(
-    config.OptionsManagerMixIn,
-    MessagesHandlerMixIn,
-    reporters.ReportsHandlerMixIn,
-    checkers.BaseTokenChecker,
-):
-    """lint Python modules using external checkers.
-
-    This is the main checker controlling the other ones and the reports
-    generation. It is itself both a raw checker and an astroid checker in order
-    to:
-    * handle message activation / deactivation at the module level
-    * handle some basic but necessary stats'data (number of classes, methods...)
-
-    IDE plugin developers: you may have to call
-    `astroid.builder.MANAGER.astroid_cache.clear()` across runs if you want
-    to ensure the latest code version is actually checked.
-    """
-
-    __implements__ = (interfaces.ITokenChecker,)
-
-    name = MAIN_CHECKER_NAME
-    priority = 0
-    level = 0
-    msgs = MSGS
-
-    @staticmethod
-    def make_options():
-        return (
-            (
-                "ignore",
-                {
-                    "type": "csv",
-                    "metavar": "<file>[,<file>...]",
-                    "dest": "black_list",
-                    "default": ("CVS",),
-                    "help": "Add files or directories to the blacklist. "
-                    "They should be base names, not paths.",
-                },
-            ),
-            (
-                "ignore-patterns",
-                {
-                    "type": "regexp_csv",
-                    "metavar": "<pattern>[,<pattern>...]",
-                    "dest": "black_list_re",
-                    "default": (),
-                    "help": "Add files or directories matching the regex patterns to the"
-                    " blacklist. The regex matches against base names, not paths.",
-                },
-            ),
-            (
-                "persistent",
-                {
-                    "default": True,
-                    "type": "yn",
-                    "metavar": "<y_or_n>",
-                    "level": 1,
-                    "help": "Pickle collected data for later comparisons.",
-                },
-            ),
-            (
-                "load-plugins",
-                {
-                    "type": "csv",
-                    "metavar": "<modules>",
-                    "default": (),
-                    "level": 1,
-                    "help": "List of plugins (as comma separated values of "
-                    "python module names) to load, usually to register "
-                    "additional checkers.",
-                },
-            ),
-            (
-                "output-format",
-                {
-                    "default": "text",
-                    "type": "string",
-                    "metavar": "<format>",
-                    "short": "f",
-                    "group": "Reports",
-                    "help": "Set the output format. Available formats are text,"
-                    " parseable, colorized, json and msvs (visual studio)."
-                    " You can also give a reporter class, e.g. mypackage.mymodule."
-                    "MyReporterClass.",
-                },
-            ),
-            (
-                "reports",
-                {
-                    "default": False,
-                    "type": "yn",
-                    "metavar": "<y_or_n>",
-                    "short": "r",
-                    "group": "Reports",
-                    "help": "Tells whether to display a full report or only the "
-                    "messages.",
-                },
-            ),
-            (
-                "evaluation",
-                {
-                    "type": "string",
-                    "metavar": "<python_expression>",
-                    "group": "Reports",
-                    "level": 1,
-                    "default": "10.0 - ((float(5 * error + warning + refactor + "
-                    "convention) / statement) * 10)",
-                    "help": "Python expression which should return a score less "
-                    "than or equal to 10. You have access to the variables "
-                    "'error', 'warning', 'refactor', and 'convention' which "
-                    "contain the number of messages in each category, as well as "
-                    "'statement' which is the total number of statements "
-                    "analyzed. This score is used by the global "
-                    "evaluation report (RP0004).",
-                },
-            ),
-            (
-                "score",
-                {
-                    "default": True,
-                    "type": "yn",
-                    "metavar": "<y_or_n>",
-                    "short": "s",
-                    "group": "Reports",
-                    "help": "Activate the evaluation score.",
-                },
-            ),
-            (
-                "confidence",
-                {
-                    "type": "multiple_choice",
-                    "metavar": "<levels>",
-                    "default": "",
-                    "choices": [c.name for c in interfaces.CONFIDENCE_LEVELS],
-                    "group": "Messages control",
-                    "help": "Only show warnings with the listed confidence levels."
-                    " Leave empty to show all. Valid levels: %s."
-                    % (", ".join(c.name for c in interfaces.CONFIDENCE_LEVELS),),
-                },
-            ),
-            (
-                "enable",
-                {
-                    "type": "csv",
-                    "metavar": "<msg ids>",
-                    "short": "e",
-                    "group": "Messages control",
-                    "help": "Enable the message, report, category or checker with the "
-                    "given id(s). You can either give multiple identifier "
-                    "separated by comma (,) or put this option multiple time "
-                    "(only on the command line, not in the configuration file "
-                    "where it should appear only once). "
-                    'See also the "--disable" option for examples.',
-                },
-            ),
-            (
-                "disable",
-                {
-                    "type": "csv",
-                    "metavar": "<msg ids>",
-                    "short": "d",
-                    "group": "Messages control",
-                    "help": "Disable the message, report, category or checker "
-                    "with the given id(s). You can either give multiple identifiers "
-                    "separated by comma (,) or put this option multiple times "
-                    "(only on the command line, not in the configuration file "
-                    "where it should appear only once). "
-                    'You can also use "--disable=all" to disable everything first '
-                    "and then reenable specific checks. For example, if you want "
-                    "to run only the similarities checker, you can use "
-                    '"--disable=all --enable=similarities". '
-                    "If you want to run only the classes checker, but have no "
-                    "Warning level messages displayed, use "
-                    '"--disable=all --enable=classes --disable=W".',
-                },
-            ),
-            (
-                "msg-template",
-                {
-                    "type": "string",
-                    "metavar": "<template>",
-                    "group": "Reports",
-                    "help": (
-                        "Template used to display messages. "
-                        "This is a python new-style format string "
-                        "used to format the message information. "
-                        "See doc for all details."
-                    ),
-                },
-            ),
-            (
-                "jobs",
-                {
-                    "type": "int",
-                    "metavar": "<n-processes>",
-                    "short": "j",
-                    "default": 1,
-                    "help": "Use multiple processes to speed up Pylint. Specifying 0 will "
-                    "auto-detect the number of processors available to use.",
-                },
-            ),
-            (
-                "unsafe-load-any-extension",
-                {
-                    "type": "yn",
-                    "metavar": "<yn>",
-                    "default": False,
-                    "hide": True,
-                    "help": (
-                        "Allow loading of arbitrary C extensions. Extensions"
-                        " are imported into the active Python interpreter and"
-                        " may run arbitrary code."
-                    ),
-                },
-            ),
-            (
-                "limit-inference-results",
-                {
-                    "type": "int",
-                    "metavar": "<number-of-results>",
-                    "default": 100,
-                    "help": (
-                        "Control the amount of potential inferred values when inferring "
-                        "a single object. This can help the performance when dealing with "
-                        "large functions or complex, nested conditions. "
-                    ),
-                },
-            ),
-            (
-                "extension-pkg-whitelist",
-                {
-                    "type": "csv",
-                    "metavar": "<pkg[,pkg]>",
-                    "default": [],
-                    "help": (
-                        "A comma-separated list of package or module names"
-                        " from where C extensions may be loaded. Extensions are"
-                        " loading into the active Python interpreter and may run"
-                        " arbitrary code."
-                    ),
-                },
-            ),
-            (
-                "suggestion-mode",
-                {
-                    "type": "yn",
-                    "metavar": "<yn>",
-                    "default": True,
-                    "help": (
-                        "When enabled, pylint would attempt to guess common "
-                        "misconfiguration and emit user-friendly hints instead "
-                        "of false-positive error messages."
-                    ),
-                },
-            ),
-            (
-                "exit-zero",
-                {
-                    "action": "store_true",
-                    "help": (
-                        "Always return a 0 (non-error) status code, even if "
-                        "lint errors are found. This is primarily useful in "
-                        "continuous integration scripts."
-                    ),
-                },
-            ),
-            (
-                "from-stdin",
-                {
-                    "action": "store_true",
-                    "help": (
-                        "Interpret the stdin as a python script, whose filename "
-                        "needs to be passed as the module_or_package argument."
-                    ),
-                },
-            ),
-        )
-
-    option_groups = (
-        ("Messages control", "Options controlling analysis messages"),
-        ("Reports", "Options related to output formatting and reporting"),
-    )
-
-    def __init__(self, options=(), reporter=None, option_groups=(), pylintrc=None):
-        # some stuff has to be done before ancestors initialization...
-        #
-        # messages store / checkers / reporter / astroid manager
-        self.msgs_store = MessageDefinitionStore()
-        self.reporter = None
-        self._reporter_name = None
-        self._reporters = {}
-        self._checkers = collections.defaultdict(list)
-        self._pragma_lineno = {}
-        self._ignore_file = False
-        # visit variables
-        self.file_state = FileState()
-        self.current_name = None
-        self.current_file = None
-        self.stats = None
-        # init options
-        self._external_opts = options
-        self.options = options + PyLinter.make_options()
-        self.option_groups = option_groups + PyLinter.option_groups
-        self._options_methods = {"enable": self.enable, "disable": self.disable}
-        self._bw_options_methods = {
-            "disable-msg": self.disable,
-            "enable-msg": self.enable,
-        }
-        full_version = "pylint %s\nastroid %s\nPython %s" % (
-            version,
-            astroid_version,
-            sys.version,
-        )
-        MessagesHandlerMixIn.__init__(self)
-        reporters.ReportsHandlerMixIn.__init__(self)
-        super(PyLinter, self).__init__(
-            usage=__doc__, version=full_version, config_file=pylintrc or config.PYLINTRC
-        )
-        checkers.BaseTokenChecker.__init__(self)
-        # provided reports
-        self.reports = (
-            ("RP0001", "Messages by category", report_total_messages_stats),
-            (
-                "RP0002",
-                "% errors / warnings by module",
-                report_messages_by_module_stats,
-            ),
-            ("RP0003", "Messages", report_messages_stats),
-        )
-        self.register_checker(self)
-        self._dynamic_plugins = set()
-        self._python3_porting_mode = False
-        self._error_mode = False
-        self.load_provider_defaults()
-        if reporter:
-            self.set_reporter(reporter)
-
-    def load_default_plugins(self):
-        checkers.initialize(self)
-        reporters.initialize(self)
-        # Make sure to load the default reporter, because
-        # the option has been set before the plugins had been loaded.
-        if not self.reporter:
-            self._load_reporter()
-
-    def load_plugin_modules(self, modnames):
-        """take a list of module names which are pylint plugins and load
-        and register them
-        """
-        for modname in modnames:
-            if modname in self._dynamic_plugins:
-                continue
-            self._dynamic_plugins.add(modname)
-            module = modutils.load_module_from_name(modname)
-            module.register(self)
-
-    def load_plugin_configuration(self):
-        """Call the configuration hook for plugins
-
-        This walks through the list of plugins, grabs the "load_configuration"
-        hook, if exposed, and calls it to allow plugins to configure specific
-        settings.
-        """
-        for modname in self._dynamic_plugins:
-            module = modutils.load_module_from_name(modname)
-            if hasattr(module, "load_configuration"):
-                module.load_configuration(self)
-
-    def _load_reporter(self):
-        name = self._reporter_name.lower()
-        if name in self._reporters:
-            self.set_reporter(self._reporters[name]())
-        else:
-            try:
-                reporter_class = self._load_reporter_class()
-            except (ImportError, AttributeError):
-                raise exceptions.InvalidReporterError(name)
-            else:
-                self.set_reporter(reporter_class())
-
-    def _load_reporter_class(self):
-        qname = self._reporter_name
-        module = modutils.load_module_from_name(modutils.get_module_part(qname))
-        class_name = qname.split(".")[-1]
-        reporter_class = getattr(module, class_name)
-        return reporter_class
-
-    def set_reporter(self, reporter):
-        """set the reporter used to display messages and reports"""
-        self.reporter = reporter
-        reporter.linter = self
-
-    def set_option(self, optname, value, action=None, optdict=None):
-        """overridden from config.OptionsProviderMixin to handle some
-        special options
-        """
-        if optname in self._options_methods or optname in self._bw_options_methods:
-            if value:
-                try:
-                    meth = self._options_methods[optname]
-                except KeyError:
-                    meth = self._bw_options_methods[optname]
-                    warnings.warn(
-                        "%s is deprecated, replace it by %s"
-                        % (optname, optname.split("-")[0]),
-                        DeprecationWarning,
-                    )
-                value = utils._check_csv(value)
-                if isinstance(value, (list, tuple)):
-                    for _id in value:
-                        meth(_id, ignore_unknown=True)
-                else:
-                    meth(value)
-                return  # no need to call set_option, disable/enable methods do it
-        elif optname == "output-format":
-            self._reporter_name = value
-            # If the reporters are already available, load
-            # the reporter class.
-            if self._reporters:
-                self._load_reporter()
-
-        try:
-            checkers.BaseTokenChecker.set_option(self, optname, value, action, optdict)
-        except config.UnsupportedAction:
-            print("option %s can't be read from config file" % optname, file=sys.stderr)
-
-    def register_reporter(self, reporter_class):
-        self._reporters[reporter_class.name] = reporter_class
-
-    def report_order(self):
-        reports = sorted(self._reports, key=lambda x: getattr(x, "name", ""))
-        try:
-            # Remove the current reporter and add it
-            # at the end of the list.
-            reports.pop(reports.index(self))
-        except ValueError:
-            pass
-        else:
-            reports.append(self)
-        return reports
-
-    # checkers manipulation methods ############################################
-
-    def register_checker(self, checker):
-        """register a new checker
-
-        checker is an object implementing IRawChecker or / and IAstroidChecker
-        """
-        assert checker.priority <= 0, "checker priority can't be >= 0"
-        self._checkers[checker.name].append(checker)
-        for r_id, r_title, r_cb in checker.reports:
-            self.register_report(r_id, r_title, r_cb, checker)
-        self.register_options_provider(checker)
-        if hasattr(checker, "msgs"):
-            self.msgs_store.register_messages_from_checker(checker)
-        checker.load_defaults()
-
-        # Register the checker, but disable all of its messages.
-        if not getattr(checker, "enabled", True):
-            self.disable(checker.name)
-
-    def disable_noerror_messages(self):
-        for msgcat, msgids in self.msgs_store._msgs_by_category.items():
-            # enable only messages with 'error' severity and above ('fatal')
-            if msgcat in ["E", "F"]:
-                for msgid in msgids:
-                    self.enable(msgid)
-            else:
-                for msgid in msgids:
-                    self.disable(msgid)
-
-    def disable_reporters(self):
-        """disable all reporters"""
-        for _reporters in self._reports.values():
-            for report_id, _, _ in _reporters:
-                self.disable_report(report_id)
-
-    def error_mode(self):
-        """error mode: enable only errors; no reports, no persistent"""
-        self._error_mode = True
-        self.disable_noerror_messages()
-        self.disable("miscellaneous")
-        if self._python3_porting_mode:
-            self.disable("all")
-            for msg_id in self._checker_messages("python3"):
-                if msg_id.startswith("E"):
-                    self.enable(msg_id)
-            config_parser = self.cfgfile_parser
-            if config_parser.has_option("MESSAGES CONTROL", "disable"):
-                value = config_parser.get("MESSAGES CONTROL", "disable")
-                self.global_set_option("disable", value)
-        else:
-            self.disable("python3")
-        self.set_option("reports", False)
-        self.set_option("persistent", False)
-        self.set_option("score", False)
-
-    def python3_porting_mode(self):
-        """Disable all other checkers and enable Python 3 warnings."""
-        self.disable("all")
-        self.enable("python3")
-        if self._error_mode:
-            # The error mode was activated, using the -E flag.
-            # So we'll need to enable only the errors from the
-            # Python 3 porting checker.
-            for msg_id in self._checker_messages("python3"):
-                if msg_id.startswith("E"):
-                    self.enable(msg_id)
-                else:
-                    self.disable(msg_id)
-        config_parser = self.cfgfile_parser
-        if config_parser.has_option("MESSAGES CONTROL", "disable"):
-            value = config_parser.get("MESSAGES CONTROL", "disable")
-            self.global_set_option("disable", value)
-        self._python3_porting_mode = True
-
-    def list_messages_enabled(self):
-        enabled = [
-            "  %s (%s)" % (message.symbol, message.msgid)
-            for message in self.msgs_store.messages
-            if self.is_message_enabled(message.msgid)
-        ]
-        disabled = [
-            "  %s (%s)" % (message.symbol, message.msgid)
-            for message in self.msgs_store.messages
-            if not self.is_message_enabled(message.msgid)
-        ]
-        print("Enabled messages:")
-        for msg in sorted(enabled):
-            print(msg)
-        print("\nDisabled messages:")
-        for msg in sorted(disabled):
-            print(msg)
-        print("")
-
-    # block level option handling #############################################
-    #
-    # see func_block_disable_msg.py test case for expected behaviour
-
-    def process_tokens(self, tokens):
-        """process tokens from the current module to search for module/block
-        level options
-        """
-        control_pragmas = {"disable", "enable"}
-        prev_line = None
-        saw_newline = True
-        seen_newline = True
-        for (tok_type, content, start, _, _) in tokens:
-            if prev_line and prev_line != start[0]:
-                saw_newline = seen_newline
-                seen_newline = False
-
-            prev_line = start[0]
-            if tok_type in (tokenize.NL, tokenize.NEWLINE):
-                seen_newline = True
-
-            if tok_type != tokenize.COMMENT:
-                continue
-            match = OPTION_RGX.search(content)
-            if match is None:
-                continue
-
-            first_group = match.group(1)
-            if (
-                first_group.strip() == "disable-all"
-                or first_group.strip() == "skip-file"
-            ):
-                if first_group.strip() == "disable-all":
-                    self.add_message(
-                        "deprecated-pragma",
-                        line=start[0],
-                        args=("disable-all", "skip-file"),
-                    )
-                self.add_message("file-ignored", line=start[0])
-                self._ignore_file = True
-                return
-            try:
-                opt, value = first_group.split("=", 1)
-            except ValueError:
-                self.add_message(
-                    "bad-inline-option", args=first_group.strip(), line=start[0]
-                )
-                continue
-            opt = opt.strip()
-            if opt in self._options_methods or opt in self._bw_options_methods:
-                try:
-                    meth = self._options_methods[opt]
-                except KeyError:
-                    meth = self._bw_options_methods[opt]
-                    # found a "(dis|en)able-msg" pragma deprecated suppression
-                    self.add_message(
-                        "deprecated-pragma",
-                        line=start[0],
-                        args=(opt, opt.replace("-msg", "")),
-                    )
-                for msgid in utils._splitstrip(value):
-                    # Add the line where a control pragma was encountered.
-                    if opt in control_pragmas:
-                        self._pragma_lineno[msgid] = start[0]
-
-                    try:
-                        if (opt, msgid) == ("disable", "all"):
-                            self.add_message(
-                                "deprecated-pragma",
-                                line=start[0],
-                                args=("disable=all", "skip-file"),
-                            )
-                            self.add_message("file-ignored", line=start[0])
-                            self._ignore_file = True
-                            return
-                        # If we did not see a newline between the previous line and now,
-                        # we saw a backslash so treat the two lines as one.
-                        if not saw_newline:
-                            meth(msgid, "module", start[0] - 1)
-                        meth(msgid, "module", start[0])
-                    except exceptions.UnknownMessageError:
-                        self.add_message("bad-option-value", args=msgid, line=start[0])
-            else:
-                self.add_message("unrecognized-inline-option", args=opt, line=start[0])
-
-    # code checking methods ###################################################
-
-    def get_checkers(self):
-        """return all available checkers as a list"""
-        return [self] + [
-            c
-            for _checkers in self._checkers.values()
-            for c in _checkers
-            if c is not self
-        ]
-
-    def get_checker_names(self):
-        """Get all the checker names that this linter knows about."""
-        current_checkers = self.get_checkers()
-        return sorted(
-            {
-                checker.name
-                for checker in current_checkers
-                if checker.name != MAIN_CHECKER_NAME
-            }
-        )
-
-    def prepare_checkers(self):
-        """return checkers needed for activated messages and reports"""
-        if not self.config.reports:
-            self.disable_reporters()
-        # get needed checkers
-        needed_checkers = [self]
-        for checker in self.get_checkers()[1:]:
-            messages = {msg for msg in checker.msgs if self.is_message_enabled(msg)}
-            if messages or any(self.report_is_enabled(r[0]) for r in checker.reports):
-                needed_checkers.append(checker)
-        # Sort checkers by priority
-        needed_checkers = sorted(
-            needed_checkers, key=operator.attrgetter("priority"), reverse=True
-        )
-        return needed_checkers
-
-    # pylint: disable=unused-argument
-    @staticmethod
-    def should_analyze_file(modname, path, is_argument=False):
-        """Returns whether or not a module should be checked.
-
-        This implementation returns True for all python source file, indicating
-        that all files should be linted.
-
-        Subclasses may override this method to indicate that modules satisfying
-        certain conditions should not be linted.
-
-        :param str modname: The name of the module to be checked.
-        :param str path: The full path to the source code of the module.
-        :param bool is_argument: Whetter the file is an argument to pylint or not.
-                                 Files which respect this property are always
-                                 checked, since the user requested it explicitly.
-        :returns: True if the module should be checked.
-        :rtype: bool
-        """
-        if is_argument:
-            return True
-        return path.endswith(".py")
-
-    # pylint: enable=unused-argument
-
-    def check(self, files_or_modules):
-        """main checking entry: check a list of files or modules from their
-        name.
-        """
-        # initialize msgs_state now that all messages have been registered into
-        # the store
-        for msg in self.msgs_store.messages:
-            if not msg.may_be_emitted():
-                self._msgs_state[msg.msgid] = False
-
-        if not isinstance(files_or_modules, (list, tuple)):
-            files_or_modules = (files_or_modules,)
-
-        if self.config.jobs == 1:
-            self._do_check(files_or_modules)
-        else:
-            self._parallel_check(files_or_modules)
-
-    def _get_jobs_config(self):
-        child_config = collections.OrderedDict()
-        filter_options = {"long-help"}
-        filter_options.update((opt_name for opt_name, _ in self._external_opts))
-        for opt_providers in self._all_options.values():
-            for optname, optdict, val in opt_providers.options_and_values():
-                if optdict.get("deprecated"):
-                    continue
-
-                if optname not in filter_options:
-                    child_config[optname] = utils._format_option_value(optdict, val)
-        child_config["python3_porting_mode"] = self._python3_porting_mode
-        child_config["plugins"] = self._dynamic_plugins
-        return child_config
-
-    def _parallel_task(self, files_or_modules):
-        # Prepare configuration for child linters.
-        child_config = self._get_jobs_config()
-
-        children = []
-        manager = multiprocessing.Manager()
-        tasks_queue = manager.Queue()
-        results_queue = manager.Queue()
-
-        # Send files to child linters.
-        expanded_files = []
-        for descr in self.expand_files(files_or_modules):
-            modname, filepath, is_arg = descr["name"], descr["path"], descr["isarg"]
-            if self.should_analyze_file(modname, filepath, is_argument=is_arg):
-                expanded_files.append(descr)
-
-        # do not start more jobs than needed
-        for _ in range(min(self.config.jobs, len(expanded_files))):
-            child_linter = ChildLinter(args=(tasks_queue, results_queue, child_config))
-            child_linter.start()
-            children.append(child_linter)
-
-        for files_or_module in expanded_files:
-            path = files_or_module["path"]
-            tasks_queue.put([path])
-
-        # collect results from child linters
-        failed = False
-        for _ in expanded_files:
-            try:
-                result = results_queue.get()
-            except Exception as ex:
-                print(
-                    "internal error while receiving results from child linter",
-                    file=sys.stderr,
-                )
-                print(ex, file=sys.stderr)
-                failed = True
-                break
-            yield result
-
-        # Stop child linters and wait for their completion.
-        for _ in range(self.config.jobs):
-            tasks_queue.put("STOP")
-        for child in children:
-            child.join()
-
-        if failed:
-            print("Error occurred, stopping the linter.", file=sys.stderr)
-            sys.exit(32)
-
-    def _parallel_check(self, files_or_modules):
-        # Reset stats.
-        self.open()
-
-        all_stats = []
-        module = None
-        for result in self._parallel_task(files_or_modules):
-            if not result:
-                continue
-            (_, self.file_state.base_name, module, messages, stats, msg_status) = result
-
-            for msg in messages:
-                msg = Message(*msg)
-                self.set_current_module(module)
-                self.reporter.handle_message(msg)
-
-            all_stats.append(stats)
-            self.msg_status |= msg_status
-
-        self.stats = _merge_stats(all_stats)
-        self.current_name = module
-
-        # Insert stats data to local checkers.
-        for checker in self.get_checkers():
-            if checker is not self:
-                checker.stats = self.stats
-
-    def _do_check(self, files_or_modules):
-        walker = ASTWalker(self)
-        _checkers = self.prepare_checkers()
-        tokencheckers = [
-            c
-            for c in _checkers
-            if interfaces.implements(c, interfaces.ITokenChecker) and c is not self
-        ]
-        rawcheckers = [
-            c for c in _checkers if interfaces.implements(c, interfaces.IRawChecker)
-        ]
-        # notify global begin
-        for checker in _checkers:
-            checker.open()
-            if interfaces.implements(checker, interfaces.IAstroidChecker):
-                walker.add_checker(checker)
-        # build ast and check modules or packages
-        if self.config.from_stdin:
-            if len(files_or_modules) != 1:
-                raise exceptions.InvalidArgsError(
-                    "Missing filename required for --from-stdin"
-                )
-
-            filepath = files_or_modules[0]
-            try:
-                # Note that this function does not really perform an
-                # __import__ but may raise an ImportError exception, which
-                # we want to catch here.
-                modname = ".".join(modutils.modpath_from_file(filepath))
-            except ImportError:
-                modname = os.path.splitext(os.path.basename(filepath))[0]
-
-            self.set_current_module(modname, filepath)
-
-            # get the module representation
-            ast_node = _ast_from_string(_read_stdin(), filepath, modname)
-
-            if ast_node is not None:
-                self.file_state = FileState(filepath)
-                self.check_astroid_module(ast_node, walker, rawcheckers, tokencheckers)
-                # warn about spurious inline messages handling
-                spurious_messages = self.file_state.iter_spurious_suppression_messages(
-                    self.msgs_store
-                )
-                for msgid, line, args in spurious_messages:
-                    self.add_message(msgid, line, None, args)
-        else:
-            for descr in self.expand_files(files_or_modules):
-                modname, filepath, is_arg = descr["name"], descr["path"], descr["isarg"]
-                if not self.should_analyze_file(modname, filepath, is_argument=is_arg):
-                    continue
-
-                self.set_current_module(modname, filepath)
-                # get the module representation
-                ast_node = self.get_ast(filepath, modname)
-                if ast_node is None:
-                    continue
-
-                self.file_state = FileState(descr["basename"])
-                self._ignore_file = False
-                # fix the current file (if the source file was not available or
-                # if it's actually a c extension)
-                self.current_file = ast_node.file  # pylint: disable=maybe-no-member
-                before_check_statements = walker.nbstatements
-                self.check_astroid_module(ast_node, walker, rawcheckers, tokencheckers)
-                self.stats["by_module"][modname]["statement"] = (
-                    walker.nbstatements - before_check_statements
-                )
-                # warn about spurious inline messages handling
-                spurious_messages = self.file_state.iter_spurious_suppression_messages(
-                    self.msgs_store
-                )
-                for msgid, line, args in spurious_messages:
-                    self.add_message(msgid, line, None, args)
-        # notify global end
-        self.stats["statement"] = walker.nbstatements
-        for checker in reversed(_checkers):
-            checker.close()
-
-    def expand_files(self, modules):
-        """get modules and errors from a list of modules and handle errors
-        """
-        result, errors = utils.expand_modules(
-            modules, self.config.black_list, self.config.black_list_re
-        )
-        for error in errors:
-            message = modname = error["mod"]
-            key = error["key"]
-            self.set_current_module(modname)
-            if key == "fatal":
-                message = str(error["ex"]).replace(os.getcwd() + os.sep, "")
-            self.add_message(key, args=message)
-        return result
-
-    def set_current_module(self, modname, filepath=None):
-        """set the name of the currently analyzed module and
-        init statistics for it
-        """
-        if not modname and filepath is None:
-            return
-        self.reporter.on_set_current_module(modname, filepath)
-        self.current_name = modname
-        self.current_file = filepath or modname
-        self.stats["by_module"][modname] = {}
-        self.stats["by_module"][modname]["statement"] = 0
-        for msg_cat in MSG_TYPES.values():
-            self.stats["by_module"][modname][msg_cat] = 0
-
-    def get_ast(self, filepath, modname):
-        """return an ast(roid) representation for a module"""
-        try:
-            return MANAGER.ast_from_file(filepath, modname, source=True)
-        except astroid.AstroidSyntaxError as ex:
-            # pylint: disable=no-member
-            self.add_message(
-                "syntax-error",
-                line=getattr(ex.error, "lineno", 0),
-                col_offset=getattr(ex.error, "offset", None),
-                args=str(ex.error),
-            )
-        except astroid.AstroidBuildingException as ex:
-            self.add_message("parse-error", args=ex)
-        except Exception as ex:
-            traceback.print_exc()
-            self.add_message("astroid-error", args=(ex.__class__, ex))
-
-    def check_astroid_module(self, ast_node, walker, rawcheckers, tokencheckers):
-        """Check a module from its astroid representation."""
-        try:
-            tokens = utils.tokenize_module(ast_node)
-        except tokenize.TokenError as ex:
-            self.add_message("syntax-error", line=ex.args[1][0], args=ex.args[0])
-            return None
-
-        if not ast_node.pure_python:
-            self.add_message("raw-checker-failed", args=ast_node.name)
-        else:
-            # assert astroid.file.endswith('.py')
-            # invoke ITokenChecker interface on self to fetch module/block
-            # level options
-            self.process_tokens(tokens)
-            if self._ignore_file:
-                return False
-            # walk ast to collect line numbers
-            self.file_state.collect_block_lines(self.msgs_store, ast_node)
-            # run raw and tokens checkers
-            for checker in rawcheckers:
-                checker.process_module(ast_node)
-            for checker in tokencheckers:
-                checker.process_tokens(tokens)
-        # generate events to astroid checkers
-        walker.walk(ast_node)
-        return True
-
-    # IAstroidChecker interface #################################################
-
-    def open(self):
-        """initialize counters"""
-        self.stats = {"by_module": {}, "by_msg": {}}
-        MANAGER.always_load_extensions = self.config.unsafe_load_any_extension
-        MANAGER.max_inferable_values = self.config.limit_inference_results
-        MANAGER.extension_package_whitelist.update(self.config.extension_pkg_whitelist)
-        for msg_cat in MSG_TYPES.values():
-            self.stats[msg_cat] = 0
-
-    def generate_reports(self):
-        """close the whole package /module, it's time to make reports !
-
-        if persistent run, pickle results for later comparison
-        """
-        # Display whatever messages are left on the reporter.
-        self.reporter.display_messages(report_nodes.Section())
-
-        if self.file_state.base_name is not None:
-            # load previous results if any
-            previous_stats = config.load_results(self.file_state.base_name)
-            self.reporter.on_close(self.stats, previous_stats)
-            if self.config.reports:
-                sect = self.make_reports(self.stats, previous_stats)
-            else:
-                sect = report_nodes.Section()
-
-            if self.config.reports:
-                self.reporter.display_reports(sect)
-            self._report_evaluation()
-            # save results if persistent run
-            if self.config.persistent:
-                config.save_results(self.stats, self.file_state.base_name)
-        else:
-            self.reporter.on_close(self.stats, {})
-
-    def _report_evaluation(self):
-        """make the global evaluation report"""
-        # check with at least check 1 statements (usually 0 when there is a
-        # syntax error preventing pylint from further processing)
-        previous_stats = config.load_results(self.file_state.base_name)
-        if self.stats["statement"] == 0:
-            return
-
-        # get a global note for the code
-        evaluation = self.config.evaluation
-        try:
-            note = eval(evaluation, {}, self.stats)  # pylint: disable=eval-used
-        except Exception as ex:
-            msg = "An exception occurred while rating: %s" % ex
-        else:
-            self.stats["global_note"] = note
-            msg = "Your code has been rated at %.2f/10" % note
-            pnote = previous_stats.get("global_note")
-            if pnote is not None:
-                msg += " (previous run: %.2f/10, %+.2f)" % (pnote, note - pnote)
-
-        if self.config.score:
-            sect = report_nodes.EvaluationSection(msg)
-            self.reporter.display_reports(sect)
-
-
-# some reporting functions ####################################################
-
-
-def report_total_messages_stats(sect, stats, previous_stats):
-    """make total errors / warnings report"""
-    lines = ["type", "number", "previous", "difference"]
-    lines += checkers.table_lines_from_stats(
-        stats, previous_stats, ("convention", "refactor", "warning", "error")
-    )
-    sect.append(report_nodes.Table(children=lines, cols=4, rheaders=1))
-
-
-def report_messages_stats(sect, stats, _):
-    """make messages type report"""
-    if not stats["by_msg"]:
-        # don't print this report when we didn't detected any errors
-        raise exceptions.EmptyReportError()
-    in_order = sorted(
-        [
-            (value, msg_id)
-            for msg_id, value in stats["by_msg"].items()
-            if not msg_id.startswith("I")
-        ]
-    )
-    in_order.reverse()
-    lines = ("message id", "occurrences")
-    for value, msg_id in in_order:
-        lines += (msg_id, str(value))
-    sect.append(report_nodes.Table(children=lines, cols=2, rheaders=1))
-
-
-def report_messages_by_module_stats(sect, stats, _):
-    """make errors / warnings by modules report"""
-    if len(stats["by_module"]) == 1:
-        # don't print this report when we are analysing a single module
-        raise exceptions.EmptyReportError()
-    by_mod = collections.defaultdict(dict)
-    for m_type in ("fatal", "error", "warning", "refactor", "convention"):
-        total = stats[m_type]
-        for module in stats["by_module"].keys():
-            mod_total = stats["by_module"][module][m_type]
-            if total == 0:
-                percent = 0
-            else:
-                percent = float((mod_total) * 100) / total
-            by_mod[module][m_type] = percent
-    sorted_result = []
-    for module, mod_info in by_mod.items():
-        sorted_result.append(
-            (
-                mod_info["error"],
-                mod_info["warning"],
-                mod_info["refactor"],
-                mod_info["convention"],
-                module,
-            )
-        )
-    sorted_result.sort()
-    sorted_result.reverse()
-    lines = ["module", "error", "warning", "refactor", "convention"]
-    for line in sorted_result:
-        # Don't report clean modules.
-        if all(entry == 0 for entry in line[:-1]):
-            continue
-        lines.append(line[-1])
-        for val in line[:-1]:
-            lines.append("%.2f" % val)
-    if len(lines) == 5:
-        raise exceptions.EmptyReportError()
-    sect.append(report_nodes.Table(children=lines, cols=5, rheaders=1))
-
-
-# utilities ###################################################################
-
-
-class ArgumentPreprocessingError(Exception):
-    """Raised if an error occurs during argument preprocessing."""
-
-
-def preprocess_options(args, search_for):
-    """look for some options (keys of <search_for>) which have to be processed
-    before others
-
-    values of <search_for> are callback functions to call when the option is
-    found
-    """
-    i = 0
-    while i < len(args):
-        arg = args[i]
-        if arg.startswith("--"):
-            try:
-                option, val = arg[2:].split("=", 1)
-            except ValueError:
-                option, val = arg[2:], None
-            try:
-                cb, takearg = search_for[option]
-            except KeyError:
-                i += 1
-            else:
-                del args[i]
-                if takearg and val is None:
-                    if i >= len(args) or args[i].startswith("-"):
-                        msg = "Option %s expects a value" % option
-                        raise ArgumentPreprocessingError(msg)
-                    val = args[i]
-                    del args[i]
-                elif not takearg and val is not None:
-                    msg = "Option %s doesn't expects a value" % option
-                    raise ArgumentPreprocessingError(msg)
-                cb(option, val)
-        else:
-            i += 1
-
-
-@contextlib.contextmanager
-def fix_import_path(args):
-    """Prepare sys.path for running the linter checks.
-
-    Within this context, each of the given arguments is importable.
-    Paths are added to sys.path in corresponding order to the arguments.
-    We avoid adding duplicate directories to sys.path.
-    `sys.path` is reset to its original value upon exiting this context.
-    """
-    orig = list(sys.path)
-    changes = []
-    for arg in args:
-        path = _get_python_path(arg)
-        if path not in changes:
-            changes.append(path)
-    sys.path[:] = changes + ["."] + sys.path
-    try:
-        yield
-    finally:
-        sys.path[:] = orig
-
-
-class Run:
-    """helper class to use as main for pylint :
-
-    run(*sys.argv[1:])
-    """
-
-    LinterClass = PyLinter
-    option_groups = (
-        (
-            "Commands",
-            "Options which are actually commands. Options in this \
-group are mutually exclusive.",
-        ),
-    )
-
-    def __init__(self, args, reporter=None, do_exit=True):
-        self._rcfile = None
-        self._plugins = []
-        self.verbose = None
-        try:
-            preprocess_options(
-                args,
-                {
-                    # option: (callback, takearg)
-                    "init-hook": (cb_init_hook, True),
-                    "rcfile": (self.cb_set_rcfile, True),
-                    "load-plugins": (self.cb_add_plugins, True),
-                    "verbose": (self.cb_verbose_mode, False),
-                },
-            )
-        except ArgumentPreprocessingError as ex:
-            print(ex, file=sys.stderr)
-            sys.exit(32)
-
-        self.linter = linter = self.LinterClass(
-            (
-                (
-                    "rcfile",
-                    {
-                        "action": "callback",
-                        "callback": lambda *args: 1,
-                        "type": "string",
-                        "metavar": "<file>",
-                        "help": "Specify a configuration file.",
-                    },
-                ),
-                (
-                    "init-hook",
-                    {
-                        "action": "callback",
-                        "callback": lambda *args: 1,
-                        "type": "string",
-                        "metavar": "<code>",
-                        "level": 1,
-                        "help": "Python code to execute, usually for sys.path "
-                        "manipulation such as pygtk.require().",
-                    },
-                ),
-                (
-                    "help-msg",
-                    {
-                        "action": "callback",
-                        "type": "string",
-                        "metavar": "<msg-id>",
-                        "callback": self.cb_help_message,
-                        "group": "Commands",
-                        "help": "Display a help message for the given message id and "
-                        "exit. The value may be a comma separated list of message ids.",
-                    },
-                ),
-                (
-                    "list-msgs",
-                    {
-                        "action": "callback",
-                        "metavar": "<msg-id>",
-                        "callback": self.cb_list_messages,
-                        "group": "Commands",
-                        "level": 1,
-                        "help": "Generate pylint's messages.",
-                    },
-                ),
-                (
-                    "list-msgs-enabled",
-                    {
-                        "action": "callback",
-                        "metavar": "<msg-id>",
-                        "callback": self.cb_list_messages_enabled,
-                        "group": "Commands",
-                        "level": 1,
-                        "help": "Display a list of what messages are enabled "
-                        "and disabled with the given configuration.",
-                    },
-                ),
-                (
-                    "list-groups",
-                    {
-                        "action": "callback",
-                        "metavar": "<msg-id>",
-                        "callback": self.cb_list_groups,
-                        "group": "Commands",
-                        "level": 1,
-                        "help": "List pylint's message groups.",
-                    },
-                ),
-                (
-                    "list-conf-levels",
-                    {
-                        "action": "callback",
-                        "callback": cb_list_confidence_levels,
-                        "group": "Commands",
-                        "level": 1,
-                        "help": "Generate pylint's confidence levels.",
-                    },
-                ),
-                (
-                    "full-documentation",
-                    {
-                        "action": "callback",
-                        "metavar": "<msg-id>",
-                        "callback": self.cb_full_documentation,
-                        "group": "Commands",
-                        "level": 1,
-                        "help": "Generate pylint's full documentation.",
-                    },
-                ),
-                (
-                    "generate-rcfile",
-                    {
-                        "action": "callback",
-                        "callback": self.cb_generate_config,
-                        "group": "Commands",
-                        "help": "Generate a sample configuration file according to "
-                        "the current configuration. You can put other options "
-                        "before this one to get them in the generated "
-                        "configuration.",
-                    },
-                ),
-                (
-                    "generate-man",
-                    {
-                        "action": "callback",
-                        "callback": self.cb_generate_manpage,
-                        "group": "Commands",
-                        "help": "Generate pylint's man page.",
-                        "hide": True,
-                    },
-                ),
-                (
-                    "errors-only",
-                    {
-                        "action": "callback",
-                        "callback": self.cb_error_mode,
-                        "short": "E",
-                        "help": "In error mode, checkers without error messages are "
-                        "disabled and for others, only the ERROR messages are "
-                        "displayed, and no reports are done by default.",
-                    },
-                ),
-                (
-                    "py3k",
-                    {
-                        "action": "callback",
-                        "callback": self.cb_python3_porting_mode,
-                        "help": "In Python 3 porting mode, all checkers will be "
-                        "disabled and only messages emitted by the porting "
-                        "checker will be displayed.",
-                    },
-                ),
-                (
-                    "verbose",
-                    {
-                        "action": "callback",
-                        "callback": self.cb_verbose_mode,
-                        "short": "v",
-                        "help": "In verbose mode, extra non-checker-related info "
-                        "will be displayed.",
-                    },
-                ),
-            ),
-            option_groups=self.option_groups,
-            pylintrc=self._rcfile,
-        )
-        # register standard checkers
-        linter.load_default_plugins()
-        # load command line plugins
-        linter.load_plugin_modules(self._plugins)
-        # add some help section
-        linter.add_help_section("Environment variables", config.ENV_HELP, level=1)
-        # pylint: disable=bad-continuation
-        linter.add_help_section(
-            "Output",
-            "Using the default text output, the message format is :                          \n"
-            "                                                                                \n"
-            "        MESSAGE_TYPE: LINE_NUM:[OBJECT:] MESSAGE                                \n"
-            "                                                                                \n"
-            "There are 5 kind of message types :                                             \n"
-            "    * (C) convention, for programming standard violation                        \n"
-            "    * (R) refactor, for bad code smell                                          \n"
-            "    * (W) warning, for python specific problems                                 \n"
-            "    * (E) error, for probable bugs in the code                                  \n"
-            "    * (F) fatal, if an error occurred which prevented pylint from doing further\n"
-            "processing.\n",
-            level=1,
-        )
-        linter.add_help_section(
-            "Output status code",
-            "Pylint should leave with following status code:                                 \n"
-            "    * 0 if everything went fine                                                 \n"
-            "    * 1 if a fatal message was issued                                           \n"
-            "    * 2 if an error message was issued                                          \n"
-            "    * 4 if a warning message was issued                                         \n"
-            "    * 8 if a refactor message was issued                                        \n"
-            "    * 16 if a convention message was issued                                     \n"
-            "    * 32 on usage error                                                         \n"
-            "                                                                                \n"
-            "status 1 to 16 will be bit-ORed so you can know which different categories has\n"
-            "been issued by analysing pylint output status code\n",
-            level=1,
-        )
-        # read configuration
-        linter.disable("I")
-        linter.enable("c-extension-no-member")
-        linter.read_config_file(verbose=self.verbose)
-        config_parser = linter.cfgfile_parser
-        # run init hook, if present, before loading plugins
-        if config_parser.has_option("MASTER", "init-hook"):
-            cb_init_hook(
-                "init-hook", utils._unquote(config_parser.get("MASTER", "init-hook"))
-            )
-        # is there some additional plugins in the file configuration, in
-        if config_parser.has_option("MASTER", "load-plugins"):
-            plugins = utils._splitstrip(config_parser.get("MASTER", "load-plugins"))
-            linter.load_plugin_modules(plugins)
-        # now we can load file config and command line, plugins (which can
-        # provide options) have been registered
-        linter.load_config_file()
-
-        if reporter:
-            # if a custom reporter is provided as argument, it may be overridden
-            # by file parameters, so re-set it here, but before command line
-            # parsing so it's still overrideable by command line option
-            linter.set_reporter(reporter)
-        try:
-            args = linter.load_command_line_configuration(args)
-        except SystemExit as exc:
-            if exc.code == 2:  # bad options
-                exc.code = 32
-            raise
-        if not args:
-            print(linter.help())
-            sys.exit(32)
-
-        if linter.config.jobs < 0:
-            print(
-                "Jobs number (%d) should be greater than or equal to 0"
-                % linter.config.jobs,
-                file=sys.stderr,
-            )
-            sys.exit(32)
-        if linter.config.jobs > 1 or linter.config.jobs == 0:
-            if multiprocessing is None:
-                print(
-                    "Multiprocessing library is missing, " "fallback to single process",
-                    file=sys.stderr,
-                )
-                linter.set_option("jobs", 1)
-            else:
-                if linter.config.jobs == 0:
-                    linter.config.jobs = _cpu_count()
-
-        # We have loaded configuration from config file and command line. Now, we can
-        # load plugin specific configuration.
-        linter.load_plugin_configuration()
-
-        # insert current working directory to the python path to have a correct
-        # behaviour
-        with fix_import_path(args):
-            linter.check(args)
-            linter.generate_reports()
-        if do_exit:
-            if linter.config.exit_zero:
-                sys.exit(0)
-            else:
-                sys.exit(self.linter.msg_status)
-
-    def cb_set_rcfile(self, name, value):
-        """callback for option preprocessing (i.e. before option parsing)"""
-        self._rcfile = value
-
-    def cb_add_plugins(self, name, value):
-        """callback for option preprocessing (i.e. before option parsing)"""
-        self._plugins.extend(utils._splitstrip(value))
-
-    def cb_error_mode(self, *args, **kwargs):
-        """error mode:
-        * disable all but error messages
-        * disable the 'miscellaneous' checker which can be safely deactivated in
-          debug
-        * disable reports
-        * do not save execution information
-        """
-        self.linter.error_mode()
-
-    def cb_generate_config(self, *args, **kwargs):
-        """optik callback for sample config file generation"""
-        self.linter.generate_config(skipsections=("COMMANDS",))
-        sys.exit(0)
-
-    def cb_generate_manpage(self, *args, **kwargs):
-        """optik callback for sample config file generation"""
-        self.linter.generate_manpage(__pkginfo__)
-        sys.exit(0)
-
-    def cb_help_message(self, option, optname, value, parser):
-        """optik callback for printing some help about a particular message"""
-        self.linter.msgs_store.help_message(utils._splitstrip(value))
-        sys.exit(0)
-
-    def cb_full_documentation(self, option, optname, value, parser):
-        """optik callback for printing full documentation"""
-        self.linter.print_full_documentation()
-        sys.exit(0)
-
-    def cb_list_messages(self, option, optname, value, parser):
-        """optik callback for printing available messages"""
-        self.linter.msgs_store.list_messages()
-        sys.exit(0)
-
-    def cb_list_messages_enabled(self, option, optname, value, parser):
-        """optik callback for printing available messages"""
-        self.linter.list_messages_enabled()
-        sys.exit(0)
-
-    def cb_list_groups(self, *args, **kwargs):
-        """List all the check groups that pylint knows about
-
-        These should be useful to know what check groups someone can disable
-        or enable.
-        """
-        for check in self.linter.get_checker_names():
-            print(check)
-        sys.exit(0)
-
-    def cb_python3_porting_mode(self, *args, **kwargs):
-        """Activate only the python3 porting checker."""
-        self.linter.python3_porting_mode()
-
-    def cb_verbose_mode(self, *args, **kwargs):
-        self.verbose = True
-
-
-def cb_list_confidence_levels(option, optname, value, parser):
-    for level in interfaces.CONFIDENCE_LEVELS:
-        print("%-18s: %s" % level)
-    sys.exit(0)
-
-
-def cb_init_hook(optname, value):
-    """exec arbitrary code to set sys.path for instance"""
-    exec(value)  # pylint: disable=exec-used
-
-
-if __name__ == "__main__":
-    Run(sys.argv[1:])
diff --git a/venv/Lib/site-packages/pylint/message/__init__.py b/venv/Lib/site-packages/pylint/message/__init__.py
deleted file mode 100644
index 5ac8411..0000000
--- a/venv/Lib/site-packages/pylint/message/__init__.py
+++ /dev/null
@@ -1,54 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2009 Vincent
-# Copyright (c) 2009 Mads Kiilerich <mads@kiilerich.com>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014-2015 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 LCD 47 <lcd047@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2014 Damien Nozay <damien.nozay@gmail.com>
-# Copyright (c) 2015 Aru Sahni <arusahni@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Simu Toni <simutoni@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2016 Glenn Matthews <glmatthe@cisco.com>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016 xmo-odoo <xmo-odoo@users.noreply.github.com>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Pierre Sassoulas <pierre.sassoulas@cea.fr>
-# Copyright (c) 2017 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2017 Chris Lamb <chris@chris-lamb.co.uk>
-# Copyright (c) 2017 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2017 Thomas Hisch <t.hisch@gmail.com>
-# Copyright (c) 2017 Mikhail Fesenko <proggga@gmail.com>
-# Copyright (c) 2017 Craig Citro <craigcitro@gmail.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Pierre Sassoulas <pierre.sassoulas@wisebim.fr>
-# Copyright (c) 2018 Reverb C <reverbc@users.noreply.github.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""All the classes related to Message handling."""
-
-from pylint.message.message import Message
-from pylint.message.message_definition import MessageDefinition
-from pylint.message.message_definition_store import MessageDefinitionStore
-from pylint.message.message_handler_mix_in import MessagesHandlerMixIn
-from pylint.message.message_id_store import MessageIdStore
-
-__all__ = [
-    "Message",
-    "MessageDefinition",
-    "MessageDefinitionStore",
-    "MessagesHandlerMixIn",
-    "MessageIdStore",
-]
diff --git a/venv/Lib/site-packages/pylint/message/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/message/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index f3462f1..0000000
--- a/venv/Lib/site-packages/pylint/message/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/message/__pycache__/message.cpython-37.pyc b/venv/Lib/site-packages/pylint/message/__pycache__/message.cpython-37.pyc
deleted file mode 100644
index 6c89577..0000000
--- a/venv/Lib/site-packages/pylint/message/__pycache__/message.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/message/__pycache__/message_definition.cpython-37.pyc b/venv/Lib/site-packages/pylint/message/__pycache__/message_definition.cpython-37.pyc
deleted file mode 100644
index 952803b..0000000
--- a/venv/Lib/site-packages/pylint/message/__pycache__/message_definition.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/message/__pycache__/message_definition_store.cpython-37.pyc b/venv/Lib/site-packages/pylint/message/__pycache__/message_definition_store.cpython-37.pyc
deleted file mode 100644
index ce6f867..0000000
--- a/venv/Lib/site-packages/pylint/message/__pycache__/message_definition_store.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/message/__pycache__/message_handler_mix_in.cpython-37.pyc b/venv/Lib/site-packages/pylint/message/__pycache__/message_handler_mix_in.cpython-37.pyc
deleted file mode 100644
index 23cc65a..0000000
--- a/venv/Lib/site-packages/pylint/message/__pycache__/message_handler_mix_in.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/message/__pycache__/message_id_store.cpython-37.pyc b/venv/Lib/site-packages/pylint/message/__pycache__/message_id_store.cpython-37.pyc
deleted file mode 100644
index f132b88..0000000
--- a/venv/Lib/site-packages/pylint/message/__pycache__/message_id_store.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/message/message.py b/venv/Lib/site-packages/pylint/message/message.py
deleted file mode 100644
index e2b0320..0000000
--- a/venv/Lib/site-packages/pylint/message/message.py
+++ /dev/null
@@ -1,53 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-
-import collections
-
-from pylint.constants import MSG_TYPES
-
-_MsgBase = collections.namedtuple(
-    "_MsgBase",
-    [
-        "msg_id",
-        "symbol",
-        "msg",
-        "C",
-        "category",
-        "confidence",
-        "abspath",
-        "path",
-        "module",
-        "obj",
-        "line",
-        "column",
-    ],
-)
-
-
-class Message(_MsgBase):
-    """This class represent a message to be issued by the reporters"""
-
-    def __new__(cls, msg_id, symbol, location, msg, confidence):
-        return _MsgBase.__new__(
-            cls,
-            msg_id,
-            symbol,
-            msg,
-            msg_id[0],
-            MSG_TYPES[msg_id[0]],
-            confidence,
-            *location
-        )
-
-    def format(self, template):
-        """Format the message according to the given template.
-
-        The template format is the one of the format method :
-        cf. http://docs.python.org/2/library/string.html#formatstrings
-        """
-        # For some reason, _asdict on derived namedtuples does not work with
-        # Python 3.4. Needs some investigation.
-        return template.format(**dict(zip(self._fields, self)))
diff --git a/venv/Lib/site-packages/pylint/message/message_definition.py b/venv/Lib/site-packages/pylint/message/message_definition.py
deleted file mode 100644
index e54c15a..0000000
--- a/venv/Lib/site-packages/pylint/message/message_definition.py
+++ /dev/null
@@ -1,84 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import sys
-
-from pylint.constants import MSG_TYPES
-from pylint.exceptions import InvalidMessageError
-from pylint.utils import normalize_text
-
-
-class MessageDefinition:
-    def __init__(
-        self,
-        checker,
-        msgid,
-        msg,
-        description,
-        symbol,
-        scope,
-        minversion=None,
-        maxversion=None,
-        old_names=None,
-    ):
-        self.checker = checker
-        self.check_msgid(msgid)
-        self.msgid = msgid
-        self.symbol = symbol
-        self.msg = msg
-        self.description = description
-        self.scope = scope
-        self.minversion = minversion
-        self.maxversion = maxversion
-        self.old_names = []
-        if old_names:
-            for old_msgid, old_symbol in old_names:
-                self.check_msgid(old_msgid)
-                self.old_names.append([old_msgid, old_symbol])
-
-    @staticmethod
-    def check_msgid(msgid: str) -> None:
-        if len(msgid) != 5:
-            raise InvalidMessageError("Invalid message id %r" % msgid)
-        if msgid[0] not in MSG_TYPES:
-            raise InvalidMessageError("Bad message type %s in %r" % (msgid[0], msgid))
-
-    def __repr__(self):
-        return "MessageDefinition:%s (%s)" % (self.symbol, self.msgid)
-
-    def __str__(self):
-        return "%s:\n%s %s" % (repr(self), self.msg, self.description)
-
-    def may_be_emitted(self):
-        """return True if message may be emitted using the current interpreter"""
-        if self.minversion is not None and self.minversion > sys.version_info:
-            return False
-        if self.maxversion is not None and self.maxversion <= sys.version_info:
-            return False
-        return True
-
-    def format_help(self, checkerref=False):
-        """return the help string for the given message id"""
-        desc = self.description
-        if checkerref:
-            desc += " This message belongs to the %s checker." % self.checker.name
-        title = self.msg
-        if self.minversion or self.maxversion:
-            restr = []
-            if self.minversion:
-                restr.append("< %s" % ".".join([str(n) for n in self.minversion]))
-            if self.maxversion:
-                restr.append(">= %s" % ".".join([str(n) for n in self.maxversion]))
-            restr = " or ".join(restr)
-            if checkerref:
-                desc += " It can't be emitted when using Python %s." % restr
-            else:
-                desc += " This message can't be emitted when using Python %s." % restr
-        msg_help = normalize_text(" ".join(desc.split()), indent="  ")
-        message_id = "%s (%s)" % (self.symbol, self.msgid)
-        if title != "%s":
-            title = title.splitlines()[0]
-            return ":%s: *%s*\n%s" % (message_id, title.rstrip(" "), msg_help)
-        return ":%s:\n%s" % (message_id, msg_help)
diff --git a/venv/Lib/site-packages/pylint/message/message_definition_store.py b/venv/Lib/site-packages/pylint/message/message_definition_store.py
deleted file mode 100644
index f7d87b6..0000000
--- a/venv/Lib/site-packages/pylint/message/message_definition_store.py
+++ /dev/null
@@ -1,90 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import collections
-
-from pylint.exceptions import UnknownMessageError
-from pylint.message.message_id_store import MessageIdStore
-
-
-class MessageDefinitionStore:
-
-    """The messages store knows information about every possible message definition but has
-    no particular state during analysis.
-    """
-
-    def __init__(self):
-        self.message_id_store = MessageIdStore()
-        # Primary registry for all active messages definitions.
-        # It contains the 1:1 mapping from msgid to MessageDefinition.
-        # Keys are msgid, values are MessageDefinition
-        self._messages_definitions = {}
-        # MessageDefinition kept by category
-        self._msgs_by_category = collections.defaultdict(list)
-
-    @property
-    def messages(self) -> list:
-        """The list of all active messages."""
-        return self._messages_definitions.values()
-
-    def register_messages_from_checker(self, checker):
-        """Register all messages definitions from a checker.
-
-        :param BaseChecker checker:
-        """
-        checker.check_consistency()
-        for message in checker.messages:
-            self.register_message(message)
-
-    def register_message(self, message):
-        """Register a MessageDefinition with consistency in mind.
-
-        :param MessageDefinition message: The message definition being added.
-        """
-        self.message_id_store.register_message_definition(message)
-        self._messages_definitions[message.msgid] = message
-        self._msgs_by_category[message.msgid[0]].append(message.msgid)
-
-    def get_message_definitions(self, msgid_or_symbol: str) -> list:
-        """Returns the Message object for this message.
-        :param str msgid_or_symbol: msgid_or_symbol may be either a numeric or symbolic id.
-        :raises UnknownMessageError: if the message id is not defined.
-        :rtype: List of MessageDefinition
-        :return: A message definition corresponding to msgid_or_symbol
-        """
-        return [
-            self._messages_definitions[m]
-            for m in self.message_id_store.get_active_msgids(msgid_or_symbol)
-        ]
-
-    def get_msg_display_string(self, msgid_or_symbol: str):
-        """Generates a user-consumable representation of a message. """
-        message_definitions = self.get_message_definitions(msgid_or_symbol)
-        if len(message_definitions) == 1:
-            return repr(message_definitions[0].symbol)
-        return repr([md.symbol for md in message_definitions])
-
-    def help_message(self, msgids_or_symbols: list):
-        """Display help messages for the given message identifiers"""
-        for msgids_or_symbol in msgids_or_symbols:
-            try:
-                for message_definition in self.get_message_definitions(
-                    msgids_or_symbol
-                ):
-                    print(message_definition.format_help(checkerref=True))
-                    print("")
-            except UnknownMessageError as ex:
-                print(ex)
-                print("")
-                continue
-
-    def list_messages(self):
-        """Output full messages list documentation in ReST format. """
-        messages = sorted(self._messages_definitions.values(), key=lambda m: m.msgid)
-        for message in messages:
-            if not message.may_be_emitted():
-                continue
-            print(message.format_help(checkerref=False))
-        print("")
diff --git a/venv/Lib/site-packages/pylint/message/message_handler_mix_in.py b/venv/Lib/site-packages/pylint/message/message_handler_mix_in.py
deleted file mode 100644
index 813cdd7..0000000
--- a/venv/Lib/site-packages/pylint/message/message_handler_mix_in.py
+++ /dev/null
@@ -1,393 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import sys
-
-from pylint.constants import (
-    _SCOPE_EXEMPT,
-    MAIN_CHECKER_NAME,
-    MSG_STATE_CONFIDENCE,
-    MSG_STATE_SCOPE_CONFIG,
-    MSG_STATE_SCOPE_MODULE,
-    MSG_TYPES,
-    MSG_TYPES_LONG,
-    MSG_TYPES_STATUS,
-    WarningScope,
-)
-from pylint.exceptions import InvalidMessageError, UnknownMessageError
-from pylint.interfaces import UNDEFINED
-from pylint.message.message import Message
-from pylint.utils import get_module_and_frameid, get_rst_section, get_rst_title
-
-
-class MessagesHandlerMixIn:
-    """a mix-in class containing all the messages related methods for the main
-    lint class
-    """
-
-    __by_id_managed_msgs = []  # type: ignore
-
-    def __init__(self):
-        self._msgs_state = {}
-        self.msg_status = 0
-
-    def _checker_messages(self, checker):
-        for known_checker in self._checkers[checker.lower()]:
-            for msgid in known_checker.msgs:
-                yield msgid
-
-    @classmethod
-    def clear_by_id_managed_msgs(cls):
-        cls.__by_id_managed_msgs.clear()
-
-    @classmethod
-    def get_by_id_managed_msgs(cls):
-        return cls.__by_id_managed_msgs
-
-    def _register_by_id_managed_msg(self, msgid, line, is_disabled=True):
-        """If the msgid is a numeric one, then register it to inform the user
-        it could furnish instead a symbolic msgid."""
-        try:
-            message_definitions = self.msgs_store.get_message_definitions(msgid)
-            for message_definition in message_definitions:
-                if msgid == message_definition.msgid:
-                    MessagesHandlerMixIn.__by_id_managed_msgs.append(
-                        (
-                            self.current_name,
-                            message_definition.msgid,
-                            message_definition.symbol,
-                            line,
-                            is_disabled,
-                        )
-                    )
-        except UnknownMessageError:
-            pass
-
-    def disable(self, msgid, scope="package", line=None, ignore_unknown=False):
-        """don't output message of the given id"""
-        self._set_msg_status(
-            msgid, enable=False, scope=scope, line=line, ignore_unknown=ignore_unknown
-        )
-        self._register_by_id_managed_msg(msgid, line)
-
-    def enable(self, msgid, scope="package", line=None, ignore_unknown=False):
-        """reenable message of the given id"""
-        self._set_msg_status(
-            msgid, enable=True, scope=scope, line=line, ignore_unknown=ignore_unknown
-        )
-        self._register_by_id_managed_msg(msgid, line, is_disabled=False)
-
-    def _set_msg_status(
-        self, msgid, enable, scope="package", line=None, ignore_unknown=False
-    ):
-        assert scope in ("package", "module")
-
-        if msgid == "all":
-            for _msgid in MSG_TYPES:
-                self._set_msg_status(_msgid, enable, scope, line, ignore_unknown)
-            if enable and not self._python3_porting_mode:
-                # Don't activate the python 3 porting checker if it wasn't activated explicitly.
-                self.disable("python3")
-            return
-
-        # msgid is a category?
-        category_id = msgid.upper()
-        if category_id not in MSG_TYPES:
-            category_id = MSG_TYPES_LONG.get(category_id)
-        if category_id is not None:
-            for _msgid in self.msgs_store._msgs_by_category.get(category_id):
-                self._set_msg_status(_msgid, enable, scope, line)
-            return
-
-        # msgid is a checker name?
-        if msgid.lower() in self._checkers:
-            for checker in self._checkers[msgid.lower()]:
-                for _msgid in checker.msgs:
-                    self._set_msg_status(_msgid, enable, scope, line)
-            return
-
-        # msgid is report id?
-        if msgid.lower().startswith("rp"):
-            if enable:
-                self.enable_report(msgid)
-            else:
-                self.disable_report(msgid)
-            return
-
-        try:
-            # msgid is a symbolic or numeric msgid.
-            message_definitions = self.msgs_store.get_message_definitions(msgid)
-        except UnknownMessageError:
-            if ignore_unknown:
-                return
-            raise
-        for message_definition in message_definitions:
-            self._set_one_msg_status(scope, message_definition, line, enable)
-
-    def _set_one_msg_status(self, scope, msg, line, enable):
-        if scope == "module":
-            self.file_state.set_msg_status(msg, line, enable)
-            if not enable and msg.symbol != "locally-disabled":
-                self.add_message(
-                    "locally-disabled", line=line, args=(msg.symbol, msg.msgid)
-                )
-        else:
-            msgs = self._msgs_state
-            msgs[msg.msgid] = enable
-            # sync configuration object
-            self.config.enable = [
-                self._message_symbol(mid) for mid, val in sorted(msgs.items()) if val
-            ]
-            self.config.disable = [
-                self._message_symbol(mid)
-                for mid, val in sorted(msgs.items())
-                if not val
-            ]
-
-    def _message_symbol(self, msgid):
-        """Get the message symbol of the given message id
-
-        Return the original message id if the message does not
-        exist.
-        """
-        try:
-            return [md.symbol for md in self.msgs_store.get_message_definitions(msgid)]
-        except UnknownMessageError:
-            return msgid
-
-    def get_message_state_scope(self, msgid, line=None, confidence=UNDEFINED):
-        """Returns the scope at which a message was enabled/disabled."""
-        if self.config.confidence and confidence.name not in self.config.confidence:
-            return MSG_STATE_CONFIDENCE
-        try:
-            if line in self.file_state._module_msgs_state[msgid]:
-                return MSG_STATE_SCOPE_MODULE
-        except (KeyError, TypeError):
-            return MSG_STATE_SCOPE_CONFIG
-        return None
-
-    def is_message_enabled(self, msg_descr, line=None, confidence=None):
-        """return true if the message associated to the given message id is
-        enabled
-
-        msgid may be either a numeric or symbolic message id.
-        """
-        if self.config.confidence and confidence:
-            if confidence.name not in self.config.confidence:
-                return False
-        try:
-            message_definitions = self.msgs_store.get_message_definitions(msg_descr)
-            msgids = [md.msgid for md in message_definitions]
-        except UnknownMessageError:
-            # The linter checks for messages that are not registered
-            # due to version mismatch, just treat them as message IDs
-            # for now.
-            msgids = [msg_descr]
-        for msgid in msgids:
-            if self.is_one_message_enabled(msgid, line):
-                return True
-        return False
-
-    def is_one_message_enabled(self, msgid, line):
-        if line is None:
-            return self._msgs_state.get(msgid, True)
-        try:
-            return self.file_state._module_msgs_state[msgid][line]
-        except KeyError:
-            # Check if the message's line is after the maximum line existing in ast tree.
-            # This line won't appear in the ast tree and won't be referred in
-            #  self.file_state._module_msgs_state
-            # This happens for example with a commented line at the end of a module.
-            max_line_number = self.file_state.get_effective_max_line_number()
-            if max_line_number and line > max_line_number:
-                fallback = True
-                lines = self.file_state._raw_module_msgs_state.get(msgid, {})
-
-                # Doesn't consider scopes, as a disable can be in a different scope
-                # than that of the current line.
-                closest_lines = reversed(
-                    [
-                        (message_line, enable)
-                        for message_line, enable in lines.items()
-                        if message_line <= line
-                    ]
-                )
-                last_line, is_enabled = next(closest_lines, (None, None))
-                if last_line is not None:
-                    fallback = is_enabled
-
-                return self._msgs_state.get(msgid, fallback)
-            return self._msgs_state.get(msgid, True)
-
-    def add_message(
-        self, msgid, line=None, node=None, args=None, confidence=None, col_offset=None
-    ):
-        """Adds a message given by ID or name.
-
-        If provided, the message string is expanded using args.
-
-        AST checkers must provide the node argument (but may optionally
-        provide line if the line number is different), raw and token checkers
-        must provide the line argument.
-        """
-        if confidence is None:
-            confidence = UNDEFINED
-        message_definitions = self.msgs_store.get_message_definitions(msgid)
-        for message_definition in message_definitions:
-            self.add_one_message(
-                message_definition, line, node, args, confidence, col_offset
-            )
-
-    @staticmethod
-    def check_message_definition(message_definition, line, node):
-        if message_definition.msgid[0] not in _SCOPE_EXEMPT:
-            # Fatal messages and reports are special, the node/scope distinction
-            # does not apply to them.
-            if message_definition.scope == WarningScope.LINE:
-                if line is None:
-                    raise InvalidMessageError(
-                        "Message %s must provide line, got None"
-                        % message_definition.msgid
-                    )
-                if node is not None:
-                    raise InvalidMessageError(
-                        "Message %s must only provide line, "
-                        "got line=%s, node=%s" % (message_definition.msgid, line, node)
-                    )
-            elif message_definition.scope == WarningScope.NODE:
-                # Node-based warnings may provide an override line.
-                if node is None:
-                    raise InvalidMessageError(
-                        "Message %s must provide Node, got None"
-                        % message_definition.msgid
-                    )
-
-    def add_one_message(
-        self, message_definition, line, node, args, confidence, col_offset
-    ):
-        self.check_message_definition(message_definition, line, node)
-        if line is None and node is not None:
-            line = node.fromlineno
-        if col_offset is None and hasattr(node, "col_offset"):
-            col_offset = node.col_offset
-
-        # should this message be displayed
-        if not self.is_message_enabled(message_definition.msgid, line, confidence):
-            self.file_state.handle_ignored_message(
-                self.get_message_state_scope(
-                    message_definition.msgid, line, confidence
-                ),
-                message_definition.msgid,
-                line,
-                node,
-                args,
-                confidence,
-            )
-            return
-        # update stats
-        msg_cat = MSG_TYPES[message_definition.msgid[0]]
-        self.msg_status |= MSG_TYPES_STATUS[message_definition.msgid[0]]
-        self.stats[msg_cat] += 1
-        self.stats["by_module"][self.current_name][msg_cat] += 1
-        try:
-            self.stats["by_msg"][message_definition.symbol] += 1
-        except KeyError:
-            self.stats["by_msg"][message_definition.symbol] = 1
-        # expand message ?
-        msg = message_definition.msg
-        if args:
-            msg %= args
-        # get module and object
-        if node is None:
-            module, obj = self.current_name, ""
-            abspath = self.current_file
-        else:
-            module, obj = get_module_and_frameid(node)
-            abspath = node.root().file
-        path = abspath.replace(self.reporter.path_strip_prefix, "", 1)
-        # add the message
-        self.reporter.handle_message(
-            Message(
-                message_definition.msgid,
-                message_definition.symbol,
-                (abspath, path, module, obj, line or 1, col_offset or 0),
-                msg,
-                confidence,
-            )
-        )
-
-    def _get_checkers_infos(self):
-        by_checker = {}
-        for checker in self.get_checkers():
-            name = checker.name
-            if name != "master":
-                try:
-                    by_checker[name]["checker"] = checker
-                    by_checker[name]["options"] += checker.options_and_values()
-                    by_checker[name]["msgs"].update(checker.msgs)
-                    by_checker[name]["reports"] += checker.reports
-                except KeyError:
-                    by_checker[name] = {
-                        "checker": checker,
-                        "options": list(checker.options_and_values()),
-                        "msgs": dict(checker.msgs),
-                        "reports": list(checker.reports),
-                    }
-        return by_checker
-
-    def get_checkers_documentation(self):
-        result = get_rst_title("Pylint global options and switches", "-")
-        result += """
-Pylint provides global options and switches.
-
-"""
-        for checker in self.get_checkers():
-            name = checker.name
-            if name == MAIN_CHECKER_NAME:
-                if checker.options:
-                    for section, options in checker.options_by_section():
-                        if section is None:
-                            title = "General options"
-                        else:
-                            title = "%s options" % section.capitalize()
-                        result += get_rst_title(title, "~")
-                        result += "%s\n" % get_rst_section(None, options)
-        result += get_rst_title("Pylint checkers' options and switches", "-")
-        result += """\
-
-Pylint checkers can provide three set of features:
-
-* options that control their execution,
-* messages that they can raise,
-* reports that they can generate.
-
-Below is a list of all checkers and their features.
-
-"""
-        by_checker = self._get_checkers_infos()
-        for checker in sorted(by_checker):
-            information = by_checker[checker]
-            checker = information["checker"]
-            del information["checker"]
-            result += checker.get_full_documentation(**information)
-        return result
-
-    def print_full_documentation(self, stream=None):
-        """output a full documentation in ReST format"""
-        if not stream:
-            stream = sys.stdout
-        print(self.get_checkers_documentation()[:-1], file=stream)
-
-    @staticmethod
-    def _print_checker_doc(information, stream=None):
-        """Helper method for print_full_documentation.
-
-        Also used by doc/exts/pylint_extensions.py.
-        """
-        if not stream:
-            stream = sys.stdout
-        checker = information["checker"]
-        del information["checker"]
-        print(checker.get_full_documentation(**information)[:-1], file=stream)
diff --git a/venv/Lib/site-packages/pylint/message/message_id_store.py b/venv/Lib/site-packages/pylint/message/message_id_store.py
deleted file mode 100644
index 756888a..0000000
--- a/venv/Lib/site-packages/pylint/message/message_id_store.py
+++ /dev/null
@@ -1,128 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-from typing import List
-
-from pylint.exceptions import InvalidMessageError, UnknownMessageError
-
-
-class MessageIdStore:
-
-    """The MessageIdStore store MessageId and make sure that there is a 1-1 relation between msgid and symbol."""
-
-    def __init__(self):
-        self.__msgid_to_symbol = {}
-        self.__symbol_to_msgid = {}
-        self.__old_names = {}
-
-    def __len__(self):
-        return len(self.__msgid_to_symbol)
-
-    def __repr__(self):
-        result = "MessageIdStore: [\n"
-        for msgid, symbol in self.__msgid_to_symbol.items():
-            result += "  - {msgid} ({symbol})\n".format(msgid=msgid, symbol=symbol)
-        result += "]"
-        return result
-
-    def get_symbol(self, msgid: str) -> str:
-        return self.__msgid_to_symbol[msgid]
-
-    def get_msgid(self, symbol: str) -> str:
-        return self.__symbol_to_msgid[symbol]
-
-    def register_message_definition(self, message_definition):
-        self.check_msgid_and_symbol(message_definition.msgid, message_definition.symbol)
-        self.add_msgid_and_symbol(message_definition.msgid, message_definition.symbol)
-        for old_msgid, old_symbol in message_definition.old_names:
-            self.check_msgid_and_symbol(old_msgid, old_symbol)
-            self.add_legacy_msgid_and_symbol(
-                old_msgid, old_symbol, message_definition.msgid
-            )
-
-    def add_msgid_and_symbol(self, msgid: str, symbol: str) -> None:
-        """Add valid message id.
-
-        There is a little duplication with add_legacy_msgid_and_symbol to avoid a function call,
-        this is called a lot at initialization."""
-        self.__msgid_to_symbol[msgid] = symbol
-        self.__symbol_to_msgid[symbol] = msgid
-
-    def add_legacy_msgid_and_symbol(self, msgid: str, symbol: str, new_msgid: str):
-        """Add valid legacy message id.
-
-        There is a little duplication with add_msgid_and_symbol to avoid a function call,
-        this is called a lot at initialization."""
-        self.__msgid_to_symbol[msgid] = symbol
-        self.__symbol_to_msgid[symbol] = msgid
-        existing_old_names = self.__old_names.get(msgid, [])
-        existing_old_names.append(new_msgid)
-        self.__old_names[msgid] = existing_old_names
-
-    def check_msgid_and_symbol(self, msgid: str, symbol: str) -> None:
-        existing_msgid = self.__symbol_to_msgid.get(symbol)
-        existing_symbol = self.__msgid_to_symbol.get(msgid)
-        if existing_symbol is None and existing_msgid is None:
-            return
-        if existing_msgid is not None:
-            if existing_msgid != msgid:
-                self._raise_duplicate_msgid(symbol, msgid, existing_msgid)
-        if existing_symbol != symbol:
-            self._raise_duplicate_symbol(msgid, symbol, existing_symbol)
-
-    @staticmethod
-    def _raise_duplicate_symbol(msgid, symbol, other_symbol):
-        """Raise an error when a symbol is duplicated.
-
-        :param str msgid: The msgid corresponding to the symbols
-        :param str symbol: Offending symbol
-        :param str other_symbol: Other offending symbol
-        :raises InvalidMessageError:"""
-        symbols = [symbol, other_symbol]
-        symbols.sort()
-        error_message = "Message id '{msgid}' cannot have both ".format(msgid=msgid)
-        error_message += "'{other_symbol}' and '{symbol}' as symbolic name.".format(
-            other_symbol=symbols[0], symbol=symbols[1]
-        )
-        raise InvalidMessageError(error_message)
-
-    @staticmethod
-    def _raise_duplicate_msgid(symbol, msgid, other_msgid):
-        """Raise an error when a msgid is duplicated.
-
-        :param str symbol: The symbol corresponding to the msgids
-        :param str msgid: Offending msgid
-        :param str other_msgid: Other offending msgid
-        :raises InvalidMessageError:"""
-        msgids = [msgid, other_msgid]
-        msgids.sort()
-        error_message = (
-            "Message symbol '{symbol}' cannot be used for "
-            "'{other_msgid}' and '{msgid}' at the same time."
-            " If you're creating an 'old_names' use 'old-{symbol}' as the old symbol."
-        ).format(symbol=symbol, other_msgid=msgids[0], msgid=msgids[1])
-        raise InvalidMessageError(error_message)
-
-    def get_active_msgids(self, msgid_or_symbol: str) -> List[str]:
-        """Return msgids but the input can be a symbol."""
-        # Only msgid can have a digit as second letter
-        is_msgid = msgid_or_symbol[1:].isdigit()
-        if is_msgid:
-            msgid = msgid_or_symbol.upper()
-            symbol = self.__msgid_to_symbol.get(msgid)
-        else:
-            msgid = self.__symbol_to_msgid.get(msgid_or_symbol)
-            symbol = msgid_or_symbol
-        if not msgid or not symbol:
-            error_msg = "No such message id or symbol '{msgid_or_symbol}'.".format(
-                msgid_or_symbol=msgid_or_symbol
-            )
-            raise UnknownMessageError(error_msg)
-        # logging.debug(
-        #    "Return for {} and msgid {} is {}".format(
-        #        msgid_or_symbol, msgid, self.__old_names.get(msgid, [msgid])
-        #    )
-        # )
-        return self.__old_names.get(msgid, [msgid])
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__init__.py b/venv/Lib/site-packages/pylint/pyreverse/__init__.py
deleted file mode 100644
index 9ca1da5..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__init__.py
+++ /dev/null
@@ -1,8 +0,0 @@
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""
-pyreverse.extensions
-"""
-
-__revision__ = "$Id $"
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 6054dd9..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/diadefslib.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/diadefslib.cpython-37.pyc
deleted file mode 100644
index 64bdd6b..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/diadefslib.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/diagrams.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/diagrams.cpython-37.pyc
deleted file mode 100644
index cd5a663..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/diagrams.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/inspector.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/inspector.cpython-37.pyc
deleted file mode 100644
index 0bcfb4d..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/inspector.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/main.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/main.cpython-37.pyc
deleted file mode 100644
index c8f9398..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/main.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index 1711f15..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/vcgutils.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/vcgutils.cpython-37.pyc
deleted file mode 100644
index f1a93f5..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/vcgutils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/writer.cpython-37.pyc b/venv/Lib/site-packages/pylint/pyreverse/__pycache__/writer.cpython-37.pyc
deleted file mode 100644
index a0ac15c..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/__pycache__/writer.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/pyreverse/diadefslib.py b/venv/Lib/site-packages/pylint/pyreverse/diadefslib.py
deleted file mode 100644
index de4e9fd..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/diadefslib.py
+++ /dev/null
@@ -1,238 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006, 2008-2010, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""handle diagram generation options for class diagram or default diagrams
-"""
-
-import astroid
-
-from pylint.pyreverse.diagrams import ClassDiagram, PackageDiagram
-from pylint.pyreverse.utils import LocalsVisitor
-
-BUILTINS_NAME = "builtins"
-
-# diagram generators ##########################################################
-
-
-class DiaDefGenerator:
-    """handle diagram generation options"""
-
-    def __init__(self, linker, handler):
-        """common Diagram Handler initialization"""
-        self.config = handler.config
-        self._set_default_options()
-        self.linker = linker
-        self.classdiagram = None  # defined by subclasses
-
-    def get_title(self, node):
-        """get title for objects"""
-        title = node.name
-        if self.module_names:
-            title = "%s.%s" % (node.root().name, title)
-        return title
-
-    def _set_option(self, option):
-        """activate some options if not explicitly deactivated"""
-        # if we have a class diagram, we want more information by default;
-        # so if the option is None, we return True
-        if option is None:
-            return bool(self.config.classes)
-        return option
-
-    def _set_default_options(self):
-        """set different default options with _default dictionary"""
-        self.module_names = self._set_option(self.config.module_names)
-        all_ancestors = self._set_option(self.config.all_ancestors)
-        all_associated = self._set_option(self.config.all_associated)
-        anc_level, association_level = (0, 0)
-        if all_ancestors:
-            anc_level = -1
-        if all_associated:
-            association_level = -1
-        if self.config.show_ancestors is not None:
-            anc_level = self.config.show_ancestors
-        if self.config.show_associated is not None:
-            association_level = self.config.show_associated
-        self.anc_level, self.association_level = anc_level, association_level
-
-    def _get_levels(self):
-        """help function for search levels"""
-        return self.anc_level, self.association_level
-
-    def show_node(self, node):
-        """true if builtins and not show_builtins"""
-        if self.config.show_builtin:
-            return True
-        return node.root().name != BUILTINS_NAME
-
-    def add_class(self, node):
-        """visit one class and add it to diagram"""
-        self.linker.visit(node)
-        self.classdiagram.add_object(self.get_title(node), node)
-
-    def get_ancestors(self, node, level):
-        """return ancestor nodes of a class node"""
-        if level == 0:
-            return
-        for ancestor in node.ancestors(recurs=False):
-            if not self.show_node(ancestor):
-                continue
-            yield ancestor
-
-    def get_associated(self, klass_node, level):
-        """return associated nodes of a class node"""
-        if level == 0:
-            return
-        for association_nodes in list(klass_node.instance_attrs_type.values()) + list(
-            klass_node.locals_type.values()
-        ):
-            for node in association_nodes:
-                if isinstance(node, astroid.Instance):
-                    node = node._proxied
-                if not (isinstance(node, astroid.ClassDef) and self.show_node(node)):
-                    continue
-                yield node
-
-    def extract_classes(self, klass_node, anc_level, association_level):
-        """extract recursively classes related to klass_node"""
-        if self.classdiagram.has_node(klass_node) or not self.show_node(klass_node):
-            return
-        self.add_class(klass_node)
-
-        for ancestor in self.get_ancestors(klass_node, anc_level):
-            self.extract_classes(ancestor, anc_level - 1, association_level)
-
-        for node in self.get_associated(klass_node, association_level):
-            self.extract_classes(node, anc_level, association_level - 1)
-
-
-class DefaultDiadefGenerator(LocalsVisitor, DiaDefGenerator):
-    """generate minimum diagram definition for the project :
-
-    * a package diagram including project's modules
-    * a class diagram including project's classes
-    """
-
-    def __init__(self, linker, handler):
-        DiaDefGenerator.__init__(self, linker, handler)
-        LocalsVisitor.__init__(self)
-
-    def visit_project(self, node):
-        """visit a pyreverse.utils.Project node
-
-        create a diagram definition for packages
-        """
-        mode = self.config.mode
-        if len(node.modules) > 1:
-            self.pkgdiagram = PackageDiagram("packages %s" % node.name, mode)
-        else:
-            self.pkgdiagram = None
-        self.classdiagram = ClassDiagram("classes %s" % node.name, mode)
-
-    def leave_project(self, node):  # pylint: disable=unused-argument
-        """leave the pyreverse.utils.Project node
-
-        return the generated diagram definition
-        """
-        if self.pkgdiagram:
-            return self.pkgdiagram, self.classdiagram
-        return (self.classdiagram,)
-
-    def visit_module(self, node):
-        """visit an astroid.Module node
-
-        add this class to the package diagram definition
-        """
-        if self.pkgdiagram:
-            self.linker.visit(node)
-            self.pkgdiagram.add_object(node.name, node)
-
-    def visit_classdef(self, node):
-        """visit an astroid.Class node
-
-        add this class to the class diagram definition
-        """
-        anc_level, association_level = self._get_levels()
-        self.extract_classes(node, anc_level, association_level)
-
-    def visit_importfrom(self, node):
-        """visit astroid.ImportFrom  and catch modules for package diagram
-        """
-        if self.pkgdiagram:
-            self.pkgdiagram.add_from_depend(node, node.modname)
-
-
-class ClassDiadefGenerator(DiaDefGenerator):
-    """generate a class diagram definition including all classes related to a
-    given class
-    """
-
-    def __init__(self, linker, handler):
-        DiaDefGenerator.__init__(self, linker, handler)
-
-    def class_diagram(self, project, klass):
-        """return a class diagram definition for the given klass and its
-        related klasses
-        """
-
-        self.classdiagram = ClassDiagram(klass, self.config.mode)
-        if len(project.modules) > 1:
-            module, klass = klass.rsplit(".", 1)
-            module = project.get_module(module)
-        else:
-            module = project.modules[0]
-            klass = klass.split(".")[-1]
-        klass = next(module.ilookup(klass))
-
-        anc_level, association_level = self._get_levels()
-        self.extract_classes(klass, anc_level, association_level)
-        return self.classdiagram
-
-
-# diagram handler #############################################################
-
-
-class DiadefsHandler:
-    """handle diagram definitions :
-
-    get it from user (i.e. xml files) or generate them
-    """
-
-    def __init__(self, config):
-        self.config = config
-
-    def get_diadefs(self, project, linker):
-        """Get the diagrams configuration data
-
-        :param project:The pyreverse project
-        :type project: pyreverse.utils.Project
-        :param linker: The linker
-        :type linker: pyreverse.inspector.Linker(IdGeneratorMixIn, LocalsVisitor)
-
-        :returns: The list of diagram definitions
-        :rtype: list(:class:`pylint.pyreverse.diagrams.ClassDiagram`)
-        """
-
-        #  read and interpret diagram definitions (Diadefs)
-        diagrams = []
-        generator = ClassDiadefGenerator(linker, self)
-        for klass in self.config.classes:
-            diagrams.append(generator.class_diagram(project, klass))
-        if not diagrams:
-            diagrams = DefaultDiadefGenerator(linker, self).visit(project)
-        for diagram in diagrams:
-            diagram.extract_relationships()
-        return diagrams
diff --git a/venv/Lib/site-packages/pylint/pyreverse/diagrams.py b/venv/Lib/site-packages/pylint/pyreverse/diagrams.py
deleted file mode 100644
index b53b845..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/diagrams.py
+++ /dev/null
@@ -1,268 +0,0 @@
-# Copyright (c) 2006, 2008-2010, 2012-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""diagram objects
-"""
-
-import astroid
-
-from pylint.checkers.utils import decorated_with_property
-from pylint.pyreverse.utils import FilterMixIn, is_interface
-
-
-class Figure:
-    """base class for counter handling"""
-
-
-class Relationship(Figure):
-    """a relation ship from an object in the diagram to another
-    """
-
-    def __init__(self, from_object, to_object, relation_type, name=None):
-        Figure.__init__(self)
-        self.from_object = from_object
-        self.to_object = to_object
-        self.type = relation_type
-        self.name = name
-
-
-class DiagramEntity(Figure):
-    """a diagram object, i.e. a label associated to an astroid node
-    """
-
-    def __init__(self, title="No name", node=None):
-        Figure.__init__(self)
-        self.title = title
-        self.node = node
-
-
-class ClassDiagram(Figure, FilterMixIn):
-    """main class diagram handling
-    """
-
-    TYPE = "class"
-
-    def __init__(self, title, mode):
-        FilterMixIn.__init__(self, mode)
-        Figure.__init__(self)
-        self.title = title
-        self.objects = []
-        self.relationships = {}
-        self._nodes = {}
-        self.depends = []
-
-    def get_relationships(self, role):
-        # sorted to get predictable (hence testable) results
-        return sorted(
-            self.relationships.get(role, ()),
-            key=lambda x: (x.from_object.fig_id, x.to_object.fig_id),
-        )
-
-    def add_relationship(self, from_object, to_object, relation_type, name=None):
-        """create a relation ship
-        """
-        rel = Relationship(from_object, to_object, relation_type, name)
-        self.relationships.setdefault(relation_type, []).append(rel)
-
-    def get_relationship(self, from_object, relation_type):
-        """return a relation ship or None
-        """
-        for rel in self.relationships.get(relation_type, ()):
-            if rel.from_object is from_object:
-                return rel
-        raise KeyError(relation_type)
-
-    def get_attrs(self, node):
-        """return visible attributes, possibly with class name"""
-        attrs = []
-        properties = [
-            (n, m)
-            for n, m in node.items()
-            if isinstance(m, astroid.FunctionDef) and decorated_with_property(m)
-        ]
-        for node_name, associated_nodes in (
-            list(node.instance_attrs_type.items())
-            + list(node.locals_type.items())
-            + properties
-        ):
-            if not self.show_attr(node_name):
-                continue
-            names = self.class_names(associated_nodes)
-            if names:
-                node_name = "%s : %s" % (node_name, ", ".join(names))
-            attrs.append(node_name)
-        return sorted(attrs)
-
-    def get_methods(self, node):
-        """return visible methods"""
-        methods = [
-            m
-            for m in node.values()
-            if isinstance(m, astroid.FunctionDef)
-            and not decorated_with_property(m)
-            and self.show_attr(m.name)
-        ]
-        return sorted(methods, key=lambda n: n.name)
-
-    def add_object(self, title, node):
-        """create a diagram object
-        """
-        assert node not in self._nodes
-        ent = DiagramEntity(title, node)
-        self._nodes[node] = ent
-        self.objects.append(ent)
-
-    def class_names(self, nodes):
-        """return class names if needed in diagram"""
-        names = []
-        for node in nodes:
-            if isinstance(node, astroid.Instance):
-                node = node._proxied
-            if (
-                isinstance(node, astroid.ClassDef)
-                and hasattr(node, "name")
-                and not self.has_node(node)
-            ):
-                if node.name not in names:
-                    node_name = node.name
-                    names.append(node_name)
-        return names
-
-    def nodes(self):
-        """return the list of underlying nodes
-        """
-        return self._nodes.keys()
-
-    def has_node(self, node):
-        """return true if the given node is included in the diagram
-        """
-        return node in self._nodes
-
-    def object_from_node(self, node):
-        """return the diagram object mapped to node
-        """
-        return self._nodes[node]
-
-    def classes(self):
-        """return all class nodes in the diagram"""
-        return [o for o in self.objects if isinstance(o.node, astroid.ClassDef)]
-
-    def classe(self, name):
-        """return a class by its name, raise KeyError if not found
-        """
-        for klass in self.classes():
-            if klass.node.name == name:
-                return klass
-        raise KeyError(name)
-
-    def extract_relationships(self):
-        """extract relation ships between nodes in the diagram
-        """
-        for obj in self.classes():
-            node = obj.node
-            obj.attrs = self.get_attrs(node)
-            obj.methods = self.get_methods(node)
-            # shape
-            if is_interface(node):
-                obj.shape = "interface"
-            else:
-                obj.shape = "class"
-            # inheritance link
-            for par_node in node.ancestors(recurs=False):
-                try:
-                    par_obj = self.object_from_node(par_node)
-                    self.add_relationship(obj, par_obj, "specialization")
-                except KeyError:
-                    continue
-            # implements link
-            for impl_node in node.implements:
-                try:
-                    impl_obj = self.object_from_node(impl_node)
-                    self.add_relationship(obj, impl_obj, "implements")
-                except KeyError:
-                    continue
-            # associations link
-            for name, values in list(node.instance_attrs_type.items()) + list(
-                node.locals_type.items()
-            ):
-                for value in values:
-                    if value is astroid.Uninferable:
-                        continue
-                    if isinstance(value, astroid.Instance):
-                        value = value._proxied
-                    try:
-                        associated_obj = self.object_from_node(value)
-                        self.add_relationship(associated_obj, obj, "association", name)
-                    except KeyError:
-                        continue
-
-
-class PackageDiagram(ClassDiagram):
-    """package diagram handling
-    """
-
-    TYPE = "package"
-
-    def modules(self):
-        """return all module nodes in the diagram"""
-        return [o for o in self.objects if isinstance(o.node, astroid.Module)]
-
-    def module(self, name):
-        """return a module by its name, raise KeyError if not found
-        """
-        for mod in self.modules():
-            if mod.node.name == name:
-                return mod
-        raise KeyError(name)
-
-    def get_module(self, name, node):
-        """return a module by its name, looking also for relative imports;
-        raise KeyError if not found
-        """
-        for mod in self.modules():
-            mod_name = mod.node.name
-            if mod_name == name:
-                return mod
-            # search for fullname of relative import modules
-            package = node.root().name
-            if mod_name == "%s.%s" % (package, name):
-                return mod
-            if mod_name == "%s.%s" % (package.rsplit(".", 1)[0], name):
-                return mod
-        raise KeyError(name)
-
-    def add_from_depend(self, node, from_module):
-        """add dependencies created by from-imports
-        """
-        mod_name = node.root().name
-        obj = self.module(mod_name)
-        if from_module not in obj.node.depends:
-            obj.node.depends.append(from_module)
-
-    def extract_relationships(self):
-        """extract relation ships between nodes in the diagram
-        """
-        ClassDiagram.extract_relationships(self)
-        for obj in self.classes():
-            # ownership
-            try:
-                mod = self.object_from_node(obj.node.root())
-                self.add_relationship(obj, mod, "ownership")
-            except KeyError:
-                continue
-        for obj in self.modules():
-            obj.shape = "package"
-            # dependencies
-            for dep_name in obj.node.depends:
-                try:
-                    dep = self.get_module(dep_name, obj.node)
-                except KeyError:
-                    continue
-                self.add_relationship(obj, dep, "depends")
diff --git a/venv/Lib/site-packages/pylint/pyreverse/inspector.py b/venv/Lib/site-packages/pylint/pyreverse/inspector.py
deleted file mode 100644
index 702b108..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/inspector.py
+++ /dev/null
@@ -1,357 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2017 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""
-Visitor doing some postprocessing on the astroid tree.
-Try to resolve definitions (namespace) dictionary, relationship...
-"""
-import collections
-import os
-import traceback
-
-import astroid
-from astroid import bases, exceptions, manager, modutils, node_classes
-
-from pylint.pyreverse import utils
-
-
-def _iface_hdlr(_):
-    """Handler used by interfaces to handle suspicious interface nodes."""
-    return True
-
-
-def _astroid_wrapper(func, modname):
-    print("parsing %s..." % modname)
-    try:
-        return func(modname)
-    except exceptions.AstroidBuildingException as exc:
-        print(exc)
-    except Exception as exc:  # pylint: disable=broad-except
-        traceback.print_exc()
-
-
-def interfaces(node, herited=True, handler_func=_iface_hdlr):
-    """Return an iterator on interfaces implemented by the given class node."""
-    try:
-        implements = bases.Instance(node).getattr("__implements__")[0]
-    except exceptions.NotFoundError:
-        return
-    if not herited and implements.frame() is not node:
-        return
-    found = set()
-    missing = False
-    for iface in node_classes.unpack_infer(implements):
-        if iface is astroid.Uninferable:
-            missing = True
-            continue
-        if iface not in found and handler_func(iface):
-            found.add(iface)
-            yield iface
-    if missing:
-        raise exceptions.InferenceError()
-
-
-class IdGeneratorMixIn:
-    """Mixin adding the ability to generate integer uid."""
-
-    def __init__(self, start_value=0):
-        self.id_count = start_value
-
-    def init_counter(self, start_value=0):
-        """init the id counter
-        """
-        self.id_count = start_value
-
-    def generate_id(self):
-        """generate a new identifier
-        """
-        self.id_count += 1
-        return self.id_count
-
-
-class Linker(IdGeneratorMixIn, utils.LocalsVisitor):
-    """Walk on the project tree and resolve relationships.
-
-    According to options the following attributes may be
-    added to visited nodes:
-
-    * uid,
-      a unique identifier for the node (on astroid.Project, astroid.Module,
-      astroid.Class and astroid.locals_type). Only if the linker
-      has been instantiated with tag=True parameter (False by default).
-
-    * Function
-      a mapping from locals names to their bounded value, which may be a
-      constant like a string or an integer, or an astroid node
-      (on astroid.Module, astroid.Class and astroid.Function).
-
-    * instance_attrs_type
-      as locals_type but for klass member attributes (only on astroid.Class)
-
-    * implements,
-      list of implemented interface _objects_ (only on astroid.Class nodes)
-    """
-
-    def __init__(self, project, inherited_interfaces=0, tag=False):
-        IdGeneratorMixIn.__init__(self)
-        utils.LocalsVisitor.__init__(self)
-        # take inherited interface in consideration or not
-        self.inherited_interfaces = inherited_interfaces
-        # tag nodes or not
-        self.tag = tag
-        # visited project
-        self.project = project
-
-    def visit_project(self, node):
-        """visit a pyreverse.utils.Project node
-
-         * optionally tag the node with a unique id
-        """
-        if self.tag:
-            node.uid = self.generate_id()
-        for module in node.modules:
-            self.visit(module)
-
-    def visit_package(self, node):
-        """visit an astroid.Package node
-
-         * optionally tag the node with a unique id
-        """
-        if self.tag:
-            node.uid = self.generate_id()
-        for subelmt in node.values():
-            self.visit(subelmt)
-
-    def visit_module(self, node):
-        """visit an astroid.Module node
-
-         * set the locals_type mapping
-         * set the depends mapping
-         * optionally tag the node with a unique id
-        """
-        if hasattr(node, "locals_type"):
-            return
-        node.locals_type = collections.defaultdict(list)
-        node.depends = []
-        if self.tag:
-            node.uid = self.generate_id()
-
-    def visit_classdef(self, node):
-        """visit an astroid.Class node
-
-         * set the locals_type and instance_attrs_type mappings
-         * set the implements list and build it
-         * optionally tag the node with a unique id
-        """
-        if hasattr(node, "locals_type"):
-            return
-        node.locals_type = collections.defaultdict(list)
-        if self.tag:
-            node.uid = self.generate_id()
-        # resolve ancestors
-        for baseobj in node.ancestors(recurs=False):
-            specializations = getattr(baseobj, "specializations", [])
-            specializations.append(node)
-            baseobj.specializations = specializations
-        # resolve instance attributes
-        node.instance_attrs_type = collections.defaultdict(list)
-        for assignattrs in node.instance_attrs.values():
-            for assignattr in assignattrs:
-                self.handle_assignattr_type(assignattr, node)
-        # resolve implemented interface
-        try:
-            node.implements = list(interfaces(node, self.inherited_interfaces))
-        except astroid.InferenceError:
-            node.implements = ()
-
-    def visit_functiondef(self, node):
-        """visit an astroid.Function node
-
-         * set the locals_type mapping
-         * optionally tag the node with a unique id
-        """
-        if hasattr(node, "locals_type"):
-            return
-        node.locals_type = collections.defaultdict(list)
-        if self.tag:
-            node.uid = self.generate_id()
-
-    link_project = visit_project
-    link_module = visit_module
-    link_class = visit_classdef
-    link_function = visit_functiondef
-
-    def visit_assignname(self, node):
-        """visit an astroid.AssignName node
-
-        handle locals_type
-        """
-        # avoid double parsing done by different Linkers.visit
-        # running over the same project:
-        if hasattr(node, "_handled"):
-            return
-        node._handled = True
-        if node.name in node.frame():
-            frame = node.frame()
-        else:
-            # the name has been defined as 'global' in the frame and belongs
-            # there.
-            frame = node.root()
-        try:
-            if not hasattr(frame, "locals_type"):
-                # If the frame doesn't have a locals_type yet,
-                # it means it wasn't yet visited. Visit it now
-                # to add what's missing from it.
-                if isinstance(frame, astroid.ClassDef):
-                    self.visit_classdef(frame)
-                elif isinstance(frame, astroid.FunctionDef):
-                    self.visit_functiondef(frame)
-                else:
-                    self.visit_module(frame)
-
-            current = frame.locals_type[node.name]
-            values = set(node.infer())
-            frame.locals_type[node.name] = list(set(current) | values)
-        except astroid.InferenceError:
-            pass
-
-    @staticmethod
-    def handle_assignattr_type(node, parent):
-        """handle an astroid.assignattr node
-
-        handle instance_attrs_type
-        """
-        try:
-            values = set(node.infer())
-            current = set(parent.instance_attrs_type[node.attrname])
-            parent.instance_attrs_type[node.attrname] = list(current | values)
-        except astroid.InferenceError:
-            pass
-
-    def visit_import(self, node):
-        """visit an astroid.Import node
-
-        resolve module dependencies
-        """
-        context_file = node.root().file
-        for name in node.names:
-            relative = modutils.is_relative(name[0], context_file)
-            self._imported_module(node, name[0], relative)
-
-    def visit_importfrom(self, node):
-        """visit an astroid.ImportFrom node
-
-        resolve module dependencies
-        """
-        basename = node.modname
-        context_file = node.root().file
-        if context_file is not None:
-            relative = modutils.is_relative(basename, context_file)
-        else:
-            relative = False
-        for name in node.names:
-            if name[0] == "*":
-                continue
-            # analyze dependencies
-            fullname = "%s.%s" % (basename, name[0])
-            if fullname.find(".") > -1:
-                try:
-                    fullname = modutils.get_module_part(fullname, context_file)
-                except ImportError:
-                    continue
-            if fullname != basename:
-                self._imported_module(node, fullname, relative)
-
-    def compute_module(self, context_name, mod_path):
-        """return true if the module should be added to dependencies"""
-        package_dir = os.path.dirname(self.project.path)
-        if context_name == mod_path:
-            return 0
-        if modutils.is_standard_module(mod_path, (package_dir,)):
-            return 1
-        return 0
-
-    def _imported_module(self, node, mod_path, relative):
-        """Notify an imported module, used to analyze dependencies"""
-        module = node.root()
-        context_name = module.name
-        if relative:
-            mod_path = "%s.%s" % (".".join(context_name.split(".")[:-1]), mod_path)
-        if self.compute_module(context_name, mod_path):
-            # handle dependencies
-            if not hasattr(module, "depends"):
-                module.depends = []
-            mod_paths = module.depends
-            if mod_path not in mod_paths:
-                mod_paths.append(mod_path)
-
-
-class Project:
-    """a project handle a set of modules / packages"""
-
-    def __init__(self, name=""):
-        self.name = name
-        self.path = None
-        self.modules = []
-        self.locals = {}
-        self.__getitem__ = self.locals.__getitem__
-        self.__iter__ = self.locals.__iter__
-        self.values = self.locals.values
-        self.keys = self.locals.keys
-        self.items = self.locals.items
-
-    def add_module(self, node):
-        self.locals[node.name] = node
-        self.modules.append(node)
-
-    def get_module(self, name):
-        return self.locals[name]
-
-    def get_children(self):
-        return self.modules
-
-    def __repr__(self):
-        return "<Project %r at %s (%s modules)>" % (
-            self.name,
-            id(self),
-            len(self.modules),
-        )
-
-
-def project_from_files(
-    files, func_wrapper=_astroid_wrapper, project_name="no name", black_list=("CVS",)
-):
-    """return a Project from a list of files or modules"""
-    # build the project representation
-    astroid_manager = manager.AstroidManager()
-    project = Project(project_name)
-    for something in files:
-        if not os.path.exists(something):
-            fpath = modutils.file_from_modpath(something.split("."))
-        elif os.path.isdir(something):
-            fpath = os.path.join(something, "__init__.py")
-        else:
-            fpath = something
-        ast = func_wrapper(astroid_manager.ast_from_file, fpath)
-        if ast is None:
-            continue
-        project.path = project.path or ast.file
-        project.add_module(ast)
-        base_name = ast.name
-        # recurse in package except if __init__ was explicitly given
-        if ast.package and something.find("__init__") == -1:
-            # recurse on others packages / modules if this is a package
-            for fpath in modutils.get_module_files(
-                os.path.dirname(ast.file), black_list
-            ):
-                ast = func_wrapper(astroid_manager.ast_from_file, fpath)
-                if ast is None or ast.name == base_name:
-                    continue
-                project.add_module(ast)
-    return project
diff --git a/venv/Lib/site-packages/pylint/pyreverse/main.py b/venv/Lib/site-packages/pylint/pyreverse/main.py
deleted file mode 100644
index 652b954..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/main.py
+++ /dev/null
@@ -1,214 +0,0 @@
-# Copyright (c) 2008-2010, 2012-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Alexander Pervakov <frost.nzcr4@jagmort.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""
-  %prog [options] <packages>
-
-  create UML diagrams for classes and modules in <packages>
-"""
-import os
-import subprocess
-import sys
-
-from pylint.config import ConfigurationMixIn
-from pylint.pyreverse import writer
-from pylint.pyreverse.diadefslib import DiadefsHandler
-from pylint.pyreverse.inspector import Linker, project_from_files
-from pylint.pyreverse.utils import insert_default_options
-
-OPTIONS = (
-    (
-        "filter-mode",
-        dict(
-            short="f",
-            default="PUB_ONLY",
-            dest="mode",
-            type="string",
-            action="store",
-            metavar="<mode>",
-            help="""filter attributes and functions according to
-    <mode>. Correct modes are :
-                            'PUB_ONLY' filter all non public attributes
-                                [DEFAULT], equivalent to PRIVATE+SPECIAL_A
-                            'ALL' no filter
-                            'SPECIAL' filter Python special functions
-                                except constructor
-                            'OTHER' filter protected and private
-                                attributes""",
-        ),
-    ),
-    (
-        "class",
-        dict(
-            short="c",
-            action="append",
-            metavar="<class>",
-            dest="classes",
-            default=[],
-            help="create a class diagram with all classes related to <class>;\
- this uses by default the options -ASmy",
-        ),
-    ),
-    (
-        "show-ancestors",
-        dict(
-            short="a",
-            action="store",
-            metavar="<ancestor>",
-            type="int",
-            help="show <ancestor> generations of ancestor classes not in <projects>",
-        ),
-    ),
-    (
-        "all-ancestors",
-        dict(
-            short="A",
-            default=None,
-            help="show all ancestors off all classes in <projects>",
-        ),
-    ),
-    (
-        "show-associated",
-        dict(
-            short="s",
-            action="store",
-            metavar="<association_level>",
-            type="int",
-            help="show <association_level> levels of associated classes not in <projects>",
-        ),
-    ),
-    (
-        "all-associated",
-        dict(
-            short="S",
-            default=None,
-            help="show recursively all associated off all associated classes",
-        ),
-    ),
-    (
-        "show-builtin",
-        dict(
-            short="b",
-            action="store_true",
-            default=False,
-            help="include builtin objects in representation of classes",
-        ),
-    ),
-    (
-        "module-names",
-        dict(
-            short="m",
-            default=None,
-            type="yn",
-            metavar="[yn]",
-            help="include module name in representation of classes",
-        ),
-    ),
-    (
-        "only-classnames",
-        dict(
-            short="k",
-            action="store_true",
-            default=False,
-            help="don't show attributes and methods in the class boxes; \
-this disables -f values",
-        ),
-    ),
-    (
-        "output",
-        dict(
-            short="o",
-            dest="output_format",
-            action="store",
-            default="dot",
-            metavar="<format>",
-            help="create a *.<format> output file if format available.",
-        ),
-    ),
-    (
-        "ignore",
-        {
-            "type": "csv",
-            "metavar": "<file[,file...]>",
-            "dest": "black_list",
-            "default": ("CVS",),
-            "help": "Add files or directories to the blacklist. They "
-            "should be base names, not paths.",
-        },
-    ),
-    (
-        "project",
-        {
-            "default": "",
-            "type": "string",
-            "short": "p",
-            "metavar": "<project name>",
-            "help": "set the project name.",
-        },
-    ),
-)
-
-
-def _check_graphviz_available(output_format):
-    """check if we need graphviz for different output format"""
-    try:
-        subprocess.call(["dot", "-V"], stdout=subprocess.PIPE, stderr=subprocess.PIPE)
-    except OSError:
-        print(
-            "The output format '%s' is currently not available.\n"
-            "Please install 'Graphviz' to have other output formats "
-            "than 'dot' or 'vcg'." % output_format
-        )
-        sys.exit(32)
-
-
-class Run(ConfigurationMixIn):
-    """base class providing common behaviour for pyreverse commands"""
-
-    options = OPTIONS  # type: ignore
-
-    def __init__(self, args):
-        ConfigurationMixIn.__init__(self, usage=__doc__)
-        insert_default_options()
-        args = self.load_command_line_configuration()
-        if self.config.output_format not in ("dot", "vcg"):
-            _check_graphviz_available(self.config.output_format)
-
-        sys.exit(self.run(args))
-
-    def run(self, args):
-        """checking arguments and run project"""
-        if not args:
-            print(self.help())
-            return 1
-        # insert current working directory to the python path to recognize
-        # dependencies to local modules even if cwd is not in the PYTHONPATH
-        sys.path.insert(0, os.getcwd())
-        try:
-            project = project_from_files(
-                args,
-                project_name=self.config.project,
-                black_list=self.config.black_list,
-            )
-            linker = Linker(project, tag=True)
-            handler = DiadefsHandler(self.config)
-            diadefs = handler.get_diadefs(project, linker)
-        finally:
-            sys.path.pop(0)
-
-        if self.config.output_format == "vcg":
-            writer.VCGWriter(self.config).write(diadefs)
-        else:
-            writer.DotWriter(self.config).write(diadefs)
-        return 0
-
-
-if __name__ == "__main__":
-    Run(sys.argv[1:])
diff --git a/venv/Lib/site-packages/pylint/pyreverse/utils.py b/venv/Lib/site-packages/pylint/pyreverse/utils.py
deleted file mode 100644
index 5a1e7e2..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/utils.py
+++ /dev/null
@@ -1,220 +0,0 @@
-# Copyright (c) 2006, 2008, 2010, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2017 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""
-generic classes/functions for pyreverse core/extensions
-"""
-import os
-import re
-import sys
-
-########### pyreverse option utils ##############################
-
-
-RCFILE = ".pyreverserc"
-
-
-def get_default_options():
-    """
-    Read config file and return list of options
-    """
-    options = []
-    home = os.environ.get("HOME", "")
-    if home:
-        rcfile = os.path.join(home, RCFILE)
-        try:
-            options = open(rcfile).read().split()
-        except IOError:
-            pass  # ignore if no config file found
-    return options
-
-
-def insert_default_options():
-    """insert default options to sys.argv
-    """
-    options = get_default_options()
-    options.reverse()
-    for arg in options:
-        sys.argv.insert(1, arg)
-
-
-# astroid utilities ###########################################################
-
-SPECIAL = re.compile("^__[A-Za-z0-9]+[A-Za-z0-9_]*__$")
-PRIVATE = re.compile("^__[_A-Za-z0-9]*[A-Za-z0-9]+_?$")
-PROTECTED = re.compile("^_[_A-Za-z0-9]*$")
-
-
-def get_visibility(name):
-    """return the visibility from a name: public, protected, private or special
-    """
-    if SPECIAL.match(name):
-        visibility = "special"
-    elif PRIVATE.match(name):
-        visibility = "private"
-    elif PROTECTED.match(name):
-        visibility = "protected"
-
-    else:
-        visibility = "public"
-    return visibility
-
-
-ABSTRACT = re.compile("^.*Abstract.*")
-FINAL = re.compile("^[A-Z_]*$")
-
-
-def is_abstract(node):
-    """return true if the given class node correspond to an abstract class
-    definition
-    """
-    return ABSTRACT.match(node.name)
-
-
-def is_final(node):
-    """return true if the given class/function node correspond to final
-    definition
-    """
-    return FINAL.match(node.name)
-
-
-def is_interface(node):
-    # bw compat
-    return node.type == "interface"
-
-
-def is_exception(node):
-    # bw compat
-    return node.type == "exception"
-
-
-# Helpers #####################################################################
-
-_CONSTRUCTOR = 1
-_SPECIAL = 2
-_PROTECTED = 4
-_PRIVATE = 8
-MODES = {
-    "ALL": 0,
-    "PUB_ONLY": _SPECIAL + _PROTECTED + _PRIVATE,
-    "SPECIAL": _SPECIAL,
-    "OTHER": _PROTECTED + _PRIVATE,
-}
-VIS_MOD = {
-    "special": _SPECIAL,
-    "protected": _PROTECTED,
-    "private": _PRIVATE,
-    "public": 0,
-}
-
-
-class FilterMixIn:
-    """filter nodes according to a mode and nodes' visibility
-    """
-
-    def __init__(self, mode):
-        "init filter modes"
-        __mode = 0
-        for nummod in mode.split("+"):
-            try:
-                __mode += MODES[nummod]
-            except KeyError as ex:
-                print("Unknown filter mode %s" % ex, file=sys.stderr)
-        self.__mode = __mode
-
-    def show_attr(self, node):
-        """return true if the node should be treated
-        """
-        visibility = get_visibility(getattr(node, "name", node))
-        return not self.__mode & VIS_MOD[visibility]
-
-
-class ASTWalker:
-    """a walker visiting a tree in preorder, calling on the handler:
-
-    * visit_<class name> on entering a node, where class name is the class of
-    the node in lower case
-
-    * leave_<class name> on leaving a node, where class name is the class of
-    the node in lower case
-    """
-
-    def __init__(self, handler):
-        self.handler = handler
-        self._cache = {}
-
-    def walk(self, node, _done=None):
-        """walk on the tree from <node>, getting callbacks from handler"""
-        if _done is None:
-            _done = set()
-        if node in _done:
-            raise AssertionError((id(node), node, node.parent))
-        _done.add(node)
-        self.visit(node)
-        for child_node in node.get_children():
-            assert child_node is not node
-            self.walk(child_node, _done)
-        self.leave(node)
-        assert node.parent is not node
-
-    def get_callbacks(self, node):
-        """get callbacks from handler for the visited node"""
-        klass = node.__class__
-        methods = self._cache.get(klass)
-        if methods is None:
-            handler = self.handler
-            kid = klass.__name__.lower()
-            e_method = getattr(
-                handler, "visit_%s" % kid, getattr(handler, "visit_default", None)
-            )
-            l_method = getattr(
-                handler, "leave_%s" % kid, getattr(handler, "leave_default", None)
-            )
-            self._cache[klass] = (e_method, l_method)
-        else:
-            e_method, l_method = methods
-        return e_method, l_method
-
-    def visit(self, node):
-        """walk on the tree from <node>, getting callbacks from handler"""
-        method = self.get_callbacks(node)[0]
-        if method is not None:
-            method(node)
-
-    def leave(self, node):
-        """walk on the tree from <node>, getting callbacks from handler"""
-        method = self.get_callbacks(node)[1]
-        if method is not None:
-            method(node)
-
-
-class LocalsVisitor(ASTWalker):
-    """visit a project by traversing the locals dictionary"""
-
-    def __init__(self):
-        ASTWalker.__init__(self, self)
-        self._visited = set()
-
-    def visit(self, node):
-        """launch the visit starting from the given node"""
-        if node in self._visited:
-            return None
-
-        self._visited.add(node)
-        methods = self.get_callbacks(node)
-        if methods[0] is not None:
-            methods[0](node)
-        if hasattr(node, "locals"):  # skip Instance and other proxy
-            for local_node in node.values():
-                self.visit(local_node)
-        if methods[1] is not None:
-            return methods[1](node)
-        return None
diff --git a/venv/Lib/site-packages/pylint/pyreverse/vcgutils.py b/venv/Lib/site-packages/pylint/pyreverse/vcgutils.py
deleted file mode 100644
index 89c6911..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/vcgutils.py
+++ /dev/null
@@ -1,229 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Functions to generate files readable with Georg Sander's vcg
-(Visualization of Compiler Graphs).
-
-You can download vcg at http://rw4.cs.uni-sb.de/~sander/html/gshome.html
-Note that vcg exists as a debian package.
-
-See vcg's documentation for explanation about the different values that
-maybe used for the functions parameters.
-"""
-
-ATTRS_VAL = {
-    "algos": (
-        "dfs",
-        "tree",
-        "minbackward",
-        "left_to_right",
-        "right_to_left",
-        "top_to_bottom",
-        "bottom_to_top",
-        "maxdepth",
-        "maxdepthslow",
-        "mindepth",
-        "mindepthslow",
-        "mindegree",
-        "minindegree",
-        "minoutdegree",
-        "maxdegree",
-        "maxindegree",
-        "maxoutdegree",
-    ),
-    "booleans": ("yes", "no"),
-    "colors": (
-        "black",
-        "white",
-        "blue",
-        "red",
-        "green",
-        "yellow",
-        "magenta",
-        "lightgrey",
-        "cyan",
-        "darkgrey",
-        "darkblue",
-        "darkred",
-        "darkgreen",
-        "darkyellow",
-        "darkmagenta",
-        "darkcyan",
-        "gold",
-        "lightblue",
-        "lightred",
-        "lightgreen",
-        "lightyellow",
-        "lightmagenta",
-        "lightcyan",
-        "lilac",
-        "turquoise",
-        "aquamarine",
-        "khaki",
-        "purple",
-        "yellowgreen",
-        "pink",
-        "orange",
-        "orchid",
-    ),
-    "shapes": ("box", "ellipse", "rhomb", "triangle"),
-    "textmodes": ("center", "left_justify", "right_justify"),
-    "arrowstyles": ("solid", "line", "none"),
-    "linestyles": ("continuous", "dashed", "dotted", "invisible"),
-}
-
-# meaning of possible values:
-#   O    -> string
-#   1    -> int
-#   list -> value in list
-GRAPH_ATTRS = {
-    "title": 0,
-    "label": 0,
-    "color": ATTRS_VAL["colors"],
-    "textcolor": ATTRS_VAL["colors"],
-    "bordercolor": ATTRS_VAL["colors"],
-    "width": 1,
-    "height": 1,
-    "borderwidth": 1,
-    "textmode": ATTRS_VAL["textmodes"],
-    "shape": ATTRS_VAL["shapes"],
-    "shrink": 1,
-    "stretch": 1,
-    "orientation": ATTRS_VAL["algos"],
-    "vertical_order": 1,
-    "horizontal_order": 1,
-    "xspace": 1,
-    "yspace": 1,
-    "layoutalgorithm": ATTRS_VAL["algos"],
-    "late_edge_labels": ATTRS_VAL["booleans"],
-    "display_edge_labels": ATTRS_VAL["booleans"],
-    "dirty_edge_labels": ATTRS_VAL["booleans"],
-    "finetuning": ATTRS_VAL["booleans"],
-    "manhattan_edges": ATTRS_VAL["booleans"],
-    "smanhattan_edges": ATTRS_VAL["booleans"],
-    "port_sharing": ATTRS_VAL["booleans"],
-    "edges": ATTRS_VAL["booleans"],
-    "nodes": ATTRS_VAL["booleans"],
-    "splines": ATTRS_VAL["booleans"],
-}
-NODE_ATTRS = {
-    "title": 0,
-    "label": 0,
-    "color": ATTRS_VAL["colors"],
-    "textcolor": ATTRS_VAL["colors"],
-    "bordercolor": ATTRS_VAL["colors"],
-    "width": 1,
-    "height": 1,
-    "borderwidth": 1,
-    "textmode": ATTRS_VAL["textmodes"],
-    "shape": ATTRS_VAL["shapes"],
-    "shrink": 1,
-    "stretch": 1,
-    "vertical_order": 1,
-    "horizontal_order": 1,
-}
-EDGE_ATTRS = {
-    "sourcename": 0,
-    "targetname": 0,
-    "label": 0,
-    "linestyle": ATTRS_VAL["linestyles"],
-    "class": 1,
-    "thickness": 0,
-    "color": ATTRS_VAL["colors"],
-    "textcolor": ATTRS_VAL["colors"],
-    "arrowcolor": ATTRS_VAL["colors"],
-    "backarrowcolor": ATTRS_VAL["colors"],
-    "arrowsize": 1,
-    "backarrowsize": 1,
-    "arrowstyle": ATTRS_VAL["arrowstyles"],
-    "backarrowstyle": ATTRS_VAL["arrowstyles"],
-    "textmode": ATTRS_VAL["textmodes"],
-    "priority": 1,
-    "anchor": 1,
-    "horizontal_order": 1,
-}
-
-
-# Misc utilities ###############################################################
-
-
-class VCGPrinter:
-    """A vcg graph writer.
-    """
-
-    def __init__(self, output_stream):
-        self._stream = output_stream
-        self._indent = ""
-
-    def open_graph(self, **args):
-        """open a vcg graph
-        """
-        self._stream.write("%sgraph:{\n" % self._indent)
-        self._inc_indent()
-        self._write_attributes(GRAPH_ATTRS, **args)
-
-    def close_graph(self):
-        """close a vcg graph
-        """
-        self._dec_indent()
-        self._stream.write("%s}\n" % self._indent)
-
-    def node(self, title, **args):
-        """draw a node
-        """
-        self._stream.write('%snode: {title:"%s"' % (self._indent, title))
-        self._write_attributes(NODE_ATTRS, **args)
-        self._stream.write("}\n")
-
-    def edge(self, from_node, to_node, edge_type="", **args):
-        """draw an edge from a node to another.
-        """
-        self._stream.write(
-            '%s%sedge: {sourcename:"%s" targetname:"%s"'
-            % (self._indent, edge_type, from_node, to_node)
-        )
-        self._write_attributes(EDGE_ATTRS, **args)
-        self._stream.write("}\n")
-
-    # private ##################################################################
-
-    def _write_attributes(self, attributes_dict, **args):
-        """write graph, node or edge attributes
-        """
-        for key, value in args.items():
-            try:
-                _type = attributes_dict[key]
-            except KeyError:
-                raise Exception(
-                    """no such attribute %s
-possible attributes are %s"""
-                    % (key, attributes_dict.keys())
-                )
-
-            if not _type:
-                self._stream.write('%s%s:"%s"\n' % (self._indent, key, value))
-            elif _type == 1:
-                self._stream.write("%s%s:%s\n" % (self._indent, key, int(value)))
-            elif value in _type:
-                self._stream.write("%s%s:%s\n" % (self._indent, key, value))
-            else:
-                raise Exception(
-                    """value %s isn\'t correct for attribute %s
-correct values are %s"""
-                    % (value, key, _type)
-                )
-
-    def _inc_indent(self):
-        """increment indentation
-        """
-        self._indent = "  %s" % self._indent
-
-    def _dec_indent(self):
-        """decrement indentation
-        """
-        self._indent = self._indent[:-2]
diff --git a/venv/Lib/site-packages/pylint/pyreverse/writer.py b/venv/Lib/site-packages/pylint/pyreverse/writer.py
deleted file mode 100644
index 609b1ef..0000000
--- a/venv/Lib/site-packages/pylint/pyreverse/writer.py
+++ /dev/null
@@ -1,213 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2008-2010, 2013-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Mike Frysinger <vapier@gentoo.org>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Utilities for creating VCG and Dot diagrams"""
-
-from pylint.graph import DotBackend
-from pylint.pyreverse.utils import is_exception
-from pylint.pyreverse.vcgutils import VCGPrinter
-
-
-class DiagramWriter:
-    """base class for writing project diagrams
-    """
-
-    def __init__(self, config, styles):
-        self.config = config
-        self.pkg_edges, self.inh_edges, self.imp_edges, self.association_edges = styles
-        self.printer = None  # defined in set_printer
-
-    def write(self, diadefs):
-        """write files for <project> according to <diadefs>
-        """
-        for diagram in diadefs:
-            basename = diagram.title.strip().replace(" ", "_")
-            file_name = "%s.%s" % (basename, self.config.output_format)
-            self.set_printer(file_name, basename)
-            if diagram.TYPE == "class":
-                self.write_classes(diagram)
-            else:
-                self.write_packages(diagram)
-            self.close_graph()
-
-    def write_packages(self, diagram):
-        """write a package diagram"""
-        # sorted to get predictable (hence testable) results
-        for i, obj in enumerate(sorted(diagram.modules(), key=lambda x: x.title)):
-            self.printer.emit_node(i, label=self.get_title(obj), shape="box")
-            obj.fig_id = i
-        # package dependencies
-        for rel in diagram.get_relationships("depends"):
-            self.printer.emit_edge(
-                rel.from_object.fig_id, rel.to_object.fig_id, **self.pkg_edges
-            )
-
-    def write_classes(self, diagram):
-        """write a class diagram"""
-        # sorted to get predictable (hence testable) results
-        for i, obj in enumerate(sorted(diagram.objects, key=lambda x: x.title)):
-            self.printer.emit_node(i, **self.get_values(obj))
-            obj.fig_id = i
-        # inheritance links
-        for rel in diagram.get_relationships("specialization"):
-            self.printer.emit_edge(
-                rel.from_object.fig_id, rel.to_object.fig_id, **self.inh_edges
-            )
-        # implementation links
-        for rel in diagram.get_relationships("implements"):
-            self.printer.emit_edge(
-                rel.from_object.fig_id, rel.to_object.fig_id, **self.imp_edges
-            )
-        # generate associations
-        for rel in diagram.get_relationships("association"):
-            self.printer.emit_edge(
-                rel.from_object.fig_id,
-                rel.to_object.fig_id,
-                label=rel.name,
-                **self.association_edges
-            )
-
-    def set_printer(self, file_name, basename):
-        """set printer"""
-        raise NotImplementedError
-
-    def get_title(self, obj):
-        """get project title"""
-        raise NotImplementedError
-
-    def get_values(self, obj):
-        """get label and shape for classes."""
-        raise NotImplementedError
-
-    def close_graph(self):
-        """finalize the graph"""
-        raise NotImplementedError
-
-
-class DotWriter(DiagramWriter):
-    """write dot graphs from a diagram definition and a project
-    """
-
-    def __init__(self, config):
-        styles = [
-            dict(arrowtail="none", arrowhead="open"),
-            dict(arrowtail="none", arrowhead="empty"),
-            dict(arrowtail="node", arrowhead="empty", style="dashed"),
-            dict(
-                fontcolor="green", arrowtail="none", arrowhead="diamond", style="solid"
-            ),
-        ]
-        DiagramWriter.__init__(self, config, styles)
-
-    def set_printer(self, file_name, basename):
-        """initialize DotWriter and add options for layout.
-        """
-        layout = dict(rankdir="BT")
-        self.printer = DotBackend(basename, additional_param=layout)
-        self.file_name = file_name
-
-    def get_title(self, obj):
-        """get project title"""
-        return obj.title
-
-    def get_values(self, obj):
-        """get label and shape for classes.
-
-        The label contains all attributes and methods
-        """
-        label = obj.title
-        if obj.shape == "interface":
-            label = "«interface»\\n%s" % label
-        if not self.config.only_classnames:
-            label = r"%s|%s\l|" % (label, r"\l".join(obj.attrs))
-            for func in obj.methods:
-                args = [arg.name for arg in func.args.args if arg.name != "self"]
-                label = r"%s%s(%s)\l" % (label, func.name, ", ".join(args))
-            label = "{%s}" % label
-        if is_exception(obj.node):
-            return dict(fontcolor="red", label=label, shape="record")
-        return dict(label=label, shape="record")
-
-    def close_graph(self):
-        """print the dot graph into <file_name>"""
-        self.printer.generate(self.file_name)
-
-
-class VCGWriter(DiagramWriter):
-    """write vcg graphs from a diagram definition and a project
-    """
-
-    def __init__(self, config):
-        styles = [
-            dict(arrowstyle="solid", backarrowstyle="none", backarrowsize=0),
-            dict(arrowstyle="solid", backarrowstyle="none", backarrowsize=10),
-            dict(
-                arrowstyle="solid",
-                backarrowstyle="none",
-                linestyle="dotted",
-                backarrowsize=10,
-            ),
-            dict(arrowstyle="solid", backarrowstyle="none", textcolor="green"),
-        ]
-        DiagramWriter.__init__(self, config, styles)
-
-    def set_printer(self, file_name, basename):
-        """initialize VCGWriter for a UML graph"""
-        self.graph_file = open(file_name, "w+")
-        self.printer = VCGPrinter(self.graph_file)
-        self.printer.open_graph(
-            title=basename,
-            layoutalgorithm="dfs",
-            late_edge_labels="yes",
-            port_sharing="no",
-            manhattan_edges="yes",
-        )
-        self.printer.emit_node = self.printer.node
-        self.printer.emit_edge = self.printer.edge
-
-    def get_title(self, obj):
-        """get project title in vcg format"""
-        return r"\fb%s\fn" % obj.title
-
-    def get_values(self, obj):
-        """get label and shape for classes.
-
-        The label contains all attributes and methods
-        """
-        if is_exception(obj.node):
-            label = r"\fb\f09%s\fn" % obj.title
-        else:
-            label = r"\fb%s\fn" % obj.title
-        if obj.shape == "interface":
-            shape = "ellipse"
-        else:
-            shape = "box"
-        if not self.config.only_classnames:
-            attrs = obj.attrs
-            methods = [func.name for func in obj.methods]
-            # box width for UML like diagram
-            maxlen = max(len(name) for name in [obj.title] + methods + attrs)
-            line = "_" * (maxlen + 2)
-            label = r"%s\n\f%s" % (label, line)
-            for attr in attrs:
-                label = r"%s\n\f08%s" % (label, attr)
-            if attrs:
-                label = r"%s\n\f%s" % (label, line)
-            for func in methods:
-                label = r"%s\n\f10%s()" % (label, func)
-        return dict(label=label, shape=shape)
-
-    def close_graph(self):
-        """close graph and file"""
-        self.printer.close_graph()
-        self.graph_file.close()
diff --git a/venv/Lib/site-packages/pylint/reporters/__init__.py b/venv/Lib/site-packages/pylint/reporters/__init__.py
deleted file mode 100644
index f01629b..0000000
--- a/venv/Lib/site-packages/pylint/reporters/__init__.py
+++ /dev/null
@@ -1,34 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006, 2010, 2012-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2014-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Ricardo Gemignani <ricardo.gemignani@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Simu Toni <simutoni@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2017 Kári Tristan Helgason <kthelgason@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Ville Skyttä <ville.skytta@upcloud.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""utilities methods and classes for reporters"""
-
-
-from pylint import utils
-from pylint.reporters.base_reporter import BaseReporter
-from pylint.reporters.collecting_reporter import CollectingReporter
-from pylint.reporters.json_reporter import JSONReporter
-from pylint.reporters.reports_handler_mix_in import ReportsHandlerMixIn
-
-
-def initialize(linter):
-    """initialize linter with reporters in this package """
-    utils.register_plugins(linter, __path__[0])
-
-
-__all__ = ["BaseReporter", "ReportsHandlerMixIn", "JSONReporter", "CollectingReporter"]
diff --git a/venv/Lib/site-packages/pylint/reporters/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index a1b55a7..0000000
--- a/venv/Lib/site-packages/pylint/reporters/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/__pycache__/base_reporter.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/__pycache__/base_reporter.cpython-37.pyc
deleted file mode 100644
index 5f35295..0000000
--- a/venv/Lib/site-packages/pylint/reporters/__pycache__/base_reporter.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/__pycache__/collecting_reporter.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/__pycache__/collecting_reporter.cpython-37.pyc
deleted file mode 100644
index 066140c..0000000
--- a/venv/Lib/site-packages/pylint/reporters/__pycache__/collecting_reporter.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/__pycache__/json_reporter.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/__pycache__/json_reporter.cpython-37.pyc
deleted file mode 100644
index ca871c3..0000000
--- a/venv/Lib/site-packages/pylint/reporters/__pycache__/json_reporter.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/__pycache__/reports_handler_mix_in.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/__pycache__/reports_handler_mix_in.cpython-37.pyc
deleted file mode 100644
index 8269f35..0000000
--- a/venv/Lib/site-packages/pylint/reporters/__pycache__/reports_handler_mix_in.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/__pycache__/text.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/__pycache__/text.cpython-37.pyc
deleted file mode 100644
index f40cc5e..0000000
--- a/venv/Lib/site-packages/pylint/reporters/__pycache__/text.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/base_reporter.py b/venv/Lib/site-packages/pylint/reporters/base_reporter.py
deleted file mode 100644
index 1003eeb..0000000
--- a/venv/Lib/site-packages/pylint/reporters/base_reporter.py
+++ /dev/null
@@ -1,66 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import os
-import sys
-
-
-class BaseReporter:
-    """base class for reporters
-
-    symbols: show short symbolic names for messages.
-    """
-
-    extension = ""
-
-    def __init__(self, output=None):
-        self.linter = None
-        self.section = 0
-        self.out = None
-        self.out_encoding = None
-        self.set_output(output)
-        # Build the path prefix to strip to get relative paths
-        self.path_strip_prefix = os.getcwd() + os.sep
-
-    def handle_message(self, msg):
-        """Handle a new message triggered on the current file."""
-
-    def set_output(self, output=None):
-        """set output stream"""
-        self.out = output or sys.stdout
-
-    def writeln(self, string=""):
-        """write a line in the output buffer"""
-        print(string, file=self.out)
-
-    def display_reports(self, layout):
-        """display results encapsulated in the layout tree"""
-        self.section = 0
-        if hasattr(layout, "report_id"):
-            layout.children[0].children[0].data += " (%s)" % layout.report_id
-        self._display(layout)
-
-    def _display(self, layout):
-        """display the layout"""
-        raise NotImplementedError()
-
-    def display_messages(self, layout):
-        """Hook for displaying the messages of the reporter
-
-        This will be called whenever the underlying messages
-        needs to be displayed. For some reporters, it probably
-        doesn't make sense to display messages as soon as they
-        are available, so some mechanism of storing them could be used.
-        This method can be implemented to display them after they've
-        been aggregated.
-        """
-
-    # Event callbacks
-
-    def on_set_current_module(self, module, filepath):
-        """Hook called when a module starts to be analysed."""
-
-    def on_close(self, stats, previous_stats):
-        """Hook called when a module finished analyzing."""
diff --git a/venv/Lib/site-packages/pylint/reporters/collecting_reporter.py b/venv/Lib/site-packages/pylint/reporters/collecting_reporter.py
deleted file mode 100644
index 7798d83..0000000
--- a/venv/Lib/site-packages/pylint/reporters/collecting_reporter.py
+++ /dev/null
@@ -1,21 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-from pylint.reporters.base_reporter import BaseReporter
-
-
-class CollectingReporter(BaseReporter):
-    """collects messages"""
-
-    name = "collector"
-
-    def __init__(self):
-        BaseReporter.__init__(self)
-        self.messages = []
-
-    def handle_message(self, msg):
-        self.messages.append(msg)
-
-    _display = None
diff --git a/venv/Lib/site-packages/pylint/reporters/json_reporter.py b/venv/Lib/site-packages/pylint/reporters/json_reporter.py
deleted file mode 100644
index fa6a0f8..0000000
--- a/venv/Lib/site-packages/pylint/reporters/json_reporter.py
+++ /dev/null
@@ -1,58 +0,0 @@
-# Copyright (c) 2014 Vlad Temian <vladtemian@gmail.com>
-# Copyright (c) 2015-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2017 guillaume2 <guillaume.peillex@gmail.col>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""JSON reporter"""
-import html
-import json
-import sys
-
-from pylint.interfaces import IReporter
-from pylint.reporters.base_reporter import BaseReporter
-
-
-class JSONReporter(BaseReporter):
-    """Report messages and layouts in JSON."""
-
-    __implements__ = IReporter
-    name = "json"
-    extension = "json"
-
-    def __init__(self, output=sys.stdout):
-        BaseReporter.__init__(self, output)
-        self.messages = []
-
-    def handle_message(self, msg):
-        """Manage message of different type and in the context of path."""
-        self.messages.append(
-            {
-                "type": msg.category,
-                "module": msg.module,
-                "obj": msg.obj,
-                "line": msg.line,
-                "column": msg.column,
-                "path": msg.path,
-                "symbol": msg.symbol,
-                "message": html.escape(msg.msg or "", quote=False),
-                "message-id": msg.msg_id,
-            }
-        )
-
-    def display_messages(self, layout):
-        """Launch layouts display"""
-        print(json.dumps(self.messages, indent=4), file=self.out)
-
-    def display_reports(self, layout):
-        """Don't do nothing in this reporter."""
-
-    def _display(self, layout):
-        """Do nothing."""
-
-
-def register(linter):
-    """Register the reporter classes with the linter."""
-    linter.register_reporter(JSONReporter)
diff --git a/venv/Lib/site-packages/pylint/reporters/reports_handler_mix_in.py b/venv/Lib/site-packages/pylint/reporters/reports_handler_mix_in.py
deleted file mode 100644
index 6f91a97..0000000
--- a/venv/Lib/site-packages/pylint/reporters/reports_handler_mix_in.py
+++ /dev/null
@@ -1,79 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import collections
-
-from pylint.exceptions import EmptyReportError
-from pylint.reporters.ureports.nodes import Section
-
-
-class ReportsHandlerMixIn:
-    """a mix-in class containing all the reports and stats manipulation
-    related methods for the main lint class
-    """
-
-    def __init__(self):
-        self._reports = collections.defaultdict(list)
-        self._reports_state = {}
-
-    def report_order(self):
-        """ Return a list of reports, sorted in the order
-        in which they must be called.
-        """
-        return list(self._reports)
-
-    def register_report(self, reportid, r_title, r_cb, checker):
-        """register a report
-
-        reportid is the unique identifier for the report
-        r_title the report's title
-        r_cb the method to call to make the report
-        checker is the checker defining the report
-        """
-        reportid = reportid.upper()
-        self._reports[checker].append((reportid, r_title, r_cb))
-
-    def enable_report(self, reportid):
-        """disable the report of the given id"""
-        reportid = reportid.upper()
-        self._reports_state[reportid] = True
-
-    def disable_report(self, reportid):
-        """disable the report of the given id"""
-        reportid = reportid.upper()
-        self._reports_state[reportid] = False
-
-    def report_is_enabled(self, reportid):
-        """return true if the report associated to the given identifier is
-        enabled
-        """
-        return self._reports_state.get(reportid, True)
-
-    def make_reports(self, stats, old_stats):
-        """render registered reports"""
-        sect = Section("Report", "%s statements analysed." % (self.stats["statement"]))
-        for checker in self.report_order():
-            for reportid, r_title, r_cb in self._reports[checker]:
-                if not self.report_is_enabled(reportid):
-                    continue
-                report_sect = Section(r_title)
-                try:
-                    r_cb(report_sect, stats, old_stats)
-                except EmptyReportError:
-                    continue
-                report_sect.report_id = reportid
-                sect.append(report_sect)
-        return sect
-
-    def add_stats(self, **kwargs):
-        """add some stats entries to the statistic dictionary
-        raise an AssertionError if there is a key conflict
-        """
-        for key, value in kwargs.items():
-            if key[-1] == "_":
-                key = key[:-1]
-            assert key not in self.stats
-            self.stats[key] = value
-        return self.stats
diff --git a/venv/Lib/site-packages/pylint/reporters/text.py b/venv/Lib/site-packages/pylint/reporters/text.py
deleted file mode 100644
index ce74174..0000000
--- a/venv/Lib/site-packages/pylint/reporters/text.py
+++ /dev/null
@@ -1,247 +0,0 @@
-# Copyright (c) 2006-2007, 2010-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 y2kbugger <y2kbugger@users.noreply.github.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Jace Browning <jacebrowning@gmail.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Plain text reporters:
-
-:text: the default one grouping messages by module
-:colorized: an ANSI colorized text reporter
-"""
-import os
-import sys
-import warnings
-
-from pylint import utils
-from pylint.interfaces import IReporter
-from pylint.reporters import BaseReporter
-from pylint.reporters.ureports.text_writer import TextWriter
-
-TITLE_UNDERLINES = ["", "=", "-", "."]
-
-ANSI_PREFIX = "\033["
-ANSI_END = "m"
-ANSI_RESET = "\033[0m"
-ANSI_STYLES = {
-    "reset": "0",
-    "bold": "1",
-    "italic": "3",
-    "underline": "4",
-    "blink": "5",
-    "inverse": "7",
-    "strike": "9",
-}
-ANSI_COLORS = {
-    "reset": "0",
-    "black": "30",
-    "red": "31",
-    "green": "32",
-    "yellow": "33",
-    "blue": "34",
-    "magenta": "35",
-    "cyan": "36",
-    "white": "37",
-}
-
-
-def _get_ansi_code(color=None, style=None):
-    """return ansi escape code corresponding to color and style
-
-    :type color: str or None
-    :param color:
-      the color name (see `ANSI_COLORS` for available values)
-      or the color number when 256 colors are available
-
-    :type style: str or None
-    :param style:
-      style string (see `ANSI_COLORS` for available values). To get
-      several style effects at the same time, use a coma as separator.
-
-    :raise KeyError: if an unexistent color or style identifier is given
-
-    :rtype: str
-    :return: the built escape code
-    """
-    ansi_code = []
-    if style:
-        style_attrs = utils._splitstrip(style)
-        for effect in style_attrs:
-            ansi_code.append(ANSI_STYLES[effect])
-    if color:
-        if color.isdigit():
-            ansi_code.extend(["38", "5"])
-            ansi_code.append(color)
-        else:
-            ansi_code.append(ANSI_COLORS[color])
-    if ansi_code:
-        return ANSI_PREFIX + ";".join(ansi_code) + ANSI_END
-    return ""
-
-
-def colorize_ansi(msg, color=None, style=None):
-    """colorize message by wrapping it with ansi escape codes
-
-    :type msg: str or unicode
-    :param msg: the message string to colorize
-
-    :type color: str or None
-    :param color:
-      the color identifier (see `ANSI_COLORS` for available values)
-
-    :type style: str or None
-    :param style:
-      style string (see `ANSI_COLORS` for available values). To get
-      several style effects at the same time, use a coma as separator.
-
-    :raise KeyError: if an unexistent color or style identifier is given
-
-    :rtype: str or unicode
-    :return: the ansi escaped string
-    """
-    # If both color and style are not defined, then leave the text as is
-    if color is None and style is None:
-        return msg
-    escape_code = _get_ansi_code(color, style)
-    # If invalid (or unknown) color, don't wrap msg with ansi codes
-    if escape_code:
-        return "%s%s%s" % (escape_code, msg, ANSI_RESET)
-    return msg
-
-
-class TextReporter(BaseReporter):
-    """reports messages and layouts in plain text"""
-
-    __implements__ = IReporter
-    name = "text"
-    extension = "txt"
-    line_format = "{path}:{line}:{column}: {msg_id}: {msg} ({symbol})"
-
-    def __init__(self, output=None):
-        BaseReporter.__init__(self, output)
-        self._modules = set()
-        self._template = None
-
-    def on_set_current_module(self, module, filepath):
-        self._template = str(self.linter.config.msg_template or self.line_format)
-
-    def write_message(self, msg):
-        """Convenience method to write a formated message with class default template"""
-        self.writeln(msg.format(self._template))
-
-    def handle_message(self, msg):
-        """manage message of different type and in the context of path"""
-        if msg.module not in self._modules:
-            if msg.module:
-                self.writeln("************* Module %s" % msg.module)
-                self._modules.add(msg.module)
-            else:
-                self.writeln("************* ")
-        self.write_message(msg)
-
-    def _display(self, layout):
-        """launch layouts display"""
-        print(file=self.out)
-        TextWriter().format(layout, self.out)
-
-
-class ParseableTextReporter(TextReporter):
-    """a reporter very similar to TextReporter, but display messages in a form
-    recognized by most text editors :
-
-    <filename>:<linenum>:<msg>
-    """
-
-    name = "parseable"
-    line_format = "{path}:{line}: [{msg_id}({symbol}), {obj}] {msg}"
-
-    def __init__(self, output=None):
-        warnings.warn(
-            "%s output format is deprecated. This is equivalent "
-            "to --msg-template=%s" % (self.name, self.line_format),
-            DeprecationWarning,
-        )
-        TextReporter.__init__(self, output)
-
-
-class VSTextReporter(ParseableTextReporter):
-    """Visual studio text reporter"""
-
-    name = "msvs"
-    line_format = "{path}({line}): [{msg_id}({symbol}){obj}] {msg}"
-
-
-class ColorizedTextReporter(TextReporter):
-    """Simple TextReporter that colorizes text output"""
-
-    name = "colorized"
-    COLOR_MAPPING = {
-        "I": ("green", None),
-        "C": (None, "bold"),
-        "R": ("magenta", "bold, italic"),
-        "W": ("magenta", None),
-        "E": ("red", "bold"),
-        "F": ("red", "bold, underline"),
-        "S": ("yellow", "inverse"),  # S stands for module Separator
-    }
-
-    def __init__(self, output=None, color_mapping=None):
-        TextReporter.__init__(self, output)
-        self.color_mapping = color_mapping or dict(ColorizedTextReporter.COLOR_MAPPING)
-        ansi_terms = ["xterm-16color", "xterm-256color"]
-        if os.environ.get("TERM") not in ansi_terms:
-            if sys.platform == "win32":
-                # pylint: disable=import-error,import-outside-toplevel
-                import colorama
-
-                self.out = colorama.AnsiToWin32(self.out)
-
-    def _get_decoration(self, msg_id):
-        """Returns the tuple color, style associated with msg_id as defined
-        in self.color_mapping
-        """
-        try:
-            return self.color_mapping[msg_id[0]]
-        except KeyError:
-            return None, None
-
-    def handle_message(self, msg):
-        """manage message of different types, and colorize output
-        using ansi escape codes
-        """
-        if msg.module not in self._modules:
-            color, style = self._get_decoration("S")
-            if msg.module:
-                modsep = colorize_ansi(
-                    "************* Module %s" % msg.module, color, style
-                )
-            else:
-                modsep = colorize_ansi("************* %s" % msg.module, color, style)
-            self.writeln(modsep)
-            self._modules.add(msg.module)
-        color, style = self._get_decoration(msg.C)
-
-        msg = msg._replace(
-            **{
-                attr: colorize_ansi(getattr(msg, attr), color, style)
-                for attr in ("msg", "symbol", "category", "C")
-            }
-        )
-        self.write_message(msg)
-
-
-def register(linter):
-    """Register the reporter classes with the linter."""
-    linter.register_reporter(TextReporter)
-    linter.register_reporter(ParseableTextReporter)
-    linter.register_reporter(VSTextReporter)
-    linter.register_reporter(ColorizedTextReporter)
diff --git a/venv/Lib/site-packages/pylint/reporters/ureports/__init__.py b/venv/Lib/site-packages/pylint/reporters/ureports/__init__.py
deleted file mode 100644
index 361552b..0000000
--- a/venv/Lib/site-packages/pylint/reporters/ureports/__init__.py
+++ /dev/null
@@ -1,96 +0,0 @@
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Universal report objects and some formatting drivers.
-
-A way to create simple reports using python objects, primarily designed to be
-formatted as text and html.
-"""
-import os
-import sys
-from io import StringIO
-
-
-class BaseWriter:
-    """base class for ureport writers"""
-
-    def format(self, layout, stream=None, encoding=None):
-        """format and write the given layout into the stream object
-
-        unicode policy: unicode strings may be found in the layout;
-        try to call stream.write with it, but give it back encoded using
-        the given encoding if it fails
-        """
-        if stream is None:
-            stream = sys.stdout
-        if not encoding:
-            encoding = getattr(stream, "encoding", "UTF-8")
-        self.encoding = encoding or "UTF-8"
-        self.out = stream
-        self.begin_format()
-        layout.accept(self)
-        self.end_format()
-
-    def format_children(self, layout):
-        """recurse on the layout children and call their accept method
-        (see the Visitor pattern)
-        """
-        for child in getattr(layout, "children", ()):
-            child.accept(self)
-
-    def writeln(self, string=""):
-        """write a line in the output buffer"""
-        self.write(string + os.linesep)
-
-    def write(self, string):
-        """write a string in the output buffer"""
-        self.out.write(string)
-
-    def begin_format(self):
-        """begin to format a layout"""
-        self.section = 0
-
-    def end_format(self):
-        """finished to format a layout"""
-
-    def get_table_content(self, table):
-        """trick to get table content without actually writing it
-
-        return an aligned list of lists containing table cells values as string
-        """
-        result = [[]]
-        cols = table.cols
-        for cell in self.compute_content(table):
-            if cols == 0:
-                result.append([])
-                cols = table.cols
-            cols -= 1
-            result[-1].append(cell)
-        # fill missing cells
-        while len(result[-1]) < cols:
-            result[-1].append("")
-        return result
-
-    def compute_content(self, layout):
-        """trick to compute the formatting of children layout before actually
-        writing it
-
-        return an iterator on strings (one for each child element)
-        """
-        # Patch the underlying output stream with a fresh-generated stream,
-        # which is used to store a temporary representation of a child
-        # node.
-        out = self.out
-        try:
-            for child in layout.children:
-                stream = StringIO()
-                self.out = stream
-                child.accept(self)
-                yield stream.getvalue()
-        finally:
-            self.out = out
diff --git a/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 408b51f..0000000
--- a/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/nodes.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/nodes.cpython-37.pyc
deleted file mode 100644
index 2640b32..0000000
--- a/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/nodes.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/text_writer.cpython-37.pyc b/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/text_writer.cpython-37.pyc
deleted file mode 100644
index 7222ed4..0000000
--- a/venv/Lib/site-packages/pylint/reporters/ureports/__pycache__/text_writer.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/reporters/ureports/nodes.py b/venv/Lib/site-packages/pylint/reporters/ureports/nodes.py
deleted file mode 100644
index 8fafb20..0000000
--- a/venv/Lib/site-packages/pylint/reporters/ureports/nodes.py
+++ /dev/null
@@ -1,188 +0,0 @@
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Micro reports objects.
-
-A micro report is a tree of layout and content objects.
-"""
-
-
-class VNode:
-    def __init__(self, nid=None):
-        self.id = nid
-        # navigation
-        self.parent = None
-        self.children = []
-
-    def __iter__(self):
-        return iter(self.children)
-
-    def append(self, child):
-        """add a node to children"""
-        self.children.append(child)
-        child.parent = self
-
-    def insert(self, index, child):
-        """insert a child node"""
-        self.children.insert(index, child)
-        child.parent = self
-
-    def _get_visit_name(self):
-        """
-        return the visit name for the mixed class. When calling 'accept', the
-        method <'visit_' + name returned by this method> will be called on the
-        visitor
-        """
-        try:
-            # pylint: disable=no-member
-            return self.TYPE.replace("-", "_")
-        # pylint: disable=broad-except
-        except Exception:
-            return self.__class__.__name__.lower()
-
-    def accept(self, visitor, *args, **kwargs):
-        func = getattr(visitor, "visit_%s" % self._get_visit_name())
-        return func(self, *args, **kwargs)
-
-    def leave(self, visitor, *args, **kwargs):
-        func = getattr(visitor, "leave_%s" % self._get_visit_name())
-        return func(self, *args, **kwargs)
-
-
-class BaseLayout(VNode):
-    """base container node
-
-    attributes
-    * children : components in this table (i.e. the table's cells)
-    """
-
-    def __init__(self, children=(), **kwargs):
-        super(BaseLayout, self).__init__(**kwargs)
-        for child in children:
-            if isinstance(child, VNode):
-                self.append(child)
-            else:
-                self.add_text(child)
-
-    def append(self, child):
-        """overridden to detect problems easily"""
-        assert child not in self.parents()
-        VNode.append(self, child)
-
-    def parents(self):
-        """return the ancestor nodes"""
-        assert self.parent is not self
-        if self.parent is None:
-            return []
-        return [self.parent] + self.parent.parents()
-
-    def add_text(self, text):
-        """shortcut to add text data"""
-        self.children.append(Text(text))
-
-
-# non container nodes #########################################################
-
-
-class Text(VNode):
-    """a text portion
-
-    attributes :
-    * data : the text value as an encoded or unicode string
-    """
-
-    def __init__(self, data, escaped=True, **kwargs):
-        super(Text, self).__init__(**kwargs)
-        # if isinstance(data, unicode):
-        #    data = data.encode('ascii')
-        assert isinstance(data, str), data.__class__
-        self.escaped = escaped
-        self.data = data
-
-
-class VerbatimText(Text):
-    """a verbatim text, display the raw data
-
-    attributes :
-    * data : the text value as an encoded or unicode string
-    """
-
-
-# container nodes #############################################################
-
-
-class Section(BaseLayout):
-    """a section
-
-    attributes :
-    * BaseLayout attributes
-
-    a title may also be given to the constructor, it'll be added
-    as a first element
-    a description may also be given to the constructor, it'll be added
-    as a first paragraph
-    """
-
-    def __init__(self, title=None, description=None, **kwargs):
-        super(Section, self).__init__(**kwargs)
-        if description:
-            self.insert(0, Paragraph([Text(description)]))
-        if title:
-            self.insert(0, Title(children=(title,)))
-
-
-class EvaluationSection(Section):
-    def __init__(self, message, **kwargs):
-        super(EvaluationSection, self).__init__(**kwargs)
-        title = Paragraph()
-        title.append(Text("-" * len(message)))
-        self.append(title)
-
-        message_body = Paragraph()
-        message_body.append(Text(message))
-        self.append(message_body)
-
-
-class Title(BaseLayout):
-    """a title
-
-    attributes :
-    * BaseLayout attributes
-
-    A title must not contains a section nor a paragraph!
-    """
-
-
-class Paragraph(BaseLayout):
-    """a simple text paragraph
-
-    attributes :
-    * BaseLayout attributes
-
-    A paragraph must not contains a section !
-    """
-
-
-class Table(BaseLayout):
-    """some tabular data
-
-    attributes :
-    * BaseLayout attributes
-    * cols : the number of columns of the table (REQUIRED)
-    * rheaders : the first row's elements are table's header
-    * cheaders : the first col's elements are table's header
-    * title : the table's optional title
-    """
-
-    def __init__(self, cols, title=None, rheaders=0, cheaders=0, **kwargs):
-        super(Table, self).__init__(**kwargs)
-        assert isinstance(cols, int)
-        self.cols = cols
-        self.title = title
-        self.rheaders = rheaders
-        self.cheaders = cheaders
diff --git a/venv/Lib/site-packages/pylint/reporters/ureports/text_writer.py b/venv/Lib/site-packages/pylint/reporters/ureports/text_writer.py
deleted file mode 100644
index 8f6aea2..0000000
--- a/venv/Lib/site-packages/pylint/reporters/ureports/text_writer.py
+++ /dev/null
@@ -1,94 +0,0 @@
-# Copyright (c) 2015-2016 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2018 Anthony Sottile <asottile@umich.edu>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""Text formatting drivers for ureports"""
-
-from pylint.reporters.ureports import BaseWriter
-
-TITLE_UNDERLINES = ["", "=", "-", "`", ".", "~", "^"]
-BULLETS = ["*", "-"]
-
-
-class TextWriter(BaseWriter):
-    """format layouts as text
-    (ReStructured inspiration but not totally handled yet)
-    """
-
-    def begin_format(self):
-        super(TextWriter, self).begin_format()
-        self.list_level = 0
-
-    def visit_section(self, layout):
-        """display a section as text
-        """
-        self.section += 1
-        self.writeln()
-        self.format_children(layout)
-        self.section -= 1
-        self.writeln()
-
-    def visit_evaluationsection(self, layout):
-        """Display an evaluation section as a text."""
-        self.section += 1
-        self.format_children(layout)
-        self.section -= 1
-        self.writeln()
-
-    def visit_title(self, layout):
-        title = "".join(list(self.compute_content(layout)))
-        self.writeln(title)
-        try:
-            self.writeln(TITLE_UNDERLINES[self.section] * len(title))
-        except IndexError:
-            print("FIXME TITLE TOO DEEP. TURNING TITLE INTO TEXT")
-
-    def visit_paragraph(self, layout):
-        """enter a paragraph"""
-        self.format_children(layout)
-        self.writeln()
-
-    def visit_table(self, layout):
-        """display a table as text"""
-        table_content = self.get_table_content(layout)
-        # get columns width
-        cols_width = [0] * len(table_content[0])
-        for row in table_content:
-            for index, col in enumerate(row):
-                cols_width[index] = max(cols_width[index], len(col))
-        self.default_table(layout, table_content, cols_width)
-        self.writeln()
-
-    def default_table(self, layout, table_content, cols_width):
-        """format a table"""
-        cols_width = [size + 1 for size in cols_width]
-        format_strings = " ".join(["%%-%ss"] * len(cols_width))
-        format_strings = format_strings % tuple(cols_width)
-        format_strings = format_strings.split(" ")
-        table_linesep = "\n+" + "+".join(["-" * w for w in cols_width]) + "+\n"
-        headsep = "\n+" + "+".join(["=" * w for w in cols_width]) + "+\n"
-
-        self.write(table_linesep)
-        for index, line in enumerate(table_content):
-            self.write("|")
-            for line_index, at_index in enumerate(line):
-                self.write(format_strings[line_index] % at_index)
-                self.write("|")
-            if index == 0 and layout.rheaders:
-                self.write(headsep)
-            else:
-                self.write(table_linesep)
-
-    def visit_verbatimtext(self, layout):
-        """display a verbatim layout as text (so difficult ;)
-        """
-        self.writeln("::\n")
-        for line in layout.data.splitlines():
-            self.writeln("    " + line)
-        self.writeln()
-
-    def visit_text(self, layout):
-        """add some text"""
-        self.write("%s" % layout.data)
diff --git a/venv/Lib/site-packages/pylint/testutils.py b/venv/Lib/site-packages/pylint/testutils.py
deleted file mode 100644
index f214208..0000000
--- a/venv/Lib/site-packages/pylint/testutils.py
+++ /dev/null
@@ -1,298 +0,0 @@
-# Copyright (c) 2012-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2012 FELD Boris <lothiraldan@gmail.com>
-# Copyright (c) 2013-2017 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2013-2014 Google, Inc.
-# Copyright (c) 2013 buck@yelp.com <buck@yelp.com>
-# Copyright (c) 2014 LCD 47 <lcd047@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Ricardo Gemignani <ricardo.gemignani@gmail.com>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2015 Pavel Roskin <proski@gnu.org>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Derek Gustafson <degustaf@gmail.com>
-# Copyright (c) 2016 Roy Williams <roy.williams.iii@gmail.com>
-# Copyright (c) 2016 xmo-odoo <xmo-odoo@users.noreply.github.com>
-# Copyright (c) 2017 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""functional/non regression tests for pylint"""
-import collections
-import contextlib
-import functools
-import sys
-import tempfile
-import tokenize
-from glob import glob
-from io import StringIO
-from os import close, getcwd, linesep, remove, sep, write
-from os.path import abspath, basename, dirname, join, splitext
-
-import astroid
-
-from pylint import checkers
-from pylint.interfaces import IReporter
-from pylint.lint import PyLinter
-from pylint.reporters import BaseReporter
-from pylint.utils import ASTWalker
-
-# Utils
-
-SYS_VERS_STR = "%d%d%d" % sys.version_info[:3]
-TITLE_UNDERLINES = ["", "=", "-", "."]
-PREFIX = abspath(dirname(__file__))
-
-
-def _get_tests_info(input_dir, msg_dir, prefix, suffix):
-    """get python input examples and output messages
-
-    We use following conventions for input files and messages:
-    for different inputs:
-        test for python  >= x.y    ->  input   =  <name>_pyxy.py
-        test for python  <  x.y    ->  input   =  <name>_py_xy.py
-    for one input and different messages:
-        message for python >=  x.y ->  message =  <name>_pyxy.txt
-        lower versions             ->  message with highest num
-    """
-    result = []
-    for fname in glob(join(input_dir, prefix + "*" + suffix)):
-        infile = basename(fname)
-        fbase = splitext(infile)[0]
-        # filter input files :
-        pyrestr = fbase.rsplit("_py", 1)[-1]  # like _26 or 26
-        if pyrestr.isdigit():  # '24', '25'...
-            if SYS_VERS_STR < pyrestr:
-                continue
-        if pyrestr.startswith("_") and pyrestr[1:].isdigit():
-            # skip test for higher python versions
-            if SYS_VERS_STR >= pyrestr[1:]:
-                continue
-        messages = glob(join(msg_dir, fbase + "*.txt"))
-        # the last one will be without ext, i.e. for all or upper versions:
-        if messages:
-            for outfile in sorted(messages, reverse=True):
-                py_rest = outfile.rsplit("_py", 1)[-1][:-4]
-                if py_rest.isdigit() and SYS_VERS_STR >= py_rest:
-                    break
-        else:
-            # This will provide an error message indicating the missing filename.
-            outfile = join(msg_dir, fbase + ".txt")
-        result.append((infile, outfile))
-    return result
-
-
-class TestReporter(BaseReporter):
-    """reporter storing plain text messages"""
-
-    __implements__ = IReporter
-
-    def __init__(self):  # pylint: disable=super-init-not-called
-
-        self.message_ids = {}
-        self.reset()
-        self.path_strip_prefix = getcwd() + sep
-
-    def reset(self):
-        self.out = StringIO()
-        self.messages = []
-
-    def handle_message(self, msg):
-        """manage message of different type and in the context of path """
-        obj = msg.obj
-        line = msg.line
-        msg_id = msg.msg_id
-        msg = msg.msg
-        self.message_ids[msg_id] = 1
-        if obj:
-            obj = ":%s" % obj
-        sigle = msg_id[0]
-        if linesep != "\n":
-            # 2to3 writes os.linesep instead of using
-            # the previosly used line separators
-            msg = msg.replace("\r\n", "\n")
-        self.messages.append("%s:%3s%s: %s" % (sigle, line, obj, msg))
-
-    def finalize(self):
-        self.messages.sort()
-        for msg in self.messages:
-            print(msg, file=self.out)
-        result = self.out.getvalue()
-        self.reset()
-        return result
-
-    # pylint: disable=unused-argument
-    def on_set_current_module(self, module, filepath):
-        pass
-
-    # pylint: enable=unused-argument
-
-    def display_reports(self, layout):
-        """ignore layouts"""
-
-    _display = None
-
-
-class MinimalTestReporter(BaseReporter):
-    def handle_message(self, msg):
-        self.messages.append(msg)
-
-    def on_set_current_module(self, module, filepath):
-        self.messages = []
-
-    _display = None
-
-
-class Message(
-    collections.namedtuple("Message", ["msg_id", "line", "node", "args", "confidence"])
-):
-    def __new__(cls, msg_id, line=None, node=None, args=None, confidence=None):
-        return tuple.__new__(cls, (msg_id, line, node, args, confidence))
-
-    def __eq__(self, other):
-        if isinstance(other, Message):
-            if self.confidence and other.confidence:
-                return super(Message, self).__eq__(other)
-            return self[:-1] == other[:-1]
-        return NotImplemented  # pragma: no cover
-
-    __hash__ = None
-
-
-class UnittestLinter:
-    """A fake linter class to capture checker messages."""
-
-    # pylint: disable=unused-argument, no-self-use
-
-    def __init__(self):
-        self._messages = []
-        self.stats = {}
-
-    def release_messages(self):
-        try:
-            return self._messages
-        finally:
-            self._messages = []
-
-    def add_message(
-        self, msg_id, line=None, node=None, args=None, confidence=None, col_offset=None
-    ):
-        # Do not test col_offset for now since changing Message breaks everything
-        self._messages.append(Message(msg_id, line, node, args, confidence))
-
-    def is_message_enabled(self, *unused_args, **unused_kwargs):
-        return True
-
-    def add_stats(self, **kwargs):
-        for name, value in kwargs.items():
-            self.stats[name] = value
-        return self.stats
-
-    @property
-    def options_providers(self):
-        return linter.options_providers
-
-
-def set_config(**kwargs):
-    """Decorator for setting config values on a checker."""
-
-    def _wrapper(fun):
-        @functools.wraps(fun)
-        def _forward(self):
-            for key, value in kwargs.items():
-                setattr(self.checker.config, key, value)
-            if isinstance(self, CheckerTestCase):
-                # reopen checker in case, it may be interested in configuration change
-                self.checker.open()
-            fun(self)
-
-        return _forward
-
-    return _wrapper
-
-
-class CheckerTestCase:
-    """A base testcase class for unit testing individual checker classes."""
-
-    CHECKER_CLASS = None
-    CONFIG = {}
-
-    def setup_method(self):
-        self.linter = UnittestLinter()
-        self.checker = self.CHECKER_CLASS(self.linter)  # pylint: disable=not-callable
-        for key, value in self.CONFIG.items():
-            setattr(self.checker.config, key, value)
-        self.checker.open()
-
-    @contextlib.contextmanager
-    def assertNoMessages(self):
-        """Assert that no messages are added by the given method."""
-        with self.assertAddsMessages():
-            yield
-
-    @contextlib.contextmanager
-    def assertAddsMessages(self, *messages):
-        """Assert that exactly the given method adds the given messages.
-
-        The list of messages must exactly match *all* the messages added by the
-        method. Additionally, we check to see whether the args in each message can
-        actually be substituted into the message string.
-        """
-        yield
-        got = self.linter.release_messages()
-        msg = "Expected messages did not match actual.\n" "Expected:\n%s\nGot:\n%s" % (
-            "\n".join(repr(m) for m in messages),
-            "\n".join(repr(m) for m in got),
-        )
-        assert list(messages) == got, msg
-
-    def walk(self, node):
-        """recursive walk on the given node"""
-        walker = ASTWalker(linter)
-        walker.add_checker(self.checker)
-        walker.walk(node)
-
-
-# Init
-test_reporter = TestReporter()
-linter = PyLinter()
-linter.set_reporter(test_reporter)
-linter.config.persistent = 0
-checkers.initialize(linter)
-
-
-def _tokenize_str(code):
-    return list(tokenize.generate_tokens(StringIO(code).readline))
-
-
-@contextlib.contextmanager
-def _create_tempfile(content=None):
-    """Create a new temporary file.
-
-    If *content* parameter is given, then it will be written
-    in the temporary file, before passing it back.
-    This is a context manager and should be used with a *with* statement.
-    """
-    # Can't use tempfile.NamedTemporaryFile here
-    # because on Windows the file must be closed before writing to it,
-    # see http://bugs.python.org/issue14243
-    file_handle, tmp = tempfile.mkstemp()
-    if content:
-        # erff
-        write(file_handle, bytes(content, "ascii"))
-    try:
-        yield tmp
-    finally:
-        close(file_handle)
-        remove(tmp)
-
-
-@contextlib.contextmanager
-def _create_file_backed_module(code):
-    """Create an astroid module for the given code, backed by a real file."""
-    with _create_tempfile() as temp:
-        module = astroid.parse(code)
-        module.file = temp
-        yield module
diff --git a/venv/Lib/site-packages/pylint/utils/__init__.py b/venv/Lib/site-packages/pylint/utils/__init__.py
deleted file mode 100644
index 8ee9e07..0000000
--- a/venv/Lib/site-packages/pylint/utils/__init__.py
+++ /dev/null
@@ -1,64 +0,0 @@
-# -*- coding: utf-8 -*-
-# Copyright (c) 2006-2014 LOGILAB S.A. (Paris, FRANCE) <contact@logilab.fr>
-# Copyright (c) 2009 Vincent
-# Copyright (c) 2009 Mads Kiilerich <mads@kiilerich.com>
-# Copyright (c) 2012-2014 Google, Inc.
-# Copyright (c) 2014-2018 Claudiu Popa <pcmanticore@gmail.com>
-# Copyright (c) 2014-2015 Michal Nowikowski <godfryd@gmail.com>
-# Copyright (c) 2014 LCD 47 <lcd047@gmail.com>
-# Copyright (c) 2014 Brett Cannon <brett@python.org>
-# Copyright (c) 2014 Arun Persaud <arun@nubati.net>
-# Copyright (c) 2014 Damien Nozay <damien.nozay@gmail.com>
-# Copyright (c) 2015 Aru Sahni <arusahni@gmail.com>
-# Copyright (c) 2015 Florian Bruhin <me@the-compiler.org>
-# Copyright (c) 2015 Simu Toni <simutoni@gmail.com>
-# Copyright (c) 2015 Ionel Cristian Maries <contact@ionelmc.ro>
-# Copyright (c) 2016 Łukasz Rogalski <rogalski.91@gmail.com>
-# Copyright (c) 2016 Moises Lopez <moylop260@vauxoo.com>
-# Copyright (c) 2016 Glenn Matthews <glenn@e-dad.net>
-# Copyright (c) 2016 Glenn Matthews <glmatthe@cisco.com>
-# Copyright (c) 2016 Ashley Whetter <ashley@awhetter.co.uk>
-# Copyright (c) 2016 xmo-odoo <xmo-odoo@users.noreply.github.com>
-# Copyright (c) 2017-2018 hippo91 <guillaume.peillex@gmail.com>
-# Copyright (c) 2017 Pierre Sassoulas <pierre.sassoulas@cea.fr>
-# Copyright (c) 2017 Bryce Guinta <bryce.paul.guinta@gmail.com>
-# Copyright (c) 2017 Chris Lamb <chris@chris-lamb.co.uk>
-# Copyright (c) 2017 Anthony Sottile <asottile@umich.edu>
-# Copyright (c) 2017 Thomas Hisch <t.hisch@gmail.com>
-# Copyright (c) 2017 Mikhail Fesenko <proggga@gmail.com>
-# Copyright (c) 2017 Craig Citro <craigcitro@gmail.com>
-# Copyright (c) 2017 Ville Skyttä <ville.skytta@iki.fi>
-# Copyright (c) 2018 ssolanki <sushobhitsolanki@gmail.com>
-# Copyright (c) 2018 Sushobhit <31987769+sushobhit27@users.noreply.github.com>
-# Copyright (c) 2018 Pierre Sassoulas <pierre.sassoulas@wisebim.fr>
-# Copyright (c) 2018 Reverb C <reverbc@users.noreply.github.com>
-# Copyright (c) 2018 Nick Drozd <nicholasdrozd@gmail.com>
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-"""some various utilities and helper classes, most of them used in the
-main pylint class
-"""
-
-from pylint.utils.ast_walker import ASTWalker
-from pylint.utils.file_state import FileState
-from pylint.utils.utils import (
-    _basename_in_blacklist_re,
-    _check_csv,
-    _format_option_value,
-    _splitstrip,
-    _unquote,
-    decoding_stream,
-    deprecated_option,
-    expand_modules,
-    format_section,
-    get_global_option,
-    get_module_and_frameid,
-    get_rst_section,
-    get_rst_title,
-    normalize_text,
-    register_plugins,
-    safe_decode,
-    tokenize_module,
-)
diff --git a/venv/Lib/site-packages/pylint/utils/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/pylint/utils/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 6f3569d..0000000
--- a/venv/Lib/site-packages/pylint/utils/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/utils/__pycache__/ast_walker.cpython-37.pyc b/venv/Lib/site-packages/pylint/utils/__pycache__/ast_walker.cpython-37.pyc
deleted file mode 100644
index af27609..0000000
--- a/venv/Lib/site-packages/pylint/utils/__pycache__/ast_walker.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/utils/__pycache__/file_state.cpython-37.pyc b/venv/Lib/site-packages/pylint/utils/__pycache__/file_state.cpython-37.pyc
deleted file mode 100644
index 4a43508..0000000
--- a/venv/Lib/site-packages/pylint/utils/__pycache__/file_state.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/utils/__pycache__/utils.cpython-37.pyc b/venv/Lib/site-packages/pylint/utils/__pycache__/utils.cpython-37.pyc
deleted file mode 100644
index 9049995..0000000
--- a/venv/Lib/site-packages/pylint/utils/__pycache__/utils.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/pylint/utils/ast_walker.py b/venv/Lib/site-packages/pylint/utils/ast_walker.py
deleted file mode 100644
index 2e7a6da..0000000
--- a/venv/Lib/site-packages/pylint/utils/ast_walker.py
+++ /dev/null
@@ -1,79 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import collections
-
-from astroid import nodes
-
-
-class ASTWalker:
-    def __init__(self, linter):
-        # callbacks per node types
-        self.nbstatements = 0
-        self.visit_events = collections.defaultdict(list)
-        self.leave_events = collections.defaultdict(list)
-        self.linter = linter
-
-    def _is_method_enabled(self, method):
-        if not hasattr(method, "checks_msgs"):
-            return True
-        for msg_desc in method.checks_msgs:
-            if self.linter.is_message_enabled(msg_desc):
-                return True
-        return False
-
-    def add_checker(self, checker):
-        """walk to the checker's dir and collect visit and leave methods"""
-        vcids = set()
-        lcids = set()
-        visits = self.visit_events
-        leaves = self.leave_events
-        for member in dir(checker):
-            cid = member[6:]
-            if cid == "default":
-                continue
-            if member.startswith("visit_"):
-                v_meth = getattr(checker, member)
-                # don't use visit_methods with no activated message:
-                if self._is_method_enabled(v_meth):
-                    visits[cid].append(v_meth)
-                    vcids.add(cid)
-            elif member.startswith("leave_"):
-                l_meth = getattr(checker, member)
-                # don't use leave_methods with no activated message:
-                if self._is_method_enabled(l_meth):
-                    leaves[cid].append(l_meth)
-                    lcids.add(cid)
-        visit_default = getattr(checker, "visit_default", None)
-        if visit_default:
-            for cls in nodes.ALL_NODE_CLASSES:
-                cid = cls.__name__.lower()
-                if cid not in vcids:
-                    visits[cid].append(visit_default)
-        # for now we have no "leave_default" method in Pylint
-
-    def walk(self, astroid):
-        """call visit events of astroid checkers for the given node, recurse on
-        its children, then leave events.
-        """
-        cid = astroid.__class__.__name__.lower()
-
-        # Detect if the node is a new name for a deprecated alias.
-        # In this case, favour the methods for the deprecated
-        # alias if any,  in order to maintain backwards
-        # compatibility.
-        visit_events = self.visit_events.get(cid, ())
-        leave_events = self.leave_events.get(cid, ())
-
-        if astroid.is_statement:
-            self.nbstatements += 1
-        # generate events for this node on each checker
-        for callback in visit_events or ():
-            callback(astroid)
-        # recurse on children
-        for child in astroid.get_children():
-            self.walk(child)
-        for callback in leave_events or ():
-            callback(astroid)
diff --git a/venv/Lib/site-packages/pylint/utils/file_state.py b/venv/Lib/site-packages/pylint/utils/file_state.py
deleted file mode 100644
index 1a8dd4d..0000000
--- a/venv/Lib/site-packages/pylint/utils/file_state.py
+++ /dev/null
@@ -1,138 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import collections
-
-from astroid import nodes
-
-from pylint.constants import MSG_STATE_SCOPE_MODULE, WarningScope
-
-
-class FileState:
-    """Hold internal state specific to the currently analyzed file"""
-
-    def __init__(self, modname=None):
-        self.base_name = modname
-        self._module_msgs_state = {}
-        self._raw_module_msgs_state = {}
-        self._ignored_msgs = collections.defaultdict(set)
-        self._suppression_mapping = {}
-        self._effective_max_line_number = None
-
-    def collect_block_lines(self, msgs_store, module_node):
-        """Walk the AST to collect block level options line numbers."""
-        for msg, lines in self._module_msgs_state.items():
-            self._raw_module_msgs_state[msg] = lines.copy()
-        orig_state = self._module_msgs_state.copy()
-        self._module_msgs_state = {}
-        self._suppression_mapping = {}
-        self._effective_max_line_number = module_node.tolineno
-        self._collect_block_lines(msgs_store, module_node, orig_state)
-
-    def _collect_block_lines(self, msgs_store, node, msg_state):
-        """Recursively walk (depth first) AST to collect block level options
-        line numbers.
-        """
-        for child in node.get_children():
-            self._collect_block_lines(msgs_store, child, msg_state)
-        first = node.fromlineno
-        last = node.tolineno
-        # first child line number used to distinguish between disable
-        # which are the first child of scoped node with those defined later.
-        # For instance in the code below:
-        #
-        # 1.   def meth8(self):
-        # 2.        """test late disabling"""
-        # 3.        pylint: disable=not-callable
-        # 4.        print(self.blip)
-        # 5.        pylint: disable=no-member
-        # 6.        print(self.bla)
-        #
-        # E1102 should be disabled from line 1 to 6 while E1101 from line 5 to 6
-        #
-        # this is necessary to disable locally messages applying to class /
-        # function using their fromlineno
-        if (
-            isinstance(node, (nodes.Module, nodes.ClassDef, nodes.FunctionDef))
-            and node.body
-        ):
-            firstchildlineno = node.body[0].fromlineno
-        else:
-            firstchildlineno = last
-        for msgid, lines in msg_state.items():
-            for lineno, state in list(lines.items()):
-                original_lineno = lineno
-                if first > lineno or last < lineno:
-                    continue
-                # Set state for all lines for this block, if the
-                # warning is applied to nodes.
-                message_definitions = msgs_store.get_message_definitions(msgid)
-                for message_definition in message_definitions:
-                    if message_definition.scope == WarningScope.NODE:
-                        if lineno > firstchildlineno:
-                            state = True
-                        first_, last_ = node.block_range(lineno)
-                    else:
-                        first_ = lineno
-                        last_ = last
-                for line in range(first_, last_ + 1):
-                    # do not override existing entries
-                    if line in self._module_msgs_state.get(msgid, ()):
-                        continue
-                    if line in lines:  # state change in the same block
-                        state = lines[line]
-                        original_lineno = line
-                    if not state:
-                        self._suppression_mapping[(msgid, line)] = original_lineno
-                    try:
-                        self._module_msgs_state[msgid][line] = state
-                    except KeyError:
-                        self._module_msgs_state[msgid] = {line: state}
-                del lines[lineno]
-
-    def set_msg_status(self, msg, line, status):
-        """Set status (enabled/disable) for a given message at a given line"""
-        assert line > 0
-        try:
-            self._module_msgs_state[msg.msgid][line] = status
-        except KeyError:
-            self._module_msgs_state[msg.msgid] = {line: status}
-
-    def handle_ignored_message(
-        self, state_scope, msgid, line, node, args, confidence
-    ):  # pylint: disable=unused-argument
-        """Report an ignored message.
-
-        state_scope is either MSG_STATE_SCOPE_MODULE or MSG_STATE_SCOPE_CONFIG,
-        depending on whether the message was disabled locally in the module,
-        or globally. The other arguments are the same as for add_message.
-        """
-        if state_scope == MSG_STATE_SCOPE_MODULE:
-            try:
-                orig_line = self._suppression_mapping[(msgid, line)]
-                self._ignored_msgs[(msgid, orig_line)].add(line)
-            except KeyError:
-                pass
-
-    def iter_spurious_suppression_messages(self, msgs_store):
-        for warning, lines in self._raw_module_msgs_state.items():
-            for line, enable in lines.items():
-                if not enable and (warning, line) not in self._ignored_msgs:
-                    # ignore cyclic-import check which can show false positives
-                    # here due to incomplete context
-                    if warning != "R0401":
-                        yield "useless-suppression", line, (
-                            msgs_store.get_msg_display_string(warning),
-                        )
-        # don't use iteritems here, _ignored_msgs may be modified by add_message
-        for (warning, from_), lines in list(self._ignored_msgs.items()):
-            for line in lines:
-                yield "suppressed-message", line, (
-                    msgs_store.get_msg_display_string(warning),
-                    from_,
-                )
-
-    def get_effective_max_line_number(self):
-        return self._effective_max_line_number
diff --git a/venv/Lib/site-packages/pylint/utils/utils.py b/venv/Lib/site-packages/pylint/utils/utils.py
deleted file mode 100644
index 5605ecd..0000000
--- a/venv/Lib/site-packages/pylint/utils/utils.py
+++ /dev/null
@@ -1,371 +0,0 @@
-# -*- coding: utf-8 -*-
-
-# Licensed under the GPL: https://www.gnu.org/licenses/old-licenses/gpl-2.0.html
-# For details: https://github.com/PyCQA/pylint/blob/master/COPYING
-
-import codecs
-import re
-import sys
-import textwrap
-import tokenize
-from os import linesep, listdir
-from os.path import basename, dirname, exists, isdir, join, normpath, splitext
-
-from astroid import Module, modutils
-
-from pylint.constants import PY_EXTS
-
-
-def normalize_text(text, line_len=80, indent=""):
-    """Wrap the text on the given line length."""
-    return "\n".join(
-        textwrap.wrap(
-            text, width=line_len, initial_indent=indent, subsequent_indent=indent
-        )
-    )
-
-
-def get_module_and_frameid(node):
-    """return the module name and the frame id in the module"""
-    frame = node.frame()
-    module, obj = "", []
-    while frame:
-        if isinstance(frame, Module):
-            module = frame.name
-        else:
-            obj.append(getattr(frame, "name", "<lambda>"))
-        try:
-            frame = frame.parent.frame()
-        except AttributeError:
-            frame = None
-    obj.reverse()
-    return module, ".".join(obj)
-
-
-def get_rst_title(title, character):
-    """Permit to get a title formatted as ReStructuredText test (underlined with a chosen character)."""
-    return "%s\n%s\n" % (title, character * len(title))
-
-
-def get_rst_section(section, options, doc=None):
-    """format an options section using as a ReStructuredText formatted output"""
-    result = ""
-    if section:
-        result += get_rst_title(section, "'")
-    if doc:
-        formatted_doc = normalize_text(doc, line_len=79, indent="")
-        result += "%s\n\n" % formatted_doc
-    for optname, optdict, value in options:
-        help_opt = optdict.get("help")
-        result += ":%s:\n" % optname
-        if help_opt:
-            formatted_help = normalize_text(help_opt, line_len=79, indent="  ")
-            result += "%s\n" % formatted_help
-        if value:
-            value = str(_format_option_value(optdict, value))
-            result += "\n  Default: ``%s``\n" % value.replace("`` ", "```` ``")
-    return result
-
-
-def safe_decode(line, encoding, *args, **kwargs):
-    """return decoded line from encoding or decode with default encoding"""
-    try:
-        return line.decode(encoding or sys.getdefaultencoding(), *args, **kwargs)
-    except LookupError:
-        return line.decode(sys.getdefaultencoding(), *args, **kwargs)
-
-
-def decoding_stream(stream, encoding, errors="strict"):
-    try:
-        reader_cls = codecs.getreader(encoding or sys.getdefaultencoding())
-    except LookupError:
-        reader_cls = codecs.getreader(sys.getdefaultencoding())
-    return reader_cls(stream, errors)
-
-
-def tokenize_module(module):
-    with module.stream() as stream:
-        readline = stream.readline
-        return list(tokenize.tokenize(readline))
-
-
-def _basename_in_blacklist_re(base_name, black_list_re):
-    """Determines if the basename is matched in a regex blacklist
-
-    :param str base_name: The basename of the file
-    :param list black_list_re: A collection of regex patterns to match against.
-        Successful matches are blacklisted.
-
-    :returns: `True` if the basename is blacklisted, `False` otherwise.
-    :rtype: bool
-    """
-    for file_pattern in black_list_re:
-        if file_pattern.match(base_name):
-            return True
-    return False
-
-
-def _modpath_from_file(filename, is_namespace):
-    def _is_package_cb(path, parts):
-        return modutils.check_modpath_has_init(path, parts) or is_namespace
-
-    return modutils.modpath_from_file_with_callback(
-        filename, is_package_cb=_is_package_cb
-    )
-
-
-def expand_modules(files_or_modules, black_list, black_list_re):
-    """take a list of files/modules/packages and return the list of tuple
-    (file, module name) which have to be actually checked
-    """
-    result = []
-    errors = []
-    for something in files_or_modules:
-        if basename(something) in black_list:
-            continue
-        if _basename_in_blacklist_re(basename(something), black_list_re):
-            continue
-        if exists(something):
-            # this is a file or a directory
-            try:
-                modname = ".".join(modutils.modpath_from_file(something))
-            except ImportError:
-                modname = splitext(basename(something))[0]
-            if isdir(something):
-                filepath = join(something, "__init__.py")
-            else:
-                filepath = something
-        else:
-            # suppose it's a module or package
-            modname = something
-            try:
-                filepath = modutils.file_from_modpath(modname.split("."))
-                if filepath is None:
-                    continue
-            except (ImportError, SyntaxError) as ex:
-                # The SyntaxError is a Python bug and should be
-                # removed once we move away from imp.find_module: http://bugs.python.org/issue10588
-                errors.append({"key": "fatal", "mod": modname, "ex": ex})
-                continue
-
-        filepath = normpath(filepath)
-        modparts = (modname or something).split(".")
-
-        try:
-            spec = modutils.file_info_from_modpath(modparts, path=sys.path)
-        except ImportError:
-            # Might not be acceptable, don't crash.
-            is_namespace = False
-            is_directory = isdir(something)
-        else:
-            is_namespace = modutils.is_namespace(spec)
-            is_directory = modutils.is_directory(spec)
-
-        if not is_namespace:
-            result.append(
-                {
-                    "path": filepath,
-                    "name": modname,
-                    "isarg": True,
-                    "basepath": filepath,
-                    "basename": modname,
-                }
-            )
-
-        has_init = (
-            not (modname.endswith(".__init__") or modname == "__init__")
-            and basename(filepath) == "__init__.py"
-        )
-
-        if has_init or is_namespace or is_directory:
-            for subfilepath in modutils.get_module_files(
-                dirname(filepath), black_list, list_all=is_namespace
-            ):
-                if filepath == subfilepath:
-                    continue
-                if _basename_in_blacklist_re(basename(subfilepath), black_list_re):
-                    continue
-
-                modpath = _modpath_from_file(subfilepath, is_namespace)
-                submodname = ".".join(modpath)
-                result.append(
-                    {
-                        "path": subfilepath,
-                        "name": submodname,
-                        "isarg": False,
-                        "basepath": filepath,
-                        "basename": modname,
-                    }
-                )
-    return result, errors
-
-
-def register_plugins(linter, directory):
-    """load all module and package in the given directory, looking for a
-    'register' function in each one, used to register pylint checkers
-    """
-    imported = {}
-    for filename in listdir(directory):
-        base, extension = splitext(filename)
-        if base in imported or base == "__pycache__":
-            continue
-        if (
-            extension in PY_EXTS
-            and base != "__init__"
-            or (not extension and isdir(join(directory, base)))
-        ):
-            try:
-                module = modutils.load_module_from_file(join(directory, filename))
-            except ValueError:
-                # empty module name (usually emacs auto-save files)
-                continue
-            except ImportError as exc:
-                print(
-                    "Problem importing module %s: %s" % (filename, exc), file=sys.stderr
-                )
-            else:
-                if hasattr(module, "register"):
-                    module.register(linter)
-                    imported[base] = 1
-
-
-def get_global_option(checker, option, default=None):
-    """ Retrieve an option defined by the given *checker* or
-    by all known option providers.
-
-    It will look in the list of all options providers
-    until the given *option* will be found.
-    If the option wasn't found, the *default* value will be returned.
-    """
-    # First, try in the given checker's config.
-    # After that, look in the options providers.
-
-    try:
-        return getattr(checker.config, option.replace("-", "_"))
-    except AttributeError:
-        pass
-    for provider in checker.linter.options_providers:
-        for options in provider.options:
-            if options[0] == option:
-                return getattr(provider.config, option.replace("-", "_"))
-    return default
-
-
-def deprecated_option(
-    shortname=None, opt_type=None, help_msg=None, deprecation_msg=None
-):
-    def _warn_deprecated(option, optname, *args):  # pylint: disable=unused-argument
-        if deprecation_msg:
-            sys.stderr.write(deprecation_msg % (optname,))
-
-    option = {
-        "help": help_msg,
-        "hide": True,
-        "type": opt_type,
-        "action": "callback",
-        "callback": _warn_deprecated,
-        "deprecated": True,
-    }
-    if shortname:
-        option["shortname"] = shortname
-    return option
-
-
-def _splitstrip(string, sep=","):
-    """return a list of stripped string by splitting the string given as
-    argument on `sep` (',' by default). Empty string are discarded.
-
-    >>> _splitstrip('a, b, c   ,  4,,')
-    ['a', 'b', 'c', '4']
-    >>> _splitstrip('a')
-    ['a']
-    >>> _splitstrip('a,\nb,\nc,')
-    ['a', 'b', 'c']
-
-    :type string: str or unicode
-    :param string: a csv line
-
-    :type sep: str or unicode
-    :param sep: field separator, default to the comma (',')
-
-    :rtype: str or unicode
-    :return: the unquoted string (or the input string if it wasn't quoted)
-    """
-    return [word.strip() for word in string.split(sep) if word.strip()]
-
-
-def _unquote(string):
-    """remove optional quotes (simple or double) from the string
-
-    :type string: str or unicode
-    :param string: an optionally quoted string
-
-    :rtype: str or unicode
-    :return: the unquoted string (or the input string if it wasn't quoted)
-    """
-    if not string:
-        return string
-    if string[0] in "\"'":
-        string = string[1:]
-    if string[-1] in "\"'":
-        string = string[:-1]
-    return string
-
-
-def _check_csv(value):
-    if isinstance(value, (list, tuple)):
-        return value
-    return _splitstrip(value)
-
-
-def _comment(string):
-    """return string as a comment"""
-    lines = [line.strip() for line in string.splitlines()]
-    return "# " + ("%s# " % linesep).join(lines)
-
-
-def _format_option_value(optdict, value):
-    """return the user input's value from a 'compiled' value"""
-    if isinstance(value, (list, tuple)):
-        value = ",".join(_format_option_value(optdict, item) for item in value)
-    elif isinstance(value, dict):
-        value = ",".join("%s:%s" % (k, v) for k, v in value.items())
-    elif hasattr(value, "match"):  # optdict.get('type') == 'regexp'
-        # compiled regexp
-        value = value.pattern
-    elif optdict.get("type") == "yn":
-        value = "yes" if value else "no"
-    elif isinstance(value, str) and value.isspace():
-        value = "'%s'" % value
-    return value
-
-
-def format_section(stream, section, options, doc=None):
-    """format an options section using the INI format"""
-    if doc:
-        print(_comment(doc), file=stream)
-    print("[%s]" % section, file=stream)
-    _ini_format(stream, options)
-
-
-def _ini_format(stream, options):
-    """format options using the INI format"""
-    for optname, optdict, value in options:
-        value = _format_option_value(optdict, value)
-        help_opt = optdict.get("help")
-        if help_opt:
-            help_opt = normalize_text(help_opt, line_len=79, indent="# ")
-            print(file=stream)
-            print(help_opt, file=stream)
-        else:
-            print(file=stream)
-        if value is None:
-            print("#%s=" % optname, file=stream)
-        else:
-            value = str(value).strip()
-            if re.match(r"^([\w-]+,)+[\w-]+$", str(value)):
-                separator = "\n " + " " * len(optname)
-                value = separator.join(x + "," for x in str(value).split(","))
-                # remove trailing ',' from last element of the list
-                value = value[:-1]
-            print("%s=%s" % (optname, value), file=stream)
diff --git a/venv/Lib/site-packages/setuptools-40.8.0-py3.7.egg b/venv/Lib/site-packages/setuptools-40.8.0-py3.7.egg
deleted file mode 100644
index 5c31edb..0000000
--- a/venv/Lib/site-packages/setuptools-40.8.0-py3.7.egg
+++ /dev/null
diff --git a/venv/Lib/site-packages/setuptools.pth b/venv/Lib/site-packages/setuptools.pth
deleted file mode 100644
index ca49991..0000000
--- a/venv/Lib/site-packages/setuptools.pth
+++ /dev/null
@@ -1 +0,0 @@
-./setuptools-40.8.0-py3.7.egg
diff --git a/venv/Lib/site-packages/six-1.14.0.dist-info/INSTALLER b/venv/Lib/site-packages/six-1.14.0.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/six-1.14.0.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/six-1.14.0.dist-info/LICENSE b/venv/Lib/site-packages/six-1.14.0.dist-info/LICENSE
deleted file mode 100644
index de66331..0000000
--- a/venv/Lib/site-packages/six-1.14.0.dist-info/LICENSE
+++ /dev/null
@@ -1,18 +0,0 @@
-Copyright (c) 2010-2020 Benjamin Peterson
-
-Permission is hereby granted, free of charge, to any person obtaining a copy of
-this software and associated documentation files (the "Software"), to deal in
-the Software without restriction, including without limitation the rights to
-use, copy, modify, merge, publish, distribute, sublicense, and/or sell copies of
-the Software, and to permit persons to whom the Software is furnished to do so,
-subject to the following conditions:
-
-The above copyright notice and this permission notice shall be included in all
-copies or substantial portions of the Software.
-
-THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR
-IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF MERCHANTABILITY, FITNESS
-FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL THE AUTHORS OR
-COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER LIABILITY, WHETHER
-IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN
-CONNECTION WITH THE SOFTWARE OR THE USE OR OTHER DEALINGS IN THE SOFTWARE.
diff --git a/venv/Lib/site-packages/six-1.14.0.dist-info/METADATA b/venv/Lib/site-packages/six-1.14.0.dist-info/METADATA
deleted file mode 100644
index b9c24c7..0000000
--- a/venv/Lib/site-packages/six-1.14.0.dist-info/METADATA
+++ /dev/null
@@ -1,49 +0,0 @@
-Metadata-Version: 2.1
-Name: six
-Version: 1.14.0
-Summary: Python 2 and 3 compatibility utilities
-Home-page: https://github.com/benjaminp/six
-Author: Benjamin Peterson
-Author-email: benjamin@python.org
-License: MIT
-Platform: UNKNOWN
-Classifier: Development Status :: 5 - Production/Stable
-Classifier: Programming Language :: Python :: 2
-Classifier: Programming Language :: Python :: 3
-Classifier: Intended Audience :: Developers
-Classifier: License :: OSI Approved :: MIT License
-Classifier: Topic :: Software Development :: Libraries
-Classifier: Topic :: Utilities
-Requires-Python: >=2.7, !=3.0.*, !=3.1.*, !=3.2.*
-
-.. image:: https://img.shields.io/pypi/v/six.svg
-   :target: https://pypi.org/project/six/
-   :alt: six on PyPI
-
-.. image:: https://travis-ci.org/benjaminp/six.svg?branch=master
-   :target: https://travis-ci.org/benjaminp/six
-   :alt: six on TravisCI
-
-.. image:: https://readthedocs.org/projects/six/badge/?version=latest
-   :target: https://six.readthedocs.io/
-   :alt: six's documentation on Read the Docs
-
-.. image:: https://img.shields.io/badge/license-MIT-green.svg
-   :target: https://github.com/benjaminp/six/blob/master/LICENSE
-   :alt: MIT License badge
-
-Six is a Python 2 and 3 compatibility library.  It provides utility functions
-for smoothing over the differences between the Python versions with the goal of
-writing Python code that is compatible on both Python versions.  See the
-documentation for more information on what is provided.
-
-Six supports Python 2.7 and 3.3+.  It is contained in only one Python
-file, so it can be easily copied into your project. (The copyright and license
-notice must be retained.)
-
-Online documentation is at https://six.readthedocs.io/.
-
-Bugs can be reported to https://github.com/benjaminp/six.  The code can also
-be found there.
-
-
diff --git a/venv/Lib/site-packages/six-1.14.0.dist-info/RECORD b/venv/Lib/site-packages/six-1.14.0.dist-info/RECORD
deleted file mode 100644
index 3515abb..0000000
--- a/venv/Lib/site-packages/six-1.14.0.dist-info/RECORD
+++ /dev/null
@@ -1,8 +0,0 @@
-__pycache__/six.cpython-37.pyc,,
-six-1.14.0.dist-info/INSTALLER,sha256=zuuue4knoyJ-UwPPXg8fezS7VCrXJQrAP7zeNuwvFQg,4
-six-1.14.0.dist-info/LICENSE,sha256=i7hQxWWqOJ_cFvOkaWWtI9gq3_YPI5P8J2K2MYXo5sk,1066
-six-1.14.0.dist-info/METADATA,sha256=nEAc9huAtn13Bna3MQ1ZSswoyaV7GMJdKfGluHFX4DU,1795
-six-1.14.0.dist-info/RECORD,,
-six-1.14.0.dist-info/WHEEL,sha256=8zNYZbwQSXoB9IfXOjPfeNwvAsALAjffgk27FqvCWbo,110
-six-1.14.0.dist-info/top_level.txt,sha256=_iVH_iYEtEXnD8nYGQYpYFUvkUW9sEO1GYbkeKSAais,4
-six.py,sha256=Q6WvEXZ1DGEASAo3CGNCJkKv2tPy8xkSmK-VHE9PYIA,34074
diff --git a/venv/Lib/site-packages/six-1.14.0.dist-info/WHEEL b/venv/Lib/site-packages/six-1.14.0.dist-info/WHEEL
deleted file mode 100644
index 8b701e9..0000000
--- a/venv/Lib/site-packages/six-1.14.0.dist-info/WHEEL
+++ /dev/null
@@ -1,6 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.33.6)
-Root-Is-Purelib: true
-Tag: py2-none-any
-Tag: py3-none-any
-
diff --git a/venv/Lib/site-packages/six-1.14.0.dist-info/top_level.txt b/venv/Lib/site-packages/six-1.14.0.dist-info/top_level.txt
deleted file mode 100644
index ffe2fce..0000000
--- a/venv/Lib/site-packages/six-1.14.0.dist-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-six
diff --git a/venv/Lib/site-packages/six.py b/venv/Lib/site-packages/six.py
deleted file mode 100644
index 5fe9f8e..0000000
--- a/venv/Lib/site-packages/six.py
+++ /dev/null
@@ -1,980 +0,0 @@
-# Copyright (c) 2010-2020 Benjamin Peterson
-#
-# Permission is hereby granted, free of charge, to any person obtaining a copy
-# of this software and associated documentation files (the "Software"), to deal
-# in the Software without restriction, including without limitation the rights
-# to use, copy, modify, merge, publish, distribute, sublicense, and/or sell
-# copies of the Software, and to permit persons to whom the Software is
-# furnished to do so, subject to the following conditions:
-#
-# The above copyright notice and this permission notice shall be included in all
-# copies or substantial portions of the Software.
-#
-# THE SOFTWARE IS PROVIDED "AS IS", WITHOUT WARRANTY OF ANY KIND, EXPRESS OR
-# IMPLIED, INCLUDING BUT NOT LIMITED TO THE WARRANTIES OF MERCHANTABILITY,
-# FITNESS FOR A PARTICULAR PURPOSE AND NONINFRINGEMENT. IN NO EVENT SHALL THE
-# AUTHORS OR COPYRIGHT HOLDERS BE LIABLE FOR ANY CLAIM, DAMAGES OR OTHER
-# LIABILITY, WHETHER IN AN ACTION OF CONTRACT, TORT OR OTHERWISE, ARISING FROM,
-# OUT OF OR IN CONNECTION WITH THE SOFTWARE OR THE USE OR OTHER DEALINGS IN THE
-# SOFTWARE.
-
-"""Utilities for writing code that runs on Python 2 and 3"""
-
-from __future__ import absolute_import
-
-import functools
-import itertools
-import operator
-import sys
-import types
-
-__author__ = "Benjamin Peterson <benjamin@python.org>"
-__version__ = "1.14.0"
-
-
-# Useful for very coarse version differentiation.
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-PY34 = sys.version_info[0:2] >= (3, 4)
-
-if PY3:
-    string_types = str,
-    integer_types = int,
-    class_types = type,
-    text_type = str
-    binary_type = bytes
-
-    MAXSIZE = sys.maxsize
-else:
-    string_types = basestring,
-    integer_types = (int, long)
-    class_types = (type, types.ClassType)
-    text_type = unicode
-    binary_type = str
-
-    if sys.platform.startswith("java"):
-        # Jython always uses 32 bits.
-        MAXSIZE = int((1 << 31) - 1)
-    else:
-        # It's possible to have sizeof(long) != sizeof(Py_ssize_t).
-        class X(object):
-
-            def __len__(self):
-                return 1 << 31
-        try:
-            len(X())
-        except OverflowError:
-            # 32-bit
-            MAXSIZE = int((1 << 31) - 1)
-        else:
-            # 64-bit
-            MAXSIZE = int((1 << 63) - 1)
-        del X
-
-
-def _add_doc(func, doc):
-    """Add documentation to a function."""
-    func.__doc__ = doc
-
-
-def _import_module(name):
-    """Import module, returning the module after the last dot."""
-    __import__(name)
-    return sys.modules[name]
-
-
-class _LazyDescr(object):
-
-    def __init__(self, name):
-        self.name = name
-
-    def __get__(self, obj, tp):
-        result = self._resolve()
-        setattr(obj, self.name, result)  # Invokes __set__.
-        try:
-            # This is a bit ugly, but it avoids running this again by
-            # removing this descriptor.
-            delattr(obj.__class__, self.name)
-        except AttributeError:
-            pass
-        return result
-
-
-class MovedModule(_LazyDescr):
-
-    def __init__(self, name, old, new=None):
-        super(MovedModule, self).__init__(name)
-        if PY3:
-            if new is None:
-                new = name
-            self.mod = new
-        else:
-            self.mod = old
-
-    def _resolve(self):
-        return _import_module(self.mod)
-
-    def __getattr__(self, attr):
-        _module = self._resolve()
-        value = getattr(_module, attr)
-        setattr(self, attr, value)
-        return value
-
-
-class _LazyModule(types.ModuleType):
-
-    def __init__(self, name):
-        super(_LazyModule, self).__init__(name)
-        self.__doc__ = self.__class__.__doc__
-
-    def __dir__(self):
-        attrs = ["__doc__", "__name__"]
-        attrs += [attr.name for attr in self._moved_attributes]
-        return attrs
-
-    # Subclasses should override this
-    _moved_attributes = []
-
-
-class MovedAttribute(_LazyDescr):
-
-    def __init__(self, name, old_mod, new_mod, old_attr=None, new_attr=None):
-        super(MovedAttribute, self).__init__(name)
-        if PY3:
-            if new_mod is None:
-                new_mod = name
-            self.mod = new_mod
-            if new_attr is None:
-                if old_attr is None:
-                    new_attr = name
-                else:
-                    new_attr = old_attr
-            self.attr = new_attr
-        else:
-            self.mod = old_mod
-            if old_attr is None:
-                old_attr = name
-            self.attr = old_attr
-
-    def _resolve(self):
-        module = _import_module(self.mod)
-        return getattr(module, self.attr)
-
-
-class _SixMetaPathImporter(object):
-
-    """
-    A meta path importer to import six.moves and its submodules.
-
-    This class implements a PEP302 finder and loader. It should be compatible
-    with Python 2.5 and all existing versions of Python3
-    """
-
-    def __init__(self, six_module_name):
-        self.name = six_module_name
-        self.known_modules = {}
-
-    def _add_module(self, mod, *fullnames):
-        for fullname in fullnames:
-            self.known_modules[self.name + "." + fullname] = mod
-
-    def _get_module(self, fullname):
-        return self.known_modules[self.name + "." + fullname]
-
-    def find_module(self, fullname, path=None):
-        if fullname in self.known_modules:
-            return self
-        return None
-
-    def __get_module(self, fullname):
-        try:
-            return self.known_modules[fullname]
-        except KeyError:
-            raise ImportError("This loader does not know module " + fullname)
-
-    def load_module(self, fullname):
-        try:
-            # in case of a reload
-            return sys.modules[fullname]
-        except KeyError:
-            pass
-        mod = self.__get_module(fullname)
-        if isinstance(mod, MovedModule):
-            mod = mod._resolve()
-        else:
-            mod.__loader__ = self
-        sys.modules[fullname] = mod
-        return mod
-
-    def is_package(self, fullname):
-        """
-        Return true, if the named module is a package.
-
-        We need this method to get correct spec objects with
-        Python 3.4 (see PEP451)
-        """
-        return hasattr(self.__get_module(fullname), "__path__")
-
-    def get_code(self, fullname):
-        """Return None
-
-        Required, if is_package is implemented"""
-        self.__get_module(fullname)  # eventually raises ImportError
-        return None
-    get_source = get_code  # same as get_code
-
-_importer = _SixMetaPathImporter(__name__)
-
-
-class _MovedItems(_LazyModule):
-
-    """Lazy loading of moved objects"""
-    __path__ = []  # mark as package
-
-
-_moved_attributes = [
-    MovedAttribute("cStringIO", "cStringIO", "io", "StringIO"),
-    MovedAttribute("filter", "itertools", "builtins", "ifilter", "filter"),
-    MovedAttribute("filterfalse", "itertools", "itertools", "ifilterfalse", "filterfalse"),
-    MovedAttribute("input", "__builtin__", "builtins", "raw_input", "input"),
-    MovedAttribute("intern", "__builtin__", "sys"),
-    MovedAttribute("map", "itertools", "builtins", "imap", "map"),
-    MovedAttribute("getcwd", "os", "os", "getcwdu", "getcwd"),
-    MovedAttribute("getcwdb", "os", "os", "getcwd", "getcwdb"),
-    MovedAttribute("getoutput", "commands", "subprocess"),
-    MovedAttribute("range", "__builtin__", "builtins", "xrange", "range"),
-    MovedAttribute("reload_module", "__builtin__", "importlib" if PY34 else "imp", "reload"),
-    MovedAttribute("reduce", "__builtin__", "functools"),
-    MovedAttribute("shlex_quote", "pipes", "shlex", "quote"),
-    MovedAttribute("StringIO", "StringIO", "io"),
-    MovedAttribute("UserDict", "UserDict", "collections"),
-    MovedAttribute("UserList", "UserList", "collections"),
-    MovedAttribute("UserString", "UserString", "collections"),
-    MovedAttribute("xrange", "__builtin__", "builtins", "xrange", "range"),
-    MovedAttribute("zip", "itertools", "builtins", "izip", "zip"),
-    MovedAttribute("zip_longest", "itertools", "itertools", "izip_longest", "zip_longest"),
-    MovedModule("builtins", "__builtin__"),
-    MovedModule("configparser", "ConfigParser"),
-    MovedModule("collections_abc", "collections", "collections.abc" if sys.version_info >= (3, 3) else "collections"),
-    MovedModule("copyreg", "copy_reg"),
-    MovedModule("dbm_gnu", "gdbm", "dbm.gnu"),
-    MovedModule("dbm_ndbm", "dbm", "dbm.ndbm"),
-    MovedModule("_dummy_thread", "dummy_thread", "_dummy_thread" if sys.version_info < (3, 9) else "_thread"),
-    MovedModule("http_cookiejar", "cookielib", "http.cookiejar"),
-    MovedModule("http_cookies", "Cookie", "http.cookies"),
-    MovedModule("html_entities", "htmlentitydefs", "html.entities"),
-    MovedModule("html_parser", "HTMLParser", "html.parser"),
-    MovedModule("http_client", "httplib", "http.client"),
-    MovedModule("email_mime_base", "email.MIMEBase", "email.mime.base"),
-    MovedModule("email_mime_image", "email.MIMEImage", "email.mime.image"),
-    MovedModule("email_mime_multipart", "email.MIMEMultipart", "email.mime.multipart"),
-    MovedModule("email_mime_nonmultipart", "email.MIMENonMultipart", "email.mime.nonmultipart"),
-    MovedModule("email_mime_text", "email.MIMEText", "email.mime.text"),
-    MovedModule("BaseHTTPServer", "BaseHTTPServer", "http.server"),
-    MovedModule("CGIHTTPServer", "CGIHTTPServer", "http.server"),
-    MovedModule("SimpleHTTPServer", "SimpleHTTPServer", "http.server"),
-    MovedModule("cPickle", "cPickle", "pickle"),
-    MovedModule("queue", "Queue"),
-    MovedModule("reprlib", "repr"),
-    MovedModule("socketserver", "SocketServer"),
-    MovedModule("_thread", "thread", "_thread"),
-    MovedModule("tkinter", "Tkinter"),
-    MovedModule("tkinter_dialog", "Dialog", "tkinter.dialog"),
-    MovedModule("tkinter_filedialog", "FileDialog", "tkinter.filedialog"),
-    MovedModule("tkinter_scrolledtext", "ScrolledText", "tkinter.scrolledtext"),
-    MovedModule("tkinter_simpledialog", "SimpleDialog", "tkinter.simpledialog"),
-    MovedModule("tkinter_tix", "Tix", "tkinter.tix"),
-    MovedModule("tkinter_ttk", "ttk", "tkinter.ttk"),
-    MovedModule("tkinter_constants", "Tkconstants", "tkinter.constants"),
-    MovedModule("tkinter_dnd", "Tkdnd", "tkinter.dnd"),
-    MovedModule("tkinter_colorchooser", "tkColorChooser",
-                "tkinter.colorchooser"),
-    MovedModule("tkinter_commondialog", "tkCommonDialog",
-                "tkinter.commondialog"),
-    MovedModule("tkinter_tkfiledialog", "tkFileDialog", "tkinter.filedialog"),
-    MovedModule("tkinter_font", "tkFont", "tkinter.font"),
-    MovedModule("tkinter_messagebox", "tkMessageBox", "tkinter.messagebox"),
-    MovedModule("tkinter_tksimpledialog", "tkSimpleDialog",
-                "tkinter.simpledialog"),
-    MovedModule("urllib_parse", __name__ + ".moves.urllib_parse", "urllib.parse"),
-    MovedModule("urllib_error", __name__ + ".moves.urllib_error", "urllib.error"),
-    MovedModule("urllib", __name__ + ".moves.urllib", __name__ + ".moves.urllib"),
-    MovedModule("urllib_robotparser", "robotparser", "urllib.robotparser"),
-    MovedModule("xmlrpc_client", "xmlrpclib", "xmlrpc.client"),
-    MovedModule("xmlrpc_server", "SimpleXMLRPCServer", "xmlrpc.server"),
-]
-# Add windows specific modules.
-if sys.platform == "win32":
-    _moved_attributes += [
-        MovedModule("winreg", "_winreg"),
-    ]
-
-for attr in _moved_attributes:
-    setattr(_MovedItems, attr.name, attr)
-    if isinstance(attr, MovedModule):
-        _importer._add_module(attr, "moves." + attr.name)
-del attr
-
-_MovedItems._moved_attributes = _moved_attributes
-
-moves = _MovedItems(__name__ + ".moves")
-_importer._add_module(moves, "moves")
-
-
-class Module_six_moves_urllib_parse(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_parse"""
-
-
-_urllib_parse_moved_attributes = [
-    MovedAttribute("ParseResult", "urlparse", "urllib.parse"),
-    MovedAttribute("SplitResult", "urlparse", "urllib.parse"),
-    MovedAttribute("parse_qs", "urlparse", "urllib.parse"),
-    MovedAttribute("parse_qsl", "urlparse", "urllib.parse"),
-    MovedAttribute("urldefrag", "urlparse", "urllib.parse"),
-    MovedAttribute("urljoin", "urlparse", "urllib.parse"),
-    MovedAttribute("urlparse", "urlparse", "urllib.parse"),
-    MovedAttribute("urlsplit", "urlparse", "urllib.parse"),
-    MovedAttribute("urlunparse", "urlparse", "urllib.parse"),
-    MovedAttribute("urlunsplit", "urlparse", "urllib.parse"),
-    MovedAttribute("quote", "urllib", "urllib.parse"),
-    MovedAttribute("quote_plus", "urllib", "urllib.parse"),
-    MovedAttribute("unquote", "urllib", "urllib.parse"),
-    MovedAttribute("unquote_plus", "urllib", "urllib.parse"),
-    MovedAttribute("unquote_to_bytes", "urllib", "urllib.parse", "unquote", "unquote_to_bytes"),
-    MovedAttribute("urlencode", "urllib", "urllib.parse"),
-    MovedAttribute("splitquery", "urllib", "urllib.parse"),
-    MovedAttribute("splittag", "urllib", "urllib.parse"),
-    MovedAttribute("splituser", "urllib", "urllib.parse"),
-    MovedAttribute("splitvalue", "urllib", "urllib.parse"),
-    MovedAttribute("uses_fragment", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_netloc", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_params", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_query", "urlparse", "urllib.parse"),
-    MovedAttribute("uses_relative", "urlparse", "urllib.parse"),
-]
-for attr in _urllib_parse_moved_attributes:
-    setattr(Module_six_moves_urllib_parse, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_parse._moved_attributes = _urllib_parse_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_parse(__name__ + ".moves.urllib_parse"),
-                      "moves.urllib_parse", "moves.urllib.parse")
-
-
-class Module_six_moves_urllib_error(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_error"""
-
-
-_urllib_error_moved_attributes = [
-    MovedAttribute("URLError", "urllib2", "urllib.error"),
-    MovedAttribute("HTTPError", "urllib2", "urllib.error"),
-    MovedAttribute("ContentTooShortError", "urllib", "urllib.error"),
-]
-for attr in _urllib_error_moved_attributes:
-    setattr(Module_six_moves_urllib_error, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_error._moved_attributes = _urllib_error_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_error(__name__ + ".moves.urllib.error"),
-                      "moves.urllib_error", "moves.urllib.error")
-
-
-class Module_six_moves_urllib_request(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_request"""
-
-
-_urllib_request_moved_attributes = [
-    MovedAttribute("urlopen", "urllib2", "urllib.request"),
-    MovedAttribute("install_opener", "urllib2", "urllib.request"),
-    MovedAttribute("build_opener", "urllib2", "urllib.request"),
-    MovedAttribute("pathname2url", "urllib", "urllib.request"),
-    MovedAttribute("url2pathname", "urllib", "urllib.request"),
-    MovedAttribute("getproxies", "urllib", "urllib.request"),
-    MovedAttribute("Request", "urllib2", "urllib.request"),
-    MovedAttribute("OpenerDirector", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPDefaultErrorHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPRedirectHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPCookieProcessor", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyHandler", "urllib2", "urllib.request"),
-    MovedAttribute("BaseHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPPasswordMgr", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPPasswordMgrWithDefaultRealm", "urllib2", "urllib.request"),
-    MovedAttribute("AbstractBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyBasicAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("AbstractDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("ProxyDigestAuthHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPSHandler", "urllib2", "urllib.request"),
-    MovedAttribute("FileHandler", "urllib2", "urllib.request"),
-    MovedAttribute("FTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("CacheFTPHandler", "urllib2", "urllib.request"),
-    MovedAttribute("UnknownHandler", "urllib2", "urllib.request"),
-    MovedAttribute("HTTPErrorProcessor", "urllib2", "urllib.request"),
-    MovedAttribute("urlretrieve", "urllib", "urllib.request"),
-    MovedAttribute("urlcleanup", "urllib", "urllib.request"),
-    MovedAttribute("URLopener", "urllib", "urllib.request"),
-    MovedAttribute("FancyURLopener", "urllib", "urllib.request"),
-    MovedAttribute("proxy_bypass", "urllib", "urllib.request"),
-    MovedAttribute("parse_http_list", "urllib2", "urllib.request"),
-    MovedAttribute("parse_keqv_list", "urllib2", "urllib.request"),
-]
-for attr in _urllib_request_moved_attributes:
-    setattr(Module_six_moves_urllib_request, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_request._moved_attributes = _urllib_request_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_request(__name__ + ".moves.urllib.request"),
-                      "moves.urllib_request", "moves.urllib.request")
-
-
-class Module_six_moves_urllib_response(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_response"""
-
-
-_urllib_response_moved_attributes = [
-    MovedAttribute("addbase", "urllib", "urllib.response"),
-    MovedAttribute("addclosehook", "urllib", "urllib.response"),
-    MovedAttribute("addinfo", "urllib", "urllib.response"),
-    MovedAttribute("addinfourl", "urllib", "urllib.response"),
-]
-for attr in _urllib_response_moved_attributes:
-    setattr(Module_six_moves_urllib_response, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_response._moved_attributes = _urllib_response_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_response(__name__ + ".moves.urllib.response"),
-                      "moves.urllib_response", "moves.urllib.response")
-
-
-class Module_six_moves_urllib_robotparser(_LazyModule):
-
-    """Lazy loading of moved objects in six.moves.urllib_robotparser"""
-
-
-_urllib_robotparser_moved_attributes = [
-    MovedAttribute("RobotFileParser", "robotparser", "urllib.robotparser"),
-]
-for attr in _urllib_robotparser_moved_attributes:
-    setattr(Module_six_moves_urllib_robotparser, attr.name, attr)
-del attr
-
-Module_six_moves_urllib_robotparser._moved_attributes = _urllib_robotparser_moved_attributes
-
-_importer._add_module(Module_six_moves_urllib_robotparser(__name__ + ".moves.urllib.robotparser"),
-                      "moves.urllib_robotparser", "moves.urllib.robotparser")
-
-
-class Module_six_moves_urllib(types.ModuleType):
-
-    """Create a six.moves.urllib namespace that resembles the Python 3 namespace"""
-    __path__ = []  # mark as package
-    parse = _importer._get_module("moves.urllib_parse")
-    error = _importer._get_module("moves.urllib_error")
-    request = _importer._get_module("moves.urllib_request")
-    response = _importer._get_module("moves.urllib_response")
-    robotparser = _importer._get_module("moves.urllib_robotparser")
-
-    def __dir__(self):
-        return ['parse', 'error', 'request', 'response', 'robotparser']
-
-_importer._add_module(Module_six_moves_urllib(__name__ + ".moves.urllib"),
-                      "moves.urllib")
-
-
-def add_move(move):
-    """Add an item to six.moves."""
-    setattr(_MovedItems, move.name, move)
-
-
-def remove_move(name):
-    """Remove item from six.moves."""
-    try:
-        delattr(_MovedItems, name)
-    except AttributeError:
-        try:
-            del moves.__dict__[name]
-        except KeyError:
-            raise AttributeError("no such move, %r" % (name,))
-
-
-if PY3:
-    _meth_func = "__func__"
-    _meth_self = "__self__"
-
-    _func_closure = "__closure__"
-    _func_code = "__code__"
-    _func_defaults = "__defaults__"
-    _func_globals = "__globals__"
-else:
-    _meth_func = "im_func"
-    _meth_self = "im_self"
-
-    _func_closure = "func_closure"
-    _func_code = "func_code"
-    _func_defaults = "func_defaults"
-    _func_globals = "func_globals"
-
-
-try:
-    advance_iterator = next
-except NameError:
-    def advance_iterator(it):
-        return it.next()
-next = advance_iterator
-
-
-try:
-    callable = callable
-except NameError:
-    def callable(obj):
-        return any("__call__" in klass.__dict__ for klass in type(obj).__mro__)
-
-
-if PY3:
-    def get_unbound_function(unbound):
-        return unbound
-
-    create_bound_method = types.MethodType
-
-    def create_unbound_method(func, cls):
-        return func
-
-    Iterator = object
-else:
-    def get_unbound_function(unbound):
-        return unbound.im_func
-
-    def create_bound_method(func, obj):
-        return types.MethodType(func, obj, obj.__class__)
-
-    def create_unbound_method(func, cls):
-        return types.MethodType(func, None, cls)
-
-    class Iterator(object):
-
-        def next(self):
-            return type(self).__next__(self)
-
-    callable = callable
-_add_doc(get_unbound_function,
-         """Get the function out of a possibly unbound function""")
-
-
-get_method_function = operator.attrgetter(_meth_func)
-get_method_self = operator.attrgetter(_meth_self)
-get_function_closure = operator.attrgetter(_func_closure)
-get_function_code = operator.attrgetter(_func_code)
-get_function_defaults = operator.attrgetter(_func_defaults)
-get_function_globals = operator.attrgetter(_func_globals)
-
-
-if PY3:
-    def iterkeys(d, **kw):
-        return iter(d.keys(**kw))
-
-    def itervalues(d, **kw):
-        return iter(d.values(**kw))
-
-    def iteritems(d, **kw):
-        return iter(d.items(**kw))
-
-    def iterlists(d, **kw):
-        return iter(d.lists(**kw))
-
-    viewkeys = operator.methodcaller("keys")
-
-    viewvalues = operator.methodcaller("values")
-
-    viewitems = operator.methodcaller("items")
-else:
-    def iterkeys(d, **kw):
-        return d.iterkeys(**kw)
-
-    def itervalues(d, **kw):
-        return d.itervalues(**kw)
-
-    def iteritems(d, **kw):
-        return d.iteritems(**kw)
-
-    def iterlists(d, **kw):
-        return d.iterlists(**kw)
-
-    viewkeys = operator.methodcaller("viewkeys")
-
-    viewvalues = operator.methodcaller("viewvalues")
-
-    viewitems = operator.methodcaller("viewitems")
-
-_add_doc(iterkeys, "Return an iterator over the keys of a dictionary.")
-_add_doc(itervalues, "Return an iterator over the values of a dictionary.")
-_add_doc(iteritems,
-         "Return an iterator over the (key, value) pairs of a dictionary.")
-_add_doc(iterlists,
-         "Return an iterator over the (key, [values]) pairs of a dictionary.")
-
-
-if PY3:
-    def b(s):
-        return s.encode("latin-1")
-
-    def u(s):
-        return s
-    unichr = chr
-    import struct
-    int2byte = struct.Struct(">B").pack
-    del struct
-    byte2int = operator.itemgetter(0)
-    indexbytes = operator.getitem
-    iterbytes = iter
-    import io
-    StringIO = io.StringIO
-    BytesIO = io.BytesIO
-    del io
-    _assertCountEqual = "assertCountEqual"
-    if sys.version_info[1] <= 1:
-        _assertRaisesRegex = "assertRaisesRegexp"
-        _assertRegex = "assertRegexpMatches"
-        _assertNotRegex = "assertNotRegexpMatches"
-    else:
-        _assertRaisesRegex = "assertRaisesRegex"
-        _assertRegex = "assertRegex"
-        _assertNotRegex = "assertNotRegex"
-else:
-    def b(s):
-        return s
-    # Workaround for standalone backslash
-
-    def u(s):
-        return unicode(s.replace(r'\\', r'\\\\'), "unicode_escape")
-    unichr = unichr
-    int2byte = chr
-
-    def byte2int(bs):
-        return ord(bs[0])
-
-    def indexbytes(buf, i):
-        return ord(buf[i])
-    iterbytes = functools.partial(itertools.imap, ord)
-    import StringIO
-    StringIO = BytesIO = StringIO.StringIO
-    _assertCountEqual = "assertItemsEqual"
-    _assertRaisesRegex = "assertRaisesRegexp"
-    _assertRegex = "assertRegexpMatches"
-    _assertNotRegex = "assertNotRegexpMatches"
-_add_doc(b, """Byte literal""")
-_add_doc(u, """Text literal""")
-
-
-def assertCountEqual(self, *args, **kwargs):
-    return getattr(self, _assertCountEqual)(*args, **kwargs)
-
-
-def assertRaisesRegex(self, *args, **kwargs):
-    return getattr(self, _assertRaisesRegex)(*args, **kwargs)
-
-
-def assertRegex(self, *args, **kwargs):
-    return getattr(self, _assertRegex)(*args, **kwargs)
-
-
-def assertNotRegex(self, *args, **kwargs):
-    return getattr(self, _assertNotRegex)(*args, **kwargs)
-
-
-if PY3:
-    exec_ = getattr(moves.builtins, "exec")
-
-    def reraise(tp, value, tb=None):
-        try:
-            if value is None:
-                value = tp()
-            if value.__traceback__ is not tb:
-                raise value.with_traceback(tb)
-            raise value
-        finally:
-            value = None
-            tb = None
-
-else:
-    def exec_(_code_, _globs_=None, _locs_=None):
-        """Execute code in a namespace."""
-        if _globs_ is None:
-            frame = sys._getframe(1)
-            _globs_ = frame.f_globals
-            if _locs_ is None:
-                _locs_ = frame.f_locals
-            del frame
-        elif _locs_ is None:
-            _locs_ = _globs_
-        exec("""exec _code_ in _globs_, _locs_""")
-
-    exec_("""def reraise(tp, value, tb=None):
-    try:
-        raise tp, value, tb
-    finally:
-        tb = None
-""")
-
-
-if sys.version_info[:2] > (3,):
-    exec_("""def raise_from(value, from_value):
-    try:
-        raise value from from_value
-    finally:
-        value = None
-""")
-else:
-    def raise_from(value, from_value):
-        raise value
-
-
-print_ = getattr(moves.builtins, "print", None)
-if print_ is None:
-    def print_(*args, **kwargs):
-        """The new-style print function for Python 2.4 and 2.5."""
-        fp = kwargs.pop("file", sys.stdout)
-        if fp is None:
-            return
-
-        def write(data):
-            if not isinstance(data, basestring):
-                data = str(data)
-            # If the file has an encoding, encode unicode with it.
-            if (isinstance(fp, file) and
-                    isinstance(data, unicode) and
-                    fp.encoding is not None):
-                errors = getattr(fp, "errors", None)
-                if errors is None:
-                    errors = "strict"
-                data = data.encode(fp.encoding, errors)
-            fp.write(data)
-        want_unicode = False
-        sep = kwargs.pop("sep", None)
-        if sep is not None:
-            if isinstance(sep, unicode):
-                want_unicode = True
-            elif not isinstance(sep, str):
-                raise TypeError("sep must be None or a string")
-        end = kwargs.pop("end", None)
-        if end is not None:
-            if isinstance(end, unicode):
-                want_unicode = True
-            elif not isinstance(end, str):
-                raise TypeError("end must be None or a string")
-        if kwargs:
-            raise TypeError("invalid keyword arguments to print()")
-        if not want_unicode:
-            for arg in args:
-                if isinstance(arg, unicode):
-                    want_unicode = True
-                    break
-        if want_unicode:
-            newline = unicode("\n")
-            space = unicode(" ")
-        else:
-            newline = "\n"
-            space = " "
-        if sep is None:
-            sep = space
-        if end is None:
-            end = newline
-        for i, arg in enumerate(args):
-            if i:
-                write(sep)
-            write(arg)
-        write(end)
-if sys.version_info[:2] < (3, 3):
-    _print = print_
-
-    def print_(*args, **kwargs):
-        fp = kwargs.get("file", sys.stdout)
-        flush = kwargs.pop("flush", False)
-        _print(*args, **kwargs)
-        if flush and fp is not None:
-            fp.flush()
-
-_add_doc(reraise, """Reraise an exception.""")
-
-if sys.version_info[0:2] < (3, 4):
-    # This does exactly the same what the :func:`py3:functools.update_wrapper`
-    # function does on Python versions after 3.2. It sets the ``__wrapped__``
-    # attribute on ``wrapper`` object and it doesn't raise an error if any of
-    # the attributes mentioned in ``assigned`` and ``updated`` are missing on
-    # ``wrapped`` object.
-    def _update_wrapper(wrapper, wrapped,
-                        assigned=functools.WRAPPER_ASSIGNMENTS,
-                        updated=functools.WRAPPER_UPDATES):
-        for attr in assigned:
-            try:
-                value = getattr(wrapped, attr)
-            except AttributeError:
-                continue
-            else:
-                setattr(wrapper, attr, value)
-        for attr in updated:
-            getattr(wrapper, attr).update(getattr(wrapped, attr, {}))
-        wrapper.__wrapped__ = wrapped
-        return wrapper
-    _update_wrapper.__doc__ = functools.update_wrapper.__doc__
-
-    def wraps(wrapped, assigned=functools.WRAPPER_ASSIGNMENTS,
-              updated=functools.WRAPPER_UPDATES):
-        return functools.partial(_update_wrapper, wrapped=wrapped,
-                                 assigned=assigned, updated=updated)
-    wraps.__doc__ = functools.wraps.__doc__
-
-else:
-    wraps = functools.wraps
-
-
-def with_metaclass(meta, *bases):
-    """Create a base class with a metaclass."""
-    # This requires a bit of explanation: the basic idea is to make a dummy
-    # metaclass for one level of class instantiation that replaces itself with
-    # the actual metaclass.
-    class metaclass(type):
-
-        def __new__(cls, name, this_bases, d):
-            if sys.version_info[:2] >= (3, 7):
-                # This version introduced PEP 560 that requires a bit
-                # of extra care (we mimic what is done by __build_class__).
-                resolved_bases = types.resolve_bases(bases)
-                if resolved_bases is not bases:
-                    d['__orig_bases__'] = bases
-            else:
-                resolved_bases = bases
-            return meta(name, resolved_bases, d)
-
-        @classmethod
-        def __prepare__(cls, name, this_bases):
-            return meta.__prepare__(name, bases)
-    return type.__new__(metaclass, 'temporary_class', (), {})
-
-
-def add_metaclass(metaclass):
-    """Class decorator for creating a class with a metaclass."""
-    def wrapper(cls):
-        orig_vars = cls.__dict__.copy()
-        slots = orig_vars.get('__slots__')
-        if slots is not None:
-            if isinstance(slots, str):
-                slots = [slots]
-            for slots_var in slots:
-                orig_vars.pop(slots_var)
-        orig_vars.pop('__dict__', None)
-        orig_vars.pop('__weakref__', None)
-        if hasattr(cls, '__qualname__'):
-            orig_vars['__qualname__'] = cls.__qualname__
-        return metaclass(cls.__name__, cls.__bases__, orig_vars)
-    return wrapper
-
-
-def ensure_binary(s, encoding='utf-8', errors='strict'):
-    """Coerce **s** to six.binary_type.
-
-    For Python 2:
-      - `unicode` -> encoded to `str`
-      - `str` -> `str`
-
-    For Python 3:
-      - `str` -> encoded to `bytes`
-      - `bytes` -> `bytes`
-    """
-    if isinstance(s, text_type):
-        return s.encode(encoding, errors)
-    elif isinstance(s, binary_type):
-        return s
-    else:
-        raise TypeError("not expecting type '%s'" % type(s))
-
-
-def ensure_str(s, encoding='utf-8', errors='strict'):
-    """Coerce *s* to `str`.
-
-    For Python 2:
-      - `unicode` -> encoded to `str`
-      - `str` -> `str`
-
-    For Python 3:
-      - `str` -> `str`
-      - `bytes` -> decoded to `str`
-    """
-    if not isinstance(s, (text_type, binary_type)):
-        raise TypeError("not expecting type '%s'" % type(s))
-    if PY2 and isinstance(s, text_type):
-        s = s.encode(encoding, errors)
-    elif PY3 and isinstance(s, binary_type):
-        s = s.decode(encoding, errors)
-    return s
-
-
-def ensure_text(s, encoding='utf-8', errors='strict'):
-    """Coerce *s* to six.text_type.
-
-    For Python 2:
-      - `unicode` -> `unicode`
-      - `str` -> `unicode`
-
-    For Python 3:
-      - `str` -> `str`
-      - `bytes` -> decoded to `str`
-    """
-    if isinstance(s, binary_type):
-        return s.decode(encoding, errors)
-    elif isinstance(s, text_type):
-        return s
-    else:
-        raise TypeError("not expecting type '%s'" % type(s))
-
-
-def python_2_unicode_compatible(klass):
-    """
-    A class decorator that defines __unicode__ and __str__ methods under Python 2.
-    Under Python 3 it does nothing.
-
-    To support Python 2 and 3 with a single code base, define a __str__ method
-    returning text and apply this decorator to the class.
-    """
-    if PY2:
-        if '__str__' not in klass.__dict__:
-            raise ValueError("@python_2_unicode_compatible cannot be applied "
-                             "to %s because it doesn't define __str__()." %
-                             klass.__name__)
-        klass.__unicode__ = klass.__str__
-        klass.__str__ = lambda self: self.__unicode__().encode('utf-8')
-    return klass
-
-
-# Complete the moves implementation.
-# This code is at the end of this module to speed up module loading.
-# Turn this module into a package.
-__path__ = []  # required for PEP 302 and PEP 451
-__package__ = __name__  # see PEP 366 @ReservedAssignment
-if globals().get("__spec__") is not None:
-    __spec__.submodule_search_locations = []  # PEP 451 @UndefinedVariable
-# Remove other six meta path importers, since they cause problems. This can
-# happen if six is removed from sys.modules and then reloaded. (Setuptools does
-# this for some reason.)
-if sys.meta_path:
-    for i, importer in enumerate(sys.meta_path):
-        # Here's some real nastiness: Another "instance" of the six module might
-        # be floating around. Therefore, we can't use isinstance() to check for
-        # the six meta path importer, since the other six instance will have
-        # inserted an importer with different class.
-        if (type(importer).__name__ == "_SixMetaPathImporter" and
-                importer.name == __name__):
-            del sys.meta_path[i]
-            break
-    del i, importer
-# Finally, add the importer to the meta path import hook.
-sys.meta_path.append(_importer)
diff --git a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/INSTALLER b/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/INSTALLER
deleted file mode 100644
index a1b589e..0000000
--- a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/INSTALLER
+++ /dev/null
@@ -1 +0,0 @@
-pip
diff --git a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/LICENSE b/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/LICENSE
deleted file mode 100644
index 2565558..0000000
--- a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/LICENSE
+++ /dev/null
@@ -1,290 +0,0 @@
-Format: https://www.debian.org/doc/packaging-manuals/copyright-format/1.0/
-Upstream-Name: typed-ast
-Source: https://pypi.python.org/pypi/typed-ast
-
-Files: *
-Copyright: © 2016 David Fisher <ddfisher@dropbox.com>
-License: Apache-2.0
-
-Files: *
-Copyright: © 2016 David Fisher <ddfisher@dropbox.com>
-           © 2008 Armin Ronacher
-Comment: The original CPython source is licensed under the
- Python Software Foundation License Version 2
-License: Python
-
-Files: ast27/Parser/spark.py
-Copyright: © 1998-2002 John Aycock
-License: Expat
- Permission is hereby granted, free of charge, to any person obtaining
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- TORT OR OTHERWISE, ARISING FROM, OUT OF OR IN CONNECTION WITH THE
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-
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-License: Apache-2.0
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- PYTHON SOFTWARE FOUNDATION LICENSE VERSION 2
- --------------------------------------------
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- 1. This LICENSE AGREEMENT is between the Python Software Foundation
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- Agreement.
diff --git a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/METADATA b/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/METADATA
deleted file mode 100644
index 4310a0d..0000000
--- a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/METADATA
+++ /dev/null
@@ -1,28 +0,0 @@
-Metadata-Version: 2.1
-Name: typed-ast
-Version: 1.4.1
-Summary: a fork of Python 2 and 3 ast modules with type comment support
-Home-page: https://github.com/python/typed_ast
-Author: David Fisher
-Author-email: UNKNOWN
-License: Apache License 2.0
-Platform: POSIX
-Platform: Windows
-Classifier: Development Status :: 5 - Production/Stable
-Classifier: Environment :: Console
-Classifier: Intended Audience :: Developers
-Classifier: Operating System :: POSIX
-Classifier: Operating System :: Microsoft
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: 3.8
-Classifier: Topic :: Software Development
-
-`typed_ast` is a Python 3 package that provides a Python 2.7 and Python 3
-parser similar to the standard `ast` library.  Unlike `ast`, the parsers in
-`typed_ast` include PEP 484 type comments and are independent of the version of
-Python under which they are run.  The `typed_ast` parsers produce the standard
-Python AST (plus type comments), and are both fast and correct, as they are
-based on the CPython 2.7 and 3.6 parsers.
-
diff --git a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/RECORD b/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/RECORD
deleted file mode 100644
index aec2f89..0000000
--- a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/RECORD
+++ /dev/null
@@ -1,18 +0,0 @@
-typed_ast-1.4.1.dist-info/INSTALLER,sha256=zuuue4knoyJ-UwPPXg8fezS7VCrXJQrAP7zeNuwvFQg,4
-typed_ast-1.4.1.dist-info/LICENSE,sha256=PwfDPiHJOi2_T6I50fxiYmilsIHot5rKO48KR7BQ8Uw,15191
-typed_ast-1.4.1.dist-info/METADATA,sha256=L2YMWfFrFfLLglAbPDeooa2VWjr66S9yx5z2k3cIl1g,1163
-typed_ast-1.4.1.dist-info/RECORD,,
-typed_ast-1.4.1.dist-info/WHEEL,sha256=uaZe_9gV-4T_d4AskuIQkCgcY8wMc0UXsVFnf0_mBGs,106
-typed_ast-1.4.1.dist-info/top_level.txt,sha256=LCmBygYWBo6qqIoaZNicoxU-DO9gR2JvhQkVJwSyN1k,23
-typed_ast/__init__.py,sha256=BqOI5y46o1G1RWC9bF1DPL-YM68lGYPmZt1pn6FZFZs,22
-typed_ast/__pycache__/__init__.cpython-37.pyc,,
-typed_ast/__pycache__/ast27.cpython-37.pyc,,
-typed_ast/__pycache__/ast3.cpython-37.pyc,,
-typed_ast/__pycache__/conversions.cpython-37.pyc,,
-typed_ast/_ast27.cp37-win_amd64.pyd,sha256=Br_xsc8o9mz2WB2f4hjB2DE83vdVi7wpY_a0bnPG1ts,165888
-typed_ast/_ast3.cp37-win_amd64.pyd,sha256=SeQgXupZuH-oJEMKYRSSrzqjNDbi-a834i1q44ATaJo,186368
-typed_ast/ast27.py,sha256=MouNmlSUIINEyl3LBa796DXBvZNOjo5-gCPzoYRDb1Q,12630
-typed_ast/ast3.py,sha256=2Fb_0TUknxmDPzBXPYe1XkGhJL1JxeR2zLivWII3TqI,13761
-typed_ast/conversions.py,sha256=J9wBDCg-it3cxfSnIAMWnBDiwLypfRBc7RTftRImwak,8632
-typed_ast/tests/__pycache__/test_basics.cpython-37.pyc,,
-typed_ast/tests/test_basics.py,sha256=2aQmOXfqKyBNaVpB9FeYkMqSWy9Qz1aGwVCs70IrDKo,7516
diff --git a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/WHEEL b/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/WHEEL
deleted file mode 100644
index c4dd0f9..0000000
--- a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/WHEEL
+++ /dev/null
@@ -1,5 +0,0 @@
-Wheel-Version: 1.0
-Generator: bdist_wheel (0.33.6)
-Root-Is-Purelib: false
-Tag: cp37-cp37m-win_amd64
-
diff --git a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/top_level.txt b/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/top_level.txt
deleted file mode 100644
index 8c96e51..0000000
--- a/venv/Lib/site-packages/typed_ast-1.4.1.dist-info/top_level.txt
+++ /dev/null
@@ -1,3 +0,0 @@
-_ast27
-_ast3
-typed_ast
diff --git a/venv/Lib/site-packages/typed_ast/__init__.py b/venv/Lib/site-packages/typed_ast/__init__.py
deleted file mode 100644
index bf25615..0000000
--- a/venv/Lib/site-packages/typed_ast/__init__.py
+++ /dev/null
@@ -1 +0,0 @@
-__version__ = "1.4.1"
diff --git a/venv/Lib/site-packages/typed_ast/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/typed_ast/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 8d1e8cf..0000000
--- a/venv/Lib/site-packages/typed_ast/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/typed_ast/__pycache__/ast27.cpython-37.pyc b/venv/Lib/site-packages/typed_ast/__pycache__/ast27.cpython-37.pyc
deleted file mode 100644
index bc79e0c..0000000
--- a/venv/Lib/site-packages/typed_ast/__pycache__/ast27.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/typed_ast/__pycache__/ast3.cpython-37.pyc b/venv/Lib/site-packages/typed_ast/__pycache__/ast3.cpython-37.pyc
deleted file mode 100644
index f59503a..0000000
--- a/venv/Lib/site-packages/typed_ast/__pycache__/ast3.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/typed_ast/__pycache__/conversions.cpython-37.pyc b/venv/Lib/site-packages/typed_ast/__pycache__/conversions.cpython-37.pyc
deleted file mode 100644
index b5d2c32..0000000
--- a/venv/Lib/site-packages/typed_ast/__pycache__/conversions.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/typed_ast/_ast27.cp37-win_amd64.pyd b/venv/Lib/site-packages/typed_ast/_ast27.cp37-win_amd64.pyd
deleted file mode 100644
index 1e1b24a..0000000
--- a/venv/Lib/site-packages/typed_ast/_ast27.cp37-win_amd64.pyd
+++ /dev/null
diff --git a/venv/Lib/site-packages/typed_ast/_ast3.cp37-win_amd64.pyd b/venv/Lib/site-packages/typed_ast/_ast3.cp37-win_amd64.pyd
deleted file mode 100644
index acc389b..0000000
--- a/venv/Lib/site-packages/typed_ast/_ast3.cp37-win_amd64.pyd
+++ /dev/null
diff --git a/venv/Lib/site-packages/typed_ast/ast27.py b/venv/Lib/site-packages/typed_ast/ast27.py
deleted file mode 100644
index 4ed7a6c..0000000
--- a/venv/Lib/site-packages/typed_ast/ast27.py
+++ /dev/null
@@ -1,324 +0,0 @@
-# -*- coding: utf-8 -*-
-"""
-    ast27
-    ~~~
-
-    The `ast27` module helps Python applications to process trees of the Python
-    abstract syntax grammar.  The abstract syntax itself might change with
-    each Python release; this module helps to find out programmatically what
-    the current grammar looks like and allows modifications of it.  The `ast27`
-    module is similar to the builtin `ast` module on Python 2.7, except `ast27`
-    runs on Python 3 and provides PEP 484 type comments as part of the AST.
-
-    Specifically, these changes are made to the Python 2.7 AST:
-    - The `FunctionDef`, `Assign`, `For`, and `With` classes all have a
-      `type_comment` field which contains a `str` with the text of the
-      associated type comment, if any.
-    - `arguments` has a `type_comments` list of per-argument type comments.
-    - `parse` has been augmented so it can parse function signature types when
-      called with `mode=func_type`.
-    - `Module` has a `type_ignores` field which contains a list of
-      lines which have been `# type: ignore`d.
-    - `Str` has a `kind` string field which preserves the original string
-      prefix, so that `ast27.parse('br"test"').body[0].value.kind == 'br'`.
-
-    An abstract syntax tree can be generated by using the `parse()`
-    function from this module.  The result will be a tree of objects whose
-    classes all inherit from `ast27.AST`.
-
-    A modified abstract syntax tree can be compiled into a Python code object
-    using the built-in `compile()` function.
-
-    Additionally various helper functions are provided that make working with
-    the trees simpler.  The main intention of the helper functions and this
-    module in general is to provide an easy to use interface for libraries
-    that work tightly with the python syntax (template engines for example).
-
-
-    :copyright: Copyright 2008 by Armin Ronacher.
-    :license: Python License.
-"""
-from typed_ast import _ast27
-from typed_ast._ast27 import *
-
-
-def parse(source, filename='<unknown>', mode='exec'):
-    """
-    Parse the source into an AST node with type comments.
-    Equivalent to compile(source, filename, mode, PyCF_ONLY_AST).
-    """
-    return _ast27.parse(source, filename, mode)
-
-
-def literal_eval(node_or_string):
-    """
-    Safely evaluate an expression node or a string containing a Python
-    expression.  The string or node provided may only consist of the following
-    Python literal structures: strings, numbers, tuples, lists, dicts, booleans,
-    and None.
-    """
-    _safe_names = {'None': None, 'True': True, 'False': False}
-    if isinstance(node_or_string, (str, bytes)):
-        node_or_string = parse(node_or_string, mode='eval')
-    if isinstance(node_or_string, Expression):
-        node_or_string = node_or_string.body
-    def _convert(node):
-        if isinstance(node, Str):
-            return node.s
-        elif isinstance(node, Num):
-            return node.n
-        elif isinstance(node, Tuple):
-            return tuple(map(_convert, node.elts))
-        elif isinstance(node, List):
-            return list(map(_convert, node.elts))
-        elif isinstance(node, Dict):
-            return dict((_convert(k), _convert(v)) for k, v
-                        in zip(node.keys, node.values))
-        elif isinstance(node, Name):
-            if node.id in _safe_names:
-                return _safe_names[node.id]
-        elif isinstance(node, BinOp) and \
-             isinstance(node.op, (Add, Sub)) and \
-             isinstance(node.right, Num) and \
-             isinstance(node.right.n, complex) and \
-             isinstance(node.left, Num) and \
-             isinstance(node.left.n, (int, long, float)):
-            left = node.left.n
-            right = node.right.n
-            if isinstance(node.op, Add):
-                return left + right
-            else:
-                return left - right
-        raise ValueError('malformed string')
-    return _convert(node_or_string)
-
-
-def dump(node, annotate_fields=True, include_attributes=False):
-    """
-    Return a formatted dump of the tree in *node*.  This is mainly useful for
-    debugging purposes.  The returned string will show the names and the values
-    for fields.  This makes the code impossible to evaluate, so if evaluation is
-    wanted *annotate_fields* must be set to False.  Attributes such as line
-    numbers and column offsets are not dumped by default.  If this is wanted,
-    *include_attributes* can be set to True.
-    """
-    def _format(node):
-        if isinstance(node, AST):
-            fields = [(a, _format(b)) for a, b in iter_fields(node)]
-            rv = '%s(%s' % (node.__class__.__name__, ', '.join(
-                ('%s=%s' % field for field in fields)
-                if annotate_fields else
-                (b for a, b in fields)
-            ))
-            if include_attributes and node._attributes:
-                rv += fields and ', ' or ' '
-                rv += ', '.join('%s=%s' % (a, _format(getattr(node, a)))
-                                for a in node._attributes)
-            return rv + ')'
-        elif isinstance(node, list):
-            return '[%s]' % ', '.join(_format(x) for x in node)
-        return repr(node)
-    if not isinstance(node, AST):
-        raise TypeError('expected AST, got %r' % node.__class__.__name__)
-    return _format(node)
-
-
-def copy_location(new_node, old_node):
-    """
-    Copy source location (`lineno` and `col_offset` attributes) from
-    *old_node* to *new_node* if possible, and return *new_node*.
-    """
-    for attr in 'lineno', 'col_offset':
-        if attr in old_node._attributes and attr in new_node._attributes \
-           and hasattr(old_node, attr):
-            setattr(new_node, attr, getattr(old_node, attr))
-    return new_node
-
-
-def fix_missing_locations(node):
-    """
-    When you compile a node tree with compile(), the compiler expects lineno and
-    col_offset attributes for every node that supports them.  This is rather
-    tedious to fill in for generated nodes, so this helper adds these attributes
-    recursively where not already set, by setting them to the values of the
-    parent node.  It works recursively starting at *node*.
-    """
-    def _fix(node, lineno, col_offset):
-        if 'lineno' in node._attributes:
-            if not hasattr(node, 'lineno'):
-                node.lineno = lineno
-            else:
-                lineno = node.lineno
-        if 'col_offset' in node._attributes:
-            if not hasattr(node, 'col_offset'):
-                node.col_offset = col_offset
-            else:
-                col_offset = node.col_offset
-        for child in iter_child_nodes(node):
-            _fix(child, lineno, col_offset)
-    _fix(node, 1, 0)
-    return node
-
-
-def increment_lineno(node, n=1):
-    """
-    Increment the line number of each node in the tree starting at *node* by *n*.
-    This is useful to "move code" to a different location in a file.
-    """
-    for child in walk(node):
-        if 'lineno' in child._attributes:
-            child.lineno = getattr(child, 'lineno', 0) + n
-    return node
-
-
-def iter_fields(node):
-    """
-    Yield a tuple of ``(fieldname, value)`` for each field in ``node._fields``
-    that is present on *node*.
-    """
-    for field in node._fields:
-        try:
-            yield field, getattr(node, field)
-        except AttributeError:
-            pass
-
-
-def iter_child_nodes(node):
-    """
-    Yield all direct child nodes of *node*, that is, all fields that are nodes
-    and all items of fields that are lists of nodes.
-    """
-    for name, field in iter_fields(node):
-        if isinstance(field, AST):
-            yield field
-        elif isinstance(field, list):
-            for item in field:
-                if isinstance(item, AST):
-                    yield item
-
-
-def get_docstring(node, clean=True):
-    """
-    Return the docstring for the given node or None if no docstring can
-    be found.  If the node provided does not have docstrings a TypeError
-    will be raised.
-    """
-    if not isinstance(node, (FunctionDef, ClassDef, Module)):
-        raise TypeError("%r can't have docstrings" % node.__class__.__name__)
-    if node.body and isinstance(node.body[0], Expr) and \
-       isinstance(node.body[0].value, Str):
-        if clean:
-            import inspect
-            return inspect.cleandoc(node.body[0].value.s)
-        return node.body[0].value.s
-
-
-def walk(node):
-    """
-    Recursively yield all descendant nodes in the tree starting at *node*
-    (including *node* itself), in no specified order.  This is useful if you
-    only want to modify nodes in place and don't care about the context.
-    """
-    from collections import deque
-    todo = deque([node])
-    while todo:
-        node = todo.popleft()
-        todo.extend(iter_child_nodes(node))
-        yield node
-
-
-class NodeVisitor(object):
-    """
-    A node visitor base class that walks the abstract syntax tree and calls a
-    visitor function for every node found.  This function may return a value
-    which is forwarded by the `visit` method.
-
-    This class is meant to be subclassed, with the subclass adding visitor
-    methods.
-
-    Per default the visitor functions for the nodes are ``'visit_'`` +
-    class name of the node.  So a `TryFinally` node visit function would
-    be `visit_TryFinally`.  This behavior can be changed by overriding
-    the `visit` method.  If no visitor function exists for a node
-    (return value `None`) the `generic_visit` visitor is used instead.
-
-    Don't use the `NodeVisitor` if you want to apply changes to nodes during
-    traversing.  For this a special visitor exists (`NodeTransformer`) that
-    allows modifications.
-    """
-
-    def visit(self, node):
-        """Visit a node."""
-        method = 'visit_' + node.__class__.__name__
-        visitor = getattr(self, method, self.generic_visit)
-        return visitor(node)
-
-    def generic_visit(self, node):
-        """Called if no explicit visitor function exists for a node."""
-        for field, value in iter_fields(node):
-            if isinstance(value, list):
-                for item in value:
-                    if isinstance(item, AST):
-                        self.visit(item)
-            elif isinstance(value, AST):
-                self.visit(value)
-
-
-class NodeTransformer(NodeVisitor):
-    """
-    A :class:`NodeVisitor` subclass that walks the abstract syntax tree and
-    allows modification of nodes.
-
-    The `NodeTransformer` will walk the AST and use the return value of the
-    visitor methods to replace or remove the old node.  If the return value of
-    the visitor method is ``None``, the node will be removed from its location,
-    otherwise it is replaced with the return value.  The return value may be the
-    original node in which case no replacement takes place.
-
-    Here is an example transformer that rewrites all occurrences of name lookups
-    (``foo``) to ``data['foo']``::
-
-       class RewriteName(NodeTransformer):
-
-           def visit_Name(self, node):
-               return copy_location(Subscript(
-                   value=Name(id='data', ctx=Load()),
-                   slice=Index(value=Str(s=node.id, kind='')),
-                   ctx=node.ctx
-               ), node)
-
-    Keep in mind that if the node you're operating on has child nodes you must
-    either transform the child nodes yourself or call the :meth:`generic_visit`
-    method for the node first.
-
-    For nodes that were part of a collection of statements (that applies to all
-    statement nodes), the visitor may also return a list of nodes rather than
-    just a single node.
-
-    Usually you use the transformer like this::
-
-       node = YourTransformer().visit(node)
-    """
-
-    def generic_visit(self, node):
-        for field, old_value in iter_fields(node):
-            old_value = getattr(node, field, None)
-            if isinstance(old_value, list):
-                new_values = []
-                for value in old_value:
-                    if isinstance(value, AST):
-                        value = self.visit(value)
-                        if value is None:
-                            continue
-                        elif not isinstance(value, AST):
-                            new_values.extend(value)
-                            continue
-                    new_values.append(value)
-                old_value[:] = new_values
-            elif isinstance(old_value, AST):
-                new_node = self.visit(old_value)
-                if new_node is None:
-                    delattr(node, field)
-                else:
-                    setattr(node, field, new_node)
-        return node
diff --git a/venv/Lib/site-packages/typed_ast/ast3.py b/venv/Lib/site-packages/typed_ast/ast3.py
deleted file mode 100644
index 0a8a700..0000000
--- a/venv/Lib/site-packages/typed_ast/ast3.py
+++ /dev/null
@@ -1,348 +0,0 @@
-"""
-    typed_ast.ast3
-    ~~~
-
-    The `ast3` module helps Python applications to process trees of the Python
-    abstract syntax grammar.  The abstract syntax itself might change with
-    each Python release; this module helps to find out programmatically what
-    the current grammar looks like and allows modifications of it.  The
-    difference between the `ast3` module and the builtin `ast` module is
-    that `ast3` is version-independent and provides PEP 484 type comments as
-    part of the AST.
-
-    Specifically, these changes are made to the latest Python 3 AST:
-    - The `FunctionDef`, `AsyncFunctionDef`, `Assign`, `For`, `AsyncFor`,
-      `With`, `AsyncWith`, and `arg` classes all have a `type_comment` field
-      which contains a `str` with the text of the associated type comment, if
-      any.
-    - `parse` has been augmented so it can parse function signature types when
-      called with `mode=func_type`.
-    - `parse` has an additional argument `feature_version`, which disables
-      newer Python syntax features.
-    - `Module` has a `type_ignores` field which contains a list of
-      lines which have been `# type: ignore`d.
-    - `Str` has a `kind` string field which preserves the original string
-      prefix, so that `ast3.parse('u"test"').body[0].value.kind == 'u'`.
-
-    An abstract syntax tree can be generated by using the `parse()`
-    function from this module.  The result will be a tree of objects whose
-    classes all inherit from `ast3.AST`.
-
-    Additionally various helper functions are provided that make working with
-    the trees simpler.  The main intention of the helper functions and this
-    module in general is to provide an easy to use interface for libraries
-    that work tightly with the python syntax (template engines for example).
-
-
-    :copyright: Copyright 2008 by Armin Ronacher.
-    :license: Python License.
-"""
-from typed_ast import _ast3
-from typed_ast._ast3 import *
-
-LATEST_MINOR_VERSION = 7
-
-def parse(source, filename='<unknown>', mode='exec', feature_version=LATEST_MINOR_VERSION):
-    """
-    Parse the source into an AST node including type comments.
-    Similar to compile(source, filename, mode, PyCF_ONLY_AST).
-
-    Set feature_version to limit the syntax parsed to that minor version of
-    Python 3.  For example, feature_version=5 will prevent new syntax features
-    from Python 3.6+ from being used, such as fstrings.  Currently only
-    fully supported for Python 3.5+ with partial support for Python 3.4.
-    So, feature_version=3 or less are all equivalent to feature_version=4.
-
-    When feature_version=4, the parser will forbid the use of the async/await
-    keywords and the '@' operator, but will not forbid the use of PEP 448
-    additional unpacking generalizations, which were also added in Python 3.5.
-
-    When feature_version>=7, 'async' and 'await' are always keywords.
-    """
-    return _ast3._parse(source, filename, mode, feature_version)
-
-_NUM_TYPES = (int, float, complex)
-
-def literal_eval(node_or_string):
-    """
-    Safely evaluate an expression node or a string containing a Python
-    expression.  The string or node provided may only consist of the following
-    Python literal structures: strings, bytes, numbers, tuples, lists, dicts,
-    sets, booleans, and None.
-    """
-    if isinstance(node_or_string, str):
-        node_or_string = parse(node_or_string, mode='eval')
-    if isinstance(node_or_string, Expression):
-        node_or_string = node_or_string.body
-    def _convert(node):
-        if isinstance(node, Constant):
-            return node.value
-        elif isinstance(node, (Str, Bytes)):
-            return node.s
-        elif isinstance(node, Num):
-            return node.n
-        elif isinstance(node, Tuple):
-            return tuple(map(_convert, node.elts))
-        elif isinstance(node, List):
-            return list(map(_convert, node.elts))
-        elif isinstance(node, Set):
-            return set(map(_convert, node.elts))
-        elif isinstance(node, Dict):
-            return dict((_convert(k), _convert(v)) for k, v
-                        in zip(node.keys, node.values))
-        elif isinstance(node, NameConstant):
-            return node.value
-        elif isinstance(node, UnaryOp) and isinstance(node.op, (UAdd, USub)):
-            operand = _convert(node.operand)
-            if isinstance(operand, _NUM_TYPES):
-                if isinstance(node.op, UAdd):
-                    return + operand
-                else:
-                    return - operand
-        elif isinstance(node, BinOp) and isinstance(node.op, (Add, Sub)):
-            left = _convert(node.left)
-            right = _convert(node.right)
-            if isinstance(left, _NUM_TYPES) and isinstance(right, _NUM_TYPES):
-                if isinstance(node.op, Add):
-                    return left + right
-                else:
-                    return left - right
-        raise ValueError('malformed node or string: ' + repr(node))
-    return _convert(node_or_string)
-
-
-def dump(node, annotate_fields=True, include_attributes=False):
-    """
-    Return a formatted dump of the tree in *node*.  This is mainly useful for
-    debugging purposes.  The returned string will show the names and the values
-    for fields.  This makes the code impossible to evaluate, so if evaluation is
-    wanted *annotate_fields* must be set to False.  Attributes such as line
-    numbers and column offsets are not dumped by default.  If this is wanted,
-    *include_attributes* can be set to True.
-    """
-    def _format(node):
-        if isinstance(node, AST):
-            fields = [(a, _format(b)) for a, b in iter_fields(node)]
-            rv = '%s(%s' % (node.__class__.__name__, ', '.join(
-                ('%s=%s' % field for field in fields)
-                if annotate_fields else
-                (b for a, b in fields)
-            ))
-            if include_attributes and node._attributes:
-                rv += fields and ', ' or ' '
-                rv += ', '.join('%s=%s' % (a, _format(getattr(node, a)))
-                                for a in node._attributes)
-            return rv + ')'
-        elif isinstance(node, list):
-            return '[%s]' % ', '.join(_format(x) for x in node)
-        return repr(node)
-    if not isinstance(node, AST):
-        raise TypeError('expected AST, got %r' % node.__class__.__name__)
-    return _format(node)
-
-
-def copy_location(new_node, old_node):
-    """
-    Copy source location (`lineno` and `col_offset` attributes) from
-    *old_node* to *new_node* if possible, and return *new_node*.
-    """
-    for attr in 'lineno', 'col_offset':
-        if attr in old_node._attributes and attr in new_node._attributes \
-           and hasattr(old_node, attr):
-            setattr(new_node, attr, getattr(old_node, attr))
-    return new_node
-
-
-def fix_missing_locations(node):
-    """
-    When you compile a node tree with compile(), the compiler expects lineno and
-    col_offset attributes for every node that supports them.  This is rather
-    tedious to fill in for generated nodes, so this helper adds these attributes
-    recursively where not already set, by setting them to the values of the
-    parent node.  It works recursively starting at *node*.
-    """
-    def _fix(node, lineno, col_offset):
-        if 'lineno' in node._attributes:
-            if not hasattr(node, 'lineno'):
-                node.lineno = lineno
-            else:
-                lineno = node.lineno
-        if 'col_offset' in node._attributes:
-            if not hasattr(node, 'col_offset'):
-                node.col_offset = col_offset
-            else:
-                col_offset = node.col_offset
-        for child in iter_child_nodes(node):
-            _fix(child, lineno, col_offset)
-    _fix(node, 1, 0)
-    return node
-
-
-def increment_lineno(node, n=1):
-    """
-    Increment the line number of each node in the tree starting at *node* by *n*.
-    This is useful to "move code" to a different location in a file.
-    """
-    for child in walk(node):
-        if 'lineno' in child._attributes:
-            child.lineno = getattr(child, 'lineno', 0) + n
-    return node
-
-
-def iter_fields(node):
-    """
-    Yield a tuple of ``(fieldname, value)`` for each field in ``node._fields``
-    that is present on *node*.
-    """
-    for field in node._fields:
-        try:
-            yield field, getattr(node, field)
-        except AttributeError:
-            pass
-
-
-def iter_child_nodes(node):
-    """
-    Yield all direct child nodes of *node*, that is, all fields that are nodes
-    and all items of fields that are lists of nodes.
-    """
-    for name, field in iter_fields(node):
-        if isinstance(field, AST):
-            yield field
-        elif isinstance(field, list):
-            for item in field:
-                if isinstance(item, AST):
-                    yield item
-
-
-def get_docstring(node, clean=True):
-    """
-    Return the docstring for the given node or None if no docstring can
-    be found.  If the node provided does not have docstrings a TypeError
-    will be raised.
-    """
-    if not isinstance(node, (AsyncFunctionDef, FunctionDef, ClassDef, Module)):
-        raise TypeError("%r can't have docstrings" % node.__class__.__name__)
-    if not(node.body and isinstance(node.body[0], Expr)):
-        return
-    node = node.body[0].value
-    if isinstance(node, Str):
-        text = node.s
-    elif isinstance(node, Constant) and isinstance(node.value, str):
-        text = node.value
-    else:
-        return
-    if clean:
-        import inspect
-        text = inspect.cleandoc(text)
-    return text
-
-
-def walk(node):
-    """
-    Recursively yield all descendant nodes in the tree starting at *node*
-    (including *node* itself), in no specified order.  This is useful if you
-    only want to modify nodes in place and don't care about the context.
-    """
-    from collections import deque
-    todo = deque([node])
-    while todo:
-        node = todo.popleft()
-        todo.extend(iter_child_nodes(node))
-        yield node
-
-
-class NodeVisitor(object):
-    """
-    A node visitor base class that walks the abstract syntax tree and calls a
-    visitor function for every node found.  This function may return a value
-    which is forwarded by the `visit` method.
-
-    This class is meant to be subclassed, with the subclass adding visitor
-    methods.
-
-    Per default the visitor functions for the nodes are ``'visit_'`` +
-    class name of the node.  So a `TryFinally` node visit function would
-    be `visit_TryFinally`.  This behavior can be changed by overriding
-    the `visit` method.  If no visitor function exists for a node
-    (return value `None`) the `generic_visit` visitor is used instead.
-
-    Don't use the `NodeVisitor` if you want to apply changes to nodes during
-    traversing.  For this a special visitor exists (`NodeTransformer`) that
-    allows modifications.
-    """
-
-    def visit(self, node):
-        """Visit a node."""
-        method = 'visit_' + node.__class__.__name__
-        visitor = getattr(self, method, self.generic_visit)
-        return visitor(node)
-
-    def generic_visit(self, node):
-        """Called if no explicit visitor function exists for a node."""
-        for field, value in iter_fields(node):
-            if isinstance(value, list):
-                for item in value:
-                    if isinstance(item, AST):
-                        self.visit(item)
-            elif isinstance(value, AST):
-                self.visit(value)
-
-
-class NodeTransformer(NodeVisitor):
-    """
-    A :class:`NodeVisitor` subclass that walks the abstract syntax tree and
-    allows modification of nodes.
-
-    The `NodeTransformer` will walk the AST and use the return value of the
-    visitor methods to replace or remove the old node.  If the return value of
-    the visitor method is ``None``, the node will be removed from its location,
-    otherwise it is replaced with the return value.  The return value may be the
-    original node in which case no replacement takes place.
-
-    Here is an example transformer that rewrites all occurrences of name lookups
-    (``foo``) to ``data['foo']``::
-
-       class RewriteName(NodeTransformer):
-
-           def visit_Name(self, node):
-               return copy_location(Subscript(
-                   value=Name(id='data', ctx=Load()),
-                   slice=Index(value=Str(s=node.id, kind='')),
-                   ctx=node.ctx
-               ), node)
-
-    Keep in mind that if the node you're operating on has child nodes you must
-    either transform the child nodes yourself or call the :meth:`generic_visit`
-    method for the node first.
-
-    For nodes that were part of a collection of statements (that applies to all
-    statement nodes), the visitor may also return a list of nodes rather than
-    just a single node.
-
-    Usually you use the transformer like this::
-
-       node = YourTransformer().visit(node)
-    """
-
-    def generic_visit(self, node):
-        for field, old_value in iter_fields(node):
-            if isinstance(old_value, list):
-                new_values = []
-                for value in old_value:
-                    if isinstance(value, AST):
-                        value = self.visit(value)
-                        if value is None:
-                            continue
-                        elif not isinstance(value, AST):
-                            new_values.extend(value)
-                            continue
-                    new_values.append(value)
-                old_value[:] = new_values
-            elif isinstance(old_value, AST):
-                new_node = self.visit(old_value)
-                if new_node is None:
-                    delattr(node, field)
-                else:
-                    setattr(node, field, new_node)
-        return node
diff --git a/venv/Lib/site-packages/typed_ast/conversions.py b/venv/Lib/site-packages/typed_ast/conversions.py
deleted file mode 100644
index b6862dc..0000000
--- a/venv/Lib/site-packages/typed_ast/conversions.py
+++ /dev/null
@@ -1,232 +0,0 @@
-from typed_ast import ast27
-from typed_ast import ast3
-
-def py2to3(ast):
-    """Converts a typed Python 2.7 ast to a typed Python 3.5 ast.  The returned
-        ast is a valid Python 3 ast with two exceptions:
-
-        - `arg` objects may contain Tuple objects instead of just identifiers
-           in the case of Python 2 function definitions/lambdas that use the tuple
-           unpacking syntax.
-        - `Raise` objects will have a `traceback` attribute added if the 3
-           argument version of the Python 2 raise is used.
-
-
-    Strange and Rare Uncovered Edge Cases:
-        - Raise: if the second argument to a raise statement is a tuple, its
-          contents are unpacked as arguments to the exception constructor.  This
-          case is handled correctly if it's a literal tuple, but not if it's any
-          other sort of tuple expression.
-    """
-    return _AST2To3().visit(ast)
-
-def _copy_attributes(new_value, old_value):
-    attrs = getattr(old_value, '_attributes', None)
-    if attrs is not None:
-        for attr in attrs:
-            setattr(new_value, attr, getattr(old_value, attr))
-    return new_value
-
-class _AST2To3(ast27.NodeTransformer):
-    # note: None, True, and False are *not* translated into NameConstants.
-    def __init__(self):
-        pass
-
-    def visit(self, node):
-        """Visit a node."""
-        method = 'visit_' + node.__class__.__name__
-        visitor = getattr(self, method, self.generic_visit)
-        ret = _copy_attributes(visitor(node), node)
-        return ret
-
-    def maybe_visit(self, node):
-        if node is not None:
-            return self.visit(node)
-        else:
-            return None
-
-    def generic_visit(self, node):
-        class_name = node.__class__.__name__
-        converted_class = getattr(ast3, class_name)
-        new_node = converted_class()
-        for field, old_value in ast27.iter_fields(node):
-            if isinstance(old_value, (ast27.AST, list)):
-                setattr(new_node, field, self.visit(old_value))
-            else:
-                setattr(new_node, field, old_value)
-        return new_node
-
-
-    def visit_list(self, l):
-        return [self.visit(e) if isinstance(e, (ast27.AST, list)) else e for e in l]
-
-    def visit_FunctionDef(self, n):
-        new = self.generic_visit(n)
-        new.returns = None
-        return new
-
-    def visit_ClassDef(self, n):
-        new = self.generic_visit(n)
-        new.keywords = []
-        return new
-
-    def visit_TryExcept(self, n):
-        return ast3.Try(self.visit(n.body),
-                        self.visit(n.handlers),
-                        self.visit(n.orelse),
-                        [])
-
-    def visit_TryFinally(self, n):
-        if len(n.body) == 1 and isinstance(n.body[0], ast27.TryExcept):
-            new = self.visit(n.body[0])
-            new.finalbody = self.visit(n.finalbody)
-            return new
-        else:
-            return ast3.Try(self.visit(n.body),
-                            [],
-                            [],
-                            self.visit(n.finalbody))
-
-
-    def visit_ExceptHandler(self, n):
-        if n.name is None:
-            name = None
-        elif isinstance(n.name, ast27.Name):
-            name = n.name.id
-        else:
-            raise RuntimeError("'{}' has non-Name name.".format(ast27.dump(n)))
-
-        return ast3.ExceptHandler(self.maybe_visit(n.type),
-                                  name,
-                                  self.visit(n.body))
-
-    def visit_Print(self, n):
-        keywords = []
-        if n.dest is not None:
-            keywords.append(ast3.keyword("file", self.visit(n.dest)))
-
-        if not n.nl:
-            keywords.append(ast3.keyword("end",
-                                         ast3.Str(s=" ", kind='', lineno=n.lineno, col_offset=-1)))
-
-        return ast3.Expr(ast3.Call(ast3.Name("print", ast3.Load(), lineno=n.lineno, col_offset=-1),
-                                   self.visit(n.values),
-                                   keywords,
-                                   lineno=n.lineno, col_offset=-1))
-
-    def visit_Raise(self, n):
-        e = None
-        if n.type is not None:
-            e = self.visit(n.type)
-
-            if n.inst is not None and not (isinstance(n.inst, ast27.Name) and n.inst.id == "None"):
-                inst = self.visit(n.inst)
-                if isinstance(inst, ast3.Tuple):
-                    args = inst.elts
-                else:
-                    args = [inst]
-                e = ast3.Call(e, args, [], lineno=e.lineno, col_offset=-1)
-
-        ret = ast3.Raise(e, None)
-        if n.tback is not None:
-            ret.traceback = self.visit(n.tback)
-        return ret
-
-    def visit_Exec(self, n):
-        new_globals = self.maybe_visit(n.globals)
-        if new_globals is None:
-            new_globals = ast3.Name("None", ast3.Load(), lineno=-1, col_offset=-1)
-        new_locals = self.maybe_visit(n.locals)
-        if new_locals is None:
-            new_locals = ast3.Name("None", ast3.Load(), lineno=-1, col_offset=-1)
-
-        return ast3.Expr(ast3.Call(ast3.Name("exec", ast3.Load(), lineno=n.lineno, col_offset=-1),
-                                   [self.visit(n.body), new_globals, new_locals],
-                                   [],
-                                   lineno=n.lineno, col_offset=-1))
-
-    # TODO(ddfisher): the name repr could be used locally as something else; disambiguate
-    def visit_Repr(self, n):
-        return ast3.Call(ast3.Name("repr", ast3.Load(), lineno=n.lineno, col_offset=-1),
-                         [self.visit(n.value)],
-                         [])
-
-    # TODO(ddfisher): this will cause strange behavior on multi-item with statements with type comments
-    def visit_With(self, n):
-        return ast3.With([ast3.withitem(self.visit(n.context_expr), self.maybe_visit(n.optional_vars))],
-                          self.visit(n.body),
-                          n.type_comment)
-
-    def visit_Call(self, n):
-        args = self.visit(n.args)
-        if n.starargs is not None:
-            args.append(ast3.Starred(self.visit(n.starargs), ast3.Load(), lineno=n.starargs.lineno, col_offset=n.starargs.col_offset))
-
-        keywords = self.visit(n.keywords)
-        if n.kwargs is not None:
-            keywords.append(ast3.keyword(None, self.visit(n.kwargs)))
-
-        return ast3.Call(self.visit(n.func),
-                         args,
-                         keywords)
-
-    # TODO(ddfisher): find better attributes to give Ellipses
-    def visit_Ellipsis(self, n):
-        # ellipses in Python 2 only exist as a slice index
-        return ast3.Index(ast3.Ellipsis(lineno=-1, col_offset=-1))
-
-    def visit_arguments(self, n):
-        def convert_arg(arg, type_comment):
-            if isinstance(arg, ast27.Name):
-                v = arg.id
-            elif isinstance(arg, ast27.Tuple):
-                v = self.visit(arg)
-            else:
-                raise RuntimeError("'{}' is not a valid argument.".format(ast27.dump(arg)))
-            return ast3.arg(v, None, type_comment, lineno=arg.lineno, col_offset=arg.col_offset)
-
-        def get_type_comment(i):
-            if i < len(n.type_comments) and n.type_comments[i] is not None:
-                return n.type_comments[i]
-            return None
-
-        args = [convert_arg(arg, get_type_comment(i)) for i, arg in enumerate(n.args)]
-
-        vararg = None
-        if n.vararg is not None:
-            vararg = ast3.arg(n.vararg,
-                              None,
-                              get_type_comment(len(args)),
-                              lineno=-1, col_offset=-1)
-
-        kwarg = None
-        if n.kwarg is not None:
-            kwarg = ast3.arg(n.kwarg,
-                             None,
-                             get_type_comment(len(args) + (0 if n.vararg is None else 1)),
-                             lineno=-1, col_offset=-1)
-
-        defaults = self.visit(n.defaults)
-
-        return ast3.arguments(args,
-                              vararg,
-                              [],
-                              [],
-                              kwarg,
-                              defaults)
-
-    def visit_Str(self, s):
-        if isinstance(s.s, bytes):
-            return ast3.Bytes(s.s, s.kind)
-        else:
-            return ast3.Str(s.s, s.kind)
-
-    def visit_Num(self, n):
-        new = self.generic_visit(n)
-        if new.n < 0:
-            # Python 3 uses a unary - operator for negative literals.
-            new.n = -new.n
-            return ast3.UnaryOp(op=ast3.USub(),
-                                operand=_copy_attributes(new, n))
-        else:
-            return new
diff --git a/venv/Lib/site-packages/typed_ast/tests/__pycache__/test_basics.cpython-37.pyc b/venv/Lib/site-packages/typed_ast/tests/__pycache__/test_basics.cpython-37.pyc
deleted file mode 100644
index 434e554..0000000
--- a/venv/Lib/site-packages/typed_ast/tests/__pycache__/test_basics.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/typed_ast/tests/test_basics.py b/venv/Lib/site-packages/typed_ast/tests/test_basics.py
deleted file mode 100644
index aa240ec..0000000
--- a/venv/Lib/site-packages/typed_ast/tests/test_basics.py
+++ /dev/null
@@ -1,326 +0,0 @@
-import os
-
-import pytest
-
-from typed_ast import _ast3
-from typed_ast import _ast27
-import typed_ast.conversions
-
-# Lowest and highest supported Python 3 minor version (inclusive)
-MIN_VER = 4
-MAX_VER = 7
-NEXT_VER = MAX_VER + 1
-
-
-basics = """\
-def foo():
-    # type: () -> int
-    pass
-
-def bar():  # type: () -> None
-    pass
-"""
-def test_basics():
-    for version in range(MIN_VER, NEXT_VER):
-        tree = _ast3._parse(basics, "<basics>", "exec", version)
-        assert tree.body[0].type_comment == "() -> int"
-        assert tree.body[1].type_comment == "() -> None"
-
-
-redundantdef = """\
-def foo():  # type: () -> int
-    # type: () -> str
-    return ''
-"""
-def test_redundantdef():
-    for version in range(MIN_VER, NEXT_VER):
-        with pytest.raises(SyntaxError):
-            t = _ast3._parse(redundantdef, "<redundantdef>", "exec", version)
-
-
-vardecl = """\
-a = 0  # type: int
-a  # type: int
-"""
-def test_vardecl():
-    for version in range(MIN_VER, NEXT_VER):
-        tree = _ast3._parse(vardecl, "<vardecl>", "exec", version)
-        assert tree.body[0].type_comment == "int"
-        # Curious fact: an expression can have a type comment
-        # but it is lost in the AST.
-
-
-forstmt = """\
-for a in []:  # type: int
-    pass
-"""
-def test_forstmt():
-    for version in range(MIN_VER, NEXT_VER):
-        tree = _ast3._parse(forstmt, "<forstmt>", "exec", version)
-        assert tree.body[0].type_comment == "int"
-
-
-withstmt = """\
-with context():  # type: int
-    pass
-"""
-def test_withstmt():
-    for version in range(MIN_VER, NEXT_VER):
-        tree = _ast3._parse(withstmt, "<withstmt>", "exec", version)
-        assert tree.body[0].type_comment == "int"
-
-
-# A test function named 'fabvk' would have two positional args, a and b,
-# plus a var-arg *v, plus a kw-arg **k.  It is verified in test_longargs()
-# that it has exactly these arguments, no more, no fewer.
-longargs = """\
-def fa(
-    a = 1,  # type: A
-):
-    pass
-
-def fa(
-    a = 1  # type: A
-):
-    pass
-
-def fab(
-    a,  # type: A
-    b,  # type: B
-):
-    pass
-
-def fab(
-    a,  # type: A
-    b  # type: B
-):
-    pass
-
-def fv(
-    *v,  # type: V
-):
-    pass
-
-def fv(
-    *v  # type: V
-):
-    pass
-
-def fk(
-    **k,  # type: K
-):
-    pass
-
-def fk(
-    **k  # type: K
-):
-    pass
-
-def fvk(
-    *v,  # type: V
-    **k,  # type: K
-):
-    pass
-
-def fvk(
-    *v,  # type: V
-    **k  # type: K
-):
-    pass
-
-def fav(
-    a,  # type: A
-    *v,  # type: V
-):
-    pass
-
-def fav(
-    a,  # type: A
-    *v  # type: V
-):
-    pass
-
-def fak(
-    a,  # type: A
-    **k,  # type: K
-):
-    pass
-
-def fak(
-    a,  # type: A
-    **k  # type: K
-):
-    pass
-
-def favk(
-    a,  # type: A
-    *v,  # type: V
-    **k,  # type: K
-):
-    pass
-
-def favk(
-    a,  # type: A
-    *v,  # type: V
-    **k  # type: K
-):
-    pass
-
-"""
-def test_longargs():
-    for version in range(MIN_VER, NEXT_VER):
-        tree = _ast3._parse(longargs, "<longargs>", "exec", version)
-        for t in tree.body:
-            # The expected args are encoded in the function name
-            todo = set(t.name[1:])
-            assert len(t.args.args) == len(todo) - bool(t.args.vararg) - bool(t.args.kwarg)
-            assert t.name.startswith('f')
-            for c in t.name[1:]:
-                todo.remove(c)
-                if c == 'v':
-                    arg = t.args.vararg
-                elif c == 'k':
-                    arg = t.args.kwarg
-                else:
-                    assert 0 <= ord(c) - ord('a') < len(t.args.args)
-                    arg = t.args.args[ord(c) - ord('a')]
-                assert arg.arg == c  # That's the argument name
-                assert arg.type_comment == arg.arg.upper()
-            assert not todo
-
-
-ignores = """\
-def foo():
-    pass  # type: ignore
-
-def bar():
-    x = 1  # type: ignore
-
-def baz():
-    pass  # type: ignore[excuse]
-    pass  # type: ignore=excuse
-    pass  # type: ignore [excuse]
-    x = 1  # type: ignore whatever
-"""
-def test_ignores():
-    expected = [
-        (2, ''),
-        (5, ''),
-        (8, '[excuse]'),
-        (9, '=excuse'),
-        (10, ' [excuse]'),
-        (11, ' whatever'),
-    ]
-
-    for version in range(MIN_VER, NEXT_VER):
-        tree = _ast3._parse(ignores, "<ignores>", "exec", version)
-        assert [(ti.lineno, ti.tag) for ti in tree.type_ignores] == expected
-        with pytest.raises(SyntaxError):
-            _ast3._parse("pass  # type: ignoreé\n", "<ignores>", "exec", version)
-
-
-    tree = _ast27.parse(ignores, "<ignores>", "exec")
-    assert [(ti.lineno, ti.tag) for ti in tree.type_ignores] == expected
-    with pytest.raises(SyntaxError):
-        _ast27.parse("pass  # type: ignoreé\n", "<ignores>", "exec")
-
-
-
-asyncfunc = """\
-async def foo():
-    # type: () -> int
-    return await bar()
-"""
-def test_asyncfunc():
-    for version in range(3, 5):
-        with pytest.raises(SyntaxError):
-            _ast3._parse(asyncfunc, "<asyncfunc>", "exec", version)
-    for version in range(5, NEXT_VER):
-        tree = _ast3._parse(asyncfunc, "<asyncfunc>", "exec", version)
-        assert tree.body[0].type_comment == "() -> int"
-
-
-asyncvar = """\
-async = 12
-await = 13
-"""
-def test_asyncvar():
-    for version in range(3, 7):
-        tree = _ast3._parse(asyncvar, "<asyncvar>", "exec", version)
-    for version in range(7, NEXT_VER):
-        with pytest.raises(SyntaxError):
-            _ast3._parse(asyncvar, "<asyncvar>", "exec", version)
-
-
-asynccomp = """\
-async def foo(xs):
-    [x async for x in xs]
-"""
-def test_asynccomp():
-    for version in range(3, 6):
-        with pytest.raises(SyntaxError):
-            tree = _ast3._parse(asynccomp, "<asynccomp>", "exec", version)
-    for version in range(6, NEXT_VER):
-            _ast3._parse(asynccomp, "<asynccomp>", "exec", version)
-
-
-matmul = """\
-a = b @ c
-"""
-def test_matmul():
-    for version in range(3, 5):
-        with pytest.raises(SyntaxError):
-            tree = _ast3._parse(matmul, "<matmul>", "exec", version)
-    for version in range(5, NEXT_VER):
-        tree = _ast3._parse(matmul, "<matmul>", "exec", version)
-
-
-strkind = """\
-plain = 'abc'
-raw = r'abc'
-plain_bytes = b'abc'
-raw_bytes = br'abc'
-"""
-def test_strkind():
-    # Test that Str() objects have a kind argument/attribute.
-    node = _ast3.Str("foo", "r")
-    assert node.s == "foo"
-    assert node.kind == "r"
-    for version in range(MIN_VER, NEXT_VER):
-        tree = _ast3._parse(strkind, "<strkind>", "exec", version)
-        assert tree.body[0].value.kind == ""
-        assert tree.body[1].value.kind == "r"
-        assert tree.body[2].value.kind == "b"
-        assert tree.body[3].value.kind == "br"
-
-
-basic_py2 = """\
-a = 'hello'
-b = u'hello'
-c = b'hello'
-"""
-def test_convert_strs():
-    ast = _ast27.parse(basic_py2, "<basic_py2>", "exec")
-    tree = typed_ast.conversions.py2to3(ast)
-    assert tree.body[0].value.kind == ""
-    assert tree.body[1].value.kind == "u"
-    assert tree.body[2].value.kind == "b"
-
-simple_fstring = """\
-f'{5}'
-"""
-def test_simple_fstring():
-    for version in range(6, NEXT_VER):
-        tree = _ast3._parse(simple_fstring, "<fstring>", "exec", version)
-        assert isinstance(tree.body[0].value, _ast3.JoinedStr)
-        assert isinstance(tree.body[0].value.values[0].value, _ast3.Num)
-
-# Test the interaction between versions and f strings
-await_fstring = """\
-f'1 + {f"{await}"}'
-"""
-def test_await_fstring():
-    # Should work on 6 but fail on 7
-    _ast3._parse(await_fstring, "<bad-f-string>", "exec", 6)
-    with pytest.raises(SyntaxError):
-        _ast3._parse(await_fstring, "<bad-f-string>", "exec", 7)
diff --git a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/PKG-INFO b/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/PKG-INFO
deleted file mode 100644
index 7e42ef0..0000000
--- a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/PKG-INFO
+++ /dev/null
@@ -1,166 +0,0 @@
-Metadata-Version: 1.1
-Name: wrapt
-Version: 1.11.2
-Summary: Module for decorators, wrappers and monkey patching.
-Home-page: https://github.com/GrahamDumpleton/wrapt
-Author: Graham Dumpleton
-Author-email: Graham.Dumpleton@gmail.com
-License: BSD
-Description: wrapt
-        =====
-        
-        |Travis| |AppVeyor| |Coveralls| |PyPI|
-        
-        The aim of the **wrapt** module is to provide a transparent object proxy
-        for Python, which can be used as the basis for the construction of function
-        wrappers and decorator functions.
-        
-        The **wrapt** module focuses very much on correctness. It therefore goes
-        way beyond existing mechanisms such as ``functools.wraps()`` to ensure that
-        decorators preserve introspectability, signatures, type checking abilities
-        etc. The decorators that can be constructed using this module will work in
-        far more scenarios than typical decorators and provide more predictable and
-        consistent behaviour.
-        
-        To ensure that the overhead is as minimal as possible, a C extension module
-        is used for performance critical components. An automatic fallback to a
-        pure Python implementation is also provided where a target system does not
-        have a compiler to allow the C extension to be compiled.
-        
-        Documentation
-        -------------
-        
-        For further information on the **wrapt** module see:
-        
-        * http://wrapt.readthedocs.org/
-        
-        Quick Start
-        -----------
-        
-        To implement your decorator you need to first define a wrapper function.
-        This will be called each time a decorated function is called. The wrapper
-        function needs to take four positional arguments:
-        
-        * ``wrapped`` - The wrapped function which in turns needs to be called by your wrapper function.
-        * ``instance`` - The object to which the wrapped function was bound when it was called.
-        * ``args`` - The list of positional arguments supplied when the decorated function was called.
-        * ``kwargs`` - The dictionary of keyword arguments supplied when the decorated function was called.
-        
-        The wrapper function would do whatever it needs to, but would usually in
-        turn call the wrapped function that is passed in via the ``wrapped``
-        argument.
-        
-        The decorator ``@wrapt.decorator`` then needs to be applied to the wrapper
-        function to convert it into a decorator which can in turn be applied to
-        other functions.
-        
-        ::
-        
-            import wrapt
-            
-            @wrapt.decorator
-            def pass_through(wrapped, instance, args, kwargs):
-                return wrapped(*args, **kwargs)
-        
-            @pass_through
-            def function():
-                pass
-        
-        If you wish to implement a decorator which accepts arguments, then wrap the
-        definition of the decorator in a function closure. Any arguments supplied
-        to the outer function when the decorator is applied, will be available to
-        the inner wrapper when the wrapped function is called.
-        
-        ::
-        
-            import wrapt
-        
-            def with_arguments(myarg1, myarg2):
-                @wrapt.decorator
-                def wrapper(wrapped, instance, args, kwargs):
-                    return wrapped(*args, **kwargs)
-                return wrapper
-        
-            @with_arguments(1, 2)
-            def function():
-                pass
-        
-        When applied to a normal function or static method, the wrapper function
-        when called will be passed ``None`` as the ``instance`` argument.
-        
-        When applied to an instance method, the wrapper function when called will
-        be passed the instance of the class the method is being called on as the
-        ``instance`` argument. This will be the case even when the instance method
-        was called explicitly via the class and the instance passed as the first
-        argument. That is, the instance will never be passed as part of ``args``.
-        
-        When applied to a class method, the wrapper function when called will be
-        passed the class type as the ``instance`` argument.
-        
-        When applied to a class, the wrapper function when called will be passed
-        ``None`` as the ``instance`` argument. The ``wrapped`` argument in this
-        case will be the class.
-        
-        The above rules can be summarised with the following example.
-        
-        ::
-        
-            import inspect
-            
-            @wrapt.decorator
-            def universal(wrapped, instance, args, kwargs):
-                if instance is None:
-                    if inspect.isclass(wrapped):
-                        # Decorator was applied to a class.
-                        return wrapped(*args, **kwargs)
-                    else:
-                        # Decorator was applied to a function or staticmethod.
-                        return wrapped(*args, **kwargs)
-                else:
-                    if inspect.isclass(instance):
-                        # Decorator was applied to a classmethod.
-                        return wrapped(*args, **kwargs)
-                    else:
-                        # Decorator was applied to an instancemethod.
-                        return wrapped(*args, **kwargs)
-        
-        Using these checks it is therefore possible to create a universal decorator
-        that can be applied in all situations. It is no longer necessary to create
-        different variants of decorators for normal functions and instance methods,
-        or use additional wrappers to convert a function decorator into one that
-        will work for instance methods.
-        
-        In all cases, the wrapped function passed to the wrapper function is called
-        in the same way, with ``args`` and ``kwargs`` being passed. The
-        ``instance`` argument doesn't need to be used in calling the wrapped
-        function.
-        
-        Repository
-        ----------
-        
-        Full source code for the **wrapt** module, including documentation files
-        and unit tests, can be obtained from github.
-        
-        * https://github.com/GrahamDumpleton/wrapt
-        
-        .. |Travis| image:: https://travis-ci.org/GrahamDumpleton/wrapt.svg?branch=develop
-           :target: https://travis-ci.org/GrahamDumpleton/wrapt
-        .. |Appveyor| image:: https://ci.appveyor.com/api/projects/status/32r7s2skrgm9ubva?svg=true
-           :target: https://ci.appveyor.com/project/GrahamDumpleton/wrapt/branch/develop
-        .. |Coveralls| image:: https://img.shields.io/coveralls/GrahamDumpleton/wrapt/develop.svg
-           :target: https://coveralls.io/github/GrahamDumpleton/wrapt?branch=develop
-        .. |PyPI| image:: https://img.shields.io/pypi/v/wrapt.svg
-           :target: https://pypi.python.org/pypi/wrapt
-        
-Platform: UNKNOWN
-Classifier: Development Status :: 5 - Production/Stable
-Classifier: License :: OSI Approved :: BSD License
-Classifier: Programming Language :: Python :: 2
-Classifier: Programming Language :: Python :: 2.7
-Classifier: Programming Language :: Python :: 3
-Classifier: Programming Language :: Python :: 3.4
-Classifier: Programming Language :: Python :: 3.5
-Classifier: Programming Language :: Python :: 3.6
-Classifier: Programming Language :: Python :: 3.7
-Classifier: Programming Language :: Python :: Implementation :: CPython
-Classifier: Programming Language :: Python :: Implementation :: PyPy
diff --git a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/SOURCES.txt b/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/SOURCES.txt
deleted file mode 100644
index 3bc59f3..0000000
--- a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/SOURCES.txt
+++ /dev/null
@@ -1,10 +0,0 @@
-README.rst
-setup.py
-src/wrapt/__init__.py
-src/wrapt/decorators.py
-src/wrapt/importer.py
-src/wrapt/wrappers.py
-src/wrapt.egg-info/PKG-INFO
-src/wrapt.egg-info/SOURCES.txt
-src/wrapt.egg-info/dependency_links.txt
-src/wrapt.egg-info/top_level.txt
\ No newline at end of file
diff --git a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/dependency_links.txt b/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/dependency_links.txt
deleted file mode 100644
index 8b13789..0000000
--- a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/dependency_links.txt
+++ /dev/null
@@ -1 +0,0 @@
-
diff --git a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/installed-files.txt b/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/installed-files.txt
deleted file mode 100644
index 1bc0573..0000000
--- a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/installed-files.txt
+++ /dev/null
@@ -1,12 +0,0 @@
-..\wrapt\__init__.py
-..\wrapt\__pycache__\__init__.cpython-37.pyc
-..\wrapt\__pycache__\decorators.cpython-37.pyc
-..\wrapt\__pycache__\importer.cpython-37.pyc
-..\wrapt\__pycache__\wrappers.cpython-37.pyc
-..\wrapt\decorators.py
-..\wrapt\importer.py
-..\wrapt\wrappers.py
-PKG-INFO
-SOURCES.txt
-dependency_links.txt
-top_level.txt
diff --git a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/top_level.txt b/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/top_level.txt
deleted file mode 100644
index ba11553..0000000
--- a/venv/Lib/site-packages/wrapt-1.11.2-py3.7.egg-info/top_level.txt
+++ /dev/null
@@ -1 +0,0 @@
-wrapt
diff --git a/venv/Lib/site-packages/wrapt/__init__.py b/venv/Lib/site-packages/wrapt/__init__.py
deleted file mode 100644
index 8e858a0..0000000
--- a/venv/Lib/site-packages/wrapt/__init__.py
+++ /dev/null
@@ -1,16 +0,0 @@
-__version_info__ = ('1', '11', '2')
-__version__ = '.'.join(__version_info__)
-
-from .wrappers import (ObjectProxy, CallableObjectProxy, FunctionWrapper,
-        BoundFunctionWrapper, WeakFunctionProxy, PartialCallableObjectProxy,
-        resolve_path, apply_patch, wrap_object, wrap_object_attribute,
-        function_wrapper, wrap_function_wrapper, patch_function_wrapper,
-        transient_function_wrapper)
-
-from .decorators import (adapter_factory, AdapterFactory, decorator,
-        synchronized)
-
-from .importer import (register_post_import_hook, when_imported,
-        notify_module_loaded, discover_post_import_hooks)
-
-from inspect import getcallargs
diff --git a/venv/Lib/site-packages/wrapt/__pycache__/__init__.cpython-37.pyc b/venv/Lib/site-packages/wrapt/__pycache__/__init__.cpython-37.pyc
deleted file mode 100644
index 2e30dcf..0000000
--- a/venv/Lib/site-packages/wrapt/__pycache__/__init__.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/wrapt/__pycache__/decorators.cpython-37.pyc b/venv/Lib/site-packages/wrapt/__pycache__/decorators.cpython-37.pyc
deleted file mode 100644
index aee61e9..0000000
--- a/venv/Lib/site-packages/wrapt/__pycache__/decorators.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/wrapt/__pycache__/importer.cpython-37.pyc b/venv/Lib/site-packages/wrapt/__pycache__/importer.cpython-37.pyc
deleted file mode 100644
index d468b2d..0000000
--- a/venv/Lib/site-packages/wrapt/__pycache__/importer.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/wrapt/__pycache__/wrappers.cpython-37.pyc b/venv/Lib/site-packages/wrapt/__pycache__/wrappers.cpython-37.pyc
deleted file mode 100644
index c21924d..0000000
--- a/venv/Lib/site-packages/wrapt/__pycache__/wrappers.cpython-37.pyc
+++ /dev/null
diff --git a/venv/Lib/site-packages/wrapt/decorators.py b/venv/Lib/site-packages/wrapt/decorators.py
deleted file mode 100644
index 11e11de..0000000
--- a/venv/Lib/site-packages/wrapt/decorators.py
+++ /dev/null
@@ -1,514 +0,0 @@
-"""This module implements decorators for implementing other decorators
-as well as some commonly used decorators.
-
-"""
-
-import sys
-
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-
-if PY3:
-    string_types = str,
-
-    import builtins
-    exec_ = getattr(builtins, "exec")
-    del builtins
-
-else:
-    string_types = basestring,
-
-    def exec_(_code_, _globs_=None, _locs_=None):
-        """Execute code in a namespace."""
-        if _globs_ is None:
-            frame = sys._getframe(1)
-            _globs_ = frame.f_globals
-            if _locs_ is None:
-                _locs_ = frame.f_locals
-            del frame
-        elif _locs_ is None:
-            _locs_ = _globs_
-        exec("""exec _code_ in _globs_, _locs_""")
-
-from functools import partial
-from inspect import ismethod, isclass, formatargspec
-from collections import namedtuple
-from threading import Lock, RLock
-
-try:
-    from inspect import signature
-except ImportError:
-    pass
-
-from .wrappers import (FunctionWrapper, BoundFunctionWrapper, ObjectProxy,
-    CallableObjectProxy)
-
-# Adapter wrapper for the wrapped function which will overlay certain
-# properties from the adapter function onto the wrapped function so that
-# functions such as inspect.getargspec(), inspect.getfullargspec(),
-# inspect.signature() and inspect.getsource() return the correct results
-# one would expect.
-
-class _AdapterFunctionCode(CallableObjectProxy):
-
-    def __init__(self, wrapped_code, adapter_code):
-        super(_AdapterFunctionCode, self).__init__(wrapped_code)
-        self._self_adapter_code = adapter_code
-
-    @property
-    def co_argcount(self):
-        return self._self_adapter_code.co_argcount
-
-    @property
-    def co_code(self):
-        return self._self_adapter_code.co_code
-
-    @property
-    def co_flags(self):
-        return self._self_adapter_code.co_flags
-
-    @property
-    def co_kwonlyargcount(self):
-        return self._self_adapter_code.co_kwonlyargcount
-
-    @property
-    def co_varnames(self):
-        return self._self_adapter_code.co_varnames
-
-class _AdapterFunctionSurrogate(CallableObjectProxy):
-
-    def __init__(self, wrapped, adapter):
-        super(_AdapterFunctionSurrogate, self).__init__(wrapped)
-        self._self_adapter = adapter
-
-    @property
-    def __code__(self):
-        return _AdapterFunctionCode(self.__wrapped__.__code__,
-                self._self_adapter.__code__)
-
-    @property
-    def __defaults__(self):
-        return self._self_adapter.__defaults__
-
-    @property
-    def __kwdefaults__(self):
-        return self._self_adapter.__kwdefaults__
-
-    @property
-    def __signature__(self):
-        if 'signature' not in globals():
-            return self._self_adapter.__signature__
-        else:
-            # Can't allow this to fail on Python 3 else it falls
-            # through to using __wrapped__, but that will be the
-            # wrong function we want to derive the signature
-            # from. Thus generate the signature ourselves.
-
-            return signature(self._self_adapter)
-
-    if PY2:
-        func_code = __code__
-        func_defaults = __defaults__
-
-class _BoundAdapterWrapper(BoundFunctionWrapper):
-
-    @property
-    def __func__(self):
-        return _AdapterFunctionSurrogate(self.__wrapped__.__func__,
-                self._self_parent._self_adapter)
-
-    if PY2:
-        im_func = __func__
-
-class AdapterWrapper(FunctionWrapper):
-
-    __bound_function_wrapper__ = _BoundAdapterWrapper
-
-    def __init__(self, *args, **kwargs):
-        adapter = kwargs.pop('adapter')
-        super(AdapterWrapper, self).__init__(*args, **kwargs)
-        self._self_surrogate = _AdapterFunctionSurrogate(
-                self.__wrapped__, adapter)
-        self._self_adapter = adapter
-
-    @property
-    def __code__(self):
-        return self._self_surrogate.__code__
-
-    @property
-    def __defaults__(self):
-        return self._self_surrogate.__defaults__
-
-    @property
-    def __kwdefaults__(self):
-        return self._self_surrogate.__kwdefaults__
-
-    if PY2:
-        func_code = __code__
-        func_defaults = __defaults__
-
-    @property
-    def __signature__(self):
-        return self._self_surrogate.__signature__
-
-class AdapterFactory(object):
-    def __call__(self, wrapped):
-        raise NotImplementedError()
-
-class DelegatedAdapterFactory(AdapterFactory):
-    def __init__(self, factory):
-        super(DelegatedAdapterFactory, self).__init__()
-        self.factory = factory
-    def __call__(self, wrapped):
-        return self.factory(wrapped)
-
-adapter_factory = DelegatedAdapterFactory
-
-# Decorator for creating other decorators. This decorator and the
-# wrappers which they use are designed to properly preserve any name
-# attributes, function signatures etc, in addition to the wrappers
-# themselves acting like a transparent proxy for the original wrapped
-# function so the wrapper is effectively indistinguishable from the
-# original wrapped function.
-
-def decorator(wrapper=None, enabled=None, adapter=None):
-    # The decorator should be supplied with a single positional argument
-    # which is the wrapper function to be used to implement the
-    # decorator. This may be preceded by a step whereby the keyword
-    # arguments are supplied to customise the behaviour of the
-    # decorator. The 'adapter' argument is used to optionally denote a
-    # separate function which is notionally used by an adapter
-    # decorator. In that case parts of the function '__code__' and
-    # '__defaults__' attributes are used from the adapter function
-    # rather than those of the wrapped function. This allows for the
-    # argument specification from inspect.getargspec() and similar
-    # functions to be overridden with a prototype for a different
-    # function than what was wrapped. The 'enabled' argument provides a
-    # way to enable/disable the use of the decorator. If the type of
-    # 'enabled' is a boolean, then it is evaluated immediately and the
-    # wrapper not even applied if it is False. If not a boolean, it will
-    # be evaluated when the wrapper is called for an unbound wrapper,
-    # and when binding occurs for a bound wrapper. When being evaluated,
-    # if 'enabled' is callable it will be called to obtain the value to
-    # be checked. If False, the wrapper will not be called and instead
-    # the original wrapped function will be called directly instead.
-
-    if wrapper is not None:
-        # Helper function for creating wrapper of the appropriate
-        # time when we need it down below.
-
-        def _build(wrapped, wrapper, enabled=None, adapter=None):
-            if adapter:
-                if isinstance(adapter, AdapterFactory):
-                    adapter = adapter(wrapped)
-
-                if not callable(adapter):
-                    ns = {}
-                    if not isinstance(adapter, string_types):
-                        adapter = formatargspec(*adapter)
-                    exec_('def adapter{}: pass'.format(adapter), ns, ns)
-                    adapter = ns['adapter']
-
-                return AdapterWrapper(wrapped=wrapped, wrapper=wrapper,
-                        enabled=enabled, adapter=adapter)
-
-            return FunctionWrapper(wrapped=wrapped, wrapper=wrapper,
-                    enabled=enabled)
-
-        # The wrapper has been provided so return the final decorator.
-        # The decorator is itself one of our function wrappers so we
-        # can determine when it is applied to functions, instance methods
-        # or class methods. This allows us to bind the instance or class
-        # method so the appropriate self or cls attribute is supplied
-        # when it is finally called.
-
-        def _wrapper(wrapped, instance, args, kwargs):
-            # We first check for the case where the decorator was applied
-            # to a class type.
-            #
-            #     @decorator
-            #     class mydecoratorclass(object):
-            #         def __init__(self, arg=None):
-            #             self.arg = arg
-            #         def __call__(self, wrapped, instance, args, kwargs):
-            #             return wrapped(*args, **kwargs)
-            #
-            #     @mydecoratorclass(arg=1)
-            #     def function():
-            #         pass
-            #
-            # In this case an instance of the class is to be used as the
-            # decorator wrapper function. If args was empty at this point,
-            # then it means that there were optional keyword arguments
-            # supplied to be used when creating an instance of the class
-            # to be used as the wrapper function.
-
-            if instance is None and isclass(wrapped) and not args:
-                # We still need to be passed the target function to be
-                # wrapped as yet, so we need to return a further function
-                # to be able to capture it.
-
-                def _capture(target_wrapped):
-                    # Now have the target function to be wrapped and need
-                    # to create an instance of the class which is to act
-                    # as the decorator wrapper function. Before we do that,
-                    # we need to first check that use of the decorator
-                    # hadn't been disabled by a simple boolean. If it was,
-                    # the target function to be wrapped is returned instead.
-
-                    _enabled = enabled
-                    if type(_enabled) is bool:
-                        if not _enabled:
-                            return target_wrapped
-                        _enabled = None
-
-                    # Now create an instance of the class which is to act
-                    # as the decorator wrapper function. Any arguments had
-                    # to be supplied as keyword only arguments so that is
-                    # all we pass when creating it.
-
-                    target_wrapper = wrapped(**kwargs)
-
-                    # Finally build the wrapper itself and return it.
-
-                    return _build(target_wrapped, target_wrapper,
-                            _enabled, adapter)
-
-                return _capture
-
-            # We should always have the target function to be wrapped at
-            # this point as the first (and only) value in args.
-
-            target_wrapped = args[0]
-
-            # Need to now check that use of the decorator hadn't been
-            # disabled by a simple boolean. If it was, then target
-            # function to be wrapped is returned instead.
-
-            _enabled = enabled
-            if type(_enabled) is bool:
-                if not _enabled:
-                    return target_wrapped
-                _enabled = None
-
-            # We now need to build the wrapper, but there are a couple of
-            # different cases we need to consider.
-
-            if instance is None:
-                if isclass(wrapped):
-                    # In this case the decorator was applied to a class
-                    # type but optional keyword arguments were not supplied
-                    # for initialising an instance of the class to be used
-                    # as the decorator wrapper function.
-                    #
-                    #     @decorator
-                    #     class mydecoratorclass(object):
-                    #         def __init__(self, arg=None):
-                    #             self.arg = arg
-                    #         def __call__(self, wrapped, instance,
-                    #                 args, kwargs):
-                    #             return wrapped(*args, **kwargs)
-                    #
-                    #     @mydecoratorclass
-                    #     def function():
-                    #         pass
-                    #
-                    # We still need to create an instance of the class to
-                    # be used as the decorator wrapper function, but no
-                    # arguments are pass.
-
-                    target_wrapper = wrapped()
-
-                else:
-                    # In this case the decorator was applied to a normal
-                    # function, or possibly a static method of a class.
-                    #
-                    #     @decorator
-                    #     def mydecoratorfuntion(wrapped, instance,
-                    #             args, kwargs):
-                    #         return wrapped(*args, **kwargs)
-                    #
-                    #     @mydecoratorfunction
-                    #     def function():
-                    #         pass
-                    #
-                    # That normal function becomes the decorator wrapper
-                    # function.
-
-                    target_wrapper = wrapper
-
-            else:
-                if isclass(instance):
-                    # In this case the decorator was applied to a class
-                    # method.
-                    #
-                    #     class myclass(object):
-                    #         @decorator
-                    #         @classmethod
-                    #         def decoratorclassmethod(cls, wrapped,
-                    #                 instance, args, kwargs):
-                    #             return wrapped(*args, **kwargs)
-                    #
-                    #     instance = myclass()
-                    #
-                    #     @instance.decoratorclassmethod
-                    #     def function():
-                    #         pass
-                    #
-                    # This one is a bit strange because binding was actually
-                    # performed on the wrapper created by our decorator
-                    # factory. We need to apply that binding to the decorator
-                    # wrapper function which which the decorator factory
-                    # was applied to.
-
-                    target_wrapper = wrapper.__get__(None, instance)
-
-                else:
-                    # In this case the decorator was applied to an instance
-                    # method.
-                    #
-                    #     class myclass(object):
-                    #         @decorator
-                    #         def decoratorclassmethod(self, wrapped,
-                    #                 instance, args, kwargs):
-                    #             return wrapped(*args, **kwargs)
-                    #
-                    #     instance = myclass()
-                    #
-                    #     @instance.decoratorclassmethod
-                    #     def function():
-                    #         pass
-                    #
-                    # This one is a bit strange because binding was actually
-                    # performed on the wrapper created by our decorator
-                    # factory. We need to apply that binding to the decorator
-                    # wrapper function which which the decorator factory
-                    # was applied to.
-
-                    target_wrapper = wrapper.__get__(instance, type(instance))
-
-            # Finally build the wrapper itself and return it.
-
-            return _build(target_wrapped, target_wrapper, _enabled, adapter)
-
-        # We first return our magic function wrapper here so we can
-        # determine in what context the decorator factory was used. In
-        # other words, it is itself a universal decorator. The decorator
-        # function is used as the adapter so that linters see a signature
-        # corresponding to the decorator and not the wrapper it is being
-        # applied to.
-
-        return _build(wrapper, _wrapper, adapter=decorator)
-
-    else:
-        # The wrapper still has not been provided, so we are just
-        # collecting the optional keyword arguments. Return the
-        # decorator again wrapped in a partial using the collected
-        # arguments.
-
-        return partial(decorator, enabled=enabled, adapter=adapter)
-
-# Decorator for implementing thread synchronization. It can be used as a
-# decorator, in which case the synchronization context is determined by
-# what type of function is wrapped, or it can also be used as a context
-# manager, where the user needs to supply the correct synchronization
-# context. It is also possible to supply an object which appears to be a
-# synchronization primitive of some sort, by virtue of having release()
-# and acquire() methods. In that case that will be used directly as the
-# synchronization primitive without creating a separate lock against the
-# derived or supplied context.
-
-def synchronized(wrapped):
-    # Determine if being passed an object which is a synchronization
-    # primitive. We can't check by type for Lock, RLock, Semaphore etc,
-    # as the means of creating them isn't the type. Therefore use the
-    # existence of acquire() and release() methods. This is more
-    # extensible anyway as it allows custom synchronization mechanisms.
-
-    if hasattr(wrapped, 'acquire') and hasattr(wrapped, 'release'):
-        # We remember what the original lock is and then return a new
-        # decorator which accesses and locks it. When returning the new
-        # decorator we wrap it with an object proxy so we can override
-        # the context manager methods in case it is being used to wrap
-        # synchronized statements with a 'with' statement.
-
-        lock = wrapped
-
-        @decorator
-        def _synchronized(wrapped, instance, args, kwargs):
-            # Execute the wrapped function while the original supplied
-            # lock is held.
-
-            with lock:
-                return wrapped(*args, **kwargs)
-
-        class _PartialDecorator(CallableObjectProxy):
-
-            def __enter__(self):
-                lock.acquire()
-                return lock
-
-            def __exit__(self, *args):
-                lock.release()
-
-        return _PartialDecorator(wrapped=_synchronized)
-
-    # Following only apply when the lock is being created automatically
-    # based on the context of what was supplied. In this case we supply
-    # a final decorator, but need to use FunctionWrapper directly as we
-    # want to derive from it to add context manager methods in case it is
-    # being used to wrap synchronized statements with a 'with' statement.
-
-    def _synchronized_lock(context):
-        # Attempt to retrieve the lock for the specific context.
-
-        lock = vars(context).get('_synchronized_lock', None)
-
-        if lock is None:
-            # There is no existing lock defined for the context we
-            # are dealing with so we need to create one. This needs
-            # to be done in a way to guarantee there is only one
-            # created, even if multiple threads try and create it at
-            # the same time. We can't always use the setdefault()
-            # method on the __dict__ for the context. This is the
-            # case where the context is a class, as __dict__ is
-            # actually a dictproxy. What we therefore do is use a
-            # meta lock on this wrapper itself, to control the
-            # creation and assignment of the lock attribute against
-            # the context.
-
-            with synchronized._synchronized_meta_lock:
-                # We need to check again for whether the lock we want
-                # exists in case two threads were trying to create it
-                # at the same time and were competing to create the
-                # meta lock.
-
-                lock = vars(context).get('_synchronized_lock', None)
-
-                if lock is None:
-                    lock = RLock()
-                    setattr(context, '_synchronized_lock', lock)
-
-        return lock
-
-    def _synchronized_wrapper(wrapped, instance, args, kwargs):
-        # Execute the wrapped function while the lock for the
-        # desired context is held. If instance is None then the
-        # wrapped function is used as the context.
-
-        with _synchronized_lock(instance or wrapped):
-            return wrapped(*args, **kwargs)
-
-    class _FinalDecorator(FunctionWrapper):
-
-        def __enter__(self):
-            self._self_lock = _synchronized_lock(self.__wrapped__)
-            self._self_lock.acquire()
-            return self._self_lock
-
-        def __exit__(self, *args):
-            self._self_lock.release()
-
-    return _FinalDecorator(wrapped=wrapped, wrapper=_synchronized_wrapper)
-
-synchronized._synchronized_meta_lock = Lock()
diff --git a/venv/Lib/site-packages/wrapt/importer.py b/venv/Lib/site-packages/wrapt/importer.py
deleted file mode 100644
index 9e617cd..0000000
--- a/venv/Lib/site-packages/wrapt/importer.py
+++ /dev/null
@@ -1,230 +0,0 @@
-"""This module implements a post import hook mechanism styled after what is
-described in PEP-369. Note that it doesn't cope with modules being reloaded.
-
-"""
-
-import sys
-import threading
-
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-
-if PY3:
-    import importlib
-    string_types = str,
-else:
-    string_types = basestring,
-
-from .decorators import synchronized
-
-# The dictionary registering any post import hooks to be triggered once
-# the target module has been imported. Once a module has been imported
-# and the hooks fired, the list of hooks recorded against the target
-# module will be truncacted but the list left in the dictionary. This
-# acts as a flag to indicate that the module had already been imported.
-
-_post_import_hooks = {}
-_post_import_hooks_init = False
-_post_import_hooks_lock = threading.RLock()
-
-# Register a new post import hook for the target module name. This
-# differs from the PEP-369 implementation in that it also allows the
-# hook function to be specified as a string consisting of the name of
-# the callback in the form 'module:function'. This will result in a
-# proxy callback being registered which will defer loading of the
-# specified module containing the callback function until required.
-
-def _create_import_hook_from_string(name):
-    def import_hook(module):
-        module_name, function = name.split(':')
-        attrs = function.split('.')
-        __import__(module_name)
-        callback = sys.modules[module_name]
-        for attr in attrs:
-            callback = getattr(callback, attr)
-        return callback(module)
-    return import_hook
-
-@synchronized(_post_import_hooks_lock)
-def register_post_import_hook(hook, name):
-    # Create a deferred import hook if hook is a string name rather than
-    # a callable function.
-
-    if isinstance(hook, string_types):
-        hook = _create_import_hook_from_string(hook)
-
-    # Automatically install the import hook finder if it has not already
-    # been installed.
-
-    global _post_import_hooks_init
-
-    if not _post_import_hooks_init:
-        _post_import_hooks_init = True
-        sys.meta_path.insert(0, ImportHookFinder())
-
-    # Determine if any prior registration of a post import hook for
-    # the target modules has occurred and act appropriately.
-
-    hooks = _post_import_hooks.get(name, None)
-
-    if hooks is None:
-        # No prior registration of post import hooks for the target
-        # module. We need to check whether the module has already been
-        # imported. If it has we fire the hook immediately and add an
-        # empty list to the registry to indicate that the module has
-        # already been imported and hooks have fired. Otherwise add
-        # the post import hook to the registry.
-
-        module = sys.modules.get(name, None)
-
-        if module is not None:
-            _post_import_hooks[name] = []
-            hook(module)
-
-        else:
-            _post_import_hooks[name] = [hook]
-
-    elif hooks == []:
-        # A prior registration of port import hooks for the target
-        # module was done and the hooks already fired. Fire the hook
-        # immediately.
-
-        module = sys.modules[name]
-        hook(module)
-
-    else:
-        # A prior registration of port import hooks for the target
-        # module was done but the module has not yet been imported.
-
-        _post_import_hooks[name].append(hook)
-
-# Register post import hooks defined as package entry points.
-
-def _create_import_hook_from_entrypoint(entrypoint):
-    def import_hook(module):
-        __import__(entrypoint.module_name)
-        callback = sys.modules[entrypoint.module_name]
-        for attr in entrypoint.attrs:
-            callback = getattr(callback, attr)
-        return callback(module)
-    return import_hook
-
-def discover_post_import_hooks(group):
-    try:
-        import pkg_resources
-    except ImportError:
-        return
-
-    for entrypoint in pkg_resources.iter_entry_points(group=group):
-        callback = _create_import_hook_from_entrypoint(entrypoint)
-        register_post_import_hook(callback, entrypoint.name)
-
-# Indicate that a module has been loaded. Any post import hooks which
-# were registered against the target module will be invoked. If an
-# exception is raised in any of the post import hooks, that will cause
-# the import of the target module to fail.
-
-@synchronized(_post_import_hooks_lock)
-def notify_module_loaded(module):
-    name = getattr(module, '__name__', None)
-    hooks = _post_import_hooks.get(name, None)
-
-    if hooks:
-        _post_import_hooks[name] = []
-
-        for hook in hooks:
-            hook(module)
-
-# A custom module import finder. This intercepts attempts to import
-# modules and watches out for attempts to import target modules of
-# interest. When a module of interest is imported, then any post import
-# hooks which are registered will be invoked.
-
-class _ImportHookLoader:
-
-    def load_module(self, fullname):
-        module = sys.modules[fullname]
-        notify_module_loaded(module)
-
-        return module
-
-class _ImportHookChainedLoader:
-
-    def __init__(self, loader):
-        self.loader = loader
-
-    def load_module(self, fullname):
-        module = self.loader.load_module(fullname)
-        notify_module_loaded(module)
-
-        return module
-
-class ImportHookFinder:
-
-    def __init__(self):
-        self.in_progress = {}
-
-    @synchronized(_post_import_hooks_lock)
-    def find_module(self, fullname, path=None):
-        # If the module being imported is not one we have registered
-        # post import hooks for, we can return immediately. We will
-        # take no further part in the importing of this module.
-
-        if not fullname in _post_import_hooks:
-            return None
-
-        # When we are interested in a specific module, we will call back
-        # into the import system a second time to defer to the import
-        # finder that is supposed to handle the importing of the module.
-        # We set an in progress flag for the target module so that on
-        # the second time through we don't trigger another call back
-        # into the import system and cause a infinite loop.
-
-        if fullname in self.in_progress:
-            return None
-
-        self.in_progress[fullname] = True
-
-        # Now call back into the import system again.
-
-        try:
-            if PY3:
-                # For Python 3 we need to use find_spec().loader
-                # from the importlib.util module. It doesn't actually
-                # import the target module and only finds the
-                # loader. If a loader is found, we need to return
-                # our own loader which will then in turn call the
-                # real loader to import the module and invoke the
-                # post import hooks.
-                try:
-                    import importlib.util
-                    loader = importlib.util.find_spec(fullname).loader
-                except (ImportError, AttributeError):
-                    loader = importlib.find_loader(fullname, path)
-                if loader:
-                    return _ImportHookChainedLoader(loader)
-
-            else:
-                # For Python 2 we don't have much choice but to
-                # call back in to __import__(). This will
-                # actually cause the module to be imported. If no
-                # module could be found then ImportError will be
-                # raised. Otherwise we return a loader which
-                # returns the already loaded module and invokes
-                # the post import hooks.
-
-                __import__(fullname)
-
-                return _ImportHookLoader()
-
-        finally:
-            del self.in_progress[fullname]
-
-# Decorator for marking that a function should be called as a post
-# import hook when the target module is imported.
-
-def when_imported(name):
-    def register(hook):
-        register_post_import_hook(hook, name)
-        return hook
-    return register
diff --git a/venv/Lib/site-packages/wrapt/wrappers.py b/venv/Lib/site-packages/wrapt/wrappers.py
deleted file mode 100644
index 1d6131d..0000000
--- a/venv/Lib/site-packages/wrapt/wrappers.py
+++ /dev/null
@@ -1,943 +0,0 @@
-import os
-import sys
-import functools
-import operator
-import weakref
-import inspect
-
-PY2 = sys.version_info[0] == 2
-PY3 = sys.version_info[0] == 3
-
-if PY3:
-    string_types = str,
-else:
-    string_types = basestring,
-
-def with_metaclass(meta, *bases):
-    """Create a base class with a metaclass."""
-    return meta("NewBase", bases, {})
-
-class _ObjectProxyMethods(object):
-
-    # We use properties to override the values of __module__ and
-    # __doc__. If we add these in ObjectProxy, the derived class
-    # __dict__ will still be setup to have string variants of these
-    # attributes and the rules of descriptors means that they appear to
-    # take precedence over the properties in the base class. To avoid
-    # that, we copy the properties into the derived class type itself
-    # via a meta class. In that way the properties will always take
-    # precedence.
-
-    @property
-    def __module__(self):
-        return self.__wrapped__.__module__
-
-    @__module__.setter
-    def __module__(self, value):
-        self.__wrapped__.__module__ = value
-
-    @property
-    def __doc__(self):
-        return self.__wrapped__.__doc__
-
-    @__doc__.setter
-    def __doc__(self, value):
-        self.__wrapped__.__doc__ = value
-
-    # We similar use a property for __dict__. We need __dict__ to be
-    # explicit to ensure that vars() works as expected.
-
-    @property
-    def __dict__(self):
-        return self.__wrapped__.__dict__
-
-    # Need to also propagate the special __weakref__ attribute for case
-    # where decorating classes which will define this. If do not define
-    # it and use a function like inspect.getmembers() on a decorator
-    # class it will fail. This can't be in the derived classes.
-
-    @property
-    def __weakref__(self):
-        return self.__wrapped__.__weakref__
-
-class _ObjectProxyMetaType(type):
-    def __new__(cls, name, bases, dictionary):
-        # Copy our special properties into the class so that they
-        # always take precedence over attributes of the same name added
-        # during construction of a derived class. This is to save
-        # duplicating the implementation for them in all derived classes.
-
-        dictionary.update(vars(_ObjectProxyMethods))
-
-        return type.__new__(cls, name, bases, dictionary)
-
-class ObjectProxy(with_metaclass(_ObjectProxyMetaType)):
-
-    __slots__ = '__wrapped__'
-
-    def __init__(self, wrapped):
-        object.__setattr__(self, '__wrapped__', wrapped)
-
-        # Python 3.2+ has the __qualname__ attribute, but it does not
-        # allow it to be overridden using a property and it must instead
-        # be an actual string object instead.
-
-        try:
-            object.__setattr__(self, '__qualname__', wrapped.__qualname__)
-        except AttributeError:
-            pass
-
-    @property
-    def __name__(self):
-        return self.__wrapped__.__name__
-
-    @__name__.setter
-    def __name__(self, value):
-        self.__wrapped__.__name__ = value
-
-    @property
-    def __class__(self):
-        return self.__wrapped__.__class__
-
-    @__class__.setter
-    def __class__(self, value):
-        self.__wrapped__.__class__ = value
-
-    @property
-    def __annotations__(self):
-        return self.__wrapped__.__annotations__
-
-    @__annotations__.setter
-    def __annotations__(self, value):
-        self.__wrapped__.__annotations__ = value
-
-    def __dir__(self):
-        return dir(self.__wrapped__)
-
-    def __str__(self):
-        return str(self.__wrapped__)
-
-    if PY3:
-        def __bytes__(self):
-            return bytes(self.__wrapped__)
-
-    def __repr__(self):
-        return '<{} at 0x{:x} for {} at 0x{:x}>'.format(
-                type(self).__name__, id(self),
-                type(self.__wrapped__).__name__,
-                id(self.__wrapped__))
-
-    def __reversed__(self):
-        return reversed(self.__wrapped__)
-
-    if PY3:
-        def __round__(self):
-            return round(self.__wrapped__)
-
-    def __lt__(self, other):
-        return self.__wrapped__ < other
-
-    def __le__(self, other):
-        return self.__wrapped__ <= other
-
-    def __eq__(self, other):
-        return self.__wrapped__ == other
-
-    def __ne__(self, other):
-        return self.__wrapped__ != other
-
-    def __gt__(self, other):
-        return self.__wrapped__ > other
-
-    def __ge__(self, other):
-        return self.__wrapped__ >= other
-
-    def __hash__(self):
-        return hash(self.__wrapped__)
-
-    def __nonzero__(self):
-        return bool(self.__wrapped__)
-
-    def __bool__(self):
-        return bool(self.__wrapped__)
-
-    def __setattr__(self, name, value):
-        if name.startswith('_self_'):
-            object.__setattr__(self, name, value)
-
-        elif name == '__wrapped__':
-            object.__setattr__(self, name, value)
-            try:
-                object.__delattr__(self, '__qualname__')
-            except AttributeError:
-                pass
-            try:
-                object.__setattr__(self, '__qualname__', value.__qualname__)
-            except AttributeError:
-                pass
-
-        elif name == '__qualname__':
-            setattr(self.__wrapped__, name, value)
-            object.__setattr__(self, name, value)
-
-        elif hasattr(type(self), name):
-            object.__setattr__(self, name, value)
-
-        else:
-            setattr(self.__wrapped__, name, value)
-
-    def __getattr__(self, name):
-        # If we are being to lookup '__wrapped__' then the
-        # '__init__()' method cannot have been called.
-
-        if name == '__wrapped__':
-            raise ValueError('wrapper has not been initialised')
-
-        return getattr(self.__wrapped__, name)
-
-    def __delattr__(self, name):
-        if name.startswith('_self_'):
-            object.__delattr__(self, name)
-
-        elif name == '__wrapped__':
-            raise TypeError('__wrapped__ must be an object')
-
-        elif name == '__qualname__':
-            object.__delattr__(self, name)
-            delattr(self.__wrapped__, name)
-
-        elif hasattr(type(self), name):
-            object.__delattr__(self, name)
-
-        else:
-            delattr(self.__wrapped__, name)
-
-    def __add__(self, other):
-        return self.__wrapped__ + other
-
-    def __sub__(self, other):
-        return self.__wrapped__ - other
-
-    def __mul__(self, other):
-        return self.__wrapped__ * other
-
-    def __div__(self, other):
-        return operator.div(self.__wrapped__, other)
-
-    def __truediv__(self, other):
-        return operator.truediv(self.__wrapped__, other)
-
-    def __floordiv__(self, other):
-        return self.__wrapped__ // other
-
-    def __mod__(self, other):
-        return self.__wrapped__ % other
-
-    def __divmod__(self, other):
-        return divmod(self.__wrapped__, other)
-
-    def __pow__(self, other, *args):
-        return pow(self.__wrapped__, other, *args)
-
-    def __lshift__(self, other):
-        return self.__wrapped__ << other
-
-    def __rshift__(self, other):
-        return self.__wrapped__ >> other
-
-    def __and__(self, other):
-        return self.__wrapped__ & other
-
-    def __xor__(self, other):
-        return self.__wrapped__ ^ other
-
-    def __or__(self, other):
-        return self.__wrapped__ | other
-
-    def __radd__(self, other):
-        return other + self.__wrapped__
-
-    def __rsub__(self, other):
-        return other - self.__wrapped__
-
-    def __rmul__(self, other):
-        return other * self.__wrapped__
-
-    def __rdiv__(self, other):
-        return operator.div(other, self.__wrapped__)
-
-    def __rtruediv__(self, other):
-        return operator.truediv(other, self.__wrapped__)
-
-    def __rfloordiv__(self, other):
-        return other // self.__wrapped__
-
-    def __rmod__(self, other):
-        return other % self.__wrapped__
-
-    def __rdivmod__(self, other):
-        return divmod(other, self.__wrapped__)
-
-    def __rpow__(self, other, *args):
-        return pow(other, self.__wrapped__, *args)
-
-    def __rlshift__(self, other):
-        return other << self.__wrapped__
-
-    def __rrshift__(self, other):
-        return other >> self.__wrapped__
-
-    def __rand__(self, other):
-        return other & self.__wrapped__
-
-    def __rxor__(self, other):
-        return other ^ self.__wrapped__
-
-    def __ror__(self, other):
-        return other | self.__wrapped__
-
-    def __iadd__(self, other):
-        self.__wrapped__ += other
-        return self
-
-    def __isub__(self, other):
-        self.__wrapped__ -= other
-        return self
-
-    def __imul__(self, other):
-        self.__wrapped__ *= other
-        return self
-
-    def __idiv__(self, other):
-        self.__wrapped__ = operator.idiv(self.__wrapped__, other)
-        return self
-
-    def __itruediv__(self, other):
-        self.__wrapped__ = operator.itruediv(self.__wrapped__, other)
-        return self
-
-    def __ifloordiv__(self, other):
-        self.__wrapped__ //= other
-        return self
-
-    def __imod__(self, other):
-        self.__wrapped__ %= other
-        return self
-
-    def __ipow__(self, other):
-        self.__wrapped__ **= other
-        return self
-
-    def __ilshift__(self, other):
-        self.__wrapped__ <<= other
-        return self
-
-    def __irshift__(self, other):
-        self.__wrapped__ >>= other
-        return self
-
-    def __iand__(self, other):
-        self.__wrapped__ &= other
-        return self
-
-    def __ixor__(self, other):
-        self.__wrapped__ ^= other
-        return self
-
-    def __ior__(self, other):
-        self.__wrapped__ |= other
-        return self
-
-    def __neg__(self):
-        return -self.__wrapped__
-
-    def __pos__(self):
-        return +self.__wrapped__
-
-    def __abs__(self):
-        return abs(self.__wrapped__)
-
-    def __invert__(self):
-        return ~self.__wrapped__
-
-    def __int__(self):
-        return int(self.__wrapped__)
-
-    def __long__(self):
-        return long(self.__wrapped__)
-
-    def __float__(self):
-        return float(self.__wrapped__)
-
-    def __complex__(self):
-        return complex(self.__wrapped__)
-
-    def __oct__(self):
-        return oct(self.__wrapped__)
-
-    def __hex__(self):
-        return hex(self.__wrapped__)
-
-    def __index__(self):
-        return operator.index(self.__wrapped__)
-
-    def __len__(self):
-        return len(self.__wrapped__)
-
-    def __contains__(self, value):
-        return value in self.__wrapped__
-
-    def __getitem__(self, key):
-        return self.__wrapped__[key]
-
-    def __setitem__(self, key, value):
-        self.__wrapped__[key] = value
-
-    def __delitem__(self, key):
-        del self.__wrapped__[key]
-
-    def __getslice__(self, i, j):
-        return self.__wrapped__[i:j]
-
-    def __setslice__(self, i, j, value):
-        self.__wrapped__[i:j] = value
-
-    def __delslice__(self, i, j):
-        del self.__wrapped__[i:j]
-
-    def __enter__(self):
-        return self.__wrapped__.__enter__()
-
-    def __exit__(self, *args, **kwargs):
-        return self.__wrapped__.__exit__(*args, **kwargs)
-
-    def __iter__(self):
-        return iter(self.__wrapped__)
-
-    def __copy__(self):
-        raise NotImplementedError('object proxy must define __copy__()')
-
-    def __deepcopy__(self, memo):
-        raise NotImplementedError('object proxy must define __deepcopy__()')
-
-    def __reduce__(self):
-        raise NotImplementedError(
-                'object proxy must define __reduce_ex__()')
-
-    def __reduce_ex__(self, protocol):
-        raise NotImplementedError(
-                'object proxy must define __reduce_ex__()')
-
-class CallableObjectProxy(ObjectProxy):
-
-    def __call__(self, *args, **kwargs):
-        return self.__wrapped__(*args, **kwargs)
-
-class PartialCallableObjectProxy(ObjectProxy):
-
-    def __init__(self, *args, **kwargs):
-        if len(args) < 1:
-            raise TypeError('partial type takes at least one argument')
-
-        wrapped, args = args[0], args[1:]
-
-        if not callable(wrapped):
-            raise TypeError('the first argument must be callable')
-
-        super(PartialCallableObjectProxy, self).__init__(wrapped)
-
-        self._self_args = args
-        self._self_kwargs = kwargs
-
-    def __call__(self, *args, **kwargs):
-        _args = self._self_args + args
-
-        _kwargs = dict(self._self_kwargs)
-        _kwargs.update(kwargs)
-
-        return self.__wrapped__(*_args, **_kwargs)
-
-class _FunctionWrapperBase(ObjectProxy):
-
-    __slots__ = ('_self_instance', '_self_wrapper', '_self_enabled',
-            '_self_binding', '_self_parent')
-
-    def __init__(self, wrapped, instance, wrapper, enabled=None,
-            binding='function', parent=None):
-
-        super(_FunctionWrapperBase, self).__init__(wrapped)
-
-        object.__setattr__(self, '_self_instance', instance)
-        object.__setattr__(self, '_self_wrapper', wrapper)
-        object.__setattr__(self, '_self_enabled', enabled)
-        object.__setattr__(self, '_self_binding', binding)
-        object.__setattr__(self, '_self_parent', parent)
-
-    def __get__(self, instance, owner):
-        # This method is actually doing double duty for both unbound and
-        # bound derived wrapper classes. It should possibly be broken up
-        # and the distinct functionality moved into the derived classes.
-        # Can't do that straight away due to some legacy code which is
-        # relying on it being here in this base class.
-        #
-        # The distinguishing attribute which determines whether we are
-        # being called in an unbound or bound wrapper is the parent
-        # attribute. If binding has never occurred, then the parent will
-        # be None.
-        #
-        # First therefore, is if we are called in an unbound wrapper. In
-        # this case we perform the binding.
-        #
-        # We have one special case to worry about here. This is where we
-        # are decorating a nested class. In this case the wrapped class
-        # would not have a __get__() method to call. In that case we
-        # simply return self.
-        #
-        # Note that we otherwise still do binding even if instance is
-        # None and accessing an unbound instance method from a class.
-        # This is because we need to be able to later detect that
-        # specific case as we will need to extract the instance from the
-        # first argument of those passed in.
-
-        if self._self_parent is None:
-            if not inspect.isclass(self.__wrapped__):
-                descriptor = self.__wrapped__.__get__(instance, owner)
-
-                return self.__bound_function_wrapper__(descriptor, instance,
-                        self._self_wrapper, self._self_enabled,
-                        self._self_binding, self)
-
-            return self
-
-        # Now we have the case of binding occurring a second time on what
-        # was already a bound function. In this case we would usually
-        # return ourselves again. This mirrors what Python does.
-        #
-        # The special case this time is where we were originally bound
-        # with an instance of None and we were likely an instance
-        # method. In that case we rebind against the original wrapped
-        # function from the parent again.
-
-        if self._self_instance is None and self._self_binding == 'function':
-            descriptor = self._self_parent.__wrapped__.__get__(
-                    instance, owner)
-
-            return self._self_parent.__bound_function_wrapper__(
-                    descriptor, instance, self._self_wrapper,
-                    self._self_enabled, self._self_binding,
-                    self._self_parent)
-
-        return self
-
-    def __call__(self, *args, **kwargs):
-        # If enabled has been specified, then evaluate it at this point
-        # and if the wrapper is not to be executed, then simply return
-        # the bound function rather than a bound wrapper for the bound
-        # function. When evaluating enabled, if it is callable we call
-        # it, otherwise we evaluate it as a boolean.
-
-        if self._self_enabled is not None:
-            if callable(self._self_enabled):
-                if not self._self_enabled():
-                    return self.__wrapped__(*args, **kwargs)
-            elif not self._self_enabled:
-                return self.__wrapped__(*args, **kwargs)
-
-        # This can occur where initial function wrapper was applied to
-        # a function that was already bound to an instance. In that case
-        # we want to extract the instance from the function and use it.
-
-        if self._self_binding == 'function':
-            if self._self_instance is None:
-                instance = getattr(self.__wrapped__, '__self__', None)
-                if instance is not None:
-                    return self._self_wrapper(self.__wrapped__, instance,
-                            args, kwargs)
-
-        # This is generally invoked when the wrapped function is being
-        # called as a normal function and is not bound to a class as an
-        # instance method. This is also invoked in the case where the
-        # wrapped function was a method, but this wrapper was in turn
-        # wrapped using the staticmethod decorator.
-
-        return self._self_wrapper(self.__wrapped__, self._self_instance,
-                args, kwargs)
-
-class BoundFunctionWrapper(_FunctionWrapperBase):
-
-    def __call__(self, *args, **kwargs):
-        # If enabled has been specified, then evaluate it at this point
-        # and if the wrapper is not to be executed, then simply return
-        # the bound function rather than a bound wrapper for the bound
-        # function. When evaluating enabled, if it is callable we call
-        # it, otherwise we evaluate it as a boolean.
-
-        if self._self_enabled is not None:
-            if callable(self._self_enabled):
-                if not self._self_enabled():
-                    return self.__wrapped__(*args, **kwargs)
-            elif not self._self_enabled:
-                return self.__wrapped__(*args, **kwargs)
-
-        # We need to do things different depending on whether we are
-        # likely wrapping an instance method vs a static method or class
-        # method.
-
-        if self._self_binding == 'function':
-            if self._self_instance is None:
-                # This situation can occur where someone is calling the
-                # instancemethod via the class type and passing the instance
-                # as the first argument. We need to shift the args before
-                # making the call to the wrapper and effectively bind the
-                # instance to the wrapped function using a partial so the
-                # wrapper doesn't see anything as being different.
-
-                if not args:
-                    raise TypeError('missing 1 required positional argument')
-
-                instance, args = args[0], args[1:]
-                wrapped = PartialCallableObjectProxy(self.__wrapped__, instance)
-                return self._self_wrapper(wrapped, instance, args, kwargs)
-
-            return self._self_wrapper(self.__wrapped__, self._self_instance,
-                    args, kwargs)
-
-        else:
-            # As in this case we would be dealing with a classmethod or
-            # staticmethod, then _self_instance will only tell us whether
-            # when calling the classmethod or staticmethod they did it via an
-            # instance of the class it is bound to and not the case where
-            # done by the class type itself. We thus ignore _self_instance
-            # and use the __self__ attribute of the bound function instead.
-            # For a classmethod, this means instance will be the class type
-            # and for a staticmethod it will be None. This is probably the
-            # more useful thing we can pass through even though we loose
-            # knowledge of whether they were called on the instance vs the
-            # class type, as it reflects what they have available in the
-            # decoratored function.
-
-            instance = getattr(self.__wrapped__, '__self__', None)
-
-            return self._self_wrapper(self.__wrapped__, instance, args,
-                    kwargs)
-
-class FunctionWrapper(_FunctionWrapperBase):
-
-    __bound_function_wrapper__ = BoundFunctionWrapper
-
-    def __init__(self, wrapped, wrapper, enabled=None):
-        # What it is we are wrapping here could be anything. We need to
-        # try and detect specific cases though. In particular, we need
-        # to detect when we are given something that is a method of a
-        # class. Further, we need to know when it is likely an instance
-        # method, as opposed to a class or static method. This can
-        # become problematic though as there isn't strictly a fool proof
-        # method of knowing.
-        #
-        # The situations we could encounter when wrapping a method are:
-        #
-        # 1. The wrapper is being applied as part of a decorator which
-        # is a part of the class definition. In this case what we are
-        # given is the raw unbound function, classmethod or staticmethod
-        # wrapper objects.
-        #
-        # The problem here is that we will not know we are being applied
-        # in the context of the class being set up. This becomes
-        # important later for the case of an instance method, because in
-        # that case we just see it as a raw function and can't
-        # distinguish it from wrapping a normal function outside of
-        # a class context.
-        #
-        # 2. The wrapper is being applied when performing monkey
-        # patching of the class type afterwards and the method to be
-        # wrapped was retrieved direct from the __dict__ of the class
-        # type. This is effectively the same as (1) above.
-        #
-        # 3. The wrapper is being applied when performing monkey
-        # patching of the class type afterwards and the method to be
-        # wrapped was retrieved from the class type. In this case
-        # binding will have been performed where the instance against
-        # which the method is bound will be None at that point.
-        #
-        # This case is a problem because we can no longer tell if the
-        # method was a static method, plus if using Python3, we cannot
-        # tell if it was an instance method as the concept of an
-        # unnbound method no longer exists.
-        #
-        # 4. The wrapper is being applied when performing monkey
-        # patching of an instance of a class. In this case binding will
-        # have been perfomed where the instance was not None.
-        #
-        # This case is a problem because we can no longer tell if the
-        # method was a static method.
-        #
-        # Overall, the best we can do is look at the original type of the
-        # object which was wrapped prior to any binding being done and
-        # see if it is an instance of classmethod or staticmethod. In
-        # the case where other decorators are between us and them, if
-        # they do not propagate the __class__  attribute so that the
-        # isinstance() checks works, then likely this will do the wrong
-        # thing where classmethod and staticmethod are used.
-        #
-        # Since it is likely to be very rare that anyone even puts
-        # decorators around classmethod and staticmethod, likelihood of
-        # that being an issue is very small, so we accept it and suggest
-        # that those other decorators be fixed. It is also only an issue
-        # if a decorator wants to actually do things with the arguments.
-        #
-        # As to not being able to identify static methods properly, we
-        # just hope that that isn't something people are going to want
-        # to wrap, or if they do suggest they do it the correct way by
-        # ensuring that it is decorated in the class definition itself,
-        # or patch it in the __dict__ of the class type.
-        #
-        # So to get the best outcome we can, whenever we aren't sure what
-        # it is, we label it as a 'function'. If it was already bound and
-        # that is rebound later, we assume that it will be an instance
-        # method and try an cope with the possibility that the 'self'
-        # argument it being passed as an explicit argument and shuffle
-        # the arguments around to extract 'self' for use as the instance.
-
-        if isinstance(wrapped, classmethod):
-            binding = 'classmethod'
-
-        elif isinstance(wrapped, staticmethod):
-            binding = 'staticmethod'
-
-        elif hasattr(wrapped, '__self__'):
-            if inspect.isclass(wrapped.__self__):
-                binding = 'classmethod'
-            else:
-                binding = 'function'
-
-        else:
-            binding = 'function'
-
-        super(FunctionWrapper, self).__init__(wrapped, None, wrapper,
-                enabled, binding)
-
-try:
-    if not os.environ.get('WRAPT_DISABLE_EXTENSIONS'):
-        from ._wrappers import (ObjectProxy, CallableObjectProxy,
-            PartialCallableObjectProxy, FunctionWrapper,
-            BoundFunctionWrapper, _FunctionWrapperBase)
-except ImportError:
-    pass
-
-# Helper functions for applying wrappers to existing functions.
-
-def resolve_path(module, name):
-    if isinstance(module, string_types):
-        __import__(module)
-        module = sys.modules[module]
-
-    parent = module
-
-    path = name.split('.')
-    attribute = path[0]
-
-    original = getattr(parent, attribute)
-    for attribute in path[1:]:
-        parent = original
-
-        # We can't just always use getattr() because in doing
-        # that on a class it will cause binding to occur which
-        # will complicate things later and cause some things not
-        # to work. For the case of a class we therefore access
-        # the __dict__ directly. To cope though with the wrong
-        # class being given to us, or a method being moved into
-        # a base class, we need to walk the class hierarchy to
-        # work out exactly which __dict__ the method was defined
-        # in, as accessing it from __dict__ will fail if it was
-        # not actually on the class given. Fallback to using
-        # getattr() if we can't find it. If it truly doesn't
-        # exist, then that will fail.
-
-        if inspect.isclass(original):
-            for cls in inspect.getmro(original):
-                if attribute in vars(cls):
-                    original = vars(cls)[attribute]
-                    break
-            else:
-                original = getattr(original, attribute)
-
-        else:
-            original = getattr(original, attribute)
-
-    return (parent, attribute, original)
-
-def apply_patch(parent, attribute, replacement):
-    setattr(parent, attribute, replacement)
-
-def wrap_object(module, name, factory, args=(), kwargs={}):
-    (parent, attribute, original) = resolve_path(module, name)
-    wrapper = factory(original, *args, **kwargs)
-    apply_patch(parent, attribute, wrapper)
-    return wrapper
-
-# Function for applying a proxy object to an attribute of a class
-# instance. The wrapper works by defining an attribute of the same name
-# on the class which is a descriptor and which intercepts access to the
-# instance attribute. Note that this cannot be used on attributes which
-# are themselves defined by a property object.
-
-class AttributeWrapper(object):
-
-    def __init__(self, attribute, factory, args, kwargs):
-        self.attribute = attribute
-        self.factory = factory
-        self.args = args
-        self.kwargs = kwargs
-
-    def __get__(self, instance, owner):
-        value = instance.__dict__[self.attribute]
-        return self.factory(value, *self.args, **self.kwargs)
-
-    def __set__(self, instance, value):
-        instance.__dict__[self.attribute] = value
-
-    def __delete__(self, instance):
-        del instance.__dict__[self.attribute]
-
-def wrap_object_attribute(module, name, factory, args=(), kwargs={}):
-    path, attribute = name.rsplit('.', 1)
-    parent = resolve_path(module, path)[2]
-    wrapper = AttributeWrapper(attribute, factory, args, kwargs)
-    apply_patch(parent, attribute, wrapper)
-    return wrapper
-
-# Functions for creating a simple decorator using a FunctionWrapper,
-# plus short cut functions for applying wrappers to functions. These are
-# for use when doing monkey patching. For a more featured way of
-# creating decorators see the decorator decorator instead.
-
-def function_wrapper(wrapper):
-    def _wrapper(wrapped, instance, args, kwargs):
-        target_wrapped = args[0]
-        if instance is None:
-            target_wrapper = wrapper
-        elif inspect.isclass(instance):
-            target_wrapper = wrapper.__get__(None, instance)
-        else:
-            target_wrapper = wrapper.__get__(instance, type(instance))
-        return FunctionWrapper(target_wrapped, target_wrapper)
-    return FunctionWrapper(wrapper, _wrapper)
-
-def wrap_function_wrapper(module, name, wrapper):
-    return wrap_object(module, name, FunctionWrapper, (wrapper,))
-
-def patch_function_wrapper(module, name):
-    def _wrapper(wrapper):
-        return wrap_object(module, name, FunctionWrapper, (wrapper,))
-    return _wrapper
-
-def transient_function_wrapper(module, name):
-    def _decorator(wrapper):
-        def _wrapper(wrapped, instance, args, kwargs):
-            target_wrapped = args[0]
-            if instance is None:
-                target_wrapper = wrapper
-            elif inspect.isclass(instance):
-                target_wrapper = wrapper.__get__(None, instance)
-            else:
-                target_wrapper = wrapper.__get__(instance, type(instance))
-            def _execute(wrapped, instance, args, kwargs):
-                (parent, attribute, original) = resolve_path(module, name)
-                replacement = FunctionWrapper(original, target_wrapper)
-                setattr(parent, attribute, replacement)
-                try:
-                    return wrapped(*args, **kwargs)
-                finally:
-                    setattr(parent, attribute, original)
-            return FunctionWrapper(target_wrapped, _execute)
-        return FunctionWrapper(wrapper, _wrapper)
-    return _decorator
-
-# A weak function proxy. This will work on instance methods, class
-# methods, static methods and regular functions. Special treatment is
-# needed for the method types because the bound method is effectively a
-# transient object and applying a weak reference to one will immediately
-# result in it being destroyed and the weakref callback called. The weak
-# reference is therefore applied to the instance the method is bound to
-# and the original function. The function is then rebound at the point
-# of a call via the weak function proxy.
-
-def _weak_function_proxy_callback(ref, proxy, callback):
-    if proxy._self_expired:
-        return
-
-    proxy._self_expired = True
-
-    # This could raise an exception. We let it propagate back and let
-    # the weakref.proxy() deal with it, at which point it generally
-    # prints out a short error message direct to stderr and keeps going.
-
-    if callback is not None:
-        callback(proxy)
-
-class WeakFunctionProxy(ObjectProxy):
-
-    __slots__ = ('_self_expired', '_self_instance')
-
-    def __init__(self, wrapped, callback=None):
-        # We need to determine if the wrapped function is actually a
-        # bound method. In the case of a bound method, we need to keep a
-        # reference to the original unbound function and the instance.
-        # This is necessary because if we hold a reference to the bound
-        # function, it will be the only reference and given it is a
-        # temporary object, it will almost immediately expire and
-        # the weakref callback triggered. So what is done is that we
-        # hold a reference to the instance and unbound function and
-        # when called bind the function to the instance once again and
-        # then call it. Note that we avoid using a nested function for
-        # the callback here so as not to cause any odd reference cycles.
-
-        _callback = callback and functools.partial(
-                _weak_function_proxy_callback, proxy=self,
-                callback=callback)
-
-        self._self_expired = False
-
-        if isinstance(wrapped, _FunctionWrapperBase):
-            self._self_instance = weakref.ref(wrapped._self_instance,
-                    _callback)
-
-            if wrapped._self_parent is not None:
-                super(WeakFunctionProxy, self).__init__(
-                        weakref.proxy(wrapped._self_parent, _callback))
-
-            else:
-                super(WeakFunctionProxy, self).__init__(
-                        weakref.proxy(wrapped, _callback))
-
-            return
-
-        try:
-            self._self_instance = weakref.ref(wrapped.__self__, _callback)
-
-            super(WeakFunctionProxy, self).__init__(
-                    weakref.proxy(wrapped.__func__, _callback))
-
-        except AttributeError:
-            self._self_instance = None
-
-            super(WeakFunctionProxy, self).__init__(
-                    weakref.proxy(wrapped, _callback))
-
-    def __call__(self, *args, **kwargs):
-        # We perform a boolean check here on the instance and wrapped
-        # function as that will trigger the reference error prior to
-        # calling if the reference had expired.
-
-        instance = self._self_instance and self._self_instance()
-        function = self.__wrapped__ and self.__wrapped__
-
-        # If the wrapped function was originally a bound function, for
-        # which we retained a reference to the instance and the unbound
-        # function we need to rebind the function and then call it. If
-        # not just called the wrapped function.
-
-        if instance is None:
-            return self.__wrapped__(*args, **kwargs)
-
-        return function.__get__(instance, type(instance))(*args, **kwargs)
diff --git a/venv/Scripts/Activate.ps1 b/venv/Scripts/Activate.ps1
deleted file mode 100644
index a46533f..0000000
--- a/venv/Scripts/Activate.ps1
+++ /dev/null
@@ -1,51 +0,0 @@
-function global:deactivate ([switch]$NonDestructive) {
-    # Revert to original values
-    if (Test-Path function:_OLD_VIRTUAL_PROMPT) {
-        copy-item function:_OLD_VIRTUAL_PROMPT function:prompt
-        remove-item function:_OLD_VIRTUAL_PROMPT
-    }
-
-    if (Test-Path env:_OLD_VIRTUAL_PYTHONHOME) {
-        copy-item env:_OLD_VIRTUAL_PYTHONHOME env:PYTHONHOME
-        remove-item env:_OLD_VIRTUAL_PYTHONHOME
-    }
-
-    if (Test-Path env:_OLD_VIRTUAL_PATH) {
-        copy-item env:_OLD_VIRTUAL_PATH env:PATH
-        remove-item env:_OLD_VIRTUAL_PATH
-    }
-
-    if (Test-Path env:VIRTUAL_ENV) {
-        remove-item env:VIRTUAL_ENV
-    }
-
-    if (!$NonDestructive) {
-        # Self destruct!
-        remove-item function:deactivate
-    }
-}
-
-deactivate -nondestructive
-
-$env:VIRTUAL_ENV="C:\Part of my life\iit bombay\3 Jan 2020 updated\venv"
-
-if (! $env:VIRTUAL_ENV_DISABLE_PROMPT) {
-    # Set the prompt to include the env name
-    # Make sure _OLD_VIRTUAL_PROMPT is global
-    function global:_OLD_VIRTUAL_PROMPT {""}
-    copy-item function:prompt function:_OLD_VIRTUAL_PROMPT
-    function global:prompt {
-        Write-Host -NoNewline -ForegroundColor Green '(venv) '
-        _OLD_VIRTUAL_PROMPT
-    }
-}
-
-# Clear PYTHONHOME
-if (Test-Path env:PYTHONHOME) {
-    copy-item env:PYTHONHOME env:_OLD_VIRTUAL_PYTHONHOME
-    remove-item env:PYTHONHOME
-}
-
-# Add the venv to the PATH
-copy-item env:PATH env:_OLD_VIRTUAL_PATH
-$env:PATH = "$env:VIRTUAL_ENV\Scripts;$env:PATH"
diff --git a/venv/Scripts/activate b/venv/Scripts/activate
deleted file mode 100644
index 97dd559..0000000
--- a/venv/Scripts/activate
+++ /dev/null
@@ -1,76 +0,0 @@
-# This file must be used with "source bin/activate" *from bash*
-# you cannot run it directly
-
-deactivate () {
-    # reset old environment variables
-    if [ -n "${_OLD_VIRTUAL_PATH:-}" ] ; then
-        PATH="${_OLD_VIRTUAL_PATH:-}"
-        export PATH
-        unset _OLD_VIRTUAL_PATH
-    fi
-    if [ -n "${_OLD_VIRTUAL_PYTHONHOME:-}" ] ; then
-        PYTHONHOME="${_OLD_VIRTUAL_PYTHONHOME:-}"
-        export PYTHONHOME
-        unset _OLD_VIRTUAL_PYTHONHOME
-    fi
-
-    # This should detect bash and zsh, which have a hash command that must
-    # be called to get it to forget past commands.  Without forgetting
-    # past commands the $PATH changes we made may not be respected
-    if [ -n "${BASH:-}" -o -n "${ZSH_VERSION:-}" ] ; then
-        hash -r
-    fi
-
-    if [ -n "${_OLD_VIRTUAL_PS1:-}" ] ; then
-        PS1="${_OLD_VIRTUAL_PS1:-}"
-        export PS1
-        unset _OLD_VIRTUAL_PS1
-    fi
-
-    unset VIRTUAL_ENV
-    if [ ! "$1" = "nondestructive" ] ; then
-    # Self destruct!
-        unset -f deactivate
-    fi
-}
-
-# unset irrelevant variables
-deactivate nondestructive
-
-VIRTUAL_ENV="C:\Part of my life\iit bombay\3 Jan 2020 updated\venv"
-export VIRTUAL_ENV
-
-_OLD_VIRTUAL_PATH="$PATH"
-PATH="$VIRTUAL_ENV/Scripts:$PATH"
-export PATH
-
-# unset PYTHONHOME if set
-# this will fail if PYTHONHOME is set to the empty string (which is bad anyway)
-# could use `if (set -u; : $PYTHONHOME) ;` in bash
-if [ -n "${PYTHONHOME:-}" ] ; then
-    _OLD_VIRTUAL_PYTHONHOME="${PYTHONHOME:-}"
-    unset PYTHONHOME
-fi
-
-if [ -z "${VIRTUAL_ENV_DISABLE_PROMPT:-}" ] ; then
-    _OLD_VIRTUAL_PS1="${PS1:-}"
-    if [ "x(venv) " != x ] ; then
-	PS1="(venv) ${PS1:-}"
-    else
-    if [ "`basename \"$VIRTUAL_ENV\"`" = "__" ] ; then
-        # special case for Aspen magic directories
-        # see http://www.zetadev.com/software/aspen/
-        PS1="[`basename \`dirname \"$VIRTUAL_ENV\"\``] $PS1"
-    else
-        PS1="(`basename \"$VIRTUAL_ENV\"`)$PS1"
-    fi
-    fi
-    export PS1
-fi
-
-# This should detect bash and zsh, which have a hash command that must
-# be called to get it to forget past commands.  Without forgetting
-# past commands the $PATH changes we made may not be respected
-if [ -n "${BASH:-}" -o -n "${ZSH_VERSION:-}" ] ; then
-    hash -r
-fi
diff --git a/venv/Scripts/activate.bat b/venv/Scripts/activate.bat
deleted file mode 100644
index 120cc2e..0000000
--- a/venv/Scripts/activate.bat
+++ /dev/null
@@ -1,45 +0,0 @@
-@echo off
-
-rem This file is UTF-8 encoded, so we need to update the current code page while executing it
-for /f "tokens=2 delims=:." %%a in ('"%SystemRoot%\System32\chcp.com"') do (
-    set "_OLD_CODEPAGE=%%a"
-)
-if defined _OLD_CODEPAGE (
-    "%SystemRoot%\System32\chcp.com" 65001 > nul
-)
-
-set "VIRTUAL_ENV=C:\Part of my life\iit bombay\3 Jan 2020 updated\venv"
-
-if not defined PROMPT (
-    set "PROMPT=$P$G"
-)
-
-if defined _OLD_VIRTUAL_PROMPT (
-    set "PROMPT=%_OLD_VIRTUAL_PROMPT%"
-)
-
-if defined _OLD_VIRTUAL_PYTHONHOME (
-    set "PYTHONHOME=%_OLD_VIRTUAL_PYTHONHOME%"
-)
-
-set "_OLD_VIRTUAL_PROMPT=%PROMPT%"
-set "PROMPT=(venv) %PROMPT%"
-
-if defined PYTHONHOME (
-    set "_OLD_VIRTUAL_PYTHONHOME=%PYTHONHOME%"
-    set PYTHONHOME=
-)
-
-if defined _OLD_VIRTUAL_PATH (
-    set "PATH=%_OLD_VIRTUAL_PATH%"
-) else (
-    set "_OLD_VIRTUAL_PATH=%PATH%"
-)
-
-set "PATH=%VIRTUAL_ENV%\Scripts;%PATH%"
-
-:END
-if defined _OLD_CODEPAGE (
-    "%SystemRoot%\System32\chcp.com" %_OLD_CODEPAGE% > nul
-    set "_OLD_CODEPAGE="
-)
diff --git a/venv/Scripts/deactivate.bat b/venv/Scripts/deactivate.bat
deleted file mode 100644
index 1205c61..0000000
--- a/venv/Scripts/deactivate.bat
+++ /dev/null
@@ -1,21 +0,0 @@
-@echo off
-
-if defined _OLD_VIRTUAL_PROMPT (
-    set "PROMPT=%_OLD_VIRTUAL_PROMPT%"
-)
-set _OLD_VIRTUAL_PROMPT=
-
-if defined _OLD_VIRTUAL_PYTHONHOME (
-    set "PYTHONHOME=%_OLD_VIRTUAL_PYTHONHOME%"
-    set _OLD_VIRTUAL_PYTHONHOME=
-)
-
-if defined _OLD_VIRTUAL_PATH (
-    set "PATH=%_OLD_VIRTUAL_PATH%"
-)
-
-set _OLD_VIRTUAL_PATH=
-
-set VIRTUAL_ENV=
-
-:END
diff --git a/venv/Scripts/easy_install-3.7-script.py b/venv/Scripts/easy_install-3.7-script.py
deleted file mode 100644
index 0948078..0000000
--- a/venv/Scripts/easy_install-3.7-script.py
+++ /dev/null
@@ -1,12 +0,0 @@
-#!"C:\Part of my life\iit bombay\3 Jan 2020 updated\venv\Scripts\python.exe"
-# EASY-INSTALL-ENTRY-SCRIPT: 'setuptools==40.8.0','console_scripts','easy_install-3.7'
-__requires__ = 'setuptools==40.8.0'
-import re
-import sys
-from pkg_resources import load_entry_point
-
-if __name__ == '__main__':
-    sys.argv[0] = re.sub(r'(-script\.pyw?|\.exe)?$', '', sys.argv[0])
-    sys.exit(
-        load_entry_point('setuptools==40.8.0', 'console_scripts', 'easy_install-3.7')()
-    )
diff --git a/venv/Scripts/easy_install-3.7.exe b/venv/Scripts/easy_install-3.7.exe
deleted file mode 100644
index 675e6bf..0000000
--- a/venv/Scripts/easy_install-3.7.exe
+++ /dev/null
diff --git a/venv/Scripts/easy_install-script.py b/venv/Scripts/easy_install-script.py
deleted file mode 100644
index 4c28941..0000000
--- a/venv/Scripts/easy_install-script.py
+++ /dev/null
@@ -1,12 +0,0 @@
-#!"C:\Part of my life\iit bombay\3 Jan 2020 updated\venv\Scripts\python.exe"
-# EASY-INSTALL-ENTRY-SCRIPT: 'setuptools==40.8.0','console_scripts','easy_install'
-__requires__ = 'setuptools==40.8.0'
-import re
-import sys
-from pkg_resources import load_entry_point
-
-if __name__ == '__main__':
-    sys.argv[0] = re.sub(r'(-script\.pyw?|\.exe)?$', '', sys.argv[0])
-    sys.exit(
-        load_entry_point('setuptools==40.8.0', 'console_scripts', 'easy_install')()
-    )
diff --git a/venv/Scripts/easy_install.exe b/venv/Scripts/easy_install.exe
deleted file mode 100644
index 675e6bf..0000000
--- a/venv/Scripts/easy_install.exe
+++ /dev/null
diff --git a/venv/Scripts/epylint.exe b/venv/Scripts/epylint.exe
deleted file mode 100644
index 832257f..0000000
--- a/venv/Scripts/epylint.exe
+++ /dev/null
diff --git a/venv/Scripts/isort.exe b/venv/Scripts/isort.exe
deleted file mode 100644
index 76fcf01..0000000
--- a/venv/Scripts/isort.exe
+++ /dev/null
diff --git a/venv/Scripts/pip-script.py b/venv/Scripts/pip-script.py
deleted file mode 100644
index ac70cac..0000000
--- a/venv/Scripts/pip-script.py
+++ /dev/null
@@ -1,12 +0,0 @@
-#!"C:\Part of my life\iit bombay\3 Jan 2020 updated\venv\Scripts\python.exe"
-# EASY-INSTALL-ENTRY-SCRIPT: 'pip==19.0.3','console_scripts','pip'
-__requires__ = 'pip==19.0.3'
-import re
-import sys
-from pkg_resources import load_entry_point
-
-if __name__ == '__main__':
-    sys.argv[0] = re.sub(r'(-script\.pyw?|\.exe)?$', '', sys.argv[0])
-    sys.exit(
-        load_entry_point('pip==19.0.3', 'console_scripts', 'pip')()
-    )
diff --git a/venv/Scripts/pip.exe b/venv/Scripts/pip.exe
deleted file mode 100644
index 675e6bf..0000000
--- a/venv/Scripts/pip.exe
+++ /dev/null
diff --git a/venv/Scripts/pip3-script.py b/venv/Scripts/pip3-script.py
deleted file mode 100644
index e15e678..0000000
--- a/venv/Scripts/pip3-script.py
+++ /dev/null
@@ -1,12 +0,0 @@
-#!"C:\Part of my life\iit bombay\3 Jan 2020 updated\venv\Scripts\python.exe"
-# EASY-INSTALL-ENTRY-SCRIPT: 'pip==19.0.3','console_scripts','pip3'
-__requires__ = 'pip==19.0.3'
-import re
-import sys
-from pkg_resources import load_entry_point
-
-if __name__ == '__main__':
-    sys.argv[0] = re.sub(r'(-script\.pyw?|\.exe)?$', '', sys.argv[0])
-    sys.exit(
-        load_entry_point('pip==19.0.3', 'console_scripts', 'pip3')()
-    )
diff --git a/venv/Scripts/pip3.7-script.py b/venv/Scripts/pip3.7-script.py
deleted file mode 100644
index f6a9c74..0000000
--- a/venv/Scripts/pip3.7-script.py
+++ /dev/null
@@ -1,12 +0,0 @@
-#!"C:\Part of my life\iit bombay\3 Jan 2020 updated\venv\Scripts\python.exe"
-# EASY-INSTALL-ENTRY-SCRIPT: 'pip==19.0.3','console_scripts','pip3.7'
-__requires__ = 'pip==19.0.3'
-import re
-import sys
-from pkg_resources import load_entry_point
-
-if __name__ == '__main__':
-    sys.argv[0] = re.sub(r'(-script\.pyw?|\.exe)?$', '', sys.argv[0])
-    sys.exit(
-        load_entry_point('pip==19.0.3', 'console_scripts', 'pip3.7')()
-    )
diff --git a/venv/Scripts/pip3.7.exe b/venv/Scripts/pip3.7.exe
deleted file mode 100644
index 675e6bf..0000000
--- a/venv/Scripts/pip3.7.exe
+++ /dev/null
diff --git a/venv/Scripts/pip3.exe b/venv/Scripts/pip3.exe
deleted file mode 100644
index 675e6bf..0000000
--- a/venv/Scripts/pip3.exe
+++ /dev/null
diff --git a/venv/Scripts/pylint.exe b/venv/Scripts/pylint.exe
deleted file mode 100644
index 97bd505..0000000
--- a/venv/Scripts/pylint.exe
+++ /dev/null
diff --git a/venv/Scripts/pyreverse.exe b/venv/Scripts/pyreverse.exe
deleted file mode 100644
index 2a17b2f..0000000
--- a/venv/Scripts/pyreverse.exe
+++ /dev/null
diff --git a/venv/Scripts/python.exe b/venv/Scripts/python.exe
deleted file mode 100644
index 9ab088b..0000000
--- a/venv/Scripts/python.exe
+++ /dev/null
diff --git a/venv/Scripts/python_d.exe b/venv/Scripts/python_d.exe
deleted file mode 100644
index 33b837f..0000000
--- a/venv/Scripts/python_d.exe
+++ /dev/null
diff --git a/venv/Scripts/pythonw.exe b/venv/Scripts/pythonw.exe
deleted file mode 100644
index d5fc547..0000000
--- a/venv/Scripts/pythonw.exe
+++ /dev/null
diff --git a/venv/Scripts/pythonw_d.exe b/venv/Scripts/pythonw_d.exe
deleted file mode 100644
index 4bfa6eb..0000000
--- a/venv/Scripts/pythonw_d.exe
+++ /dev/null
diff --git a/venv/Scripts/symilar.exe b/venv/Scripts/symilar.exe
deleted file mode 100644
index d357103..0000000
--- a/venv/Scripts/symilar.exe
+++ /dev/null
diff --git a/venv/pyvenv.cfg b/venv/pyvenv.cfg
deleted file mode 100644
index a9ec033..0000000
--- a/venv/pyvenv.cfg
+++ /dev/null
@@ -1,3 +0,0 @@
-home = C:\Program Files\Python37
-include-system-site-packages = false
-version = 3.7.4